WO2008011839A2 - Equipment for the discontinuous or continuous hydrolysis of organic matter - Google Patents

Equipment for the discontinuous or continuous hydrolysis of organic matter Download PDF

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Publication number
WO2008011839A2
WO2008011839A2 PCT/CZ2007/000073 CZ2007000073W WO2008011839A2 WO 2008011839 A2 WO2008011839 A2 WO 2008011839A2 CZ 2007000073 W CZ2007000073 W CZ 2007000073W WO 2008011839 A2 WO2008011839 A2 WO 2008011839A2
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WO
WIPO (PCT)
Prior art keywords
pipe
discharge
waste
pump
equipment
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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.)
Ceased
Application number
PCT/CZ2007/000073
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French (fr)
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WO2008011839A3 (en
Inventor
Martin Snajdr
Vilém SNAJDR
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Coramexport Sro
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Coramexport Sro
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Filing date
Publication date
Application filed by Coramexport Sro filed Critical Coramexport Sro
Priority to CN2007800341767A priority Critical patent/CN101517062B/en
Priority to EP07785500A priority patent/EP2049648A2/en
Publication of WO2008011839A2 publication Critical patent/WO2008011839A2/en
Publication of WO2008011839A3 publication Critical patent/WO2008011839A3/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M45/00—Means for pre-treatment of biological substances
    • C12M45/06—Means for pre-treatment of biological substances by chemical means or hydrolysis
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M21/00—Bioreactors or fermenters specially adapted for specific uses
    • C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M45/00—Means for pre-treatment of biological substances
    • C12M45/02—Means for pre-treatment of biological substances by mechanical forces; Stirring; Trituration; Comminuting
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M45/00—Means for pre-treatment of biological substances
    • C12M45/20—Heating; Cooling

Definitions

  • the invention involves the equipment for the discontinuous or continuous hydrolysis of organic matter, which reaches the raw material destruction up to a level of the cellular structure.
  • the system drawback consisted in that the raw material was not perfectly disturbed / crushed, which resulted in the reduced methane production, and the period of keeping the raw material in the retaining container could not be shortened.
  • the equipment for the discontinuous or continuous hydrolysis of organic matter i.e. according to this invention, the substance of which consists in that the equipment for discontinuous hydrolysis consists of the receiving trough connected to the crusher, to which the measurement tank is connected.
  • the latter is connected to the hydrolyzer interconnected via the overshooting pipe to the expander with the connected pipe to discharge waste vapours, connected to the condenser to which the pipe conducting cooling medium is connected, as well as the pipe of the cooling medium outlet and the pipe to conduct waste condensate and not condensed gases.
  • This pipe is further connected to the degasifierto which the fan to suck not condensed gases is connected, as well as the pipe of waste condensate connected to the expander, to which the pump of boiled matter, interconnected with the fermenter, connected Hydrolyser is designed with the connected pipe to feed the steam and the pipe to discharge the steam condensate.
  • the equipment is conveniently interconnected with the pump of boiled matter to the input raw material cooler, to which the supply pipe of water heating circuit, discharge pipe and cooled material pipe are conducted.
  • the supply and discharge pipes of the water heating circuit are connected to the input raw material pre-heater, interconnected between the crusher and the measuring tank.
  • the equipment for continuous hydrolysis consists of the receiving trough interconnected with the crusher with the connected pump of crushed raw material, which is connected to the inter-container connected by high-pressure pump to the hydrolyser.
  • the hydrolyser is connected to the heat source via the fume conduit to the stack.
  • the hydrolyser is further connected via the overshooting pipe to the counter-pressure head , connected with the pipe to discharge waste vapours to the condenser designed for the cooling medium inlet and outlet and the pipe to discharge waste condensate and not condensed gases, which is connected to the degasifier, to which the fan and waste condensate pipe, connected to the shower head, are connected.
  • Expander is connected via the boiled matter pump to the fermenter.
  • the equipment is conveniently designed connected after the boiled matter pump with the output raw material cooler connected to the supply and discharge pipes of the water heating circuit to the inlet raw material pre-heater and the connected pipe for the cooled material, brought out to the fermenter.
  • the biggest advantages of the above equipment include the fact that the raw material is completely destroyed during its operation to a level of cellular structure, so that more methane is obtained from such significantly decomposed matter and the period of keeping the matter in the fermenter is reduced.
  • Fig. 1 shows the discontinuous plant without the preheating of input raw material
  • Fig. 2 shows the plant with the preheating of input raw material
  • Fig. 3 shows the continuous process utilizing the thermal source waste gases and the counter-pressure head to accelerate the technologic process
  • Fig. 4 shows utilization of the heating medium during the raw material pre-heating.
  • the equipment for the discontinuous or continuous hydrolysis of organic matter consists of the of the receiving trough 1 connected to the crusher 2, to which the measurement tank 16 is connected, and further connected to the hydrolyzer 3 interconnected via the overshooting pipe 12 to the expander 13 with the connected pipe 4 to discharge waste vapours, connected to the condenser 5. to which the pipe 6 conducting cooling medium is connected, as well as the pipe 7 of the cooling medium outlet and the pipe 8 to conduct waste condensate and not condensed gases.
  • This pipe is further connected to the degasifier 9 to which the fan H to suck not condensed gases is connected, as well as the pipe 10 of waste condensate connected to the expander 13, to which the pump 14 ' of boiled matter interconnected with the fermenter 15 is connected.
  • Hydrolyser 3 is designed with the connected pipe 1_7 to feed the steam and the pipe 18 to discharge the steam condensate from the hydrolyzer 3.
  • the equipment for the discontinuous hydrolysis of organic matter is designed with the pipe 14 of boiled material connected to the cooler 19 of output raw material, to which the supply pipe 21 of water heating circuit, discharge pipe 20 of water heating circuit and pipe 23 of cooled material are connected, and both the pipes 20 and 21 are connected to the pre-heater 22 of the input raw material, interconnected between the crusher 2 and the measurement tank 16.
  • the equipment for the continuous hydrolysis of organic matter consists of the receiving trough 1 connected to the crusher 2 with the connected pump 24 of crushed raw material, which is connected to the inter-container 25 connected by high-pressure pump 26 to the hydrolyser 3.
  • the hydrolyser 3 is connected to the heat source 27 via the waste gases conduit 28 to the stack 30.
  • the hydrolyser is further connected via the overshooting pipe 12 to the counter-pressure head 29, connected via the pipe 4 to discharge the waste vapours to the condenser 5 designed with the pipe 6 of the cooling medium inlet and the pipe 7 of the cooling medium outlet and the pipe 8 to discharge waste condensate and not condensed gases, which is connected to the degasifier 9, to which the fan H and waste condensate pipe 10 , connected to the shower head 31, are connected.
  • Expander 13 is connected via the boiled matter pump 14 of boiler material to the fermenter 15.
  • the equipment for the continuous hydrolysis of organic matter is designed with the pump 14 of boiler material connected to the cooler 19 of output raw material, into which the supply pipe 21 of water heating circuit, discharge pipe 20 of water heating circuit and pipe 23 of cooled material are connected, and both the pipes 20 and 21_are connected to the pre-heater 22 of the input raw material, and connected to the pipe 23 for the cooled material, brought out to the fermenterl ⁇ .

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  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Zoology (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Organic Chemistry (AREA)
  • Wood Science & Technology (AREA)
  • Molecular Biology (AREA)
  • Genetics & Genomics (AREA)
  • Biochemistry (AREA)
  • Sustainable Development (AREA)
  • Microbiology (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Biotechnology (AREA)
  • Biomedical Technology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Mechanical Engineering (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Apparatus For Disinfection Or Sterilisation (AREA)
  • Fertilizers (AREA)

Abstract

The equipment for the discontinuous or continuous hydrolysis of organic matter according to Fig. 1 and Fig. 2 consists of the of the receiving trough (1) connected to the crusher (2), to which the measurement tank (16) is connected, and further connected to the hydrolyzer (3) interconnected via the shooting pipe (12) to the expander (13) with the connected pipe (4) to discharge waste vapours, connected to the condenser (5) to which the pipe (6) conducting cooling medium is connected, as well as the pipe (7) of the cooling medium outlet and the pipe (8) to conduct waste condensate and not condensed gases. This pipe is further connected to the degasifier (9) to which the fan (11) to suck not condensed gases is connected, as well as the pipe (10) of waste condensate connected to the expander (13), to which the pump (14) of boiled matter interconnected with the fermeter (15). is connected Hydrolyser (3) is designed with the connected pipe (17) to feed the steam and the pipe (18) to discharge the steam condensate from the hydrolyzer (3).

Description

Equipment for the discontinuous or continuous hydrolysis of organic matter
TECHNICAL FIELDS
The invention involves the equipment for the discontinuous or continuous hydrolysis of organic matter, which reaches the raw material destruction up to a level of the cellular structure.
1
BACKGROUND ARTS
Until now the hydrolysis has been performed so that the matter was transported from the receiving trough to the crusher in which the raw material was crushed to the required size. Raw material was transported from the crusher by means of the pump to the heat exchanger, where the raw material was heated to the required temperature. The heated raw material was transported to the retaining container to be kept for a period of one hour, resulting in the raw material pasteurization. After that the material was pumped off by means of a pump to the fermenter and the whole cycle was repeated.
The system drawback consisted in that the raw material was not perfectly disturbed / crushed, which resulted in the reduced methane production, and the period of keeping the raw material in the retaining container could not be shortened.
DISCLOSURE OF INVENTION
The above deficiencies are eliminated by the equipment for the discontinuous or continuous hydrolysis of organic matter, i.e. according to this invention, the substance of which consists in that the equipment for discontinuous hydrolysis consists of the receiving trough connected to the crusher, to which the measurement tank is connected. The latter is connected to the hydrolyzer interconnected via the overshooting pipe to the expander with the connected pipe to discharge waste vapours, connected to the condenser to which the pipe conducting cooling medium is connected, as well as the pipe of the cooling medium outlet and the pipe to conduct waste condensate and not condensed gases. This pipe is further connected to the degasifierto which the fan to suck not condensed gases is connected, as well as the pipe of waste condensate connected to the expander, to which the pump of boiled matter, interconnected with the fermenter, connected Hydrolyser is designed with the connected pipe to feed the steam and the pipe to discharge the steam condensate.
The equipment is conveniently interconnected with the pump of boiled matter to the input raw material cooler, to which the supply pipe of water heating circuit, discharge pipe and cooled material pipe are conducted. The supply and discharge pipes of the water heating circuit are connected to the input raw material pre-heater, interconnected between the crusher and the measuring tank.
i The equipment for continuous hydrolysis consists of the receiving trough interconnected with the crusher with the connected pump of crushed raw material, which is connected to the inter-container connected by high-pressure pump to the hydrolyser. The hydrolyser is connected to the heat source via the fume conduit to the stack. The hydrolyser is further connected via the overshooting pipe to the counter-pressure head , connected with the pipe to discharge waste vapours to the condenser designed for the cooling medium inlet and outlet and the pipe to discharge waste condensate and not condensed gases, which is connected to the degasifier, to which the fan and waste condensate pipe, connected to the shower head, are connected. Expander is connected via the boiled matter pump to the fermenter.
The equipment is conveniently designed connected after the boiled matter pump with the output raw material cooler connected to the supply and discharge pipes of the water heating circuit to the inlet raw material pre-heater and the connected pipe for the cooled material, brought out to the fermenter.
The biggest advantages of the above equipment include the fact that the raw material is completely destroyed during its operation to a level of cellular structure, so that more methane is obtained from such significantly decomposed matter and the period of keeping the matter in the fermenter is reduced.
BRIEF DESCRIPTION OF DRAWINGS
The invention will be clarified more in detail by means of the drawings, among which Fig. 1 shows the discontinuous plant without the preheating of input raw material, Fig. 2 shows the plant with the preheating of input raw material, Fig. 3 shows the continuous process utilizing the thermal source waste gases and the counter-pressure head to accelerate the technologic process. Fig. 4 shows utilization of the heating medium during the raw material pre-heating.
MADE FOR CARRING OUT THE INVENTION
Example 1
The equipment for the discontinuous or continuous hydrolysis of organic matter according to Fig. 1 and Fig. 2 consists of the of the receiving trough 1 connected to the crusher 2, to which the measurement tank 16 is connected, and further connected to the hydrolyzer 3 interconnected via the overshooting pipe 12 to the expander 13 with the connected pipe 4 to discharge waste vapours, connected to the condenser 5. to which the pipe 6 conducting cooling medium is connected, as well as the pipe 7 of the cooling medium outlet and the pipe 8 to conduct waste condensate and not condensed gases. This pipe is further connected to the degasifier 9 to which the fan H to suck not condensed gases is connected, as well as the pipe 10 of waste condensate connected to the expander 13, to which the pump 14' of boiled matter interconnected with the fermenter 15 is connected. Hydrolyser 3 is designed with the connected pipe 1_7 to feed the steam and the pipe 18 to discharge the steam condensate from the hydrolyzer 3. The equipment for the discontinuous hydrolysis of organic matter is designed with the pipe 14 of boiled material connected to the cooler 19 of output raw material, to which the supply pipe 21 of water heating circuit, discharge pipe 20 of water heating circuit and pipe 23 of cooled material are connected, and both the pipes 20 and 21 are connected to the pre-heater 22 of the input raw material, interconnected between the crusher 2 and the measurement tank 16.
Example 2
The equipment for the continuous hydrolysis of organic matter according to Fig. 3 and Fig. 4 consists of the receiving trough 1 connected to the crusher 2 with the connected pump 24 of crushed raw material, which is connected to the inter-container 25 connected by high-pressure pump 26 to the hydrolyser 3. The hydrolyser 3 is connected to the heat source 27 via the waste gases conduit 28 to the stack 30. The hydrolyser is further connected via the overshooting pipe 12 to the counter-pressure head 29, connected via the pipe 4 to discharge the waste vapours to the condenser 5 designed with the pipe 6 of the cooling medium inlet and the pipe 7 of the cooling medium outlet and the pipe 8 to discharge waste condensate and not condensed gases, which is connected to the degasifier 9, to which the fan H and waste condensate pipe 10 , connected to the shower head 31, are connected. Expander 13 is connected via the boiled matter pump 14 of boiler material to the fermenter 15. The equipment for the continuous hydrolysis of organic matter is designed with the pump 14 of boiler material connected to the cooler 19 of output raw material, into which the supply pipe 21 of water heating circuit, discharge pipe 20 of water heating circuit and pipe 23 of cooled material are connected, and both the pipes 20 and 21_are connected to the pre-heater 22 of the input raw material, and connected to the pipe 23 for the cooled material, brought out to the fermenterlδ.

Claims

PATENT CLAIMS
1. Equipment for discontinuous hydrolysis of organic matter distinguished by that it consists of the of the receiving trough (1) connected to the crusher (2) to which the measurement tank (16) is connected, and further connected to the hydrolyzer (3) interconnected via the overshooting pipe (12) to the expander (13) with the connected pipe (4) to discharge waste vapours, connected to the condenser (5) to which the pipe (6) conducting cooling medium is connected, as well as the pipe (7) of the cooling medium outlet and the pipe (8) to conduct waste condensate and not condensed gases. This pipe is further connected to the degasifier (9) to which the fan (11) to suck not condensed gases is connected, as well as the pipe (10) of waste condensate connected to the expander(13), to which the pump (14) of boiled matter interconnected with the fermenter (15) is connected. Hydrolyser (3) is designed with the connected pipe (17) to feed the steam and the pipe 18 to discharge the steam condensate from the hydrolyzer 3^
2. Equipment for discontinuous hydrolysis of organic matter according to claim 1 distinguished by that the pump (14) of boiled material is connected to the cooler (19) of output raw material, to which the supply pipe (21) of water heating circuit, discharge pipe (20) of water heating circuit and pipe (23) of cooled material are connected, while both the pipes (20, 21) are connected to the pre-heater (22) of input raw material, which is interconnected between the crusher (2) and the measurement tank (16).
3. Equipment for continuous hydrolysis of organic matter distinguished by that it consists of the receiving trough (1) connected to the crusher (2) with the connected pump (24) of crushed raw material, which is connected to the inter-container (25) connected by high- pressure pump (26) to the hydrolyser (3). The hydrolyser (3) is connected to the heat source (27) via the waste gases conduit (28) to the stack(30). The hydrolyser is further connected via the overshooting pipe (12) to the counter-pressure head (29), connected via the pipe {4} to discharge the waste vapours to the condenser (5) designed with the pipe (6) of the cooling medium inlet and the pipe (7) of the cooling medium outlet and the pipe (8) to discharge waste condensate and not condensed gases, which is connected to the degasifier (9), to which the fan (11) and waste condensate pipe (10) . connected to the shower head (31), are connected. Expander (13) is connected via the boiled matter pump (14) to the fermenter 15.
4. Equipment for continuous hydrolysis of organic matter distinguished by that the cooler (19) of output raw mineral is connected after the pump (14) of boiled material, with the connected supply and discharge pipes (20, 21) of water heating circuit to the pre-heater (22) of input raw material and the connected pipe (23) for cooled material, brought out to the fermenter (15).
PCT/CZ2007/000073 2006-07-24 2007-07-20 Equipment for the discontinuous or continuous hydrolysis of organic matter Ceased WO2008011839A2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN2007800341767A CN101517062B (en) 2006-07-24 2007-07-20 Equipment for the discontinuous or continuous hydrolysis of organic matter
EP07785500A EP2049648A2 (en) 2006-07-24 2007-07-20 Equipment for the discontinuous or continuous hydrolysis of organic matter

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CZPUV2006-17956 2006-07-24
CZ200617956U CZ17066U1 (en) 2006-07-24 2006-07-24 Apparatus for discontinuous and continuous hydrolysis of organic material

Publications (2)

Publication Number Publication Date
WO2008011839A2 true WO2008011839A2 (en) 2008-01-31
WO2008011839A3 WO2008011839A3 (en) 2008-03-27

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PCT/CZ2007/000073 Ceased WO2008011839A2 (en) 2006-07-24 2007-07-20 Equipment for the discontinuous or continuous hydrolysis of organic matter

Country Status (5)

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EP (1) EP2049648A2 (en)
CN (1) CN101517062B (en)
CZ (1) CZ17066U1 (en)
RU (1) RU2426777C2 (en)
WO (1) WO2008011839A2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2177280A2 (en) 2008-10-16 2010-04-21 Hermann Dauser Method and device for discontinuous hydrolysis of organic substrates
DE202011003234U1 (en) 2010-12-13 2011-08-11 WGM Winter Gerätebau und Metallverarbeitung GmbH Fire door
AT509319A4 (en) * 2010-05-25 2011-08-15 Biogas Systems Gmbh METHOD AND DEVICE FOR HYDROLYSIS OF PREFERABLY SOLID, ORGANIC SUBSTRATES
ITTO20130914A1 (en) * 2013-11-12 2014-02-11 Lucio Sanasi THERMAL HYDROLISER FOR ORGANIC SUBSTANCE AGENT AT TEMPERATURE, PRESSURE AND AGITATION WITH THE COMBINATION OF THE DISMANTLING OF THE ORGANIC MATERIAL, SUCH AS TO MAKE IT READY FOR FAST BIO-MANAGEMENT. THE ACHIEVEMENT OF TEMPERATURE COMES OPT
WO2021102498A1 (en) * 2019-11-29 2021-06-03 Leinich Beteiligungen Gmbh Method and plant for obtaining cellulose fibres

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CN102021252B (en) * 2010-12-21 2013-02-27 山东省鲁洲食品集团有限公司 Method and device for continuously hydrolyzing corn bran
FR3003558B1 (en) * 2013-03-25 2015-04-24 Veolia Water Solutions & Tech METHOD AND DEVICE FOR CONTINUOUS THERMAL HYDROLYSIS
FR3010403B1 (en) * 2013-09-06 2017-01-13 Veolia Water Solutions & Tech METHOD AND DEVICE FOR CONTINUOUS THERMAL HYDROLYSIS WITH RECIRCULATION STEAM RECIRCULATION
CN107513497A (en) * 2017-10-10 2017-12-26 杭州同孚环保科技有限公司 A kind of bionical reactor temperature control system of multisection type

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2040138C1 (en) * 1992-09-02 1995-07-25 Римма Павловна Наумова Manure processing plant
CZ281504B6 (en) * 1995-02-08 1996-10-16 Zdeněk Kratochvíl Process of treating ligno-cellulosic materials by continuous pressure hydrolysis and apparatus for making the same
RU2162626C1 (en) * 1999-06-28 2001-02-10 Андрюхин Тимофей Яковлевич Method and apparatus for sequential phase-by-phase anaerobic fermentation of liquid organic wastes
CN1114696C (en) * 2000-06-02 2003-07-16 唐山市冀东溶剂厂 Process for producing alcohol with xylose slag
CN1114695C (en) * 2000-06-02 2003-07-16 唐山市冀东溶剂厂 Method for producing alcohol by using plant fiber as raw material
US6905600B2 (en) * 2001-11-16 2005-06-14 Ch2M Hill, Inc. Method and apparatus for the treatment of particulate biodegradable organic waste
RU2279325C2 (en) * 2002-06-06 2006-07-10 Государственное научное учреждение Всероссийский научно-исследовательский институт сельскохозяйственной микробиологии (ГНУ ВНИИСХМ Россельхозакадемии) Method of obtaining microbial preparation for disposal of pesticides, pesticide disposal process (options), and pesticide disposal apparatus
US7015028B2 (en) * 2003-04-30 2006-03-21 Alta Environmental Services, Inc. Process for treatment of organic waste materials
EP1836181B1 (en) * 2004-08-31 2009-03-11 Biomass Technology Ltd. Method and devices for the continuous processing of renewable raw materials

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2177280A2 (en) 2008-10-16 2010-04-21 Hermann Dauser Method and device for discontinuous hydrolysis of organic substrates
EP2177280A3 (en) * 2008-10-16 2011-06-15 Systems Gmbh Biogas Method and device for discontinuous hydrolysis of organic substrates
AT509319A4 (en) * 2010-05-25 2011-08-15 Biogas Systems Gmbh METHOD AND DEVICE FOR HYDROLYSIS OF PREFERABLY SOLID, ORGANIC SUBSTRATES
AT509319B1 (en) * 2010-05-25 2011-08-15 Biogas Systems Gmbh METHOD AND DEVICE FOR HYDROLYSIS OF PREFERABLY SOLID, ORGANIC SUBSTRATES
WO2011147601A1 (en) 2010-05-25 2011-12-01 Biogas Systems Gmbh Method and device for the hydrolysis of preferably solid organic substrates
RU2566997C2 (en) * 2010-05-25 2015-10-27 Биогаз Системз Гмбх Method and device for hydrolysis of preferably solid organic substrates
DE202011003234U1 (en) 2010-12-13 2011-08-11 WGM Winter Gerätebau und Metallverarbeitung GmbH Fire door
DE102011087859A1 (en) 2010-12-13 2012-06-14 WGM Winter Gerätebau und Metallverarbeitung GmbH Fire protection door for protecting e.g. motorway tunnel against fire of high mechanical/thermal loading, has anchor for forming form-fit stop, where deformation forces are discharged by door hinges and reinforcement elements in anchor
ITTO20130914A1 (en) * 2013-11-12 2014-02-11 Lucio Sanasi THERMAL HYDROLISER FOR ORGANIC SUBSTANCE AGENT AT TEMPERATURE, PRESSURE AND AGITATION WITH THE COMBINATION OF THE DISMANTLING OF THE ORGANIC MATERIAL, SUCH AS TO MAKE IT READY FOR FAST BIO-MANAGEMENT. THE ACHIEVEMENT OF TEMPERATURE COMES OPT
WO2021102498A1 (en) * 2019-11-29 2021-06-03 Leinich Beteiligungen Gmbh Method and plant for obtaining cellulose fibres

Also Published As

Publication number Publication date
CN101517062A (en) 2009-08-26
RU2426777C2 (en) 2011-08-20
WO2008011839A3 (en) 2008-03-27
EP2049648A2 (en) 2009-04-22
CZ17066U1 (en) 2006-12-12
CN101517062B (en) 2012-08-29
RU2009107019A (en) 2010-08-27

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