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25 DUAL BED ION EXCHANGE REGENERATION-OPTIMIZATION FOR HIGH PURITY WATER SYSTEMS James A. Mueller, Professor Environmental Engineering and Science Manhattan College Bronx, New York 10471 Warren Riznychok, Senior Associate Chemist Gordon Bie, Senior Operator IBM Thomas J. Watson Research Center Yorktown Heights, New York 10598 INTRODUCTION The Thomas J. Watson Research Center in Yorktown Heights, New York, is International Business Machines (IBM) basic and applied research division headquarters. Historically, wastewater generated by the research activities has been treated by an Industrial Wastewater Treatment Facility and its effluent recycled for reuse in laboratory sinks, as boiler makeup and feedwater to the sites deionized water systems. In January 1984 a newly constructed High Purity Water System (HPW) was brought on-line and also received recycled industrial waste as a source of makeup water. High purity water, used primarily in semiconductor research at the Center, can have a significant impact on research and development if it does not meet required ionic, organic, and 6 quality specifications. Due to upgrading of the industrial wastewater treatment plant, the HPW began to use city water directly in January 1985, and by March 1985 the two bed ion exchange process, heart of the HPW system, showed significant reductions in throughput volumes and quality. High pH and conductivity focused attention to the cation unit as the problem. The body of this paper will discuss in detail the steps taken to quickly recover cation bed capacity and to optimize regeneration efficiency. PROCESS DESCRIPTION A total water flow scheme is illustrated in Figure 1. Industrial waste characterization in 1982 of the daytime (7:30 A.M.-7:30 P.M.) and nighttime waste demonstrated feasibility of segregation of the waste stream into separate holding tanks, enhancing process operation. Daytime waste undergoes neutralization, biological treatment with rotating biological contactors, settling, disinfection with chlorine, and air stripping. Air stripper effluent quality determines if the pretreated day waste will be discharged to the Westchester County Sewer System or undergo further treatment. The dilute night waste, which contains 40% deionized water, or pretreated day waste, is further treated by dual media filtration, activated carbon adsorption and two bed ion exchange present in the nighttime waste process flow scheme. Provisions are also in place to pretreat city water through this process area to assure adequate supply for makeup and users. Figure 2 indicates process flow and water treatment possibilities. High purity water is produced using dual media filtration for gross particulate removal, activated carbon adsorption for removal of organics and chlorine, UV sterilization, two bed ion exchange, mixed bed ion exchange, UV sterilization, 0.6 micron and 0.2 micron membrane filtration (Figure 3). This high quality point of distribution effluent is pumped to the research center where it is repolished by two separate stations. Water that is not required for makeup at the two polishing stations is returned to intermediate storage in the main processing plant. The polishing station servicing the Advanced Silicon Technology Laboratory and Aisles 1-6 repuri- fies the water with nonregenerable mixed beds UV sterilization and 0.1 micron filtration. The second 219
Object Description
Purdue Identification Number | ETRIWC198625 |
Title | Dual bed ion exchange regeneration : optimization for high purity water systems |
Author |
Mueller, James A. Riznychok, Warren Bie, Gordon |
Date of Original | 1986 |
Conference Title | Proceedings of the 41st Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,37786 |
Extent of Original | p. 219-233 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Date Digitized | 2009-07-13 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 219 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Transcript | 25 DUAL BED ION EXCHANGE REGENERATION-OPTIMIZATION FOR HIGH PURITY WATER SYSTEMS James A. Mueller, Professor Environmental Engineering and Science Manhattan College Bronx, New York 10471 Warren Riznychok, Senior Associate Chemist Gordon Bie, Senior Operator IBM Thomas J. Watson Research Center Yorktown Heights, New York 10598 INTRODUCTION The Thomas J. Watson Research Center in Yorktown Heights, New York, is International Business Machines (IBM) basic and applied research division headquarters. Historically, wastewater generated by the research activities has been treated by an Industrial Wastewater Treatment Facility and its effluent recycled for reuse in laboratory sinks, as boiler makeup and feedwater to the sites deionized water systems. In January 1984 a newly constructed High Purity Water System (HPW) was brought on-line and also received recycled industrial waste as a source of makeup water. High purity water, used primarily in semiconductor research at the Center, can have a significant impact on research and development if it does not meet required ionic, organic, and 6 quality specifications. Due to upgrading of the industrial wastewater treatment plant, the HPW began to use city water directly in January 1985, and by March 1985 the two bed ion exchange process, heart of the HPW system, showed significant reductions in throughput volumes and quality. High pH and conductivity focused attention to the cation unit as the problem. The body of this paper will discuss in detail the steps taken to quickly recover cation bed capacity and to optimize regeneration efficiency. PROCESS DESCRIPTION A total water flow scheme is illustrated in Figure 1. Industrial waste characterization in 1982 of the daytime (7:30 A.M.-7:30 P.M.) and nighttime waste demonstrated feasibility of segregation of the waste stream into separate holding tanks, enhancing process operation. Daytime waste undergoes neutralization, biological treatment with rotating biological contactors, settling, disinfection with chlorine, and air stripping. Air stripper effluent quality determines if the pretreated day waste will be discharged to the Westchester County Sewer System or undergo further treatment. The dilute night waste, which contains 40% deionized water, or pretreated day waste, is further treated by dual media filtration, activated carbon adsorption and two bed ion exchange present in the nighttime waste process flow scheme. Provisions are also in place to pretreat city water through this process area to assure adequate supply for makeup and users. Figure 2 indicates process flow and water treatment possibilities. High purity water is produced using dual media filtration for gross particulate removal, activated carbon adsorption for removal of organics and chlorine, UV sterilization, two bed ion exchange, mixed bed ion exchange, UV sterilization, 0.6 micron and 0.2 micron membrane filtration (Figure 3). This high quality point of distribution effluent is pumped to the research center where it is repolished by two separate stations. Water that is not required for makeup at the two polishing stations is returned to intermediate storage in the main processing plant. The polishing station servicing the Advanced Silicon Technology Laboratory and Aisles 1-6 repuri- fies the water with nonregenerable mixed beds UV sterilization and 0.1 micron filtration. The second 219 |
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