RU2015113354A - WASTE WATER CONCENTRATION METHOD (OPTIONS) - Google Patents

WASTE WATER CONCENTRATION METHOD (OPTIONS) Download PDF

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Publication number
RU2015113354A
RU2015113354A RU2015113354/05A RU2015113354A RU2015113354A RU 2015113354 A RU2015113354 A RU 2015113354A RU 2015113354/05 A RU2015113354/05 A RU 2015113354/05A RU 2015113354 A RU2015113354 A RU 2015113354A RU 2015113354 A RU2015113354 A RU 2015113354A
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RU
Russia
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liquid
mixture
gas
wastewater
concentrated
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RU2015113354/05A
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Russian (ru)
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RU2672451C2 (en
RU2015113354A3 (en
Inventor
Бернард Ф. Дж. ДЬЮЗЕЛЬ
Майкл Дж. РАТШ
Крег КЛАРКИН
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Хартлэнд Текнолоджи Партнерс Ллк
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Priority claimed from US12/705,462 external-priority patent/US8568557B2/en
Application filed by Хартлэнд Текнолоджи Партнерс Ллк filed Critical Хартлэнд Текнолоджи Партнерс Ллк
Publication of RU2015113354A publication Critical patent/RU2015113354A/en
Publication of RU2015113354A3 publication Critical patent/RU2015113354A3/ru
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/048—Purification of waste water by evaporation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/16—Treatment of sludge; Devices therefor by de-watering, drying or thickening using drying or composting beds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/14—Evaporating with heated gases or vapours or liquids in contact with the liquid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/16—Evaporating by spraying
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/16—Evaporating by spraying
    • B01D1/20—Sprayers
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/16—Treatment of water, waste water, or sewage by heating by distillation or evaporation using waste heat from other processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77—Liquid phase processes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/13—Treatment of sludge; Devices therefor by de-watering, drying or thickening by heating
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00—Nature of the contaminant
    • C02F2101/10—Inorganic compounds
    • C02F2101/101—Sulfur compounds
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00—Nature of the contaminant
    • C02F2101/10—Inorganic compounds
    • C02F2101/16—Nitrogen compounds, e.g. ammonia
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/001—Runoff or storm water
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/06—Contaminated groundwater or leachate
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/10—Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00—Apparatus for treatment of water, waste water or sewage
    • C02F2201/008—Mobile apparatus and plants, e.g. mounted on a vehicle
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/005—Processes using a programmable logic controller [PLC]
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T50/00—Aeronautics or air transport
    • Y02T50/60—Efficient propulsion technologies, e.g. for aircraft
    • Y02T50/678—Aviation using fuels of non-fossil origin

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Hydrology & Water Resources (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Drying Of Gases (AREA)
  • Gas Separation By Absorption (AREA)
  • Treating Waste Gases (AREA)
  • Physical Water Treatments (AREA)
  • Separation Of Particles Using Liquids (AREA)

Abstract

1. Способ концентрирования сточных вод, включающий:а. комбинирование нагретого газа и жидкого потока сточных вод под давлением;б. прохождение комбинированного потока нагретого газа и жидкого потока сточных вод через канал смешивания концентратора для образования газо-жидкостной смеси, имеющей жидкую концентрацию от приблизительно 5 масс. % до приблизительно 20 масс. % от общей массы смеси, канал смешивания, имеющий суженный участок, в котором газо-жидкостный поток в пределах канала смешивания ускоряется при прохождении от впускного отверстия к выпускному отверстию канала;в. отделение части жидкости от газожидкостной смеси для получения газовой смеси с переносимыми каплями жидкости;г. удаление капель жидкости, переносимых газовой смесью, полученной на этапе в., для получения концентрированной жидкости и газа, в основном свободного от жидкости.2. Способ по п. 1, отличающийся тем, что дополнительно включает рециркуляцию и комбинирование с жидким потоком сточных вод этапа а. концентрированной жидкости, полученной на этапе г.3. Способ концентрирования сточных вод, включающий:а. комбинирование нагретого газа и жидкого потока сточных вод под давлением для образования смеси;б. снижение статического давления смеси для испарения части жидкости из смеси для получения частично выпаренной смеси, содержащей переносимую концентрированную жидкость;в. удаление части переносимой концентрированной жидкости с частично выпаренной смеси для получения газа без содержания жидкости.1. A method for concentrating wastewater, comprising: a. a combination of heated gas and a liquid wastewater stream under pressure b. passing a combined stream of heated gas and a liquid stream of wastewater through the mixing channel of the concentrator to form a gas-liquid mixture having a liquid concentration of from about 5 mass. % to about 20 mass. % of the total mass of the mixture, a mixing channel having a narrowed portion in which the gas-liquid flow within the mixing channel is accelerated as it passes from the inlet to the outlet of the channel; separating part of the liquid from the gas-liquid mixture to obtain a gas mixture with portable drops of liquid; removing droplets of liquid carried by the gas mixture obtained in step c. to obtain a concentrated liquid and gas, mainly free of liquid. 2. The method according to claim 1, characterized in that it further includes recycling and combining with the liquid wastewater stream of step a. concentrated liquid obtained in step g.3. A method for concentrating wastewater, comprising: a. a combination of heated gas and a liquid wastewater stream under pressure to form a mixture; b. reducing the static pressure of the mixture to evaporate part of the liquid from the mixture to obtain a partially evaporated mixture containing a portable concentrated liquid; removing part of the concentrated concentrated liquid from the partially evaporated mixture to obtain a gas without liquid content.

Claims (3)

1. Способ концентрирования сточных вод, включающий:1. A method of concentrating wastewater, including: а. комбинирование нагретого газа и жидкого потока сточных вод под давлением;but. a combination of heated gas and a liquid wastewater stream under pressure; б. прохождение комбинированного потока нагретого газа и жидкого потока сточных вод через канал смешивания концентратора для образования газо-жидкостной смеси, имеющей жидкую концентрацию от приблизительно 5 масс. % до приблизительно 20 масс. % от общей массы смеси, канал смешивания, имеющий суженный участок, в котором газо-жидкостный поток в пределах канала смешивания ускоряется при прохождении от впускного отверстия к выпускному отверстию канала;b. passing a combined stream of heated gas and a liquid stream of wastewater through the mixing channel of the concentrator to form a gas-liquid mixture having a liquid concentration of from about 5 mass. % to about 20 mass. % of the total mass of the mixture, a mixing channel having a narrowed portion in which the gas-liquid flow within the mixing channel is accelerated as it passes from the inlet to the outlet of the channel; в. отделение части жидкости от газожидкостной смеси для получения газовой смеси с переносимыми каплями жидкости;at. separating part of the liquid from the gas-liquid mixture to obtain a gas mixture with portable drops of liquid; г. удаление капель жидкости, переносимых газовой смесью, полученной на этапе в., для получения концентрированной жидкости и газа, в основном свободного от жидкости.d. removing droplets of liquid carried by the gas mixture obtained in step c. to obtain concentrated liquid and gas, mainly free of liquid. 2. Способ по п. 1, отличающийся тем, что дополнительно включает рециркуляцию и комбинирование с жидким потоком сточных вод этапа а. концентрированной жидкости, полученной на этапе г. 2. The method according to p. 1, characterized in that it further includes recycling and combination with a liquid wastewater stream of stage a. concentrated liquid obtained in step g. 3. Способ концентрирования сточных вод, включающий:3. A method of concentrating wastewater, including: а. комбинирование нагретого газа и жидкого потока сточных вод под давлением для образования смеси;but. combining heated gas and a liquid wastewater stream under pressure to form a mixture; б. снижение статического давления смеси для испарения части жидкости из смеси для получения частично выпаренной смеси, содержащей переносимую концентрированную жидкость;b. reducing the static pressure of the mixture to evaporate part of the liquid from the mixture to obtain a partially evaporated mixture containing a portable concentrated liquid; в. удаление части переносимой концентрированной жидкости с частично выпаренной смеси для получения газа без содержания жидкости. at. removing part of the concentrated concentrated liquid from the partially evaporated mixture to obtain a gas without liquid content.
RU2015113354A 2009-07-29 2010-07-29 Method of concentration of wastewater (variants) RU2672451C2 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US22965009P 2009-07-29 2009-07-29
US61/229,650 2009-07-29
US12/705,462 2010-02-12
US12/705,462 US8568557B2 (en) 2007-03-13 2010-02-12 Compact wastewater concentrator using waste heat

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
RU2012104408/05A Division RU2551494C2 (en) 2009-07-29 2010-07-29 Compact effluents concentrator running on waste heat

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RU2015113354A true RU2015113354A (en) 2015-11-10
RU2015113354A3 RU2015113354A3 (en) 2018-09-13
RU2672451C2 RU2672451C2 (en) 2018-11-14

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RU2012104412/05A RU2547117C2 (en) 2009-07-29 2010-07-29 Compact concentrator of effluents and gas-flushing unit for removal of contaminants
RU2012104408/05A RU2551494C2 (en) 2009-07-29 2010-07-29 Compact effluents concentrator running on waste heat
RU2015113354A RU2672451C2 (en) 2009-07-29 2010-07-29 Method of concentration of wastewater (variants)

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RU2012104412/05A RU2547117C2 (en) 2009-07-29 2010-07-29 Compact concentrator of effluents and gas-flushing unit for removal of contaminants
RU2012104408/05A RU2551494C2 (en) 2009-07-29 2010-07-29 Compact effluents concentrator running on waste heat

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EP (2) EP2473446A4 (en)
JP (3) JP5823963B2 (en)
CN (3) CN105126366B (en)
AR (3) AR077776A1 (en)
AU (4) AU2010279004B2 (en)
BR (2) BR112012001724A2 (en)
CA (2) CA2768188A1 (en)
MX (2) MX2012001292A (en)
RU (3) RU2547117C2 (en)
UA (2) UA107800C2 (en)
WO (2) WO2011014616A2 (en)

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WO2011014617A3 (en) 2011-06-16
BR112012001718A2 (en) 2017-06-13
AU2017221790A1 (en) 2017-09-21
AU2010279005A1 (en) 2012-02-02
AR077508A1 (en) 2011-08-31
EP2459488A2 (en) 2012-06-06
AR077781A1 (en) 2011-09-21
JP5823963B2 (en) 2015-11-25
CN102471094A (en) 2012-05-23
EP2459488A4 (en) 2013-03-06
RU2551494C2 (en) 2015-05-27
EP2473446A2 (en) 2012-07-11
WO2011014616A2 (en) 2011-02-03
AU2015203696A1 (en) 2015-07-16
RU2672451C2 (en) 2018-11-14
UA107800C2 (en) 2015-02-25
JP2016040037A (en) 2016-03-24
AU2010279005B2 (en) 2015-03-26
AU2010279004B2 (en) 2014-07-24
WO2011014617A2 (en) 2011-02-03
CA2769381A1 (en) 2011-02-03
RU2015113354A3 (en) 2018-09-13
UA105049C2 (en) 2014-04-10
CN102471094B (en) 2015-12-16
WO2011014616A3 (en) 2011-06-16
AR077776A1 (en) 2011-09-21
CN105126366B (en) 2017-09-05
CN102471095B (en) 2015-08-19
EP2473446A4 (en) 2013-03-27
JP2013500853A (en) 2013-01-10
RU2012104412A (en) 2013-09-10
AU2010279004A1 (en) 2012-02-02
RU2547117C2 (en) 2015-04-10
MX2012001292A (en) 2012-03-26
CN105126366A (en) 2015-12-09
CN102471095A (en) 2012-05-23
AU2015203696B2 (en) 2017-06-01
RU2012104408A (en) 2013-09-10
BR112012001724A2 (en) 2016-11-22
CA2768188A1 (en) 2011-02-03
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JP2013500852A (en) 2013-01-10

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