[go: up one dir, main page]

RU2014147054A - REACTOR FOR GASIFICATION AND / OR CLEANING, IN PARTICULAR FOR DEPOLIMERIZATION OF SYNTHETIC MATERIAL AND RELATED METHOD - Google Patents

REACTOR FOR GASIFICATION AND / OR CLEANING, IN PARTICULAR FOR DEPOLIMERIZATION OF SYNTHETIC MATERIAL AND RELATED METHOD Download PDF

Info

Publication number
RU2014147054A
RU2014147054A RU2014147054A RU2014147054A RU2014147054A RU 2014147054 A RU2014147054 A RU 2014147054A RU 2014147054 A RU2014147054 A RU 2014147054A RU 2014147054 A RU2014147054 A RU 2014147054A RU 2014147054 A RU2014147054 A RU 2014147054A
Authority
RU
Russia
Prior art keywords
waste
reactor
liquid metal
synthetic material
bath
Prior art date
Application number
RU2014147054A
Other languages
Russian (ru)
Inventor
Адам ХАНДЕРЕК
Original Assignee
ШЛЮТЕР Хартвиг
Адам ХАНДЕРЕК
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 ШЛЮТЕР Хартвиг, Адам ХАНДЕРЕК filed Critical ШЛЮТЕР Хартвиг
Publication of RU2014147054A publication Critical patent/RU2014147054A/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/14—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot liquids, e.g. molten metals
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0006—Controlling or regulating processes
    • B01J19/0013—Controlling the temperature of the process
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2415—Tubular reactors
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/07—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of solid raw materials consisting of synthetic polymeric materials, e.g. tyres
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002—Chemical plants
    • B01J2219/00027—Process aspects
    • B01J2219/0004—Processes in series
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00121—Controlling the temperature by direct heating or cooling
    • B01J2219/00123—Controlling the temperature by direct heating or cooling adding a temperature modifying medium to the reactants
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00139—Controlling the temperature using electromagnetic heating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/30—Details relating to random packing elements
    • B01J2219/302—Basic shape of the elements
    • B01J2219/30207—Sphere
    • 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
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/141—Feedstock
    • Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Wood Science & Technology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Processing Of Solid Wastes (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

1. Реактор для газификации и/или очистки, в частности для деполимеризации синтетического материала (12), содержащий(а) корпус (14) реактора для принятия исходного материала (12), в частности синтетического материала (12),(b) ванну (26) жидкого металла, которая- размещена в корпусе (14) реактора и- содержит жидкий металлический материал, который имеет температуру (T) плавления ванны жидкого металла,(с) множество заполняющих элементов (25) в ванне (26) жидкого металла,(d) нагреватель (18) для нагревания синтетического материала (12) в корпусе (14) реактора, и(е) устройство удаления отходов, по меньшей мере, для частичного выведения отходов (38), которые образуются при газификации и/или очистке исходного материала (12),отличающийся тем, что(f) устройство удаления отходов включает размещенное по центру корпуса (14) реактора перепускное устройство, так что плавающие в ванне (26) жидкого металла отходы (38) могут быть выведены через перепускное устройство.2. Реактор по п. 1, отличающийся тем, что перепускное устройство образовано заборной трубой (36), которая находится в термическом контакте с ванной (26) жидкого металла.3. Реактор по п. 2, отличающийся тем, что в заборной трубе (36) размещено устройство транспортирования отходов, которое выполнено для продвижения отходов механическим воздействием.4. Реактор по п. 2, отличающийся тем, что заборная труба (36) имеет внутренний диаметр (d) трубы, который составляет, по меньшей мере, десятую часть внутреннего диаметра (d) корпуса (14) реактора.5. Реактор по п. 1, отличающийся тем, что устройство удаления отходов включает резервуар (48) для хранения и газонепроницаемый шлюз, так что резервуар (48) для хранения является герметично съемным.6. Способ эксплуатации реактора (10) для газификации и/или очистки, в част1. A reactor for gasification and / or purification, in particular for the depolymerization of synthetic material (12), containing (a) the housing (14) of the reactor for receiving the source material (12), in particular synthetic material (12), (b) a bath ( 26) a liquid metal, which is located in the reactor vessel (14) and contains a liquid metal material that has a melting temperature (T) of the liquid metal bath, (c) a plurality of filling elements (25) in the liquid metal bath (26), ( d) a heater (18) for heating the synthetic material (12) in the reactor vessel (14), and (e) arrangement waste removal means, at least for partial removal of waste (38) that is formed during gasification and / or purification of the source material (12), characterized in that (f) the waste removal device includes a bypass located in the center of the reactor vessel (14) device, so that waste (38) floating in the liquid metal bath (26) can be discharged through the bypass device. 2. The reactor according to claim 1, characterized in that the bypass device is formed by an intake pipe (36), which is in thermal contact with the molten metal bath (26). 3. The reactor according to claim 2, characterized in that a waste transport device is arranged in the intake pipe (36), which is designed to promote the waste by mechanical action. 4. The reactor according to claim 2, characterized in that the intake pipe (36) has an inner diameter (d) of the pipe, which is at least a tenth of the inner diameter (d) of the reactor vessel (14). 5. The reactor according to claim 1, characterized in that the waste disposal device includes a storage tank (48) and a gas tight lock, so that the storage tank (48) is hermetically removable. The method of operation of the reactor (10) for gasification and / or purification, in particular

Claims (7)

1. Реактор для газификации и/или очистки, в частности для деполимеризации синтетического материала (12), содержащий1. A reactor for gasification and / or purification, in particular for depolymerization of synthetic material (12), containing (а) корпус (14) реактора для принятия исходного материала (12), в частности синтетического материала (12),(a) a reactor vessel (14) for accepting a source material (12), in particular a synthetic material (12), (b) ванну (26) жидкого металла, которая(b) a bath (26) of molten metal, which - размещена в корпусе (14) реактора и- placed in the reactor vessel (14) and - содержит жидкий металлический материал, который имеет температуру (TSchmelz) плавления ванны жидкого металла,- contains a liquid metal material that has a melting temperature (T Schmelz ) of a liquid metal bath, (с) множество заполняющих элементов (25) в ванне (26) жидкого металла,(c) a plurality of filling elements (25) in a bath (26) of molten metal, (d) нагреватель (18) для нагревания синтетического материала (12) в корпусе (14) реактора, и(d) a heater (18) for heating the synthetic material (12) in the reactor vessel (14), and (е) устройство удаления отходов, по меньшей мере, для частичного выведения отходов (38), которые образуются при газификации и/или очистке исходного материала (12),(e) a device for removing waste, at least for the partial removal of waste (38) that is formed during gasification and / or purification of the source material (12), отличающийся тем, чтоcharacterized in that (f) устройство удаления отходов включает размещенное по центру корпуса (14) реактора перепускное устройство, так что плавающие в ванне (26) жидкого металла отходы (38) могут быть выведены через перепускное устройство.(f) the waste disposal device includes a bypass device located in the center of the reactor vessel (14), so that waste (38) floating in the liquid metal bath (26) can be discharged through the bypass device. 2. Реактор по п. 1, отличающийся тем, что перепускное устройство образовано заборной трубой (36), которая находится в термическом контакте с ванной (26) жидкого металла.2. The reactor according to claim 1, characterized in that the bypass device is formed by an intake pipe (36), which is in thermal contact with the molten metal bath (26). 3. Реактор по п. 2, отличающийся тем, что в заборной трубе (36) размещено устройство транспортирования отходов, которое выполнено для продвижения отходов механическим воздействием.3. The reactor according to claim 2, characterized in that a waste transport device is arranged in the intake pipe (36), which is designed to promote the waste by mechanical action. 4. Реактор по п. 2, отличающийся тем, что заборная труба (36) имеет внутренний диаметр (d36) трубы, который составляет, по меньшей мере, десятую часть внутреннего диаметра (d14) корпуса (14) реактора.4. Reactor according to claim. 2, characterized in that the fence pipe (36) has an internal diameter (d 36) of the tube which is at least a tenth of the internal diameter (d 14) of the housing (14) of the reactor. 5. Реактор по п. 1, отличающийся тем, что устройство удаления отходов включает резервуар (48) для хранения и газонепроницаемый шлюз, так что резервуар (48) для хранения является герметично съемным.5. The reactor according to claim 1, characterized in that the waste disposal device includes a storage tank (48) and a gas-tight lock, so that the storage tank (48) is hermetically removable. 6. Способ эксплуатации реактора (10) для газификации и/или очистки, в частности для деполимеризации синтетического материала (12), который имеет6. The method of operation of the reactor (10) for gasification and / or purification, in particular for the depolymerization of synthetic material (12), which has (а) корпус (14) реактора для принятия синтетического материала (12),(a) a reactor vessel (14) for accepting synthetic material (12), (b) ванну (26) жидкого металла, которая(b) a bath (26) of molten metal, which - размещена в корпусе (14) реактора и- placed in the reactor vessel (14) and - содержит жидкий металлический материал, который имеет температуру (TSchmelz) плавления ванны жидкого металла,- contains a liquid metal material that has a melting temperature (T Schmelz ) of a liquid metal bath, (с) нагреватель (18) для нагревания синтетического материала (12) в корпусе (14) реактора, и(c) a heater (18) for heating the synthetic material (12) in the reactor vessel (14), and (d) устройство удаления отходов, по меньшей мере, для частичного выведения отходов (38), которые образуются при газификации и/или очистке синтетического материала (12), содержащее размещенное по центру корпуса (14) реактора перепускное устройство, так что плавающие в ванне (26) жидкого металла отходы (38) могут быть выведены через перепускное устройство,(d) a device for removing waste, at least for the partial removal of waste (38) that is generated during gasification and / or purification of synthetic material (12), containing a bypass device located in the center of the reactor vessel (14), so that they float in the bath (26) liquid metal waste (38) can be removed through a bypass device, включающий этапы:including steps: (i) повышения уровня ванны (26) жидкого металла, так что отходы (38) поступают в перепускное устройство (36), и(i) increasing the level of the bath (26) of the molten metal, so that the waste (38) goes to the bypass device (36), and (ii) выведения отходов (38) через перепускное устройство (36).(ii) waste disposal (38) through a transfer device (36). 7. Способ по п. 6, отличающийся тем, что имеет этапы:7. The method according to p. 6, characterized in that it has the steps of: - подачи синтетического материала (12) в корпус (14) реактора,- supply of synthetic material (12) to the reactor vessel (14), - причем подачу синтетического материала (12) в корпус (14) реактора и/или регулирование уровня ванны (26) жидкого металла осуществляют таким образом, что на ванне (26) жидкого металла образуется слой отходов из отходов (38),- moreover, the supply of synthetic material (12) to the reactor vessel (14) and / or the regulation of the level of the liquid metal bath (26) is carried out in such a way that a layer of waste from the waste (38) is formed on the liquid metal bath (26), - причем толщина (Н38) слоя отходов составляет, по меньшей мере, 10 сантиметров. - wherein the thickness (H 38 ) of the waste layer is at least 10 centimeters.
RU2014147054A 2012-04-24 2013-04-23 REACTOR FOR GASIFICATION AND / OR CLEANING, IN PARTICULAR FOR DEPOLIMERIZATION OF SYNTHETIC MATERIAL AND RELATED METHOD RU2014147054A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE102012008457.9 2012-04-24
DE102012008457.9A DE102012008457B4 (en) 2012-04-24 2012-04-24 Reactor for gasifying and / or purifying, in particular for depolymerizing plastic material, and associated method
PCT/EP2013/001221 WO2013159914A1 (en) 2012-04-24 2013-04-23 Reactor for gasifying and/or cleaning, especially for depolymerizing, plastic material and associated method

Publications (1)

Publication Number Publication Date
RU2014147054A true RU2014147054A (en) 2016-06-10

Family

ID=48184134

Family Applications (1)

Application Number Title Priority Date Filing Date
RU2014147054A RU2014147054A (en) 2012-04-24 2013-04-23 REACTOR FOR GASIFICATION AND / OR CLEANING, IN PARTICULAR FOR DEPOLIMERIZATION OF SYNTHETIC MATERIAL AND RELATED METHOD

Country Status (11)

Country Link
US (1) US20150083572A1 (en)
EP (1) EP2841531A1 (en)
JP (1) JP2015521213A (en)
CN (1) CN104471032A (en)
AU (1) AU2013252106A1 (en)
BR (1) BR112014026405A2 (en)
CA (1) CA2870350A1 (en)
DE (1) DE102012008457B4 (en)
MX (1) MX2014012445A (en)
RU (1) RU2014147054A (en)
WO (1) WO2013159914A1 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017072057A1 (en) 2015-10-28 2017-05-04 Haldor Topsøe A/S Dehydrogenation of alkanes
IT201800009798A1 (en) * 2018-10-25 2020-04-25 Proil Srl PROCESS AND RELATIVE PLANT FOR THE DEPOLYMERIZATION OF PLASTIC MATERIALS FOR THE PRODUCTION OF HYDROCARBONS
CN116134118A (en) 2020-09-14 2023-05-16 埃科莱布美国股份有限公司 Cold-flow additives for plastic-derived synthetic feedstocks
KR20230153399A (en) 2021-03-10 2023-11-06 에코랍 유에스에이 인코퍼레이티드 Stabilizer additives for plastic-derived synthetic feedstocks
CN113284640B (en) * 2021-05-26 2024-09-27 中国原子能科学研究院 Floating impurity capturing device for reactor
JP2024537380A (en) 2021-10-14 2024-10-10 エコラボ ユーエスエー インコーポレイティド Antifouling agents for plastic-derived synthetic materials

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2787584A (en) * 1954-02-04 1957-04-02 Farafonow Wladimir Michael Continuous carbonization process and apparatus for solid carbonaceous materials
US5435982A (en) * 1993-03-31 1995-07-25 Molten Metal Technology, Inc. Method for dissociating waste in a packed bed reactor
DE19629544C2 (en) * 1996-07-22 1998-10-22 Linde Kca Dresden Gmbh Process for the preparation of polyvinyl chloride (PVC) and use of the process
DE19735153C2 (en) * 1997-08-13 2003-10-16 Linde Kca Dresden Gmbh Process and device for gasifying waste materials
DE10212105A1 (en) * 2002-03-11 2003-09-25 Abf Entwicklungsbetr Fuer Inno Pyrolysis of waste containing organic components, controls reactor pressure, adjusting and holding it to a value slightly above ambient
CN101088581B (en) * 2007-08-20 2011-08-10 丁家亮 Poisonous waste treating method and special apparatus
DE102008008999A1 (en) * 2007-11-26 2009-05-28 Werning, Holger, Dr. Thermal conversion of waste with a carbon content brings it in contact with molten metal in a reactor, with excluded oxygen, giving a gas flow with a hydrocarbon content for further processing
RU2540614C2 (en) * 2009-05-14 2015-02-10 ШЛЮТЕР Хартвиг Method and device for carrying out chemical processes
CN101695704B (en) * 2009-10-23 2012-02-01 中国科学院等离子体物理研究所 Apparatus and method for thermal plasma treatment of solid waste
DE102010050153B4 (en) * 2010-11-02 2012-10-25 Adam Handerek Reactor and method for at least partially decomposing and / or cleaning plastic material
CN102260515B (en) * 2011-06-24 2013-08-21 华东理工大学 Method and device for thermal cracking treatment of waste plastics

Also Published As

Publication number Publication date
DE102012008457B4 (en) 2016-11-03
DE102012008457A1 (en) 2013-10-24
WO2013159914A1 (en) 2013-10-31
JP2015521213A (en) 2015-07-27
CN104471032A (en) 2015-03-25
AU2013252106A1 (en) 2014-10-30
MX2014012445A (en) 2015-05-07
CA2870350A1 (en) 2013-10-31
US20150083572A1 (en) 2015-03-26
BR112014026405A2 (en) 2017-06-27
EP2841531A1 (en) 2015-03-04

Similar Documents

Publication Publication Date Title
RU2014147054A (en) REACTOR FOR GASIFICATION AND / OR CLEANING, IN PARTICULAR FOR DEPOLIMERIZATION OF SYNTHETIC MATERIAL AND RELATED METHOD
KR101138350B1 (en) Apparatus of condensation oily vapor for ship and ship with the same
RU2014147053A (en) REACTOR AND METHOD OF GASIFICATION AND / OR CLEANING OF THE ORIGINAL MATERIAL
TWI669412B (en) Reagent delivery system freeze prevention heat exchanger
ES2204353T1 (en) BIOMASS PREHYDROLYSIS DEVICE AND USE OF IT.
EA201690367A2 (en) INSTALLATION FOR ORGANIC RAW MATERIAL PROCESSING BY PYROLYSIS METHOD
RU2011135525A (en) METHOD FOR REGENERATING HYDRATE EDUCATION INHIBITOR
PH12012501642A1 (en) Device and method for condensing, separating, and storing liquid sulfur in a claus plant
RU2010140607A (en) GASIFICATION DEVICE WITH EQUIPMENT FOR SLAG REMOVAL
JPS59502074A (en) Method for purifying heat exchanger for engine exhaust gas
KR101224725B1 (en) Method and apparatus for disposing radioactive wastewater
MX2016002829A (en) Method of fuel for energetics production and fuel producing device.
RU126268U1 (en) DEVICE FOR PARPING CLEANING DEVICES
JP2012012459A (en) Treatment apparatus for waste and method for treating waste
EA201990829A1 (en) METHOD AND INSTALLATION FOR THERMAL ELIMINATION OF FETAL EMISSIONS FROM A CLEANING INSTALLATION WITH ENERGY RECOVERY FROM THE SPECIFIED REMEDY
CN203959982U (en) Integrated sewage treatment machine group
RU2010149031A (en) METHOD FOR MODELING THE PROCESS OF GASIFICATION OF RESIDUES OF LIQUID ROCKET FUEL AND DEVICE FOR IMPLEMENTATION
CN105780033B (en) A kind of environmental protection and energy saving derusting acid dip pickle suitable for laboratory
RU116780U1 (en) LABORATORY INSTALLATION FOR EXTRACTION OF VEGETABLE RAW MATERIALS
CN207418379U (en) For the upflow anaerobic sludge blanket reactor of teaching
CN104949134A (en) Double-layer water seal anti-explosion pre-warning system for rubbish pyrolysis gasifier
CN103357203B (en) A kind of rapid precipitation overflow tower structure
CN202762247U (en) Flue gas decoking purification device for charring furnace
RU2533724C1 (en) Method and device for tank purification from polluted water and oil sludge
RU72302U1 (en) STEAM GENERATOR WITH LEAD COOLANT OR ITS ALLOYS

Legal Events

Date Code Title Description
FA92 Acknowledgement of application withdrawn (lack of supplementary materials submitted)

Effective date: 20170801