CN102153196A - Heating type integrated sewage treatment device - Google Patents
Heating type integrated sewage treatment device Download PDFInfo
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- CN102153196A CN102153196A CN2011100870665A CN201110087066A CN102153196A CN 102153196 A CN102153196 A CN 102153196A CN 2011100870665 A CN2011100870665 A CN 2011100870665A CN 201110087066 A CN201110087066 A CN 201110087066A CN 102153196 A CN102153196 A CN 102153196A
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- reactor
- methane
- flow deflector
- acidification pool
- methane pond
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- 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
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- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
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- Treatment Of Sludge (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The invention discloses a heating type integrated sewage treatment device. In the sewage treatment device, a reactor (1) is divided to a hydrolysis-acidification tank (1a), a methane-producing tank (1b) and a transition zone (1c) by baffles (6) which are arranged longitudinally, wherein the upper part of the hydrolysis-acidification tank (1a) is communicated with the lower part of the methane-producing tank (1b) through the transition zone (1c); and the sewage treatment device also comprises a mixer (7) and a solar heat transfer system (8). By adopting the device disclosed by the invention, hydrolysis-acidification and methane producing are combined in a reactor; the transition zone is arranged between the hydrolysis-acidification tank and the methane-producing tank to ensure that sewage can flow into the lower part of the methane-producing tank from top to bottom; and the solar heat transfer system is combined, thus the sewage temperature can be increased, the mass transfer effect between sludge and water can be increased, and the device is good for acid-producing bacteria and methanogens and is very energy-saving and environmentally friendly.
Description
Technical field
The present invention relates to the anaerobic waste water biologic treating technique, concretely, is a kind of new and effective two-phase integrated sewage treating apparatus.
Background technology
Traditional diphasic anaerobic reaction process is divided into acidication and produces two processes of methane, and these two process needs carry out in two independent reactors respectively.The acidication process is mainly the biodegradability that improves matrix, provides suitable matrix for producing methane; Producing methane and mainly be the substrate conversion that acidization provides is methane, and both constitute the diphasic anaerobic reaction process jointly.
At present, the two-phase integral anaerobic reactor is a kind of new and effective anaerobic waste water treatment facility, acidifying and two technologies of product methane are finished in a reactor, its decoration form commonly used is vertical or telescoping structure, exists problems such as complex structure, installation difficulty are big, mass transfer effect difference; On the other hand, sewage directly inserts acidification pool by pipeline, and especially in temperature lower winter, the sewage water temperature is on the low side to be unfavorable for the generation of acidifying bacterium the treatment effect of reactor being reduced greatly.
Summary of the invention
The object of the present invention is to provide a kind of simple in structure, mass transfer effect good, processing power is strong two-phase integral anaerobic reactor.
For achieving the above object, the technical solution used in the present invention is: a kind of heating-type integrated sewage treating apparatus, comprise reactor (1), water-in (2), water outlet (3), gas collection mouth (4) and mud discharging mouth (5), key is: described reactor (1) is divided into hydrolysis acidification pool (1a) by the dividing plate (6) of vertical setting, produce methane pond (1b) and zone of transition (1c), the top of described hydrolysis acidification pool (1a) is communicated with by the bottom of described zone of transition (1c) with described product methane pond (1b), be provided with agitator (7) and coil pipe (8a) in the described hydrolysis acidification pool (1a), the solar heat-collection plate (8b) that described coil pipe (8a) is outer with being arranged on described reactor (1), pressure pump (8c) constitutes heat-exchange system (8) jointly, and the middle part in described product methane pond (1b) is provided with filler (11).
Anaerobic biological treatment is divided into acidication and produces two stages of methane, the present invention is by the reactor of integrated design, acidication with produce methane and be combined in the reactor and finish, so can make the left part of reactor and the optimum growh environment that right part satisfies acid-producing bacteria and methanogen respectively, in a reactor, realize producing acid phase and effective separation of producing the methane phase.Sewage enters acidification pool from water-in, under the stirring of agitator, carry out abundant heat exchange with the high temperature coil pipe, the rising of temperature helps sewage at the acidification pool acid-producing bacteria, flows into zone of transition from the top down through the acidification pool pretreated sewage, enters from the bottom of producing the methane pond and produces the methane pond; Discharge from the gas collection mouth through the methane gas that produces after the methane pond transforms, the sewage after handling is then discharged from water outlet, discharges by mud discharging mouth behind the sludge settling.Filler is used for attached microbial, forms microbial film, reduces the loss of reactor microorganism, strengthens the water outlet quality.
Described reactor (1) is cylindrical and have a bottom of back taper, totally two and be separately positioned on described hydrolysis acidification pool (1a) and produce methane pond (1b) bottom of described mud discharging mouths (5).Reactor is arranged to have the round shape of back taper bottom, helps mud and discharge, avoid forming the dead angle along the scarp precipitation of back taper bottom and through two mud discharging mouths; Simultaneously, the reactor good looking appearance, and make things convenient for monolithic molding.
The position that described zone of transition (3) is communicated with described product methane pond (1b) is provided with first flow deflector (9) and second flow deflector (10), the lower end of described first flow deflector (9) tilts towards described product methane pond (1b), and described second flow deflector (10) is horizontally installed on the below of first flow deflector (9).Two flow deflectors are arranged on zone of transition and produce the position that the methane pond is communicated with, and sewage has been played good guide functions, have avoided sewage to be deposited on reactor bottom and have formed stagnant water.
As preferably, described heat-exchange system (8) also comprises temperature control meter (8d) and coil pipe support (8e), the coil pipe support is used to support coil pipe is stabilized in the hydrolysis acidification pool it, the temperature control meter is used to control sewage and is in all the time in the suitable water temperature range, avoid the water temperature rapid drawdown that rises sharply, fluctuation is too big and influence the growth of acidifying bacterium.
Beneficial effect of the present invention:
1) place same reactor to finish acid-producing bacteria and methanogen, reduced reactor quantity, solved traditional diphasic anaerobic technique owing to the construction of adopting two separate reactors to cause and working cost height, problem that floor space is big, thereby whole construction costs and maintenance cost are obviously reduced.
2) zone of transition by being provided with between hydrolysis acidification pool and product methane pond makes sewage flow into the bottom of producing the methane pond from top to bottom, improves the mass transfer effect between mud and the water, improves reaction efficiency;
3) absorb heat to improve sewage temperature by solar heat-collection plate, help acid-producing bacteria and methanogen, increase the biomass of two technological processs, further improve effluent quality, and very energy-conserving and environment-protective.
In sum, simple in structure, advantages such as mass transfer effect good, processing power is strong, energy-conserving and environment-protective that the present invention has have vast market prospect.
Description of drawings
Fig. 1 is a structural representation of the present invention.
Embodiment
The invention will be further described below in conjunction with drawings and Examples:
Heating-type integrated sewage treating apparatus as shown in Figure 1 is made of reactor 1, water-in 2, water outlet 3, gas collection mouth 4, mud discharging mouth 5, agitator 7 and heat-exchange system 8 etc.Heat-exchange system 8 is made up of coil pipe 8a, solar heat-collection plate 8b and pressure pump 8c, preferably also comprises temperature control meter 8d and coil pipe support 8e.Reactor 1 is divided into hydrolysis acidification pool 1a, is produced methane pond 1b and zone of transition 1c by the dividing plate 6 of vertical setting, and left cavity is hydrolysis acidification pool 1a, and right cavity is for producing methane pond 1b, and zone of transition 1c is between hydrolysis acidification pool 1a and product methane pond 1b.Be provided with agitator 7, coil pipe 8a in the hydrolysis acidification pool 1a and be used to support the coil pipe support 8e of coil pipe 8a.The middle part of producing methane pond 1b is provided with filler 11, and water-in 2 is arranged on the sidewall of hydrolysis acidification pool 1a, and water outlet 3 is arranged on the sidewall that produces methane pond 1b, and gas collection mouth 4 is arranged on the top of producing methane pond 1b.
The top of hydrolysis acidification pool 1a is communicated with the bottom of producing methane pond 1b by zone of transition 1c, and the sewage of hydrolysis acidification pool 1a flows into the bottom of producing methane pond 1b through zone of transition 1c from top to bottom.Solar heat-collection plate 8b, pressure pump 8c and temperature control meter 8d are arranged on outside the reactor 1, the inductive head of temperature control meter 8d extend into and is used to measure sewage temperature in the hydrolysis acidification pool 1a, and give pressure pump 8c with signal feedback, with the heat transfer rate of sewage in control coil pipe 8a and the hydrolysis acidification pool 1a.Reactor 1 is whole cylindrical and have a bottom of back taper, totally two and be separately positioned on hydrolysis acidification pool 1a and produce methane pond 1b bottom of mud discharging mouths 5.
As preferably, be provided with first flow deflector 9 and second flow deflector 10 in zone of transition 3 with the position that product methane pond 1b is communicated with, the lower end of first flow deflector 9 tilts towards producing methane pond 1b, second flow deflector 10 is horizontally installed on the below of first flow deflector 9, and the sewage of zone of transition 3 flows into the bottom of producing methane pond 1b through the flow-guiding channel of the common formation of first flow deflector 9 and second flow deflector 10.Current route in the reactor 1 is shown in arrow among the figure.
Claims (4)
1. heating-type integrated sewage treating apparatus, comprise reactor (1), water-in (2), water outlet (3), gas collection mouth (4) and mud discharging mouth (5), it is characterized in that: described reactor (1) is divided into hydrolysis acidification pool (1a) by the dividing plate (6) of vertical setting, produce methane pond (1b) and zone of transition (1c), the top of described hydrolysis acidification pool (1a) is communicated with by the bottom of described zone of transition (1c) with described product methane pond (1b), be provided with agitator (7) and coil pipe (8a) in the described hydrolysis acidification pool (1a), the solar heat-collection plate (8b) that described coil pipe (8a) is outer with being arranged on described reactor (1), pressure pump (8c) constitutes heat-exchange system (8) jointly, and the middle part in described product methane pond (1b) is provided with filler (11).
2. according to the described heating-type integrated sewage treating apparatus of claim 1, it is characterized in that: described reactor (1) is cylindrical and have a bottom of back taper, totally two and be separately positioned on described hydrolysis acidification pool (1a) and produce methane pond (1b) bottom of described mud discharging mouths (5).
3. according to the described heating-type integrated sewage treating apparatus of claim 1, it is characterized in that: the position that described zone of transition (3) is communicated with described product methane pond (1b) is provided with first flow deflector (9) and second flow deflector (10), the lower end of described first flow deflector (9) tilts towards described product methane pond (1b), and described second flow deflector (10) is horizontally installed on the below of first flow deflector (9).
4. according to the described heating-type integrated sewage treating apparatus of claim 1, it is characterized in that: described heat-exchange system (8) also comprises temperature control meter (8d) and coil pipe support (8e).
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CN2011100870665A CN102153196B (en) | 2011-04-08 | 2011-04-08 | Heating type integrated sewage treatment device |
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CN2011100870665A CN102153196B (en) | 2011-04-08 | 2011-04-08 | Heating type integrated sewage treatment device |
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CN102153196B CN102153196B (en) | 2012-07-25 |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105016485A (en) * | 2015-07-14 | 2015-11-04 | 顾瑞芳 | Biomembrane heating device in sewage treatment biochemistry pond |
CN106336042A (en) * | 2016-10-31 | 2017-01-18 | 威德环境科技股份有限公司 | Biological kitchen waste biogas slurry curing treatment system |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IT1172943B (en) * | 1982-12-08 | 1987-06-18 | Maurice Guerin | CONTINUOUS DIGESTORE FOR THE PRODUCTION OF BIOMETHANE FROM ORGANIC SUBSTANCES |
EP0335825B1 (en) * | 1988-03-23 | 1992-09-02 | MANNESMANN Aktiengesellschaft | Process and device for a two-step anaerobic treatment of liquid substrates |
CN2420272Y (en) * | 2000-03-11 | 2001-02-21 | 任南琪 | Integrated two phase anaerobe treatment reactor |
CN101172737A (en) * | 2007-10-17 | 2008-05-07 | 哈尔滨工程大学 | Integrated high concentration difficult degradable sewage processor |
CN101429480A (en) * | 2008-12-18 | 2009-05-13 | 新疆西域牧歌农业科技有限公司 | Method and apparatus for fermentation production of sludge gas with mixed stalk raw material |
CN201330193Y (en) * | 2008-11-11 | 2009-10-21 | 林英姿 | Integrated two-phase anaerobic reactor |
CN201501814U (en) * | 2009-09-29 | 2010-06-09 | 河北农业大学 | Solar anaerobic granular sludge circulating reactor |
CN101948175A (en) * | 2010-09-15 | 2011-01-19 | 崔勇 | Automatic modular anaerobic and aerobic fermentation device |
-
2011
- 2011-04-08 CN CN2011100870665A patent/CN102153196B/en not_active Expired - Fee Related
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IT1172943B (en) * | 1982-12-08 | 1987-06-18 | Maurice Guerin | CONTINUOUS DIGESTORE FOR THE PRODUCTION OF BIOMETHANE FROM ORGANIC SUBSTANCES |
EP0335825B1 (en) * | 1988-03-23 | 1992-09-02 | MANNESMANN Aktiengesellschaft | Process and device for a two-step anaerobic treatment of liquid substrates |
CN2420272Y (en) * | 2000-03-11 | 2001-02-21 | 任南琪 | Integrated two phase anaerobe treatment reactor |
CN101172737A (en) * | 2007-10-17 | 2008-05-07 | 哈尔滨工程大学 | Integrated high concentration difficult degradable sewage processor |
CN201330193Y (en) * | 2008-11-11 | 2009-10-21 | 林英姿 | Integrated two-phase anaerobic reactor |
CN101429480A (en) * | 2008-12-18 | 2009-05-13 | 新疆西域牧歌农业科技有限公司 | Method and apparatus for fermentation production of sludge gas with mixed stalk raw material |
CN201501814U (en) * | 2009-09-29 | 2010-06-09 | 河北农业大学 | Solar anaerobic granular sludge circulating reactor |
CN101948175A (en) * | 2010-09-15 | 2011-01-19 | 崔勇 | Automatic modular anaerobic and aerobic fermentation device |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105016485A (en) * | 2015-07-14 | 2015-11-04 | 顾瑞芳 | Biomembrane heating device in sewage treatment biochemistry pond |
CN105016485B (en) * | 2015-07-14 | 2017-08-04 | 顾瑞芳 | Biological film heating device in biochemical waste water treatment pool |
CN106336042A (en) * | 2016-10-31 | 2017-01-18 | 威德环境科技股份有限公司 | Biological kitchen waste biogas slurry curing treatment system |
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