GB727156A - Improvements relating to the treatment of gas works effluent liquors - Google Patents

Improvements relating to the treatment of gas works effluent liquors

Info

Publication number
GB727156A
GB727156A GB1085352A GB1085352A GB727156A GB 727156 A GB727156 A GB 727156A GB 1085352 A GB1085352 A GB 1085352A GB 1085352 A GB1085352 A GB 1085352A GB 727156 A GB727156 A GB 727156A
Authority
GB
United Kingdom
Prior art keywords
liquor
liquors
river
effluent
phenols
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB1085352A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CECIL FREDERICK DAVIES
Simon Carves Ltd
Carves Simon Ltd
Original Assignee
CECIL FREDERICK DAVIES
Simon Carves Ltd
Carves Simon Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by CECIL FREDERICK DAVIES, Simon Carves Ltd, Carves Simon Ltd filed Critical CECIL FREDERICK DAVIES
Priority to GB1085352A priority Critical patent/GB727156A/en
Publication of GB727156A publication Critical patent/GB727156A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10KPURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00Purifying combustible gases containing carbon monoxide
    • C10K1/001Purifying combustible gases containing carbon monoxide working-up the condensates

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Physical Water Treatments (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

In a process for treating the ammoniacal liquors obtained in a gas works, the retort house liquor and the liquor from the hot sections of the condensers and the gas detarrers are stripped of free ammonia and dephenolated while the other liquors such as the liquors from the washing processes and cooler sections of the condensers are distilled to obtain concentrated ammonia liquor, in each case an effluent liquor being obtained suitable for discharge into a sewer. The retort house liquor may be dephenolated by extraction with butyl acetate or methyl isobutyl ketone and the phenols, which are mainly polyhydric phenols, after separation from the solvent may be burnt in a furnace. The washing liquor may also be dephenolated, for example by extraction with benzene, in which case the effluent liquors may be discharged into a river if the toxicity of the river is not important. The phenols, which in this case are mainly monohydric phenols, may be separated from the benzene solution by steam distillation or extraction with caustic soda. The effluent liquor obtained in distilling the washing liquor may also be partly used in gas washing plant, the remainder being discharged to a sewer or river or concentrated and the concentrate treated with sulphuric or nitric acid or destroyed in a coke-burning furnace. The effluent liquor resulting from the treatment of the retort house liquor if it is not desired to or it is impossible to discharge it into a sewer or a river may be concentrated to obtain ammonium chloride and the mother liquor treated with acid or destroyed in a coke-burning furnace.ALSO:In a process for treating the ammoniacal liquors obtained in a p gas works, the retort house liquor and the liquor from the hot sections of the condensers and the gas detarrers are stripped of free ammonia and dephenolated while the other liquors such as the liquors from the washing processes and cooler sections of the condensers are distilled to obtained concentrated ammonia liquor, in each case an effluent liquor being obtained suitable for discharge into a sewer. The retort house liquor may be dephenolated by extraction with butyl acetate or methyl isobutyl ketone and the phenols, which are mainly polyhydric phenols, after separation from the solvent may be burnt in a furnace. The washing liquor may also be dephenolated, for example by extraction with benzene, in which case the effluent liquors may be discharged into a river if the toxicity of the river is not important. The phenols, which in this case are mainly monohydric phenols, may be separated from the benzene solution by steam distillation or extraction with caustic soda. The effluent liquor obtained in distilling the washing liquor may also be partly used in gas washing plant, the remainder being discharged to a sewer or river or concentrated and the concentrate treated with sulphuric or nitric acid or destroyed in a coke-burning furnace. The effluent liquor resulting from the treatment of the retort house liquor if it is not desired to or it is impossible to discharge it into a sewer or a river may be concentrated to obtain ammonium chloride and the mother liquor treated with acid or destroyed in a coke-burning furnace.ALSO:In a process for treating the ammoniacal liquors obtained in gas works, the retort house liquor and the liquor from the hot sections of the condensers and the gas detarrers are stripped of free ammonia and dephenolated while the other liquors such as the liquors from the washing processes and cooler sections of the condensers are distilled to obtain concentrated ammonia liquor, in each case an effluent liquor being obtained suitable for discharge into a sewer. The retort house liquor may be dephenolated by extraction with butyl acetate or methyl isobutyl ketone and the phenols, which are mainly polyhydric phenols, after separation from the solvent may be burnt in a furnace. The washing liquor may also be dephenolated, for example by extraction with benzene, in which case the effluent liquors may be discharged into a river if the toxicity of the river is not important. The phenols, which in this case are mainly monohydric phenols, may be separated from the benzene solution by steam distillation or extraction with caustic soda. The effluent obtained in distilling the washing liquor may also be partly used in gas washing plant, the remainder being discharged to a sewer or river or concentrated and the concentrate treated with sulphuric or nitric acid or destroyed in a coke-burning furnace. The effluent liquor resulting from the treatment of the retort house liquor if it is not desired to or it is impossible to discharge it into a sewer or a river may be concentrated to obtain ammonium chloride and the mother liquor treated with acid or destroyed in a coke-burning furnace.
GB1085352A 1952-04-30 1952-04-30 Improvements relating to the treatment of gas works effluent liquors Expired GB727156A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB1085352A GB727156A (en) 1952-04-30 1952-04-30 Improvements relating to the treatment of gas works effluent liquors

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1085352A GB727156A (en) 1952-04-30 1952-04-30 Improvements relating to the treatment of gas works effluent liquors

Publications (1)

Publication Number Publication Date
GB727156A true GB727156A (en) 1955-03-30

Family

ID=9975524

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1085352A Expired GB727156A (en) 1952-04-30 1952-04-30 Improvements relating to the treatment of gas works effluent liquors

Country Status (1)

Country Link
GB (1) GB727156A (en)

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