My WebLink
|
Help
|
About
|
Sign Out
Home
Browse
Search
2006-03-31_REVISION - M1977208
DRMS
>
Day Forward
>
Revision
>
Minerals
>
M1977208
>
2006-03-31_REVISION - M1977208
Metadata
Thumbnails
Annotations
Entry Properties
Last modified
6/16/2021 6:27:11 PM
Creation date
11/21/2007 12:31:06 PM
Metadata
Fields
Template:
DRMS Permit Index
Permit No
M1977208
IBM Index Class Name
Revision
Doc Date
3/31/2006
Doc Name
pH and Selenium Treatment of C-pit Water
From
CEMEX
To
DMG
Type & Sequence
TR7
Media Type
D
Archive
No
There are no annotations on this page.
Document management portal powered by Laserfiche WebLink 9 © 1998-2015
Laserfiche.
All rights reserved.
/
5
PDF
Print
Pages to print
Enter page numbers and/or page ranges separated by commas. For example, 1,3,5-12.
After downloading, print the document using a PDF reader (e.g. Adobe Reader).
View images
View plain text
TECHNICAL REVISION No. 07 <br />SELENIUM REMOVAL SYSTEM <br />CEMEX LYONS PLANT <br />C-PIT WATER <br />As TR-07 to the permit fox the CEMEX Lyons Plant in Lyons, Colorado, the Division of <br />Minerals and Geology (DMG) requires CEMEX to prepare a design and cost estimate to <br />support the calculation of a bond to cover the cost of implementing a treatment remedy for <br />water remaining in C-Pit in the unlikely event that CEMEX defaults and ceases operations. <br />This document presents a conceptual design and cost estimate for a biological water <br />treatment system to-remove selenium from water that has accumulated in C-Pit at the <br />CEMEX Lyons Plant. Continuous-flow, bench-scale ueatabiliry testing has demonstrated <br />that the process can reduce C-Pit water selenium concentrations from 430 micrograms per <br />liter (µg/L) to below 60 µg/L. The average selenium removal rate exceeded 90 percent. <br />DESIGN OBJECTIVES <br />The proposed system will meet the following objectives: <br />• Remove as much residual water as practicable from C-Pit <br />• Leave no final free water surface in C-Pit <br />• Reduce the selenium concentration of the water to 60 micrograms per liter (µg/L) or <br />lower <br />• Be operable independent of the existing cement manufacturing operations. <br />DESCRIPTION OF PROCESS <br />Figure 1 shows the conceptual design of the biological treatment process. Water is conveyed <br />by the C-Pit pump via the C-Pit line to the treatment area. Concentrated sulfuric acid is <br />injected by a metering pump into the C-Pit line upstream of an in-line mixer, thereby <br />reducing the influent pH to the neutral range of 6-9. The C-Pit pump, C-Pit line, acid <br />storage tank, acid metering pump and in-line mixer are all existing items that are in the <br />process of being installed under the terms of Technical Revision TR-06, dated December 2, <br />2005. <br />The bulk of the treatment process is provided by Zenon Environmental (Zenon) of <br />Oakville, Ontario, Canada (http://www.zenon.com). Proprietary nutrient solution provided <br />by Zenon is injected by a metering pump into the C-Pit line. This mixture flows to the <br />bottom of Reactor 1, which is a rented 21,000-gallon tank filled with activated carbon and <br />inoculated with selenium-reducing bacteria. Effluent is drawn from the top of this tank and <br />conveyed by gravity to the bottom of an identical Reactor 2. Additional nutrient is pumped <br />into the Reactor 2 feed. <br />
The URL can be used to link to this page
Your browser does not support the video tag.