TYPICAL INJECTION SYSTEM AND SILO DESIGN FOR AMENDED SILICATES · TYPICAL INJECTION SYSTEM AND SILO DESIGN FOR AMENDED SILICATES Provided By NOVINDA CORPORATION 999 18TH Street Suite

TYPICAL INJECTION SYSTEM AND SILO DESIGN FOR

AMENDED SILICATES

Provided By

NOVINDA CORPORATION 999 18TH Street

Suite 1755, North Tower Denver, CO 80202

October 2013

DISCLAIMER:

The information provided within these documents has been provided by Novinda and its representatives, and is to be used for general

background informational purposes only. The information regarding the use, application, storage, or delivery of Novinda’s amended silicates

mercury sorbent material is conceptual only, and has not been demonstrated in full scale application. Novinda is unable to report on or

accurately predict events that may affect full scale application. Novinda and its representatives provide no warranty of any kind, implied or

expressed, regarding the accuracy or suitability of this information. As such, the Receiving Party acknowledges and agrees that Novinda and its

representatives will under no circumstances be liable for any damage or loss however incurred from this information.

Rev. 10/09/13 Page 1 of 9

AMENDED SILICATES INJECTION SYSTEM

Table of Contents

1. General Description 2. Scope of Work 3. Material Properties & Injection Rates 4. Technical Requirements 5. Performance Requirements 6. Typical Silo Design for Amended Silicates and Powdered Activated Carbon

Appendix A – Schematic Flow Diagram – Novinda Amended Silicates

Appendix B – MSDS Sheets – Novinda Amended Silicates

Appendix C – Instructions to Bidders

Appendix D – Terms and Conditions – Provided by Owner

Appendix E – Facility Details – Provided by Owner

Appendix F – Lance Details

Appendix G – Jenike & Johanson Typical Silo Design for Amended Silicates and Powdered Activated Carbon

Rev. 10/09/13 Page 2 of 9

AMENDED SILICATES INJECTION SYSTEM

1. General Description

This specification covers the overall description, work scope, technical and performance requirements of a reagent injection system for a mercury emission control project. The specification requirements listed herein are based primarily on the work by Jenike & Johanson for Novinda and represent the minimum requirements to achieve consistent flow of the amended silicates material, and Novinda retains the right to review Owner’s design and drawings prior to fabrication and installation of the injection system. Designs deviating from these specifications may be considered on a case by case basis.

2. Scope of Work

The scope of work is to design, engineer, procure, fabricate and deliver the specified reagent injection system, support start up and testing of a complete, fully functional and operational mercury emission control system, which includes at a minimum but not limited to the items and services listed below. A typical schematic flow diagram of the injection system with termination points for the scope of work is shown in Appendix A.

1. Reagent Injection System including transfer blowers, material metering and feeding equipment and all required manual and motorized valves.

2. Reagent storage silo with vacuum/pressure relief door, bin vent fabric filter & vent fan and transfer pipe suitable to receive and transfer material from either rail cars or delivery trucks.

3. Transfer pipes from blower discharge to lance inlets including manual isolation valve at each. 4. All auxiliary electric system and controls for above scope.

3. Material Properties

The injection system shall be capable of unloading, handling, feeding, and injecting multiple sorbent materials, including amended silicates and powdered activated carbon (PAC). Detailed material properties and injection equipment design criteria for amended silicates are provided by Jenike & Johanson (J&J) and are listed within this specification section. Equipment design and operational considerations for the explosive and flammable properties of any sorbent material is the responsibility of the Owner and Bidder. Bidder shall also be responsible for ensuring that other PAC materials can be also utilized by the injection system. The injection system silo shall be designed to allow mass flow instead of funnel flow. A mass flow silo allows for first-in-first-out material flow, eliminates ratholes and stagnant material, and minimizes material segregation effects. The following criterion represents typical limiting conditions for flow, therefore larger silo outlets, steeper hoppers, and flow rates summarized below are acceptable: Cohesive Strength Since sorbent materials are cohesive and have the capacity to form a rathole in the injection system storage silo, the following are minimum mass flow silo discharge outlet diameter dimensions for gravity feed (GF) and air assisted silo bin bottoms. Continuous flow (GF) 1.3 feet After 1 day at rest (GF) 2.1 feet

Rev. 10/09/13 Page 3 of 9

For air assisted silo bin bottom 0.5 feet Compressibility Bulk density shall be considered in the design for silo loads, silo capacities, and system feed density. The range of bulk density for the amended silicates material is as follows: Measured range of bulk density 32.2 to 58.5 pounds per cubic foot PAC assumed bulk density 30 pounds per cubic foot Mass Flow Hopper Angles Design of the mass flow silo hopper shall include hopper angle, materials of construction, and surface finish. Hopper material shall have interior sloping surfaces lined with 304 stainless steel and #2B finish (cold rolled mill finish which cannot be achieved by polishing). Maximum recommended mass flow wall angles 10 degrees (from vertical for both continuous flow and after 1 day storage at rest) The MSDS for the amended silicates material can be found in Appendix B.

4. Technical Requirements

4.1 General

4.1.1 Engineering

The Contractor shall be responsible for performing all engineering and design, necessary for a complete and operating facility designated to be within Contractor’s scope, as spelled out herein. All project documents shall be signed and sealed by an engineer or architect registered in the state where the installation shall be located.

4.1.2 Procurement

The Contractor shall be responsible for the procurement of all permanent materials and engineered equipment necessary for a complete and operating facility designated to be within Contractor’s scope, including freight to the site, unloading and/or safe storage,

unless materials are specifically spelled out as “Owner-provided” within this document.

4.2 Mechanical

4.2.1 Equipment

Major pieces of equipment, include but not limited to, are listed in the following table.

Table1. Equipment List

No. Equipment No. Required. 1 Reagent Storage Silo 1 2 Air-assisted discharger 1 3 Manual Slide Gate Isolation Valve (at Silo Bottom) 1

Rev. 10/09/13 Page 4 of 9

4 Motorized dome valve 1 5 Motorized diverter valve 1 6 Gravimetric Feeder with Variable Frequency Drive (VFD) 2 (1 Operating &

1 Spare) 7 Drop Tube 2 (1 Operating &

1 Spare) 8 Motorized Rotary Lock-Hopper Valve 2 (1 Operating &

1 Spare) 9 Positive Displacement Transfer Blower & Motor 2 (1 Operating &

1 Spare) 10 Manual Isolation Valves (one at each Lance Inlet) TBD 11 Injections Lances TBD

4.2.2 Equipment Details

4.2.2.1 Reagent Storage Silo

The storage silo shall be designed to operate in Mass Flow when charged with Amended Silicates reagent, which exhibits material properties as described in Section 3 above. The storage silo shall be of welded construction with a roof for weather protection. It shall have an active storage capacity of 14-days calculated at maximum required reagent feed rate. It shall be provided with a fill pipe for pneumatic transfer of material from rail cars or delivery trucks using rail/truck transfer blowers. The silo shall have appropriately sized bin vent fabric filter with vent fan, a vacuum/pressure relief door at the roof, a caged ladder, roof man-way, safety railings, roof mounted level indicators and a side-wall mounted refill level indicator. Poke holes and access doors are not recommended for a mass flow silo since they have a tendency to restrict material flow; however, if necessary they shall be located in the vertical cylindrical section instead of the hopper. The material of construction for the cylindrical section shall be carbon steel and the conical section at the hopper bottom shall be constructed or have interior surface lined with 304 stainless steel, with #2B finish. Sheet thickness 10 gauge or thinner generally result in a smoother finish, which facilitates better material flow. As noted earlier, the conical section shall be designed to facilitate Mass Flow of material and avoid plugging. The hopper shall be designed to incorporate the use of an air-assisted discharge system, which consists of a 304 #2B lined conical hopper and the air-assisted discharger; with the hopper and air-assisted discharger being connected by a short vertical section required to maintain uniform flow (See Section 6.0). The material in the hopper is not intended to fluidize until material level drops below 5 feet.

4.2.2.2 Air-assisted Discharger

The air-assisted discharge membrane shall have a minimum pressure drop of 0.035 psi per scfm per sq. ft. of membrane area. The air supply should provide a no-flow pressure of 1.1 psig, maintain a pressure of 0.5 psig at 148.5 scfm, and provide a maximum (choked) flow of 6.4 scfm/ft2 of projected horizontal discharger area. Expected air flow during discharge is approximately 3.6 to 5.7 scfm/ft2 of projected horizontal discharger area. The recommended material for

Rev. 10/09/13 Page 5 of 9

the membrane is Polyveyor 1950 which is available from BeltService Corporation, or J&J approved equal.

The air-assisted discharger shall be a standard 6 foot diameter unit with minimum 6 inch outlet, and be supplied by Premier Pneumatics, Kice Industries, Nol-Tec Systems, Young Industries, Clyde Bergemann, or J&J approved equal. Compressed air that is introduced to the silo and that can come in contact with the silo contents shall be dried to a maximum dew point of -40◦F. The compressed air supply to the air-assisted discharger shall be provided by a pilot operated low-pressure regulator, such as a Fisher-Rosemont 299 series, or J&J approved equal. A pressure gauge shall be connected to the membrane plenum to serve as an indicator of a plugged or damaged membrane. Alternative air supply methods include regenerative blowers, or lobed-type blowers if supplied with controls to maintain constant pressure output over the required range of flow rates. Regardless of air supply equipment, an overpressure protection device shall be installed to the membrane plenum for safety. As an additional safety precaution, the silo shall be vented and an overpressure protection device utilized to allow for air flow into the silo.

4.2.2.3 Manual Isolation Valve at Silo Bottom

Bidder’s standard design proven in similar applications is acceptable.

4.2.2.4 Motorized Dome Valve

The outlet valve shall be high duty cycle dome type valve, supplied by Gemco, RoValve, Clyde Industries, or J&J approved equal. The outlet valve shall be fully open or fully closed, and shall not be operated partially open to throttle flow.

4.2.2.5 Automated Diverter Valve

The outlet stream can be directed to multiple fill points with the use of 12 inch air slides and diverter valves. Bidder’s standard design proven in similar applications is acceptable.

4.2.2.6 Gravimetric Feeder

The gravimetric feeder shall be capable of supplying 10-500 lb/hr as delivered with the capability to change the feed rate range by changing out the feed screw and delivery tube. The gravimetric feeder screw shall be controlled by a Variable Frequency Drive (VFD) that provides finite local adjustment of the reagent feed rate. The feeder shall be accurate within + / - 1% or 1 lb/hr (whichever is more) over a one minute interval. Modulation of material flow shall be accomplished by the feeder and not by a valve.

4.2.2.7 Drop Tube

The drop tube connected downstream of the gravimetric feeder outlet and upstream of the motorized rotary lock-hopper valve inlet shall be equipped with an inlet air filter that shall also provide a barrier against material exiting the top of the drop tube.

Rev. 10/09/13 Page 6 of 9

4.2.2.8 Motorized Rotary Lock-Hopper Valves

The rotary lock hopper valve shall be designed to convey a fine powder of the quantity specified in the Section 3 above and the distance of the Transfer Pipe System. Valve body/cylinder clearances shall be a ‘close-tolerance’ design.

4.2.2.9 Positive Displacement Transfer Blowers

Two positive displacement transfer blowers (one operating and one in-line spare) capable of meeting the feed rates listed in the Facility Details found in Appendix E and conveying the distance of the Transfer Pipe System (distance to be determined by Contractor and Owner). Blowers shall be sized to maintain Industry-practice velocities in all transfer lines and lances. The blowers shall be equipped with an inlet filter/silencer and all appurtenances necessary for safe start-up, operation & maintenance, and shut-down.

4.2.2.10 Manual Lance Isolation Valve

Bidder’s standard design proven in similar applications is acceptable.

4.2.2.11 Injection Lances

The lance shall use a concentric tube design that incorporates a flat or angled baffle affixed to the upstream side of the lance, normal to the bulk flow of the flue gas. The concentric tubes shall terminate at various distances across the duct to promote uniform distribution of reagent downstream of the baffle plate. The baffle plate induces local turbulence near the lance discharge points and promotes distribution along the axis of the lance. A sketch showing lance details is included in Appendix F. The number and location of the injection lances are to be determined by Contractor and Owner; however, lance spacing shall not be greater than 30 inches.

4.2.3 Equipment O&M Manual

Contractor shall provide the operations and maintenance (O&M) manuals for the scope of work. The O&M manuals shall consist of hard-copy binders and CDs with operations and maintenance data and information for the scope of work.

4.3 Piping

4.3.1 Feed Pipe System

The feed pipe system connects the storage silo outlet, manual isolation slide gate valve, motorized dome valve, motorized diverter valve, gravimetric feeder, drop tube, and motorized rotary lock-hopper valve to the transfer pipe system. Equipment within the feed pipe system is arranged as shown in Appendix A, and shall be close-coupled so as to minimize the length of feed pipe required; no elbows are allowed. The feed pipe shall be Schedule 80 carbon steel.

A spare feed pipe system consisting of the gravimetric feeder, drop tube, and motorized rotary lock-hopper valve shall be installed for redundancy to allow for scheduled and unscheduled maintenance activities. The automated diverter valve will be used to select

Rev. 10/09/13 Page 7 of 9

the feed pipe system. In all locations that include two phase flow, i.e. transport air + solids, minimum acceptable gas velocity must be maintained in order to avoid saltation of the larger particles present in the solid material.

4.3.2 Transfer Pipe System

The transfer pipe system consists of transfer pipes from the discharges of the transfer blower and motorized rotary lock-hopper valve to the lances, inclusive. The downstream side of the lance isolation valves shall be flanged connections. The injection lances shall bolt up to these isolation valve flanged connections. The transfer pipe shall be Schedule 80 carbon steel, with a minimum of 2” bidder’s standard thermal insulation with cladding proven in similar applications. Long radius elbows shall be used to mitigate erosion and the elbows and tee sections shall have replaceable wear plates to facilitate maintenance. The system shall be designed with transport velocities that prevent settling in the pipes at all load conditions and shall accommodate a nominal flow of 35 scfm per lance. The conveying distance shall be specific to each site/installation. The Contractor shall work with the facility Owner to identify the optimum Transfer Pipe routing. The transfer pipe shall be routed to the lance locations, which shall be uniquely identified for each unit; however lance spacing shall not be greater than 30 inches. The transfer pipe system lay out shall consider flow balance to injection lances, access for existing plant equipment in the area for maintenance, and minimal interference with plant operation during construction.

4.4 Electrical

4.4.1 Power Supply

Contractor is to provide a single 480 V, 3 Phase, 60 Hz power supply to supply all of the necessary electrical functions of the system.

4.4.2 Power Distribution

A main disconnect breaker shall be provided in the control panel, which shall be utilized to protect and to de-energize all reagent injection system equipment. A motor circuit protector, a starter and overload protection shall be provided for the 480-volt transfer blower motor. Three phase breakers shall be provided for power distribution to the control power transformer.

4.4.3 Control Panel

The reagent injection system controls and power distribution shall be contained within a dedicated control panel(s), including Programmable Logic Controller (PLC), Human Machine Interface (HMI), power supply, control relays, lights, terminal blocks, motor circuit protectors, motor starters, circuit breakers, etc. The control panel(s) shall be mounted in a conveniently accessible location. Panels shall be rated NEMA 4X. Terminal blocks shall be installed for termination of all District installed cables. All devices that shall be visible on the front of the control panels shall have durable, tight- adhering nameplates. Wiring shall be stranded copper, 600 volt, insulated, extra flexible type. As a minimum, wire size shall be #12 American Wire Gauge (AWG) for all power wiring, #14 AWG for all control panel exterior control wiring, #16 for all control panel interior control wiring and #18 AWG twisted shielded pair for analog signal conductors.

Rev. 10/09/13 Page 8 of 9

4.5 Instrumentation and Control

The system shall have the capability to set the maximum feed rate locally and adjust the feed rate from zero to the maximum user defined feed rate via an external 4-20mA signal. The system shall be capable of storing and exporting time stamped operating data which shall include the system feed rate as measured by the gravimetric feeder. The system shall be capable of storing at least one week’s worth (seven x twenty-four hour days) of such data taken at one (1) minute intervals. The data must be formatted such that it can easily be imported to a PC and Windows Excel.

4.5.1 PLC

The PLC shall control all necessary system functions such as startup, shutdown, feed rate control, feed piping selection (via diverter valve position), alarm functions and trips.

4.5.2 HMI

All local control and alarm monitoring shall be provided through a local HMI. The HMI shall have sufficient screens to display the following controls as a minimum:

1. System Control

2. Feeder Control

3. Status Display

4. Fluidizing Control

5. Transfer Blower Control

6. Feed Rate Set Point

7. Feed Piping Selection (A/B Train)

8. Active Alarms

a. The following status and alarms shall be displayed on the HMI:

i. Transfer Blower Status ON/OFF

ii. Gravimetric Feeder Status (A & B trains) ON/OFF

iii. Reagent Storage Silo Level Status LOW

iv. Gravimetric Feeder Status (A & B trains) MALFUNCTION

v. Transfer Blower Discharge Pressure HIGH/LOW

vi. Rotary Lock Hopper Valve Inlet Pressure (A & B trains) HIGH/LOW

b. The following control functions shall be on the HMI:

i. Local Start Selection Key

ii. Local Stop Selection Key

iii. Gravimetric Feeder OFF/AUTO Selection Keys (A & B trains)

iv. Alarm Acknowledge Selection Key

v. System Operation Local/Remote Selection Key

vi. System Mode Non-Paced/Paced Selection Key

vii. Fluidization System HAND/OFF/AUTO Selection Key

c. The following control switches shall be located on the control panel:

Rev. 10/09/13 Page 9 of 9

i. System Stop Pushbutton Switch / Emergency Stop

4.5.3 Gravimetric Feeder Speed Controllers

Each gravimetric feeder screw shall be controlled by a Variable Frequency Drive (VFD) providing finite local adjustment of the reagent feeding rate. Based on the system operating mode selected, the controller shall follow a constant feed rate or an analog 4-20 mA signal provided by an external source.

4.5.4 Sensors and Trips

The following system sensors and trips shall be provided at a minimum:

1. Transfer Blower Outlet Pressure Sensor

2. Rotary Lock Hopper Valve Inlet Pressure Sensor (A & B trains)

3. Drop Tube pressure differential (A & B trains) - if this approaches zero, the trip shall at a minimum shutdown the Gravimetric Feeder.

4. Gravimetric Feeder Hopper Low level Switch (A & B trains)

5. Gravimetric Feeder Hopper High Level Switch (A & B trains)

5. Performance Requirements

The Performance Requirements shall include but not limited to:

The system shall be capable of delivering the maximum and the minimum reagent feed rates specified.

The reagent distribution between the lances shall be uniform at all injection rates, i.e., the reagent flow at each lance shall be the same

Noise level shall not exceed 85 dBA at 3 ft. from the blower and all rotary/other equipment.

6. Typical Silo Design for Amended Silicates and Powdered Activated Carbon

The J&J silo design drawings in Appendix G provide an example of a typical amended silicates mass flow silo. The design and other details are provided for information only and to facilitate the Bidder in designing a silo suitable for this application. Each injection system and silo shall be designed for specific facility site conditions, duty, and performance requirements. Alternative designs may be considered at the discretion of the Owner.

Rev. 10/09/13

APPENDIX A

Schematic Flow Diagram

Novinda Amended Silicates

08/28/13

_______ - ____

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NONE

SILO

REAGENT STORAGE

SLIDE GATE VALVE

MANUAL ISOLATION

*OPTIONAL

AMBIENT AIR

*OPTIONAL

SKID*

AFTER COOLER

BIN VENT FILTER

RELIEF DOOR

VAC/PRESSURE

M

M

ISOLATION VALVES

MANUAL LANCE

PROCESS FLOW DIAGRAM

INJECTION SYSTEM

SK-00005

ISOLATION VALVES

MANUAL LANCE

M

(1 OPERATING & 1 SPARE)

TRANSFER BLOWER

POSITIVE DISPLACEMENT

TO AIR HEATER

TO AIR HEATER

(THERMAL INSULATION, OPTIONAL)

TRANSFER PIPE

GENERIC FLOW DIAGRAM

AMENDED SILICATES

RAIL / TRUCK UNLOADING

SKID*

DEHUMIDIFIER

LANCE SPACING < 30"

TOTAL NUMBER OF LANCES TBD

REGULATED AIR TO AIR-ASSISTED DISCHARGER

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DIVERTER VALVE

MOTORIZED

A

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B

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A

DROP TUBE

B

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MOTORIZED ROTARY

B

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MOTORIZED ROTARY

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SYSTEM. SPECIFIC ARRANGEMENT AND DETAILS

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Rev. 10/09/13

APPENDIX B

MSDS Sheets – Amended Silicates

MATERIAL SAFETY DATA SHEET

1. Product and Company Identification

Material name Amended Silicates™ HgX

Version # 08

Revision date April 26, 2013

Chemical description Modified Bentonite

CAS # Mixture

Manufacturer information Novinda Corporation2000 S. Colorado Blvd; Suite A-315Denver, Colorado 80222General Information: 720-473-8320Emergency (800) 424-9300

2. Hazards Identification

Emergency overview Material can be slippery when wet. Exposure to powder or dusts may be irritating to eyes, noseand throat.

Potential health effects

Routes of exposure Inhalation. Skin contact. Eye contact.

Eyes Dust in the eyes will cause irritation. Symptoms include itching, burning, redness and tearing.

Skin Dust or powder may irritate the skin. May cause skin irritation.

Inhalation Dust may irritate respiratory system. Inhalation of dusts may cause respiratory irritation. Repeatedor prolonged inhalation may cause toxic effects. For additional information on inhalation hazards,see Section 11 of this safety data sheet.

Ingestion May cause irritation. No significant adverse effects are expected upon ingestion of the product.

Target organs Lungs.

Chronic effects This product has the potential for generation of respirable dust during handling and use. Dustmay contain respirable crystalline silica. Overexposure to dust may result in pneumocononiosis, arespiratory disease caused by inhalation of mineral dust, which can lead to fibrotic changes to thelung tissue, or silicosis, a respiratory disease caused by inhalation of silica dust, which can lead toinflammation and fibrosis of the lung tissue. Occupational exposure to respirable dust andrespirable crystalline silica should be monitored and controlled.

3. Composition / Information on Ingredients

The manufacturer lists no ingredients as hazardous according to OSHA 29 CFR 1910.1200.

Constituents CAS # Percent

QUARTZ 14808-60-7 <= 5

Composition comments Occupational Exposure Limits for constituents are listed in Section 8. This product contains <5%total crystalline silica. The respirable crystalline silica as determined by the SWeRF method is<0.1% w/w.

4. First Aid Measures

First aid procedures

Eye contact Get medical attention if irritation persists after washing. Immediately flush with plenty of water forup to 15 minutes. Remove any contact lenses and open eyelids widely. If irritation persists:Continue flushing during transport to hospital. Take along these instructions.

Skin contact Wash the skin immediately with soap and water. Get medical attention if irritation develops orpersists.

Inhalation If dust from the material is inhaled, remove the affected person immediately to fresh air. Ifsymptoms are experienced, remove source of contamination or move victim to fresh air. If theaffected person is not breathing, apply artificial respiration. If breathing is difficult, give oxygen.Call a physician if symptoms develop or persist.

MSDS US

1 / 7

Material Name: AS HgX Version #8; April 26, 2013

Ingestion If ingestion of a large amount does occur, seek medical attention. No special measures required.

Notes to physician Provide general supportive measures and treat symptomatically.

General advice If you feel unwell, seek medical advice (show the label where possible).

5. Fire Fighting Measures

Flammable properties The product is not flammable. No unusual fire or explosion hazards noted. This material will notburn.

Extinguishing media

Suitable extinguishing media

Dry chemical, CO2, water spray or regular foam. Use any media suitable for the surrounding fires.

Protection of firefighters

Protective equipment andprecautions for firefighters

As in any fire, wear self-contained breathing apparatus pressure-demand, MSHA/NIOSH(approved or equivalent) and full protective gear. Material can be slippery when wet.

Fire fighting equipment/instructions

In the event of fire, cool tanks with water spray. Material can be slippery when wet..

Specific methods Cool containers exposed to flames with water until well after the fire is out.

Hazardous combustionproducts

None known.

6. Accidental Release Measures

Personal precautions Keep unnecessary personnel away. Local authorities should be advised if significant spillagescannot be contained. Use a NIOSH/MSHA approved respirator if there is a risk of exposure todust/fume at levels exceeding the exposure limits. Avoid inhalation of dust from the spilledmaterial. Material can be slippery when wet. Material can be slippery when wet. Forms smooth,slippery surfaces on floors, posing an accident risk.

Environmental precautions Prevent further leakage or spillage if safe to do so. Do not let product enter drains. Runoff fromfire control or dilution water may cause pollution. Do not contaminate water. Do not flush intosurface water or sanitary sewer system.

Methods for containment If sweeping of a contaminated area is necessary use a dust suppressant agent which does notreact with the product. This material is classified as a water pollutant under the Clean Water Actand should be prevented from contaminating soil or from entering sewage and drainage systemswhich lead to waterways. Block any potential routes to water systems.

Methods for cleaning up Should not be released into the environment. This product is miscible in water. Collect dust usinga vacuum cleaner equipped with HEPA filter. Collect dust or particulates using a vacuum cleanerwith a HEPA filter. Avoid the generation of dusts during clean-up. Following product recovery,flush area with water. For waste disposal, see section 13 of the MSDS. Reduce airborne dust andprevent scattering by moistening with water.

7. Handling and Storage

Handling Avoid dust formation. Do not breathe dust from this material. In case of insufficient ventilation,wear suitable respiratory equipment. Provide appropriate exhaust ventilation at places where dustis formed. Guard against dust accumulation of this material. Avoid contact with skin and eyes.Avoid release to the environment. Handle and open container with care. Practice goodhousekeeping. Material can be slippery when wet. Forms smooth, slippery surfaces on floors,posing an accident risk.

Storage No special restrictions on storage with other products. Store in a well-ventilated place. Keepcontainer tightly closed. Avoid dust formation. No special storage conditions required. Guardagainst dust accumulation of this material. Use care in handling/storage.

8. Exposure Controls / Personal Protection

Occupational exposure limits

US. ACGIH Threshold Limit ValuesFormValue TypeConstituents

INERT OR NUISANCEDUSTS (SEQ250)

TWA 10 mg/m3 Inhalable particles.

3 mg/m3 Respirable particles.QUARTZ (14808-60-7) TWA 0.025 mg/m3 Respirable fraction.

MSDS US

2 / 7


US. OSHA Table Z-1 Limits for Air Contaminants (29 CFR 1910.1000)FormValue TypeConstituents


PEL 15 mg/m3 Total dust.

5 mg/m3 Respirable fraction.

US. OSHA Table Z-3 (29 CFR 1910.1000)FormValue TypeConstituents


TWA 15 mppcf Respirable fraction.

15 mg/m3 Total dust.5 mg/m3 Respirable fraction.50 mppcf Total dust.

QUARTZ (14808-60-7) TWA 0.1 mg/m3 Respirable.0.3 mg/m3 Total dust.2.4 mppcf Respirable.

Exposure guidelines Occupational exposure to nuisance dust (total and respirable) and respirable crystalline silicashould be monitored and controlled.

Engineering controls Ventilation should be sufficient to effectively remove and prevent buildup of any dusts or fumesthat may be generated during handling or thermal processing. If engineering measures are notsufficient to maintain concentrations of dust particulates below the OEL, suitable respiratoryprotection must be worn.

Personal protective equipment

Eye / face protection Wear dust goggles.

Skin protection No special protective equipment required.

Respiratory protection Wear respirator with dust filter. Use a NIOSH/MSHA approved respirator if there is a risk ofexposure to dust/fume at levels exceeding the exposure limits.

General hygiene considerations

Do not breathe dust. Avoid contact with eyes. Handle in accordance with good industrial hygieneand safety practice. Eye wash fountain is recommended. Use good industrial hygiene practices inhandling this material.

9. Physical & Chemical Properties

Appearance Powder.

Physical state Solid.

Form Powder. Various.

Color Various.

Odor None.

Odor threshold Not available.

pH 5.5 - 6.5

Vapor pressure 0.050339494 hPa estimated

Vapor density Not available.

Boiling point Not available.

Melting point/Freezing point 1584.9 °F (862.714287557 °C) estimated

Solubility (water) Not available.

Specific gravity 3.15400096 estimated

Relative density Not available.

Flash point Not available.

Flammability limits in air, upper, % by volume

Not available.

Flammability limits in air, lower, % by volume

Not available.

Auto-ignition temperature Not available.

VOC 0 % estimated

Percent volatile 0 % estimated

MSDS US

3 / 7


Other data

Density 3.15368556 g/cm3 estimated

10. Chemical Stability & Reactivity Information

Chemical stability Stable at normal conditions.

Conditions to avoid Avoid spread of dust. None known.

Incompatible materials None known.

Hazardous decompositionproducts

Toxic gas. None known.

Possibility of hazardous reactions

Will not occur. Hazardous polymerization does not occur.

Toxicological data

11. Toxicological Information

Product Test Results

Acute Dermal LD50 Rabbit: 72856.7656 mg/kg estimatedAS HgX (Mixture)

Acute Oral LD100 Mouse: 5099.959 mg/kg estimated Acute Oral LD50 Mouse: 17352.5586 mg/kg estimated Acute Oral LD50 Rabbit: 12749.8984 mg/kg estimated Acute Oral LD50 Rat: 9927.5566 mg/kg estimated Acute Other LD50 Mouse: 66350.4688 mg/kg estimated Acute Other LD50 Rabbit: 51.0003 g/kg estimated

Constituents Test Results

Acute Oral LD50 Rat: 500 mg/kgQUARTZ (14808-60-7)

Acute effects Dust in the eyes will cause irritation. May cause skin irritation.

Local effects Inhalation of dusts may cause respiratory irritation.

Chronic effects In 1997, IARC (the International Agency for Research on Cancer) concluded that crystalline silicainhaled from occupational sources can cause lung cancer in humans. However in making theoverall evaluation, IARC noted that "carcinogenicity was not detected in all industrialcircumstances studied. Carcinogenicity may be dependent on inherent characteristics of thecrystalline silica or on external factors affecting its biological activity or distribution of itspolymorphs." (IARC Monographs on the evaluation of the carcinogenic risks of chemicals tohumans, Silica, silicates dust and organic fibres, 1997, Vol. 68, IARC, Lyon, France.)

In June 2003, SCOEL (the EU Scientific Committee on Occupational Exposure Limits) concludedthat the main effect in humans of the inhalation of respirable crystalline silica dust is silicosis."There is sufficient information to conclude that the relative risk of lung cancer is increased inpersons with silicosis (and, apparently, not in employees without silicosis exposed to silica dust inquarries and in the ceramic industry). Therefore, preventing the onset of silicosis will also reducethe cancer risk..." (SCOEL SUM Doc 94-final, June 2003)

According to the current state of the art, worker protection against silicosis can be consistentlyassured by respecting the existing regulatory occupational exposure limits. Occupationalexposure to nuisance dust (total and respirable) and respirable crystalline silica should bemonitored and controlled.

Carcinogenicity

ACGIH Carcinogens

QUARTZ (CAS 14808-60-7) A2 Suspected human carcinogen.IARC Monographs. Overall Evaluation of Carcinogenicity

QUARTZ (CAS 14808-60-7) 1 Carcinogenic to humans.US NTP Report on Carcinogens: Known carcinogen

QUARTZ (CAS 14808-60-7) Known carcinogen.

Ecotoxicological data

12. Ecological Information


EC50 Daphnia: 163.4608 mg/l 48 hours estimatedAS HgX (Mixture)

MSDS US

4 / 7



LC50 Fish: 908.895 mg/l 96 hours estimated

* Estimates for product may be based on additional component data not shown.

Ecotoxicity Components of this product are hazardous to aquatic life. No data available for this product.

Environmental effects An environmental hazard cannot be excluded in the event of unprofessional handling or disposal.

Persistence and degradability

Not available.

13. Disposal Considerations

Disposal instructions Collect and reclaim or dispose in sealed containers at licensed waste disposal site. Do not allowthis material to drain into sewers/water supplies. This product, in its present state, when discardedor disposed of, is not a hazardous waste according to Federal regulations (40 CFR 261.4 (b)(4)).Under RCRA, it is the responsibility of the user of the product to determine, at the time ofdisposal, whether the product meets RCRA criteria for hazardous waste. Dispose in accordancewith all applicable regulations. Material should be recycled if possible.

Waste from residues / unused products

Not applicable.

Contaminated packaging Empty containers should be taken to an approved waste handling site for recycling or disposal.

14. Transport Information

DOT

Not regulated as dangerous goods.

DOT

Packages less than 83 lbs


IATA


IMDG


15. Regulatory Information

US federal regulations OSHA Process Safety Standard: This material is not known to be hazardous by the OSHA HighlyHazardous Process Safety Standard, 29 CFR 1910.119.

Drug Enforcement Administration (DEA). List 2, Essential Chemicals (21 CFR 1310.02(b) and 1310.04(f)(2) Not regulatedDEA Essential Chemical Code Number

Not regulatedDrug Enforcement Administration (DEA). List 1 & 2 Exempt Chemical Mixtures (21 CFR 1310.12(c))

Not regulatedDEA Exempt Chemical Mixtures Code Number

Not regulated

CERCLA (Superfund) reportable quantity

None

Superfund Amendments and Reauthorization Act of 1986 (SARA)

Hazard categories Immediate Hazard - NoDelayed Hazard - YesFire Hazard - NoPressure Hazard - NoReactivity Hazard - No

Section 302 extremelyhazardous substance

No

Section 311 hazardous chemica

No

MSDS US

5 / 7


Inventory status

Country(s) or region Inventory name On inventory (yes/no)*YesAustralia Australian Inventory of Chemical Substances (AICS)

YesCanada Domestic Substances List (DSL)

NoCanada Non-Domestic Substances List (NDSL)

YesChina Inventory of Existing Chemical Substances in China (IECSC)

YesEurope European Inventory of Existing Commercial ChemicalSubstances (EINECS)

NoEurope European List of Notified Chemical Substances (ELINCS)

NoJapan Inventory of Existing and New Chemical Substances (ENCS)

YesKorea Existing Chemicals List (ECL)

YesNew Zealand New Zealand Inventory

NoPhilippines Philippine Inventory of Chemicals and Chemical Substances (PICCS)

YesUnited States & Puerto Rico Toxic Substances Control Act (TSCA) Inventory*A "Yes" indicates that all components of this product comply with the inventory requirements administered by the governingcountry(s) State regulations WARNING: This product contains a chemical known to the State of California to cause cancer.

US - California Proposition 65 - CRT: Listed date/Carcinogenic substance

QUARTZ (CAS 14808-60-7) Listed: October 1, 1988 Carcinogenic. US - New Jersey RTK - Substances: Listed substance

QUARTZ (CAS 14808-60-7) Listed.US - Pennsylvania RTK - Hazardous Substances: Listed substance

QUARTZ (CAS 14808-60-7) Listed.

16. Other Information

Recommended restrictions Workers (and your customers or users in the case of resale) should be informed of the potentialpresence of respirable dust and respirable crystalline silica as well as their potential hazards.Appropriate training in the proper use and handling of this material should be provided as requiredunder applicable regulations.

Further information This safety datasheet only contains information relating to safety and does not replace anyproduct information or product specification. HMIS® is a registered trade and service mark of theNPCA.

HMIS® ratings Health: 1*Flammability: 0Physical hazard: 0Personal protection:

NFPA ratings Health: 1 Flammability: 0Instability: 0

Disclaimer The information provided in this Safety Data Sheet is correct to the best of our knowledge,information and belief at the date of its publication. The information given is designed only as aguidance for safe handling, use, processing, storage, transportation, disposal and release and isnot to be considered a warranty or quality specification. The manufacturer expressly does notmake any representations, warranties, or guarantees as to its accuracy, reliability orcompleteness nor assumes any liability, for its use. It is the user's responsibility to verify thesuitability and completeness of such information for each particular use.

Third party materials: Insofar as materials not manufactured or supplied by this manufacturer areused in conjunction with, or instead of this product, it is the responsibility of the customer toobtain, from the manufacturer or supplier, all technical data and other properties relating to theseand other materials and to obtain all necessary information relating to them. No liability can beaccepted in respect of the use of this product in conjunction with materials from another supplier.The information relates only to the specific material designated and may not be valid for suchmaterial used in combination with any other materials or in any process, unless specified in thetext. The information in the sheet was written based on the best knowledge and experiencecurrently available.

Issue date 28-July-2011

MSDS US

6 / 7


This data sheet containschanges from the previousversion in section(s):

Product and Company Identification: Alternate Trade NamesHazards Identification: Emergency overviewHazards Identification: Potential environmental effectsHazards Identification: OSHA regulatory statusToxicological InformationRegulatory Information: US federal regulationsRegulatory Information: State regulations

MSDS US

7 / 7

Rev. 10/09/13

APPENDIX C

Instructions to Bidders

Project (______) Page 1 of 6 Rev.0

Project Name: Project No.: ______ Project Location:

To: All Bidders

You are invited to submit your PROPOSAL to furnish and deliver all items described herein, in strict accordance with the Instructions to Bidders and the following, which are attached and made part of this Inquiry:

1. Instruction to Bidders, 3 pages2. Special Notes to Bidders – Approved Suppliers, 2 pages3. Price Summary Form, 3 pages4. Intent to Quote*, 1 page5. Purchase Order Terms and Conditions, __ pages6. Site Conditions

*Bidder completion action is required: Complete, sign and return this document within 3working days of receipt of the Inquiry.

TO BE CONSIDERED, YOUR PROPOSAL MUST BE SUBMITTED BY: _________ ET on _________, 2013

Your proposal and any questions relative to this Inquiry shall be submitted in writing, via email and one electronic copy of all proposal document delivered to:

_______________ _________________________ _________________________ _________________________ EMail: __________________ Phone: __________________ Facsimile: ________________

INQUIRY Not an Order

Date:


INSTRUCTIONS TO BIDDERS

INQUIRY DESCRIPTION

You are invited to submit your best price proposal for the equipment and/or materials and related services described herein, complete with technical details, documents, and schedule to design, furnish, fabricate, manufacture, test, and deliver, FCA Jobsite (Latest INCOTERMS) or DDP Jobsite (Latest INCOTERMS) - Full Freight Prepaid and Allowed in accordance with the requirements stated herein and the attached Inquiry Documents.

Unless otherwise described in the Inquiry Documents, Bidders shall use the Project Location as the Destination for pricing the requirements of the proposal.

PROJECT DESCRIPTION

Design, procurement, construction, commissioning, and start-up of a sorbent injection system.

PROJECT SCHEDULE

Activity Date

Anticipated Award Date

Required On Site Date

Substantial Completion Guaranteed Date

PROPOSAL PROCEDURE

Bidder shall advise Buyer of its intent to provide a proposal, or its election not to provide a proposal, by completing and returning the attached Intent to Quote form within 3 days of receipt of this Inquiry. Proposals must be submitted in sufficient time to arrive no later than the date indicated on the Inquiry. LATE OR INCOMPLETE PROPOSALS WILL NOT BE CONSIDERED.

BIDDERS PROPOSAL MUST BE SUBMITTED ON THE ATTACHED PROPOSAL FORM, along with other attachments as required to satisfy the Proposal requirements listed herein and attached.

Proposals MUST include, but not be limited to, the following:

1. Firm Pricing for the goods and services itemized herein, detailed to identify: Firm Unit Item Costs (by items/groups) Required Warranty Freight costs Sales Taxes that will apply unless an exemption is provided

2. A Statement that proposal is valid for a period of not less than 90 days from the Bid Due Date3. Project Schedule4. Point(s) of fabrication, inspection and shipment5. Estimated shipping weight with recommended mode(s) of shipment

Bidder agrees to further itemize the bid prices, and to further describe its offering, when requested.

Proposals shall be signed by a duly authorized representative of the company with the signatory’s name and title printed or typed above the signature. Unsigned proposals may be considered invalid.

Buyer reserves the absolute right to withdraw this Inquiry or to reject or accept all or any part of the proposal without explanation, to waive any informalities therein, or to accept any proposal where it may


appear in the Owner’s or Buyer’s interest to do so. No liability or obligation of any kind shall be attached to the Owner or Buyer by reason of such action.

COMPLIANCE WITH SPECIFICATION AND ALTERNATE OFFERINGS

All proposals must respond to the material and/or equipment exactly as described in this Inquiry and all its attached documents. No modifications to, or deviation from, the Inquiry specifications shall be made unless authorized by written addenda. Proposals shall be submitted using all criteria specified. FAILURE TO ADDRESS THE BASE BID REQUIREMENTS MAY RESULT IN REJECTION OF THE PROPOSAL.

TERMS AND CONDITIONS

Any Order resulting from this Inquiry will be subject to the terms and conditions detailed herein and listed in the Inquiry Documents

INSPECTIONS AND TESTING

If required by the Inquiry Documents, Bidder’s proposal shall include any costs for witness testing and/or inspections by Buyer and/or Owner representatives, including being present at those stages of manufacture and testing demanded by the specified code or standard. Such inspection will include checking important points and dimensions, workmanship and acceptance of manufacturer’s test certificates where required. Successful bidder shall provide a suitable area and reasonable assistance to the inspector(s).

RESPONSIBILITY OF BIDDERS

Each bidder shall carefully examine all documents and material bound herewith or related hereto, together with all appropriate Addenda. Each bidder, by making its proposal, represents that 1) it has read and understands the Inquiry Documents and its proposal is made in accordance therewith; 2) its proposal is based upon the services, materials, and equipment described in the Inquiry Documents; 3) no extra charge will be allowed for ignorance of the requirements. The inter-relationships of all Inquiry Documents must be carefully examined by bidders.

The submission by any bidder of a proposal shall constitute conclusive evidence of compliance by such bidder with the above responsibility, and any claim relating to the established Price, at any future time, for labor, equipment or materials required, or for difficulties encountered which could have been foreseen had the Bidder so complied with its responsibilities hereunder, will not be recognized by Owner or Buyer.

The submission of a proposal shall constitute conclusive evidence that the Bidder has satisfied itself, as to the character, quality, and quantities of equipment or materials to be furnished and services to be performed, and as to the requirements of the Inquiry Documents, and if Bidder’s proposal is subsequently accepted, no allowance or concession to the Order Price will be made by Owner or Buyer at any time, for lack of such information on the part of the Bidder.

The Owner or the Buyer will not consider, for any purpose, any claim of the Bidder of any mistake or omission in the proposal. Negligence of the Bidder in preparing its proposal shall not confer or be deemed to confer any right of the Bidder to withdraw such proposal after the time fixed in the Inquiry Documents as the time for receiving and opening of proposals has passed.


PRICE SUMMARY FORM

BIDDER’S COMPANY NAME:

INQUIRY NO.: PROJECT NAME:

Base Bid Prices:

*ROS – Required On Site Date / *ARO – Calendar Days After Receipt of Order / All Pricing in U.S. Dollars (USD)

Tag Number

Qty U/M Description ROS* Promised Delivery

Days ARO*

Unit Cost $ (USD)

Extended Cost $(USD)

1 lot1 lot1 lot1 lot

N/A 1 Lot Standard Warranty (18/12

Months)

Additional Costs for Itemized Equipment Remarks/Clarifications Total Cost US$Startup and Commissioning Technical Support Freight Cost (FCA, Jobsite or DDP): Firm not-to-exceed freight cost delivered to Jobsite, full freight, including export/import duties, VAT taxes and insurance prepaid and allowed (latest INCOTERMS).

Total All Inclusive Base Bid Price USD $

Options:

The following Options or Alternate Prices are offered in addition to the Base Bid:

Option Number

Quantity Description Unit Cost US$ Add (Deduct)

Extended Cost $Add (Deduct)

1 LOT Three (3) years operation-maintenance (insurance) spares, including required spare parts catalogs recommended by Bidder.

Alternates:

Alternate Number

Quantity Description Unit Cost US$ Add (Deduct)

Extended Cost $Add (Deduct)

Addenda Receipt:

Receipt of the following Inquiry Addenda is hereby acknowledged:

Addendum No. Dated:

Addendum No. Dated:

Addendum No. Dated:


Proposal Contents:

In addition to this Proposal Form, Bidders proposal consists of the following (insert Attachment Number/Title and Date):

Document Submittal:

Approval Drawings on or before: days ARO Certified/Record Drawings on or before: days ARO

Delivery Complete:

Complete delivery to the location specified in the Inquiry Documents on or before ________days ARO

Additional Terms and Provisions:

Bid Validity Period: 90 days after bid date FCA / DDP Point: Freight:

Payment Terms: Shipping Points: Shipping Method: Estimated Shipping Weight: Heaviest Component / Container: Number of Shipments:

Agreement to Accept the Terms and Provisions of the Inquiry Documents:

We have reviewed the provisions of the Inquiry, the Inquiry Documents attached to the Inquiry, and the Addenda received and agree to accept the provisions without exception on any Order resulting from this Inquiry.

YES NO

If NO, our exceptions are listed below or on a separate document attached hereto. We understand that exceptions may be grounds for rejection of the proposal:

Technical Exceptions:

Commercial Exceptions:


INTENT TO QUOTE

RETURN IMMEDIATELY VIA FAX OR E-MAIL

TO: __________________

E-MAIL: ___________________

FACSIMILE NO: _____________

PROJECT: ___________________

INQUIRY NO: ____________

INQUIRY TITLE: ASI

QUOTE DUE : By ___________ ET on _________________, 2012

We have received your INQUIRY invitation and will submit our Quotation on or before the required due date.

YES NO

If NO, please state reason:

(Please print the following information:) (Representing Manufacturer, if applicable:)

COMPANY:

CONTACT: TITLE:

DATE: PHONE: FAX:

Rev. 10/09/13

APPENDIX D

Terms and Conditions

Provided by Owner

Rev. 10/09/13

APPENDIX E

Facility Details

Provided by Owner

Rev. 10/09/13

APPENDIX F

Lance Details

PLAN VIEW

04 PIPE PORT

TO SUIT TEST PORT NIPPLE

INLET PIPING AND FLANGE

TB

D

A A

T

BD

TB

D

SEE DETAIL 1

C C

B B

AIR PIPE

SORBENT & CARRIER

TB

D

FLOW TB

D

T

BD

01-1/4" & 02" SCH 40 PIPE

SORBENT & CARRIER AIR SUPPLYL3"X3" 1/4"X11’-0"

FLOW

04" SCH 40 PIPE PORT

LANCE TO FIT IN

TRIMMED IN ORDER FOR

ANGLE EDGES TO BE

3/16"

B/S

TYP

1/4

NESTED PIPE CONFIGURATION

PLACE @ END OF 02" PIPE

4 PLC’S TACK WELDED IN

1X3/16"X1/8" SPACER TAB TYP

VIEW A-A

RIB 1/4"X3/8"X4’ LG

1/8 3-12

01-1/4 SCH 40 PIPE

FLOW

FLOW

1 11/16

"X10’ 10

"

1 3/16"

VIEW B-B

VIEW C-C

1/8

45°

01-1/4"SCH 40 PIPE

DETAIL 1

1/8

1/8

3-12

3-9

SK-00006

TYPICAL LANCE DESIGN

DRY SORBENT INJECTION

NONE

08/28/13

08/28/13 AAH

.

.

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.

.

.

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.

.

.

_______ - ____

08/28/130

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FILENAME: PLOT DATE:

REV

DISCIPLINE

CIVIL

STRUCTURAL

MECHANICAL

PROCESS

DISCIPLINE

PIPING

ELECTRICAL

REVIEWED REVIEWED

REVISION APPROVAL DATE

REV.

PE #

SCALE

DATE

STATUS

FOR CONSTRUCTION

REVISED & APPROVED

CONSTRUCTION

APPROVED FOR

ISSUED REV SDE PEM

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SP

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421334PLANT LAYOUTS

ARCHITECTURAL

CH2MHILL Engineers, Inc.

ISSUED TO CLIENT

APPROVAL

FOR REVIEW AND

Rev. 10/09/13

APPENDIX G

Jenike & Johanson

Typical Silo Design for Amended Silicates and Powdered Activated

Carbon

TYPICAL - NOT FOR CONSTRUCTION

FOR INFORMATION ONLY

TYPICAL SILO DESIGN

NOVINDA CORPORATION

FOR AMENDED SILICATES AND

POWDERED ACTIVATED CARBON

INDEX OF DRAWINGS

11257-01 GENERAL ARRANGEMENT11257-01 GENERAL ARRANGEMENT11257-01 GENERAL ARRANGEMENT11257-01 GENERAL ARRANGEMENTCOVER SHEET1.GENERAL NOTES2.GENERAL NOTES CONTINUED3.GENERAL ARRANGEMENT4.

11257-02 CONICAL HOPPER AND RING GIRDER11257-02 CONICAL HOPPER AND RING GIRDER11257-02 CONICAL HOPPER AND RING GIRDER11257-02 CONICAL HOPPER AND RING GIRDERCONICAL HOPPER AND VERTICAL OUTLET DETAILS1.

2. RING GIRDER DETAILS

11257-03 SILO SUPPORT STRUCTURE11257-03 SILO SUPPORT STRUCTURE11257-03 SILO SUPPORT STRUCTURE11257-03 SILO SUPPORT STRUCTURESILO SUPPORT STRUCTURE1.SILO SUPPORT STRUCTURE DETAILS2.SILO SUPPORT STRUCTURE DETAILS (CONT'D)3.SILO SUPPORT STRUCTURE DETAILS (CONT'D)4.SILO SUPPORT STRUCTURE DETAILS (CONT'D)5.SILO SUPPORT STRUCTURE DETAILS (CONT'D)6.

11257-04 SILO ROOF DETAILS11257-04 SILO ROOF DETAILS11257-04 SILO ROOF DETAILS11257-04 SILO ROOF DETAILS1. ROOF DETAILS

MGH

24 Jun 13 0

TYPICAL SILO DESIGN

TYNGSBORO

TPN

11257-01

(978) 649-3300

4

NOVINDA CORPORATION

JCS

Perth, Australia

OF

DRAWING No.:

SCALE:

www.jenike.com

REVISION

TITLE:Tyngsboro, Massachusetts, USA

San Luis Obispo, California, USA

Toronto, Canada

Vina del Mar, Chile

SHEET FORMAT:

NONE

COVER SHEET

TPN JCS0 MGHFOR INFORMATION

1

130829

1"

SHEET SHEETS

DATEAPPDCHKDESCRIPTIONREV DWNDATECHK APPDDESCRIPTION DWNREV

TEL No.:

OFFICE:

APP'D:

DRAWN:

DATE:

CHK'D:

ANSI B (17x11in)

0

Bulk Solids: Science/Engineering/Design

SHEET SCALE:

PLOT DATE: 8/29/2013

JOHANSONJENIKE &



General Notes

(978) 649-3300

11257-01

NONE

0

TYPICAL SILO DESIGN

TYNGSBORO

TPN

24 Jun 13

MGH

4

NOVINDA CORPORATION

JCS

Perth, Australia

OF

DRAWING No.:

SCALE:

www.jenike.com

REVISION



Toronto, Canada

Vina del Mar, Chile

SHEET FORMAT:

130829

GENERAL NOTES

2

FOR INFORMATION MGH0 JCSTPN

1"

SHEET SHEETS


TEL No.:

OFFICE:

APP'D:

DRAWN:

DATE:

CHK'D:

ANSI B (17x11in)

0


SHEET SCALE:


JOHANSONJENIKE &

3.5 Some areas of the hoppers exposed to flow, such as weld joints, penetrations, etc., will require weld cleanup and finishing. The following

procedures are recommended.

3.5.1 Vertical butt joints in stainless steel hopper sections and liners:

- Grind weld to nearly flush with 100 grit disk. Minimize contact with adjacent surfaces and try to contain grinding to an area no greater

than 1/2" on each side of the weld bead.

- Finish with a narrow (1/2" maximum width) abrasive belt (180 grit or smoother), working so that the grain is produced parallel to the

weld joint and all 100 grit grind marks are removed. Finish with coarse Scotchbright surface conditioning belt, or equivalent. Contain

finishing to an area 1" to each side of joint.

3.5.2 Horizontal joints between top edge of a hopper or liner and a vertical wall:

- It is not critically important that this joint be smooth. It is imperative that the hopper surface be protected during welding because of the

potential for excessive spatter onto the surface below the joint, particularly for field installed liners.

- Cleanup should be limited to smoothing over any high spots or obvious protrusions. This joint does not have to be smooth and polished.

It is better to leave the weld bead unfinished and avoid the possibility of scuffing the surface below the joint.

Under no circumstance shall the downhill edge of a horizontal joint be allowed to protrude inward and create an upward facing ledge.

(A protrusion will impede material flow.)

3.5.3 Plug welds should not protrude above the liner surface. Cleanup of plug welds should be limited to smoothing over, using a 100 grit

disc, any high spots or protrusions above the liner surface. Minimize contact with the liner surface around the plug welds and try to

contain grinding to an area no greater than 1 in. from the edge of the plug weld. Finish the surface of the liner around the plug weld

using a narrow (1/2 in. maximum) width abrasive belt, (120 grit or smoother) working so the grain is produced in the direction of flow.

Contain finishing to an area 1 in. around the plug weld perimeter.

3.5.4 Areas that are inadvertently scuffed or damaged by welding can be cleaned and polished with a belt sander or flap wheel (180 grit or

smoother).

Cleanup should be limited to the smallest possible area around the blemish, and done so that the grain of the finish aligns with the

direction of material flow along the hopper wall.

If cleanup from scuffing or weld spatter exceeds 10% of the surface area of any single section, tests must be run on samples of the repaired

surface, or in the actual hopper, to confirm that the surface finish is acceptable.

3.5.5 Narrow abrasive belt sanders are available from Dynabrade, Inc., 8989 Sheridan Drive, Clarence, NY, tel. 1-800-828-7333,

www.Dynabrade.com. Suggested model is Dynafile model 40320, with no. 11304 contact arm for flat surfaces, which uses 1/2" wide

belts.

4 Painting and Gasketing

4.1 Painting shall confirm to the project contract specification.

4.2 Omit shop paint 2” on each side of field welded connections.

4.3 All flanges shall be gasketed with Dow Corning 732 silicone rubber adhesive sealant, or engineering approved equal.

3.2 Every precaution must be taken to protect the interior sloping surfaces or liners during fabrication and erection. It is very difficult, and sometimes impossible, to restore the original frictional characteristics of a cold rolled surface by mechanical finishing.

3.3 It is recommended that 1/16" thick fiberglass fire-resistant fabric be used to protect stainless steel wall surfaces. A suitable fiberglass cloth

(part no. 8816K42) is available from McMaster-Carr Supply Co.: Atlanta tel. (404) 346-7000; Chicago tel. (630) 833-0300; Cleveland tel. (330) 995-5500; Los Angeles tel. 562-692-5911; New Jersey tel. (732) 329-3200.

3.4 Do not use pickling paste, oven cleaner, or any other similar product on the sloped stainless steel wall surfaces or finished weld joints

exposed to flow. These products will damage the cold rolled 2B surface finish and alter its flow characteristics. The surfaces should be cleaned only with hot water and mild detergent. Only soft cotton cloths, not abrasive pads, should be used.

rolling the conical hopper to shape with unsuitable rolls that could mar or scratch the 2B finish.

the successful operation of the silo will be jeopardized if the surface finish of 2B finish is destroyed by weld spatter, careless grinding, or 3.1 Maintaining the surface finish on the inside surfaces of sloping hopper sections is critical. This silo is designed to provide mass flow, and

3 Interior Surface Finish

seal welded as indicated on the drawings.

fastened to intermediate structural elements by 5/8” diameter plug welds at 12” intervals. In some cases plates may be required to be 2.8 Checkered plate shall be fastened to the structural elements by 3/16”x4” long fillet welds at 12” intervals. As well, the plates shall be

2.7 All internal welds shall be ground flush and smooth.

subcontractor cost. 2.6 All welds that fail non-destructive inspection or complete penetration welds that are not 100% penetration shall be repaired at

Welded Steel Tanks for Oil Storage, Section 8, except base the number of spot radiographs on the aggregate footage of weld in each silo.

welds welded in seller's shop. Conform to the standards of acceptance as specified in American Petroleum Institute Specification API 650, 2.5 Radiographically inspect structure shell (e.g. cylinder, cone, transition hopper, wedge hopper) joints with complete joint penetration (CJP)

2.4 All welds shall be visually inspected and documented.

2.3 All weld operators shall be currently AWS qualified. 2.2 Connections between the hopper cone and cylinder, as well as hopper sections, shall be complete joint penetration welds.

ER309L Wire: Carbon steel to 304(L) stainless steel E71 T-1 (Flux Cored): Carbon steel to carbon steel

ER70S3 Wire (unless noted otherwise): Carbon steel to carbon steel

Gas Metal Arc Welding (GMAW):

1 General

1.1 The contractor must compare and coordinate the drawings of all disciplines and report any discrepancies before the start of the work.

1.2 Do not scale dimensions from the drawings.

1.3 All steel shall be designed, supplied, fabricated and erected in accordance with the latest provisions of the ASTM designation (last edition), the applicable client standards and the project contract specifications.

W-shapes and WT-shapes ASTM A992

C-shapes, Angles and Plates ASTM A36

HSS shapes ASTM A500, Grade B

1.4 NOVINDA retains the right to review silo design and shop drawings prior to fabrication.

2 Welding

2.1 All welding shall in accordance with AWS D1.1 Structural Welding Code - Steel (latest edition).

Shielded Metal Arc Welding (SMAW):

E7018 Electrodes (unless noted otherwise): Carbon steel to carbon steel E309 Electrodes: Carbon steel to 304(L) stainless steel



TYNGSBORO

(978) 649-3300

11257-0124 Jun 13 0

TPN

MGHNONE

4

NOVINDA CORPORATION

TYPICAL SILO DESIGN

JCS

TITLE:

Perth, Australia

OF

DRAWING No.:

SCALE:

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REVISION

Tyngsboro, Massachusetts, USA


Toronto, Canada

Vina del Mar, Chile

SHEET FORMAT:

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GENERAL NOTES CONTINUED

3

FOR INFORMATION JCSMGH0 TPN

JOHANSON

1"

SHEET SHEETS


TEL No.:

OFFICE:

APP'D:

DRAWN:

DATE:

CHK'D:

ANSI B (17x11in)

0


SHEET SCALE:


JENIKE &

5 Erection

5.1 Unless noted otherwise, bolts shall conform to ASTM A325. Nuts shall conform to ASTM A563, Grade DH, heavy hex or ASTM A194, Grade 2H, heavy hex. All bolts and nuts shall be hot-dipped galvanized per ASTM A153. Provide bolts and nuts from the same

manufacturer. Obtain manufacturers certification of the compatibility of the components after galvanizing, regardless of the

galvanizing method specified. 5.2 Under no circumstance shall the downhill edge of a horizontal joint be allowed to protrude above the joint plane and create a ledge

that would impede material flow.

5.3 Shop fit-up of some silo components are required prior to shipment to erection site. 5.4 NOVINDA retains the right to witness shop fit-up of silo components, erection of silo and equipment, and silo start-up and

commissioning activities.

5.5 Tighten all A325 fasteners using load indicating washers per AISC specification for structural joints using ASTM A325 bolts, (last edition)

5.6 It shall be the installation contractor's responsibility to adequately brace and support all members, including temporary scaffolding,

for wind, seismic, snow and construction loads. 5.7 All weld-on lifting lugs installed in the field shall be removed and the surface metal ground flush with 100 grit disk. Finish with 180

grit disk.

5.8 All fabrication and erection details shall be in accordance with AISC Manual of Steel Construction (14th edition). 5.9 During the erection of steel beams and diagonal bracing, all bolting and field welding shall be completed.

6 Design Data

6.1 The silo is designed to store modified bentonite and PAC based on material flow properties per J&J report 11257-2, dated November 15,

2012, and report 11257-4R1, dated April 3, 2013 6.2 Structural design is based on a bulk density of 58 pcf.

6.3 External load analysis according to ASCE/SEI 7-05.

6.4 Design Basis:- 400 MW Plant

- Material moisture content ≤ 1.2%

- Max storage at rest: 24 hr- Estimated Capacity:

140 tons Bentonite (based on 50 pcf)

84 tons PAC (based on 30 pcf) 6.5 Design Notes:

- Seismic:

0.2 Second Spectral Response 27.9%1.0 Second Spectral Response 6.0%

Seismic Site Class D

-Wind:Basic Wind Speed 90 MPH

Surface Roughness C

B.P.

I.D.CL

CJP

O.D.PLCSREFSTIFSHTTHKTYPU.N.O.U/S

General Notes

7 Abbreviations

Base PlateComplete Joint PenetrationCenterlineInside DiameterOutside DiameterPlacesReferenceStiffenerSHTThickTypicalUnless Noted OtherwiseUnder SideDiameter



RING GIRDER,

SEE DWG 11257-02

11257-0124 Jun 13 0

TYPICAL SILO DESIGN

TYNGSBORO

(978) 649-3300

TPN

MGH

4

NOVINDA CORPORATION

JCS

Perth, Australia

OF

DRAWING No.:

SCALE:

www.jenike.com

REVISION



Toronto, Canada

Vina del Mar, Chile

SHEET FORMAT:

AS SHOWN

GENERAL ARRANGEMENT


4

130829

1"

SHEET SHEETS


TEL No.:

OFFICE:

APP'D:

DRAWN:

DATE:

CHK'D:

ANSI B (17x11in)

0


SHEET SCALE:


JOHANSONJENIKE &

270 0

PLAN VIEW

180

90

ROOF COMPONENTS NOT

SHOWN FOR VIEW CLARITY

60°

COLUMNS,

TYP (6) PLCS

SILO CYLINDER

SEE DWG 11257-02

SEE DWG 11257-03

SUPPORT STRUCTURE,

AND VERTICAL OUTLET,

ISOMETRIC VIEW

SCALE 1 : 100

CONICAL HOPPER

SILO ROOF,

SEE DWG 11257-04

ONLY PARTIALLY SHOWN

FOR VIEW CLARITY

CJP,

SCALE 1 : 80

ELEVATION VIEW

DWG

SILO TRANSITION

ELEV = 0'-0"

SHT 1

SILO SUPPORT STRUCTURE

ELEV = 41'-0"

U/S BP

TYP

11257-02

3/8" THK CS PLATE,

2'-8"

RING GIRDER

SILO CYLINDER

26'-0"

VERTICAL OUTLET

1/4" THK CS PLATE,

3'-0"

14'-0" I.D. CYLINDER

1/4" THK CS PLATE,

23'-4"

6'-0"

I.D. OUTLET

CYLINDER RINGS

41'-0"

SUPPORT STRUCTURE

22'-8"

1/4" THK CS PLATE,

CONICAL HOPPER

A A

10°

(REF)

10°

REF

1 1/4" MAX.

SEE MEC. DWG

20°

ANGLE STIF SPACING,

TYP (12) PLCS

60°

SUPPORT COLUMN

SPACING, TYP

(6) PLCS

TYPICAL - NOT FOR CONSTRUCTIONFOR INFORMATION ONLY

D2

D1TYPICAL AIR ASSISTED DISCHARGER

ARRANGEMENT DEPENDS ON MFG

SPECIFICATION

SECTION B-B

CONICAL HOPPER ELEVATION

SHT 2

6'-0" I.D. OUTLET

22'-8"

1/4" THK CS PLATE,

CONICAL HOPPER

3'-0"

1/4" THK CS PLATE,

VERTICAL OUTLET

2'-8"

RING GIRDER

AT CYLINDER

1/2" THK CS

FLANGE

14'-0" I.D.

AA

C C

SECTION C-C

OUTLET MATING FLANGE

6'-6 1/2"

O.D. FLANGE

MIN. (40) 13/16" THRU HOLES

EQ. SPACED ON MAX 6'-3" BOLT

CIRCLE FOR 3/4" HEX HD,

GRADE 5, ZINC PLATED BOLTS,

SEE AIR ASSISTED DISCHARGER DWG

CLBOLT

SCALE 1 : 6DETAIL D1

OUTLET FLANGE WELD

3/16

3/16

1/4" GAP

MIN. 1/2" THK CS

PLATE FLANGE, SEE

MEC. DWG

CJP,TYP

SILO CYLINDER PLATE,

SCALE 1 :80ISOMETRIC VIEW

SHEET 2 FOR DETAILS

CONICAL HOPPER

VERTICAL OUTLET

RING GIRDER, SEE

1/2" THK CS PLATE

OUTLET FLANGE,

(SHOWN HERE FOR REF ONLY),

SEE DWG 11257-02

SHT 2

CL

DWG 11257-01, SHT 3SECTION A-A

90

0

180

270

CL COLUMN

CL ANGLE STIF

CL COLUMNCL COLUMN

CL COLUMNCL COLUMN

COLUMN

ALL INTERIOR SLOPING SURFACES SHALL BE LINED

WITH 304 #2B FINISH STAINLESS STEEL SHEET.

(WELDING AND OTHER SPECIFICATIONS TO BE

DESIGNED)

B B

D

D

11257-02 0

TYPICAL SILO DESIGN

NOVINDA CORPORATION

224 Jun 13

TPN

(978) 649-3300

TYNGSBORO

MGH

JCS

OF

DRAWING No.:

SCALE:

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REVISION



Toronto, Canada

Vina del Mar, Chile

Perth, Australia

SHEET FORMAT:

1:50 UNO

CONICAL HOPPER AND

VERTICAL OUTLET DETAILS


1

130829

SHEET SHEETS


TEL No.:

OFFICE:

APP'D:

DRAWN:

DATE:

CHK'D:

ANSI B (17x11in)

01"

SHEET SCALE:


JOHANSON Bulk Solids: Science/Engineering/Design

JENIKE &

NOTE:

1. DETAIL NUMBERS ARE FOR DRAWINGS 11257-02.


3/16

SHT 1SECTION D-D

CONE PLATE

WT8x18

1/4" THK CS

6"x5/8" THK CS PLATE,

RING GIRDER STIFFENER CONNECTION

CONTINUOUS RING GIRDER TOP PLATE

SILO

L4x4x1/4" STIFFENER, TYP

INSIDE

TYP3/16

CYLINDER PLATE

1/4

SCALE 1 : 4DETAIL D3

1/4

WT8x18

SILO SUPPORT COLUMN

CONE TRANSITION CONNECTIONS

CJP

1/4" THK CONE PLATE

1/4

SHT 1DETAIL D2

CONTINUOUS RING GIRDER TOP PLATE

SILO TRANSITION

1:1 NOTCH, TOP OF COLUMN

RING GIRDER CONFIGURATION

WT8x18 RING

6"x5/8" THK CS PLATE,

TYP (6) PLCS

1:1 NOTCH

SILO

SILO SUPPORT COLUMN,

INSIDE

CONE PLATE

1/4

SEE DWG 11257-03,

CJP6-12

1/4

1/4

6-12

1/4TYP

2'-8"

3/8" THK CS

RING GIRDER PLATE

2"

CYLINDER PLATE

E E

3/8" THK CS RING

GIRDER PLATE

CL

1 : 6SCALE E-E

TYPICAL COLUMN WELD CONNECTION

WT8x18 RING

SECTION

COLUMN

5/16

5/16TYP

11257-02 0

TYPICAL SILO DESIGN

NOVINDA CORPORATION

224 Jun 13

TPN

(978) 649-3300

TYNGSBORO

MGH

JCS

OF

DRAWING No.:

SCALE:

www.jenike.com

REVISION



Toronto, Canada

Vina del Mar, Chile

Perth, Australia

SHEET FORMAT:

1:10 UNO

RING GIRDER DETAILS


2

130829

SHEET SHEETS


TEL No.:

OFFICE:

APP'D:

DRAWN:

DATE:

CHK'D:

ANSI B (17x11in)

01"

SHEET SCALE:



JENIKE &


10'-3"

10'-3"

10'-3"

10'-3"

RING GIRDER,

SHOWN FOR REF ONLY,

SEE DWG 11257-02

R7'-5 7/16"

60°

TYP

TYNGSBORO

MGH

11257-03 0

(978) 649-3300

TPN

24 Jun 13 6

NOVINDA CORPORATION

TYPICAL SILO DESIGN

JCS

TITLE:

Perth, Australia

OF

DRAWING No.:

SCALE:

www.jenike.com

REVISION



Toronto, Canada

Vina del Mar, Chile

SHEET FORMAT:

130829

1 : 80

SILO SUPPORT STRUCTURE


1JOHANSON Bulk Solids: Science/Engineering/Design

SHEET SHEETS


TEL No.:

OFFICE:

APP'D:

DRAWN:

DATE:

CHK'D:

ANSI B (17x11in)

01"

SHEET SCALE:


JENIKE &

ISOMETRIC VIEWNTS

SECTION B-B

SUPPORT COLUMN,

TYP (6) PLCS

D1

D8

D3

D4

D9

SECTION A-A

SHT 5

ELEV=0'-0"

SILO TRANSITION

HSS 4x4x1/4" TYP

W8x28 BEAM, TYP CL BEAM

BEAM

BEAM

TOP OF CONE

U/S BP

ELEV=10'-3"

ELEV=20'-6"

ELEV=30'-9"

W10x45 COLUMN, TYP

CL

CL

SHT 3

SHT 4

W8x28 BEAM, TYP

W8x28 BEAM, TYP

SHT 2

ELEV=41'-0"

SILO CYLINDER,

SHOWN FOR REF ONLY,

SEE DWG 11257-01

SHT 6

D2

SILO

CL

BASE PLATE PLAN

SHT 2

W10x45

COLUMN, TYP

NOTE:

1. DETAIL NUMBERS ARE FOR DRAWINGS 11257-03.

W8x28

W8x28

W8x28

W8x28

10'-3", 20'-6", 30'-9"

W8x28

PLAN AT ELEV:

W8x28

A A

BB


7" PLATE

2" THRU HOLE FOR

1-1/4" ANCHOR RODS,

TYP (4) PLCS

TYPICAL W8 BEAM TO W10 COLUMN CONNECTION

SHT 1DETAIL D2

TYPICAL SUPPORT COLUMN BASE PLATE

COLUMN LOADS (PER EACH COLUMN)

VERTICAL (kips) HORIZONTAL (kips)

DEAD LOAD (SELF WEIGHT) 10-

MATERIAL LOAD 60 -

LIVE/SNOW LOAD 5 -

WIND LOAD 40 5

SEISMIC LOAD 150 15

MGH

11257-03

1:8

0

TYPICAL SILO DESIGN

TYNGSBORO

(978) 649-3300

TPN

24 Jun 13 6

NOVINDA CORPORATION

JCS

Perth, Australia

OF

DRAWING No.:

SCALE:

www.jenike.com

REVISION



Toronto, Canada

Vina del Mar, Chile

SHEET FORMAT:

SILO SUPPORT STRUCTURE DETAILS


2

130829


SHEET SHEETS


TEL No.:

OFFICE:

APP'D:

DRAWN:

DATE:

CHK'D:

ANSI B (17x11in)

01"

SHEET SCALE:


JOHANSONJENIKE &

DETAIL D1

PLAN VIEW

SHT 1

SUPPORT COLUMN

BEAM, TYP

NOTCH BEAM FLANGE AS

REQ'D TO FIT COLUMN

CONNECTION, TYP

CL

CCSUPPORT COLUMN

PLATE, TYP EACH FACE

ISOMETRIC VIEW

5/16" THK CONNECTION

BEAM

ELEVATION C-C

1/4

1/4

BEAM WEB

TO CONNECTION

PLATE, TYP

CL3"

FOR 3/4" HEX BOLT,

BOLTSCL

8"

PLATEBOLTS

13/16" THRU HOLE

TYP (4) PLCS

4"

2 1/2" TYP

1-1/4" THK BASE PLATE

W10 COLUMN

CL

CL

5/16

7 1/2"

7 1/2"

6 1/2"

5 1/2"

5 1/2"

8 1/2" 8 1/2"

6 1/2"


DETAIL D3SHT 1

TYPICAL HSS BRACE TO W8 COLUMN CONNECTION

MGH

11257-03

1:10

0

TYPICAL SILO DESIGN

TYNGSBORO

(978) 649-3300

TPN

24 Jun 13 6

NOVINDA CORPORATION

JCS

Perth, Australia

OF

DRAWING No.:

SCALE:

www.jenike.com

REVISION



Toronto, Canada

Vina del Mar, Chile

SHEET FORMAT:



3

130829


SHEET SHEETS


TEL No.:

OFFICE:

APP'D:

DRAWN:

DATE:

CHK'D:

ANSI B (17x11in)

01"

SHEET SCALE:


JOHANSONJENIKE &

PLAN VIEW

CL BEAM AND PLATE

2"

3"

FOR 3/4" BOLT, TYP

13/16" THRU HOLE

3"

2"

2" TYP

GUSSET, BOTH SIDES DD

SIDES

BOTH

EACH FACE, TYP

W.P.

PLATE, TYP

3/8" THK GUSSET PLATE,

3/16

ELEVATION D-D

6-1/2"x3/8" THK

1'-4 1/2" PLATE, TYP

TYP

8"TYP

PLATE,

1'-0 5/8"

1/2" TYP

TYP

HSS, TYP

TYP

1/4

ISOMETRIC VIEW

W8x28 BEAM, TYP

BRACE

3/16

3/8" THK PLATE,

3/16

GUSSET PLATE

1/4

TYP (2) PLCS

1/4" THK END CAP,

TO W8,

THRU HOLES FOR 3/4" HEX BOLT

AND NUT, TYP (16) PLCS

UPWARD FACING ENDS ONLY, TYP

GUSSET

BRACE CONNECTION CLIP,

3/16

CAP TO

TYPICAL - NOT FOR CONSTRUCTIONFOR INFORMATION ONLYSHT 1

HERE ONLY. INFORMATION IS MIRRORED ALONG BEAM

3/16

THIS DETAIL IS TYPICAL FOR A BOTTOM-SIDE

DETAIL D4

CLARITY, A BOTTOM-SIDE CONNECTION IS SHOWN

W.P.

AND A TOP-SIDE BEAM CONNECTION. FOR VIEW

CENTER-LINE FOR TOP-SIDE CONNECTION.

TYPICAL HSS BRACE TO W8 BEAM AND W8 COLUMN CONNECTION

NOTE:

3/16

MGH

11257-03

1:10

0

TYPICAL SILO DESIGN

TYNGSBORO

(978) 649-3300

TPN

24 Jun 13 6

NOVINDA CORPORATION

JCS

Perth, Australia

OF

DRAWING No.:

SCALE:

www.jenike.com

REVISION



Toronto, Canada

Vina del Mar, Chile

SHEET FORMAT:



4

130829


SHEET SHEETS


TEL No.:

OFFICE:

APP'D:

DRAWN:

DATE:

CHK'D:

ANSI B (17x11in)

01"

SHEET SCALE:


JOHANSONJENIKE &

PLATE, BOTTOM SIDE OF BEAM,

SEE DWG 11257-03, SHT 2

ISOMETRIC VIEW

ON THIS SHEET

3/16

ATTACHMENT CLIP PLATE

W10 COLUMN, TYP

PLATE, SEE DETAIL D6

BRACE

3/16" THK CS CAP PLATE,

TOP SIDE LOCATIONS ONLY

W8x28 BEAM, TYP

3/8" THK CS BRACE

SEE DETAIL D5 ON THIS SHT

PLATE SHOWN FOR REF ONLY,PLAN VIEW

NOTCH BEAM AS REQ'D TO FIT

AT COLUMN INTERSECTION, TYP

EE

5/16" THK BOLTING PLATE #1

DETAIL D5

MATCH BEAM

NOTCH

4"

3"

3" TYP

1'-2"

7"

13/16" THRU HOLES

FOR 3/4" HEX BOLTS, TYP


DETAIL D6

3"

3"

TYP

1'-11 3/8"

3"

TYP

7"

4"

3"

13/16" THRU HOLES


D7

ELEVATION E-E

SIDES

3/16

3/16

BOTH

3/16

TYP

1'-6" CLIP PLATE

2'-3 3/8"

8"

PLATE

CLIP PLATE

BOLTING

1/2" TYP

DETAIL D7

1

1

NOTCH

NOTCH DETAIL

9 1/2"


PLAN VIEW

7"

TOP PLATE

F F

BOTH

W.P.

SIDES

3/16

ELEVATION F-F

3/16

3/16

NOTCH

45°

1/2" TYP

CLIP PLATE

1'-10 7/8"

1/2"

6" TOP

PLATE

8"

TYP

DETAIL D8SHT 1

TYPICAL HSS BRACE TO W10 COLUMNCONNECTION AT RING GIRDER

MGH

11257-03

1:10

0

TYPICAL SILO DESIGN

TYNGSBORO

(978) 649-3300

TPN

24 Jun 13 6

NOVINDA CORPORATION

JCS

Perth, Australia

OF

DRAWING No.:

SCALE:

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REVISION



Toronto, Canada

Vina del Mar, Chile

SHEET FORMAT:



5

130829


SHEET SHEETS


TEL No.:

OFFICE:

APP'D:

DRAWN:

DATE:

CHK'D:

ANSI B (17x11in)

01"

SHEET SCALE:


JOHANSONJENIKE &

BOLTING PLATE, SEE

DETAIL D6, ON SHT 4


3/8" THK CS BRACE

3/16

3/16

3/16

WT8 RING

ISOMETRIC VIEW

W10 COLUMN

6"x7"x1/2" THK PLATE

TOP-SIDE OF BRACE,

3/16" THK CAP PLATE,

BRACE

BOTH SIDES


MGH

11257-03

1:10

0

TYPICAL SILO DESIGN

TYNGSBORO

(978) 649-3300

TPN

24 Jun 13 6

NOVINDA CORPORATION

JCS

Perth, Australia

OF

DRAWING No.:

SCALE:

www.jenike.com

REVISION



Toronto, Canada

Vina del Mar, Chile

SHEET FORMAT:



6

130829


SHEET SHEETS


TEL No.:

OFFICE:

APP'D:

DRAWN:

DATE:

CHK'D:

ANSI B (17x11in)

01"

SHEET SCALE:


JOHANSONJENIKE &

3/8" THK BRACE

COLUMN BASE PLATE,


BOLTING PLATE, SEE

SEE DETAIL D2, ON SHT 2

DETAIL D10, ON THIS SHT

W10 COLUMN

3/16

3/16

3/16

BRACE

ISOMETRIC VIEW

3/16

PLAN VIEW

GG

ELEVATION G-G

W.P.

SIDES

BOTH

3/16

2'-6"

CLIP PLATE

8"

1/2" TYP

DETAIL D10


3"

3"

TYP

TYP

13/16" THRU HOLES


3"

7"

2'-6"

3"

4"

SHT 1DETAIL D9

TYPICAL HSS BRACE TO W10 COLUMNCONNECTION AT BASE PLATE

2'-7 15/16"

(NOTE 3)

5'-3 7/8"

2 EQ SPACES



1/2"

1/2"

CHECKERED PLATE

NOTES:

ALL DIMENSIONS ARE TO INSIDE FACES UNLESS 1.

OTHERWISE NOTED.

MAXIMUM CHECKERED PLATE SPAN IS 3'-0".2.

DIMENSIONS TO BE COORDINATED WITH3.

MECHANICAL DRAWINGS.

DETAIL NUMBERS ARE FOR DRAWINGS 11257-04.4.

(978) 649-3300

TYNGSBORO

MGH

11257-04

JSB

05 July 13 1

NOVINDA CORPORATION

TYPICAL SILO DESIGN

0JCS

REVISION

TITLE:

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OF

DRAWING No.:

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SHEET FORMAT:

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1:32

ROOF DETAILS

JSB JCS0 MGHFOR INFORMATION

1

SHEET SCALE:



SHEET SHEETS


TEL No.:

OFFICE:

APP'D:

DRAWN:

DATE:

CHK'D:

ANSI B (17x11in)

01"

JENIKE &

ISOMETRIC VIEW

D2W10x22

5/16" THK

W10x22

C8x11.5

DEPENDS ON MFG SPECIFICATIONS

C8x11.5

W10x22

CHECKERED PLATE,

W10x22

C8x11.5

NUMBER AND ARRANGEMENT

D1

TYP.

ROOF PLANC8x11.5

LEVEL MEASUREMENT PROBE

PRESSURE RELIEF DOOR

ARRANGEMENT DEPENDS

ON MFG SPECIFICATIONS

2'-7 15/16"

(NOTE 3)

1'-8 1/8"

2'-10 1/2" CLR

(NOTE 3) (NOTE 3)

(NOTE 3)

(NOTE 3)

2'-8 3/8" CLR

(NOTE 3)

2'-0" CLR

14'-0" ID

VENT FABRIC FILTER

ARRANGEMENT DEPENDS

ON MFG SPECIFICATIONS

PLAN

SILO WALL

ANGLE RING

REINFORCING PAD

TYP CLIP TO

FABRICATE PLATE ANGLE

CLIPS TO FOLLOW RADIAL

EDGE. (TYP)

TYP W-BEAM

FRONT/SECTIONFRONT/SECTIONFRONT/SECTIONFRONT/SECTION

5/16" THK

2

1

TYP

W-BEAM

TYP

REINFORCING PAD,

1/4

3/16

x5/16

4-12

SILO WALL

4-12

CLIP,

L31

2x3

3/16

1/4

1'-0"

1/2"

1'-0"

R2"

TYP

W-BEAM

1/4TYP

SILO WALL

1/4

3/16

DETAIL D1 - TYP CONNECTION - W10 TO SILO WALL

SCALE 1:8

(ALL AROUND)

3/16

SIDE/SECTIONSIDE/SECTIONSIDE/SECTIONSIDE/SECTION

CLIP, L

REINFORCING PAD

L4x4x1/4

ANGLE RING,

1/4TYP

CLR

6"

1/2"

2"

SCALE 1:8

L3x3x5/16

FRONT/SECTIONFRONT/SECTIONFRONT/SECTIONFRONT/SECTION

CLIP,

DETAIL D2 - TYP CONNECTION - C8 TO W10

C8 BEAM

W-BEAM

3/16TYP

5"

C8 BEAM

TYP

SIDE/SECTIONSIDE/SECTIONSIDE/SECTIONSIDE/SECTION

3/16

W-BEAM

CLIP, L

3/16

3/16TYP

1"

9/16"

1/2" CLR