# Development of Chemical Precipitation Purchased Equipment

Costs:

Chemical Feed Systems

Purchased Equipment Costs are the sum of the following cost elements:

(1) Pump Costs

(2) Tank Costs

(3) Chemical Feed System Costs

(4) Mixer Costs

(5) Clarifier Costs

(6) Filter Press Costs

(7) Sand Filter Costs

Each cost component includes the cost of freight and associated ancillary equipment such as piping, valves, and

controllers.

This tele phone contact report support s EPA’ s development of cost element (3 ) by providing purchase cost s and

information regarding chemical feed systems used in the Steam Electric cost model.Project No.: 0172. 08 .02 9 .0 4 4 DISTRIBUTION

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Project Name: Steam /Cost/Compliance Modeling

TELEPHONE CALL RECORD

Outgoing Call Date: 04 /05 / 2011 Time: 1 :00 pm EST

Company Name: EnPro Technologies Contact Name: Troy Litherland

Phone No : (816 ) 350

- 5223

Email: tlitherland@enpro

- tech.com

Name: Kavya Kasturi ERG

GENERAL SUBJECT: Vendor cost request for chemical feed systems for a chemical precipitation wastewater treatment system.

TOPICS DISCUSSED AND ACTION TAKEN

On April 5 , 20 1 1 at 1 :00 p m I contacted EnPro Technologies to obtain costs for chemical feed systems needed

for chemical precipitation wastewater treatment systems for FGD wastewater . I was directed to Mr. Troy

Litherland. I explained to Mr. Litherland that we are working on conceptual level costing of a chemical

precipitation wastewater treatment system to treat FGD (flue gas desulfurization) wastewater fr om steam

electric power plants

, and a s a part of this project we are trying to collect cost information on different

components or units of a chem ical precipitation system . I discussed the types of chemicals we expected would

be added to the treatment systems.

Mr. Litherland stated that the approximate cost of a liquid feed point would be $15,000 per feed point. This cost

includes the peristaltic p ump, controls, typical accessories , and an additional pump for redundancy . For ferric

chloride, a feed point could add up to 50 gallons/hour. For polymer, the feed point could add up to 20

gallons/min of polymer solution which contains 0.5% nea t polymer. O rganosulfide is expected to be similar to

polymer for the feed point. For acid, double containment piping would be used. Mr. Litherland stated the liquid

feed systems require a 0.5 hp motor.

For lime feed, a hydrate lime silo with volumetric feeder would cost approximately $350,000. The silo volume

is 2,000 cubic feet.

Mr. Litherland stated that a liquid feed system weighed no more than 500 lbs and its dimensions are

approximately 3’x3’x5’. Mr. Litherland estimated freight costs assuming shipment from Kan sas City to the

Northeast. For liquid feed systems, he estimated freight costs to be under $300. For bulk feed systems, the

freight cost depends on the size of the silo. For silos under 12’, a regular truck can be used for shipment and the

estimated cost i s approximately $10,000. For larger silos, the cost is approximately $30,000.

Mr. Litherland stated that liquid chemicals could be stored in 55 gallon drums, 275 gallon totes, or in bulk

storage tanks. Dry chemicals could be stored in 50 lb bags, 2,000 lb bulk bags, or storage silos. He stated that

plants typically operate 14

- 30 days of storage a nd for non

- critical operations, a 15 day supply is reasonable. The

storage duration may also depend on proximity to the chemical supplier

.Project No.: 0172.08.029.044 DISTRIBUTION

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Project Name: Steam/Cost/Compliance Modeling

TELEPHONE CALL RECORD

Outgoing Call Date: 04/20/2011 Time: 4:50 pm EST

Company Name: EnPro Technologies Contact Name: Troy Litherland

Phone No : (816) 350

- 5223

Email: tlitherland@enpro

- tech.com

Name: Kavya Kasturi ERG

GENERAL SUBJECT: Vendor cost request for chemical feed systems for a chemical precipitation wastewater treatment system.

TOPICS DISCUSSED AND ACTION TAKEN

On April 20, 2011 at 4:50 pm I contacted Mr. Troy Litherland to follow up on our previous call.

I asked Mr. Litherland about chemical storage tanks. He stated that tanks were a separate cost and range from

$8,000 to $20,000. He said chemical feed rates w ould be required for better estimates. He also stated that totes

could hook up directly to the pump.

Mr. Litherland provided additional information on the lime feed system. The system includes a silo, volumetric

feeder, mix tank, control system and 2 slur ry pumps (40

- 60 gpm). The second pump is included for redundancy.

Mr. Litherland estimate d the cost to be approximately $300,000 to $325,000

, including a cost of $25,000 to

$30,000 for the pumps.

For hydrochloric acid, Mr. Litherland said the feed point c ould feed up to 50 gallons/hour. He expected that one

feed point would be sufficient based on that feed rate.Project No.: 0172.08.029.044 DISTRIBUTION

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Project Name: Steam/Cost/Compliance Modeling

TELEPHONE CALL RECORD

Outgoing Call Date: 06/30/2011 Time: 11:00 am PD T

Company Name: EnPro Technologies Contact Name: Troy Litherland

Phone No : (816) 350

- 5223

Email: tlitherland@enpro

- tech.com

Name: Kavya Kasturi ERG

GENERAL SUBJECT: Vendor cost request for chemical feed systems for a chemical precipitation wastewater treatment system.

TOPICS DISCUSSED AND ACTION TAKEN

On June 30, 2011 at 11:00 am I contacted Mr. Troy Litherland with additional questions on the feed systems.

Mr. Litherland stated that for a system containing two small peristaltic pumps, a silo, and a volumetric feeder,

the low end of the price range wo uld be $200, 0 00

- $250,000. A conservative cost estimate would be $300,000.

The system would require 3

- 4 days start up time and a cost of $4,000

- $5,000 for training and start up.

For liquid feed systems, Mr. Litherland said a small size system could be used for feed rates under 100 gal/hour

and would cost $5,000. For feed rates greater than 100 gal/hour, the cost of a feed point would be $15,000.