CN101148373A - Sludge aerobic composting reactor - Google Patents
Sludge aerobic composting reactor Download PDFInfo
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- CN101148373A CN101148373A CNA2007100094545A CN200710009454A CN101148373A CN 101148373 A CN101148373 A CN 101148373A CN A2007100094545 A CNA2007100094545 A CN A2007100094545A CN 200710009454 A CN200710009454 A CN 200710009454A CN 101148373 A CN101148373 A CN 101148373A
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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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
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Abstract
The present invention relates to aerobic sludge compost reactor, and is especially one kind of aerobic sludge compost reactor for utilizing high water content sludge. Technologically, the aerobic sludge compost reactor consists of one air controlling system, one stirring system, one fermentation tank system and one heating and temperature controlling system. The fermentation tank system consists of one inner tank and one outer tank, and has sludge inlet, compost outlet, sewage discharge port and manually controlled sewage discharging unit. The air controlling system comprising blower and vacuumizing machine is connected to the fermentation tank through pipeline. The stirring system consists of motor, link rod and stirring blades. The heating and temperature controlling system consists of ceramic casing, asbestos, temperature inductor and control circuit. The present invention has convenient use, low cost, no environmental pollution and other advantages.
Description
Technical field
The present invention relates to a kind of sludge composting technology, particularly relate to a kind of high water content sludge aerobic compost reactor that utilizes.
Background technology:
Mud (Sludge) is a kind of water ratio height (the liquid sludge water ratio can reach 99%), be the flow-like material of black or chocolate, generally the aggregate formed of the zoogloea that is formed by multiple microorganism and its adsorbed organic matter and inorganics.Mud is mainly derived from municipal sludge (Civil sludge, also be sewage sludge Sewage sludge,), pipe network mud, river and lake silt, industrial sludge, municipal sludge particularly, along with urbanization develops rapidly, urban sewage treatment system perfect, municipal sludge becomes a class mud of quantity maximum, becomes the key influence factor that urban construction and urban sewage treatment system are normally moved.Mud is the water ratio height not only, perishable, strong odor is arranged, also concentrated nutritive element, heavy metal and salt such as most organic matter, nitrogen phosphorus in the sewage, and a spot of pathogenic micro-organism and parasitic ovum etc., if not by rational treatment and disposal, these pollutents will directly enter environment, influence the appearance of the city, polluted-water and soil, even be detrimental to health.At present, the treatment and disposal of mud has become one of focus that environmental protection circle and municipal administration very pay close attention to.
Sludge compostingization is to rely on microorganisms such as bacterium in the mud, actinomycetes, fungi under certain artificial condition, controlledly promotes the Biochemical processes that biodegradable organism transforms to stable soil ulmin.Mud is through compost treatment, and volume generally can be reduced to the 50%-70% of original volume, and most of pathogenic bacteria and virus are killed.Mud is through behind the compost, the finished product that makes is called compost (Compost), it is that a class is brown, the very high bulk material of humus content as the peat, so be also referred to as " vegetable mould ", its stable in properties, can be used as soil improvement agent and carry out the soil utilization, realize the recycling of nutritive elements such as carbon source, nitrogen phosphorus in the mud.Therefore sludge compostingization is to realize sludge reduction, innoxious, stabilization and the comparatively effective a kind of treatment process of resource utilization.
Sludge compostingization can be divided into two kinds of anaerobic composting and aerobic composts by principle.Advantages such as aerobic compost is fast because of organism speed, and it is more abundant to degrade, and the compost cycle is short, and envrionment conditions is better and widespread use.Aerobic composting process is ripe relatively at present, according to having or not fermentation unit compositing system simply can be divided into open system and reactor assembly, the former can be divided into natural ventilation bar buttress formula system, passive air duct slats buttress system, forced ventilation static buttress system composting process again.The latter only adopts the box compost of simple type, and efficient is low, and level of automation is low.Because water content is high in the mud, it is extremely limited to adopt reactor assembly to carry out the quantity of compost, therefore, utilize mud to carry out the main employing open system of compost, promptly traditional artificial nature's composting mode, its composting process is as follows: the mud mummification of at first anhydrating, manually admix amendment, carry out aerobic fermentation, after the stage of becoming thoroughly decomposed, make composting production again.
Adopt traditional composting mode, yet cost is low, the floor area that takies is big, causes second environmental pollution easily; Adopt the box composting mode of simplification, still there is certain problem, mainly comprise: (1) moisture percentage in sewage sludge is too high, mud water ratio after processed generally still reaches 82%, and the suitable water ratio of sludge aerobic compost process is 50-65%, mud need pass through mummification, add a large amount of pre-treatment such as amendment before the compost, and this brings difficulty to practical engineering application, increases the expense of sludge composting; (2) there be the loss, particularly nitrogen of nutritions such as nitrogen, phosphorus in composting process, loses in a large number with volatilization and the filtrate loss form of N; (3) having certain heavy metal contamination in the mud, is one of key factor of restriction sludge composting soil utilization.
Summary of the invention
In view of existing these the three aspects restraining factors of mud, purpose of the present invention be exactly to design a kind of easy to use, the compost cost is low, the reactor of high water content sludge aerobic compost that environment is not polluted, and realize the aerobic compost of high water content sludge by this reactor, improve the sludge composting benefit, improve sludge composting product fertilizer efficiency, reduce sludge composting product heavy metal contamination risk.
The present invention is achieved through the following technical solutions: include the turnover air control system for air that gas blower and vacuum air pump constitute, the stirring system that electric motor, connecting rod, stirring blades constitute, the fermentor tank system of interior tank body and the nestable formation of outer tank body, the heating temperature controlling system that asbestos, temperature inductor, well heater and temperature-adjusting circuit constitute constitutes, and wherein: gas blower links to each other with device by the air-supply pipeline with vacuum suction; Electric motor is positioned at the device top, and stirring blades is positioned at the fermentation tank interior, and links to each other with electric motor by connecting rod; Asbestos, temperature inductor, electric stove wire interior tank body and outside between the tank body.
Tank body and outer tank body are cylindrical in the fermentor tank system, outer jar greater than interior jar, mutual nestable formation between them, be provided with sludge inlet, compost discharge port, Sewage outlet, manual sewage discharge device formation therebetween, wherein inside and outside wall is made of by the punching press welding metal sheet, and the bottom surface of inwall is provided with latticed sewage discharge hole; Funnelform sludge inlet is located at tank wall top, and the compost discharge port that is equipped with hermatic door and discharging guiding groove is located at the tank wall bottom, and discharge port is greater than opening for feed.The bottom surface of interior tank body is provided with latticed sewage discharge hole.Manual sewage discharge device is fixed in outer inner tank wall, below, latticed sewage discharge hole, interior tank body bottom surface by screw rod and screw rod cover, and rotates control sewage emissions and discharge rate by rocking arm.
The turnover air control system for air is made of gas blower and vacuum air pump respectively, and by corresponding pipeline with the fermentation tank body link to each other, in being arranged at, the blower tube way outlet between tank body outer bottom and the outer tank body inner bottom part,, air is sent in the fermentor tank by gas blower and the pipeline that links to each other; Vacuum pumping opening is established as for interior tank body internal upper part; Gas blower and vacuum air pump are controlled by the respective switch that is arranged in the power source circuit controlling box.
Stirring system is made of electric motor, connecting rod, stirring blades.Electric motor is arranged at outer tank body center of top, and connecting rod links to each other with motor rotary shaft by shaft coupling, and the other end links to each other with fan blade, can realize the stirring to mud behind the actuating motor.
The heating temperature controlling system is made of ceramic insulation sleeve pipe, asbestos, temperature inductor and temperature-adjusting circuit.After electric stove wire puts the ceramic insulation sleeve pipe, be surrounded on interior tank wall in the form of a ring, fill the insulation asbestos between the inside and outside tank skin.
The reactor of sludge aerobic compost of the present invention, power of electric motor is 300W, and the zone of heating temperature is controlled in 35 ℃～85 ℃ scopes in the tank body, and the gas blower air output is controlled in 0～50L/min scope.
Accompanying drawing and description of drawings
Fig. 1 is the structure of reactor synoptic diagram of sludge aerobic compost of the present invention.
Fig. 2 is a compost discharge port synoptic diagram of the present invention.
Fig. 3 is a manual sewage discharge device structural representation of the present invention.
Among Fig. 1, the 1st, electric motor, the 2nd, the vacuum air pump pipeline, the 3rd, the electric stove wire of heating usefulness, the 4th, the mud that is used to ferment in the fermentation tank body, the 5th, stirring blades, the 6th, the power source circuit controlling box, the 7th, be fixed in the screw rod of outer inner tank wall in the manual sewage discharge device, the 8th, vacuum air pump, the 9th, gas blower, the 10th, latticed flase floor in the manual sewage discharge device, be provided with the sewage discharge control punch therebetween, the 11st, the outfall that water-containing sludge oozes out, the 12nd, compost discharge port, the 13rd, interior tank body, the 14th, outer tank body, the 15th, funnelform sludge inlet, the 16th, the asbestos of tank body insulation in being used for.
Among Fig. 3, the 16th, the asbestos of tank body insulation in being used for, the 14th, outer tank body, the 17th, in the manual sewage discharge device be fixed in the screw rod cover of screw rod 7 tablings on the tank skin, the 18th, shake wheel with screw rod joins, the 7th, be fixed in the screw rod of outer inner tank wall in the manual sewage discharge device, the 13rd, interior tank body, the 19th, the hairspring that screw rod 7 is connected with latticed flase floor 10 in the manual sewage discharge device, the 20th, the sewage discharge control punch, the 21st, the sliding bar of latticed flase floor 19 in the manual sewage discharge device, the 22nd, the sliding sleeve of sliding bar 21.
Embodiment
For the present invention is further understood, existing in conjunction with the accompanying drawings 1 and accompanying drawing 3 it is made specific description.
Embodiment 1
The reactor of sludge aerobic compost is made of turnover air control system for air, stirring system, fermentor tank system, heating temperature controlling system.
In the fermentor tank system, interior tank body is that radius is 500mm, highly is about the cylindrical of 1700mm, is made by the steel plate of 3mm thickness; The radius of outer tank body is the nestable formation of 600mm; Sludge inlet from outer tank body top 400mm, compost discharge port from interior tank base 50mm.The gas blower air output is controlled at 30L/min scope built-in motor and is powered by three-phase supply, and the electric stove wire total power is 2000W, and the zone of heating temperature is controlled at 45 ℃.
Get the mud 500kg of initial aqueous rate 82.15%, add 0.5% sodium polyacrylate, 6.0% wood chip, pour opening for feed into, leave standstill 20 minutes after, after discharging the sewage of 100kg, actuating motor, behind the stirring 20min, standing for fermentation, during this time once, the each air blast and the 10min that bleeds every 12 hours startup vacuum air pumps and gas blower; Once stir every 24 hours actuating motors, stir 10min at every turn, after 12 days, compost finishes, and opens compost jar discharge port, the discharging pack.
The structure of reactor of sludge aerobic compost is identical with embodiment 1.The gas blower air output is controlled at 30L/min scope built-in motor and is powered by three-phase supply, and the electric stove wire total power is 2000W, and the zone of heating temperature is controlled at 55 ℃.
Get the mud 500kg of initial aqueous rate 78.15%, add 0.8% sodium polyacrylate, 6.0% wood chip, pour opening for feed into, leave standstill 20 minutes after, after discharging the sewage of 95kg, actuating motor, behind the stirring 20min, standing for fermentation, during this time once, the each air blast and the 10min that bleeds every 12 hours startup vacuum air pumps and gas blower; Once stir every 24 hours actuating motors, stir 10min at every turn, after 10 days, compost finishes, and opens compost jar discharge port, the discharging pack.
Claims (6)
1. sludge aerobic composting reactor, it is characterized in that including the turnover air control system for air of gas blower and vacuum air pump formation, the stirring system that electric motor, connecting rod, stirring blades constitute, the fermentor tank system of interior tank body and the nestable formation of outer tank body, the heating temperature controlling system that asbestos, temperature inductor, well heater and temperature-adjusting circuit constitute constitutes, and wherein: gas blower links to each other with device by the air-supply pipeline with vacuum suction; Electric motor is positioned at the device top, and stirring blades is positioned at the fermentation tank interior, and links to each other with electric motor by connecting rod; Asbestos, temperature inductor, electric stove wire interior tank body and outside between the tank body.
2. sludge aerobic composting reactor according to claim 1, it is characterized in that in the fermentor tank system, interior tank body and outer tank body are cylindrical, outer jar greater than interior jar, mutual nestable formation between them, nestable interior tank body and outer tank wall are provided with sludge inlet, compost discharge port, manual sewage discharge device, and Sewage outlet is arranged at tank base.
3. sludge aerobic composting reactor according to claim 2, it is characterized in that manual sewage discharge device is fixed in outer inner tank wall, below, latticed sewage discharge hole, interior tank body bottom surface by screw rod and screw rod cover in the described fermentor tank system, and rotate control sewage emissions and discharge rate by rocking arm.
4. sludge aerobic composting reactor according to claim 1, it is characterized in that passing in and out air control system for air is made of gas blower and vacuum air pump respectively, and by corresponding pipeline with the fermentation tank body link to each other, wherein the blower tube way outlet is arranged between interior tank body outer bottom and the outer tank body inner bottom part, by gas blower and the pipeline that links to each other, air is sent in the fermentor tank; Vacuum pumping opening is established as for interior tank body internal upper part; Gas blower and vacuum air pump are controlled by the respective switch that is arranged in the power source circuit controlling box.
5. sludge aerobic composting reactor according to claim 1, it is characterized in that stirring system is made of electric motor, connecting rod, stirring blades, electric motor is arranged at outer tank body center of top, and connecting rod links to each other with motor rotary shaft by shaft coupling, and the other end links to each other with fan blade.
6. the device of high water content sludge aerobic compost according to claim 1, it is characterized in that heating temperature controlling system is made of ceramic insulation sleeve pipe, asbestos, temperature inductor, electric stove wire and temperature-adjusting circuit, after electric stove wire puts the ceramic insulation sleeve pipe, be surrounded on interior tank wall in the form of a ring, fill the insulation asbestos between the inside and outside tank skin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2007100094545A CN101148373A (en) | 2007-08-30 | 2007-08-30 | Sludge aerobic composting reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2007100094545A CN101148373A (en) | 2007-08-30 | 2007-08-30 | Sludge aerobic composting reactor |
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| CN101148373A true CN101148373A (en) | 2008-03-26 |
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Cited By (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101255077B (en) * | 2008-03-31 | 2010-12-08 | 李季 | Aerobic compost reactor |
| CN101614630B (en) * | 2009-06-11 | 2011-04-27 | 福建师范大学 | Accelerating reactor for accelerating ageing of performance of plastic film by sludge composting method |
| CN101585725B (en) * | 2009-06-24 | 2012-05-23 | 哈尔滨工业大学 | Organic solid waste water regulation high-temperature aerobic composting device and method thereof |
| CN101618978B (en) * | 2009-08-03 | 2012-05-23 | 沈阳师范大学 | Sludge aerobic mechanical composting method and dynamic roller composting device |
| CN102557772A (en) * | 2012-03-12 | 2012-07-11 | 湖南大学 | Fermentation device for sludge compost treatment and treatment method using same |
| CN102786363A (en) * | 2012-02-21 | 2012-11-21 | 天津生态城环保有限公司 | Novel kitchen garbage fermentation device and usage method |
| CN103664265A (en) * | 2012-09-04 | 2014-03-26 | 李祖德 | Fermenting mechanism for producing nursery stock cultivation nutrients |
| CN104045402A (en) * | 2014-07-03 | 2014-09-17 | 覃仁安 | Specific tea-oil tree compound fertilizer containing tung oil |
| CN104045401A (en) * | 2014-07-03 | 2014-09-17 | 覃仁安 | Special tung-oil-containing compound fertilizer for tea trees |
| CN105000925A (en) * | 2015-07-08 | 2015-10-28 | 中国农业大学 | Biogas residue combined aerobic composting method |
| CN105294190A (en) * | 2015-11-04 | 2016-02-03 | 秦玲 | Fermentation stirrer |
| CN105294188A (en) * | 2015-11-04 | 2016-02-03 | 秦玲 | Fermentation stirrer |
| CN105777239A (en) * | 2016-05-24 | 2016-07-20 | 安徽瑞丝环保能源有限公司 | Biological fertilizer fermentation tank |
| CN105906397A (en) * | 2016-05-27 | 2016-08-31 | 昆明理工大学 | Method and device for producing granular organic fertilizer by organic solid waste granulation variable-pressure composting |
| CN107473787A (en) * | 2016-12-23 | 2017-12-15 | 中国科学院遗传与发育生物学研究所 | Intelligent compost reactor system and compost reactor |
| CN107721474A (en) * | 2017-11-30 | 2018-02-23 | 东北农业大学 | A kind of method and its installation for fermenting that compost is prepared using organic waste |
| CN108165487A (en) * | 2018-03-20 | 2018-06-15 | 济宁森立生物科技有限公司 | A kind of bacterium high-efficiency fermenting tank |
| CN109180253A (en) * | 2018-09-29 | 2019-01-11 | 深圳市万信达生态环境股份有限公司 | A kind of detachable apparatus suitable for eutrophication bed mud compost fermentation |
| CN113429097A (en) * | 2021-08-11 | 2021-09-24 | 重庆灏宁生物技术有限公司 | Sludge fermentation equipment |
| CN115010340A (en) * | 2022-05-17 | 2022-09-06 | 诚邦生态环境股份有限公司 | Sludge dewatering, drying and composting integrated device and sludge treatment method |
-
2007
- 2007-08-30 CN CNA2007100094545A patent/CN101148373A/en active Pending
Cited By (30)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101255077B (en) * | 2008-03-31 | 2010-12-08 | 李季 | Aerobic compost reactor |
| CN101614630B (en) * | 2009-06-11 | 2011-04-27 | 福建师范大学 | Accelerating reactor for accelerating ageing of performance of plastic film by sludge composting method |
| CN101585725B (en) * | 2009-06-24 | 2012-05-23 | 哈尔滨工业大学 | Organic solid waste water regulation high-temperature aerobic composting device and method thereof |
| CN101618978B (en) * | 2009-08-03 | 2012-05-23 | 沈阳师范大学 | Sludge aerobic mechanical composting method and dynamic roller composting device |
| CN102786363A (en) * | 2012-02-21 | 2012-11-21 | 天津生态城环保有限公司 | Novel kitchen garbage fermentation device and usage method |
| CN102557772A (en) * | 2012-03-12 | 2012-07-11 | 湖南大学 | Fermentation device for sludge compost treatment and treatment method using same |
| CN103664265B (en) * | 2012-09-04 | 2015-07-29 | 李祖德 | The fermentation mechanism of nutriment is cultivated for the production of nursery stock |
| CN103664265A (en) * | 2012-09-04 | 2014-03-26 | 李祖德 | Fermenting mechanism for producing nursery stock cultivation nutrients |
| CN104045402B (en) * | 2014-07-03 | 2016-04-13 | 覃仁安 | A kind of oil tea compound fertilizer special containing tung oil |
| CN104045401A (en) * | 2014-07-03 | 2014-09-17 | 覃仁安 | Special tung-oil-containing compound fertilizer for tea trees |
| CN104045401B (en) * | 2014-07-03 | 2016-04-13 | 覃仁安 | A kind of tea tree compound fertilizer special containing tung oil |
| CN104045402A (en) * | 2014-07-03 | 2014-09-17 | 覃仁安 | Specific tea-oil tree compound fertilizer containing tung oil |
| CN105000925A (en) * | 2015-07-08 | 2015-10-28 | 中国农业大学 | Biogas residue combined aerobic composting method |
| CN105294190A (en) * | 2015-11-04 | 2016-02-03 | 秦玲 | Fermentation stirrer |
| CN105294188A (en) * | 2015-11-04 | 2016-02-03 | 秦玲 | Fermentation stirrer |
| CN105294190B (en) * | 2015-11-04 | 2018-09-11 | 秦玲 | A kind of stirrer for fermentation |
| CN105777239A (en) * | 2016-05-24 | 2016-07-20 | 安徽瑞丝环保能源有限公司 | Biological fertilizer fermentation tank |
| CN105906397A (en) * | 2016-05-27 | 2016-08-31 | 昆明理工大学 | Method and device for producing granular organic fertilizer by organic solid waste granulation variable-pressure composting |
| CN105906397B (en) * | 2016-05-27 | 2022-04-12 | 昆明理工大学 | Method and device for producing granular organic fertilizer by granulating organic solid waste and performing pressure swing composting |
| CN107473787A (en) * | 2016-12-23 | 2017-12-15 | 中国科学院遗传与发育生物学研究所 | Intelligent compost reactor system and compost reactor |
| CN107473787B (en) * | 2016-12-23 | 2021-03-30 | 中国科学院遗传与发育生物学研究所农业资源研究中心 | Intelligent composting reactor system and composting reactor |
| CN107721474A (en) * | 2017-11-30 | 2018-02-23 | 东北农业大学 | A kind of method and its installation for fermenting that compost is prepared using organic waste |
| CN107721474B (en) * | 2017-11-30 | 2021-07-09 | 东北农业大学 | Method for preparing compost by using organic waste and fermentation device thereof |
| CN108165487A (en) * | 2018-03-20 | 2018-06-15 | 济宁森立生物科技有限公司 | A kind of bacterium high-efficiency fermenting tank |
| CN108165487B (en) * | 2018-03-20 | 2022-02-01 | 济宁森立生物科技有限公司 | High-efficient fermentation cylinder is used to fungus |
| CN109180253A (en) * | 2018-09-29 | 2019-01-11 | 深圳市万信达生态环境股份有限公司 | A kind of detachable apparatus suitable for eutrophication bed mud compost fermentation |
| CN113429097A (en) * | 2021-08-11 | 2021-09-24 | 重庆灏宁生物技术有限公司 | Sludge fermentation equipment |
| CN113429097B (en) * | 2021-08-11 | 2024-05-14 | 怡灏环境技术有限公司 | Sludge fermentation equipment |
| CN115010340A (en) * | 2022-05-17 | 2022-09-06 | 诚邦生态环境股份有限公司 | Sludge dewatering, drying and composting integrated device and sludge treatment method |
| CN115010340B (en) * | 2022-05-17 | 2024-04-02 | 诚邦生态环境股份有限公司 | Sludge dewatering and drying composting integrated device and sludge treatment method |
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Open date: 20080326 |