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7/28/2019 Waste Heat Recovery Cdm Project at Attock Cement Pakistan Ltd.
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PROJECT DESIGN DOCUMENT FORM (CDM-SSC-PDD) - Version 03 CDM Executive Board
1
CLEAN DEVELOPMENT MECHANISM
PROJECT DESIGN DOCUMENT FORM (CDM-SSC-PDD)
Version 03 - in effect as of: 22 December 2006
CONTENTS
A. General description of the small scale project activity
B. Application of a baseline and monitoring methodology
C. Duration of the project activity / crediting period
D. Environmental impacts
E. Stakeholders comments
Annexes
Annex 1: Contact information on participants in the proposed small scale project activity
Annex 2: Information regarding public funding
Annex 3: Baseline information
Annex 4: Monitoring Information
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Revision history of this document
VersionNumber
Date Description and reason of revision
01 21 January
2003
Initial adoption
02 8 July 2005 The Board agreed to revise the CDM SSC PDD to reflectguidance and clarifications provided by the Board since
version 01 of this document.
As a consequence, the guidelines for completing CDM SSCPDD have been revised accordingly to version 2. The latest
version can be found at
.
03 22 December
2006 The Board agreed to revise the CDM project design
document for small-scale activities (CDM-SSC-PDD), taking
into account CDM-PDD and CDM-NM.
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SECTION A. General description of small-scale project activity
A.1 Title of the small-scale project activity:
>>
Waste Heat Recovery CDM Project at Attock Cement Pakistan Ltd.
Version: 2.3
28/03/2012
A.2. Description of the small-scale project activity:
>>
The Attock Cement Waste Heat Recovery for Power Generation Project, herein referred to as the project
or the project activity, will comprise the installation of waste heat recovery and electricity generation
technology at the Attock Cement Pakistan Ltd. (ACPL) cement plant in Hub Chowki, Pakistan. Projectowner is the cement plant owner Attock Cement Pakistan Ltd., international cooperation partner (CER-
buyer) of this bilateral CDM project is the German company UPM Umwelt-Projekt-Management GmbH.
The Attock Cement plant has a rated clinker output of 5,700 tons of clinker per day produced in two
production lines. Line 1 (operational since 1988) has a capacity of 2,400 tons/day and Line 2 (operational
since 2006) has a production capacity of 3,300 tons per day. The waste heat of these two production lines
will be recovered and utilized to drive a 12 MW power plant that generates electricity for captive use of
the cement plant. The average power available for consumption will be 8.1 MW. Based on the rated
capacity of the two production lines (7,200 operations hours per year), the electricity consumption of the
cement plant will be reduced by 58,320,000 KWh.
In the absence of the project activity all waste heat that will be recovered and utilized during the projectactivity is vented to the atmosphere. During the project lifetime, the generated electricity will be used for
captive purposes and thereby reduce the total power uptake of the cement plant. The power generated by
the project activity will therefore replace electricity provided by the national electricity grid of the
Karachi Electric Supply Company (KESC) Since the electricity provided by the KESC grid is mainly
generated using fossil fuels, the replacement of 58,320,000 KWh will result in an annual emission
reduction of 34,417 tCO2e. Project emissions will occur due to electricity and fossil fuel consumption of
water pumps that will provide the additional water demand of 2,800 m3/day to the waste heat recovery
plant.
The proposed project activity will contribute to a local sustainable development with the following
effects:
Economic development:
Pakistan is passing through an acute energy crisis. Under the circumstances, the power plant will at least
cut short its 8.1 MW demand of power from the national grid.
This should contribute to a reduction in the number of black-outs and brown-outs experienced by other
grid users, which can help to improve the economic performance of other businesses connected to the
grid.
Social development:
During its construction period of about 15 months, about 500 people of all categories will get jobs -
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though for a short period. While during its regular operations, it will engage around 40-45 staff members.
Environmental development:By resulting in a significant reduction of greenhouse gas emissions and reducing the so-called heat-isle
effect, the project contributes to a sustainable development of the local environment.
Technological development:
By installing Chinese technology in Pakistan, the project facilitates technology transfer and therefore
promotes technological development.
A.3. Project participants:
>>
NameofPartyinvolved
(host)indicatesaHost
Party)
Privateand/orpublic
entity(ies)
projectparticipants
(asapplicable)
Kindlyindicateif
thePartyinvolved
wishestobe
consideredas
project
participant
(Yes/No)
Islamic Republic of Pakistan Attock Cement Pakistan Ltd. No
United Kingdom of Great Britain
and Northern Ireland
UPM Umwelt-Projekt-
Management GmbH
No
Project owner: Attock Cement Pakistan Ltd.Attock Cement Pakistan Limited (ACPL) was incorporated in Pakistan on October 14, 1981 as a Public
Limited Company and listed on the Karachi Stock Exchange. The company started its commercial
production in June, 1988.
CER buyer: UPM Umwelt-Projekt-Management GmbH
UPM Umwelt-Projekt-Management GmbH was originally founded at the beginning of the 1990s to
provide project management and consulting services in the field of lean gas utilization projects. Today,
UPM is mainly working in the field of Clean Development Mechanism (CDM) within the framework of
the Kyoto Protocol.
A.4. Technical description of the small-scale project activity:
A.4.1. Location of the small-scale project activity:
>>
A.4.1.1. Host Party(ies):
>>
Islamic Republic of Pakistan
A.4.1.2. Region/State/Province etc.:
>>
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Baluchistan
A.4.1.3. City/Town/Community etc:>>
Hub Chowki, Lasbella
A.4.1.4. Details of physical location, including information allowing the
unique identification of this small-scale project activity :
>>
The proposed project activity is located at the Attock Cement plant 16 km north-west of the city centre of
Hub Chowki in the Baluchistan Province of Pakistan. Its coordinates are: Latitude: 258'23.75" Longitude
6654'55.65".
Figure 1: Geographical location of the project activity.
A.4.2. Type and category(ies) and technology/measure of the small-scale project activity:
>>
In accordance with Appendix B of the simplified modalities and procedures for small-scale CDM project
activities, the Project activity is categorized under the following type and category:
Type III. Other project activities Category Q: Waste Energy Recovery (gas/heat/pressure) ProjectsSectoral Scope 04 Manufacturing industries. As the project also uses ACM0012 to calculate the capping
factor, Sectoral Scope 1 Energy industries (renewable -/ non-renewable sources) is applied in addition.
With the proposed project, waste heat boilers will be installed at the outlet of cooler and at the exit of pre-
heater of each line, introducing water into the boilers and producing superheated steam by using waste hot
gases from Cooler and pre-heater. The superheated steam produced from all the boilers merges together
and is introduced to a turbine for power generation. The power thus produce will be connected with the
existing grid station. Exhaust steam of turbine after work condense to water and pump back to the
boilers. After passing from boilers the temperature and volume of hot gases reduced significantly and
further reduced when pass through the dust-collecting filter and then exhausted in the atmosphere. The
following flow chart shows the complete process of WHRS.
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The additional water demand of 2,800 m3
per day will be provided by additional pumps. While the
existing cement factory operates a 90 kW water pump and two 45 kW pumps as backup using gridelectricity and diesel generators during grid load sheds, three 90 kW pumps will be operated during the
project activity. Of the three pumps, two will be in constant operation, while the third will be kept as a
back-up system.
FromLine-
1
Pre-Heater
IDFan
FromLine-
2
Pre-Heater
Cooling
Tower
SPBoile
r
#2
SPBoiler
#1
STEAM
HOTGASES
DUST
WATER
ELECTRICIT
Y
COOLERLINE-1
FLOWDIAGRAM
IDFan
MAKEUPWATER
Settling
Chamber
Settling
Chamber
AQC
Boiler#2
COOLERLINE-2
STEAM
TURBINE
CONDENSER
WATERTOBOILER
TOGRID
STATIONAQC
Boiler#1
GENERATOR
WATERCOOLING
TOWER
POWERGENERATIONTHRUWHRS
Figure 2: Flow chart of the proposed project.
The waste heat recovery equipment is purchased from China. Therefore, technology transfer from China
to Pakistan will take place through the proposed project.
A.4.3 Estimated amount of emission reductions over the chosen crediting period:
>>
Years Estimation of annual emission reductions
in tonnes of CO2e
Year 1 34,417
Year 2 34,417
Year 3 34,417
Year 4 34,417
Year 5 34,417
Year 6 34,417
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Year 7 34,417
Year 8 34,417
Year 9 34,417Year 10 34,417
Total estimated reductions
(tonnes of CO2e)
344,170
Total number of crediting years 10
Annual average of estimated reductions over
the crediting period (tonnes of CO2e)
34,417
A.4.4. Public funding of the small-scale project activity:
>>
No public funding is involved in the project financing.
A.4.5. Confirmation that the small-scale project activity is not a debundled component of a
large scale project activity:
>>
Appendix C of the Simplified Modalities and Procedures for Small-Scale CDM project activities gives
the definition of a debundled component of a large project activity1:
A proposed small-scale project activity shall be deemed to be a debundled component of a large
project activity if there is a registered small-scale CDM project activity or an application to
register another small-scale CDM project activity:
(a) With the same project participants;(b)In the same project category and technology/measure; and(c)Registered within the previous 2 years; and(d) Whose project boundary is within 1 km of the project boundary of the proposed small-
scale activity at the closest point.
There is no registered small-scale CDM project activity or an application to register another small-scale
CDM project activity that meets all of the above mentioned criteria. Therefore, the Project activity is not a
debundled component of a large scale project activity.
SECTION B. Application of a baseline and monitoring methodology
B.1. Title and reference of the approved baseline and monitoring methodology applied to the
small-scale project activity:
>>
Title of the baseline methodology: AMS III.Q Waste energy recovery (gas/heat/pressure) projects
(Version 04).
1Appendix C of the Simplified Modalities and Procedures for Small-Scale CDM project activities (contained in
annex II to decision 21/CP.8, see document FCCC/CP/2002/7/Add.3).
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Reference: AMS-III.Q., Version 04 (EB 61, Sectoral Scope: 04) It has been referred from the list of
approved methodologies for CDM project activities in the UNFCCC CDM website(http://cdm.unfccc.int/methodologies/SSCmethodologies/approved.html ).
The baseline for the proposed project activity is determined using the Tool to calculate the Emission
Factor for an electricity system (Version 2.2.1, EB 63).
To calculate the project emissions, the Tool to calculate baseline, project and/or leakage emissions from
electricity consumption (Version 01, EB 39) and theTool to calculate project or leakage CO2emissions
from fossil fuel combustion (Version 02, EB 41) are applied.
To estimate the capping factor, corresponding section of ACM0012 Consolidated baseline
methodology for GHG emission reductions from waste energy recovery projects (version 4.0.0, EB560)
is referred.
B.2 Justification of the choice of the project category:
>>
In the applied methodology AMS-III.Q., v. 04, several applicability conditions are listed. Table 1
demonstrates the applicability of all listed requirements.
No. Applicability criteria Project situation Methodology
Applicability
(y/n)
1. The category is for project activities that utilizewaste gas and/or waste heat at existing facilities asan energy source for:
a) Cogeneration; orb) Generation of electricity; orc) Direct use as process heat; ord) Generation of heat in elemental process
(e.g., steam, hot water, hot oil, hot air);
e) Generation of mechanical energy.
The project activity utilizes
waste heat from existingfacilities to generate
electricity, i.e. option b.
Y
2. The category is also applicable to projectactivities that use waste pressure to generate
electricity at existing facilities.
No waste pressure utilization
is included in the project
activity. Criteria not
applicable.
Y
3. The recovery of waste gas/heat/pressure should bea new initiative (no waste gas/heat/pressure was
recovered from the project activity
source prior to the implementation of the project
activity).
The projects plant is a new
facility and no similar
technology has been installed
at the cement plant prior to
the project activity.
Y
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No. Applicability criteria Project situation Methodology
Applicability
(y/n)4. Measures are limited to those that result in
emission reductions of less than or equal to
60 ktCO2 equivalent annually.
The emission reduction will
not exceed 60 ktCO2e per
year during the crediting
period. This will be shown in
chapter B.6.4 of this PDD.
Y
5. The energy produced with the recovered wastegas/heat should be measurable.
The energy produced with
the recovered waste heat is
measurable.
Y
6. Energy generated in the project activity may beused within the industrial facility or exported to
other industrial facilities (included in the project
boundary).
All electricity generated by
the project activity will be
utilized within the Attock
cement plant.
Y
7. Electricity generated in the project activity may beexported to the grid or used for captive purposes.
However, the methodology is not applicable to
projects where the waste gas/heat/pressure
recovery project is implemented in a single-cycle
power plant (e.g. gas turbine or diesel generator)
where heat (energy) generated on-site is not
utilizable for any other purposes on-site except to
generate power. Such project activities shall
consider AMS-III.AL. Conversion from single
cycle to combined cycle power generation..Projects recovering waste energy from such power
plants for the purpose of generation of heat only
can apply this methodology;
All electricity generated by
the project activity will be
used for captive purposes.
The project is not
implemented in a single-
cycle power plant. The
project activity recovers
waste heat from the clinker
production process and
utilizes it for power
generation.
Y
8. For a project activity which recovers wastegas/heat/pressure for power generation from
multiple sources (e.g. kiln and single-cycle power
plant), this methodology can be used in
combination with AMS-III.AL provided that2:
Not applicable. The project
will only recover waste heat
from the cement plant, no
combination with
methodology AMS-III.Al is
required.
Y
9. The emission reductions are claimed by thegenerator of energy using waste energy.
The emission reductions are
claimed by the project owner
and generator of energyAttock Cement Pakistan Ltd.
Y
2The sub-criteria are not listed here, as the criteria is not applicable to the project.
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No. Applicability criteria Project situation Methodology
Applicability
(y/n)10. In cases where the energy is exported to other
facilities (included in the project boundary), the
following are required:
(i) All historical information from the recipient
plants;
(ii) An official agreement exists between the owners
of the project energy generation plant (henceforth
referred to as generator, unless specified otherwise)
with the recipient plant(s) that the emission
reductions would not be claimed by the recipient
plant(s) for using a zero-emission energy source;
The project activity will not
export energy to other
facilities.
Y
11. For those facilities and recipients included in theproject boundary, that prior to implementation of
the project activity (current situation) generated
energy on-site (sources of energy in the baseline),
the credits can be claimed for minimum of the
following time periods:
i. The remaining lifetime of equipmentcurrently being used; and
ii. Crediting period.
No energy was generated on-
site prior to the project
activity. The project activity
will reduce the electricity
uptake from the national grid
(source of energy in the
baseline). Not applicable.
Y
12. The waste gas/heat/pressure utilized in the projectactivity would have been flared or released intothe atmosphere in the absence of the project
activity. This shall be proven by one of the
following options:
i. By direct measurements of energy contentand amount of the waste gas/heat/pressure
for at least three years prior to the start of
the project activity.
ii. Energy balance of relevant sections of theplant to prove that the waste
gas/heat/pressure was not a source of energy
before the implementation of the projectactivity. For the energy balance the
representative process parameters are
required. The energy balance shall
demonstrate that the waste gas/heat/pressure
was not used and also provide conservative
estimations of the energy content and
amount of waste gas/heat/pressure released.
iii. Energy bills (electricity, fossil fuel) todemonstrate that all the energy required for
the process (e.g., based on specific energy
The baseline situation will be
demonstrated using method1. The necessary data will be
provided to the DOE during
the validation.
Y
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No. Applicability criteria Project situation Methodology
Applicability
(y/n)consumption specified by the manufacturer)
has been procured commercially. Project
participants are required to demonstrate
through the financial documents (e.g.,
balance sheets, profit and loss statement)
that no energy was generated by waste
gas/heat/pressure and sold to other facilities
and/or the grid. The bills and financial
statements should be audited by competent
authorities.
iv.
Process plant manufacturers originalspecification/information, schemes and
diagrams from the construction of the
facility could be used as an estimate of
quantity and energy content of waste
gas/heat/pressure produced for rated plant
capacity per unit of product produced.
13. For the purpose of this category waste energy isdefined as: a by-product gas/heat/pressure from
machines and industrial processes having
potential to provide usable energy, for which it
can be demonstrated that it was wasted. For
example gas flared or released into the
atmosphere, the heat or pressure not recovered
(therefore wasted). Gases that have intrinsic value
in a spot market as energy carrier or chemical
(e.g., natural gas, hydrogen, liquefied petroleum
gas, or their substitutes) are not eligible under this
category.
The waste heat recovered
from the clinker making
process complies with the
definition provided above
and it can be demonstrated
that it was wasted prior to the
start of the project activity
(see explanation in the
sections below). No gases
with intrinsic value are
included in the project
activity.
Y
Table 1: Applicability criteria of methodology AMS-III.Q.
As meeting all criteria listed above, the chosen methodology AMS-III.Q. can be deemed as applicable to
the actual project activity.
B.3. Description of the project boundary:
>>
In the small-scale methodology AMS-III.Q, the project boundary is described in paragraph 83:
7. The physical, geographical site of the facility where the waste gas/heat/ pressure is produced
and transformed into useful energy delineates the project boundary.
The geographical extent of the project boundary shall include the following:
3Cited fromAMS-III.Q Waste energy recovery (gas/heat/pressure) projects , v.04, p.3
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The industrial facility where waste energy is generated, including the part of the industrial facility
where the waste gas was utilized for generation of captive electricity prior to implementation of theproject activity;
The facility where steam/process heat in the element process/electricity/mechanical energy is
generated (generator steam/ process heat/electricity/mechanical energy). Equipment providing
auxiliary heat to the waste energy recovery process shall be included within the project boundary;
and
The facility(ies) where steam/process heat in the element process/electricity/ mechanical energy is
used (the recipient plant(s)) and/or grid where electricity is exported, if applicable.
Based on this definition, the project boundary is defined as illustrated in Figure 3 and defined as follows:
The project boundary comprises
the Attock Cement Pakistan Ltd. cement plant in Hub Chowki, Pakistan including the two clinkerproduction lines where the waste heat is generated.
and the equipment that will be installed by the project activity, mainly four waste heat boilers, asteam turbine and a generator.
As the generated electricity will be consumed on-site, the national grid that provides electricity to the
project in the baseline scenario will not be included.
Figure 3: Project boundary of the project activity.
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Table 2: Project development timeline
Assessment and demonstration of additionalityTo assess and demonstrate the additionality, attachment A to Appendix B of the simplified Modalities and
Procedures for Small-Scale CDM project activities is used. According to this guideline, a small-scale
project activity is considered additional, if at least one of the following barriers prevents the project from
being installed:
a) Investment barrierb) Technological barrierc) Barrier due to prevailing practiced) Other barriers
For this project, the demonstration of existence of an investment barrier is chosen. By demonstrating, that
a financially more feasible option (baseline scenario as described in B.4) is leading to more emissions.
Since an investment is not required for the project owner, and the project does generate economic benefits
other than the CDM related income, the benchmark analysis is chosen as appropriate to demonstrate the
additionality of the project.
Therefore, the Guidelines on the assessment of investment analysis are to be used in the following.
Table 3 demonstrates the fulfilment of all guidelines provided in the Guidelines on the assessment of
investment analysis, v. 055.
No. Guidance Project activity
3. The period of assessment should not be limited to the proposed creditingperiod of the CDM project activity. Both project IRR and equity IRR
calculations shall as a preference reflect the period of expected operation
of the underlying project activity (technical lifetime), or - if a shorter
period is chosen - include the fair value of the project activity assets at
the end of the assessment period. In general a minimum period of 10
years and a maximum of 20 years will be appropriate. The IRR
calculation may include the cost of major maintenance and/or
rehabilitation if these are expected to be incurred during the period of
assessment. Project participants are requested to justify and DOEs are
requested to validate the appropriateness of the period of assessment inthe context of the underlying project activity, without reference to the
proposed CDM crediting period.
The period of
assessment is limited
to the technical project
lifetime of 20 years.
This is in line with the
company accounting
policy.
5All guidances listed in Table 3 are cited from Guidelines on the assessment of investment analysis, v. 05.
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No. Guidance Project activity
4. The fair value of any project activity assets at the end of the assessmentperiod should be included as a cash inflow in the final year. The fairvalue should be calculated in accordance with local accounting
regulations where available, or international best practice. It is expected
that such fair value calculations will include both the book value of the
asset and the reasonable expectation of the potential profit or loss on the
realization of the assets.
According to the
companys policy, aproject lifetime of 20
years and a residual
value of 1% has been
considered..
5. Depreciation, and other non-cash items related to the project activity,which have been deducted in estimating gross profits on which tax is
calculated, should be added back to net profits for the purpose of
calculating the financial indicator (e.g. IRR, NPV). Taxation should only
be included as an expense in the IRR/NPV calculation in cases where the
benchmark or other financial indicator is intended for post-tax
comparisons.
Tax benefit on
depreciation is
included in the IRR
calculation.
6. Input values used in all investment analysis should be valid andapplicable at the time of the investment decision taken by the project
participant. The DOE is therefore expected to validate the timing of the
investment decision and the consistency and appropriateness of the input
values with this timing. The DOE should also validate that the listed
input values have been consistently applied in all calculations.
All input values reflect
to values applicable at
the time of investment
decision. As can be
seen from the timeline
presented in Table 2,
the project starting
date comes shortly
after the financial
analysis has been
conducted. It can
therefore be assumed
that the input data did
not change
significantly between
the calculation and the
final investment
decision.
7. In the case of project activities for which implementation ceases after thecommencement and where implementation is recommenced due to
consideration of the CDM the investment analysis should reflect the
economic decision making context at point of the decision to
recommence the project. Therefore capital costs incurred prior to therevised project activity start date can be reflected as the recoverable
value of the assets, which are limited to the potential reuse/resale of
tangible assets.
No capital costs that
incurred prior to the
revised project activity
start are reflected as
recoverable value ofassets.
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No. Guidance Project activity
8. Project participants should supply spreadsheet versions of all investmentanalysis. All formulas used in this analysis be readable and all relevantcells be viewable and unprotected. The spreadsheet will be made
available to the Executive Board, UNFCCC secretariat and others
contracted to assess the request for registration on behalf of the Board
including assigned members of the Registration and Issuance Team. In
cases where the project participant does not wish to make such a
spreadsheet available to the public an exact read-only or PDF copy shall
be provided for general publication. In case the PP wishes to black-out
certain elements of the publicly available version, a clear justification for
this shall be provided to the UNFCCC secretariat by the DOE when
requesting registration.
The spreadsheets are
provided to DOE andEB.
9. The cost of financing expenditures (i.e. loan repayments and interest)should not be included in the calculation of project IRR.
The project will be
financed throughequity.
10. In the calculation of equity IRR only the portion of investment costswhich is financed by equity should be considered as the net cash
outflow, the portion of the investment costs which is financed by debt
should not be considered a cash outflow.
The project is
completely financed
by equity.
11. Due to the impact of loan interest on income tax calculations it isrecommended that when a project IRR is calculated to demonstrate
additionality a pre-tax benchmark be applied. In cases where a post-tax
benchmark is applied the DOE shall ensure that actual interest payable is
taken into account in the calculation of income tax. In such situations
interest should be calculated according to the prevailing commercialinterest rates in the region, preferably by assessing the cost of other debt
recently acquired by the project developer and by applying a debt-equity
ratio used by the project developer for investments taken in the previous
three years.
Not applicable.
12. In cases where a benchmark approach is used the applied benchmarkshall be appropriate to the type of IRR calculated. Local commercial
lending rates or weighted average costs of capital (WACC) are
appropriate benchmarks for a project IRR. Required/expected returns on
equity are appropriate benchmarks for an equity IRR. Benchmarks
supplied by relevant national authorities are also appropriate if the DOE
can validate that they are applicable to the project activity and the type
of IRR calculation presented.
The benchmark used is
taken from Appendix
A of the guidelines on
the assessment of
investment analysis.
The benchmarks in
this Appendix are
appropriatebenchmarks for the
equity IRR.
13. In the cases of projects which could be developed by an entity other thanthe project participant the benchmark should be based on parameters that
are standard in the market. The DOE.s validation of the benchmark shall
also include its opinion on whether a company-specific benchmark or a
benchmark based on parameters that are standard in the market is
suitable in the context of the underlying project activity.
Source of benchmark
is publicly available
(EB62, Annex 5) and
can be validated by the
DOE.
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No. Guidance Project activity
14. Internal company benchmarks/expected returns (including those used asthe expected return on equity in the calculation of a weighted averagecost of capital WACC), should only be applied in cases where there is
only one possible project developer and should be demonstrated to have
been used for similar projects with similar risks, developed by the same
company or, if the company is brand new, would have been used for
similar projects in the same sector in the country/region. This shall
require as a minimum clear evidence of the resolution by the companies
Board and/or shareholders and will require the validating DOE to
undertake a thorough assessment of the financial statements of the
project developer including the proposed WACC to assess the past
financial behavior of the entity during at least the last 3 years in relation
to similar projects.
No internal benchmark
is used.
15. If the benchmark is based on parameters that are standard in the market,the cost of equity should be determined either by: (a) selecting the values
provided in Appendix A; or by (b) calculating the cost of equity using
best financial practices, based on data sources which can be clearly
validated by the DOE, while properly justifying all underlying factors.
The values in the table in Appendix A may also be used, as a simple
default option, if a company internal benchmark is used.
The values provided inAppendix A are
chosen as benchmarks.
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No. Guidance Project activity
16. If a company.s internal benchmark is used for the expected return onequity, the cost of debt should be based on the weighted average cost ofdebt financing of the legal entity owning the CDM project activity. For
loans, use the weighted average cost of outstanding long-term debt.
For bonds, use the weighted average yield of the bonds during the last
three months prior to the submission of the CDM-PDD for validation or
prior to the investment decision, whichever is earlier. The use of bonds
to determine the cost of debt is only appropriate for corporate bonds
issued in the host country of the CDM project. In cases where the debt
finance structure of the project is not yet available (e.g. a letter of intent
for debt funding is not available), the cost of debt can be assumed as the
commercial lending rate in the country or the yield of a 10 year bond
issued by the government of the host country or, if this is not available,
the bond with the maturity which is closest to 10 years. The followingshould be documented in the CDM-PDD: (a) for bonds: the key
parameters of the bond including the time of maturity, yield, registration
issuance in the financial system and set-up in the market; (b) for loans
from a financial institution: the contract of lending between the financial
institution and the legal entity owning the assets of the project activity,
or, in absence of the contract, a letter from the bank stating its intention
to award the loan and the key terms for the loan; (c) for debt financing
from a parent company: the transfer of capital to the legal entity,
documented with the contract of lending between the parent company
and the legal entity owning the assets of the project activity and/or the
parameters of the corporate bonds as mentioned above. This latter option
is only valid for corporate bonds issued in the host country of the CDM
project activity.
If the benchmark is based on parameters that are standard in the market,
the cost of debt should be calculated as the cost of financing in the
capital markets (e.g. commercial lending rates and guarantees required
for the country and the type of project activity concerned), based on
documented evidence from financial institutions with regard to the cost
of debt financing of comparable projects. In cases where this data is not
available, use the commercial lending rate in the host country to
calculate the cost of debt.
No companys internal
benchmark is used, butthe default values
published in the
guidelines on the
assessment of
investment analysis.
17. If a company.s internal benchmark is used for the expected return onequity, then the percentage of debt financing and equity financing shouldreflect the long-term debt/equity finance structure of the legal entity
owning the assets of the project activity. The percentage should be
determined based on the latest balance sheet provided under local
fiscal/accounting standards and rules if: (a) the legal entity owning the
assets of the project activity has balance sheets audited by a third party
within two years prior to the submission of the CDM-PDD for
validation; and (b) the accounting books of the legal entity reflect at least
the total value of all the assets needed for the project activity. If the
debt/equity finance structure is not yet available, 50% debt and 50%
equity financing may be assumed as a default.
No companys internal
benchmark is used, butthe default values
published in the
guidelines on the
assessment of
investment analysis.
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No. Guidance Project activity
18. If the benchmark is based on parameters that are standard in the market,then the typical debt/equity finance structure observed in the sector ofthe country should be used. If such information is not readily available,
50% debt and 50% equity financing may be assumed as a default.
The benchmark used is
the default value givenin the guidelines on
the assessment of
investment analysis.
19. If the proposed baseline scenario leaves the project participant no otherchoice than to make an investment to supply the same (or substitute)
products or services, a benchmark analysis is not appropriate and an
investment comparison analysis shall be used. If the alternative to the
project activity is the supply of electricity from a grid this is not to be
considered an investment and a benchmark approach is considered
appropriate.
Baseline scenario is
BAU scenario.
20. Only variables, including the initial investment cost, that constitute morethan 20% of either total project costs or total project revenues should besubjected to reasonable variation (all parameters varied need not
necessarily be subjected to both negative and positive variations of the
same magnitude), and the results of this variation should be presented in
the PDD and be reproducible in the associated spreadsheets. Where a
DOE considers that a variable which constitute less than 20% have a
material impact on the analysis they shall raise a corrective action
request to include this variable in the sensitivity analysis
The variables total
investment, electricitysavings and O&M
costs have been varied
in a range of +10% to -
10%, and sensitivity
has been conducted.
The same is reflected
in the investment
analysis spreadsheet.
21. The DOE should assess in detail whether the range of variations isreasonable in the project context. Past trends may be a guide to
determine the reasonable range. As a general point of departurevariations in the sensitivity analysis should at least cover a range of
+10% and -10%, unless this is not deemed appropriate in the context of
the specific project circumstances. In cases where a scenario will result
in the project activity passing the benchmark or becoming the most
financially attractive alternative the DOE shall provide an assessment of
the probability of the occurrence of this scenario in comparison to the
likelihood of the assumptions in the presented investment analysis,
taking into consideration correlations between the variables as well as
the specific socio-economic and policy context of the project activity.
The variables total
investment, electricity
savings and O&Mcosts have been varied
in a range of +10% to -
10%, and sensitivity
has been conducted.
The same is reflected
in the investment
analysis spreadsheet.
Table 3: Guidelines on the assessment of investment analysis.
Benchmark definition:Based on the guidelines on the assessment of investment analysis, v.05, the default benchmark for the
sectoral scope 4 (Manufacturing industries, as per the applied methodology AMS III.Q) is used. Since
version 4 of the guidelines on the assessment of investment analysis, these benchmarks are provided as a
simple default option. The applied post-tax equity benchmark is therefore 15.5%.
Following these guidelines, a financial analysis is conducted with the following main input values:
Item Value Unit
Total investment 1,583,699,389 PKR
Equity 100 %
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Item Value Unit
Net capacity 8,100 KW
Annual operation hours 7,200 hAnnual electricity savings 58,320,000 KWh
Electricity price 6.5 PKR/KWh
Water requirement 184,800,000 Imperial gallons/yr
Water price 0.052 PKR/gallon
Repair & Maintenance 5 % of total investment
Replacement costs 3 % of total investment
Annual inflation for utilities 5 %
Annual inflation for repair &
maintenance
7 %
Annual inflation for salaries 10 %
Statutory charges 7 % of net profit before taxInsurance 0.28 % of total investment
Project lifetime 20 years
Income tax 35 %
Residue or residual rate/Fair value 1 %
CERs 35,000 CERs (Based on an initial
estimation)
CER price 11.7 EUR
Table 4: Main input parameters of the financial analysis.
With these input values, two post-tax equity IRRs are calculated; one excluding CER revenues, one
including CER revenues:
IRR excluding CERs 12.13%
IRR including CERs 16.22%
Since the IRR excluding CER revenues is below the benchmark of 15.5% and the IRR including the CER
revenue surpasses this benchmark, it can be concluded that the proposed project is financially additional
with CDM.
Sensitivity analysis
To show the robustness of the results, a sensitivity analysis is carried out for the variation of the decisive
variables of the project activity. These are the total investment, electricity savings and yearly O&M costs.
The results of the sensitivity analysis are shown in the following:
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Figure 4Sensitivity analysis for the parameters total investment, electricity savings and annualO&M costs.
-10% -5% 0% 5% 10%
Total investment 15.90% 13.92% 12.13% 10.49% 8.46%
Electricity savings 8.61% 10.44% 12.13% 13.73% 15.27%
Annual O&M costs 13.35% 12.75% 12.13% 11.49% 10.84%Table 5: Detailed results of the sensitivity analysis.
The sensitivity analysis shows that the results of the Investment analysis are robust. For a change of +/-
10% in electricity savings and annual O&M cots, the IRR for the project activity is still below the
benchmark, thus strengthening the conclusions about the additionality of the project activity.
Only in once scenario, total investment -10%, the IRR would exceed the benchmark. A further analysis
shows that if the total investment would be lower than -9.05% of the initially assumed value, the IRR
would reach the benchmark of 15.5% and the project would become financially feasible. However, such
scenario can be excluded, as the total paid amount (as of 03/03/2012) already reached 1,490, 047,673
PKR. This is already 94.1% of the originally assumed 1,583,699,389PKR. A scenario, in which the
project IRR exceeds the benchmark of 15.5% due to a lower total investment is therefore impossible andcan be excluded.
By demonstrating, that the investment is not financially viable for the project owner and a financially
attractive scenario is impossible to occur, even taken into consideration a variation of input parameters
(sensitivity analysis), it is clearly shown that an investment barrier prevents the project from being
implemented and it is therefore considered additional.
B.6. Emission reductions:
B.6.1. Explanation of methodological choices:
>>
0.00%
2.00%
4.00%
6.00%
8.00%
10.00%
12.00%
14.00%
16.00%
18.00%
-10% -5% 0% 5% 10%
TotalInvestment
ElectricityProduction
O&MCosts
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Baseline emissions
According to the methodology, in the situation where the electricity is obtained from a specific existingpower plant or from the grid, mechanical energy is obtained by electric motors and heat from a fossil fuel
based element process (e.g., steam boiler, hot water generator, hot air generator, hot oil generator),
baseline emissions can be calculated as follows:
!"!#,! = !"# !"# (!,!,! !"#$,!,!,!)
!!
1
With the input values
!"!#,! Baseline emissions due to displacement of electricity during the yeary in tons of CO2.
!"# Capping factor to exclude increased waste energy utilization in the project yeary due
to increased level of activity of the plant, relative to the level of activity in the baseyears before project start.
!"#
Fraction of total electricity generated by the project activity using waste energy. With
reference to the methodology, this factor is considered 1 as the electricity generated is
driven purely by utilization of waste heat.
!,!,! The quantity of electricity supplied to the recipientjby generator, that in the absence
of the project activity would have been sourced from ith
source (i can be either grid or
identified source) during the yeary in MWh.
!"#$,!,!,! The CO2 emission factor for the electricity source i (i=gr (grid) or i=is (identified
source)), displaced due to the project activity, during the yeary in tons CO2/MWh
Two factors have to be defined in more detail:
To calculate !"#, the methodology refers to the large-scale methodology ACM0012 (latest version:
v. 4.0.0). There, the following alternatives are listed6:
Method-1: Where the historical data on energy released by the waste energy carrying medium is
available, the baseline emissions are capped at the maximum quantity of waste energy released
into the atmosphere under normal operation conditions in the three years previous to the project
activity.
Method-2:If three-year historical data is not available, the manufacturers data for the facility
shall be used to estimate the amount of waste energy the facility generates per unit of product.The product is produced by the process that generates waste energy (departmental process or
process of entire project facility, whichever is more justifiable and accurate). If any modification is
carried out by the project proponent or if the manufacturers data is not available for an
assessment, this should be carried out by independent qualified/certified external process experts
such as a chartered engineer on a conservative quantity of waste energy generated by the project
facility per unit of product manufactured by the process generating waste energy. The value
arrived at based on above sources of data, shall be used to estimate the baseline cap (fcap).
6Cited fromACM0012 - Consolidated baseline methodology for GHG emission reductions from waste energy
recovery projects, v. 4.0.0, pp. 29-32
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Method-3: In some cases, it may not be possible to measure the waste energy (heat, sensible heat,
heat of reaction, heat of combustion, etc.) enthalpy or pressure content of WECM (Method-1
requirement), nor the specific amount of WECM per unit of product (Method-2 requirement). Insuch cases, the capping shall be based on indirect information about specific parameters allowing
to estimate the amount of waste energy available. These parameters should be related to the
characteristics of a product or a by-product of the facility from which waste energy can be
recovered (e.g. volume and heat content of hot clinker produced by a kiln in a cement plant, if this
heat can be recovered using air as the WECM). These cases may be of the following two types.
Since three years of historical data are available, for this project, Method 1 is chosen to determine the
capping factor for waste heat recovering projects:
!"# =
!"#,!" !"# !"#,!" !"# + !"#,!" +!"#,!"
!"#
9
.
81 10!
!"#,!"
!"#,! !"# !"#,! !"# + !"#,! +!"#,! !"# 9.81 10
!
!"#,!
2
With the input values:
!"#,!" AveragequantityofWECMreleased(orflaredorwasted)inatmosphereinthreeyearspriortothestartoftheprojectactivity[kg].
!"#,! QuantityofWECMusedforenergygenerationduringyeary[kg].
!"# SpecificHeatofwasteenergycarryingmedium(WECM)[TJ/kg/C].
!"#
,
!" AveragetemperatureofWasteEnergyCarryingMedium(WECM)inthreeyearspriortothestartoftheprojectactivity [C].
!"#,! AveragetemperatureofWasteEnergyCarryingMedium(WECM)inyeary[C].
!"# ReferencetemperaturetobeusedtodetermineavailableenergyinWECMy[25C].
!"#,!" Averagenetcalorificvalueofwastegas(ifWECMiswastegas),threeyearspriortoimplementationofprojectactivitywhichhasunburntcomponentssuchascarbon
particles,COorCH4thatwillprovideenergyinwasteenergyrecoveryequipmenton
combustionofgas[TJ/kg].
!"!,! Averagenetcalorificvalueofwastegasinyeary(ifWECMiswastegas),whichhasunburntcomponentssuchascarbonparticles,COorCH4thatwillprovideenergyin
wasteenergyrecoveryequipmentoncombustionofgas[TJ/kg].
!"#
,
!" AveragepressureofWECMinthreeyearspriortothestartoftheprojectactivity[kg/cm2].
!"#,! AveragepressureofWECMinyeary[kg/cm2].
!"# ReferencepressureofWECM[1atm].
!"#,!" AveragedensityofWECMatactualtemperatureandpressureinthreeyearspriorto
thestartoftheprojectactivity[kg/m3]
!"#,! AveragedensityofWECMatactualtemperatureandpressureinyeary[kg/m3].
9.81 10! Factortoconvertkg-mintoTJ(Tobeusedwhenpressureisexpressedinkg/m2.
,,,
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The calculation of the grid emission factor is carried out and described in Annex 3.
Project emissions
In the methodology, the project emissions are defined as7:
14.Project Emissions include emissions due to combustion of auxiliary fuel to supplement waste gasand emissions due to consumption of electricity by the project activity.
15.If the waste gas contains carbon monoxide or hydrocarbons, other than methane, and the wastegas is vented to the atmosphere in the baseline situation, project emissions have to include CO2
emissions due to the combustion of the waste gas.
No waste gas is combusted during the project activity. Therefore, the project emission will only comprise
the baseline emissions from auxiliary fuel and electricity consumption of the project equipment. The onlyproject equipment that is not driven by the self consumption by the power plant and thereby reduces the
electricity sent to the grid, but consumes electricity from a separate line and diesel in cases of grid load
sheds are the pumps that provide water for the project. The emissions caused by the energy consumption
the pumps can be expressed as:
! = !",!,! + !",! 3
Where:
! Project emissions during the yeary in tons of CO2.
!"
,
!,! Are the CO2 emissions from fossil fuel combustion in process j during theyeary (tCO2/yr);
!",! Project emissions from electricity consumption in yeary (tCO2/yr)
The emissions from electricity consumption can be calculated following the Tool to calculate baseline,
project and/or leakage emissions from electricity consumption, version 01. As the electricity is
consumed from the grid, scenario A, described in this tool is applicable and the project emissions from
electricity consumption will be calculated accordingly:
!",! = !",!,!
!
!",!,! (1 + !,!)4
Where:
!",! Project emissions during the yeary in tons of CO2.
!",!,! Quantity of electricity consumed by the project electricity consumption
sourcejin yeary (MWh/yr)
!",!,! Emission factor for electricity generation for source j in year y
(tCO2/MWh). In this one case, this factor is the grid emission factor of the
KESC grid !"#$,!,!,! and will be calculated in Annex 3.
7Cited fromAMS-III.Q Waste energy recovery (gas/heat/pressure) projects, v.04, p.11
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!,! Average technical transmission and distribution losses for providing
electricity to sourcejin yeary. In line with the tool, a conservative
standard factor of 20% is assumed here.j Sources of electricity consumption in the project. Here only the pumps are
considered as source of electricity consumption, therefore j is 1.
To calculate the project emissions due to fossil fuel consumption during grid load sheds, the carbon
emission from the diesel generators are calculated following the Tool to calculate project or leakage CO2
emissions from fossil fuel combustion, version 02:
!",!,! = !,!,! !,! 5
Where:
!",!,! Are the CO2 emissions from fossil fuel combustion in process j during the
yeary (tCO2/yr);
!,!,! Is the quantity of fuel type i combusted in processj during the yeary (mass
or volume unit/yr);
!,! Is the CO2 emission coefficient of fuel type i in yeary (tCO2/mass or
volume unit)
i Are the fuel types combusted in processj during the yeary. As only diesel
is used in the generators, i is 1.
j Fossil fuel combusting process. As only the diesel generators consume
fossil fuel, j is 1.
To calculate the emission coefficient, the emission factor of diesel and its NCV are used:
!,! = !,!,! !"!,!,! 6
Where:
!,! Is the CO2 emission coefficient of fuel type i in yeary (tCO2/mass or
volume unit)
!,!,! Is the weighted average net calorific value of the fuel type i in yeary
(GJ/mass or volume unit)
!"!,!,! Is the weighted average CO2 emission factor of fuel type i in yeary
(tCO2/GJ)
Leakage
Since no transfer of equipment is considered in the project activity, the leakage is zero.
! = 0 7
Emission reduction
With the data calculated above, the emission reduction can be calculated:
! = ! ! LE! = ! ! 8
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B.6.2. Data and parameters that are available at validation:
Data / Parameter: !"#$,!,!,!
Data unit: tCO2/MHh
Description: Emission factor of the grid
Source of data used: Pakistan Energy Yearbook, Ministry of Minerals & Natural Resources
Value applied: 0.595
Justification of the
choice of data or
description of
measurement methods
and procedures actually
applied :
Calculated as per Tool to calculate the emissionfactor for an electricity
system v. 2.2.1. For the detailed way of calculation, see Annex 3.
Any comment:
Data / Parameter: !,!
Data unit: -
Description: Average technical transmission and distribution losses for providing electricity
to sourcejin yeary
Source of data used: Tool to calculate baseline, project and/or leakage emissions from electricity
consumption
Value applied: 20%
Justification of the
choice of data or
description of
measurement methods
and procedures actually
applied :
The default value of 20% will not be measured, but chosen in line with the
methodology.
Any comment:
Data / Parameter: !"#,!"
Data unit: kg of energy carrying medium
Description: Average quantity of WECM released (or flared or wasted) in atmosphere in
three years prior to the start of the project activity.
Source of data used: Calculated from emission recordsValue applied: Year 1 prior to the project activity: 7,088,493,600
Year 2 prior to the project activity: 7,132,089,600
Year 3 prior to the project activity: 6,768,691,200
Justification of the
choice of data or
description of
measurement methods
and procedures actually
applied :
Calculated from data based on gas temperature, pressure and composition.
Any comment:
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Data / Parameter: !"#,!"
Data unit: TJ/kg/deg CDescription: Specific Heat of waste energy carrying medium vented from the preheaters and
coolers of the two production lines.
Source of data used: Calculated from emission records
Value applied: Line 1:
Preheater: 1.05E-09
Cooler: 1.04E-09
Line 2:
Preheater: 1.05E-09
Cooler: 1.04E-09
Justification of the
choice of data or
description of
measurement methods
and procedures actually
applied :
Calculated from data based on gas composition.
Any comment:
Data / Parameter: !"#,!
Data unit: TJ/kg/deg C
Description: Specific Heat of waste energy carrying medium vented from the preheaters and
coolers of the two production lines.
Source of data used: Calculated from emission records
Value applied: Line 1:Preheater: 1.05E-09
Cooler: 1.04E-09
Line 2:
Preheater: 1.05E-09
Cooler: 1.04E-09
Justification of the
choice of data or
description of
measurement methods
and procedures actually
applied :
Calculated from data based on gas composition.
Any comment:
Data / Parameter: !"#,!"
Data unit: deg C
Description: Average temperature of Waste Energy Carrying Medium (WECM) vented from
the preheaters and coolers of the two production lines in three years prior to the
start of the project activity.
Source of data used: Calculated from emission records
Value applied:
One year prior to
project activity
Two years prior
to project activity
Three years prior
to project activity
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Line 1
Preheater 393 397 391
Line 1Cooler 290 284 274
Line 2
Preheater 339 343 332
Line 2
Cooler 409 372 341
Justification of the
choice of data or
description of
measurement methods
and procedures actually
applied :
Calculated from temperature data.
Any comment:
Data / Parameter: !"#
Data unit: deg C
Description: Reference temperature to be used to determine available energy in WECM.
Source of data used: Chosen according to methodology.
Value applied: 25
Justification of the
choice of data or
description ofmeasurement methods
and procedures actually
applied :
Chosen according to methodology.
Any comment:
Data / Parameter: !"#,!
Data unit: TJ/kg
Description: Averagenetcalorificvalueofwastegasinyeary(ifWECMiswastegas),
whichhasunburntcomponentssuchascarbonparticles,COorCH4that
willprovideenergyinwasteenergyrecoveryequipmentoncombustionof
gas.Source of data used:
Value applied: 0
Justification of the
choice of data or
description of
measurement methods
and procedures actually
applied :
AstheWECMisnotwastegas,theappliedvalueis0.
Any comment:
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Data / Parameter: !"#,!"
Data unit: TJ/kg
Description: Averagenetcalorificvalueofwastegas(ifWECMiswastegas),threeyearspriortoimplementationofprojectactivitywhichhasunburntcomponents
suchascarbonparticles,COorCH4thatwillprovideenergyinwaste
energyrecoveryequipmentoncombustionofgas.
Source of data used:
Value applied: 0
Justification of the
choice of data or
description of
measurement methods
and procedures actually
applied :
AstheWECMisnotwastegas,theappliedvalueis0.
Any comment:
Data / Parameter: !"#,!"
Data unit: kg/cm2
Description: Average pressure of WECM vented from the preheaters and coolers of the two
production lines in three years prior to the start of the project activity.
Source of data used:
Value applied:
One year prior to
project activity
Two years prior
to project activity
Three years prior
to project activity
Line 1
Preheater 0.972 0.972 0.975
Line 1
Cooler 1.03 1.03 1.03
Line 2
Preheater 0.973 0.973 0.973
Line 2
Cooler 1.03 1.03 1.03
Justification of the
choice of data or
description ofmeasurement methods
and procedures actually
applied :
Measurementrecords.
Any comment:
Data / Parameter: !"#,!"
Data unit: kg/m3
Description: AveragedensityofWECMventedfromthe preheaters and coolers of the two
production linesatactualtemperatureandpressureinthreeyearspriorto
thestartoftheprojectactivity.
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Source of data used:
Value applied:
One year prior toproject activity
Two years priorto project activity
Three years priorto project activity
Line 1
Preheater 0.6 0.59 0.6
Line 1
Cooler 0.66 0.63 0.64
Line 2
Preheater 0.65 0.65 0.66
Line 2
Cooler 0.51 0.54 0.57
Justification of the
choice of data or
description of
measurement methods
and procedures actually
applied :
Calculatedbasedonmeasurementrecords.
Any comment:
B.6.3 Ex-ante calculation of emission reductions:
>>
According to B.6.1, the emission reductions are defined as:
ERy = BEy PEy LEy
= BEy PEy
= fcap fwcm (EGi,j,y EFElec,i,j,y )i
j
ECPJ,y EFElec,i,j,y (1+TDLy )+FCy NCVy EFCO2 ,y( )
with the following input values used:
9
Abbreviation Description Value Unit
!"# Capping factor to exclude increased waste energy
utilization in the project year y due to increased level of
activity of the plant
1 1
!"#
Fraction of total electricity generated by the project activity
using waste energy. With reference to the methodology, this
factor is considered 1 as the electricity generated is driven
purely by utilization of waste heat.
1 1
!,!,! The quantity of electricity supplied to the recipient j by
generator, that in the absence of the project activity would
58,320
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have been sourced from ith
source (i can be either grid or
identified source) during the yeary in MWh.
!"#$,!,!,! The CO2 emission factor for the electricity source i (i=gr(grid) or i=is (identified source)), displaced due to the
project activity, during the yeary in tons CO2/MWh
0.595 !/
!",! Quantity of electricity consumed by the project electricity
consumption sourcejin yeary (MWh/yr)
387.60 MWh
! Average technical transmission and distribution losses for
providing electricity to source jin yeary. In line with the
tool, a conservative standard factor of 20% is assumed here.
20% -
! Is the quantity of fuel type i combusted in process j during
the yeary
19,175 l
! NCVofDieselconsumedbytheproject 43.3 TJ/Gg
!"!
,
! DefaultCO2emissionfactorfordieselcombustion 74,800 Kg/TJ
Therefore:
! = 34,417!e 10B.6.4 Summary of the ex-ante estimation of emission reductions:
>>
Total ex ante estimation of emission reductions:
Year Estimation of
project activityemissions
(tCO2e)
Estimation of
baselineemissions (tCO2e)
Estimation of
leakage (tCO2e)
Estimation of
overall emissionreductions
(tCO2e)
Year 1 283 34,700 0 34,417
Year 2 283 34,700 0 34,417
Year 3 283 34,700 0 34,417
Year 4 283 34,700 0 34,417
Year 5 283 34,700 0 34,417
Year 6 283 34,700 0 34,417
Year 7 283 34,700 0 34,417
Year 8 283 34,700 0 34,417
Year 9 283 34,700 0 34,417Year 10 283 34,700 0 34,417
Total
(tonnes of CO2e)2,830 347,000 0 344,170
B.7 Application of a monitoring methodology and description of the monitoring plan:
B.7.1 Data and parameters monitored:
Parameter: EGi,j,y
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Unit: MWh
Description: Quantity of electricity supplied by the project activity during the year y.
Source of data: Continuous on-site measurementsValue of data: Will be monitored ex-post
Brief description of
measurement methods
and procedures to be
applied:
Electricity meters
QA/QC procedures to
be applied (if any):The electricity meters will undergo maintenance/calibration according to
national and industrial standards.
Any comment:
Parameter: ECPJ,j,yUnit: MWh
Description: Quantityofgridelectricityconsumedbythewaterpumps
Source of data: Continuous on-site measurements
Value of data: 387.60
Brief description of
measurement methods
and procedures to be
applied:
During normal operation of the plant, the pumps that will provide water will be
operated by grid electricity. Since the pumps will not only provide the
electricity to the WHRS plant, but also to the cement factory, the consumption
of electricity caused by the WHRS will be determined by the electricity
consumption of the pumps scaled with the share of water that will be consumed
by the WHRS plant.
QA/QC procedures to
be applied (if any):The electricity meters will undergo maintenance/ calibration according to
industrial standards.
Any comment:
Parameter: !,!,!
Unit: litres
Description: Is the quantity of fuel type i combusted in processj during the yeary
Source of data: Diesel transportation bills between the central storage tank and the pumping
station.
Value of data: 25,188.60
Brief description of
measurement methods
and procedures to be
applied:
During normal operation of the plant, the pumps that will provide water will be
operated by grid electricity. During load sheds, a diesel-driven generator will
provide electricity. The diesel consumption will be monitored annually.
QA/QC procedures to
be applied (if any):All bills will be signed by the responsible staff and collected centrally for data
archiving.
Any comment:
Parameter: !,!,!
Unit: TJ/Gg
Description: NCVofDieselconsumedbytheproject
Source of data: IPCC2006. The chosen value reflects the conservative upper limit of the 95%
confidence interval.
Value of data: 43.3
Brief description of New IPCC publications will be checked and values be updated if necessary.
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measurement methods
and procedures to be
applied:QA/QC procedures to
be applied (if any):
Any comment:
Parameter: !"!,!,!
Unit: kg/TJ
Description: DefaultCO2emissionfactorfordieselcombustion
Source of data: IPCC2006. The chosen value reflects the conservative upper limit of the 95%
confidence interval.
Value of data: 74,800
Brief description of
measurement methods
and procedures to be
applied:
New IPCC publications will be checked and values be updated if necessary.
QA/QC procedures to
be applied (if any):
Any comment:
Parameter: !"#,!
Unit: Tonnes of energy carrying medium
Description: Average quantity of WECM released (or flared or wasted) in atmosphere in
year y.Source of data: Continuous on-site measurements
Value of data: Will be monitored ex-post
Brief description of
measurement methods
and procedures to be
applied:
Measurements of gas temperature and pressure.
QA/QC procedures to
be applied (if any):The meters will undergo maintenance/ calibration according to industrial
standards.
Any comment:
Parameter: !"#,!
Unit: deg C
Description: Average temperature of Waste Energy Carrying Medium (WECM) vented from
the preheaters and coolers of the two production lines in year y.
Source of data: Continuous on-site measurements
Value of data: Will be monitored ex-post
Brief description of
measurement methods
and procedures to be
applied:
Measurements of gas temperature.
QA/QC procedures to
be applied (if any):The meters will undergo maintenance/ calibration according to industrial
standards.
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Any comment:
Parameter: !"#,!
Unit: kg/cm2
Description: AveragepressureofWECMvented from the preheaters and coolers of the two
production lines inyeary.
Source of data: Continuous on-site measurements
Value of data: Will be monitored ex-post
Brief description of
measurement methods
and procedures to be
applied:
Measurements of gas pressure.
QA/QC procedures to
be applied (if any):The meters will undergo maintenance/ calibration according to industrial
standards.
Any comment:
Parameter: !"#,!
Unit: kg/m3
Description: AveragedensityofWECMventedfrom the preheaters and coolers of the two
production linesatactualtemperatureandpressureinyeary.
Source of data: Continuous calculation based on on-site measurements.
Value of data: Will be monitored ex-post
Brief description of
measurement methods
and procedures to beapplied:
Calculation based on temperature and pressure.
QA/QC procedures to
be applied (if any):The meters will undergo maintenance/ calibration according to industrial
standards.
Any comment:
Parameter: !"#
Unit: 1
Description: AveragedensityofWECMventedfrom the preheaters and coolers of the two
production linesatactualtemperatureandpressureinthreeyearspriorto
thestartoftheprojectactivity.
Source of data: Continuous calculation based on on-site measurements.Value of data: Will be monitored ex-post
Brief description of
measurement methods
and procedures to be
applied:
Calculation according to the mathematical procedures described above.
QA/QC procedures to
be applied (if any):The meters will undergo maintenance/ calibration according to industrial
standards.
Any comment:
B.7.2 Description of the monitoring plan:
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>>
For the operation of the Waste Heat Recovery Power Plant and monitoring of all the parameters, ACPL
has adopted the following procedures:
a) Responsibility of the Project Management
ACPL will be responsible for the execution of the monitoring plan. It will collect and store relevant data
in a systematic and reliable way, evaluate them regularly and ensure the availability of all the relevant
information for verification. Both paper and an electronic spreadsheet file will be kept for record keeping.
ACPL shall manage all monitored variables and will regularly present the same to the DOE for
verification.
b) Quality Assurance and Quality Control
The WHR Power Plant shall be considered as a separate section and effectively controlled by section
incharge under the supervision of GM (Works). The quality assurance and quality control for recording,
maintaining and archiving data shall be maintained by ACPL. It will also make sure that it provides the
staff in charge of data collection and monitoring with necessary training opportunities to enhance their job
skills and efficiencies.
c) On-site Procedures
Operation and Maintenance Logs (O&M)
Daily operational parameters will be logged and maintained for each equipment such as boilers, turbineand generator by the operator on real time basis. The maintenance of each equipment will be recorded in
the history file of each equipment. This will be reviewed by the section incharge on a regular basis. Any
event of significance will be reported and recorded in a special log, which will be reviewed by relevant
Senior Staff Members on regular basis.
Operation and Maintenance Report
The Section In-charge of WHR Power plant shall prepare a monthly report on the performance of WHR
Power Plant and submit the same to top management for their review and comments. The report will
include the following topics:
- Summary
- Production achieved
- Major cost elements- Stoppages report
- Accidents, malfunctions and remedial measure taken
- Safety and environment
- Meter records
- Any other material information
Procedure for handling of erroneous measurement, monitoring data adjustment and data
uncertainty
Respective Area supervisors are responsible for reporting and erroneous measurement, and any
uncertainty of parameters. The report will be sent to the section incharge for review and further action.
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Any erroneous measurement and uncertainty found will be recorded and the section incharge will be
required to immediate corrective actions under the supervision of GM (Works).
Procedure for training of monitoring staff
ACPL has detailed training programs for the relevant staff based on their technical knowledge
requirements that will help them to ensure smooth operations of the plant. When new equipment is
installed and/or the maintenance for the monitoring equipment is carried out, training for the proper
management and operation of the equipment will be provided to the operators.
Procedure for handling of emergencies situations
In accordance with the internal regulations, an Emergency Management Plan will be prepared. Personal
safety appliances will be provided to the shift operators according to their requirements. Regular training
for safety is provided to the shift operators by the Safety Incharge during the regular training as
mentioned above.
Data Storage and Filing Electric Workbook
All relevant data will be monitored and electronically stored at least 2 years after the end of the crediting
periods.
d) Operational and Management structure
The tentative operational and management structure of the personnel who will be involved in the project
activity is shown below:
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While the structure of the CDM responsibilities are displayed in a separate chart:
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B.8 Date of completion of the application of the baseline and monitoring methodology and thename of the responsible person(s)/entity(ies)
>>
Date of completion of the application of the baseline and monitoring methodology: 11/11/2010
Henning Huenteler
Senior CDM Services Manager
UPM Umwelt-Projekt-Management GmbH
PRC
100125 Beijing Chaoyang District
42 Liangmaqiao RoadGuangming Hotel 0708 (B)
UPM Umwelt-Projekt Management GmbH is a project participant as listed in section A.3 and Annex 1.
SECTION C. Duration of the project activity / crediting period
C.1 Duration of the project activity:
C.1.1. Starting date of the project activity:>>
13/05/2010 (Date of signature of main equipment purchase contract, it is the earliest date of real action of
the project)
C.1.2. Expected operational lifetime of the project activity:
>>
20 years, 0 months
C.2 Choice of the crediting period and related information:
A fixed crediting period is chosen. The relevant information is given in section C.2.2.
C.2.1. Renewable crediting period
C.2.1.1. Starting date of the first crediting period:
>>
Not applicable
C.2.1.2. Length of the first crediting period:
>>
Not applicable
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C.2.2. Fixed crediting period:
C.2.2.1. Starting date:
>>
15/05/2012
C.2.2.2. Length:
>>
10 years, 0 months
SECTION D. Environmental impacts
>>
D.1. If required by the host Party, documentation on the analysis of the environmental impactsof the project activity:
>>
Electric power will be produced by using the heat going waste in the exhaust gases of two coolers and
two preheaters of the already operational two cement lines. Therefore, the adoption of this technology
will contribute positively to conserve resource (heat) so far going waste while at the same time it will
further improve the environment. M/S HCRDI, China will supply technology/plant.
The total covered area for the power plant will be 1500 m2. No fuel will be used as waste heat of the
exhaust gases from two pre-heaters and two clinker coolers of the already two operational cement lines
will be used. Resultantly, there will not be any emissions of gases into the atmosphere. Further, the
process will result in lowering of the temperature of the discharged flue gases, thus avoiding the
phenomenon of "heat island". The cooling water requirement will be about 4,500 m3 for one time
charging in the cooling circuit of the plant and 106 m3/h will be used as make-up water for the minor
windage / cooling losses.
Effluent from all the areas of power plant including cooling tower and the sewage from toilets will be
mixed up with the effluent from the already operational cement plant and power plant and after its
anaerobic treatment it will be reused within the battery limits of the plant area for irrigation of vegetation,
trees, plants and sprinkling on road sides to minimize fugitive dust.
There will be no contribution of sulphur dioxide (SO2), Nitrogen Oxides (NOx), Carbon monoxide (CO)
and Particulate Matter (PM) from the power plant will not take place due to the fact that heat from the
waste gases (flue gases) of two coolers and two preheaters of the already operational cement plantpresently going waste, will be harnessed through use of Heat Exchangers (HEs). This heat will be used
for the power plant. Resultantly, zero emissions from the power plant will be achieved.
Solid wastes, to be generated from power generation activity, will be disposed off in environmentally
sustainable fashion. The plant inbuilt mechanism will help restrict the noise levels below their limiting
value of 85 dB(A) as prescribed by the National Environment Quality Standards (NEQS). Additionally,
because the plant is to be housed in a closed building, there will be further drastic cut in noise levels.
From the IEE (Initial Environmental Evaluation), it is concluded that the project requires only IEE and
there is no need of environmental studies in the form of an Environmental Impact Assessment (EIA).
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D.2. If environmental impacts are considered significant by the project participants or the host
Party, please provide conclusions and all references to support documentation of an environmental
impact assessment undertaken in accordance with the procedures as required by the host Party:>>
As described above, it is expected that there will be no significant negative environmental impacts
associated with the Project activity. Therefore, no EIA going further than the IEE-Report is necessary.
Additionally, Attock Cement Pakistan Ltd. will adopt measures to implement the issued recommended in
the IEE report.
SECTION E. Stakeholders comments
>>
E.1. Brief description how comments by local stakeholders have been invited and compiled:
>>A formal stakeholder meeting was conducted on August 03, 2010 at Officers Mess of ACPL after the
event was published by public notices on the 28 th of July on the factory gate, the workers union office and
the public market near the project site. A list of the meeting participants is presented on page 49.
During the meeting brief project description, likely environmental and socio-economic impacts, their
mitigation measures and project alternatives were defined to the stakeholders.
After description of the project, participants were to encourage asking the question regarding the project
environmental, socio- economic impacts and their mitigation measures. Their queries are incorporated to
this section.
After the introduction of the project, the stakeholders have filled out questionnaires regarding theiropinion towards the project. A summary of all answers can be reviewed in chapter E.2.
E.2. Summary of the comments received:
>>
The questio