FEASIBILITY STUDY - Auslandsgeschäftsabsicherung · FEASIBILITY STUDY Volume 2 ... - Defining the scope and level of impact of the proposed ... and limitations are given according

License series АВ №601893 since 30.12.2011

CHICKEN MANURE PROCESSING DEPARTMENT AT PAT "AVIS" POULTRY FARM

FEASIBILITY STUDY

Volume 2 Environmental impact assessment

23-0412 – EIA

CEO S.V. Fishchuk

Chief Project Engineer S.V. Fishchuk

Kiev – 2013

23-0412-EIA Page

i Cont. Quant. Page. №doc. Signature Date

i

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

FS CONTENTS

Volume# Marking Name

1 23-0412-ПЗ General explanatory note. Basic drawings

2 23-0412-ОВНС Environmental impact assessment

23-0412-EIA Page

ii Cont. Quant. Page. №doc. Signature Date

ii

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Table of Contents 1. GROUNDS FOR EIA .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. ..1 2. PHYSIOGRAPHIC PECULIARITIES OF THE AREA AND SITE (TRACK) OF THE DESIGNED OBJECT LOCATION .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .6 2.1 PHYSIOGRAPHIC CHARACTERISTICS OF THE CONSTRUCTION AREA .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .6 2.2 CLIMATE CONDITIONS OF THE CONSTRUCTION AREA.. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .7 2.3 THE MAIN DATA ON CONSTRUCTION CONDITIONS OF THE CHICKEN MANURE PROCESSING DEPARTMENT .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. ..8 2.4 WATER ENVIRONMENT .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. ..8 2.5 THE OBJECTS OF NATURAL-RESERVED FUND, HISTORICAL AND ARCHITECTURAL HERITAGE. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .8 THERE WILL BE NO OBJECT OF NATURAL-RESERVED FUND AND HISTORICAL-CULTURAL HERITAGE IN CONSTRICTION AREA... .. .. .. .. .. .. .. .. .. .. .. .. .. .. .8 2.6 ENGINEERING AND GEOLOGICAL CONDITIONS .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. ..8 3. GENERAL CHA RACTERISTICS OF THE DESIGNED OBJECT... .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. ..9 3.1. DESIGNED OBJECT LOCATION ALTERNATIV ES... .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .9 3.2. DATA ON SIZE OF THE CONSTRUCTION SITE AND OCCUPIED LAND PLOT .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .9 3.3. GENERAL CHARACTERISTICS OF THE DESIGNED OBJECT.. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .9 3.4. DATA ON INVOLVED RESOURCES .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 16 3.5. PROJECT DATA ON THE ESTIMATED AMOUNTS OF WASTE.. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 16 3.6. DESIGN DATA ABOUT THE CALCULATION WASTES’ VOLUMES.. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 16 3.7. ASSESSMENT OF POSSIBILITY OF APPEARANCE AND DEVELOPMENT OF EMERGENCY SITUATIONS .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. . 20 3.8. THE LIST AND CHARACTERISTICS OF POTENTIAL ENVIRONMENTAL IMPACT SOURCES. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 26 3.9. THE LIST OF POTENTIALLY INFLUENCED OBJECTS AND POTENTIAL BOUNDARIES OF INFLUENCED AREA DURING CONSTRUCTION AND

OPERATION OF THE OBJECT .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 26 4. ASSESSMENT OF ENVIRONMENTAL IMPACTS OF PLANNED ACTIVITIES .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 27 4.1. CLIMATE AND MICROCLIMATE.. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. . 27 4.2. AIR ENVIRONMENT... .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 28 4.3. GEOLOGICAL ENVIRONMENT AND SOIL .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. . 43 4.4. WATER ENVIRONMENT .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 43 4.5. FLORE AND FAUNA. WILDLIFE RESERVATION OBJECTS. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 44 4.6. CHARACTERISTICS OF OTHER ENVIRONMENTAL IMPACTS .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 44 4.7. NOISE POLLUTION .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 44 5. IMPACT ASSESSMENT OF PLANNED ACTIVITY ON THE SOCIAL AND TECHNOGENIC ENVIRONMENT .. .. .. .. .. .. .. .. .. .. .. .. 44 5.1 SOCIAL ENVIRONMENT .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 44 5.2 TECHNOGENIC ENVIRONMENT .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 45 6. COMPLEX MEASURES TO ENSURE NORMAL CONDITIONS OF ENVIRONMENT AND ITS SAFETY.. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 45 RESOURCE SAVING MEASURES.. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. . 45 PROTECTIVE MEASURES.. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 45 RESTORING MEASURES.. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. . 45 COMPENSATIVE MEASURES.. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 45 IMPACT ASSESSMENT OF INDUSTRIAL WASTES PRODUCED BY PLANNED ACTIVITY .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 45 ASSESSMENT OF RISK OF PLANNED ACTIVITY ON THE HEALTH OF POPULATION .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. . 46 ASSESSMENT OF SOCIAL RISK OF PLANNED ACTIVITIES INFLUENCE.. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. . 47 7. ASSESSMENT OF ENVIRONMENTAL IMPACTS DURING CONSTRUCTION.. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. 47 8. COMPREHENSIVE ASSESSMENT OF OBJECT THAT IS PROJECTED ON ENVIRONMENT AND CHARACTERISTICS OF RESIDUAL

EFFECTS.. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. . 53 9. STATEMENT ON ENVIRONMENTAL EFFECTS OF ACTIVITY.. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. . 54

ANNEXES ................................................................................................................................................. 56

23-0412-EIA Page

1 Cont. Quant. Page. №doc. Signature Date

1

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

1. GROUNDS FOR EIA

1.1. General Terms

The aim for developing EIA is to determine the feasibility and acceptability of the proposed

activity and justification of economic, technical, organizational, sanitary, public, legal and other

measures to ensure safety of the environment set out in the project documentation.

The EIA provides comprehensive description of results of the impact on natural and social

environment, including livelihoods of the population, technogenic environment and acceptable

reasoned level of their planned activities.

Main tasks of developing EIA materials:

- Providing a general description of the existing situation in the district and facility

construction, where activities are planned;

- Review and assessment of environmental, social and technological factors, sanitary and

epidemiological situation of the planned activities and study the advantages and

accommodation options;

- Defining a list of possible hazardous effects and areas of impact of the proposed activity on

the environment;

- Defining the scope and level of impact of the proposed activity on the environment;

- Prediction of environmental changes according to the list of impact;

- Identification of measures to prevent or minimize environmental effects of proposed

activities on the environment necessary for compliance with environmental and health

legislation and other laws and regulations relating to environmental safety ;

- Determination of residual impacts on the environment, which may be subject to the

implementation of all the measures envisaged;

- Drafting of Statement on ecological consequences of proposed activities.

During the development of EIA materials were fully taken into account the requirements of

current legislation, applicable state building, sanitary and fire regulations, and environmental

conditions and constraints.

EIA provided in this section, take into account the public interest and are prepared, as a part of

the design documentation, for submission for approval and going thought state examinations.

Consideration of the public interest being committed under the Law of Ukraine "On Planning and

Development of the land", Law of Ukraine "On Environmental Protection" and the Convention on

Access to Information, Public Participation in Decision-making and Access to Justice in

Environmental Matters. "Statement on the environmental effects of proposed activities" was spread

through mass media.

Facility design requires setting limits of sanitary protection zone. Sanitary and hygienic breaks

and limitations are given according to the current state sanitary standards and rules of p rotection of the

population against possible negative impacts of the planned activities.

23-0412-EIA Page


2

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

EIA data of the designed object developed on the basis of environmental-engineering, sanitary, technical-engineering surveys and studies based on modern techniques and facilities. Initial data for

EIA were all available stock data describing the state of the environment in the investigated area,

environmental monitoring data, results of geological-engineering, technical-engineering and other

surveys of previous years, cartographic materials and other information provided by the Customer -

LLC "Monolittransbud ".

EIA data of the designed object in composition and content sufficient to characterize:

- Compliance with legal documents of state and local governments;

- Compliance with applicable environmental, health and urban planning laws;

- Compliance with applicable regulations (DBN, VBN, RBN, national standards) in their

regulation of issues related to environmental issues, the use of natural resources and the problem of

safe conditions of human life and operational reliability of man-made objects;

- Do not exceed the environmental impact on the performance, standardized and limited at the

time of design object;

- Occurrence in environment hazardous endogenous and exogenous geological processes and

other phenomena;

- Compliance with environmental, health and epidemiology, engineering and local functional

planning restrictions;

- The effectiveness of the proposed resource, protection, rehabilitation, compensation and

security measures.

Alternative placement of the designed object were not considered due to the technical and

economic requirements of the customer and achievement of the sound effects of designed activity on

the selected platform that provides compliance with all environmental and sanitary standards and

requirements.

1.2. Documents that are basis for the development of EIA data

Table 1. List of output data

№ Marking Name Note

1 - Tasks for development of EIA

2 23-0412 - ПЗ FS explanatory note “Chicken manure processing department at PAT "AVIS" poultry farm”

3 - Background concentrations of pollutants in ambient air

1.3. List of potential impact sources of planned activity on the environment

During the construction:

- Emissions of pollutants and noise from construction machinery;

23-0412-EIA Page


3

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

- Contamination of construction with debris;

- Infringement of the soil on the construction territory of the facility.

During operation:

- Emissions from the chicken manure processing depart ment;

- Waste;

- Drops of water;

- Operational (project) and emergency flow of water communications.

1.4. Summary of impact types of the planned activity on the environment:

Groundwater Influences. To ensure technological process will be used groundwater.

Taking into account the height of occurrence of groundwater levels in

order to avoid flooding of underground facilities and trails of utilities is

recommended to design a drainage area protection of the projected

building. In emergency situations of leakage of water communications, pipelines of supply and removal of substrate and digestate is proposed

to create a "cushion" for protection of groundwater from these

substances.

Surface water Surface waters are far away from this area of construction, so there is no contamination of surface waters.

Atmospheric air Influences. The concentration of pollutants in the surface layer of the atmosphere will not exceed established standards.

Water Resources Influences. Water is expected from wells. The extraction of process

waters is expected into closed lagoons. 68% of process waters returns to

the process. From lagoons water goes to the Vaporizer-condenser,

where it will be cleaned and will return in the process. Expected closed

water cycle.

Waste Formation of construction debris during construction, operation - the formation of industrial waste, municipal solid waste, waste from

territory cleaning, waste after gas treatment facilities. Waste will be

disposed according to the legislation of Ukraine.

Flora and fauna Influence is limited. Valuable species of flora and fauna at the site were

not found. No nature-protected property .

Social environment Influences. Construction of plant for processing chicken manure in

Humentsi village, Kamenets-Podolsk district, Khmelnytskyi Oblast will

allow to process waste from the poultry farm PAT agro "AVIS" to organic fertilizers and reduce air pollution with hazardous substances.

During the processing of waste produced biogas will be used to generate

23-0412-EIA Page


4

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

heat and electricity for farms PAT agro "AVIS".

Technogenic

environment

No influence. Around the projected object area architectural monuments

are absent. Operation of the facility will not create the technogenic

burden on the environment.

1.5. Environmental, sanitary, epidemiological, fire and urban development

conditions and restrictions

1.5.1 Environmental conditions and restrictions

1. Given the possibility of negative public reaction on mentioned construction before designing

the documentation Customer has to publish in mass media information about this building.

Reviews for it are to be send to the Permanent Commission of Khmelnytska Oblast on

environmental policy in order to reflect public opinion when making a final decision by

Khmelnytsky Regional Council regarding the feasibility of construction of the object;

2. Design to conduct according to developed and approved way of detailed project planning (PDP) and the general plan of the whole area with applying on it in wood shooting and

driveways to the site. PPPs provide for the possibility of maximum preservation of trees and

their communities. Green areas are subject to preservation, the customer take under custody

3. Construction management provide measures to protect green space that are subject conservation

from damage to construction equipment to ensure their livelihoods;

4. At the next stage of design is developing of dendroplan, envisaging a compensatory disembark

of decorative trees with formed root system with lump of land, measuring 0.8 cubic installed

and agreed in appropriate way;

5. Project documentation development on the basis of existing standards and requirements of DBN

360-92 ** "Urban Planning. Planning and development of urban and rural settlements, "State

sanitary rules and planning of settlements № 173 from 19.06.96.;

6. Construction management has to exclude the possibility of construction materials storage and

placement of construction trailers on the surrounding area;;

7. Construction to conduct after approval of project documentation in accordance with legislation;

8. Territory use without change in functionality ..

1.6. Data on public attitude and other stakeholders to the design activity and

related problems that require solutions

Local population is not using mentioned land for recreational purposes.

Analysis of the existing urban planning documentation, territory plan with drawing the red lines (suspended), the current state of the land and surrounding area, functional zoning of the territory,

environmental conditions and social and environmental needs, confirms the feasibility of drafting a

specified area.

23-0412-EIA Page


5

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

The public was introduced to the "Statement of Intent" of planned activities.

1.7. List of used regulatory documents

During the development of this EIA following regulations and procedures were applied:

- DBN A.2.2-3-2012. Structure and content of p roject documentation for construction.

- DBN360-92.** Urban Development. Planning and development of urban and rural

settlements.

- DBN A.2.2-1-2003. EIA structure and contents during the design and construction process of

enterprises, buildings and structures.

- GKD 34.02.305 - 2002. Emissions of pollutants into the atmosphere from power plants.

Methods of determination.

- Methods of calculating air emissions of pollutants and greenhouse gases from vehicles"

approved by the State Statistics Committee № 452 of 13.11.2008.

- VNTP-SHiP-46-16.96 - "departmental rules for technological design" of road transport and

motor transport agribusiness companies of Ukraine "

- UPM-86. Method of calculating the air concentration of harmful substances in the emissions

of plants. L.: Gidrometeoizdat, 1987. - 92 p.

- DSP 173-96. State sanitary rules and planning of settlements development. Approved by the

Ministry of Health of Ukraine from 19.06.96 № 173.

- DSP 201-97. State sanitary rules on the atmospheric air protection in populated areas (from

chemical and biological agents).

- Guidelines for the development of EIA materials for DBN A.2.2-1-2003. - Kharkov:

UkrNIINTIZ Gosstroy Ukraine, 2002-04. Part I - 156 p., Part II - 200 pp.

- Soluha B.V. Impact assessment of construction objects on the environment (EIA) according to

DBN A.2.2-1-95. K.: Knowledge of Ukraine, 2000. - 112 pp.

- Soluha B.V. Impact assessment of vehicle emissions on the atmosphere in the area of residential

development (according to DBN A.2.2-1-95). - K. KNUCA, 2000. - 54 pp.

- SNIP 2.04.03-85 "Sewage. External networks and facilities ".

- STP 17-99 "Standards of disposal systems technological design and preparation for use of

manure and litter." Ministry of Agriculture of Russia.

- VNTP - AIC -04. 05. " Poultry enterprises. Departmental standards for technological design.

"Ministry of Agrarian Policy of Ukraine, Kyiv, 2005.

23-0412-EIA Page


6

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

1.8. Description of predicting methods for the environmental dynamics and

justification of the billing periods of forecast

Methodological basis of the assessment and forecasting of the environmental dynamics and

justification of the billing periods of forecast used during the development a specific section of EIA

materials are given in the relevant sections of each part of the EIA project.

Modeling and automatic software calculations were performed on the software complexes

approved according to the established procedure.

1.9. Information about the customer, general designer and the executor of EIA

Customer PAT agro company "AVIS" 32325, Donetsk region, Kamenets district,

Humentsi village, Verbitsky Highway 1

General designer Ltd. "M onolittransbud", 76000, Ivano-Frankivsk, S. Petliury str., 10.

Executor of EIA Ltd. "Energy Invest" 01042, Ky iv, str. John curls, 5.

1.10. The list and brief analysis of previous approvals and examinations

Previous approvals and examinations were not held since the project documentation will be

submitted for the state comprehensive examination of the construction projects as was defined by the

Cabinet of M inisters of Ukraine 11.04.11 #560.

2. PHYSIOGRAPHIC PECULIARITIES OF THE AREA AND SITE (TRACK)

OF THE DESIGNED OBJECT LOCATION

2.1 Physiographic characteristics of the construction area

Allotted for construction land plot is located on the leased land according to the contracts (see

appendixes) in Humentsi village, Kamenetz-Podolsk district, Khmelnytskyi Oblast.

Allocated to for the construction of chicken manure processing department land borders:

- from south - rearing flock zone and existing poultry farm PAT agro company "AVIS";

- from west - forest plantations and railway;

- the north - forest plantations and agricultural lands;

23-0412-EIA Page


7

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

- from east - highway.

In terms of geomorphology development plot is located within the Khmelnytsky forest plateau-

like plains. Relief of the plot is calm. Foundation based on the yellowish-brown clay, semi-solid, dense,

with carbonate inclusions. Ground waters located at the depth of 3.5 - 4.8 m from the surface. Seasonal

fluctuations in groundwater level ± 1,0 m.

The protected fund (NPF) within planned activities not found.

Designed object is a subject to sanitary classification of Annex 12 DSP-173-96 and requires

regulatory SPZ.

Situational placement plan of the designed object is given in Appendixes.

2.2 Climate conditions of the construction area

Construction territory refers to the P-V category, according to BNSH 2.01.01-82. The climate is

moderately continental with temperate cold winters and warm summers. According to the Khmelnitsky

weather station average annual temperature is 7,8 º C. The coldest month is January, with average

temperature of -5 º C, the warmest month is July with temperature of 18,4 º C. The absolute minimum

and maximum temperatures are -8.1 and 24,5 º C respectively. Regulatory freezing depth of soil is 0.84

m, snow load is 127 kg/cm2, wind load is 46 kg/cm2.

Coefficient of stratification - 200.

Coefficient of plot relief - 1.

Wind speed, exceeding frequency of which is 5% - 6 m / s.

Average wind speed per year - 3 m / s.

Table 1. Average annual wind rose

Direction N NE E SE S SW W NW

frequency % 13,5 4,7 6,4 22,4 16,1 2,6 10,2 24,1

According to the letter from State Department of Environmental Protection in Khmelnitsky

region concerning the background concentrations of substances in the atmosphere in Humentsi village,

Kamianets-Podilskyi Rayon, № 03/2113 of 26/09/12:

№ Name of a substance Background concentration of

pollutants, mg/m3

Maximum allowable

concentration, mg/m3

1 Ammonia 0,08 0,2

2 Methane 20,0 50,0

23-0412-EIA Page


8

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

3 Carbon oxide 0,4 5

4 Sulfur dioxide 0,02 0,5

5 Nitrous oxide 0,008 0,2

6 Suspended particles 0,05 0,15

7 Saturated hydrocarbons 0,4 1

Overall climate and physiographic conditions of the area can be characterized as favorable.

2.3 The main data on construction conditions of the chicken manure processing department Table 1.Basic information on construction conditions according to BNSH2.01.01-82

№ Data name measurement

unit Index

1 Climate district - П-В

2 Weight of the snow cover kg/sm2 127

3 Wind dynamic pressure kg/sm2 46

4 Average temperature of the warmest month ºС 18,4

5 Average temperature of the coldest month ºС -5

6 Normative freezing depth of soil м 0,8

7 Prevailing wind direction: - SE, NW

2.4 Water environment

On construction site and nearby there are no surface waters which could be influenced.

2.5 The objects of natural-reserved fund, historical and architectural heritage. There will be no object of natural-reserved fund and historical-cultural heritage in constriction area.

2.6 Engineering and geological conditions

The poultry farm is located on the lands of industrial constructions in Gumentsy, Kamianets-Podilskyi district of Chmelnitskiy region:

- replacement chicks plot and agricultural company “AVIS” in south;

- forest plantation and railway in west;

- forest plantation and farmlands in north;

- autobahn in east.

The designed plot land forms are characterized by above sea level of 245,5-268 m. From the geomorphologic point of view construction area is located in Chmelnitsky forest

valley plateau region. The underground waters horizon is on the depth 3,5 – 4,8 m from the ground surface. Seasonal fluctuations of the underground waters level are ±1,0 m.

23-0412-EIA Page


9

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

3. GENERAL CHARACTERISTICS OF THE DESIGNED OBJECT.

3.1. Designed object location alternatives.

The project foresees the compliment with the requirements concerning functional assignment of

object, corresponding to general standards and modern technological level.

At the meantime all operating requirements of corresponding institutions and authorities, local

authorities regulations, orders of construction supervision institutions conform with European norms.

The choice of a land plot for constructing the poultry farm is determined by the next objective factors: – the absence of other free rented land plots with sufficient area and with standard distance from existing residential settlements (the density of existing residential constructions); – the absence of other free rented low-valued lands with low y ield coefficient;

– low value of suggested land resources as the result of production activity in previous periods (poultry farm location in household yard);

– the presence of infrastructure nearby (roads, electric supply nets, gas pipeline etc.); – the presence of wastes processing capacities nearby; – possibility of locating of the designed object on the wind downstream side from the closest constructions with consideration of wind pattern;

The project supposes a single variant of the poultry manure processing unit location in Gumentsyі, Khmelnytskyi region.

Organization of public services and amenities is foreseen by the project.

3.2. Data on size of the construction site and occupied land plot

Table 1. Technical and economic indicators

№ Indicator Measurement unit

Total

1 Area of land lot within the fence ha 20 2 Building volume m3 186470 3 Area asphalt-concrete surfacing m

2 45000

4 Settlement gardening m2 35000

3.3. General characteristics of the designed object

In Humentsi village, Kamianets-Podilskyi Region, Khmelnytsky Area at the Agrofirma "AVIS" a

utilization problem of poultry waste has arisen. NT solve this environmental problem a construction of

chicken manure processing workshop with the capacity of 291,000 tons per year has been foreseen. For

poultry wastes processing a biogas technology will be applied.

Biogas technology is a radical way of disposal and recycling a variety of organic wastes of birds,

animal and plant origin, including animal and human excrement at the same time allowing to obtain high-energy gaseous fuels which are biogas and highly environmentally friendly organic fertilizers.

Biogas technology can solve problems of agricultural chemistry, environment, energy and investment.

The core of biogas technology is the complex natural process of biological decomposition of

slime, manure or poultry manure, their mixtures and other organic matters under anaerobic conditions

23-0412-EIA Page


10

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

(without air). However, under the influence of a particular group of anaerobic bacteria the processes take place that are accompanied by mineralization nitric, phosphorus and organic compounds and potassium

organic bonds with obtaining mineral forms of nitrogen, phosphorus and potassium, the most available

for plants with a complete destruction of pathogenic (disease) micro flora, helminthes eggs, seeds of

weed, specific fecal odors, nitrates and nitrites.

Received waste from the poultry farms will be sent to the department of chicken manure

processing. There will be 10 biogas units located in the workshop: each of the 4 biogas units will process

over 72,750 tons / year of chicken manure and each of the 6 biogas units will recycle over 42,596 tons / year of silage.

The construction of biogas plants is foreseen in 3 stages:

1 part of construction (start-up complex) - 2 biogas units processing 145,500 tons / year of

chicken manure, sanitary checkpoint, boiler of container type, control point, the system external

desulphuration;

2 part of construction (start-up complex) - 2 biogas units processing 145,500 tons / year of

chicken manure, the system external desulphuration;

3 part of construction (start-up complex) - 6 biogas units are processing 255,573 tons / year of silage (Table 5)...

Table 2 Technological process data of

chicken manure processing

Start-up complex Substrate Quantity

t/year t/day m3/year

1 Chicken manure (31%СР) 145 500 398,63 - Water 176 600 483,84 - Digestate - - 304 323

2

Chicken manure (31%СР) 145 500 398,63 -

Water 176 600 483,84 - Digestate - - 304 323

3 Silage maize (33% СР) 255 573 700,2 - Digestate - - 169 313

The main parts of 1-st part construction are 2 biogas units consist of 4 intake storage tanks, 6 fermenters with integrated gas collectors of low pressure, 2 after-fermentation tanks, 2 emergency flares

and 3 cogeneration plants, 7 lagoons, 2 external sulphur cleaning systems. The construction of second

start-up complex is done by analogue to the first. The construction of 3-d complex consists of 12

fermenters with integrated gas collectors of low pressure, 6 after-fermentation tanks, 12 downloaders of

substrate with MT-MixBox, 6 emergency flares and 12 cogeneration plants, 4 lagoons, 24 silo.

1 and 2 start-up complexes.

From the poultry factory the chicken manure is transported to the chicken manure processing

workshop wherein it is sent to intake storage tank of the capacity 616 m3 (Ø = 14 m, h = 4 m). Loading of the chicken manure (28% CP the dry matter) is performed through a special aperture

located on the roof of the storage tank. On downloading this hole closes.

Inside the intake storage tank the manure is mixed with water using by means of mixer. In this

tank the hydrolysis process takes place, i.e. acid or hydrogen fermentation: from complex organic

compounds from water is formed with acids (acetic, formic, lactic, butyric, propionic, etc.), alcohols

23-0412-EIA Page


11

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

(ethy l, propyl, butyl, etc..), gases (carbon, hydrogen, hydrogen sulfide, ammonia), amino acids, glycerin, etc. This decomposition is carried out by ordinary saprophytic anaerobic bacteria that are widely

distributed in nature, rapidly reproducing themselves and live at a pH 4,5-7. Acidic fermentation is

characterized by significant formation and release of acids, accompanied by acidifying of the media and

decrease of pH to 5-4,5.

The main reactions that take place in the tank:

1) oxidation of organic acids:

a) lactic СН

3СНОНСООН + Н

2О → СН

3СООН + СО

2 + 2Н

2;

б) propionic

СН3СН

2СООН + 2Н

2О → СН

3СООН + СО

2 + 3Н

2;

в) butyric

СН3СН

2СН

2СООН + 2Н

2О → 2СН

3СООН + 2Н

2;

2) oxidation of alcohols:

С2Н5ОН + Н2О → СН3СООН + 2Н2.

Chicken manure (199.31 tons / day) is mixed with water (241.92 tons / day) during the day. The resulting substrate in the tank is pumped via pipeline into the fermenter at 147.076 tons / day.

The storage tank has inside sand cleaning unit. This unit is moving slowly along the bottom of

the tank and removes the sand to the discharge aperture. from the discharge aperture is transported onto

the sand removing unit, where it is separated from the liquid, which flows back into tank. Sand after

processing is transferred for disposal.

2 pcs of intakes storage tank are foreseen for each 1 and 2 start-up complexes due to the fact that

while one is being filled with, from the second filled flows the substrate (mixture of chicken manure and

water) at 147.076 t / day into each fermenter. Fermenter volume is 5654 m3 (Ø = 30 m, h = 8 m). There is disintegration of organic matter taking place in the fermenter which is done by means of

methane and sulphate-reducing microorganisms which are using metabolites formed in early stages. At

the final stage of anaerobic destruction of organic matter in ecosystems with low sulfate СН4 і СО2 are

mainly formed and some amount of H2S. In natural ecosystems sulphate-forming bacteria are Н2 donors

for methanogenic bacteria. At the increase of sulfate concentration to 0.50,5 mmol/L sulphate reducing

bacteria become competitive with methanogens for energy substrates (Н2 and acetate), as far as formed

sulfides inhibit the growth of methanogens: • acetoclastic methanogenesis is the sp litting of volatile fat acids (LZHK) into methane and

carbon dioxide: CH3COOH → CH4 + CO2;

• restoration of single-carbon molecules (Carbon dioxide, formic acid, methanol) molecular

hydrogen: CO2 + 4N2 → CH4 + H2O. The process of methanogenesis is anaerobic, alkaline

environment (pH> 7). Temperature in fermenters is +38 º C. The pressure in fermenters is Pmax=3,5∙10-3

bar or Pmed=1,5∙10-3

bar. Substrate is constantly stirred by mixers at a speed of 1 m / s. Mixers are

cyclically raised to the level of the mirror surface and stir the faction that was formed on the top. This

prevents the formation of a solid crust at the interface of liquid and gaseous phases. Crust formation reduces the rate of gas emission.

The degree of digestion or decomposition of organic matter in the fermenters is 30-40%, resulting

in bio-degradable volatile organic compounds.

23-0412-EIA Page


12

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Substrate stays in fermenters within 40 days. When a new substrate (147.076 tons / day) gets in the fermenter, the part of the substrate (141.4 tons / day) which was in fermenters by the pumps onto

pipelines is pumped into the reservoir for further fermentation.

Volume of after fermentation tank is 5654 m3 (Ø = 30 m, h = 8 m). Further fermentation

continues the methanogenesis process in reservoir. The temperature in the tank is +38 º C, the substrate

is always mixed at speed of 1 m / s. Mixers are cyclically raised to the level of the mirror surface and stir

the faction that was formed on the top. This prevents the formation of a solid crust at the interface of

liquid and gaseous phases. The Substrate stays in the tank for 13 days, then is pumped via pipelines into the lagoon at 416.88 tons / day.

Regulation and management process in the fermenter and subsequent fermentation tank is carried

out by means of hot water heating system. 20-millimeter polyethylene pipelines are fixed at a specified

distance from each other inside the fermenter and after fermentation tank which serve to heat the

fermenter and subsequent fermentation vessel and heated with warm water. Distance of 10 cm between

the pipes and the inner wall of the tank provides a static equal heating of the tank. The base of tanks is

isolated outside with 5-centimeter layer of styrodur. Underground tanks and ground part are isolated

outside with 10-centimeter layer of styrodur that is securely fixed on the horizontal joints of plates by galvanized steel tapes (80mm x 8mm) horizontally, around the perimeter of the tank. Ground portion of

tanks is sheathed with aluminum floor insulation. Aluminum sheathing is bolted to galvanized steel tape.

All without exception tank apertures can be controlled visually either when they are installed on

land or underground and equipped with frost-proof foil.

The reservoirs are equipped with 2 blocking units of substrate pipeline allowing to block the

pipeline in case one of the locking device is out of order.

At the bottom of reservoirs is a control aperture of 700h800 mm size which is served to remove

the sand accumulated over time. Each tank is mounted on the perimeter of metal scaffolding for daily control. All working

scaffold are interconnected.

Fermenters and after fermentation tanks are integrated with gas collectors of low pressure (gas

holders) located above the liquid level.

Reservoirs are covered with two conical foils (material: PVC, fabric, lower foil is a highly

flexible polyethylene) and with a bar of gasometric foil fixing. By means of compressed air pump high

pressure air valve a pressure of max. 1.5 mbar is created. This low pressure is transmitted to the lower highly flexible polyethylene foil then to gas storage fermenter and after fermentation tank and creates a

system pressure of biogas. Obtained during anaerobic fermentation biogas is stored above the liquid

level in gas holders of low pressure. Inside the gas holder there is an integrated protection against high

and low pressure, which provides the biogas pressure not exceeding 3 mbar or not lower than 1 mbar.

Due to the special cut the foil creates an airproof conical PVC coverage. In the middle of the cone a

space is created that p rotects the plastic wrap from weather influences and can rise and fall depending on

the production and use of biogas.

Experiences of using such a coverage in snowy regions have demonstrated that at the slope of 30 º, the snow does not remain on smooth surface of PVC foil. It has been proved that slight pressure of 1.5

mbar is sufficient to ensure stability under strong winds. Air proof coverage is a very light structure,

which consists of two polymer foils without hard or metal inserts inside. They reliably protect the tank

from damage caused by pressure from various origins. The forces acting through the foil on the walls of

the tank are small and evenly distributed, so no additional requirements for concrete tanks are needed.

23-0412-EIA Page


13

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Heat insulation tanks are fireproof. The structure and operation gas holders meet operational safety standards of biogas plants.

From after fermentation tanks waste substrate is pumped into the lagoon (repository fermentation

of residues) at 416.88 m3/day. The bottom of the lagoon is covered with waterproof geomembrane that

protects groundwater and soil from the infiltration of the substrate. Lagoons top is closed by

geomembrane, which prevents the penetration of pollutants into the atmosphere and falling of storm

water into organic fertilizer.

3 start-up complex. - For the third phase of construction maize corn silage will be used as a raw materials. For

continuous operation of the process a silage in the quantity of 255 600 t / year should be collected. To

store such a quantity of green mass one needs approximately 9 hectares of land lot where silo storage

facilities will be constructed. The height of the storage silo is from 4 to 6 meters. Silo is placed and

stored in a ground trench of width of 25 m and height of a wall 4 m. Walls and bottom of the silo are

made of monolithic concrete. For removal of sap bows and catching funnels will be fixed by.

Silage is a biological method of preserving herbs formed by fermentation of lactic acid, without air. For

high quality silage the following conditions should be made: - Optimum moisture silage in the trenches should be 70-75%.

- Temperature of the silage mass should not exceed 35 º C

- Robust isolation from the air is to be provided.

Density of silage in trenches shall not be less than 700 kg/m3.

From the silo storage facilities the silage is fed by means forklift into the loading system for hard

substrates. The loading insensitivity of solid substrates is 54.27 tons / day. For start-up unit 12 loading

systems of solid substrates are foreseen.

The system consists of intake container with a moving bottom, electric driven auger and weighing system. Raw material is fed by means of moving bottom onto the augers and loaded onto the

fermenter by pumping system boot for solid substrates: MT-Alligator Plus.

Fermenter has a volume of 4926 m ³ (Ø = 28 m, h = 8 m). Each fermenter is integrated with low

pressure gasholder.

Inside the fermenter a disintegration process of organic matter takes place, which is done by

means of Methane forming and sulphate reducing microorganisms that use metabolites formed at the

early stages. The process of fermentation of raw materials takes place at the temperature of +38 º C, which is

supported by means of the heating tank, which is similar to 1 and 2 start-up complex for 69 days. When

a new raw material gets into the fermenter, a part of the substrate (44.36 tons / day) is pumped via pipes

into the reservoir for further fermentation.

In subsequent fermentation tank decomposition of organic matter takes place for 35 days at the

temperature of +38 º C. Volume fermentation tank is 4926 m³ (Ø=28 м, h=8 м).

Fermenters (12 pcs.) and after fermentation tanks (6 pcs) are equipped with a heating system, gas

container, insulation as complexes1 and 2. The substrate is mixed in reservoirs by agitators. Mixers are cyclically risen to the level of the

mirror surface and stir the faction that was formed on the top. This prevents the formation of a solid crust

at the interface of liquid and gaseous phases.

From after fermentation tank waste substrate is pumped into the lagoon with the intensity of 77.3

tons / day.

The design is similar to lagoons of 1 and 2 start-up complex.

23-0412-EIA Page


14

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Due to processing of chicken manure biogas is produced. Biogas yield depends on the quality of raw materials. Depending on the selected raw material a

biogas composition will be different: for 1 and 2 start-up complexes NSC CH4-58,5%, CO2-38%, for 3

start-up complex CH4-51%, CO2-47% (table 6).

Table 1 biogas composition

Substance 1 and 2 start-up complexes 3 start-up complex

Methane 58,5 % 51 %

Carbon dioxide 38 % 47 %

Oxygen 0,5 % 0,5%

Nitrogen 3 % 1,5%

The volume of produced biogas for 1 start-up complex will be 1711 m³,

41,064 m³/day, 14,988,360 m³/year. The same volume of produced biogas will be for 2 start-up

complex.

The volume of produced biogas for 3 start-up complex will be 6126 m³,

147,024 m³/day, 53,663,760 m³/year.

Biogas is accumulates in gas holders that are placed on top of the tanks. After gasholder gas is cleaned and drained, then goes to the compressor, which increases the pressure from 21 mbar to 940

mbar. When compressing gas is heated to 63 ° C it is then cooled by water to 25 ° C. Then the gas is

transported to the cogeneration plant (CHP). Excessive gas in gasholder or in case of emergency it is

automatically burnt by emergency flares.

For 1 and 2 start-up complexes according to 23-0412- PZ.TEO Jenbacher cogeneration plant

equipment J420 GS B325 in the quantity of 4 pcs and J416 GS B25 - 2 pcs. For 3 start-up unit

Jenbacher J320 C25 in the quantity of 1 pcs is foreseen.

Biogas passes two stages of cleaning: in tanks and external purification system from sulphur. By means control of the air supply in gas holders located above the tank, the air is supplied for

cleaning biogas from hydrogen sulfide. Volumetric air supply is maximum 6% of volume flow of crude

biogas. Mixed cultures of aerobic bacteria oxidize hydrogen sulfide till sulfur and sulphate which

precipitate in the form of salts.

In addition to the three fermenters and subsequent fermentation tank ferric chloride is pumped

into (II). Activation of the pump is performed by means of using a production control system.

Introduction of ferric chloride into reservoirs can reduce the formation of gaseous sulphur compounds: FeCl2 + HS- + H+ -> FeS + 2H+ + 2Cl-.

Thus the first cleaning biogas stage is taking place.

Biogas from 3 fermenters and 1 tank subsequent fermentation is collected and fed to an external

gas pipe system cleaning from sulphur.

Gas comes from reservoirs saturated with water vapor. When transporting biogas gas via pipe the

gas is dried. For condensation of water contained in the raw gas, gas is cooled and moisture is physically

transformed into condensate achieved when reaching the dew point temperature. Dry ing biogas

condensation is a very important step in the enrichment of gas. By means of condensed water a large quantity of ammonia is separated that is contained in the biogas. Ammonia content in biogas may cause

serious engine damage, especially to bearings and non-ferrous metals. Condensate obtained in the

process of drying gas is fed without excess into the biogas plant.

23-0412-EIA Page


15

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Gas drying allows to save specific heat indicator of combustion and increase efficiency at energy production use of the gas as well as to prevent the drop of the pressure in the pipeline and to protect

against corrosion. The condensate is collected and fed back into the fermenter.

For desulphuration technology SulphPur is used. Bacteria located inside the contact filter convert

hydrogen sulfide into a high-quality sulfur. Microorganisms are bacteria that use carbon dioxide for their

living. With minimal supplements of oxygen, these organisms oxidize hydrogen sulfide to elemental

sulphur. Formed sulfur together with the substrate remained are deposited on the bottom of the system

and, depending on the filling level are pumped into the lagoon. All parts are made of polymer or stainless steel. This ensures corrosion resistance and durability

of the system.

It is based on the fact that biological gas cleaning is the ability of microorganisms to oxidize

organic and inorganic compounds of biochemical pathways. Emerging oxidation products from

biological processes are safe for the environment. For example, the oxidation of sulfur-containing

compounds, depending on the availability of oxygen, is formed by sulphur or sulphuric acid.

SulphPur equipment serves to reduce the content of hydrogen sulfide in the biogas. The fate of

hydrogen sulfide in biogas depends on the substrates used for processing of chicken manure, so its work may not be permanent. Different bacteria, under the condition of feeding the oxygen, have the ability to

oxidize hydrogen sulfide to elemental sulphur or sulfuric acid.

1.) Direct oxidation of hydrogen sulfide to sulphate:

H2S+2O2→H2SO4

2.) Oxidation of sulphate at appearing of elemental sulfur as an interim product:

2H2S+O2→2S+2H2O

2S+2H2O→2H2SO4

Conditions that are necessary for biological slitting of hydrogen sulfide: - The presence of oxygen

- Availability of sources of sulphur

- Availability of nitrogen source

- Availability СО2 for bacteria as a carbon source

- Availability of phosphorus

- Minimum pH value equal to 1.

Within the SulphPur technology, contrary to the classical biological desulphurization a flow of biogas is mixed with lesser quantity of oxygen. Due to less oxygen and special performance of the filler

and the reaction chamber, conversion of hydrogen sulfide is completed at the stage of elemental sulphur.

This ensures sulphur reduce to hydrogen sulfide during the process.

Purification of biogas is carried out from carbon dioxide and hydrogen sulfide. Purified biogas is

no different from methane from other sources, i.e. natural gas or SNG (synthetic gas derived from coal

or hydrogen raw materials).

Quality of Biogas is primarily determined by the ratio of methane or fuel Methane (CH4) to the

“unnecessary” carbon dioxide (CO2). Carbon dioxide dilutes biogas and causes losses at storage. The heat of combustion of one cubic meter of biogas reaches 25 MJ which is equivalent to

combustion of 0,61 petrol m³, 0,85 l m³ of alcohol, 1.7 kg of firewood or use of 1.4 kW • h.

The spent substrate of fermentation tanks is poured into the lagoon.

These organic fertilizers contain NH4-N, N organic P2O5, K2O, CaO.

Lagoon twice a year is cleared from organic fertilizers. Organic fertilizers are transmitted onto

farms.

23-0412-EIA Page


16

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

In the fermentation of biomass we obtain highly concentrated organic fertilizer that are devoid of nitrite, weed seeds, pathogenic microorganisms. Tests have demonstrated that the use of such fertilizers

increase yields by 2-4 times.

After commissioning the plant for chicken manure processing from the poultry waste following

substances will be obtained:

- 1 phase of construction - 608,644.8 tons / year of liquid organic fertilizers;

- 2 stage construction - 608,644.8 tons / year of liquid organic fertilizers;

- 3 phase construction - 196,287 tons / year of liquid organic. Production of organic fertilizer from waste poultry (chicken manure) helps to prevent methane

emissions, reduce the use of chemical fertilizers, reduce an overload on groundwater.

3.4. Data on involved resources

Land of 36.79 hectares of land lots are leased by the customer.

Energy data are according to technical specification # 331 as of 13.07.12r. PJSC

“Khmelnitskoblenergo” PS-35/10kV “AVIS”.

Water supply of the chicken manure processing plant will be received from wells. According to

hydrological opinion # 53 of 20.08.12r. State Enterprise “Ukrainian geological companies” demand for water resources is up to 1000 m³/day. The well project will be developed by another project

organization.

Raw materials - 255,600 tons / year of silage, 291,000 tons of chicken manure / year.

Labor resources are 32 people at operation; for construction the quantity of personnel will be

defined according to the working project during the construction period.

3.5. Project data on the estimated amounts of waste

Waste Management, their storage and disposal is done in accordance with the legal documents:

Law of Ukraine “On Environmental Protection” as of 26.06.1991.

Law of Ukraine “On Waste” as of 05.03.1998.

Resolution of cabinet of Ministers “On Approval of the Procedure of state registration and

certification of waste” as of 01.11.1999

3.6. Design data about the calculation wastes’ volumes

Conduct with wastes, their storing and utilization is executed in accordance with the normative-

legal documents:

Law of Ukraine «On protection of environment» of 26.06.1991. Law of Ukraine «On wastes» of 05.03.1998.

Resolution of Cabinet of Ministry of Ukraine «On approval of execution order of state registration

and passport system of wastes» of 01.11.1999.

3.5.1. Calculation of volumes of wastes formation

23-0412-EIA Page


17

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

The quantity of SDW of wastes is calculated according to «Recommended norms of services provision of removal of domestic wastes» (Order of Ministry of questions of housing and communal

services of Ukraine № 75 of 22.03.2010):

Source of domestic wastes formation

Norm of formation of wastes for one calculation unit per month

Norm of wastes creation for one calculation unit per year

kg m3 Kg m

3

Enterprises, institutions and organizations, per one working place

6,25 0,027 - 0,032 75,0 0,32 - 0,38

The construction of poultry manure processing department will be executed in 3 startup

facilities and in the such a succession will be commissioned the biogas units.

Maintenance of 1st startup facility requires 4 persons, for 2d startup facility of construction – 20

persons, for 3d startup facility of construction – 30 people.

The quantity of SDW, which are created at the object during the year is calculated according to

the formula:

P=1000

чп , t/year;

where p – norm of wastes’ creation per one person, kg/year;

ч – quantity of people.

Startup

facility

Quantity of

maintenance staff of

biogas units, pers.

Quantity of wastes, which

are created per month

Quantity of wastes,

which are created per

year

t/month. m3/month. t/year m

3/year

1 8 0,05 0,26 0,6 3,04 2 6 0,04 0,19 0,45 2,28

3 18 0,11 0,58 1,35 6,84

Wastes, received in the process of cleaning of streets, places of general use.

Norm of creation of sweep from the territory is 0,01 t/year with 1 m2 of solid covers, which are

put in order (construction norms and rules 2.07.01-89). The general squire of territory which is swept – 99929,2 m

2.

The quantity of wastes from the putting in order of territory is:

0,01 х 89869,2 = 898,692 t/year.

The cleaning of territory of green planting (grass, leafs and sticks from plantings).

During the cleaning of green territory the norm of creation of wastes of dry leafs, grass and

sticks from plantings is 1,6 kg/year with 1 m2 of landscape territory .

According to cl. 2.17 CN V.2.4-3-95 for sanitary-protection zones broad wise more than 100

meter from the side of village zone have to be provided for planting and have to be no less than 15% from general squire of legal entity.

The squire of landscape is 99929,2 m2.

23-0412-EIA Page


18

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

The quantity of wastes from the cleaning of landscaped territory is: 1,6 х 99929,2 / 1000 = 160 t/year.

It is set up the 4х18W 120 units of luminous tubes for the working lightening of operator

premises of biogas units for the working lightening of operator premises of biogas units - І class of

insecurity .

Outward lightening is executed by the lamp of type ZhKU-250W with lamps DRI-250-6 – 36

pieces set up at the zinc metal supports СС 60/172/3 (h=8m) with distributive box and apparatus of

protection. The quantity of lamps which have to be utilized are:

С = К х G х D / Н, pieces.

where: К – quantity of installed mercury lamps, pieces;

G – approximately average time of work of one luminous tube per twenty four hours, hour.;

D – quantity of working hours per year, twenty four hours.

Н – normative term of service of one luminous tube, hour.

Weight of tubes, which contains the mercury:

Р = СхАх10-3

,т. where: А – weight of one tube, kg.

1. Luminous tubes 18 Wt.

С = 120 ∙ 8 ∙ 320 / 12000 = 26 pieces;

Р = 26∙ 0,11 ∙ 10-3

= 0,003 t.

2. Tubes DРI-250-6.

С = 36 ∙ 12 ∙ 320 / 3000 = 46 pieces.;

Р = 46∙ 0,23 ∙ 10-3

= 0,008 t.

Utilization of worked out luminous tubes is executed by the specialized legal entity. The following wastes, which are provided in the table 7 will be created during the exploitation of

designed object.

Table 1. Wastes which will be created during the exploitation of object and construction

№ п/п

Type of wastes Quantity ,

t/year Class of

insecurity Code for КВ

Method of neutralization of wastes

During the time of object’s exploitation

1 Solid domestic wastes 2,4 t/year

(12,6 m3/year) 4 7720.3.1.01

Removed according to agreement

2 Luminous tubes and wastes which contain mercury, other damaged and worked out wastes

26 piece./year 0,00495 t/year

1 7710.3.1.26 Removed according to agreement

3 Glow lamps 72 piece/year 0,011 t/year


4 Cleaning of territory of green planting (grass, leafs and sticks and sticks from planting)

160 4 1710.2.9.01 Removed according to agreement

5 Wastes of construction works, demolition and reparation of houses and construction

1 4 4510 Removed according to agreement

6 Wastes of packing material 1,68 4 7730.3.1.03 Removed according to agreement

7 Breakage of materials and glass goods 0,24 4 4510.1.3.07 Removed according to agreement

23-0412-EIA Page


19

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

№ п/п Type of wastes

Quantity , t/year

Class of insecurity Code for КВ

Method of neutralization of wastes

8 Film or cover on the basis of polymer 0,12 4 1753.1.1.03 Removed according to agreement

9 Tires, defective before the beginning of exploitation, worked out, damaged or polluted during the exploitation

5 4 6000.2.9.03 Removed according to agreement

10 Worked out oil 0,00389 2 9010.2.3.03 Removed according to agreement

11 Wiping clothes 3 3 7730.3.1.06 Removed according to agreement

12 Sweep materials 898,692 4 4510.2.9.04 Removed according to agreement

During construction of object

1

Wall items concrete defective, polluted or non-identified, which could not be used for their purpose (gas concrete blocks)

According to fact of creation


2

Substance connected damaged or non-identified, their rests, which could not be used according to their purpose (cement solution and concrete mixture)



3

Reinforced concrete constructions and metal details from iron, steel damaged (defective) or non-identified (cuttings of corners, channels and double tees )


4 4510.2.9.06


4 Worked out transmission, motor and other oils and lubricants



5 Other worked out hydraulic lubricants According to

fact of creation 2 6000.2.8.07 Removed according to agreement

6 Rests of asphalt and mixtures asphalt-concrete

According to fact of creation 3 4510.2.9.04


7 Materials glass – capacious fibrous According to fact of creation


8 Glass breakage reinforced According to


9 Cuttings of board According to


10 Cutting of metal According to

fact of creation 2811.2.1 Removed according to agreement

11 Metal and plastic tare from coloring materials



12 Wiping materials According to

fact of creation 4 7730.3.1.06


13 Sand fouled with masut According to fact of creation


Solid domestic wastes which are created in the process of exploitation, accumulated in the

specialized containers which are places at the commercial sites for waste of such territory of object.

23-0412-EIA Page


20

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

The requirements of separate gathering and storing of solid domestic wastes are taken into account with aim of the execution of requirements of Law of Ukraine «On wastes» during the designing

of object. The site for separate gathering of solid domestic wastes (SDW) is installed at the territory of

object according to the «Methodology recommendation of organization of gathering, transportation,

processing and utilization of solid domestic wastes», approved by the Order of Ministry of Housing and

Municipal of Ukraine of 11.08.2008. № 247. At each site it is installed two types of containers for the

separate collection of SDW, namely:

- container of blue color for collection of valued recourse (glass, paper, polymer) with title «secondary raw material»;

- container of red color for collection of dangerous wastes with title «dangerous wastes»;

- rubbish gathering containers which accept mixed wastes, colored in grey color;

- container of orange color for collection of a rubbish of construction.

Wastes, created under the time of exploitation of object are transferred according to agreements

to specialized legal entities.

Clean sweep devices of container type are set up for collection of wastes at the territory of

object which are placed at the sites with solid cover for maintenance of free entrance of transport for their uploading and transportation to the objects of p lacement in the places of utilization.

Wastes are gathered at the specially allotted and equipped sites of temporary storing of wastes.

All volumes of wastes will be detailed under the elaboration of design of poultry manure

processing department.

3.7. Assessment of possibility of appearance and development of emergency situations

Appearance of violation of technological process is possible during the time of exploitation of

poultry manure processing department:

- breakdown of cogeneration unit; - total rejection of network supply;

- foamy fermentation in the tank;

- overflow of tanks;

- excessive creation of biogas;

Poultry manure processing department is equipped by the specialized alarm system on breakages

in the technological process with transfer of information to the mobile phone. Transfer and warning is

executed with a help of independent from the network the accumulation system of telephone notification.

In the time of response of alarm signal, the system is not stop the attempts to connect till the moment when one from responsible for installation persons will not be notified. Thus, the chain of notification is

locked.

For securing of safe exploitation it is provided the installation of control-measuring devices and

means of automation, which will secure:

- control of technological parameters;

- control of level of raw materials in tanks;

- pressure in piping of supply for technological needs of water and wind, in gas highway and volumes;

- volumes of water, which supplied;

- quantity of produced and used for technological needs: gas, heat and electro energy;

23-0412-EIA Page


21

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

- temperature in the technological tanks and heat bearer, which is used for their heating, gas;

- remote and automatic management of technological equipment;

- alarm of normal work and emergency conditions of systems.

- the installation of complete control desk, which will provide for the local and distance

regimes of management for management of work of cogeneration and flare installations, pump station

and boreholes, compressor and ventilation equipment also.

- It is provided the installation in the premises of controller and alarm which is used for the distance management of equipment.

The management of work of technological equipment is executed according to the program or by

the controller distantly.

A gas alarm, which has the relative permission for use and certified in Ukraine for control and

alarm of increase of concentration of methane of more than accepted norm in the places of its possible

outlet and accumulation is used. Alarm is intended to the automatic continuous control of highly

explosive concentrations of methane and (or) volume part of carbon monoxide in the air, issue of light

and sound alarm and also for outlet of electrical signals for off-station facilities and switching of external electrical circles for exceeding of set up meanings of volume parts of controlled gases.

Except the equipment for operational control and management of process it is provided the

installation of equipment which secures the collection, storing and processing of information about the

work and separate components as well as poultry manure processing department in general.

The successful exploitation of biogas unit is not possible without the daily control of important

components of unit.

The permanent production of gas with small daily vibrations is the first sign of stable process.

In the most simple case the stable and steady process could be defined by the permanent filling of gas holder.

If parameters of efficiency will be stable, the process will flow stable also, however they are not

provide the information about the quality of gas.

It is possible to provide the assessment of gas quality , if execute the proportion between the

quantity of produced electrical energy and quantity of processed gas.

As the quantity of stream is going down under the same level of gas consummation, it is

connected with the worse quality of biogas (if exclude the technical mistakes in generator). In the time of the accounting of such parameters, it is possible to control and calculate all

important characteristics of process connected with production of gas and electrical energy. Herewith it

helps not only data but also trends, which show the direction of process development.

For analysis and processing of information it is provided the organization of automated working

place (APM) of controller – personal computer with special program software, program software of

analysis level and processing of information provides:

- visualization of equipment work and processes;

- permanent control for current value of technological parameters and work of equipment; - control and informing about the emergency situations in the equipment work;

- maintenance of archive database.

Also, the department is equipped by the special system of alarm about the failure in the work of

equipment with transfer of notification to the mobile phone. The transfer and notification is executed

through the independent from the electrical network accumulator system of telephone notification.

23-0412-EIA Page


22

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Under the response of alarm, the system doesn’t stop the possibility to connect to the moment, when one from the responsible for the installation person will be informed.

Breakage of cogeneration unit

In case of full breakage of cogeneration unit, the production of gas in fermenter is go down with

the help of interruption of supply of raw material in tanks till the restoration of their exploitation readiness.

The first startup facility : maximum volume of biogas production is 1711,04 m3/year. Volume of

gas holders of 1st startup facility is 10610 m3. Under the expense of biogas of cogeneration unit

705 m3/year it is executed the normal regime of exploitation of department with a minimum level of gas

in gas collector. Because the volume of gas collection of department under the normal regime of

exploitation is 10610 m3, in case of breakage of units there is the temporal buffer without the necessity

of adoption of any further measures.

The second startup facility : Maximum production of biogas is near 1711,04 m3/year. Under the expenses of biogas of cogeneration unit 1974 m3/year it is executed the normal regime of exploitation of

department under the minimum level of gas in the gas collector. Because the volume of gas collector

under the normal regime of exploitation is 10.610 m3, in case of breakage of units there is approximately

6 hour buffer without the necessity of adoption of any further measures.

Third startup facility : Maximum production of biogas is near 6122,67 m3/year. Under the expense

of biogas of cogeneration unit 12000 m3/year it is executed the normal regime of department exploitation

under the minimum level of gas in gas collector. Because the volume of gas collector of department

under the normal regime of exploitation is 10610 m3, in case of breakage of units we have approximately 2 hour buffer without the necessity of acceptance of any further measures.

Under the breakage of cogeneration unit it is provided the signal of alarm and activated the

system of telephone notification. After the receipt of notification about the breakages, the responsible for

the work of department can switch off the mixers and stop the supply of substrate. Thus, the production

of gas is noticeably decreased. As a rule, this period of time is sufficient for the restoration of normal

regime of work of cogeneration unit, execute technical and repair works or change engine.

The total rejection of network supply

Under the total refusal of network supply the accumulator system of telephone notification is

activated and supply of substrate is stopped by force. The unit is constructed in that way that in case of

total rejection of network supply, the possibility of overflow of source from tanks is stopped. The

production of gas continues however it has a falling character. When buffer of gas collector is exhausted,

the utilization of biogas begins with a help of flare.

Foam fermentation in tanks Foam fermentation could appear in case of overload of biological environment in fermenter.

The overloads raise in case:

- when technological hour of methane fermentation was calculated out of stock;

- working space of fermenter is overloaded;

- if substrates in high quantity without control were put in fermenter.

As technological time of methane fermentation is not more than 40 twenty four hours, production

23-0412-EIA Page


23

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

of working space is less than 3m³ of gas for 1 m³ of working space per day, the substrate is provided by small portions several times per day, than the substrate is supplied by small portions several times per

day the substrate is provided by small portions several times per day, than the possibility of foam

fermentation is too low. Thankful to the optimal fitting out of system of supply of liquid of first and

second startup facilities of construction supported the further uniformity of substrate.

If the foam fermentation appeared, that it is timely registered by the probe of overflow.

Under the contact with foam, the probe provides the signal of violation in work and at the same

time the system of telephone notification is activated and blocked the supply of any substrates. With a help of intensive mixture, the appeared foam could be mixed. Because the foam is

registered by the probe with the 0,5 of height of free side of tank up to the level of substrate.

The turn of system of high / decreased pressure is placed up to the 0,5 meters which gives the sufficient

time for inclusion of mixers. Thus, the situation when the protection of increased / decreased pressure

could be broken because of impact of foam fermentation is excluded.

Overflow of tanks

Overflow of tanks is excluded. All tanks are equipped by the probes of overflow. Thus, it is

achieved the timely notification about of level of overflow in tanks. Under the contact with liquid the probe is activated and signal of malfunction is provided and at the same time it is executed the activation

of notification system and blocked any supply of substrates. The substrate of fermentation is registered

by the probe with 0,5 m of free tank side under the level of substrate and the turn of protection system

from the high/decreased pressure could go out in case of impact of fermentation substrate.

Excessive production of gas.

Excessive production of gas under the right exploitation of unit is excluded. Only in case of

wrong actions, for example of excessive input of free substrate could raise the similar situation.

Because substrate is supplied by small dozes to fermenter and because the loader of solid substrates and accumulated tank has limited capacity , the appearance of similar situation is practically

excluded.

In case of appearance of similar situation when the existent volume of gas storing is fully loaded,

the utilization of rests of gas is executed by means of their burning in the flame.

The dosed quantity depends on the level of gas-collectors filling tanks and expenses of gas of

cogeneration unit.

If the level of gas in gas collector is getting low, the more substrate is loaded, if the level of gas is increased, than the dosing of substrate is decreased or timely fully stopped.

The general buffer volume for biogas produced in the process of anaerobic processing of biomass

is:

- for the first startup facility - 16.976 m³

- for second startup facility - 16.976 m³

- for third startup facility - 31.140 m³

First startup facility

6 х gas collectors of low pressure of fermenter Ø inter. 30 m x 8 m 2.122 m³ each. = 12.732 m³

2 х gas collectors of low pressure of tank of the further fermentation Ø

inter. 30 m x 8 m

2.122 m³ each. = 4.244 m³

Total 16.976 m³

Second startup facility

23-0412-EIA Page


24

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

6 х gas collectors of low pressure of fermenter Ø inter. 30 m x 8 m 2.122 m³ each. = 12.732 m³

2 х gas collectors of low pressure of tank of the further fermentation Ø

int. 30 m x 8 m

2.122 m³ each. = 4.244 m³

Total 16.976 m³

Third startup facility

12 х gas collectors of low pressure of Ø inter. 28 m x 8 m 1.730 m³ each. = 20.760 m³

6 х gas collectors of low pressure of tank of the further fermentation Ø intern. 28 m x 8 m

1.730 m³ each. = 10.380 m³

Total 31.140 m³

Under the normal work of unit, the gas collector of tanks of further fermentation is kept in the

empty state.

All gas-collectors is equipped by the indicator of level of gas. The unit can automatically switch

off the indicator of level.

For prevention of uncontrolled entrance of air, the gas system is equipped by the separate regulator of minimum pressure which under the decreased pressure of 0,5 mbar switches off the

cogeneration unit and gives the signal about the failures in the system of telephone notice.

With aim of prevention of uncontrolled inflow of air, the gas system is equipped by the separate

regulator of minimum pressure, which under the decreased pressure of 0,5 mbar switches off the

cogeneration unit and gives the signal of failure to the system of telephone notification.

Regulator in the gas collector which is activated from the vacuum of gas, directly, blocks the

supply of gas to cogeneration unit. Thus, safety device is obliquely activated in a cogeneration unit.

Thus, cogeneration unit and module of fermentation is not classified, because they are connected one with other of unit and from the side of safety engineering they are not connected one with other.

Because of the high explosiveness of collection and transportation systems of biogas the special

requirements are settled.

1. Shop for processing poultry manure must have a fence, within which at the time of

maintenance it is forbidden to smoke, to use the gas and electric welding equipment and tools that can

create a spark. The distance of the fence from the gasholder, gas appliances, relating to the system of drawing up, storage and delivery of gas should be not less than 1,0 m. on the fence there must be the

signs of safety in the places convenient for viewing.

2. Buildings and constructions of the enterprise shall be provided with primary fire extinguishing

means in accordance with the "Rules of fire safety in Ukraine" and the requirements of industry

standards. Production and storage buildings should be equipped with automatic fire-extinguishing means

and fire alarm in accordance with the lists given in DBN В.2.5-56:2010; the outer fire-extinguishing

means should be provided also.

3. Fire breaks between gasholders for combustible gases and buildings or constructions shall be defined by the table 8.

The distance from the gas-holders to air power supports = 2/3 of the distance between the

supports, but not less than 1,5 of the support`s height.

4. The room, in which the system of collection and transport of biogas is installed, should be

classified as category A (НАПБ Б.03.002-2007( The rules determining categories of premises, buildings

and outdoor facilities for fire and explosion risks).

23-0412-EIA Page


25

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Table 1. Fire breaks between gas-holders, buildings and structures for combustible gases

Name of buildings and constructions Breaks from wet gas-

holders, m

Residential and public buildings and facilities 100

Traffic areas of common use (train, tram, car-truck and pedestrian )

50

Production and auxiliary buildings of industrial enterprises

I and II level of fire resistance

III,IV and V level of fire-resistance

25

40

Auxiliary premises and facilities for maintenance of gas-holders 15

Access and internal factory Railways and roads 20

5. Electrical drives and other elements of the system in accordance with the explosion-resistance

requirements ДНАОП 0.00-1.32-01:

Class 1

gas-collecting points,

gas-holders control room,

degassing facilities room,

moisture separator & gas-cleaning equipment,

gas regulation setting ; Class 2

Degassing facilities,

Gas-holders.

Gas holders with combustible gases, according to EAR, are referred to as explosive outdoor

installations of the Class B-1g. Explosive zones around gas holders have the following dimensions: 5 m

vertically and horizontally from the discharge pipes, safety valves and vents. In case of absence of pipes

for gas discharge and valves the explosive area for these gases should be 3 m Gas input and output chambers are referred to (according to the EAR) hazardous areas Class B-

1.

To support the work of collection and recycling system for biogas it should be provided with

control of the following process parameters:

- Pressure in the pipelines;

- The temperature of biogas and recycled water in degassing units;

- Expenditure of biogas;

- Content of methane, carbon dioxide, hydrogen sulfide and oxygen in biogas. There also should be installed some special alarm sensors adjusted to recognize the explosive concentrations of methane. Biogas in a mixture with air can explode if the percentage in the total mixture is 6-12% and there is a source of ignition with temperatures over 700 ° C. Danger of explosion arises also if the content of biogas in the air is more than 12%.

7. To install light-signaler in the process control panel, which prevents formation of dangerous concentration of oxygen in the biogas pipelines and methane concentration in the premises.

8. In the premises, where leakage of Methane is possible, it is necessary to provide adequate

ventilation and air-sucking through the ceiling vents. To mark the explosive area. To ensure the curtain

of water over facilities and reservoirs. To take measures to prevent the accumulation of electrostatic

charge and avoid sources of ignition. In case of fire, to provide the using of fire extinguishers and fire-

blankets at the workplace. Location of gas must be marked with special signs.

23-0412-EIA Page


26

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

In case of emergency in the shop of processing chicken manure, it is designed a lagoon. Substrate and digestate are pumped by pipeline pressure in the lagoon.

Each tank has a valve for substrate / digestate pipelines. Each pipeline is provided with wells for

maintenance and accumulation of substrate / digestate, in case of emergencies. Substrate / digestate is

pumped out with the help of scavenge-machine and merged into the lagoon.

In case of overflow of gasholder the flare is automatically switched on and excess gas is burned.

The possibility of an emergency situation is absent.

3.8. The list and characteristics of potential environmental impact sources. Sources of impacts on the environment during the operation and building of the object are as

follows:

a) the geological environment:

- the impact on the geological layers when digging the Foundation pit and carrying out the

works on construction of engineering networks;

- influence of the building;

- load impact from vehicles during the construction and operation of the object.

b) air environment:

- when operating: air emissions from storage tanks, boiler and cogeneration devices; - during building works: emissions from motor vehicles (nitrogen dioxide, carbon monoxide,

hydrocarbons boundary) and welding (iron oxides, manganese oxides, silicon dioxide, fluorides

well/poorly soluble in water, hydrogen fluoride), paint jobs, during loading and unloading of

construction materials.

c) soil:

- The formation of excess of mineral soil during building works;

- Waste from the operation of the object.

3.9. The list of potentially influenced objects and potential boundaries of influenced area during construction and operation of the object Conditions of work execution at the site in accordance with the established order are

coordinated with the relevant bodies of the state supervision, the local administration, motor-way

police inspectorate and operational organizations.

The sources ensuring electricity and water supply while building are the existing network of the

area. Working-places, driveways and walkways to them should be well-lit. The place for the passage

of people through the trenches, descents and ascents should be equipped with stairs with handrails. At

the places where the installation work is carried out it is not allowed to perform other works, as well

as the location of unauthorized persons.

It is necessary to provide measures on fire safety , providing the placement of fire hydrants in the water supply network or a mobile tank with water.

In the process of building the environmental protection measures must be observed: it is

Prohibited to perform preparatory work, import materials and products, place machinery,

mechanisms and equipment at the work site before it is fenced and equipped with technical means to

arrange the traffic.

The location of the temporary facilities (cabins for builders, roads, networks) should be carried

out in coordination with the existing landscape. In carrying out construction works vertical planning is made alongside with continued with the least possible amount of excavation works. When

23-0412-EIA Page


27

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

performing of earthworks it will be provided to save, if possible, the landscape and soil-vegetation covering.

Temporary excavation pits, drainage ditches and other similar structures must be performed so,

that to prevent soil erosion, erosion of slopes, formation of gullies. In temporary reserves and dumps

should be excluded washout of both of vegetative and mineral soil.

Carrying out the vertical planning provides for maximum recovery of soils, which are

extracted from the pits.

When carrying out the building works all the equipment should be in working condition, it is not allowed to sp ill fuel on the territory that is being developed.

Washing, filling and maintenance of building machinery should be carried out at specially

equipped places, on which it is necessary to provide a package of measures, p reventing the ingress of

polluted water, residual fuel in underground water and in the place of location of existing green

plantations.

Delivery of construction debris and the creation of spontaneous dumps on the building site are

forbidden.

Storage of wastes of building production should be conducted in specially allocated for this field in containers for building waste. To bury wastes is strictly prohibited, they should regularly be

disposed to landfill, in accordance with a certificate provided by the customer. The collection of

debris must be performed with the use of spray guns, which pump the water in places of dust

formation.

At the summer-time the building site should be regularly watered. The area adjacent to the

building site should be cleaned of dust and dirt in time.

Arrangement of working areas and responsibility for proper placement and storage of building

equipment relies on the organization that performs the work.

4. ASSESSMENT OF ENVIRONMENTAL IMPACTS OF PLANNED ACTIVITIES

In the assessment of impact on the natural environment there are such components:

• climate and microclimate;

• air environment ; • geological environment;

• the water environment;

• soils;

• flora and fauna, and reserve area.

4.1. Climate and microclimate

The area of building site is classified as П-В in accordance with БНШ 2.01.01-82. The climate

is temperate continental with cold winters and warm summers. The average annual temperature, according to data of Khmelnitsky weather station is +7,8 º C. The coldest month - January, with an

average temperature -5 º C, the warmest month - July with temperature +18,4 º C. The absolute

minimum and maximum temperature is, respectively, -8.1 and +24,5 º C. Regulatory freezing depth

of soil is 0.84 m, the characteristic snow load 127 kg/cm2,the characteristic wind loads 46 kg/cm2.

Factor of stratification - 200.

The terrain factor - 1.

23-0412-EIA Page


28

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Speedofthewind, frequency above which is 5% - 6 m / s. The average wind speed for the year - 3 m / s.

The possibility of micro-climatic conditions favoring to spreading of harmful species of fauna and flora is absent.

Negative impact on the climate and microclimate, as well as the associated negative

environmental changes as a result of the planned facility is not expected.

4.2. Air environment.

Sources of impact on atmospheric air in the process of operation of the object are as follows:

- openings in tanks;

- chimneys of cogeneration facilities (CGF), boiler;

- motor transport.

4.2.1. Calculations of emissions from the vents in the tanks

During operation of the shop for processing poultry manure according to the technological

scheme from the bubbler tanks and pre-mixing tanks there will be released hazardous substances into

the atmospheric air. To reduce the negative impact of the reservoirs it is envisaged to direct the output

of gas in the biofilter. The efficiency of gas cleaning: for Ammonia - 80%, for hydrogen sulfide - 90%.

Emissions of the i-th component of gas from water solutions are calculated according to the formula:

- maximal emission (Мi, g / s):

- annual emission (Gt, t / year)

where: КГmin, КГmах – constant of Henry with a minimum and maximum temperatures,

respectively, mm Hg.;

Xi - mass fraction of substance;

Крср, Кр

mах - coefficients are taken from Annex 8 MU OVZVAR. Vч

max - the maximum amount of vapor mixture, which is being displaced from the tank during

pumping, m3/h;

Tжmin, Tж

mах - minimum and maximum temperature of the liquid in the reservoir, respectively,

°C;

t1, t2 - the operation of the reservoir by day / year and hour / day.

Calculated data are given in Table 6.

4.2.2. The calculation of emissions from CHP

The composition of the biogas, burned in cogenerating units of 1-2 launch complexes: CH4 = 58,5%;

CO2 = 38 %;

N2 = 3%;

23-0412-EIA Page


29

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

O2 = 0,5 %. Calculations carried on MAC 34.02.305 - 2002 "Methods of calculation of emissions of pollutants into

the atmosphere from power units."

Specific weight of each individual biogas:

413,05,5801,0716,0CH01,00,716 4CH4

vm ,

0HC01,01,342 62HC 62

vm ,

0HC01,01,967 83HC 83

vm ,

0HC01,02,593 104HC 1 04

vm ,

0HC01,03,219 125HC 1 25

vm ,

0HC01,0,8463 146C6H1 4

vm ,

0375,0301,01,250N01,01,250 2N2

vm ,

0SH01,01,521 2SH2

vm ,

0CO01,01,250CO vm ,

746,03801,01,964CO01,01,964 2CO2

vm .

Density of dry gaseous fuel under normal conditions :

2,1ρ222 COCOSHNHCн mmmmm qp kg/m

3.

Mass composition of dry gas fuel is determined by the following formulae:

%43)273,0746,0413,075,0(1,2

100

273,0429,012

12100C

2COCOHC

н

mmm

qp

pqp

daf

%6,8)0413,025,0(1,2

100

059,012

100H

SHHC

н2

mm

qp

qqp

daf

%125,30375,01,2

100

ρ

100N

2N

н

mdaf ,

0941,0ρ

100S SH

н2 mdaf ,

%2,45)746,0727,00571,0(1,2

100727,0571,0

ρ

100O

2COCO

н

mmdaf.

Where: Cdaf

– mass content of carbon in the fuel on the flammable mass, %;

Hdaf – mass content of hydrogen in the fuel on the flammable mass, %;

N daf – mass content of nitrogen in the fuel on the flammable mass, %;

O daf

– the mass of the oxygen content in the fuel on the flammable mass, %.

Thus, we obtained a value, % of mass of the element composition of biogas:

carbon – C r =Cdaf = 43;

hydrogen – H r =H

daf = 8,6;

oxygen – O r =O

daf = 45,2;

23-0412-EIA Page


30

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

nitrogen – N r =N daf = 3,125. - The mass of the spent fuel gas B, t, for a period of time P and mass combustion heat for 1 CHP:

- CHP J420 GSB325

8,724 нvBB kg/hour,

3,201 нvBB g/s,

25,6349 нvBB t/year,

- CHP J416GSB25


161 нvBB g/s,


3,182,1/22/ нriv

ri QQ МJ/kg.

According to the specifications of the manufacturer of CHP the concentration of pollutants in flue gases at 5% oxygen content is:

СNOх=500 mg\m3, CCO=980 mg\m3.

To reduce emissions of polluting substances, the catalytic method of cleaning of exhaust gases is

used. Catalyst oxidant-catalyst is installed immediately after the CHP before silencers and chimney with

efficiency of cleaning of exhaust gases CO-80% and applies nitrogen-cleaning installation of NOx -

40%.

Concentration of substances in the flowing gases at 3% oxygen content after cleaning will be:

СС� = 221mg\m�, С��х = 338mg\m�.

The composition of the biogas, which is burned at CHP of the 3-rd launch complex:

CH4 = 51 %; CO2 = 47 %;

N2 = 1,5 %;

O2 = 0,5 %.

Calculations carried on MAC 34.02.305 - 2002 "Methods of calculation of emissions of pollutants into

the atmosphere from power units."

Specific weight of each individual biogas:

365,05101,0716,0CH01,00,716 4CH4

vm ,

0HC01,01,342 62HC 62

vm ,

0HC01,01,967 83HC 83

vm ,

0HC01,02,593 104HC 1 04

vm ,

0HC01,03,219 125HC 1 25

vm ,

0HC01,0,8463 146C6H1 4

vm ,

019,05,101,01,250N01,01,250 2N2

vm ,

0SH01,01,521 2SH2

vm ,

0CO01,01,250CO vm ,

923,04701,01,964CO01,01,964 2CO2

vm .

Density of dry gaseous fuel, under normal conditions :

3,1ρ222 COCOSHNHCн mmmmm qp kg/m3.

23-0412-EIA Page


31

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Mass composition of dry gaseous fuel is determined by the following formulae:

%40)273,0923,0365,075,0(1,3

100

273,0429,012

12100C

2COCOHC

н

mmm

qp

pqp

daf

%7)0365,025,0(1,3

100

059,012

100H

SHHC

н2

mm

qp

qqp

daf

%5,1019,01,3

100

ρ

100N

2N

н

mdaf ,

0941,0ρ

100S SH

н2 mdaf ,

%6,51)923,0727,00571,0(1,3

100727,0571,0

ρ

100O

2COCO

н

mmdaf.

Where: Cdaf

– mass content of carbon in the fuel on the flammable mass, %;

Hdaf – mass content of hydrogen in the fuel on the flammable mass, %;

N daf – mass content of nitrogen in the fuel on the flammable mass, %;

O daf

– mass content of oxygen in the fuel on the flammable mass, %.

Thus, we obtained a value, % of mass of the element composition of natural gas:

carbon – C r =Cdaf = 40;

hydrogen – H r =H

daf = 7;

oxygen – O r =O

daf = 51,6;

nitrogen – N r =N daf = 1,5.

The mass of the spent fuel gas B, t, for a period of time P and mass combustion heat for 1 CHP:

- CHP J320 С25:


1,161 нvBB g/s,


9,162,1/22/ нriv

ri QQ МJ/kg.

According to the specifications of the manufacturer of CHP the concentration of pollutants in

flowing gases at 5% oxygen content is:

СNOх=450 mg\m3, CCO=900 mg\m3.

To reduce emissions of polluting substances, the catalytic method of cleaning of exhaust gases is

used. Catalyst oxidant-catalyst is installed immediately after the CHP before silencers and chimney with

efficiency of cleaning of exhaust gases СО – 80% and applies nitrogen-cleaning installation of NOx –

40%.

Concentrations of substances in the flowing gases at 3% oxygen content after cleaning will be:

СС� = 203mg\m�, С��х = 304mg\m�.

Gross emissions of polluting substances:

i

r

ii ijii jijQBkEE

610 ,

23-0412-EIA Page


32

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Where: Eji – gross emissions of the j-th pollutant during the burning of the i-th fuel for the period of time P, t;

kji – the emission indicator of the i-th pollutant for the i-th fuel, g/GJ;

Bi – the flow rate of the i-th fuel for the period of P,

(Qri)i –

below the working heat of combustion of the i-th fuel, MJ/kg.

r

iд гjQvck

j,

Where: с´j – measured mass concentration of the j-th pollutants in dry flue gas reduced to

standard conditions and standard oxygen content, mg/Nm3;

vдг – specific volume of dry flue gas, corrected to standard oxygen content, m3/kg.

1-2 start-up complexes:

23,6O7,0H56,5762,3N8,0S7,0866,1762,4100

4,1CДГ rrrrrCv Nm3/kg.

1,5O7,0H56,5762,3N8,0S7,0866,1762,4100

4,1CДГ rrrrrCv Nm3/kg.

3 start-up complex: The results of the calculations are recorded in the table. 10.

4.2.3. Calculations of pollutant emissions of motor transport.

The calculation is made according to the methodology of calculation of emissions of pollutants

and greenhouse gas emissions into the air by transport vehicles, approved by order of the State

Committee of statistics of Ukraine, № 452 of 13.11.2008 and ВНТП –СГіП 46.16-96. Release of the i-th of the pollutant (g/s) transport flow that moves on the highway (or part of it)

with fixed length L (km) is calculated by the formula:

k

VkП

ikL ikikGM

LM

1, ,3600

Where:МкіП- running exhaust emission of the i-th of the pollutant by vehicles of k-th group,

g/km;

k - the number of groups of cars, units;

Gk- the intensity of traffic, 1/hour;

�� - correcting coefficient, taking into account the average speed of traffic on the highway (or the part of it);

L - the length of the highway (or its part), km;

�

��- conversion factor "hours" into "seconds".

Average fuel consumption is 10L/100km - diesel. Fuel consumption per 1 km is 10:100 = 0.1 liters -

diesel. According to Pos. 2.1.1.of the "Methodology for calculating emissions of pollutants and greenhouse

gases into the atmosphere by vehicles" for transferring fuel in bulk unit applies a factor for diesel fuel –

0,85kg/L. Thus, the fuel consumption is:

23-0412-EIA Page


33

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

0.1 * 0.85 / 1000 = 0.000085 t / km – for diesel fuel.

4.2.4.Estimation of pollution value from 11 front-end loaders, (diesel powered)

Table 9. Pollutants emissions from vehicles

Sou

rce

#

Fue

l

Pol

luta

nt

Un

it e

mis

sio

ns,

kg

/t

The

len

gth

of

maj

or

hig

hway

or

its

par

t, k

m

Fue

l co

nsu

mpt

ion

by

1

veh

icle

, t/k

m

Inte

nsi

ty o

f m

ov

emen

t,

un

its.

/ho

ur

Coe

ffic

ien

t o

f te

chn

ical

st

ate

infl

uen

ce

Coe

ffic

ien

t o

f av

erag

e v

elo

city

of

tran

spo

rt s

trea

m

Op

erat

ion

tim

e, d

ays

Op

erat

ion

tim

e, h

ou

rs

g/s

t/ye

ar

27

Diesel fuel

Nit rogen dioxide 31 ,4 1,5 0,000085 4 0,95 1 365 12 0,0042 0,0666

Carbon oxide 36 ,2 1,5 0,000085 4 1,5 1,35 365 12 0,0104 0,1637

Sul fur dioxide 4,3 1,5 0,000085 4 1 1,35 365 12 0,0008 0,0130 Soot 3,85 1,5 0,000085 4 1,8 1,35 365 12 0,0013 0,0209

Ammonia 0 1,5 0,000085 4 1 1,35 365 12 0,0000 0,0000

Methane 0,08

3 1,5 0,000085 4 1,4 1,35 365 12 0,0000 0,0004

Nit rogen oxide 0,16

5 1,5 0,000085 4 1 1,35 365 12 0,0000 0,0005

Carbon dioxide 3138 1,5 0,000085 4 1 1,35 365 12 0,6001 9,4630 Non-methane

volatile organic compounds 3,08 1,5 0,000085 4 1 1,35 365 12 0,0006 0,0093

benzapyrene 0,03 1,5 0,000085 4 1 1,35 365 12 0,0000 0,0001 28

Diesel fuel


Carbon oxide 36 ,2 1,5 0,000085 4 1,5 1,35 365 12 0,0104 0,1637

Sul fur dioxide 4,3 1,5 0,000085 4 1 1,35 365 12 0,0008 0,0130

Soot 3,85 1,5 0,000085 4 1,8 1,35 365 12 0,0013 0,0209

Ammonia 0 1,5 0,000085 4 1 1,35 365 12 0,0000 0,0000

Methane 0,08

3 1,5 0,000085 4 1,4 1,35 365 12 0,0000 0,0004


5 1,5 0,000085 4 1 1,35 365 12 0,0000 0,0005

Carbon dioxide 3138 1,5 0,000085 4 1 1,35 365 12 0,6001 9,4630 Non-methane

volatile organic compounds 3,08 1,5 0,000085 4 1 1,35 365 12 0,0006 0,0093

benzapyrene 0,03 1,5 0,000085 4 1 1,35 365 12 0,0000 0,0001

29

Diesel fuel


Carbon oxide 36 ,2 1,5 0,000085 12 1,5 1,35 365 12 0,0312 0,4912

Sul fur dioxide 4,3 1,5 0,000085 12 1 1,35 365 12 0,0025 0,0389

Soot 3,85 1,5 0,000085 12 1,8 1,35 365 12 0,0040 0,0627

Ammonia 0 1,5 0,000085 12 1 1,35 365 12 0,0000 0,0000

Methane 0,08

3 1,5 0,000085 12 1,4 1,35 365 12 0,0001 0,0011


5 1,5 0,000085 12 1 1,35 365 12 0,0001 0,0015

Carbon dioxide 3138 1,5 0,000085 12 1 1,35 365 12 1,8004 28,3891

Non-methane volatile organic

compounds 3,08 1,5 0,000085 12 1 1,35 365 12 0,0018 0,0279

benzapyrene 0,03 1,5 0,000085 12 1 1,35 365 12 0,0000 0,0003

35

23-0412-ОВ

НС

А

ркуш

35

Зм

. Кіл.уч.

Арк..

№док

. П

ідп

ис

Д

ата

Table 10. Characteristics of atmosphere pollutants sources

Production, process,

equ ipment, un it

Emission

source nu mber

Emission source name

Emission sou rce parameter

Source coordinates on schematic map, m

The place of takin g

samples

Parameters of gas-and -du st stream in estimation place

The code of

po llutant The name of po llutant

Danger class

MAC/ The

app roximate safe

levels of con centr

ation g/m3

Maximal mass

con centration of

po llutant, mg/m3

Emission power Cons truction stages

Heigh t, m

Open end diameter,

m

Of the point or linear center of

symmetry o f slim axes

Of the second linear; width, leng th of slim

axes

exp ense, m3/s

velo city, m/s

temperature, С

X1 Y1 X2 Y2 g/s t/year

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 19 20 21 22

Storage receiver

1 Vent 2 - 14 7 54 2 2 1 0,8 0,03 18 ,4 30 3 Ammonia 4 0,2 12 ,87 0,010 0,325

start-up

facility 1

33 3 hy drogen sulfide 2 0,00 8 1,26 0,001 0,032

11 81 2 carbo n diox ide - - - 0,002 0,074

Storage receiver 2 vent 2 - 14 7 55 8 2 1 0,8 0,03 18 ,4 30 3 Ammonia 4 0,2 12 ,87 0,010 0,325


11 81 2 carbo n diox ide - - - 0,002 0,074



11 81 2 carbon diox ide - - - 0,002 0,074



11 81 2 carbo n diox ide - - - 0,002 0,074


start-up facility 2


11 81 2 carbo n diox ide - - - 0,002 0,074



11 81 2 carbo n diox ide - - - 0,002 0,074 Storage receiver 7 vent 2 -

48 5 56 2 2 1 0,8 0,03 18 ,4 30 3 Ammonia 4 0,2 12 ,87 0,010 0,325


11 81 2 carbo n diox ide - - - 0,002 0,074



11 81 2 carbo n diox ide

- - - 0,002 0,074

Heat and energy produ cer CHP J420 GS B325

9 waste-gas flue

10 0,3 28 0 48 3 0 0 1,5 21 ,6 42 4 30 1 Nitrogen diox ide 3 0,2 0,07 0,00 01 0,00 32

start-up facility 1

30 4 Nitrogen ox ide 3 0,4 0,41 0,00 06 0,01 96

41 0 Methane - 50 2,42 0,00 37 2,32 81

36

23-0412-ОВ

НС

А

ркуш

36

Зм

. Кіл.уч.

Арк..

№док

. П

ідп

ис

Д

ата


equ ipment, un it

Emission

source nu mber





samples


The code of


Danger class

MAC/ The

app roximate safe

levels of con centr

ation g/m3

Maximal mass

con centration of

po llutant,

mg/m3


Heigh t, m

Open end diameter,

m




axes

exp ense, m3/s

velo city, m/s

temperature, С


1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 19 20 21 22

33 7 Carbo n oxide 4 5 18 1,46 0,27 66 17 4,44 11

11 81 2 Carbo n dioxide - - - 31 7,12 10 00 0,64


10 waste-gas flue


30 4 Nitrogen ox ide 3 0,4 0,41 0,00 06 0,01 96

41 0 Methane - 50 2,42 0,00 37 2,32 81

33 7 Carbo n oxide 4 5 18 1,46 0,27 66 17 4,44 11

11 81 2 Carbo n dioxide - - - 31 7,12 10 00 0,64


11 waste-gas flue


30 4 Nitrogen ox ide 3 0,4 0,41 0,00 05 0,01 57

41 0 Methane - 50 2,42 0,00 30 1,86 17

33 7 Carbo n oxide 4 5 18 1,37 0,22 12 13 9,49 52

11 81 2 Carbo n dioxide - - - 25 3,59 79 97 ,20


12 waste-gas flue


start-up facility 2

30 4 Nitrogen ox ide 3 0,4 0,41 0,00 06 0,01 96

41 0 Methane - 50 2,42 0,00 37 2,32 81

33 7 Carbo n oxide 4 5 18 1,46 0,27 66 17 4,44 11

11 81 2 Carbo n dioxide - - - 31 7,12 10 00 0,64

Heat and energy produ cer CHP

J420 GS B325

13 waste-gas flue


30 4 Nitrogen ox ide 3 0,4 0,41 0,00 06 0,01 96

41 0 Methane - 50 2,42 0,00 37 2,32 81

33 7 Carbo n oxide 4 5 18 1,46 0,27 66 17 4,44 11

11 81 2 Carbo n dioxide - - - 31 7,12 10 00 0,64


14 waste-gas flue


30 4 Nitrogen ox ide 3 0,4 0,41 0,00 05 0,01 57

41 0 Methane - 50 2,42 0,00 30 1,86 17

33 7 Carbo n oxide 4 5 18 1,37 0,22 12 13 9,49 52

11 81 2 Carbo n dioxide - - - 25 3,59 79 97 ,20


15 waste-gas flue

10 0,25 25 6 82 0 0 1,1 22 ,0 45 0 30 1 Nitrogen diox ide 3 0,2 0,06 0,00 01 0,00 20 start-up facility 3 30 4 Nitrogen ox ide 3 0,4 0,36 0,00 04 0,01 23

37

23-0412-ОВ

НС

А

ркуш

37

Зм

. Кіл.уч.

Арк..

№док

. П

ідп

ис

Д

ата


equ ipment, un it

Emission

source nu mber





samples


The code of


Danger class

MAC/ The

app roximate safe

levels of con centr

ation g/m3

Maximal mass

con centration of

po llutant,

mg/m3


Heigh t, m

Open end diameter,

m




axes

exp ense, m3/s

velo city, m/s

temperature, С


1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 19 20 21 22

41 0 Methane - 50 2,53 0,00 27 1,71 91

33 7 Carbo n oxide 4 5 15 4,29 0,16 63 10 4,90 77

11 81 2 Carbo n dioxide - - - 23 5,98 74 41 ,82


16 waste-gas flue

10 0,25 26 4 81 0 0 1,1 22 ,0 45 0 30 1 Nitrogen diox ide 3 0,2 0,06 0,00 01 0,00 20

30 4 Nitrogen ox ide 3 0,4 0,36 0,00 04 0,01 23

41 0 Methane - 50 2,53 0,00 27 1,71 91

33 7 Carbo n oxide 4 5 15 4,29 0,16 63 10 4,90 77

11 81 2 Carbo n dioxide - - - 23 5,98 74 41 ,82


17 waste-gas flue


30 4 Nitrogen ox ide 3 0,4 0,36 0,00 04 0,01 23

41 0 Methane - 50 2,53 0,00 27 1,71 91

33 7 Carbo n oxide 4 5 15 4,29 0,16 63 10 4,90 77

11 81 2 Carbo n dioxide - - - 23 5,98 74 41 ,82


18 waste-gas flue


30 4 Nitrogen ox ide 3 0,4 0,36 0,00 04 0,01 23

41 0 Methane - 50 2,53 0,00 27 1,71 91

33 7 Carbo n oxide 4 5 15 4,29 0,16 63 10 4,90 77

11 81 2 Carbo n dioxide - - - 23 5,98 74 41 ,82


19 waste-gas flue


30 4 Nitrogen ox ide 3 0,4 0,36 0,00 04 0,01 23

41 0 Methane - 50 2,53 0,00 27 1,71 91

33 7 Carbo n oxide 4 5 15 4,29 0,16 63 10 4,90 77

11 81 2 Carbo n dioxide - - - 23 5,98 74 41 ,82


20 waste-gas flue


30 4 Nitrogen ox ide 3 0,4 0,36 0,00 04 0,01 23

41 0 Methane - 50 2,53 0,00 27 1,71 91

33 7 Carbo n oxide 4 5 15 4,29 0,16 63 10 4,90 77

11 81 2 Carbo n dioxide - - - 23 5,98 74 41 ,82


21 waste-gas flue


30 4 Nitrogen ox ide 3 0,4 0,36 0,00 04 0,01 23

41 0 Methane - 50 2,53 0,00 27 1,71 91

38

23-0412-ОВ

НС

А

ркуш

38

Зм

. Кіл.уч.

Арк..

№док

. П

ідп

ис

Д

ата


equ ipment, un it

Emission

source nu mber





samples


The code of


Danger class

MAC/ The

app roximate safe

levels of con centr

ation g/m3

Maximal mass

con centration of

po llutant,

mg/m3


Heigh t, m

Open end diameter,

m




axes

exp ense, m3/s

velo city, m/s

temperature, С


1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 19 20 21 22

33 7 Carbo n oxide 4 5 15 4,29 0,16 63 10 4,90 77

11 81 2 Carbo n dioxide - - - 23 5,98 74 41 ,82


22 waste-gas flue


30 4 Nitrogen ox ide 3 0,4 0,36 0,00 04 0,01 23

41 0 Methane - 50 2,53 0,00 27 1,71 91

33 7 Carbo n oxide 4 5 15 4,29 0,16 63 10 4,90 77

11 81 2 Carbo n dioxide - - - 23 5,98 74 41 ,82


23 waste-gas flue


30 4 Nitrogen ox ide 3 0,4 0,36 0,00 04 0,01 23

41 0 Methane - 50 2,53 0,00 27 1,71 91

33 7 Carbo n oxide 4 5 15 4,29 0,16 63 10 4,90 77

11 81 2 Carbo n dioxide - - - 23 5,98 74 41 ,82


24 waste-gas flue


30 4 Nitrogen ox ide 3 0,4 0,36 0,00 04 0,01 23

41 0 Methane - 50 2,53 0,00 27 1,71 91

33 7 Carbo n oxide 4 5 15 4,29 0,16 63 10 4,90 77

11 81 2 Carbo n dioxide - - - 23 5,98 74 41 ,82


25 waste-gas flue


30 4 Nitrogen ox ide 3 0,4 0,36 0,00 04 0,01 23

41 0 Methane - 50 2,53 0,00 27 1,71 91

33 7 Carbo n oxide 4 5 15 4,29 0,16 63 10 4,90 77

11 81 2 Carbo n dioxide - - - 23 5,98 74 41 ,82


26 waste-gas flue


30 4 Nitrogen ox ide 3 0,4 0,36 0,00 04 0,01 23

41 0 Methane - 50 2,53 0,00 27 1,71 91

33 7 Carbo n oxide 4 5 15 4,29 0,16 63 10 4,90 77

11 81 2 Carbo n dioxide - - - 23 5,98 74 41 ,82

Vehicles

27 - 2 - 21 8 55 7 200 10 8 - - - 18 ,4 30 1

Nitrogen diox ide (NO2) 3 0,2

- 0,00 42 0,06 66

start-up facility 1

33 7 Carbo n oxide (CO) 4 5 - 0,01 37 5 0,43 36

33 0 Sulfur dioxide (SO2) 3 0,5 - 0,01 16 2 0,366 48 84

32 8 Soot (C) 3 0,15 - 0,00 10 9 0,03 43

39

23-0412-ОВ

НС

А

ркуш

39

Зм

. Кіл.уч.

Арк..

№док

. П

ідп

ис

Д

ата


equ ipment, un it

Emission

source nu mber





samples


The code of


Danger class

MAC/ The

app roximate safe

levels of con centr

ation g/m3

Maximal mass

con centration of

po llutant,

mg/m3


Heigh t, m

Open end diameter,

m




axes

exp ense, m3/s

velo city, m/s

temperature, С


1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 19 20 21 22

30 3 Ammonia (NH3) 4 0,2 - 0,00 07 8 0,02 45 9

41 0 Methane (CH4)

- 50 - 2,94 E-05 0,00 09 2

- Nitrogen ox ide (N2O) - - - 4,18 E-05 0,00 13 1

11 81 2 Carbo n dioxide (CO2) - -

- 0,00 17 5 0,05 53 4

27 54 Non -methane vo latile organic compo un ds (НМЛОС) 4 1

- 0,79 46 3 25 ,059 5

70 3 Benzapyrene (C20 H12 ) 1 1E-07 - 7,60 E-06 0,00 02 3

Vehicles 28 - 2 - 41 3 55 6 200 10 8 - - - 18 ,4 30 1


- 0,00 42 0,06 66

start-up facility 2

33 7 Carbo n oxide (CO)

4 5 - 0,01 37 5 0,43 36 3

33 0 Sulfur dioxide (SO2)

3 0,5 - 0,01 16 2 0,36 64

32 8 Soot (C)

3 0,15 - 0,00 10 9 0,03 43 3

30 3 Ammonia (NH3)

4 0,2 - 0,00 07 8 0,02 45 9

41 0 Methane (CH4)

- 50 - 2,94 E-05 0,00 09 2

- Nitrogen ox ide (N2O) - - - 4,18 E-05 0,00 13 1

11 81 2 Carbo n dioxide (CO2) - - - 0,00 17 5 0,05 53

27 54 Non -methane vo latile organic compo un ds (НМЛОС) 4 1

- 0,79 46 3 25 ,059 5

70 3 Benzapyrene (C20 H12 ) 1 1E-07

- 7,60 E-06 0,00 02 3

Vehicles 29 - 2 - 31 0 18 0 423 21 - - - 18 ,4 30 1


- 0,01 27 0,19 99

start-up facility 3

33 7 Carbo n oxide (CO) 4 5 - 0,0137 5 0,43 36

33 0 Sulfur dioxide (SO2) 3 0,5 - 0,01 16 2 0,36 64

32 8 Soot (C) 3 0,15 - 0,00 10 9 0,03 43 3

30 3 Ammonia (NH3) 4 0,2 - 0,00 07 8 0,02 45 9

41 0 Methane (CH4) - 50 - 2,94 E-05 0,00 09 2

- Nitrogen ox ide (N2O) - - - 4,18 E-05 0,00 13

40

23-0412-ОВ

НС

А

ркуш

40

Зм

. Кіл.уч.

Арк..

№док

. П

ідп

ис

Д

ата


equ ipment, un it

Emission

source nu mber





samples


The code of


Danger class

MAC/ The

app roximate safe

levels of con centr

ation g/m3

Maximal mass

con centration of

po llutant,

mg/m3


Heigh t, m

Open end diameter,

m




axes

exp ense, m3/s

velo city, m/s

temperature, С


1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 19 20 21 22

11 81 2 Carbo n dioxide (CO2) - -

- 0,00 17 5 0,05 53 4

27 54 Non -methane vo latile organic compo un ds

4 1

- 0,79 46 3 25,05

70 3 Benzapyrene (C20 H12 ) 1 1E-07 - 7,60 E-06 0,00 02 3

23-0412-EIA Page


41

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Determination of calculation practicability The practicability of diffusion calculations is determined by formula (5.37) under OND-86

provided that:

ГДК

М

>Ф where Ф = 0.01 Н at> 10m Ф = 0.1 at H ≤ 10m M (g/s) is the total value of emission sources; MAC (mg/ m³) is maximal single maximum allowable concentration. H (m) is the average height of the emission source is determined by the formula

)3021()2011()100(

)3021()2011()100( 25155

МММ

МММН

where М is mass of emission of pollutants relative to a certain distance of heights

Table 1 Verification results of calculations of scattering

Substance Code

Class of danger (hazard)

MAC.мр М

_М_

Н Ф Utility MAC mg/m3 g/s - м м -

Nitrogen dioxide 301 3 0,2 2,24E-02 0,1121 5 0,1 Yes Carbon oxide 337 4 5 3,59E+00 0,7172 5 0,1 Yes

Sulfur dioxide 330 3 0,5 3,49E-02 0,0697 5 0,1 No Soot 328 3 0,15 3,27E-03 0,0218 5 0,1 No

Ammonia 303 4 0,2 8,47E-02 0,4236 5 0,1 Yes Methane 410 - 50 5,35E-02 0,0011 5 0,1 No

Non-methane volatile organic compounds

2754 4 1 2,38E+00 2,3839 5 0,1

Yes

Benzapyrene 703 1 1E-07 2,28E-05 227,9070 5 0,1 Yes

Hydrogen sulfide 333 2 0,008 8,09E-03 1,0114 5 0,1 Yes

Calculation of scattering should be done for nitrogen dioxide, carbon oxide, non-methane volatile organic compounds, ammonia, benzapyrene, hydrogen sulphide.

4.2.5. PC modeling of diffusion Calculation of diffusion of pollutants shall be carried out on software "EOL-2000 (h)». The

software meets the current regulatory and technical documents OND-86 and officially approved for such calculations.

Rate relief shall be taken under subclause 2 and 4 OND-86, and it is equal to one. The utility of calculations is cited above and it is performed under the terms of OND-86. The calculation is performed at the ground level. The results of calculation of diffusion of pollutants in the surface layer of the ground are listed

in Appendixes.

4.2.6. Analysis of the carried out calculation The calculation showed that the sanitary protection zone (SPZ) to shop for processing of

chicken manure taking into account of roses of wind shall constitute 560 meters in the North, South, in all other directions it shall constitute 868 meters, while the concentration of pollutants in the surface layer on the brink of SPZ are:

23-0412-EIA Page


42

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

- 0,13 MAC for nitrogen dioxide; - 0,62 MAC for Ammonia; - 0,68 MAC for hydrogen sulphide; - 0,14 MAC for carbon oxide; - 0,16 MAC for benzapyrene; - 0,9 MAC for non-methane volatile organic compounds; - 1 MAC for group of summation №3; - 0,58 MAC for group of summation № 30; - 0,17 MAC for group of summation № 31.

According to the maps of calculation of diffusion it should be possible to conclude about the safety of the object in design stage in terms of air pollution.

4.2.7. Measures of air protection under adverse meteorologic conditions The need to develop measures to regulate air emissions during adverse meteorologic conditions

is justified by territorial authorities for Hydrometeorology and Ecology. Under adverse climatic conditions the process of dispersion of pollutants is disrupted which can

lead to a sharp increase in their concentration in the surface layer of the ground. In order to prevent and effectively counteract this phenomenon its forecasting should be made

in time. The measures shall include: - Regulation of emissions is based on warnings about possible dangerous level of concentrations

of pollutants in the air. - In case of receiving of warnings, the temporary reduction of emissions in adverse

meteorological conditions (calm, fog, temperature inversion, their combination, etc.) shall be performed by the activities of conveying of working mode of the heating source and observance of regulations on operating staff while obtaining information about adverse effects in the atmosphere.

The calculation takes into account the diffusion under adverse climatic conditions (under 2.2 OND - 86).

While performing calculations on diffusion it shall be taken into account the diffusion during

adverse climate conditions (according to clause.2.2 ОНД – 86).

4.2.8. Suggestions for defining of sanitary protection zones According to ДСП 173-96 "Public Health Regulations of planning and development of urban

areas", approved by the regulation of Ministry of Health of Ukraine as of 19.06.96 № 173, the regulatory sanitary protection zone for this facility is set forth through calculation method. According to the paragraph 7.1 ВНТП-АПК-04.05 the distance from the plant for processing of chicken manure with use of biogas technology to the limits of residential development area is at least 300 meters.

According to the calculation of scattering the SPZ for workshop for processing of chicken manure taking into account the rose of winds shall be defined at the level of 560 meters in North and South directions, and 868 meters in all other directions.

4.2.9. Establishment of ambient air monitoring system, methodology,

controlling measures Control over emissions and environmental pollution during operation of the facility shall be

performed by the representative of the owner. Emissions of the pollutants from the facility shall not exceed the calculated values. Monitoring and analysis of the work shall be carried out by specialized and authorized organizations not less than provided by regulation and legal acts.

Control review shall be performed by relevant competent organizations.

23-0412-EIA Page


43

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

4.3. Geological environment and soil Characteristics and assessment of impacts on the geological environment of the designed

activity, and recommendations for mitigation of negative impact are provided in the sections "Engineering and Geological conditions" and "Engineering and hydrological conditions" of this ОВНС.

In case of respect of the above recommendations, the impact from the construction and operation of plant for processing of chicken manure on the geological environment shall be within legal parameters and shall not lead to a deterioration of conditions of the environment.

4.4. Water environment All buildings and premises on the area that need water supply shall be attached to wells located in

the south of the site. The number of wells to meet the needs of the workshop shall be 4 according to

hydro geological report. Total water consumption for industrial needs constitutes 353 200 tons per year

(176,600 tons per year for the first stage and 176 600 tons per year for the second stage). For the third

stage the supply with water is not required.

Table 1. Water consumption and water evacuation of the object

№ Name of

consumer

Water supply Water evacuation Irrevocable wastes

m3/hour m3/day m3/year m3/hour m3/day m3/year m3/hour m3/day m3/year

1 1launch facility 20,2 483,8 176600 20,2 483,8 176600 0 0 0

2 2launch facility 20,2 483,8 176600 20,16 483,82 176600 0 0 0

The water is conveyed to water supply system of the workshop for processing of chicken manure

by several ways: first - directly from the well, the second - water from treatment plant (projected under another contract). To save a reserve of water from wells, it shall be used water from the storage lake of

treatment facilities.

Water supply system passes from the well to the receiving and storage tank. To increase the ratio

of C: N the fresh water shall be mandatory supplied during the preparation of the working raw material

according to technology.

The fermenter is equipped with water pipe directly to the observation window in order to be

washed with some water from inside for visual observation over the process and to the bottom drain

pipe. Every day the bottom drain is washed with high pressure water to prevent it from silting. The source of water supply for external fire is projected water supply network of the ground

equipped with fire hydrants.

The water from wells shall be used in order to supply the sanitary container. Domestic sewage

will be connected to sewage treatment p lants.

Rain water canalization system is designed to evacuate rainwater and melt water from the

territory of the projected enterprise.

Rain and melt water from the roof of buildings, silos and from the territory of the enterprise with solid surfacing, are assigned as separate network in kind of system weirs connected to the collector of

rain water, which is laid from the farms to the treatment p lants.

The tanks for receiving of rainwater connected to the gravity rainwater drainage network shall be

installed at the site. The discharges are transported to treatment plants, where after its treatment shall be

released to the “bio lake”. Design of treatment facilities is not included in the volume of design

“Workshop for processing of chicken manure.”

Gutters, downspouts funnels shall be equipped with electrical system of anti-icing.

23-0412-EIA Page


44

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

There shall not be an effect of facility (designed object) on the conditions of surface and ground waters, water facilities and areas. The project provides for solid pavement of roadways and installation

of rain water canalization.

Wastewaters generated at the facility , shall come to the workshop for processing of chicken

manure and shall be used in the technology process.

Emergency situations, accompanied by adverse effects on ground and surface waters, and other

water facilities are not foreseen.

4.5. Flore and fauna. Wildlife reservation objects. Migration routes of animals and birds in the area of the designed object are not detected. Objects of protected areas and areas favorable to the establishment of p rotected areas (reserved

for this purpose) are not available on the playground area. The surrounding area shall be landscaped and planted with high rise and valuable gas-resistant

species according to elaborated scheme. Area of landscaping will be 99 929.2 m2 - 27% of the total area.

4.6. Characteristics of other environmental impacts

The designed object does not produce radiation, rays, radio wave pollution.

4.7. Noise pollution Analysis shall be performed over the maximum level of noise generated when driving cars

across the workshop for processing of chicken manure. The degree of danger determines exceeding of sanitary standards ГДР.мак.

Noise impact of the designed object on adjacent building is produced while entering and

leaving cars across the territory, while technology transport is driven on the territory . This effect shall

be limited to sanitary gaps.

The following condition shall be met for the designed object: entrances and exits shall be

located no closer than 15 meters from the windows of working rooms [clause 5.29 ДСП 173-96].

Equipment for the plant for processing of chicken manure shall be chosen with the lowest

noise performance. Technological equipment shall be placed in noise-isolated rooms or protective covers.

5. IMPACT ASSESSMENT OF PLANNED ACTIVITY ON THE SOCIAL AND TECHNOGENIC ENVIRONMENT

5.1 Social environment The ground for designed object is situated in the village of Humentsi, Kamianets-Podilskyi

Raion, Khmelnytskyi Oblast. Construction will be carried out on the designated area of land.

Processing of chicken manure into organic fertilizer and energy will improve the

environment, reduce emissions into the atmosphere from poultry farms and shall create new jobs for

local inhabitants.

Operation of the facility will not create adverse effects on the industrial, agricultural, housing

23-0412-EIA Page


45

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

and community facilities, surface and underground structures and other elements of the technogenic environment.

The impact on social environment is accepted as permissible.

5.2 Technogenic environment Operation of the facility will not cause technogenic load on the environment. There are no objects of technogenic environment that may provoke a negative influence on

designed activity.

6. COMPLEX MEASURES TO ENSURE NORMAL CONDITIONS OF ENVIRONMENT AND ITS SAFETY

Resource saving measures The project design decisions foresee sufficient measures for saving and rational use of land,

water, energy and fuel resources and recycling of wastes.

Protective measures Measures of nature conservation are provided in this project, including the arrangement of

temporary and permanent protective structures (including drainage and protective screens) shall be deemed as sufficient and reasonable. The proposed technological measures provide for the use of ecologically clean and waste-free technologies, modern, efficient purification systems, environmentally safe waste management. Planning events that include zoning and landscaping elements prevent excessive impact on the environment, health and welfare of local inhabitants.

Restoring measures The project design decision specifies technical and biologic recultivation of damaged land

resources with followed step by step normalization of conditions of separate components of environment.

Compensative measures Project includes measures to improve the natural, social and technological environment of the

site. It is also provided for material responsibility for the damages resulting from storing of construction and industrial waste as long as performing of building works

Impact assessment of industrial wastes produced by planned activity Evaluation of environmental impacts is provided in the relevant sections of the ОВНС

materials, together with data on the proposed technological solutions to reduce emissions, discharges and waste derived from the planned activities. It is assumed that the planned activities will not exceed the hygienic and ecologic standards established in Ukraine.

Increased frequency of accidents or other emergency situations by sector affiliation of the object of the planned activity is not expected.

Technical solutions for the prevention of accidents and assuring fire safety with a description of control systems and automatic control and alarm systems are discussed in the section “Fire security” which provides information about the systems of internal and external fire extinction.

23-0412-EIA Page


46

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Design decisions are justified and optimally satisfy the requirements of environmental and sanitation legislation and provide the necessary operational reliability for the objects of technogenic environment.

Estimated residual effects that were grounded in the material are calculated.

Assessment of risk of planned activity on the health of population

Risk assessment of the planned activity on the public health from air pollution is performed by calculating risks of carcinogenic and non-carcinogenic effects.

The risk of carcinogenic effects is determined by calculating the index of risk (НІ) which

evaluation is in accordance with Table Ж.1 according to formula (Ж.1):

)1.(, ЖHQHI i

where HQi are Hazard Quotient for separate substances that are defined according to formula (Ж.2):

)2.(, ЖCR

CHQ

if

ii

where Сі is an average annual calculated concentration of 1st substance on the limits of the

residential development, mg/m³; RfCi is reference (safe) concentration of the 1

st substance mg/m³;

HQi = 1 – limits amount of accepted risk. According to clause 4.2.2 MR 2.2.12-142-2007 to determine the risk of impact of atmospheric

air on the health of people it is actually allowed to limit their amount by the substances indicative for the given area. If we analyze the emissions of pollutants, it can be concluded that in this case the priority is the emissions of carbon oxide.

The concentration of carbon oxide at the nearest residential premises is 0.054 MAC (0.027 mg/m3) in accordance with the calculations performed on computer.

According to Section 4.4.1 MP 2.2.12-142-2007, in case of absence of reference concentrations it can be used as the equivalent the maximum allowable concentration (MAC) or maximum inactive levels or concentrations (МНР, МНК) that have been established upon the criterion of direct effect on health. In this case the reference (safe) concentration of carbon monoxide RfC = 3 mg/m

3.

09,03

027,0HQ

The evaluation of non cancerigenic risk is performed according to the Table Ж.1.

Table Ж.1

Characteristics of risk Hazard Quotient (HQ)

The risk of hazards is extremely small Less than 1

Limit value of accepted risk 1

Evidence of development of harmful effects is growing in

proportionally to increase of HQ Greater than 1

Thus, non-cancerigenic risk to public health from exposure of carbon oxide in the air is extremely small (0.09 <1), and this effect can be considered as acceptable, there is no likelihood of harmful effects among the population.

23-0412-EIA Page


47

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Assessment of social risk of planned activities influence Social risk from planned activity is defined as the risk for group of people, which may be

affected by the implementation of facility into economic activity, taking into account of particular features of natural and technogenic system.

Estimated value of social risk (Rs) is defined by the formula (И.1):

)1.(),1( ИNT

NVCRR puas

where Rs is a social risk, people/year; CRa is a cancerigenic risk of combined action of several cancerigenic substances, polluting the

atmosphere that is defined in the Appendix Ж, (3,1*10-6); Vu is vulnerability of the area from the air pollution, which is determined by the ratio of the

area, designed to the object of economic activity to the area of the object with the sanitary protection zone, ratio of a unit;

N is quantity of population that is defined by: a) data of urban district of the situation of the object, if any, and b) according to the total urban settlement, if there is no districts or if an object is city forming, c) according to urban settlements situated in the zone of influence of the project to be designed, if it is situated beyond its limits, people;

The population in the place of location of the object is N ≈ 2114 people. Т is an average life expectancy (is defined for given region or shall be taken as 70 years),

people/year; Np is ratio, defined as the ratio of additional jobs to amount of population for calculation (N)

for new construction of the facility ; while reconstruction with the increase in the amount of jobs is determined by the ratio of amount of additional jobs to the previous amount; with reduction – by the ratio of the absolute value of reducing of amount of jobs to the previous number.

56 103)016,01(70

2114

560000

200000103 sR

Evaluation of social risk from the planned activities is carried out in accordance with the Table. И.1.

Table И.1

Level of risk Lifelong risk Unacceptable for professional staff and population More than 10-3 Acceptable for professional staff and unacceptable for population 10

-3 – 10

-4

Conditionally accepted 10-4 – 10-6 Acceptable Less than 10-6

Thus, the level of social risk of planned activity is conditionally acceptable.

7. ASSESSMENT OF ENVIRONMENTAL IMPACTS DURING CONSTRUCTION

The project of building identifies the need and sufficiency for the construction and installation of the construction site. The building site is located on the construction site of the projected object.

Construction materials are produced in factories, their installation is only performed on site. The concrete will be delivered in place only in the "mixer". The bulk materials shall be covered when transporting.

The construction site does not foresee the arrangement of boiler-house plants, performance of maintenance and repair of auto vehicles, varnishing and painting works, blacksmith work, charging batteries, repair of rubber technical products, mechanic processing of metals, copper works, repair and test of engines, fuel equipment, washing parts, assemblies and aggregates. In addition to

23-0412-EIA Page


48

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

working construction and specialized machines, the most dangerous for the population are manufacturing operations of welding and cutting metal.

Characteristics of sources of air pollution It is provided that in building process it is used a typical set of construction machinery and

mechanisms (according to ПОБ).

Table 1. Major construction machinery and assemblies according to ПОБ

№ Name Type, model quantity

1 Excavator ЭО-4121 4

2 Bulldozer ДЗ-53 6

3 Clampshell-type excavator Casagrande 4

4 Excavator with clampshell equipment Hitachi EX-5 2

5 Excavator CAT-307 2

6 Frontal loader 2

7 Drillsite bench Baner BG 40 2

8 Water pumps НЦС-3, НЦС-4 2

ГНОМ 25-20 8

9 Pneumatic beetle machines or ТР-1 6

10 Electric beetle machines ІЕ-450 6

11 Smooth drum roller on pneumatic tires ДУ-31 2

12 Rollers on pneumatic tires ДУ-11 2

13 Hand guided roller BW 60S 1

14 Compressor ЗИФ-55 4

15 Cement-mixer СБ-69 4

16 Concrete pump Бн 80-20 4

17 Welding aggregate АСБ-300 8

18 Welding transformator ТД-300 8

19 Internal vibrator ИБ-61 8

20 Road vibrator 4

21 Board auto vehicle ЗИЛ-130 8

22 Gravel truck auto vehicle КАМ АЗ-5511 30

23 Tower crane COM ANSA 4

Calculation of emissions from road construction machinery is the main pollutants contained in

the exhaust gases of diesel and gasoline ICE launchers: carbon monoxide (CO), hydrocarbons (CH),

nitrogen oxides (NOx),

7.1. Calculations of pollutant emissions from vehicles and machinery during the engineering

preparation of area and construction work

The number of freight transport and mechanisms that work at the construction site taken under

the project and the construction of 131 units. In the calculations of pollutant emissions factor used

simultaneous operation of machinery, at 0.3.

Calculation of mass emission performed according VNTP-SHiP-46-16.96.

Gross Output:

23-0412-EIA Page


49

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

where - mass emissions of each pollutant;

- specific emissions of substances of one car;

- conditional car mileage;

- number of machines operating with increasing factor of production;

- correction coefficient that takes into account mode of the vehicle;

- number of working days per year. Maximum one-time (emission during 1 second):

where – mass emissions of pollutants g/sec;

– interval of production or returning cars.

For calculation the coefficient of separation adopted as 0,8

Table 4. Emissions from construction vehicles and machinery

Table 5. Total emissions from vehicles during construction:

Name of pollutants MAC Quantity of emissions

mg/m³ g/s t/year

Nitrogen dioxide 0,2 0,00856 0,08870

Carbon oxide 5,0 0,05538 0,57416

Saturated hydrocarbons 1,0 0,01533 0,15898

7.2. Welding and metal cutting

Basic designs are made in factories, directly on construction site, only fitting and their

connection occurred.

Number of pollutants during welding that depends on the brand of electrode grade welded

metal, seam type, etc., is determined by specific parameters depending on the cost of welding

materials:

;****10. 6 ДKALqрікМ ei

N

j

ijі

ірікМ .

ijq

L

iA

eK

Д

;*6,3

*****10. 3

вип

eiijN

j

іТ

ДKALqмрМ

імрМ .

випТ

Construction

1 year

Normal

excretion

The

conditio

n for

mileage

Number

of cars

coefficient

of

correction

Amount

of work

Time of

operatio

n

Maximum one

time emissions

Gross

emission

s

g/km km

pcs /

day days h/day g/sec t/year

Nitrogen

dioxide 7,7

0,8 40

1,0

360 8

0,00856 0,08870

Carbon oxide 35,6 1,4 0,05538 0,57416

Saturated

hydrocarbons 11,5 1,2 0,01533 0,15898

23-0412-EIA Page


50

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

3Gi = 3600*

3 *

раб

рабi

t

bg

where: 3Gi – maximum one-time emission in welding, g / s;

3ig – specific emissions, g / kg of welding metals;

рабb – welding materials costs during the working day, kg;

рабt – exact duration of welding during the day, h;

Specific emissions of pollutants in manual arc welding and referral artificial electrodes (g / kg), where AZ - aerosol welding; Mn - manganese and its compounds; FeO - iron oxide; Dust - inorganic

dust containing 20-70% SiO2; HF - hydrogen fluoride gas; F - solid fluorides in terms of fluorine; Cr6

+ - 6-valent chromium; NO2 - Nitrogen dioxide; CO - carbon oxide.

Table 6. Specific emissions of pollutants in manual arc welding and referral artificial

electrodes (g / kg)

Electrodes AW

Components of aerosol welding (AW) g / kg

gaseous solid

NO2 С HF Mn FeO Cr6+

F Dust

УОНИ 13/45 18,0 1,50 13,3 0,75 0,92 10,69 - 3,4 1,40

УОНИ 13/55 18,0 2,70 13,3 0,93 1,09 14,90 - - 1,00

УОНИ 13/65 7,5 - - 1,17 1,41 4,49 - 0,80 0,80

УОНИ 13/80 11,2 - - 1,14 0,78 8,32 - 1,05 1,05

УОНИ 13/85 13,0 - - 1,10 0,60 9,80 - 1,30 1,30

АНО-1 9,6 - - 2,13 0,43 9,17 - - -

АНО-3 17,0 - - - 1,58 15,42 - - -

АНО-4 17,8 - - - 1,66 15,73 - - 0,41

АНО-5 14,4 - - - 1,87 12,53 - - -

АНО-6 16,7 - - - 1,73 14,97 - - -

АНО-7 12,4 0,35 4,5 0,40 1,77 8,53 - 1,00 1,10

ОЗС-3 15,3 - - - 0,42 14,88 - - -

ОЗС-4 10,9 - - - 1,27 9,63 - - -

ОЗС-6 14,0 - - 1,53 0,86 12,94 - - -

ЭА-981/15 10,3 - - 0,80 0,74 8,75 0,81 - -

МР-3 11,5 - - 0,40 1,73 9,77 - - -

МР-4 11,0 - - 0,40 1,10 9,90 - - -

Average values 13,4 1,51 10,4 0,98 1,17 11,20 0,81 1,51 1,01

Considering that type, grade and number of electrodes should be clarified, to assess the impact

on the environment were averaged specific emissions constituents of welding fumes.

Emissions of pollutants generated during welding 1 post welding electrodes with costs 2.5 kg of

"pure" duration of 3:00

Gезі = gезі × 2.5/3.0 × 3600 = gезі×0.00023

Table 7. Components of aerosol welding

23-0412-EIA Page


51

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Electrodes AW

Components of aerosol welding (AW) g / kg

gaseous solid

NO2 С HF Mn FeO Cr 6+ F Dust

Average

values

2.5 0.003082 0.000347 0.002392 0.0002254 0.000269 0.002576 0.000186 0.000347 0.000232

Table 8. Maximum possible maximum single mass emissions of construction equipment, 2 electric

welding posts metals from construction site M.mr, g / s

Types of

works

СО СН NOх С SO2 HF Mn FeO F Cr6+

construction

machinery

0,05538 0,01533 0,00856

Electric

welding

0.000 0.0000 0.00069 0.0048 0.0000 0.00045 0.00054 0.0052 0.00069 0.00037

TOTAL 0,05538 0,01533 0,00925 0.0093 0.0020 0.00045 0.00054 0.0052 0.00069 0.00037

7.3. Definition of appropriate calculations for dispersion of pollutants in ambient air

Works performed on different heights of the building. For reliability 10m is taken Assessment

and calculation of ground concentrations of contaminants coincides with approaches to calculations and estimates emissions of from other stationary sources (see "Air quality"). To accelerate and simplify the

calculations, ground concentrations of contaminants according to p.5.21 OND-86 determined the

feasibility perform these calculations. Only the emissions of pollutants, for which the following

conditions are satisfied, are being calculated:

М / MAC.мр > Ф,

Ф = 0.01 х Н where Н > 10м; Ф = 0.10 where Н ≤ 10м;

М.мр amount of emissions from all sources, g / s

MAC.мр

maximum one-time MAC, mg/m3

Н.зв =

10.0м

average altitude of emission sources, m

The results of determining the feasibility of dispersion calculations of pollutant emissions in the

surface layer are presented in Table. 9.

Table 9. The feasibility of dispersion calculations on computers CL emissions of during

construction

Substance MAC.мр М, g/s М/MAC Н Ф Feasibility

mg/m3 - m m

301 Nitrogen

dioxide NO2 0.2 0,00925 0.04625 10 0.1 No

203 Chrome Cr6+

0.0015 0.00037 0.025 10 0.1 No

123 iron oxide FeO 0.4 0.0052 0.013 10 0.1 No

328 Soot С 0.15 0.0045 0.03 10 0.1 No

337 Carbon oxide СО 5.0 0,05538 0.011076 10 0.1 No

2754 Hydrocarbons СН 1.0 0,01533 0,01533 10 0.1 No

143 Manganese Mn 0.01 0.00054 0.05 10 0.1 No

342 Fluorides F 0.02 0.00069 0.035 10 0.1 No

23-0412-EIA Page


52

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

330 Sulfur

dioxide SO2 0.5 0.002 0.004 10 0.1 No

Calculation on software system EOL – was not performed.

During the construction small amount of construction waste and debris are produced. All of

them are exported from the object under contractual relationships.

23-0412-EIA Page


53

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

8. COMPREHENSIVE ASSESSMENT OF OBJECT THAT IS PROJECTED ON ENVIRONMENT AND CHARACTERISTICS OF RESIDUAL EFFECTS

1. The climate and microclimate - no effect; 2. Air quality - affects; 3. Geological environment - influence within the standards; 4. Aquatic environment - influence within the standards; 5. Flora and fauna - are not affected 6. Soils - no effect. There is a temporary impact during construction, it will stop with the end of

construction; 7. On the social environment - affects. 8. On the technogenic environment - does not affect. 9. In emergency situations - does not affect. Air pollution pollutants from motor vehicles, biogas and cogeneration plants are related to the

residual effects. In the surface layer on the territory of the object will increase the concentration of pollutants to:

- 0,13 MAC by nitrogen dioxide; - 0,62 MAC by Ammonia; - 0,68 MAC by hydrogen sulfide; - 0,14 MAC by carbon oxide; - 0,16 MAC by benzapyrene; - 0,9 MAC by non-methane volatile organic compounds; - 1 MAC by group summation # 3; - 0,58 MAC by group summation № 30; - 0,17 MAC by group summation № 31.

According to the maps of dispersion calculation, we can conclude about the safety of the design object in terms of air pollution.

23-0412-EIA Page


54

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

9. STATEMENT ON ENVIRONMENTAL EFFECTS OF ACTIVITY

The purpose of the planned activities - recycling poultry according to DBN 360-92 **. Ways to fulfill the purpose - building workshop for processing chicken manure. Possibility of environmental emergencies - the risk of environmental emergencies (explosion

and / or fire) does not exceed typical for populous cities of Ukraine.

Significant impacts on the natural environment: emissions from tanks, cogeneration plants, vehicles; industrial waste.

Rates of environmental risk Construction of plant for processing chicken manure comes under sanitary classification ext. 4

DSP-173-96 and requires sanitary protection zone (SPZ) 560m in N, S directions, in all other areas of 868m. Operation of the facility increases the concentration of pollutants in the air for a small amount in the surface layer of the atmosphere. When performing environmental protection and health standards during construction and exploitation of objects virtually no adverse effects on the environment.

Chemical contamination. The analysis of all components of the environment and possible impacts on them suggests that the greatest impact as a result of the project will be carried out on air. The sources of air pollution are holes in tanks shop for processing chicken manure, chimneys cogeneration plants, vehicles, p laced in the territory .

In air pollutants will be emitted annually in the amount of: Dioxin nitrogen - 0.37 tons carbon oxides - 2236.9 tons dioxin sulfur - 1.09 tons of carbon

black - 0.1 t, Ammonia - 2,67 m, Methane - 33.7 tons of carbon dioxide - 145,299.6 tons, saturated hydrocarbons - 75.1 tons, benzapyrene - 0,0007 tons of hydrogen sulfide - 0.255 t.

Calculated amount of maximum ground concentration of pollutants on the verge of SPZ is: on NOx <1M AC, in CO <1M AC, in H2S <1M AC, in NH4 <1M AC, for benzapyrene <1M AC, non-methane volatile organic compounds <1MAC - the maximum allowable concentration is not exceeded.

Noise impact on population. Technological equipment is installed in noise protection structures. The level of noise exposure does not exceed 50 dB around home, that is the nearest to the workshop of for processing chicken manure within. Humentsi.

Impact on surface waters. Water from wells, discharge waste waters occurs in closed lagoon that guarantees the safety of the planned activity for surface water.

Effects on soil and geological environment of the object are defined as immaterial. Impact on flora and fauna - the area after construction will be landscaped according to

dendrological plan. The level of impact is taken as acceptable. The level of social risk of the planned activity is acceptable Safety assessments for population activities. Security for the life of the population levels of

chemical and noise impacts are guaranteed. Measures to ensure the realization of the planned activity in accordance with environmental standards and regulations:

Using the equipment for cleaning gases. Installation of equipment in noise protection areas. Landscaping and planting the surrounding area according to dendrological plan.

The project provides the application of equipment with improved environmental, energy-efficient performance and fire protection system.

The project is designed in compliance with applicable building, sanitary, fire regulations and rules.

23-0412-EIA Page


55

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Measures taken to inform the public about planned activities, objectives and ways of implementation: awareness by the media.

Public benefits from the implementation of the planned activities: providing people with comfortable housing, new jobs are created, updated local budget.

The obligation of the customer on the design solutions in accordance with the rules and regulations of environmental protection and environmental safety requirements at all stages of construction and operation of the planned activity Issuing a statement on the environmental impact in the media; reconstruction / construction and operation of the projected activities in accordance with

regulations of environmental protection and environmental safety requirements.

Customer:

PJSC agricultural company “AVIS"

Director V. V. Rudenko

Chief designer:

Ltd. «M onolittransbud»

Director Y.Y. Rusyn

Executant EIA:

Ltd «ENERGI-INVEST»

CEO S.V.Fishchuk

23-0412-EIA Page


56

S

ub

st.

Inv

. №

S

ign

atu

re a

nd

da

te

Іnv

. №

ori

gin

al

Annexes

Зм. Кільк Арк. №док Підп. Дата

Стадія Арк.

2CPE

Verified

Director Fischuk Аркушів

M 1:500

"Energo-Invest" LLCYuzkov

2

23-0412-OBHC

AVIS POULTRY MANURE PROCESSING DEPARTMENT

ТЕОSite layout plan

03.13

03.13

03.13

03.13

cattle farm area

Poultry area

13682.08

205984.36

ʢ

ʘ

ʥ

ʘ

ʚ

ʘ

ʢ

ʘ

ʥ

ʘ

ʚ

ʘ

ʢʘ

ʥ

ʘ

ʚ

ʘ

239,08

0,4ʢʚ

13682.08

491.16

100775.46

16506.82

333.91

30.72

19.09

329.18

50.16

16522.70

301.61

54.93

300.00

30.72

24.23

16522.70

303.21

54.64

301.61

24.92

29.73

16522.70

304.80

54.35

303.21

18.75

35.61

16506.83

306.38

54.02

304.80

12.23

41.81

16484.19

285.04

59.37

277.31

2.90

13.93

0.65

52.69

16484.20

260.95

63.22

5.89

285.04

60.93

16484.19

232.12

77.56

260.95

67.68

6660.25

91.16

28.67

23.07

108.71

117.61

16522.69

338.58

24.92

24.23

333.91

49.50

16522.69

343.19

18.75

29.73

338.58

48.83

16522.69

347.74

12.23

35.61

343.19

48.18

16506.82

345.29

5.70

41.81

347.74

14.35

33.38

21086.05

296.85

65.31

5.60

297.93

70.90

21319.82

295.76

67.55

4.40

296.85

71.95

22981.58

294.58

64.27

13.59

295.76

77.86

24421.81

96.88

122.72

171.69

2.28

58.76

294.58

18781.60

297.93

67.66

2.02

13.89

216.05

29.75

40.00

29.75

26.99

43.75

22.71

16484.20

75.29

108.71

30.75

20.00

46.18

232.12

0.70

43.46

44.84

16484.20

56.27

306.80

54.81

299.01

16506.83

48.40

339.77

48.18

345.29

16538.56

5.70

48.18

307.96

53.82

306.38

24735.55

64.27

58.76

116.92

37.53

56.73

109.43

64.27

296.42

24193.06

296.42

81.25

299.91

67.55

13.59

21100.28

299.91

44.54

26.61

310.06

65.31

4.40

16999.36

310.06

19.87

58.99

23.60

168.46

20.38

77.07

67.66

5.60

277.31

60.09

299.01

46.41

15.30

7.84

9823.76

168.46

68.57

25.68

106.36

47.89

20.38

16506.82

333.91

30.72

19.09

329.18

50.16

16522.70

301.61

54.93

300.00

30.72

24.23

16522.70

303.21

54.64

301.61

24.92

29.73

16522.70

304.80

54.35

303.21

18.75

35.61

16506.83

306.38

54.02

304.80

12.23

41.81

16522.69

338.58

24.92

24.23

333.91

49.50

16522.69

343.19

18.75

29.73

338.58

48.83

16522.69

347.74

12.23

35.61

343.19

48.18

16506.82

345.29

5.70

41.81

347.74

14.35

33.38

16506.83

48.40

48.18

345.29

16538.56

5.70

48.18

307.96

53.82

306.38

20000

Poultry SPZ

PMPD SPZ SPZ - sanitary protection zone

Fischuk

Site layout plan