### .'

General Review
1. Modeled onlyWichitamountains. Caneycreek 599 KM away. UpperBuffalo 446 KM away. Hercules 558 KM.

. 2. Modeled a S02 value that is 30 times the permit allowable, this maybe apermit issue? 3. Didnot model anyofthe insignificantunits.

### ·.'

Koch BART Sources



### . PI t 

### P . nmary**R~** 

### EUG2 A

### mmoma an e ormers Location EUID PointJD Heatlnput* Manufacturer Construction Date Ammonia Plant 101Bl ·1 

### Kellogg 1973 #1 Ammonia Plant 101B2 2-9097 TJ' 

### 1975 #2**~~** 

### *Heat mput IS 

### based on a 12-month rollmg average penod and mcludes arch burners, tunnel burners, superheat burners, and auxiliary boilerburners.
NO, VOC Point Emission CO PM 10 S02 ID Unit TP TPY TPY TPY TPY Ih/hr I Ib/hr Ib/hr 112.4 492.1 2-9095 10lBl 10.2 44.5 3.5 717.1 7.4 32.2 0.8 181.9 2-9097 0.8 3.6 734.3 7.5 33.0 115.1 101B2 10.4 45.6 503.9 186.3 TOTALS 90.1 1 7.1 368.2 1451.4 14.9 65.2 227.5 996.0 20.6


### EUG3 Boilers/Heaters>50 

### MMBTUH Location EUID PointID EUNamelModel HeatInput Manufacturer Construction Date Ammonia Plant #1 2202UB 3-9099 Ammonia Unit StartupBoiler 144MMBTUH Zurn Industries 1975

Point ID Emission Unit PM 10 S02 NOx VOC CO Ib/hr 

## I TPY Ib/hr 

### I TPY Ib/hr 

## I TPY Ib/hr 

### I TPY lb/hr 

### I TPY 3-9099 2202UB 1.6 

## I 3.5 0.1 

### 1 0.2 28.8 

### 1 63.0 

### 1.21 2.6 17.8 

### I 39.0


### EUG4 Boilers/Heaters

### < 50 

### MMBTUH Location EUID Point ID HeatInput Manufacturer Construction Date Ammonia Plant #1 102Bl 4-9102 33MMBTUH Kellogg 1973 Ammonia Plant #2 102B2 4-9103 Ammonia Unit Startup HeaterNo. 2 33 MMBTUH Kellogg 1975

Point Emission PM 10 S02 NO, VOC CO

ID Unit Ib/hr ! TPY Ib/br TPY Ib/hr TPY Ib/hr TPY Ib/hr TPY 3-9102 102Bl 0.4 1.6 0.03 0.1 4.9 21.3 0.3 

### 1.2 4.1 17.9 3-9103 102B2 0.4 1.6 0.03 0.1 4.9 21.3 0.3 1.2 4.1 17.9 TOTALS 0.8 3.2 0.06 0.2 9.8 42.6 0.6 1.2 8.1 35.8


### EUG9 Location PointID EU NamelModel Construction Date UAN Plant 9-9117 UAN Wastewater Concentrator 1968/1990 

## * 

## *This unit was originally constructed in 1968 and relocated to Enid in 1990 from Kennewick, Washington. 

## ** no calculated emissions

# co S . EUGI0 2 

### tnppmg Towers Location EUID Point ID EU NamefModel Manufacturer Construction Date Ammonia Plant#1 1102E1 10-9120 CO2 Stripping Tower 1(PIC30-1) Kellogg 1973 Ammonia Plant #2 1102E2 10-9121 CO2 Stripping Tower 2 (PIC30-2) Kellogg 1975

Point ID Emission Unit CO Ib/hr TPY 10-9120 

### CO2 StrippingTower 1 5.8 25.4 10-9121 

### CO2 StrippingTower 2 5.8 25.4 TOTALS 11.6 50.8
EUGll Nitric Acid Plant EUID Point ID Manufacturer Capacity (as 100% HN03) ConstructionDate M221 12-9115 Weatherly 118 TPD 1968/1990

## * * This unit was originally constructed in 1968 and relocated to Enid in 1990 from Kennewick, Washington.

Point ID Emission Unit NOx lh/hr I TPY 12-9115 Nitric Acid Plant 5.0 

## I 21.9
EUG12 AmmoniumNitrate Plant EUID Point ID Manufacturer Capacity (as 75.5% AN) Construction Date T311 12-9116 Weatherly 176 TPD 1968/1990

## * * This unitwas constructed in a different location and relocated to Enid in 1990.

'PointID Emission Unit PM10 CO lh/hr I TPY lh/hr I TPY 12-9116 VAN Plant 2.6 I 11.0 0.1 I 0.5
EUG15 Startup, IShutdown Vents Location EUID PointID EUName Date Ammonia Plant #2 308E 15-9109 Process Condensate Stripper 1980 Ammonia Plant #1 SP73-1 15.-9151 Startup/Shutdown Vent 1 1973 Ammonia Plant#1 SP74-1 15-9152 Startup/Shutdown Vent 2 1973 Ammonia Plant #1 SP75-1**15~9153** Startup/Shutdown Vent 3 1973 Ammonia Plant #2 SP73-2 15-9154 Startup/Shutdown Vent 1 1975 Ammonia Plant #2 SP74-2 15-9155 Startup/Shutdown Vent 2 1975 Ammonia Plant #2 SP75-2**15.~9156** Startup/Shutdown Vent 3 1975 Ammonia Plant #1 1102E1**15.~9120** CO2 Stripping Tower 1 1973 Ammonia Plant #2 1102E2**15~9121** CO2 Stripping Tower 2 1975 Construction

### PointID Emission Unit CO lb/hr TPY Methanol lb/hr TPY* 15-9151

.Ammonia Plant 1 SU/SD Vent No.1 10,962.8 345.3



## -­ -­ 15-9154 AmmoniaPlant 2 SU/SD Vent No.1 10,962.8 345.3



## -­ 15-9120 CO2 

### StrippingTower 1(PIC30-1)



## -­ -­ 35.8 0.6 15-9121 CO2 

### StrippingTower 2 (PIC30-2)


### -­ 

## -­ 35.8 0.6 15-9109 Process Condensate Stripper

## ~- 131.9 k. 

### TOTALS 90.6 203.5 3.6

EUG17 InsignificantActivities
Descri tion 460-hp Emergency generator 140-hp Fire waterpum Glycol dehydration reboiler 475-hp Portable mixer engine * APP-Portable Unit APP Portable 10-34-0 Processin Unit* Diesel Gasoline UANTANKS LIME D202

*Equipment owned, operated, and maintained bya contractor. Estimates ofemissions from the emergency generator and the fire waterpump are based on 500 hours ofoperations per year, with emission factors from Table 3.3-1 ofAP-42 (10/96).

Emission Unit 

### 460-hp Generator 140-h Fire 

### Pump Ihr TPY 

### NO. VOC 

# co lb/hr TPY Lb/hr TPY lb/hr TPY 

### 0.9 0.2 14.3 3.6 1.2 0.3 3.1 

### 0.8 0.3 0.1 4.3 1.1 0.4 0.1 0.9 0.2 

### Emissions estimates from the portable fertilizer mixing unit, which is owned, operated, and maintained by a contractor, are based on 350 hours/year anticipated operation and manufacturer's data.
Emission PMJ() 

### S02 

### NOx 

### VOC CO I Unit lb/hr TPY Iblhr TPY Ib/hr TPY Ib/hr TPY lb/hr TPY I Portable 475­ 0.3 0.1 0.2 0.03 

### 8.6 1.5 0.3 1.7 0.3 

## i

hp Engine

### B. Emission Rates Review/Approval
EU Point ID NOx PM IO S02 PPH Approved PPH Approved PPH Approved lOlBl 2-9095 181.9 I 10.2 I 26.3 2 101B2 2-9097 186.3 I 10.4 I 26.5 2 2202UB 3-9099 28.8 I 1.6 1 0.1 I

102Bl 3-9102 4.9 I 0.4 I 0.03 I 102B2 3-9103 4.9 I 0.4 I 0.03 I NAP 12-9115 5.0 I


### -­ -­ -­ -­ UAN 12-9116 

## -­ - 2.6 I


### -­ -­ Insigni.ficant Activities not modeled 3 3 3

.. 1 - used maXImum I-hr emISSIOn rate as calculated m eXIstmg permIt memorandum 2 - used a value 30 times that stated in thepermit 3 - unit not modeled