Cold weather dechlorination
U.S. regulations severely limiting the concentration of chlorine permissible in the effluent from a wastewater treatment works serve as background to a review of methods for dechlorination and in particular to the use of sulphur dioxide for this purpose. The paper is principally devoted to alternati...
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Published in | Water engineering & management Vol. 137; no. 12; pp. 21 - 24 |
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Main Author | |
Format | Journal Article |
Language | English |
Published |
Des Plaines
Scranton Gillette Communications, Incorporated
01.12.1990
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Subjects | |
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Abstract | U.S. regulations severely limiting the concentration of chlorine permissible in the effluent from a wastewater treatment works serve as background to a review of methods for dechlorination and in particular to the use of sulphur dioxide for this purpose. The paper is principally devoted to alternative means of ensuring that a system using it could remain effective at temperatures below 18C, at which its vapour pressure of 35 p.s.i.g. was inadequate. Alternative means of raising the vapour pressure in the sulphur dioxide storage vessels above that determined by the ambient temperature are considered, the most favoured being reinforcement of pressure in the vessel by the addition of an externally-supplied gas. The options considered for the gas are nitrogen, dry air and sulphur dioxide. The commerically-available volume supplies of these in the U.S.A. are considered and technical difficulties associated with their use are outlined, much depending on the size, siting and warmth of the storage available and in some instances on what was legally permissible. The solution adopted at 1 works in Texas, where access for railway containers of bulk sulphur dioxide and heating for subsidiary storage tanks were available, is described and illustrated in a flow diagram. |
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AbstractList | An increasing number of plant owners are turning to sulfur dioxide for dechlorination because of its relatively low chemical cost and because it has handling characteristics similar to chlorine. However, sulfur dioxide has one major disadvantage: at temperatures below 66 degrees F, it has insufficient vapor pressure to flow from storage into the feed system without assistance. During the winter months in most parts of the US, sulfur dioxide must either be heated or pressurized before it can be fed. Such a situation arose during the design of a 35-million-gallon-a-day expansion of the Trinity River Authority's Central Regional Wastewater Treatment Plant, which serves 750,000 customers in the Dallas-Fort Worth, Texas, area. A preliminary design report identified sulfur dioxide as the most economical dechlorinating agent. In the design of any dechlorination system, several issues must be considered, such as: 1. feed rate, 2. available delivered quantities of sulfur dioxide, and 3. typical local weather conditions. U.S. regulations severely limiting the concentration of chlorine permissible in the effluent from a wastewater treatment works serve as background to a review of methods for dechlorination and in particular to the use of sulphur dioxide for this purpose. The paper is principally devoted to alternative means of ensuring that a system using it could remain effective at temperatures below 18C, at which its vapour pressure of 35 p.s.i.g. was inadequate. Alternative means of raising the vapour pressure in the sulphur dioxide storage vessels above that determined by the ambient temperature are considered, the most favoured being reinforcement of pressure in the vessel by the addition of an externally-supplied gas. The options considered for the gas are nitrogen, dry air and sulphur dioxide. The commerically-available volume supplies of these in the U.S.A. are considered and technical difficulties associated with their use are outlined, much depending on the size, siting and warmth of the storage available and in some instances on what was legally permissible. The solution adopted at 1 works in Texas, where access for railway containers of bulk sulphur dioxide and heating for subsidiary storage tanks were available, is described and illustrated in a flow diagram. In the design of any dechlorination system, several issues must be considered when choosing system components. Feed rate, available delivered quantities of sulfur dioxide and typical local weather conditions all are key considerations. |
Author | Sloan, D W |
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Snippet | U.S. regulations severely limiting the concentration of chlorine permissible in the effluent from a wastewater treatment works serve as background to a review... In the design of any dechlorination system, several issues must be considered when choosing system components. Feed rate, available delivered quantities of... An increasing number of plant owners are turning to sulfur dioxide for dechlorination because of its relatively low chemical cost and because it has handling... |
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SubjectTerms | Case studies Chemicals Effects Hazardous substances Pressure Sulfur Water treatment Water utilities Weather conditions |
Title | Cold weather dechlorination |
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