CN202322829U - Circularly-heating insulation system of high-temperature dry type anaerobic fermentation device - Google Patents

Circularly-heating insulation system of high-temperature dry type anaerobic fermentation device Download PDF

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Publication number
CN202322829U
CN202322829U CN 201120464131 CN201120464131U CN202322829U CN 202322829 U CN202322829 U CN 202322829U CN 201120464131 CN201120464131 CN 201120464131 CN 201120464131 U CN201120464131 U CN 201120464131U CN 202322829 U CN202322829 U CN 202322829U
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China
Prior art keywords
pipe
interchanger
water
anaerobic fermentation
type anaerobic
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Expired - Lifetime
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CN 201120464131
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Chinese (zh)
Inventor
陈玉鹏
巴云鹏
程红清
燕维贤
黄兴
季刚
范树平
谢晨光
苏沛仁
杨凤霞
杨发勇
钱家梅
孙惠伟
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Yunnan Kunming Shipbuilding Equipment Environmental Protection Technology Co., Ltd.
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YUNNAN KUNCHUAN 2ND MACHINERY CO Ltd
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Priority to CN 201120464131 priority Critical patent/CN202322829U/en
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS 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
    • C12M21/00Bioreactors or fermenters specially adapted for specific uses
    • C12M21/04Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS 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
    • C12M21/00Bioreactors or fermenters specially adapted for specific uses
    • C12M21/16Solid state fermenters, e.g. for koji production
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS 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
    • C12M41/00Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/12Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS 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
    • C12M41/00Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/12Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
    • C12M41/18Heat exchange systems, e.g. heat jackets or outer envelopes

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Zoology (AREA)
  • Genetics & Genomics (AREA)
  • Microbiology (AREA)
  • General Health & Medical Sciences (AREA)
  • Sustainable Development (AREA)
  • Biotechnology (AREA)
  • Biomedical Technology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • Molecular Biology (AREA)
  • Physics & Mathematics (AREA)
  • Analytical Chemistry (AREA)
  • Thermal Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Treatment Of Sludge (AREA)

Abstract

The utility model discloses a circularly-heating insulation system of a high-temperature dry type anaerobic fermentation device. The system comprises a cold water tank (1), an air source heat pump (2), a thermal insulation water tank (3), a heat radiator (5) and a heat exchanger (6) which are sequentially connected through a water pipe (7), wherein the heat radiator (5) is arranged in a fermentation tank (4); a backflow water pipe (8) is connected between the air source heat pump (2) and the thermal insulation water tank (3), the thermal insulation water tank (3) is respectively connected with a heat radiator water inlet pipe (9) and a heat radiator water outlet pipe (10) which are connected with the heat radiator (5), and a heat exchanger water inlet pipe (11) and a heat exchanger water outlet pipe (12) which are connected with the heat exchanger (6); and the heat exchanger (6) is also connected with a biogas slurry feeding pipe (13) and a biogas slurry discharging pipe (14) which are connected with the fermentation tank. The circularly-heating insulation system can be used for efficiently and rapidly carrying out heating and thermal insulation on organic matters in the organic matter high-temperature dry type anaerobic fermentation device, and is flexibly and convenient arranged in the high-temperature dry type anaerobic fermentation device.

Description

A kind of circulation heat tracing system of high temperature dry-type anaerobic fermentation device
Technical field
The utility model relates to the biogas fermentation technical field, particularly a kind of hot water circulation heating system of organic waste high temperature dry-type anaerobic fermentation device.
Background technology
The dry-type anaerobic fermentation technology has the high characteristics of fermented product solid holdup, than the wet type anaerobic fermentation technology, has advantages such as organic loading height, factor of created gase is high, floor space is little, energy consumption is low, the tunning after-treatment system is simple.Generally be divided into normal temperature fermentation (10~26 ℃), mesophilic digestion (28~38 ℃), thermophilic fermentation (45~60 ℃) according to leavening temperature.Temperature is all influential to the speed and the degree of anaerobic digestion; When temperature is lower than optimum lower limit temperature; 1 ℃ of digestion rate of every decline descends 11%, and temperature not only limits the speed of aerogenesis to the influence of anaerobic digestion process, and influences the anaerobic digestion degree; When wherein adopting thermophilic fermentation, organism decomposes soon, aerogenesis is also the fastest.If make the long-term steady running of biogas fermentation, must take the temperature raising and maintaining measure, leavening temperature is not changed, to keep constant, competent gas production rate with outside air temperature.
Existing fermentation unit heating system adopts the tubular type heating mostly, and is high for dry-type anaerobic fermentation reaction mass viscosity, and the characteristics that thermal conductivity is low can not be efficiently fast to material heating and insulation.
Summary of the invention
The utility model be the deficiency that solves prior art, for organism high temperature dry-type anaerobic fermentation device provide a kind of can be efficiently fast to the organism heating and be incubated and in fermentation unit, be provided with flexible circular heating heat-insulation system.
The purpose of the utility model realizes through following technical scheme.
A kind of circulation heat tracing system of high temperature dry-type anaerobic fermentation device comprises the cold water storage cistern, air source heat pump, attemperater, groups of fins, the interchanger that are linked in sequence through water pipe; Groups of fins is arranged in the fermentor tank; Between air source heat pump and attemperater, also be connected with the backflow water pipe, attemperater respectively with the radiator inleting pipe that is connected scatterer and radiator outlet pipe and the interchanger water inlet pipe and the interchanger rising pipe that are connected interchanger; Interchanger also is connected with natural pond liquid extraction line with the natural pond liquid feed-pipe that is connected fermentor tank.
Cold water storage cistern provides air source heat pump work required cold water, gets into air source heat pump through water pipe by cold water storage cistern, and air source heat pump heats cold water; Hot water gets into attemperater; If it is temperature required that the interior hot water of attemperater is lower than, get into air source heat pump circulation heating through the backflow water pipe, the hot water in the attemperater gets into scatterer through the connection water pipe; Hot water is back to attemperater through radiator outlet pipe after getting into scatterer through radiator inleting pipe again.When interchanger is worked; Hot water in the attemperater gets into interchanger through the interchanger water inlet pipe; Be back to attemperater through the interchanger rising pipe, the natural pond liquid in the fermentor tank 4 flow to interchanger through natural pond liquid extraction line, through the liquid feed-pipe is back in the fermentor tank through the natural pond again after the heating.
The utility model is connected and work through air source heat pump, attemperater, scatterer and the reasonable of interchanger; The heat energy that utilizes air source heat pump to provide; Both can realize insulation through the work of fermentor tank inner radiator to environment in the fermentor tank; Can liquid circulation in natural pond be heated through the work of interchanger again, thus efficient fast to heating of the material in the fermentor tank and insulation.
Further set forth the content of the utility model below in conjunction with Figure of description.
Description of drawings
Fig. 1 is the system architecture synoptic diagram of the utility model.
Embodiment
As shown in Figure 1, a kind of circulation heat tracing system of high temperature dry-type anaerobic fermentation device comprises the cold water storage cistern 1, air source heat pump 2, attemperater 3, scatterer 5, the interchanger 6 that are linked in sequence through water pipe 7.Scatterer 5 is arranged in the fermentor tank 4, and scatterer can be according to the inner tank wall shape, and each zone needs the difference of temperature, arranges in groups that in tank body present embodiment is furnished with four groups of scatterers in fermentor tank.Between air source heat pump 2 and attemperater 3, also be connected with backflow water pipe 8, attemperater 3 respectively with the radiator inleting pipe that is connected scatterer 59 and radiator outlet pipe 10 and the interchanger water inlet pipe 11 and interchanger rising pipe 12 that are connected interchanger 6; Interchanger 6 also is connected with natural pond liquid extraction line 14 with the natural pond liquid feed-pipe 13 that is connected fermentor tank.
During work, cold water storage cistern 1 provides air source heat pump 2 work required cold water, gets into air source heat pump through water pipe by cold water storage cistern; Air source heat pump heats cold water; Hot water gets into attemperater 3, and is temperature required if the interior hot water of attemperater is lower than, and gets into air source heat pumps circulation heating through backflow water pipe 8; Hot water in the attemperater is back to attemperater through radiator outlet pipe 10 after advancing 9 water pipes entering scatterer through scatterer again.When interchanger 6 work, the hot water in the attemperater gets into interchanger through interchanger water inlet pipe 11, is back to attemperater through interchanger rising pipe 12.Natural pond liquid in the fermentor tank 4 flow to interchanger through natural pond liquid extraction line 14, through liquid feed-pipe 13 is back in the fermentor tank through the natural pond again after the heating.Realize the insulation of fermentor tank and the circulation heating of natural pond liquid with this.

Claims (1)

1. the circulation heat tracing system of a high temperature dry-type anaerobic fermentation device is characterized in that, comprises the cold water storage cistern (1), air source heat pump (2), attemperater (3), scatterer (5), the interchanger (6) that are linked in sequence through water pipe (7); Scatterer (5) is arranged in the fermentor tank (4); Between air source heat pump (2) and attemperater (3), also be connected with backflow water pipe (8), attemperater (3) respectively with the radiator inleting pipe that is connected scatterer (5) (9) and radiator outlet pipe (10) and the interchanger water inlet pipe (11) and the interchanger rising pipe (12) that are connected interchanger (6); Interchanger (6) also is connected with natural pond liquid extraction line (14) with the natural pond liquid feed-pipe (13) that is connected fermentor tank.
CN 201120464131 2011-11-21 2011-11-21 Circularly-heating insulation system of high-temperature dry type anaerobic fermentation device Expired - Lifetime CN202322829U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201120464131 CN202322829U (en) 2011-11-21 2011-11-21 Circularly-heating insulation system of high-temperature dry type anaerobic fermentation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201120464131 CN202322829U (en) 2011-11-21 2011-11-21 Circularly-heating insulation system of high-temperature dry type anaerobic fermentation device

Publications (1)

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CN202322829U true CN202322829U (en) 2012-07-11

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103435162A (en) * 2013-09-04 2013-12-11 武汉兴天宇环境工程有限公司 Method for treating organic wastewater by anaerobic-aerobic combined process
CN104478510A (en) * 2014-12-22 2015-04-01 遵义联谷农业科技有限公司 Organic fertilizer fermentation device capable of utilizing energy step by step
CN113405273A (en) * 2021-05-18 2021-09-17 昆明理工大学 Biomass source heat pump system with gas compensation function and use method thereof
CN115044466A (en) * 2022-06-23 2022-09-13 南通凯赛生化工程设备有限公司 Horizontal anaerobic fermentation tank is with automatic heat preservation device and horizontal anaerobic fermentation tank

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103435162A (en) * 2013-09-04 2013-12-11 武汉兴天宇环境工程有限公司 Method for treating organic wastewater by anaerobic-aerobic combined process
CN103435162B (en) * 2013-09-04 2016-01-20 武汉兴天宇环境工程有限公司 A kind of method of anaerobic-aerobic combination process process organic waste water
CN104478510A (en) * 2014-12-22 2015-04-01 遵义联谷农业科技有限公司 Organic fertilizer fermentation device capable of utilizing energy step by step
CN113405273A (en) * 2021-05-18 2021-09-17 昆明理工大学 Biomass source heat pump system with gas compensation function and use method thereof
CN115044466A (en) * 2022-06-23 2022-09-13 南通凯赛生化工程设备有限公司 Horizontal anaerobic fermentation tank is with automatic heat preservation device and horizontal anaerobic fermentation tank
CN115044466B (en) * 2022-06-23 2023-09-29 南通凯赛生化工程设备有限公司 Automatic heat preservation device for horizontal anaerobic fermentation tank and horizontal anaerobic fermentation tank

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C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20180622

Address after: 650236 Kunqu Industrial Zone, eastern suburb of Guandu, Kunming, Yunnan

Patentee after: Yunnan Kunming Shipbuilding Equipment Environmental Protection Technology Co., Ltd.

Address before: 650236 Kunqu Industrial Zone, eastern suburb of Guandu, Kunming, Yunnan

Patentee before: Yunnan Kunchuan 2nd Machinery Co., Ltd.

CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20120711