## D. Harris September 22, 2015 Correspondence to R. Kaplan



# Exhibit B Amec Foster Wheeler Report Re: HEPA Filtration

### September 11, 2015

Amec FosterWheeler Project# 186-140054-02 Veolia ES, TWI, Sauget, IL HEPA Filter Study

Mr. Doug Harris General Manager Veolia ES Technical Solutions 7 Mobile Avenue Sauget, IL 62201

Dear Mr. Harris, 

# foster

Amec FosterWheelerwas contracted byVeolia Environmental Services to complete a high-level studyto identifythe impact and benefits of installing High Efficiency Particulate Arresting (HEPA} filters in the gas cleaning trains ofthree existing incinerators at theirTWI facility in Sauget, IL. The three incinerators consist oftwofixed hearth incinerators (Units 2 and 3} and one rotary kiln incinerator (Unit4}. Each incineration unit has its own gas cleaning train that consist ofthe same unit operations. The current gas cleaning systems include a partial quench 

### Ispray dryer with lime injection foracid gas control, followed by a baghouse with powdered activated carbon (PAC} injection for control of particulate and dioxin 

### Ifurans, followed by an induced draft (ID) fan and a stack. Stack gas flowrates, temperatures, and moisture contentwere provided by Veolia ES as follows:
• Stack temperature on all three units is normally in the 350
- 375 degree F range • Stack moisture on all three units generallyvaries between 30% to 40 %
• Stack flow during CPTs on units 2 and 3 5,000 to 6,000 dscfm (about 15,000 acfm}
• Stackflow on unit 4 (rotary kiln} was 15,000 to 16,000 dscfm (about40,000 acfm}. Summaries of particulate matter (PM}, lowvolatile metal (LVM}, and semi-volatile metal (SVM} emissions from Comprehensive Performance Tests (CPT} were also provided by Veolia ES and are attached to this letter. As shown in Attachment 1, during the lasttwo CPTs (in 2009 and 2013}the unit average emissions forthese pollutants are generallyfrom 5to 10times lowerthan the current HazardousWaste Combustor (HWC} Standards. This indicates a superior level of control with no furthertreatment required. Also attached in Attachment 1arethe results ofa one-time particle size distribution studythatwas done in 2005 on incinerator#4 (rotary kiln}. However, to determine the impacts and benefits ofadding HEPAfilters to each ofthe units downstream ofthe existing baghouses, Amec FosterWheeler contacted suppliers of HEPA

10876 S. River Front Parkway Suite 250 South Jordan, UT 84095 Phone: 801-382-6900 amecfw.com Blake D. Beckstrom, P.E. Registered office: Salt Lake City, Utah Office Registered in USA Page 1of4

### Continued

... filters and fans to obtain budgetary pricing, and sizing information. These equipment quotations are included in Attachment 2 to this letterfor your reference. The following equipmentwould be required:
• Incinerator 2: A bank of 16 HEPAfilters is required to handle the gas flowrate. Each HEPA Filter has aface size of2ft. x 2ft. and a depth of 11.5 inches. This bankwould be 8 feet wide by 8 feet tall. A second bank offilters would be required to keep the system in operation while the first bank is being replaced, once their useful life is reached. Due to the 400 F flue gastemperature, the HEPAfilters have to be designed for high temperature application. A boosterfan would also be required to provide the motive force for the additional pressure drop through the HEPAfilters, and additional dueling. The fan would have a static pressure requirement of approximately 3.5 inches ofwater column when the filters are clean, and approximately 7.5 inches ofwater column when the filters are dirty and need replacing. This results in afan that is 31 inches in diameter and requires 24 brake horsepower.
• Incinerator 3: Since this incinerator is almost identical to Incinerator2, the same equipment is assumed to be required for this unit.
• Incinerator4: Due to its larger capacity, three banks of 16 HEPAfilters, as described above, would be required to handle the gas flowrate from Incinerator4. Afourth bank would be required to keep the system in operation while one ofthe other banks offilters is being replaced, once their useful life is reached. This application would also require high temperature HEPAfilters due to the 400 Fflue gas temperature. The boosterfan forthis unit would have approximately the same static pressure requirement as incinerators 2 and 3, but since the gas flow is larger, the fan would be 48 inches in diameterand requires 64 brake horsepower. Blake Beckstrom and Dean Bybee ofAmec FosterWheelervisited the plant site on September 2, 2015, to determine where the new HEPAfilters, fans and additional dueling could be installed and what ancillary equipment might be required. Unfortunately, all three incineration units are very tightly configured, especially in the area from the baghouses to the existing ID fans and stacks, as shown in the photos in Attachment 3. Installation of HEPAfilters and fans ofthis size, with the required ductwork, would be difficult and would most probably require relocating existing buildings and/orequipmentto allowfor adequate access for maintenance ofthe new and existing equipment.

. Amec FosterWheeler used the equipment supplier's budgetary prices and applied appropriate installation factors to estimate an installed costforthe new equipmentfor each incinerator. The installation factors coverthe cost ofitems such as foundations, electrical, structures, platforms, instrumentation and controls, valves, and dueling that are necessary for installing, operating, and maintaining the equipment. This cost estimate is shown in the spreadsheet in Attachment 4. The estimated installed costs are $642,000 each for incinerators 2 and 3, and $1,177,000 for incinerator4. This is a total of$2,460,000 for all three units. Due to the difficulties ofthe installation, Amec FosterWheelerdid not identify possible locations forthe newequipment and the installed cost estimate does not include anycost of relocating existing facilities Additionally, there will be operating costs associated with the new equipment. It is estimated that the HEPAfilters will have a 1-yearservice life and will therefore need to be replaced once peryear in each incineration train. The replacement filters will cost $95,000/year. This cost Blake D. Beckstrom 10876 S. River Front Parkway Suite 250 South Jordan, UT 84095 Phone: 801-382-6900 amecfw.com Page 2of4

### Continued

... does not include the labor costs of replacement. At 90% on-stream factor and $0.08 per kw-hr for electricity, the additional cost of running the three new boosterfans is estimated to be $71 ,000/year. HEPAfilters have demonstrated removal efficiencies of 99.97% on 0.30 micrometer diameter particles as shown in the vendor information from Flanders. Based on the particle size distribution study available, the HEPA filters would be expected to reduce the total number of particles emitted by only 28.6% when the filters are operating properly. However, since the incinerators are alreadyfar exceeding the emission limits for particulate matter, as well as low volatile and semi-volatile metals, by factors of 5to 10, the actual benefit of removing this additional small increment of particulate matter is not significant. Additionally, increasing the total pressure drop through the incineration system makes it more difficultto control the small draft pressure required at the front of the incinerator. Ifthe draft pressure is too negative, the complete combustion ofthe waste is compromised by excessive leakage ofair into the incinerator. But ifthe pressure goes positive, partially combusted, hot gas (that has not been scrubbed) can be emitted at ground levels where it is much more hazardous to personnel at the plant and results in emission ofmultiple pollutants at levels above HWC standards. HEPAfilters have been used on combustors thatfeed mixed or radioactive waste material due to the need ofeliminating radioactive particulate to extremely low levels. However, Amec Foster Wheeler is not aware ofany commercial industrial hazardous waste incinerators that employ the use of HEPAfilters. Therefore they are not proven in this application and are not industry accepted standard. As shown by the operating data for these units, HEPA filters are not required as a control method to meet HWC standards. It has been a pleasure working with you and your staff on this study. Ifyou have any questions orwould like to discuss these results in more detail, please feel free to contact me. For information, the professional resumes ofthe author and Don Leavitt, who also contributed to this work, are included in Attachment 5.

Kind Regards, Blake Beckstrom Sr. Process Engineer

Attachments: 1. Plant Operating and Test Data 2. Equipment Quotations Engineered Air Systems--Flanders HEPA Filters and Housings Robinson Fans 3. Photographs ofTWI incinerators 4. Cost Estimate Spreadsheet Blake D. Beckstrom 10876 S. River Front Parkway Suite 250 South Jordan, UT 84095 Phone: 801-382-6900 amecfw.com Page 3of4

### Continued

...
5. Resumes

Blake D. Beckstrom

### Blake D. Beckstrom Don 

### R. Leavitt

10876 S. River Front Parkway Suite 250 South Jordan, UT 84095 Phone:**801~382-6900** amecfw.com Page4 of4

# amec 

# foster wheeler

ATTACHMENT 1 PLANT OPERATING AND TEST DATA" 

## 2009 and 2013 CPT Particulate Matter (PM) Results

- --- --- 

# I 

# 1"''"'-1 I '.... .I

.. . - 

### HWC Standardfor 

### PM ••· 0.013**~-~--·-** 

# I
-------- ---

-- 

### - 

### 2009 

### Unit :1. Unit 3 Unit 4

-----



### ---- .. ··-- - 

### Run 1 

### 0.0013 0.0017 0.0023

- .. - ..... -

.. Run 2 

### 0.0017 0.0015 0.0020
-·

. -----· -- 

### -- 

### Runl 1 

### 0.0008 0.0016 0.0042

---- - 

### 0.0013

# t
0.0016

-..•. Average 0.0028

·-- 

### %of**Standa~d** 

### 9.7 

### 12.3 21c8 f

. 

# I ------

" ....
I - --- --- --**---~**.. 

### 2013 

### Unit 2 Unit3 Unit 4

--· 

### -- ----- - --- - - ... 

### Run 1 0.00087 0.00194 0.00269 Run 2 0.00068 0.00202 0.00183

. ··-- Run 3 

### 0.00058 0.00204 0.00190

···--------

-------- --··- 

### Average 0.00071 0.00200 0.00214

---- - 

### %

### ofStandard 

### 5.5 15.4 16:5 

# I I I -------·

- --

-· --·· ----- 

# I**~** ------ -- 

### Unit 2Average%ofStanda!d 

### 7.6 

# I --

- --- ----- 

### Unit 3Average%ofStandard 13.8 

# -·-·-··· I •.. 

# J I Unit4 Average%ofStandard 

# . 19.1

### 2008 and 2013 CPT LVM and SVM Results 

# T HWCStandard for LVM •·· 92 ug/dsctl1_ 

### ····+----t"H""'W.._,C:..::Standard for SVM_··_·-+--""23.._0**ug/ds~m** __ _
Unit 3 

# --+-"u,..,,;

.. t

### 4='---l 22.3 

### c-·_-cc2o=-=.oc:cs-:c(L:-c.

# ~::-Mo:-)-c-1. 1:-.·-:uc-n-:cit"".z=--+-

..

## -:-:-u"n"'T"t 3,_····_·

## +---'U"-n"'it:.:c4c.·_· 

# tJ. ·· .z zooooss .

# ((.s~~~.- u,)itZ

___

### B_u_~ __10.2 28.6 5.2 

# i±=_Runi _,.3.,.2.::-4_+_"'5"'8."'6

# I--.-.-----~R~,-,_n~2+1_-_-_~"3~.2~~~:+-l ______

# -:c2-0~.1--+--1-0_.3_ . 

# j Run 2 _

# ~10c-."C4-~:~~~6:7_."Cl~---·- -+---·_.3_1_)

___

### 1**_!!~~~** 

## _ ·- _7.,.5-___t--'1'-"5'-'.6'---+--'1._,3"'.5'---+ Run 3 26.9 -'"46_,.2.,__--j--

..27.1 Average 7.0 21.4 9.7 

### 23.2 5"'.7'::.3'_--1-- 27.0 %ofStandard 7.6 23.3 10.5 %of

### Staodcwd 10.1 24.9 

# I

-- ---+----f-- 

# I

- -----1---f--

- . -+----1------1--···· 2013 (LVM) Unit2 Unit3 Unit4'-+--l-"2 00 01:o:3JSVM)

_**-'=U"'n"-it!:.2_l--'=U"'n"'it_~3** Run

# 1l 2.8
Run 2 2.4 

### r------:c--::1

.. , .. - 1----_.R_..u..,n-"43 -· 2.5 Average 2.6 %of

### Standard 

### 2.8. 

# I

Unit2Average% of**Star:-~_ard**

## l-c----"~~ 

# I Unit3 Average% of Standard Unit4 Average% ofStandard 

## \ 8.6 8.9 11.0 

## --·-·--+---+--·-- 12.0 Run 1 1.1 20.0 

### ···--1--f--- -"-'9

. ..,8

__

# -+--+--- Run 2 0.78 14.0



## .**-"·---+-~--** 7.5 Run 3 1.0 12.0

.. 9.5

_ _.9..,.8'---jf----!----"A""'ve.ra_ge

. 

# I 15.3

# ~o-3 

# t.-.**_1'0-'9--+--+-%-·_·"·_rst~!!ii:Otlll-· _q:-.4·-~lf---6;_7_·_··.•·.··**  t-----+---Fu..,ni..,t .,z.._.Av,.erage%ofStandard 5;3

## .'-------+---tc-~- . 

# I I**---+--f'U"'n'-'it-=3~Average%**ofStandard**1?~'8.** 

# [

. I I 5;2**1-0.~6** -· Unit 4Average% ofStandard 8.1- 11.8

Unit4

7.1 8.1 15.0 10.1

### MVA# Table 1. MVA 6251. METCO Project05-36 Percentages of Particles inVarious Diameter Ranges by Numberof Particles

Q0321 00322 Q0323 Metco ID R1-0536-PSD-FIL R2-0536-PSD-FIL R3-0536-PSD-FIL Diameter Range(Jlm) 0.1-0.2 55.7 52.2 49.2 0.2-0.3 21.8 23.3 22.2 0.3-0.4 9.1 7.6 9.1 0.4-0.5 3.5 4.4 4.9 0.5-1.0 7.0 8.2 10.6 1.0-2.5 2.4 3.2 3.6 2.5-5.0 0.4 0.8 0.4 5.0-7.5 0 0.4 0 7.5-10 0 0 0 >10 0 0 0

- .. 

### Total Numberof Particles 1073 502 1066

6251report031705.doc Page 3 of3 

## F-4

# amec foster wheeler



# ATTACHMENT 2 EQUIPMENT QUOTATIONS HEPA Filters- Engineered Air Systems ID Fan
- Robinson Fans

### General Flanders manufactures metal-frame separator-style HEPA filters lor applications with high-temperature requirements up to 1,000°F (540°C) for exhaust air only and 500°F (260°C) for supply air. Hightemperature filters are available with eitheragasket or fluid seal. Filters with Blu-Jel® Fluid Seal have a maximum service temperature of 390°F (199°C) 

### HEPA Filters Each HEPA filter has a m1n1mum efficiency of 99.97% on 0.30 micrometer size particles when tested at rated capacity on a Q-107 Penetrometer. Each filter is challenged with an approved nearly monodispersed oil aerosol of 0.30 micrometer size and by measuring the upstream and downstream concentration ofthese particles with a light scattering photometer, the penetration can be determined and the efficiency can be calculated. 

### ScanTested HEPA Filters Each Scan Tested HEPA filter has a m1n1mum efficiency of 99.99% on 0.30 micrometer particles. Scan testing is in accordance with Section 6.2 of IEST-RP-CC034.1, HEPA and ULPA Filters Leak Tests. In the scan test, the filter is challenged with a high concentration of an approved oil aerosol or PSL (Polystyrene Latex Spheres). The media pack and pack-to-frame seal is scanned using a photometer or particle counter to insure that there are no leaks greaterthan .01% ofthe upstream concentration at 100 fpm face velocity. Scan testing is only available for the 500°F model. 

### SealantTypes Two types of sealants for high-temperature HEPA filters are offered. Silicone Sealant 

### This is a high temperature (RTV) silastic-sealant silicone compound rated for continuous service up to 500°F(260°C). NOTE: This high-temperature sealant is not UL 586 approved. Glass PackSealant ForExhaustAirOnly 

### The glass pack seal is rated for continuous service up to 1,000°F(540°C) in exhaust air applications only. It is a mat of submicron glass fibers that creates a seal when compressed between the filter pack and filter frame. The glass packing is not an adhesive seal but a mechanical seal that functions much as the glass fiber medium of the filter itself. NOTE: Due to the possibility that the glass pack may shed glass fibers, the glass pack sealant should be used for exhaust systems only.



### Alpha HT Filter Dimensions and Capacities

11-1/2

P81403-0408 (2) 

### CFM CAPACITIES AND DIMENSIONS

GG·F 24x24 650 1000 1300 GC-F 24x12 300 455 590 YY-F' 23-3/Bx23-3/8 615 945 1235 YU-F 23·3/8x11-3/8 275 425 550 GN·F 24x30 830 1275 1655 CC-F 12x12 135 205 265



### Flanders Corporation
- Foremost in Air Filtration Toll Free: 1-800-637-2803 38 26 37 25 45 14

### 0

- 007 

## c
- 02
- 03
- IE
- 32 F

# H"dw•re~ 0**~None** T**~ E~t~ctor**  Clips Efficiency 007**~** 99,97% OOP (PUREFORM) 99.99%on ,30micr<>tn<!lern "SUSealant Capacity/Pack Style C**~Separator** Frame**Materi~l** 02**~** 16GA 409 Stainless**OJ~** 16GA 304 Stainless Frame Style 03**~** Oouble-TumedFlange 05**~** 314" DeepChannel SealantMaterial IE**~High** Temperature Silicone IG**~Ceramic** and Glass Mat SE**~High Temp!'!r~ture**  Silicone Scan Tested (99.99% on 1).30 micrometers) B=B" c=12" E"' 1B" G"'24" 

### L_ Filter Depth D=5-7/8" F = 11-112" FitterFace Sizes (H x W} N:JO" R=60" P=3G" 5=72" H=42" U= 11-318" a= 48" v=23-3/B" Odd**Si~:e** Designator Odd size designator-. are anAJpha Numberic description.The ftrsltwo digits specifythe heights whole numherwilhan alpha des1g<lator speclf)>lng theheightfraction. The secondtwo**dig~s** tpedry the I'Ad!h whole numberwith an alpha designator

specifying !hewidth fraction. Andthe last alpha designatorspecifies !hedepll1. tfthe heightor I'Adth isless than 10 Inches, use a 0 Infront of
A=O" B" 1-1/16" c "1/8" D"' 3/16" E=114" F"'5/16" G"'J/8" H"'7/16" J" 1/2" K"'9/16" !he dimension L=518" M"'11/16" N "'J/4"
Gasket Material
-- Gasket Location**~~~~------~** p =13/16" Q=718" R=15/16" O=None O"'None 3= Slllcone Sponge 1 = Upstream 4 "'Woven Glass 2=Downstream 5"'Blu Jel 3 "'BothSides Faceguard Material 0 =None G =Aluminized**E~panded** Metal 5 "22 GA. SS**4~4** Mesh Faceguard Location o"'None 1=Upstream 2"'Downstream J "'BothSides 

## Guide Specifications 1.0 1.1
1.2 General Hightemperature separatorstyle HEPAfilters shall be Alpha HT models as manufactured by Flanders. Filtersizes, capacities and construction options shall be as scheduled on the drawings. 2.0 FilterConstruction 2.1 The filter pack shall be constructed by pleilting a continuous sheet of non-woven**water~resistant** fiberglass medi11 around hemmed-edge corrugated aluminum sepamtors. 2.2 The filter packshall be sealed into a (409 stainless steel) (304 stainless steel) frame with a high temperature silicone sealant rated for 5oo•F or aglass packsealant rated for 1,ooo•F in exhaust applications. 2.3 (A chlorastlc silicone gasket) (a woven glass gasket) shall be provided to sealthe filter in the mounting device (Gasket Seal). As!l!cone gel shall be provided in achannel on one side to seal the filter in the mounting device. filters with sillcone gel have a maximum service temperature of39o•F (Gel Se11l) 3,0 Performance 3.1 Initial and final resistances shall not exceed the scheduled valu.es. 3.2 Alpha HT HEPA Filters shall have a minimum efficiency of 99.97% on 0.30 rnicrometer particles when tested at rated capacity on aQ-107 l'enetrometerin accordance with IEST-RP-CC001.3, Type A. Each filter shall be challenged with an approved nearly monodispersed oil aerosol 

### of0.30 micrometer

### size. Measure 

### the upstream and downstream concentration ofthese particles with a light scattering photometer, determine the penetration and calculate the efficiency. 3.3 Alpha HT Scan Tested HEPA Filters shall have a minimum efficiency of99.99% on0.30micrometer particles when tested at rated capacity on aQ-107 Penetrometer in accordance with IEST-RP-CC-001.3, Type C. The scan test shall consist of challenging the filter with a high concentration of an approved oil aerosol or PSL Spheres. Utilizing aphotometeror particle counter, the mediap11ckand the pack-to-frame seal shall be scanned to insure that there are no leak greater than .01% ofthe upstream concentration 11! 100fpm face velocity. 

# Ffmull.u®

# ;=:;**~** REPRESENTED BY: Flanders Corporation, Inc. 531 Fl11nders Filters Ro11d Wiishington, NC 27889 Phone: (252) 946-8081 Fax: (252) 946-3425 Toll Free: (800) 637·2803 Website: www.flanders-ffi.com
PB1403-0408 (2}

### General C-3 and C-4 Side Access HEPA/ULPA Filter Housings are designedfor use with nominal 12 inch deep HEPA/ ULPA filters. They are factory-assembled flanged units suitable for gel sealed or gasket sealed HEPA filters. Both the prefilters and the primary HEPA/ULPA filters are serviceablethrough the same gasketed side access door. 

### Versatility C-3 and C-4 housings may be used with Alpha 95 filters (95% DOP efficiency) and with Alpha Cell and Alpha 2000 filters (99.97% and 99.99% DOP efficiency). Standard housings accept nominal 12 inch deep filters and 16" and 18" carbon adsorbers in a variety of face sizes. They can be arranged from one filter high and one filter wide to tour filters high and eight filters wide. If large housings are not practical to rig into place, smaller units may be stacked in the field. 

### Options • Choice of frame construction materials • Insulation • Lifting lugs 

### •Transitions • Static pressure ports • DOP test ports • High temperature modifications • Weathercap • Magnahelic gauges (mounted) • PrefilterTrack 

### ImportantFeatures
• Choice offrame**cor1~rrummn**



### Double pin hinges emabiEfttllil level contact whh the ga:sk\j•f formlytight seal 

### Construction Housings are 24 inches deep in the direction of air flow, (26 inches deep if it has a 4" prefilter section.) and are constructed in your choice offrame materials. Flanges are furnished for duct connections on the air entering and air leaving sides. All joints are intermittently welded and finished to remove all burrs and sharp edges. The joints are then sealed with silicone enablingthe housing towithstand an internal pressure of 

### +1- 3.0 ln. w.g. The filter locking mechanism lor the fluid gel sealmodel housing is a 300 Series stainless steel handoperated arm that moves the filter's gel-filled channel on to the internal housing knife edge sealing flange. The same mechanism also pulls the filter away from the sealing flange when changing filters. The filter locking mechanism for gasket seal-model housing Is a 300 Series stainless steel and brass device. The mechanism presses the gasketed filter against the housing's sealing surface by means of a mechanical bolt and thrust assembly that is manually operated using a standard 3/4 inch socket or wrench. Standard 2 Inch or 4 inch prefilter tracks will accommodate pleated panel filters with efficiency ranges up to 50% per the ASHRAE Standard 52.2 dust spot test methods. Access doors have 0.5 in. thick closed cell neoprene gaskets around the inside perimeter. Double pin door hinges which pivot, allow the door to make level contact with the gasket when closed. Stainless steel wing nuts secure the doors.

Flanders Corporation
- Foremost in Air Filtration Toll Free: 1-800-637-2803
PB1604-0408 (4)

### Cfm Capacities and Dimensions Using Standard Alpha 95 and Alpha Cell and High CapacityAlpha 2000 HEPA Filters Face Width Code Height Velocity 1W 2W 3W 

### 1 4W 

### sw 6W 7W 

### 1 BW Code (fpm) bFM,Caoacl 1H 500 1000 4000 6000 8000 iOOOO 12000 14000 16000 275 1100 2200 3300 4400 5500 6600 7700 8800 375 1500 3000 4500 6000 7500 9000 10500 12000 500 2000 4000 6000 8000 10000 12000 14000 16000 2H 500 4000

. 

### BODO 12000 16000 20000 24000 28000 32000 275 2000 4000 6000 8000 10000 12000 14000 1600 375 3000 6000 9000 12000 15000 18000 21000 24000 500 4000 8000 12000 16000 20000 24000 28000 32000 3H 500 6000 12000 18000 24000 30000 36000 42000 48000 275 3000 6000 9000 12000 15000 18000 21000 24000 375 4500 9000 i3500 18000 22500 27000 31500 36000 500 6000 12000 18000 24000 30000 36000 42000 48000 4H 500 8000 16000 24000 32000 40000 48000 56000 64000 275 4000 8000 12000 16000 20000 24000 28000 32000 375 6000 12000 18000 24000 30000 36000 42000 48000 500 8000 16000 24000 32000 40000 48000 56000 64000 1. Height and Width code: the first numeral represents the number of 24 in. x 24 in. filters high and wide. See

also Model Number Development on page 3. 2. Standard housing depth is 24 inches with orwithout an optional prefilter track. 3. Housings greater than four wide must have filter removal from both sides. 4. Capacities shown are based on nominal 12 inch deep filters. 

## C-3 

## Gasket Seal

Gasket
Aspring-loaded filter clamping mechanism is used to maintain**seal~**

ing pressure for gasketed filters. The gasket seal is suitable for many applications. 

## C-4 Gel Seal

Housing

Knife Edge Sealing Flange A flange in the housing mates into a gel-filled channel on the filter. The gel seal guarantees**filter~to~frame** sealing and is recommended for critical applications.

Flanders Corporation
- Foremost in Air Filtration Toll Free: 1-800-637-2803

## Model Number Development

Filter type: C3G
- Gasket Seal C4F
- Fluid Seal Housing SiZe: Filters High x Wide (See Chart) 

## C3G 

# T 1H1W GGF 

# T GLV**~** Housing Material: 

## 01

FilterSize: -------------------' CCF- 12"x12"x11-112" HEPA Filter GLV: Galvanized steel 304: Type 304 SIS 304L: Type 304 L SIS

316: Type 316 SIS 316L: Type 316L SIS ALZ
- 14 gauge aluminized (non-standard) 2CCF -12"x12"x11-112" HEPA filter with a 2" prefilter 4CCF -12"x12"x11-i12" HEPA filter with a 4" prefiler CGF- 12"x24"x1t-1/2" HEPA Filter 2CGF-12"x24"xtt-112" HEPA Filter with 2" prefilter 4CGF-12"x24"xtt-1/2" HEPA filter with a 4" prefilter GCF- 24"x12"x11-1/2" HEPA filter 2GCF- 24"xt2"x11-112" HEPA filter with 2" prefilter 4GCF-24"xt2"x1HI2" HEPA filter with 4" prefilter GGF- 24"x24"x1H/2" HEPA filter 2GGF-24"x24"x1 1-1/2" HEPA filter with 2" prefilter 4GGF-24"x24"x1 1-112" HEPAfitter with 4" prefilter CC12- 12"x12"xt1-112" carbon adsorber CG12- 12"x24"xt1-112" carbon adsorber GC12- 24"x12"xtt-1/2" carbon adsorber GG12-24"x24"xtH /2" carbon adsorber CG16-12"x24"xt6" carbon adsorber GCt6- 24"x12"x16" carbon adsorber GG16- 24"x24"xt6" carbon adsorber GGta- 24"x24"xta" carbon adsorber. DoorLocations Di R Filter access and housing on one side only DtA -Doors on both sides, but filter access from one side only. 02
- Doors on both sides and filter access from both sides. The filler size arrangements listed at left are the onlystandard arrangements. 6" prefilters are available but non-standard. Any prefilter with a carbon housing is available but not standard. Multi-wide CC, CG and GC units are available but non-standard. CC16, CC18, CG18 & GC18 units are not available.



### Filter Usage and Housing Weight Height Filters/ Width Code Code Weight tW 2W 3W 4W 5W 6W 7W 8W 1H Filters 1 2 3 4 5 6 7 8 Weight 105 190 270 380 460 540 2H Filters 2 4 6 8 10 12 14 16 Weight 200 305 460 610 765 920 3H Filters 3 6 9 12 15 18 21 24 Weight 255 405 590 810 995 1180 4H Filters 4 8 12 16 20 24 28 32
(1) Filters/Weight: Top number indicates the number of filters required to fill the unit. Bottom number indicates the

approximate weightrn pounds ofthe housing EMPTY. Add 32 poundsfor each HEPAIULPAfilterand 2 pounds pereach prefilter to determine approximate weight when loaded with filters. Add 10% to calculate the approximate rigging weight of housings

Flanders Corporation
- Foremost in Air Filtration Toll Free: 1-800-637-2803

### Construction Details

AIR**n..o~**

C4 SECTION Vlflt}l SIDE C4 SECTION VIEW1 TOP Notes: 1. Standard construction is 14 ga. galvanized steel housing and doors leak tight to**+I~** 3.0 in. w.g. 2. Maximum operating temperature for standard Cw3 and C-4 Housings is 250"F. High temperature C-3 and C-4 Housings

are available for 400"F continuous and 500 "F Intermittent duty.**-~---------** 

### Guide Specifications
1.0 HEPAIULPA FilterHousings 1.1 Side access HEPA filter housings shall be C-3 and C-4 as manufact\)red byFlanders. 1.2 Units shall be factory-assembled housings with flanges for duct connections on the air entering and airleaving sides. 

### 1.3 Housings shall be suitable for operation at

### +1- 3.0 in_ w.g. internal pressure_ 2.

### 0 Construction 

### 2.1 Housings shall 

### be made of galvanized or stainless steel with 11 ga. corner posts_ Jointsshall be intermittentlywelded and sealed with silicone. 

### 2.2 Tracks lor prelilters shall be fabricated from the same material as the housing_ 2.3 The filter locking mechanism for the gel seal model shall be a 300 Series stainless steel hand# FfmulfM®;~ Flanders Corporation, Inc. 531 Flanders Filters Road Washington, NC 27889 Phone: (252) 946-8081 Fax: (252) 946-3425 Toll Free: (800) 637-2803 Website:**www.flanders~ffi.com**

PB1604-0408 (4) operated arm that moves the filter so its gel-filled channel mateswiththeinternal housing knife edge sealing flange. The same mechanism shall also pull the filter away from the sealing flange when changing filters

### 2.4 The filter locking mechanism for the gasket seal model housing shall be 

### a 300 Series stainless steel and brass device. The mechanism shall press the gasketed filter againstthe housing's sealing surface bymeansofamechanical boltand thrust assemblythatis manually operated using a standard 

### 314 inch socket or wrench. 

### 3.0 Features 

### 3.1 Model numbers and capacities shall be as specified and/or shown on the drawings. 

### 3.2 Provide options as specified.

# Proposal 

# By Robinson Fans Inc.

400 Robinson Drive, PO Box 1

### DO Zelienople PA 16063 

### Phone: 724-452-7075 

### Fax: (724) 452-0388Quote Number: 26109 Rev: 0 Ref#: Incineratorfans Customer: Amec FosterWheeler

Quote To: Amec Foster Wheeler Blake D. Beckstrom 801 382-6911 Prepared by: Kevin Sciullo 400 Robinson Drive, PO Box 100 Zelienople PA 16063 Phone: 724-452-7075 

### Fax: (724) 452-0388 Email: kevin.sciullo@robinsonfans.com 

# auqti:l
Date: 9/10/2015 Expires: 10/10/2015 Sales Representative: J.B. Industrial Inc. blake.beckstrom@amecfw.com 10876 S River Front Parkway Suite 250 Phone: 801-943-0719 

### Fax: 801-944-2414 Email: brandon@jbi2.com South Jordan UT 84095



### Line Part Number**[j~sct-Jption** 

### 1 FRO FD FAN- VFD (CASE 1)
Diameter Tip Width Fan Type Arrangement Class 31.0000 in 6.3750 in FRO 8 IV Fan Weight WR' Casing Mtl Wheel Mtl

2492 lbs 1491b-ft2 304

## ss 316L SS Speed Flow FSP Inlet Pr. Condition RE'M ACFM inWC inWC DESIGN 1780 15,000 7.50 .00 TURNDOWN 1380 15,000 3.50 .00 Accessories Included Flanged Inlet Flanged Outlet Split Casing Casing Drain Shaft Guard Coupling Guard Evase By Others Quantity 1.00
Rotation DWDI/SWSI Design Temp Discharge

CW SWSI 400"F 360 Shaft Mtl 316L SS Density



# = .0476 .0476 Motor I Brng Base Mtl Inlet Box Pas A-36 Temp Elevation Power



### :E FASL !lliE 375 0 24.00 375 0 12.60 Inspection Door(RAISED) Shaft Seal (Std.) SP-2/3 Clean-Std. High Temp (Red) Primer

### Rf'l~\'!Oach $36,660.00Optional Eguipmentoffered: (Not included in basefan price) 

### lliml COUPLING MOTOR DETECTOR DETECTOR

Notes: Description Falk T10 Steelfiex coupling (max. bore 2.75")(391b). 30HP, 1800RPM, TEFC, FRAME 286T, 460/3/60, 558LB, MODS FORVFD Two (1 per brg) T-TEC #1060 100 ohm Pt RTD's, monitor by others. One IMI- 685BOOOOA11 (RFI STD Switch) Electronic vibration switch, internaiiCP® accelerometer, 0-1.5 in/sec, 85-245 Vac power, 50/60 Hz, Triac, 5A, 0-45 sec (AC), 4 to 20 rnA output signal, standard enclosure, CE & GSA approvals, Class 1, Div. 2, Group A,B,C & D, NEMA4X enclosure, ambient temp range22 Deg. F. to 158 Deg. Fwith internal reset pushbutton w/remote option, analog vibration signal on screw terminals, dual Y,? NPT conduit hubs.; Monitor by others 

### $564.00 Ea.Fan 

### $2,324.00 Ea.Fan



### $796.00 Ea.Fan 

### $1,085.00 Ea.Fan

1. Robinson will supply electronic manuals. Hard copies are available upon request for an additional charge. 2. Due to the current volatile raw material situation, we reserve the right to re-evaluate the price and delivery of our equipment atthe time oforder placement. 3. Robinson recommends that a drive train torsional analysis is performed by others. 4. Evase required to meet stated Performance. (Supplied by others) 5. If requested Certified Material Reports will be collected and retained for all components ofthe rotating assembly (wheel and shaft assembly) and for all plate and sheet material in the static components ofthe fan assembly. 6. This fan is designed and fabricated to Robinson Fans standard practices and procedures; no other specification was taken in to account. Please review the quoted equipmentto ensure that it meets your requirements. 7. A VFD is required for cold start up with motor offered. VFD by others. 8. Lead time forthe fan equipment is based on Robinson standards, delivery ofthe fan equipmentwill be based on the longest lead time on the optional equipment. Enclosed: Terms and Conditions ofsale, Shipment: Approximately 9TO 11 weeks after drawing approval Drawings: Submitted for approval 3 TO 4 weeks ARO or sooner if possible

Orders in access of$50,000 progress payment shall be required. 10% Upon Order, 20% Submittal of Dwgs, 35% Start of Fabrication, 35% Upon Shipment. Pending credit approval atthe time oforder placement. All payments are netthirty days. Points of possible manufacture- Zelienople, PA; Salt Lake City, UT; Lakeland, FL orAbilene, TX (final manufacturing location will be based on ship to location, and shop loading attime of manufacture) All freight, fees, taxes, insurance & export packaging shall be paid & provided for by the customer. Terms: NET 30 Pending credit approval attime of order Shipping Term: FCA Factory placement.



### /o Very truly yours, Robinson Fans, Inc.

Kevin SciulloFan: 31 in x 6.375 in SWSI FRO 

### For: AMEC FOSTERWHEELER Quote# 

### 26109-0-1 Density: 0.0476 lbsfftA3 Temperature: 375 °F 

### Fan Speed: 1780 

### rpm 9/1012015 13:46 

### User: ks

10.0 

# I r=:t:- 

# L
-:**~**

# F 60.0



### 9.0

3.0

# ~- : .

# ~· • • i f '

.........

# '-..~·. -- 

### 50.0

# ~

# r.=='---1----'---

___, _____

# =r:::**~es_~~~..:t1' (infH~GJ** 

__ . ____._ . '

- . __ . __ .- __ .{_.Q 

# t**------~--·-·----** 

### 7.0

### ~- "' •

## ~ 40.0 b**~** 

# "'**~** 

### 6.0 J_ :;;**~** _L___ !**~ ~**  I 0 

### .:2 ------' ,--; 

# -+ -r· - a. 

## o; 

# s.o Jo.o


# - (f)



### ..... 4 0**~** 

### . '

. . . . . . .**~-** 

### . l.l.. 

# iii

# F·-~ 

# .**-~** 

# .**~ -~~** **,----~--** 

# '\**_;_~=------==--j-==------=---l** 1il
3:0 

# ;di**--~-~~~;zV?Jt?ff=~'i;Ft=** 

# .**~----t** zo.o 

# -r--- . 2.0

# P======+=~==+======~=====t===+=====:xt==**~------**

- --**-;---~-· ---·-·-;~-**  

### 10.0 1.0

. --+ 1

__ ;... __ _**-~!**

### __ 

### _,.WJilijie_1;-D

___121) '-"---'---

. . :-1500 

### 0.0 0.0 0 5000 10000 15000 20000 25000 30000 35000 InletVolume (ACFM) Robinson Fans, Inc. SE =1, EF =1, inlet Ps = 

### 0 in-H20Fan: 31 in x 6.375 in SWSI FRO 

### For: AMEC FOSTERWHEELER Quote# 26109-0-1 Density: 0.0476 lbs/ftA3 Temperature: 375 'F Fan Speed: 1380 rpm 

### 9110/2015 13:51 User: l<:s



### 6.0**~---------:--,--~--,---~**

# ---~---- 25.0 

## I I 

# 1--r 

# -?:ts'

--- ----+ zo.o 

# '"""" I

## ~ .



# - - I ,. 

# i

I

### -~--+--r--+-1--' 

# . X

. 

## 1---- 

# .**~** 

# ='- -1

# ~~ssm=-;**~"ll_=H20)J** _ 

# -------+ 15.0

## -~~--+-~--~~-,-1**-~-** 

# . ' 

# t**P~~j_i_~P)** 

# I**~** 

### -**~--_ ~2.6** 

# y~ . .

# ±=5 ' 

### 10.0

### ~ 

# I I 

# 't=/•**~~·** 

# . 

# 3**~** 1 , ! • . . \ 

### r-- ----, 

# j?i

_ I

1 \ 

# l --fS!l :7

. • • \

. 

## _'1\: 

# I**~~--**olume--1-(ACI'-M)-rs: 

# I 

# I I , _ ___jSO.OO**0~** 

### 0.0 0 5000 10000 15000 20000 25000
Robinson Fans, Inc. InletVolume (ACFM) SE =1, EF =1, inlet Ps 

### =0 in-H20**~** 

# "' ;: 0 

### "- 

# - " " .E !:: 

### ro 

# ""

# Robinson

Sound Output Data Customer: Quote Number: Width: Fan Type: Blades: AMEC FOSTER WHEELER 26109-0-1 SWSI FRO 12 Near Field Approximately 3 Ft Date: FO Number: CFM: Diameter: Static Pressure: RPM: 10-Sep-15 15000 31 In 7.5 In 

### H20 1780
Sound Power level ratings shown are decibels referred to 10-12 Watt and obtained in accordance with AMCA Standard 300. Related air performance ratings per AMCA Standard 210. PWL for each band and DBA are calculated perAMCA Standard 301. Levels shown do not include motor or other auxiliary equipment. Operating conditions otherthan the above stated values can result in significantly different sound levels. Data is for use by a system acoustical design engineer for evaluation of the fan singularity and within a system. Because ofthe infinite variations in system arrangements and the manyfactors which affect sound pressure levels, it is the designers responsibility to properly apply this data based on his knowledge ofthe system. Some guidelines for use ofthis data are for "Near Field" computer data to apply to dueled inlet and outlet installations, any opening in the duct must be a minimum of 100 feet remote the fan. Openings within this range are assumed to emit a sound pressure equal to the sound power level. This also applies to untreated inlet and outlet expansion joints. Note thatfor dueled inlet/outlet the ductwork thickness and density must equal that of the fan housing to achieve the sound levels noted. Near Field- A Hemispherical space where sound pressure waves from one radiating surface tend to interfere with waves generated by othersurfaces. Near Field boundry, distance from radiating surface, is related to the wavelength ofthe lowestfrequency and overall size ofsource. Free Field- Area beyond near field, with no obstructions, where sound pressure levels decay 6 dB for each doubling ofdistancefrom nearfield. 

### Band No. Mid Freq "'Levels Shown do not include motor orother auxiliary equipment*" 

### 1 2 3 4 56 

### 7 8 63 125 250 500 1000 2000 4000 8000 Sound Power Levels at Acoustic Center of Fan PWL+/-2dB 102 101 98 93 89 85 79 

### 77 DBA

96 For Dueled Inlet and Outlet Installation Estimated sound pressure level for nearfield with 0.25 Inch casing loss SPL+/-2dB 89 83 

### 77 70 62 56 46 41 73 Estimated Sound pressure level at 3 Feet beyond nearfield ofcasing SPL+/-2dB 83 

### 77 71 64 56 50 40 35 67

Sound Pressure Levels are approximate based upon nearfield calculations.D



### c

B

A 6 5 4**~** 8323/32

4i 3/16 28 5/16 1/8 GAP BETWEEN 

### -1-- COUPLING HUBS AND SHAFTS 3

# -~
i:i 2

i 24 1!8**~~** r--INSIDo " 

### i

DRIVE SIDE CLOCKWISE ROTATION

Reference Drawing #26109-0-1-1 For Fan Flange Drillings OVERALL ENVELOPE: 69ht. x 67w. 31" FRO, Arr.#8, CW@0, Cl. #4, SWSI THIS DRAWING IS THE PROPERTY OF ROBINSON FANS AND IS LOANED UPON CONDITION THAT IT IS NOTTO BE REPRODUCED OR COPIED IN WHOLE OR PART FOR COJlPUl'll! ClNlRJ.TlD DlU.JTNC. DO NIJT CHANCE BTIIAND

FURNISHING INFORMATIONTO OTHERS FOR ANY PURPOSE DETRIMENTALTO OUR INTERESTSAND WILL BE RETURNED UPON REQUEST.
5 4 3 2 D



### c

B

A

# Robinson

Proposal By Robinson Fans Inc.

400 Robinson Drive, PO Box 100 Zelienople PA 16063 Phone: 724-452-7075 Fax: (724) 452-0388

# Robinson
Quote Number: 26109 Rev: 0 Ref#: Incineratorfans Customer: Amec FosterWheeler Prepared 

### by: Kevin Sciullo 400 Robinson Drive, PO Box 100 Zelienople PA 16063 

### Phone: 724-452-7075 

### Fax: (724) 452-0388 Email: kevin.sciullo@robinsonfans.com 

# [_ · ·. Quote >, 

# I**.--~----~-** ________**__jL_~-.:cr'"'-"'--"--"--"'-"--"j__------------** --- Quote To: Amec Foster Wheeler Blake D. Beckstrom 801 382-6911 blake.beckstrom@amecfw.com 10876 S River Frant Parkway Suite 250 South Jordan UT 84095

pne Part Number**Pes_~rj_ptio_n** 

### 2 FRD FD FAN- VFD (CASE 2)
Diameter Tip Width Fan Type Arrangement Class 48.0000 in 9.8750 in FRO 8 IV Fan Weight WR' Casing Mtl Wheel MU

50391bs 1207 lb-ft2 304 

### ss 316L SS Speed Flow FSP Inlet Pr. Condition RPM 1\QEM inWC inWC DESIGN 1180 40,000 7.50 .00 TRUNDOWN 945 40,000 3.50 .00 Accessories Included Flanged Inlet Flanged Outlet Split Casing Casing Drain Shaft Guard Coupling Guard Evase By Others Date: 9/10/2015 Expires: 10/10/2015 Sales Representative: J.B. Industrial Inc. Phone: 801-943-0719 Fax: 801-944-2414 Email: brandon@jbi2.com

···. ' · Quantity ··· 

# .... 1.00
Rotation DWDI/SWSl Design Temp Discharge



### cw Shaft Mtl 316L SS Density

l__blff .0476 .0476 SWSI 400"F 360 Motor I Brng Base Mtl Inlet Box Pas A-36 Temp Elevation Power

:E Ei\S.L BHP 375 0 64.00 375 0 37.00 Inspection Door (RAISED) Shaft Seal (Std.) SP-2/3 Clean-Std. High Temp (Red) Primer Price

# Each $47,929.00Optional Equipment offered: (Not included in base fan price) 

### lllim COUPLING MOTOR DETECTOR DETECTOR

Notes: Description Falk T10 Steelflex coupling (max. bore 3.5")(931b). 75HP, 1200RPM, TEFC, FRAME 405T, 460/3/60, 1440LB, MODS FORVFD Two (1 per brg) T-TEC #1060 100 ohm Pt RTD's, monitor by others. One IMI
- 685BOOOOA11 (RFI STD Switch) Electronic vibration switch, internaiiCP®accelerometer, 0-1.5 in/sec, 85-245 Vac power, 50/60 Hz, Triac, SA, 0-45 sec (AC), 4 to 20 mA output signal, standard enclosure, CE & GSA approvals, Class 1, Div. 2, Group A,B,C & D, NEMA 4X enclosure, ambient temp range22 Deg. F. to 158 Deg. Fwith internal reset pushbutton w/remote option, analog vibration signal on screw terminals, dual%? NPT conduit hubs.; Monitor by others Price Per $1,072.00 Ea.Fan $5,316.00 Ea.Fan

$796.00 Ea.Fan $1,085.00 Ea.Fan

1. Robinson will supply electronic manuals. Hard copies are available upon request for an additional charge. 2. Due to the current volatile raw material situation, we reserve the right to re-evaluate the price and delivery of our equipment at the time of order placement. 3. Robinson recommends that a drive train torsional analysis is performed by others. 4. Evase required to meet stated Performance. (Supplied by others) 5. If requested Certified Material Reports will be collected and retained for all components ofthe rotating assembly (wheel and shaft assembly) and for all plate and sheet material in the static components ofthe fan assembly. 6. This fan is designed and fabricated to Robinson Fans standard practices and procedures; no other specification was taken in to account. Please review the quoted equipment to ensure that it meets your requirements. 7. A VFD is required for cold start up with motor offered. VFD by others. 8. Lead time for the fan equipment is based on Robinson standards, delivery ofthe fan equipment will be based on the longest lead time on the optional equipment. Enclosed: Terms and Conditions ofsale, Shipment: Approximately 9TO 11 weeks after drawing approval Drawings: Submitted for approval 3 TO 4 weeks ARO orsooner if possible

Orders in access of$50,000 progress payment shall be required. 10% Upon Order, 20% Submittal of Dwgs, 35% Start of Fabrication, 35% Upon Shipment. Pending credit approval at the time of order placement. All payments are netthirty days. Points of possible manufacture- Zelienople, PA; Salt Lake City, UT; Lakeland, FL orAbilene, TX (final manufacturing location will be based on ship to location, and shop loading at time of manufacture) All freight, fees, taxes, insurance & export packaging shall be paid & provided for by the customer. Terms: NET 30 Pending credit approval attime of order Shipping Term: FCA Factory placement.



### !o Very truly yours, Robinson Fans, Inc.

Kevin SciulloFan: 48 in x 9.875 in 

### SWSI FRO 

### For: AMEC FOSTERWHEELER 

### Quote# 26109-0-2 Density: 

### 0.0476 lbsfftA3 Temperature: 375 'F Fan Speed: 1180 rpm 9/10/2015 14:13 

### User: ks



# " b ::1 

# "' w 

# "**~** 

### "- 

# "'**~** 

# - (!) <:: 

# "' u.. 12.0 ..--------------,---,.....-,--,.--- 140.0



### 100.0 

## ' ' ' -. 1---- ---. -.I I. 

# I' ' 

# '"·' , . - ,T, r' ,

# c _,

# ~ I i!'T

. • . -'--- _, i

# _i_~ .- - - ' i

# ~ .'

. '

# --~----== '- ,--. I-- I

# ~ ' 

# a.o . ' I ' , .. 

# t : : '

. .

# ~. - . •, -=*.

. 

# j 

# ,- ·= - ' . ' ''"'

...-· ' c ' '

# ~ . 

### 8,0

. ' ,- ' -, I ' : ! 

### o;'-.ressure} -(lin-H20\-
- -, 

### I ' ' ' ' I

. ' "'-' ' 

## l

# ~ I · , ·' ! 

# "<.

# ~-- I 

## ' ;: ' I ·, 

# 'c· • - . T'

. 

## 'T ' ' I !
-- 

# .'>' ' ' +

4·0 1 '

# ~-**~** .• 

### .l. • i '..,...:. ! 

### IPowe_Co..A·,

_

# ~ -L 

# + 1



## i ,··' ' 

## ,,;--1 I ! 

## ! / '

. , ... - 

## C ·;

# ,·~ ";: -1 /. :• ; i

# [~-+_- -1- "' 

# '·'

# --~- . 

# ' 

# '\ ' • • ' I 

# '+- L .,.,., '

__j

__ , • 

# '\r-- .------ ' I 

# t -r------ 40.0

' -1---+ 

# =t=

_ -1\: --. · I I -. I
- ----1 

### 120.0

80.0

# ~ 60.0

# I~**!--v~ ~+:_e;~J** 

# .**-~**

- 

# I**-~** !

# ~---;-----1- 0 

### 10000 20000 30000 

### 40000 50000 60000 70000
Robinson Fans, Inc. InletVolume (ACFM) SE =1, EF =1, inlet Ps = 

### 0 in-H20 b 

# '" :;:: 0 

### a 

# " "' u..

### Fan: 48 in x 9.875 in SWSI FRO 

### For: AMEC FOSTERWHEELER Quote

### # 

### 26109-0-2 Density: 

### 0.0476 lbs/f!A3 Temperature: 375 °F 

### Fan Speed: 945 rpm 

### 9/10/2015 14:15



### 7.0

•

• ' 

## 6.0 I 

# 0 

# "' 

# -..... 

# - -r- :I: 

### 5.0 

### ' <::: 

# "'**~** ! 

### I -:·--·**~:~i~--** ' 

### -- ! I 

# " "' 

# "' "' b 

### 4.0 i ll. 

# " . :;::; 

# "' ' 

# - rn 

# "' 3.0 

# "' "- ! '

' I ! ' I ! I ! I ' ' ! ! ; ' '**~** 

### 2.0

i 

### / i 

## A""
I i ' 

### /: ' '**~** i 

### 1.0 

# ......-r**~!** ' ! I ! i I 

### 0.0 0 

### 10000 20000
Robinson Fans, Inc. 

### User: ks

i I 

### 10iHJ

I I

' i ;

- 

### 90.0

·--·-+----.---,
__------ 

### - 

### 80.0

- 

## --......

# '"'**·~___;__** 

# . r-----· i ------;------ 

### 1'>.. ' 70.0 

# "' 60.0 

# '**----~-----** ··-



### '\ Pres5ur<j-1-iin**-H20)-~--- ~~------**  i ' ' i '**·~-·- ~~-----~** **~~------**

. ' '\ I ! • t
.<I """

. . 

### --- 

### '\

. 

### 50.0 

# ai I 

### '\ ' 

### 40.0 i 

### '\

. 

# --**~-** 

# ..,.- 30.0

. 

### '\

; 

### \**--~** 

### \

'

## -~ 

# :w.o 1\ ' 

### \ 10.0 Volume t (**_Cj~l)** 

### 4.0.00.0 '
' 

### 30000 40000 

### 50000 60000 !LO 

### 70000 InletVolume (ACFM) SE =1, EF =1, inlet Ps = 

### 0 in-H20 b 

# "' ::: 0 ll. 0. 

### .E 

# "' ru "-

# Robinson

Sound Output Data Customer: Quote Number: Width: Fan Type: Blades: AMEC FOSTER WHEELER 26109-0-2 SWSI FRO 12 Near Field Approximately 3 Ft Date: FO Number: CFM: Diameter: Static Pressure: RPM: 1 0-Sep-15 40000 481n 7.51n H20 1180
Sound Power level ratings shown are decibels referred to 10-12 Watt and obtained in accordance with AMCA Standard 300. Related air performance ratings per AMCA Standard 210. PWL for each band and DBA are calculated per AMCA Standard 301. Levels shown do not include motor or other auxiliary equipment. Operating conditions otherthan the above stated values can result in significantly different sound levels. Data is for use by a system acoustical design engineer for evaluation of the fan singularity and within a system. Because ofthe infinite variations in system arrangements and the many factors which affect sound pressure levels, it is the designers responsibility to properly apply this data based on his knowledge ofthe system. Some guidelines for use ofthis data are for "Near Field" computer data to apply to dueled inlet and outlet installations, any opening in the duct must be a minimum of 100 feet remote the fan. Openings within this range are assumed to emit a sound pressure equal to the sound power level. This also applies to untreated inlet and outlet expansion joints. Note that for dueled inlet/outlet the ductwork thickness and density must equal that ofthe fan housing to achieve the sound levels noted. Near Field- A Hemispherical space where sound pressure waves from one radiating surface tend to interfere with waves generated by other surfaces. Near Field boundry, distance from radiating surface, is related to the wavelength ofthe lowestfrequency and overall size ofsource. Free Field- Area beyond near field, with no obstructions, where sound pressure levels decay 6 dB for each doubling ofdistance from nearfield. Band No. Mid Freq "*Levels Shown do not include motoror otherauxiliary equipment*** 

### 1 2 3 4 56 

### 7 8 63 125 250 500 1 000 2000 4000 8000 Sound Power Levels at Acoustic Centerof Fan PWL+/-2dB 106 105 102 97 93 89 83 81 DBA

100 For Dueled Inlet and Outlet Installation Estimated sound pressure levelfor nearfield with 0.25 Inch casing loss SPL+/-2dB 93 87 81 74 66 60 50 45 78 Estimated Sound pressure level at 3 Feet beyond nearfield ofcasing SPL+/-2dB 87 81 75 68 60 54 44 39 72



### Sound Pressure Levels are approximate based upon nearfield calculations.D



### c

B

A 

# "' "''" zr _w o2**~"'**

0 

## ! 6 5 4

' 

### r----- 1111/8--·----------··· 118--···-----------· 

## ' 1 3/1G GAP**BETWEEI\1~** -...--- COUPLING HUBS AND SHAFTS 3

37 1i4

### ~ - iNSIDE

Reference Drawing #261 09-0-2-1 For 2

7/8

DRIVE SIDE CLOCKWISE ROTATION

OVERALL ENVELOPE: 96ht. x 101w. Fan Flange Drillings TYPE 48" FRO, Arr.#8, CW@ 0, IBP@0, Cl.#4, SWSI TOLERANCES UNLESS OTHERVvlSE MARKED THIS DRAWING IS THE PROPERTY OF ROBINSON FANS CQJtPUTER ClNlRArED DRAJJliC. DO NOT CIHNCE BYmNIJ FOR FRACTIONS±1/32",ANGLES±1',DEC.±.005" AND IS LOANED UPON CONDITION THAT IT IS NOTTO 

### AMEC_FOSTER_WHEELER BE REPRODUCED ORCOPIED IN WHOLE OR PART FOR FAB TOLERANCE ON OVERALL DIMENSIONS FURNISHING INFORMATION TO OTHERS FORANY UNDER 54"DIA FAN±1/8" PURPOSE DETRIMENTALTO OUR 54"DIA. FAN &ABOVE +3/16"/-1/8" INTERESTS AND WILL BE RETURNED UPON REQUEST. 2 DRAWN 9/10/2015 

### Proposal Drawing #26109-0-2 ,y DATE ALL DIMENSIONSARE IN INCHES RPA 1 OF SHEET 6 5 4 3 2 D



### c

B

A

# Robh1son

RHFANS COMMENTSCLARIFICATION: (C)= COMPLY (NC) = NOTCOMPLY (COMM) = COMMENT (NA) = NOTAPPLICABLE (B/0)= SUPPLIEDBYOTHERS (OPT)= OPTIONALLY QUOTED (CHANGE) =CHANGEDBYSPEC, SEE COMMENT ON REFERENCING DOC. (DELETE) = DELETEITEM, ORPARTLINED OUT OF SPECIFICATTON.



# Comment: • Allspecificationand documentsreferenced inyourrequestfor quote, butnot suppliedtoRFI aretaken complete exceptionto.

400 Robinson Drive, 

### P.O. Box 

### 100 Zelienople, 

### PA 

### i 6063-0i00 p 

### (724) 452-6121 F (724) 452-0388 !SO 9001 Certified Quality Management System

### <'bn,li

## 1111**mlll':'\¥:-.\\\..~**

# StandardBalanceandVibration Statement

The fan wheel and shaft assembly willbe balancedto Grade G2.5, perANSI S2.19-1989 (ASA 86-1989). HDB 10/10/95

Theassembled fan will 

### have operatingvibration levels nottoexceed0.15 in./sec., measuredoneach bearing housing, in all three axis, filtered to 

### I x RPM. This assumesthatthe fan is properlymaintained and installed on an adequate foundation.

400 Robinson Drive, P.O. Box 100 Zelienople, PA 16063-0100 p (724) 452-6121 F (724) 452-0388 ISO 9001 Certified Quality Management System

# amec foster wheeler

ATTACHMENT 3 PHOTOGRAPHS OF VEOLIA INCINERATORS

# amec foster wheeler



# ATTACHMENT 4 COST ESTIMATE SPREADSHEETDate: 9/11/2015 Amec Foster Wheeler Project# 186-140054-02 Veolia ES, TWI, Sauget, IL HEPA Filter Study 

### INSTALLED COST ESTIMATE

Equipment Name Description Quantity



## - Incinerator2 Flanders, Model Alpha HT #0-011-H-03-03-5E HEPA Filters 32-00-GG-F with 304 55 Frame., 4 x 4 module, 2 8'H x8' W, with 16totalfilters per module. {1 bankoperating, 1 bankspare)

HEPA Filter Housings Flanders, Model #C3g-4hw-2GGF-304-D2, 304 SS, with service access doors on both sides.
Robinson Fans, Forced Draft Fan with VFD, motor, coupling, resistance detectors, vibration switch,flanged inletand outlet, split Booster Fan casing, casin"g drain, shaftseal, inspection 1 door, shaftguard, andcouplingguard. 31" diameter, FRD type, 400 F, 24 BHP, 30 HP motor, 304SS casing, 316SS wheel and shaft

.

Incinerator3 Flanders, Model Alpha HT #0-011-H-03-03-5EHEPA Filters 32-00-GG-F with 30455 Frame.,4 x 4 module, 2 8'H x8'W, with 16totalfilters permodule. {1 bankoperating, 1bankspare)

HEPA FilterHousings Flanders, Model#C3g-4hw-2GGF-304-D2, 304 SS, with service access doors on both sides. Robinson Fans, Forced Draft Fan with VFD, motor, coupling, resistance detectors, vibration switch,flanged inletand outlet, split BoosterFan casing, casingdrain, shaftseal, inspection 1 door, shaftguard, and couplingguard. 31" diameter, FRD type, 400 F, 24 BHP, 30 HP motor, 304SS casing, 316SS wheel and shaft Bare Equipment Installation Installed

Cost,$ Factor Cost,$

$52,875 4.5 $475,875

included with filters

$41,429 4 $165,716



### ------------ TOTAL COST $641,591

$52,875 4.5 $475,875

included with filters

$41,429 4 $165,716



### ------------ TOTAL COST $641,591Incinerator4 Flanders, Model Alpha HT#0-0ll-H-03-03-5EHEPA Filters 32-00-GG-F with 304 55 Frame.,4 x 4 module, 4 $52,875 4.5 $951,750 8'H x8'W, with 16total filters per module. (3 bankS operating, 1 bank spare)

HEPA Filter Housings Flanders, Model#C3g-4hw-2GGF-304-D2, 304 included 55, with service access doors on both sides. with filters



# ---- Robinson Fans, Forced Draft Fan with VFD, motor, coupling, resistance detectors, vibration switch, flanged inlet and outlet, split BoosterFan casing, casing drain, shaft seal, inspection 1 $56,198 4 $224,792 door, shaftguard, and coupling guard. 48" diameterFRD type, 400 F, 64BHP, 75 HP motor, 30455 casing, 316 55 wheel and shaft



### ------------ TOTAL COST $1,176,542

Total Installed Costfor $2,459,724 all 3 Incinerators:



### OPERATING COST ESTIMATE
CostofReplacing a single HEPA filter is $1,187/each

NumberofFilters replaced

### Iyear Cost of filters/yr, $ Incinerator2 16 $18,992 Incinerator 3 16 $18,992 Incinerator4 48 $56,976



### ----------- Total costforfilters

### I yr. $94,960 Assumingthe plantoperates7884hours peryear Costofelectricity is estimatedtobe $0.08/kw-hr Costof Fan kW-hr/yr. Electricity, $/yr Incinerator 2 189,216 $15,137 Incinerator3 189,216 $15,137 Incinerator4 504,576 $40,366



### --------- Total costforelectricityforfans 

### Iyr. $70,641

# amec foster wheeler



# ATTACHMENT 5 RESUMES Blake D. Beckstrom, PE Don R. 

## Leavitt, PECitizen: U.S.A. Education: • BSChE, Magna Cum

Laude, University of Utah, SLC, UT, June 1979 Qualifications: • Licensed Professional

Engineer-Chemical (Utah) Memberships/Affiliations: • AIChE Member • IT3/HWI PAC Member • AWMA Member Languages: • English 

## Career Summary Blake D. Beckstrom, P.E. 

# Project Manager/Sr. Process Engineer

Blake is a professional chemical engineer with over 35 years of experience in all areas of process design for a wide variety of chemical plants. Areas ofexpertise includewaste incineration,**flue~** gas cleaning, waste watertreatment, coal gasification,**coal~** and**oil~** fired electric plants, environmental audits and assessments, and feasibility and economic studies. He is alsoexperienced in projectand technical group management, permitting, operator training, plant**start~up,** and operations. He regularly attends and chairs sessions at technical thermal waste treatment conferences, and is a member ofthe Program Advisory Committeeforthe InternationalConference onThermal TreatmentTechnologies and Hazardous Waste Incineration. 

# Professional Experience Senior Process Engineer 

### I Project Manager
• FosterWheeler USA, Salt Lake City, Utah (2011 -present) Process Engineering (process feasibility and economic studies, mass and energy balance calculations, PFD and P&ID preparation, equipment and instrumentation sizing, specifications, and recommendations). Project Management (managed multi-discipline engineering and design team to meet scope, schedule, and budget). Technical support of marketing and bid/proposal preparation. Representative Waste Incineration Projects (Client 

### I Rotary Kiln Size 

### I Start-up Year)

• Clean Harbors
- Permit Support and Basic Design for new commercial hazardous waste incinerator- 4.4m diax 12m -In EPC Phase

o Volcano Partners
- Preliminary Project Scoping for remediating contaminated waterways with cement additive production plant • Stericycle- Permit support for new Medical Waste Incinerator

o Veolia Environmental- Basic Engineeringand Option Studyfor new HazardousWaste Incinerator Other Representative Projects

• Cripple Creek &Victor Gold
- Process design and water study for new valley leach facility • Repsol- Basic Engineering and Design ofSulfur Recovery Unit (SRU), Tail Gas Treatment Unit (TGTU), and Amine Regeneration Unit (ARU). • Sinclair Oil Wyoming- HAZOP Review of Debottlenecking/Expansion Project • Petrobras Basic Engineering and Design Package for new Sulphur Recovery Plant • Nusett Industries Debottlenecking/Expansion of Ethylene Glycol Recycling Facility • US Magnesium- Process design for new Spray Dryer Facility.

September 15 Page 1 of4

### Blake D. Beckstrom, P.E. Staff Process Engineer 

### Professional Experience (Cont'd)

• REDD Engineering and Construction, Inc., Salt Lake City, Utah (2009- 2011) PHA Compliance Support and Engineering for new diesel refining plant Forland Refining- PHA Support, Pressure Relief Study and Recommendations 

### Engineering 

### I Research Manager
• UPRI, Inc., Salt Lake City, Utah (1994- 2009) Responsible charge of research to develop patents for and demonstrate processes at ultra-high pressure and temperature. Design, construct and operate high pressure diamond optics laboratory. Prepare reports. Specify, evaluate quotes, and recommend purchase of equipment and supplies.


### AssistantVice President, Engineering
• Ford, Bacon & Davis, Inc., (FB&D) Salt Lake City, Utah (1979- 1994) Assist in obtaining corporate licenses in states requiring registration. Responsible charge of engineering projects in registered states. 

### Manager, Incineration Technology Group
• Ford, Bacon and Davis, Inc. (FB&D), Salt Lake City, Utah Transfer hazardous waste incineration and gas cleaning technology and know-how from parent company (Deutsche-BabcockAnlagen, DBA) to FB&D. Reviewand overseethe process designofall incineration projects. Ensure that DBA technology is properly applied to all incineration projects. Support marketing department through technical presentations to prospective clients, evaluate requests for bids, prepare proposals, etc. Assist in development ofcorporate business plans. Write and present technical papers and chair sessions at international thermal treatment conferences.


### Lead Process Engineer
• Ford, Bacon & Davis, Inc., (FB&D) Salt Lake City, Utah Supervise, review and check the process design of various projects including several hazardous waste incinerationfacilities, coal gasification process developmentunit, oil shale productionfacility, oil and gas production facility, etc. Work included project seeping studies, heat and material balance calculations, processflow diagrams (PFDs), piping and instrumentdiagrams (P&IDs), equipmentdata sheets and specifications, selection of equipment, hazards analysis, feasibility and economic evaluations/studies. Operator training, start-up and supervision of initial operation ofwaste incineration plants. Expert witness at contested hearings for siting of hazardous waste incineration plant. Preparation of permitting documents.

September 15 Page 2 of4

### Blake D. Beckstrom, P.E. Staff Process Engineer 

### Professional Experience (Cont'd) Project Manager
• Ford, Bacon & Davis, Inc., (FB&D) Salt Lake City, Utah Managed hazardouswaste incineration projectsfrom feasibility scoping studythrough detailed design, procurement, construction, operator training, and initial operations. Responsibilities included 

### coordination ofthe design effort betweenthe client, FB&D engineering staff, and othercontractorswho were responsible forother areas atthe site; preparation of reportsto clients, maintaining projectwithin 

### budget and schedule. Managed several process feasibility study and economic evaluation projects. Representative Waste Incineration Projects (Client I 

### Rotary Kiln Size I 

### Start-up Year) • Ciba-Geigy Corporation, St Gabriel, LA- 3.6m dia x 12m -1993 • Ciba-Geigy Corporation, Mcintosh, AL- 3.6m dia x 12m
- 1993 • Southdown Environmental Systems, Mount Pleasant, TN- Existing Cement Kiln- 1993 • Chem-Security, Ltd., Swan Hills, Alberta, Canada- 4.4m dia x 12m -1993 • APTUS, Tooele County, UT- 4.4m dia x 12m- 1991 • Ross Environmental Services, Grafton, OH
-- 4.4m dia x 12m- 1991 • E.I. duPontde Nemours, Sabine RiverWorks, Orage, TX- 4.4m dia x 12m -1991 • APTUS, Coffeyville, KS- Modifications- 1990 • Rollins Environmental, Deer Park, TX- 4.4m dia x 12m - 1988 • Rollins Environmental, Deer Park, TX- 3.3m dia x 20m (Rotaty Reactor)
- 1988 • Rollins Environmental, Deer Park, TX- 3.6m dia x 1Om- 1988 • Pyrochem, Inc., Coffeyville, KS- 3.6m dia x 1Om- 1986 • Rollins Environmental, Deer Park, TX- 3.6m dia x 1Om (Replacement)- 1986 • AT&TINassau Recycle Corp., Gaston, SC- 2.2m dia x 21m (Pyrolsis) -1984 • Rollins Environmental, Deer Park, TX- 3.3m dia x 20m- Permit Not Received • BFIICecos International, Louisville, KY- 4.4m dia x 12m- Permit Not Received • E.I. du Pont de Nemours, Chamber Works, Deepwater, NJ
- 4.4m dia x 12m
- Permit Not Received • GAF, Lindon, NJ- 4.4m dia x 12m- Permit Not Received • Rhone-Poulenc, Confidential- 4.4m dia x 12m- Permit Not Received • Mobay, Baytown, TX- 3.6m dia x 1Om -Permit Not Received • Rollins Environmental, Baton Rouge, LA- 4.4m diax 12m (Plus Rotary Kiln Reactor)- Permit Not Received • American Envirotech, Inc., Housotn, TX- 4.4m dia x 12m (2 Units)- Permit Not Received 

### Undergraduate Research Assistant- Senior Project
• University of Utah, Advanced Combustion Engineering Research Center, SLC, UT (1978- 1979) Designed and constructed a coal suspension furnace and its gas control system.

September 15 Page 3 of4

### Blake D. Beckstrom, P.E. Staff Process Engineer 

### Professional Experience (Cont'd) Sample of ProjectTypes Representative Projects

m Hazardous Waste Incineration • Gas Cleaning Systems (Wetand Dry) • Waste WaterTreatment Facilities • Entrained-flow Coal Gasification PDU • Oil and Gas Production Facility • Solid Rocket Propellant Manufacturing SourWater Stripper • Uranium Mill Tailing Site Environmental Audits and Assessments • Coal- and Oil-fired Power Plants • Oil Refineries • Oil Shale Processing Plant • Soda Ash Dissolving Facility • Low-level Waste Heat Recovery Facility • Refinery De-Bottlenecking Projects • Ultra-High Pressure Optical Laboratory Design and Operation • Tar Sands Processing Plant • Sulfur Recovery and Tail GasTreating Units

September 15 Page 4 of4Citizen: USA Education: • Chemical Engineering, B.S.

and M.S., Brigham Young University • Chemical Engineering,

Ph.D., University of Utah Qualifications: Licensed Professional Engineer- Utah, Colorado, Michigan, Nevada, Texas, Washington Memberships/Affiliations: • AICHE, IT3 PAC Member Languages: • English 

## Career Summary 

# Don 

# R. Leavitt, Ph. D., P.E. Senior Staff Process Engineer
Don has over35 years ofchemical process engineering experience in hazardous waste incineration, sulfur recovery, petrochemical operations, flue gas scrubbing, pollution control, reactor design, air dispersion modeling, oil shale recovery and coal combustionj gasification, and minerals processing. Forthe past 26 years he has been involved in various projects covering the design of hazardous waste incineration facilities and air pollution control systems, sulfur recovery units, distillation, stripper tower and FCC modelingj petrochemical operations, plant wide flare system evaluations, wastewater treating and leaching operations, and mineral and metal extraction operations. He regularly attends and chairs sessions at technical thermal waste treatment conferences, is a member ofthe Program Advisory Committee for the International Conference on Thermal TreatmentTechnologies, and received their annual service award. 

# Professional Experience SeniorStaff Process Engineer Performed evaluation ofcomplex hazardouswastefeed streams and associated listed constituentsto characterizethe elemental feed composition and resulting incineration requirements and associated flue-gas characterization for a proposed hazardous waste incinerator. Performed evaluation of medical waste incineratorfeed streams to characterize the elemental feed composition and subsequently perform heat and material balance calculations relative to a new 

### medical waste incinerator. Developed incineration operating parameters and performed heatand material balance calculations and associated air pollution control proposal and heat and material balance calculations for a proposed river sedimenttreatmentfacility. Set up and performed process simulations ofthe incineration and gas cleaning trains using HYSYS and steady-state thermodynamics modelling spreadsheets developed by the applicant. Developed a comprehensive basicengineering package to design a newincineratorand associated air pollution control equipmentto increase throughput capacity and meetthe MACT regulations. Performed processengineering in design phaseengineering, including PFD and P&ID development, as well as involvement in HAZOP review. Performed preliminary design, detailed design, purchasing and technical construction support for modification ofexisting secondarycombustion chamberto tie into a 3.6 meter replacement slagging rotary kiln. Performed process engineeringforthe design ofan afterburnerchamberand interface between the kiln and afterburner chamber. Conductedstudiesforwastewater heavy metals removal system design,waste heat boilerdesign and incineratortechnology/applicability. Performed process engineering for preliminaryand design phase ofa rotary kiln incineratorwithwaste feed storage and handling, afterburner and gas cleaning system. Performed process engineer for the process design of a flash furnace off-gas APC system and associated blowdown solids recovery system. Performed process engineeringto evaluateand sizethe proposed gas cleaning andwater blowdown September 15 Page1of7Don 

### R. Leavitt, Ph, D., P.E. Senior Staff Process Engineer 

# Senior Staff Process Engineer (Cont'dl equipment for a flash furnace off-gas back-up scrubber. Performed consultant engineering services for the evaluation of and to recommend modifications to the secondary combustion chamberto improvethe waste destruction efficiencyofthe unit. Performed process modeling and evaluation of an incineration off-gas reheater for trouble shooting plugging problems. Performed heat and material balance reviews for the gas cleaning system and water recirculation circuits associated with the hazardous waste incinerator. Developed a plant-specific comprehensive plant heat and material balance model for incineration, heat recovery, and gas cleaning. Conducted feasibility studies, conceptual design, preliminary engineering, permit support, cost estimating, detailed design, purchasing, start-upand commissioning foratotal incinerationfacilityfor destruction of a wide variety of hazardous wastes. Performed conceptual design, preliminarydesign, permitsupport, detailed design, purchasing, startup, and commissioning of a total incineration facility for destruction of a wide variety of hazardous wastes. Performed conceptual design, preliminarydesign, RCRA PartsA and Bpermitapplication preparation and public relations supportfor atotal grass roots incinerationfacilityfor destruction ofsolids, liquids, sludges, containers and a variety of hazardous wastes. Performed process evaluation tasks including review and evaluation of current operation, updating material and energy balances, evaluating majorequipment operation relative to particulate and D/F formation, recommending revisions in equipment, operating procedures and conditions. • Conducted process evaluation and budgetary cost estimate for WESP alternatives to upgrade the facility's air pollution control to meetthe MACT emission standards. Conducted studyto identify and evaluate the mosteconomicallyfeasible alternativesto upgradethe facility's air pollution control to meetthe MACT omission standards. Assisted in identification and evaluation ofalternativesforparticulate removal. Developed airpollution control PFD and utility requirements for treatment of off-gas from a proposed plasma melter hazardous waste treatment facility. Conducted the process design fora 160 MMBTU/HR hazardous waste incineration facility, including equipment sizing and cost estimation. Developed PFDs and P&IDs of the facility and associated heat and material balances for a wet scrubberair pollution controls upgrade. Conducted emission and equipment evaluations, sizing per upgrade requirements, and made recommendations. Conducted process engineering study to determine the source water in the off-gas line and to recommend a solution to eliminate the accumulated water. Conducted the process simulation, prepared the PFDs, and performed equipment sizing of major equipment in the design ofa new industrial waste feed boiler and steam turbine power generation facility based on mixed hazardous waste liquids and auxiliary fuels. Conducted process engineering study and budgetary cost estimate to convert the existing off-gas handling system to meet state and federal dioxin emission limits. Performed process engineering for finalizing the Material and Energy Balance, P&ID detailed engineering, and equipment size verification for a chlorine off-gas scrubbing system. Conducted preliminary process calculations for evaluating the required incineratorsize. Conducted process identification and scoping for definition ofthe project scope. Conducted technology evaluation/screening and facility design to provide an air pollution control system for NOx removal. Conducted technologyevaluation/screening and urea injection facility design to provide a system to decrease calciner outlet gas NOx levels to meet current state regulations. Conducted technology evaluation/screening, heat and material balance and cost analysis for nickel and cobalt nitrate September 15 Page 2 of7Don R. Leavitt, Ph. D., P.E. Senior Staff Process Engineer 

# SeniorStaff Process Engineer (Cont'dl conversion processes. Performed heat and material evaluations and associated process equipment evaluations for a particulate scrubbing system to meet new state air emission regulations. Developed heatand material balance, accompanying PFDs and P&IDs, and performed evaluationof the proposed off-gas scrubbing system and associated sizing ofequipment, dueling and piping. Also developed heatand material balances, accompanying PFDs and P&IDs and performed evaluation and sizing ofthe associated equipment, dueling and piping in each ofthose areas. Conducted evaluation of existing overland slurry transport pipeline relative to proposed new design rates. Assisted in process design and calculation review ofthe column flotation operations, and also assisted in development of P&IDs for column flotation operations. Conducted the heat and material balance evaluation to support proposed demonstration test runs. Assisted in equipmentdesign and preparation ofequipmentdata sheets, instrumentdata sheets, and evaluation for process improvements to achieve required sulfur removal performancefor anew Claus sulfur recovery unit. Performed boiler feed water evaluation. Conducted process simulation ofClaus unit, upgrading of PFDs as well as P&IDs, and performed sizing and specification ofnew equipment. Examined HYSYS simulation for the HDS1 to determine if logicfor modeling the hydrotreater reactors was sufficiently well-founded
- especially regarding sulfur. Developed the operator manual for the incinerator and waste heat boiler for a new sulfur plant installation. Performed Claus plant simulations to evaluate sulfur recovery efficiency relative to feed stream modifications and catalysttype. Performed burner modeling and heat and material balance evaluations of an existing Claus plant sulfur burner. Offered recommendations for modifications based on the evaluations. Responsible for process design ofthe amine (MDEA) unit, including process simulation forthe heat and material balance, equipment, line sizing, specifications, and relief valve sizing. Responsible for design of a liquid-liquid distributor in an amine propane contactor unit as part of an integrated sulfur recovery plant. Also performed verification simulations and equipment rating/ evaluations to develop equipment replacement recommendations forthe refinery propane recovery units- includingthe olefin splitter, depropanizer, knockoutvessels, associated shell and tube andfinfan heat exchangers, and liquid products pumps. Responsible for performing verification/update simulations and equipment rating/evaluations to develop recommendations forthe refinery's No. 2 HDS stripper loop. Also assisted in evaluation of the proposed process to scrub SRU tail gas using caustic solution. Responsiblefor modeling and evaluating the amine contacting circuits, aswell asdevelopmentofthe PFDs and P&ID for the amine units. Responsible for major equipment and line sizing in the new amine regenerator area. Conceptualtodetail design and engineeringforsulfurunitexpansionwithtail gastreating, and amine unit. Process lead to develop heat and material balances, accompanying PFDs and P&IDs and perform evaluation and sizing ofthe associated equipment, dueling and piping for facility expansions in the brine preparation, solvent extraction, spray drying, and magnesium casting areas. Consulting engineering services to evaluate and recommend changes to the recommended performance ofthe product dryer. Designed a coal partial oxidation reactor. Also determined associated processflow conditions, line and equipment sizing and specification, process control and start-up/shut down procedures. Performed process development and cost study for a mine water treatment facility. Conducted process identification, evaluation, and economicfeasibility studiesfor afacilityto destroythiosulfates September 15 Page 3 of7Don R. Leavitt, Ph. D., P.E. Senior Staff Process Engineer 

# SeniorStaff Process Engineer (Cont'dl and ammonia in an industrial wastewater discharge. Process engineering to conduct the plant heat and material balances for SRU and TGTU areas, developing the PFDs and coordinating the development of P&IDs, equipmentdata sheet packages, and other process deliverables related to the SRU and TGTU areas. Process engineer to conduct a general walk-through visual inspection of the client's product manufacturing facility and control room, aswell as reviewing process procedures and process-related drawings and control screens, developing aprocess safetyaudit study, and writing an auditsummary and recommendation report. Process engineerfor line sizing, confirming the process capacity sizing basis, coordinating the sizing ofsafety reliefvalves, and the developmentofassociated data sheetpackages, aswell as conducting some ofthatwork personally. Process engineering for developing a set of preliminary P&IDs for the ER plant to be used as the basis for producing a budgetary solvent recovery plant cost estimate. Responsiblefor reviewing PFDs and P&IDs and checking process equipmentsizing calculations and other miscellaneous calculations. Developed HYSYS simulations for various wet gas compressor options. PFDs were developed to representthe two-stage and single-stagewet gascompressorscenarios. Heatand material balance tables for the three cases were also prepared to summarize the HYSYS simulations. The heat and material balances for the three caseswere used as the basisto evaluatethe existing equipmentand to size the new equipment. Responsibletoevaluate and make recommendations regarding existing safety reliefvalves relativeto possible refinery throughput increases. Lead Process Engineer responsibleforconducting an evaluation and providing recommendations and budgetarycostestimatesfor line-over-pressure protection andventdischargeon various unprotected lines within the plant. Performed process evaluations of hydrotreating. Responsible for performing heat exchanger ratings, evaluations and sizing in an evaluation studyto determine required equipment modifications associated with a proposed increased lean oil recirculation flowto improve C3 hydrocarbons recovery at the Salt Lake City BP Refinery. Conducted the process design and cost estimation for a proposed facility to receive, store, mix and ship asphalt. Responsible for developing the process flow/piping and instrumentation diagram. Process engineeringto developthe conceptual process design basis, PFDs, and associated material balance for treating high grade ore via comminution, gravity separation, floatation, tails handling, concentrate oxidation, and cyanidation. KUCC 300M3SuperCell- Process engineeringtosizethe associated piping and slurry launders, as well as to develop P&IDs, for two experimental novel flotation cells. Carbon Column Train E - Process Engineer for reviewing and finalizing the process design and P&IDs for a duplication expansion ofthe ADR area at a gold processing facility. METSIM Modeling
- Process modelling of Copper Concentrator using the METSIM simulation software. Feed and Gas Cleaning- Finalizing the presentation ofthe Process Flow Diagramforthe feed and gas cleaning sections ofa proposed waste-to-energyfacility using gasification and plasma treatment. OCP-EI Halassa &Ouled Fares Phosphate Ore Beneficiation- Process engineeringto help develop PFDsfor afacility expansion and upgrade, as well asto review materialflow philosophyand material balance data. OCP Phosphate Product Plant- Process engineering to help develop PFDs for a facility expansion and upgrade. IPSC Ash System -Process evaluation ofthe Boiler Feed Water/Ash Slurry System to identify the primary causes for presentwater flow restrictions. The results were formalized in a report. September 15 Page4of7Don R. Leavitt, Ph. D., P£ Senior Staff Process Engineer 

# Senior Staff Process Engineer (Cont'dl Conducted evaluation of existing overland slurry transport pipeline relative to proposed new design rates. Assisted in process design and calculation reviewofthe column flotation operations, aswell as assisted in development of P&IDs for column flotation operations. Process engineering for ademonstration coal retorting unit- including heat and material balancefor the gas/condensate system, as well as equipment and line sizing. Process engineering supportto verify pump and line sizing forthe primary hotbrine circulation circuit, design ofan associated brine pH control system, and evaluation ofthe sizing ofthe by-pass lines and associated control valves. Representative Projects 

## • • • • • 

## • • • 

## • • •
0 

## • • • 

## • 

# • • 

# • • 

# • • • 

# • • 

# • • 

# • •
0 

## • September 15 Veolia North America- Chicago, IL Volcano Partners LLC- NewYork, NY Clean Harbors New Hazardous Waste Incineration and Gas Cleaning Facility- El Dorado, AR Dow Chemical Company- Midland, Ml Rollins Environmental Services- Logan, NJ Rhone-Poulenc ISHA Facility Tsinghua Tongfang Co., Ltd.- Beijing, China Waste-Tech Services U.S. P.C.I- Clive, UT BFI/CECOS International
- Louisville, KY Onyx Environmental Services
- Port Arthur, TX Earth Tech, Inc. Swan Hills Treatment Centre- Swan Hills, CA SYNGENTA Corp Protection, Inc. -St. Gabriel, LA NOV ARTIS Corp Protection, Inc.- St. Gabriel, LA FosterWheeler Environmental Corporation
- Langhorne, PA ENSCO
- El Dorado, AR Westinghouse Electric Company Western Zirconium Plant- Ogden, UT Ciba-Geigy- Mcintosh, AL Ciba-Geigy- St. Gabriel, LA Confidential Client for Liquid Waste Incinerator and Waste Heat Boiler- TX ASARCO Incorporated
- Hayden, AZ Kennecott Utah Copper Corporation
- Magna, UT Emery Energy- Salt Lake City, UT U.S. Magnesium
- Rowley, UT AutolivASP, Inc.- Promontory, UT Pharmacia and Upjohn Company- Kalamazoo, Ml Questar- Salt Lake City, UT Engelhard- Salt Lake City, UT Interstate Brick- WestJordan, UT MagCorp- Rowley, UT Petrobras- Petroleo Brasileiro S.A., Maranhoao, Brazil Page 5 of7

### Don R. 

### Leavitt, Ph. D., P.E. Senior Staff Process Engineer 

# Senior Staff Process Engineer (Cont'd)
• International Petroleum Investment Company, Fujairah, United Arab Emirates • Amoco Oil Company Refinery- North Salt Lake City, UT • BP Amoco Oil Company Refinery- North Salt Lake City, UT • Precision Systems Engineering- Sandy, UT

e American Gilsonite- Bonanza, UT 

### • Polyus Gold, JSC Matrosova Gold Mine- Magadan, Russia • Western Zirconium (Westinghouse)
- Ogden, UT • BP Oil Castellon Refinery- Castellon, Spain • Sinclair Oil Corporation Sinclair Refinery- Sinclair, WY • Repsol
- Bilbao, Spain • Repsol
- Cartagena, Spain • ConocoPhillips- Sweeny, TX • Coastal Eagle Point Company- Westville, NJ • Sinclair Casper Refinery- Evansville, WY • CEPOC -Westville, NJ • Cenex Harvest States COOP
- Laurel, MT • Tesoro Refining and Marketing Company- Salt Lake City, UT • Williams Energy- Opal, WY • Phillips Petroleum -Woods Cross, UT • Xcel Energy Planergy International
- Richmond, CA • Jack B. Parsons Asphalt Terminal
- Ogden, UT • Clean Fuels -Salt Lake City, UT • Cripple Creek 

### &Victor Gold Mining Company-Victor, CO • FLSmidth Dorr-Oiiver Eimco Inc.- Copperton, UT • Cripple Creek & 

### Victor Gold Mining Co.- Victor, CO • FLSmidth GEntry- Sandy, UT • S4 Energy Solutions- Chambers Co., Texas • Groupe OCP- Khouribga, Morocco • FLSmidth Dorr-Oiiver Eimco Inc.- Khouribga Mine, Morocco • Intermountain Power Service Corporation- Delta, UT • Millennium Synfuels- Salt Lake City, UT • PacifiCorp Blundell Geothermal Underflow Unit- Blundell, UT • American Gilsonite
- Bonanza, UT • U.S. Magnesium
- Rowley, UT • Char Fuels Association, Ltd.
- Englewood, CO • Tessenderlo Kerley Waste WaterThiosulfate Treatment Facility- Pasadena, TX

September 15 Page 6 of7Don R. Leavitt, Ph. D., P.E. Senior Staff Process Engineer 

# Senior Staff Process Engineer (Cont'd)

Lead Process Engineer Lead Process Engineerforthe basicand detailed design for an industrialwastewatertreatingfacility, including integrated facility material balance, equipment design, specification, PFD, and P&ID development. Lead Process Engineer in the developmentofa comprehensive basic engineering packageto design a new incineratorand associated air pollution control equipmentto increasethroughput capacity and meetthe MACT regulations. Lead Process Engineer in design phase engineering including PFD and P&ID development, aswell as HAZOPS review. Lead Process Engineer in preliminary design, detailed design, purchasing and technical construction supportfor modification ofexisting secondarycombustion chamberto tie into a3.6 meter replacement slagging rotary kiln. Lead Process Engineerforthe design of an afterburnerchamberand interface between the kiln and afterburner chamber. Process Engineer responsibleforwastewater heavy metals removal system design,waste heat boiler design and incinerator technology/applicability study. Lead Process Engineerfor preliminaryengineering and design phase ofa rotary kiln incineratorwith waste feed storage and handling, afterburner and gas cleaning system. Lead Process Engineerfor conductingthe processdesign ofaflash furnace off-gasAPC system and associated blowdown solids recovery system. Lead Process Engineer responsible to evaluate and size the proposed gas cleaning and water blowdown equipment for a flash furnace off-gas back-up scrubber. Lead process engineer to evaluate and design an acid leaching reactor and the associated flare system to handlethe resulting hydrogen and hydrocarbon off-gases. Also evaluated existing calcining operation ofassociated gas cleaning system relativeto increasingthe system capacityand eliminating other equipment deficiencies. Lead Process Engineerforscheduling sulfur plantdesignand costestimate. Responsibleforprocess design oftheamine unit- including processsimulation, equipmentand line sizing, safetyreliefsystem and flare design as well as overseeing the process engineering in the other areas. Lead Process Engineerto convertthe refineryflare and blowdown modeling softwareto an upgraded platform, simulate relieving conditions and evaluate the size of the relief valves, update tracking protection matrices, update maintenance reliefvalvefolders and evaluatethe capacityofthe refinery flares relative to the updated information. Lead Process Engineer responsible for developing an FCC unit model and refinery unit model with crudeandvacuum columnsto evaluate and recommend process improvements in an existingfacility meeting state air quality requirements. Lead Process Engineer responsible for conducting process evaluation, design, and calculations for mitigating heptane vapor releasesto the atmospherevia a system to recoverthe heptanevaporsfor improved in-plantenergy utilization in existing gas-fired boilers. Lead Process Engineer for the pre-feasibility and feasibility design of new Russian gold ore processing mill. Responsible for material balance calculations, development of PFDs and P&IDs, equipmentand line sizing, process specificationsfor equipmentand miscellaneous process and cost studies relative to the integrated operations of ore crushing/grinding/milling, gravity separation, flotation, thickening and sedimentation, leaching, stripping, electrowinning, carbon regeneration, and various support operations.

September 15 Page 7of 7