CN203451394U - System for producing bio-organic fertilizer through airtight aerobic fermentation of municipal sludge or kitchen residues - Google Patents
System for producing bio-organic fertilizer through airtight aerobic fermentation of municipal sludge or kitchen residues Download PDFInfo
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- CN203451394U CN203451394U CN201320568691.6U CN201320568691U CN203451394U CN 203451394 U CN203451394 U CN 203451394U CN 201320568691 U CN201320568691 U CN 201320568691U CN 203451394 U CN203451394 U CN 203451394U
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- 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
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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
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- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
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Abstract
The utility model provides a system for producing a bio-organic fertilizer through airtight aerobic fermentation of municipal sludge or kitchen residues. The system comprises a forestry and agricultural residue collection bin, a cutting device, a drying device, a crushing device, a storage tank, a sludge or kitchen residue storage bin, a stirring and mixing device, an airtight horizontal double-layer cylinder body aerobic fermentation tank, an airtight horizontal aerobic fermentation tank, a crushing and sieving device, a homogenous storage bin, an organic fertilizer packaging device, an air supply device and an exhaust device. The system provided by the utility model has the advantages of simple structure, large treatment capacity, relatively short fermentation period, uniform material fermentation degree, good treatment effect, high automation degree and low treatment cost, the primary aerobic fermentation and the secondary aerobic fermentation treatment are carried out in a totally closed manner, so that the treatment process is free of peculiar smell, the kitchen residues and the municipal sludge are recycled to produce organic fertilizers and liquid bacterial manures with large market values, and possible threats of the kitchen residues and the municipal sludge on the environment and human bodies are avoided as well, so that the harmlessness and the resource utilization of the kitchen residues and the municipal sludge are realized.
Description
Technical field
The utility model belongs to Assessment of MSW Disposal Technologies field, relates in particular to a kind of municipal sludge or the airtight aerobic biological organic fertilizer system processed of meal natural pond, kitchen slag.
Background technology
Changing food waste is topmost a kind of in food refuse, comprises food process tankage (kitchen is remaining) and edible remaining (hogwash) that family, school, dining room and catering industry etc. produce.Its complicated component, is mainly the mixture of the many kinds of substances such as oil, water, pericarp, vegetables, rice and flour, fish, meat, bone and useless tableware, plastics, paper handkerchief, chemical constitution, has starch, Mierocrystalline cellulose, protein, lipid and inorganic salt.China's changing food waste quantity is very huge, and is fast rise trend.
Changing food waste has the duplicity of significant harm and resource, and its feature can be summarized as: (1) water ratio high, can reach 80%-95%.(2) salt content is high, some areas are high containing capsicum, acetic acid.(3) high, the protein of organic content, Mierocrystalline cellulose, starch, fat etc.(4) be rich in nitrogen, phosphorus, potassium, calcium and various trace element.(5) have pathogenic bacteria, pathogenic micro-organism.Perishable, rotten, smelly, grow mosquito.
Aspect waste resource, according to the relevant expert of Ministry of Agriculture measuring and calculating, changing food waste includes a large amount of nutritive substances, and main component is grease and protein, alternative corn, fish meal, dregs of beans etc. are processed into high energy protein high-quality feed, are also the applicable raw materials of preparing biological diesel oil.Expert explains, pressing dry matter content calculates, 5000 ten thousand tons of changing food wastes are equivalent to the high-quality feed of 5,000,000 tons, and the energy equivalence including is in the Energy output amount in annual 1000 ten thousand mu of arable lands, and the protein including is equivalent to the protein quantum of output of annual 2000 ten thousand mu of soybean.That is to say, if the changing food waste of 1 year output of China is all utilized, be equivalent to save 1,000 ten thousand mu of arable lands.In the face of Chinese arable land is nervous, food shortage, need every year the present situation of a large amount of food import feeds, rationally utilizing changing food waste is the effective way that increases resource utilization, solves to a certain extent China's food problem.And this utilization, meets minimizing, recycling, resource utilization feature, it is the lively case of developing a circular economy.
For changing food waste hazardness mainly contain following some:
(1) contaminate environment, affect the appearance of the city.Because changing food waste contains higher organic matter and moisture, be easily subject to the effect of microorganism, and the phenomenon that rots; And discarded storage period is more of a specified duration, putrid and deteriorated phenomenon is just serious all the more.Particularly, to summer, temperature is higher, rots also faster, at this time easily produces a large amount of water from diffusion and foul gas, grows mosquito, and environmental health is made a very bad impression.
(2) be detrimental to health.Meat proteins in changing food waste and the lipoid material of animality, mainly come from those livestock poultry that meat-based food is provided, livestock is after directly eating food without the changing food waste of effectively processing, the homology that " cannibalism " easily occurs is polluted, and cause the cross infection of epidemic disease between people and animals, be detrimental to health, and may promote the propagation of some fatal disease.As the transmissible disease of large-scale outbreak in history.Say for another example, at present in the cause of many local bird flus of propagating etc., may be that the corpse due to sick ox, sick sheep or sick pig has been made into animal-feed, thereby cause the extensive infection of disease.
(3) spread disease.The outdoor storage of changing food waste can cause the amount reproduction of mosquitos and flies mouse worm, and it is the main media that disease spreads.
(4) the lower sepage producing while stacking in changing food waste enters into Sewage treatment systems, can cause the increase of organic content, thereby increase the weight of the burden of sewage work, increases running cost.
At present, changing food waste is generally adopted to aerobic compost or anaerobic digestion producing methane technique, idiographic flow is: unified recovery enters after process for producing line, through sorting, magnetic separation, the inorganicss such as chopsticks, plastics bag, metal are sifted out, and remaining kitchen castoff, after fragmentation, oily water separation, dehydration, send into aerobic fermentation equipment, the kitchen castoff after processing becomes industrial grease and Nutrition Soil.Anaerobic digestion process, pre-treatment and aerobic compost pre-treatment are basically identical, proposing after commercial grease slurrying sends into anaerobic jar and carries out anaerobically fermenting, produce biogas, afterwards mixture is carried out to natural pond slag by centrifugation, natural pond liquid is separated, and natural pond slag is as the raw material of fertilizer processed, and natural pond liquid is further processed qualified discharge.Existing to the natural pond slag after anaerobic digestion of kitchen wastes, generally take to add that flocculation agent precipitation adds after caliche, filter press, dehydration is to below 55%, landfill disposal.The one, cause organic resources waste, the 2nd, equipment investment is large, and processing cost is high, and the 3rd, landfill land occupation resource.And take centrifuge dehydration aerobic fermentation process, and can improve the social utilization ratio of resource, produce good society and economic benefit.
Mud is the product after sewage disposal, is a kind of extremely complicated heterogeneous body being comprised of organic relic, bacterium thalline, inorganic particle, colloid etc.The main characteristic of dewatered sludge is water ratio high (more than 80%), and organic content is high, easily degenerates smellyly, causes serious atmospheric pollution, affects resident's life; And particle is thinner, proportion is less, is gluey liquid.It is the concentrated thing between liquid and solid, can transport with pump, but it is difficult to carry out solid-liquid separation by sedimentation.
Natural pond, meal kitchen slag (the natural pond slag after changing food waste anaerobically fermenting) and dewatered sludge in city, can make full use of resource like this, takes up an area less space, produces society and economic benefit, is therefore a difficult problem of needing solution badly.
Utility model content
The utility model is in order to solve weak point of the prior art, provide a kind of simple, save great amount of cost, municipal sludge or the airtight aerobic biological organic fertilizer system processed of meal natural pond, kitchen slag that treatment capacity is large.
For solving the problems of the technologies described above, the utility model adopts following technical scheme: municipal sludge or the airtight aerobic biological organic fertilizer system processed of meal natural pond, kitchen slag, comprise agriculture and forestry organic waste material collecting bin, guillotine cutting device, drying unit, shredding unit, hold-up vessel, mud or meal natural pond, kitchen slag storage warehouse, mixing stirring device, closed horizontal double-layer barrel aerobic fermentation tank, closed horizontal aerobic fermentation tank, crush and screen device, homogeneous storage warehouse, fertilizer packing plant, air feeder and gas barrier;
The outlet of agriculture and forestry organic waste material collecting bin is connected with the import of guillotine cutting device, the discharge port of guillotine cutting device is connected with the opening for feed of drying unit, the discharge port of drying unit is connected with the opening for feed of shredding unit, the discharge port of shredding unit is connected with the opening for feed of hold-up vessel, hold-up vessel is connected with the opening for feed of mixing stirring device respectively with the discharge port of mud or meal natural pond, kitchen slag storage warehouse, the discharge port of mixing stirring device is connected with the opening for feed of closed horizontal double-layer barrel aerobic fermentation tank, the discharge port of closed horizontal double-layer barrel aerobic fermentation tank is connected with the opening for feed of closed horizontal aerobic fermentation tank, the discharge port of closed horizontal aerobic fermentation tank is connected with the opening for feed that crushes and screens device, the discharge port that crushes and screens device is connected with the opening for feed of homogeneous storage warehouse, the discharge port of homogeneous storage warehouse is connected with the opening for feed of fertilizer packing plant,
The air outlet of air feeder is connected with the inlet mouth of closed horizontal aerobic fermentation tank with closed horizontal double-layer barrel aerobic fermentation tank respectively, and the inlet mouth of gas barrier is connected with the air outlet of closed horizontal aerobic fermentation tank with closed horizontal double-layer barrel aerobic fermentation tank respectively.
Described system also comprises gas sampling tank and bacteria bed odor removal, waste gas outlet, the waste gas outlet of mixing stirring device and the waste gas outlet of gas barrier of mud or meal natural pond, kitchen slag storage warehouse are connected with the inlet mouth of gas sampling tank respectively, and the air outlet of gas sampling tank is connected with the inlet mouth of bacteria bed odor removal.
Described system also comprises leachate collecting device, anaerobic fermentation tank, tank for sewage gas, biogas residue and biogas liquid tripping device, natural pond slag storage pool, natural pond liquid storage pool, aeration tank and adds bacterial strain culture device;
The wastewater outlet of mud or meal natural pond, kitchen slag storage warehouse, the wastewater outlet of closed horizontal double-layer barrel aerobic fermentation tank is connected with the fluid inlet of leachate collecting device respectively, the liquid outlet of leachate collecting device is connected with the fluid inlet of anaerobic fermentation tank, the air outlet of anaerobic fermentation tank is connected with the inlet mouth of tank for sewage gas, the air outlet of tank for sewage gas provides heat by combustion heat supplying device for drying unit, the discharge port of anaerobic fermentation tank is connected with the opening for feed of biogas residue and biogas liquid tripping device, the discharge port of biogas residue and biogas liquid tripping device is connected with the opening for feed of natural pond slag storage pool, the discharge port of natural pond slag storage pool is connected with the opening for feed of mixing stirring device, the liquid outlet of biogas residue and biogas liquid tripping device is connected with the fluid inlet of natural pond liquid storage pool, the liquid outlet of natural pond liquid storage pool is connected with the fluid inlet of aeration tank, the liquid outlet of aeration tank with add bacterial strain culture device or municipal sewage pipe network is connected.
Adopt technique scheme, the water content of mud and meal natural pond, kitchen slag is generally 78%-80%, agriculture and forestry organic waste material is as the auxiliary material of mud or meal natural pond, kitchen slag, agriculture and forestry organic waste material need to carry out being uniformly mixed with mud or meal natural pond, kitchen slag after guillotine cutting, oven dry, pulverizing again, mixture moisture content after main fermentation, secondary aerobic fermentation is lowered, and becomes fertilizer.Waste gas in each operation is collected also and is discharged in atmosphere after deodorizing.Waste water after main fermentation is for Biogas and natural pond liquid, and biogas combustion is for the oven dry of agriculture and forestry organic waste material, natural pond liquid by aeration after useless being discharged in urban sewage pipe, useful for producing liquid bacterial manure, natural pond slag utilizes after being again uniformly mixed again again.
In the utility model, produce fertilizer most importantly main fermentation and secondary aerobic fermentation operation, this two procedures has determined the quality of the fertilizer of producing, the patent of invention that main fermentation closed horizontal double-layer barrel aerobic fermentation tank (number of patent application is 2013103484863) used is applied on August 12nd, 2013 for the applicant, the patent of invention that secondary aerobic fermentation closed horizontal aerobic fermentation tank (number of patent application is 2013102974850) the applicant used applied on July 16th, 2013.Therefore, the concrete structure of closed horizontal double-layer barrel aerobic fermentation tank and closed horizontal aerobic fermentation tank and use procedure just no longer elaborate.Owing to having adopted closed horizontal double-layer barrel aerobic fermentation tank to carry out main fermentation and having adopted closed horizontal aerobic fermentation tank to carry out secondary aerobic fermentation, so not only shortened the time of aerobic fermentation, and greatly improved quality and the fertilizer efficiency of fertilizer.
Simple in structure, treatment capacity of the present utility model is large, fermentation period is shorter, material attenuation degree is even, treatment effect good, level of automation is high, processing cost is lower, it is all totally-enclosed operations that main fermentation and secondary aerobic fermentation are processed, treating processes free from extraneous odour, meal kitchen natural pond slag and municipal sludge are made a silk purse out of a sow's ear, producing the utmost point has fertilizer and the liquid bacterial manure of marketable value, also the threat of having avoided meal natural pond, kitchen slag and municipal sludge may cause environment and human body, thus realize innoxious, the recycling of eat natural pond, kitchen slag and municipal sludge.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 adopts the utility model to produce the process flow sheet of biological organic fertilizer.
Embodiment
As shown in Figure 1, municipal sludge of the present utility model or the airtight aerobic biological organic fertilizer system processed of meal natural pond, kitchen slag, comprise agriculture and forestry organic waste material collecting bin 1, guillotine cutting device 2, drying unit 4, shredding unit 5, hold-up vessel 6, mud or meal natural pond, kitchen slag storage warehouse 7, mixing stirring device 3, closed horizontal double-layer barrel aerobic fermentation tank 8, closed horizontal aerobic fermentation tank 9, crush and screen device 10, homogeneous storage warehouse 11, fertilizer packing plant 12, air feeder 13 and gas barrier 14;
The outlet of agriculture and forestry organic waste material collecting bin 1 is connected with the import of guillotine cutting device 2, the discharge port of guillotine cutting device 2 is connected with the opening for feed of drying unit 4, the discharge port of drying unit 4 is connected with the opening for feed of shredding unit 5, the discharge port of shredding unit 5 is connected with the opening for feed of hold-up vessel 6, hold-up vessel 6 is connected with the opening for feed of mixing stirring device 3 respectively with the discharge port of mud or meal natural pond, kitchen slag storage warehouse 7, the discharge port of mixing stirring device 3 is connected with the opening for feed of closed horizontal double-layer barrel aerobic fermentation tank 8, the discharge port of closed horizontal double-layer barrel aerobic fermentation tank 8 is connected with the opening for feed of closed horizontal aerobic fermentation tank 9, the discharge port of closed horizontal aerobic fermentation tank 9 is connected with the opening for feed that crushes and screens device 10, the discharge port that crushes and screens device 10 is connected with the opening for feed of homogeneous storage warehouse 11, the discharge port of homogeneous storage warehouse 11 is connected with the opening for feed of fertilizer packing plant 12,
The air outlet of air feeder 13 is connected with the inlet mouth of closed horizontal aerobic fermentation tank 9 with closed horizontal double-layer barrel aerobic fermentation tank 8 respectively, and the inlet mouth of gas barrier 14 is connected with the air outlet of closed horizontal aerobic fermentation tank 9 with closed horizontal double-layer barrel aerobic fermentation tank 8 respectively.
The utility model also comprises gas sampling tank 15 and bacteria bed odor removal 16, waste gas outlet, the waste gas outlet of mixing stirring device 3 and the waste gas outlet of gas barrier 14 of mud or meal natural pond, kitchen slag storage warehouse 7 are connected with the inlet mouth of gas sampling tank 15 respectively, and the air outlet of gas sampling tank 15 is connected with the inlet mouth of bacteria bed odor removal 16.
The utility model also comprises leachate collecting device 17, anaerobic fermentation tank 18, tank for sewage gas 19, biogas residue and biogas liquid tripping device 20, natural pond slag storage pool 21, natural pond liquid storage pool 22, aeration tank 23 and adds bacterial strain culture device 24;
The wastewater outlet of mud or meal natural pond, kitchen slag storage warehouse 7, the wastewater outlet of closed horizontal double-layer barrel aerobic fermentation tank 8 is connected with the fluid inlet of leachate collecting device 17 respectively, the liquid outlet of leachate collecting device is connected with the fluid inlet of anaerobic fermentation tank 18, the air outlet of anaerobic fermentation tank 18 is connected with the inlet mouth of tank for sewage gas 19, the air outlet of tank for sewage gas 19 provides heat by combustion heat supplying device 25 for drying unit 4, the discharge port of anaerobic fermentation tank 18 is connected with the opening for feed of biogas residue and biogas liquid tripping device 20, the discharge port of biogas residue and biogas liquid tripping device 20 is connected with the opening for feed of natural pond slag storage pool 21, the discharge port of natural pond slag storage pool 21 is connected with the opening for feed of mixing stirring device 3, the liquid outlet of biogas residue and biogas liquid tripping device 20 is connected with the fluid inlet of natural pond liquid storage pool 22, the liquid outlet of natural pond liquid storage pool 22 is connected with the fluid inlet of aeration tank 23, the liquid outlet of aeration tank 23 with add bacterial strain culture device 24 or municipal sewage pipe network and be connected.
In the middle of the utility model, except closed horizontal double-layer barrel aerobic fermentation tank 8 and closed horizontal aerobic fermentation tank 9, other devices are existing mature technology, and concrete structure repeats no more.Between each device, solid, particle, pulverous mass transport can adopt material conveyor, and the conveying of liquids and gases adopts pipeline.
As shown in Figure 2, adopt technique of the present utility model, comprise the following steps:
(1), collect mud or meal natural pond, kitchen slag, collect agriculture and forestry organic waste material, three is uniformly mixed, make the water content of mixture be down to 55%-65%, preferably 60%;
(2), mixture is transported in closed horizontal double-layer barrel aerobic fermentation tank and carries out main fermentation, to air feed in closed horizontal double-layer barrel aerobic fermentation tank, the temperature of main fermentation is 65 °-75 °, preferably 70 ° simultaneously;
(3), then mixture is transported to and in closed horizontal aerobic fermentation tank, carries out secondary aerobic fermentation, simultaneously, to air feed in closed horizontal aerobic fermentation tank, secondary aerobic fermentation temperature is 50 °-60 °, preferably 55 °, after secondary aerobic fermentation completes, the water content of mixture is down to below 30%;
(4), mixture is pulverized and sieved, make fertilizer, the globule size of fertilizer is not more than 0.5cm, preferably 0.2cm;
(5), the fertilizer homogeneous after screening is stored;
(6), by fertilizer packing, outbound.
Agriculture and forestry organic waste material in step (1) carries out successively guillotine cutting, oven dry, pulverizing, storage procedure before being uniformly mixed.
In step (1) by the waste gas of mud, meal natural pond, kitchen slag Spontaneous release in stacking process and the gas sampling in being uniformly mixed operation in waste gas collection device; In described step (2), (3), the waste gas of discharging in fermenting process is also collected in waste gas collection device by gas barrier, then the waste gas in waste gas collection device is carried out to off gas treatment by bacteria bed odor removal, be discharged in atmosphere after up to standard.
The waste water of the discharge after main fermentation in the waste water that in step (1), mud, meal natural pond, kitchen slag naturally ooze out in stacking process and step (2) is input in anaerobic fermentation tank by leachate collecting device, after anaerobically fermenting, produce natural pond Zha, natural pond liquid and biogas, Zha, natural pond, natural pond liquid is separated with biogas.
The operation that is uniformly mixed that natural pond slag is transported to the mud in step (1) or eat natural pond, kitchen slag and agriculture and forestry organic waste material, natural pond slag utilizes again.
The purifying desulphurized rear tinning of a part of biogas is sold, and the baking operation that another part burning is agriculture and forestry organic waste material provides heat energy.
Natural pond liquid is carried out to aeration, and pollution-free and be drained into municipal sewage pipe network without the water of nutritive ingredient, nutritious natural pond liquid forms liquid bacterial manure after adding spawn culture 3-5 days.
The present embodiment is not done any pro forma restriction to shape of the present utility model, material, structure etc.; any simple modification, equivalent variations and modification that every foundation technical spirit of the present utility model is done above embodiment, all belong to the protection domain of technical solutions of the utility model.
Claims (3)
1. municipal sludge or the airtight aerobic biological organic fertilizer system processed of meal natural pond, kitchen slag, is characterized in that: comprise agriculture and forestry organic waste material collecting bin, guillotine cutting device, drying unit, shredding unit, hold-up vessel, mud or meal natural pond, kitchen slag storage warehouse, mixing stirring device, closed horizontal double-layer barrel aerobic fermentation tank, closed horizontal aerobic fermentation tank, crush and screen device, homogeneous storage warehouse, fertilizer packing plant, air feeder and gas barrier;
The outlet of agriculture and forestry organic waste material collecting bin is connected with the import of guillotine cutting device, the discharge port of guillotine cutting device is connected with the opening for feed of drying unit, the discharge port of drying unit is connected with the opening for feed of shredding unit, the discharge port of shredding unit is connected with the opening for feed of hold-up vessel, hold-up vessel is connected with the opening for feed of mixing stirring device respectively with the discharge port of mud or meal natural pond, kitchen slag storage warehouse, the discharge port of mixing stirring device is connected with the opening for feed of closed horizontal double-layer barrel aerobic fermentation tank, the discharge port of closed horizontal double-layer barrel aerobic fermentation tank is connected with the opening for feed of closed horizontal aerobic fermentation tank, the discharge port of closed horizontal aerobic fermentation tank is connected with the opening for feed that crushes and screens device, the discharge port that crushes and screens device is connected with the opening for feed of homogeneous storage warehouse, the discharge port of homogeneous storage warehouse is connected with the opening for feed of fertilizer packing plant,
The air outlet of air feeder is connected with the inlet mouth of closed horizontal aerobic fermentation tank with closed horizontal double-layer barrel aerobic fermentation tank respectively, and the inlet mouth of gas barrier is connected with the air outlet of closed horizontal aerobic fermentation tank with closed horizontal double-layer barrel aerobic fermentation tank respectively.
2. municipal sludge according to claim 1 or meal natural pond, kitchen slag airtight aerobic biological organic fertilizer system processed, it is characterized in that: described system also comprises gas sampling tank and bacteria bed odor removal, waste gas outlet, the waste gas outlet of mixing stirring device and the waste gas outlet of gas barrier of mud or meal natural pond, kitchen slag storage warehouse are connected with the inlet mouth of gas sampling tank respectively, and the air outlet of gas sampling tank is connected with the inlet mouth of bacteria bed odor removal.
3. municipal sludge according to claim 1 and 2 or the airtight aerobic biological organic fertilizer system processed of meal natural pond, kitchen slag, is characterized in that: described system also comprises leachate collecting device, anaerobic fermentation tank, tank for sewage gas, biogas residue and biogas liquid tripping device, natural pond slag storage pool, natural pond liquid storage pool, aeration tank and adds bacterial strain culture device;
The wastewater outlet of mud or meal natural pond, kitchen slag storage warehouse, the wastewater outlet of closed horizontal double-layer barrel aerobic fermentation tank is connected with the fluid inlet of leachate collecting device respectively, the liquid outlet of leachate collecting device is connected with the fluid inlet of anaerobic fermentation tank, the air outlet of anaerobic fermentation tank is connected with the inlet mouth of tank for sewage gas, the air outlet of tank for sewage gas provides heat by combustion heat supplying device for drying unit, the discharge port of anaerobic fermentation tank is connected with the opening for feed of biogas residue and biogas liquid tripping device, the discharge port of biogas residue and biogas liquid tripping device is connected with the opening for feed of natural pond slag storage pool, the discharge port of natural pond slag storage pool is connected with the opening for feed of mixing stirring device, the liquid outlet of biogas residue and biogas liquid tripping device is connected with the fluid inlet of natural pond liquid storage pool, the liquid outlet of natural pond liquid storage pool is connected with the fluid inlet of aeration tank, the liquid outlet of aeration tank with add bacterial strain culture device or municipal sewage pipe network is connected.
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| CN201320568691.6U CN203451394U (en) | 2013-09-13 | 2013-09-13 | System for producing bio-organic fertilizer through airtight aerobic fermentation of municipal sludge or kitchen residues |
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| CN201320568691.6U CN203451394U (en) | 2013-09-13 | 2013-09-13 | System for producing bio-organic fertilizer through airtight aerobic fermentation of municipal sludge or kitchen residues |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104774055A (en) * | 2015-02-04 | 2015-07-15 | 优思克（北京）生物能源科技有限公司 | Ecological cyclic utilization system for organic waste |
| CN106083239A (en) * | 2016-08-19 | 2016-11-09 | 四川凯尔丰农业科技有限公司 | A kind of novel organic bio-fertilizer production system |
| CN106116737A (en) * | 2016-08-25 | 2016-11-16 | 郑州新华重型机器有限公司 | The production system of a kind of fertilizer and production technology |
| CN106701544A (en) * | 2016-11-30 | 2017-05-24 | 重庆赛顺环保科技有限公司 | Environment-friendly process for anaerobic fermentation treatment of straw |
| CN107056552A (en) * | 2017-06-10 | 2017-08-18 | 陕西理工学院 | A kind of utilization excess sludge and agriculture and forestry organic waste material prepare the device of fertilizer |
| CN109265213A (en) * | 2018-10-17 | 2019-01-25 | 河南科技学院 | A kind of intelligence control system for aerobic fermentation process |
| CN110903110A (en) * | 2019-11-25 | 2020-03-24 | 浙江万泰环境工程有限公司 | Quick good oxygen system of becoming fertile of natural pond sediment |
| CN111423084A (en) * | 2020-03-25 | 2020-07-17 | 山东碧泉环境工程技术有限公司 | Movable container for treating excrement |
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2013
- 2013-09-13 CN CN201320568691.6U patent/CN203451394U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104774055A (en) * | 2015-02-04 | 2015-07-15 | 优思克（北京）生物能源科技有限公司 | Ecological cyclic utilization system for organic waste |
| CN106083239A (en) * | 2016-08-19 | 2016-11-09 | 四川凯尔丰农业科技有限公司 | A kind of novel organic bio-fertilizer production system |
| CN106116737A (en) * | 2016-08-25 | 2016-11-16 | 郑州新华重型机器有限公司 | The production system of a kind of fertilizer and production technology |
| CN106701544A (en) * | 2016-11-30 | 2017-05-24 | 重庆赛顺环保科技有限公司 | Environment-friendly process for anaerobic fermentation treatment of straw |
| CN106701544B (en) * | 2016-11-30 | 2019-03-19 | 重庆赛顺环保科技有限公司 | A kind of environment-friendly type stalk pressure aerobe fermentation treatment process |
| CN107056552A (en) * | 2017-06-10 | 2017-08-18 | 陕西理工学院 | A kind of utilization excess sludge and agriculture and forestry organic waste material prepare the device of fertilizer |
| CN109265213A (en) * | 2018-10-17 | 2019-01-25 | 河南科技学院 | A kind of intelligence control system for aerobic fermentation process |
| CN110903110A (en) * | 2019-11-25 | 2020-03-24 | 浙江万泰环境工程有限公司 | Quick good oxygen system of becoming fertile of natural pond sediment |
| CN111423084A (en) * | 2020-03-25 | 2020-07-17 | 山东碧泉环境工程技术有限公司 | Movable container for treating excrement |
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