CN103084380A - Municipal solid waste processing system and processing method - Google Patents
Municipal solid waste processing system and processing method Download PDFInfo
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- CN103084380A CN103084380A CN2013100419805A CN201310041980A CN103084380A CN 103084380 A CN103084380 A CN 103084380A CN 2013100419805 A CN2013100419805 A CN 2013100419805A CN 201310041980 A CN201310041980 A CN 201310041980A CN 103084380 A CN103084380 A CN 103084380A
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Abstract
The invention relates to a municipal solid waste processing system comprising a sorting system, a pretreatment system, and an anaerobic fermentation system. The sorting system comprises a receiving hopper, a plate feeder positioned on the bottom of the receiving hopper, a uniform material-toggling bag-breaking device, and a cylinder broken bag screening machine. The pretreatment system comprises a crushing device, a sand-water separation device, and a waste receiving hopper connected with a sorting platform. The waste receiving hopper is connected with the crushing device and the sand-water separation device through a conveyor. A slag-discharge screw, a grid, a gas/water circulation device, and a rotary crushing device are arranged in the sand-water separation device. The anaerobic fermentation system comprises a homogenization tank connected with a lift pump. The homogenization tank is connected with an anaerobic digestion tank. The anaerobic digestion tank is respectively connected with a biogas purification device, a power generation system, and a sludge storage tank. The system and the method provided by the invention have the advantages that: with the sorting system, the pretreatment system, and the anaerobic fermentation system, the waste is turned harmless, and is converted into resources. Also, the amount of waste is reduced.
Description
Technical field
The present invention relates to a kind of system for treating municipal solid waste and processing method thereof.
Background technology
At present, the Treatment Way of Municipal Refuse in City that extensively adopts both at home and abroad mainly contains 4 kinds of processing modes of sanitary landfills, burning, compost and comprehensive utilization (recycling utilization).
Sanitary landfills is a kind of innoxious final disposal mode of a kind of domestic waste that grows up of processing from traditional stacking and made ground.Its disposal ability is large, does not need rubbish is carried out categorised collection or focuses on, and can collect biogas and generate electricity when garbage loading embeading thickness is enough large, and investment and operating cost are lower.But landfill yard requires high to the factory site, and difficulty is large, and the land occupation resource easily causes secondary pollution, as percolate, landfill gas, flying dust and floating thing etc.Soil water body and atmosphere to the surrounding area affect greatly, and be very large in the neighbourhood social influence, causes simultaneously the ample resources waste.Sanitary landfills is only applicable to the land resource abundance, and the landfill place is easily practicable, the area that the local economy level falls behind relatively.At present, domestic most rubbish are to adopt landfill method, but wherein small part is to adopt sanitary landfills, and major part is all to adopt simple and easy stacking.
Burning refer in house refuse combustible in hot conditions (800 ~ 1000 ℃) through combustion reaction, the abundant oxidation of combustible component finally becomes the process of harmless stabilized ash.Burn the minimizing degree high, innoxious effective, heat energy can be used to generating or heat production, reaches the effect of recycling, and floor space is little, and totally enclosed pattern can not be subjected to the impact of natural conditions.But, its shortcoming is that one-time investment and operating cost are high, the operational management difficulty is larger, easily produce secondary pollution, be difficult to control, have dioxin contamination in tail gas, in the tail ash, heavy metal pollution is arranged, the recyclable resource of waste part, if qualified discharge, high standard waste gas treatment equipment investment operating cost is high.It is only applicable to, and the rubbish Lower heat value is high, and moisture content is low, the developed area.The developed countries usage comparison is many at present, descends to some extent in recent years, and Chinese development in recent years is very fast, but technology is still waiting raising, fails to reach discharge standard.
Compost is to utilize microorganism to promote artificially the Biochemical processes that in house refuse, biodegradable organic matter transforms to humus, and the product after processing is compost.It can take full advantage of organic matter in garbage, and composting production can be used for fertilizer, and secondary pollution is less, easily controls, and one-time investment and operating cost are relatively low.But the volume reduction rate of rubbish is low, also has the residue of 30-40% to need landfill disposal, easily produces stench in composting process, surrounding enviroment is produced pollute, and floor space is relatively large, and because the impurity content of compost is high, fertilizer efficiency is low, and the fertilizer market is generally bad.It is high that compost is only applicable in rubbish the labile organic compound composition, and economic condition is not high, the area that treating capacity is low.Compost is used many in Europe, develop comparatively fast during domestic " the Seventh Five-Year Plan, eight or five ", and successful example is few, and the fertilizer market is poor, is difficult to keep operation, and major part is simple and easy compost, and secondary pollution is large.
Comprehensive utilization refers to house refuse is first classified, then adopts suitable method that all kinds of products are processed respectively, reaches the purpose of comprehensive utilization of resources, and it integrates all kinds of processing methods.Its advantage is to have realized garbage harmless, resource, minimizing at the bottom of maximum limit, and secondary pollution is little, and biogas can be used to generating, and fertilizer impurity is few, and investment and operating cost are moderate, and floor space is less.But, wanting to realize fully recycling utilization, its input cost is large, and the treatment system that relates to is complicated, and equipment needed thereby requires high.
Summary of the invention
According to above-mentioned weak point, the purpose of this invention is to provide a kind of applicability is strong, treating capacity is large, treatment effect is good refuse disposal system and processing method thereof.
For achieving the above object, technical scheme of the present invention is: a kind for the treatment of system of domestic waste, it comprises sorting system, pretreatment system and anaerobic fermentation system.Sorting system comprises receiving cone, be positioned at the apron feeder of receiving cone bottom, evenly material toggling bag-breaking device and cylinder bag-broken screening machineifier, wherein, apron feeder is connected with the import of even material toggling bag-breaking device, evenly the outlet of material toggling bag-breaking device is connected with large part selection platform, and large part selection platform is connected with cylinder bag-broken screening machineifier; Cylinder bag-broken screening machineifier also is connected with pneumatic separation device and sorting platform, and wherein, the sorting platform is connected with pretreatment system.Pretreatment system comprises that breaker, sand water separation device and the rubbish that is connected with the sorting platform receive bucket, and rubbish receives bucket and is connected with the sand water separation device with breaker by conveyer; Sand water separation device inside is provided with deslagging spiral, grid, gas/water circle device and revolution crushing device; The sand water separation device is connected with anaerobic fermentation system by elevator pump.Anaerobic fermentation system comprises the homogeneous pond that is connected with elevator pump, and the homogeneous pond is connected with anaerobic digestor; Anaerobic digestor is connected with marsh gas purifying, electricity generation system and sludge storage pool respectively, and described sludge storage pool also is connected with mud and water treatment system.
Preferably: be provided with bag-breaking device and screen cloth in described cylinder bag-broken screening machineifier, wherein, the sieve diameter of screen cloth is 60-90mm.
Preferably: described pneumatic separation device is connected with light materials sorting platform and heavy substance sorting platform; Wherein, heavy substance sorting platform is connected with cylinder bag-broken screening machineifier with super power crusher by ferromagnetic deironing device successively.
Preferably: be provided with ferromagnetic deironing device between described sorting platform and pretreatment system.
Preferably: described breaker is divided into one-level disintegrating machine and secondary breaker, described sand water separation device is divided into one-level grit water separator and secondary grit water separator, wherein, rubbish receives bucket and is connected with the one-level disintegrating machine, and being connected with successively one-level grit water separator, secondary breaker, secondary grit water separator, described secondary grit water separator is connected with elevator pump.
The present invention also provides a kind of processing method of domestic waste, and its operating procedure is
(1) municipal garbage is weighed, even material toggling after broken bag, the mode that combines by machine screening, selection by winnowing and artificial separation will load in mixture rubbish and classify;
(2) organic waste after choosing is through break process;
(3) material after fragmentation first dilutes, and dilution is processed by the spiral deslagging and removed water-bed heavy inorganic matter, removes the floating thing of the water surface through grid, and all the other organic materials are further broken through the revolution crushing device;
(4) the organic waste material of removing inorganic matter carries out intermediate temperature anaerobic fermentation.
Preferably: load in mixture rubbish in described step (1) and classify after sorting when processing, the labile organic compound part enters pretreatment workshop reception bucket after the belt conveyor magnetic separation; Brick and tile are sent to the organoclay workshop, concentrate and send landfill disposal; Combustible send combustion plant to focus on according to combustible; Plastics send the recovery of classifying of plastics segmentations workshop, and recyclable plastics is not processed as combustible; Recyclable rubbish send the regrowth workshop, sells as regenerant.
Preferably: through the further pulverizing after sorting and magnetic separation of weight that selection by winnowing obtains, and be back to cylinder bag-broken screening machineifier and again sieve in described step (1).
Preferably: the water that in described step (3), the organic waste dilution is adopted is the recycle-water after water treatment system is processed through ammonia nitrogen removal.
Preferably: described step (4) anaerobic digestor charging solid content is 3-5%, and in tank, typical mean solids content is at 1.5-3%, and the time of staying, more than 22 days, the organic materials granularity was below 10mm.
Beneficial effect of the present invention is: the present invention has realized by being provided with sorting system, pretreatment system and anaerobic fermentation system: 1, innoxious: guarantee that treated house refuse, sewage really realizes innoxious, natural environment is not polluted, does not threaten health, beautify the Nature that the mankind depend on for existence, the green health home of building together; 2, resource: fully excavation can utilize regenerated resources, improves the resource reutilization rate, limited resource is able to effectively recycling; 3, minimizing: adopt high-tech means, make the discarded object of non-degradable and non-renewable utilization realize minimum quantization, to reduce discarded object to the pressure of environment for human survival.
Description of drawings
Fig. 1 is apparatus figure of the present invention.
Fig. 2 is process chart of the present invention.
The specific embodiment
The present invention will be further described below in conjunction with specific embodiment.
Apparatus figure as shown in Figure 1 as can be known, a kind for the treatment of system of domestic waste, it comprises sorting system, pretreatment system and anaerobic fermentation system.Sorting system comprises receiving cone, be positioned at the apron feeder of receiving cone bottom, evenly material toggling bag-breaking device and cylinder bag-broken screening machineifier, is provided with bag-breaking device and screen cloth in described cylinder bag-broken screening machineifier, and the sieve diameter of screen cloth is 60-90mm.Wherein, apron feeder is connected with the import of even material toggling bag-breaking device, and evenly the outlet of material toggling bag-breaking device is connected with large part selection platform, and large part selection platform is connected with cylinder bag-broken screening machineifier; Cylinder bag-broken screening machineifier also is connected with pneumatic separation device and sorting platform, and described pneumatic separation device is connected with light materials sorting platform and heavy substance sorting platform; Wherein, heavy substance sorting platform is connected with cylinder bag-broken screening machineifier with super power crusher by ferromagnetic deironing device successively.The sorting platform is connected with pretreatment system.Be provided with ferromagnetic deironing device between sorting platform and pretreatment system.Pretreatment system comprises that breaker, sand water separation device and the rubbish that is connected with the sorting platform receive bucket, and rubbish receives bucket and is connected with the sand water separation device with breaker by conveyer.Breaker is divided into one-level disintegrating machine and secondary breaker, described sand water separation device is divided into one-level grit water separator and secondary grit water separator, wherein, rubbish receives bucket and is connected with the one-level disintegrating machine, and being connected with successively one-level grit water separator, secondary breaker, secondary grit water separator, described secondary grit water separator is connected with elevator pump.Sand water separation device inside is provided with deslagging spiral, grid, gas/water circle device and revolution crushing device; The sand water separation device is connected with anaerobic fermentation system by elevator pump.Anaerobic fermentation system comprises the homogeneous pond that is connected with elevator pump, and the homogeneous pond is connected with anaerobic digestor; Anaerobic digestor is connected with marsh gas purifying, electricity generation system and sludge storage pool respectively, and described sludge storage pool also is connected with mud and water treatment system.
Fig. 2 is process chart of the present invention.
Embodiment 1
A kind of processing method of domestic waste, its operating procedure is:
(1) municipal garbage is weighed, even material toggling after broken bag, the mode that combines by machine screening, selection by winnowing and artificial separation will load in mixture rubbish and classify;
(2) organic waste after choosing is through break process;
(3) material after fragmentation first dilutes, and dilution is processed by the spiral deslagging and removed water-bed heavy inorganic matter, removes the floating thing of the water surface through grid, and all the other organic materials are further broken through the revolution crushing device;
(4) the organic waste material of removing inorganic matter carries out intermediate temperature anaerobic fermentation.
Wherein, load in mixture rubbish in step (1) and classify after sorting when processing, the labile organic compound part enters pretreatment workshop reception bucket after the belt conveyor magnetic separation; Brick and tile are sent to the organoclay workshop, concentrate and send landfill disposal; Combustible send combustion plant to focus on according to combustible; Plastics send the recovery of classifying of plastics segmentations workshop, and recyclable plastics is not processed as combustible; Recyclable rubbish send the regrowth workshop, sells as regenerant.
Through the further pulverizing after sorting and magnetic separation of weight that selection by winnowing obtains, and be back to cylinder bag-broken screening machineifier and again sieve in step (1).
The water that in step (3), the organic waste dilution is adopted is the recycle-water after water treatment system is processed through ammonia nitrogen removal.
Anaerobic digestor charging solid content is 3%, and in tank, typical mean solids content is 1.5%, and 22 days time of staying, the organic materials granularity is 10mm, and degradation effect of organic compound is high, and factor of created gase is also high.
Embodiment 2
As different from Example 1, the technological parameter during anaerobic fermentation is different, and anaerobic digestor charging solid content is 5%, and in tank, typical mean solids content is 3%, and 25 days time of staying, the organic materials granularity is 8mm, and degradation effect of organic compound is high, and factor of created gase is also high.
Embodiment 3
As different from Example 1, the technological parameter during anaerobic fermentation is different, and anaerobic digestor charging solid content is 4%, and in tank, typical mean solids content is 2.5%, and 30 days time of staying, the organic materials granularity is 5mm, and degradation effect of organic compound is high, and factor of created gase is also high.
What the present invention adopted is anaerobic fermentation, and wherein the pluses and minuses of aerobic fermentation and anaerobic fermentation relatively are shown in Table 1:
Table 1 aerobic fermentation and anaerobic fermentation comparative analysis
Anaerobic fermentation carbohydrate, protein and fat etc. under anaerobic, acting synergistically through various bacteria, at first resolve into the material of simple and stable, the continuation effect generates the main component of the biogas such as methane and carbon dioxide at last, is exactly briefly that organic matter is degraded to biogas by microbial process.
A degraded minute three phases carries out: at first, the bacterium of hydrolysis becomes monose with complicated organic substance decomposings such as polysaccharide, lipid, protein, as glucose (C
6H
12O
6).Second stage, acetic acid bacteria are converted into these sugar in the aliphatic acid that mainly is made of acetic acid.At last, methane backeria is converted into biogas with aliphatic acid again.
According to different bacterium optimum growth temperature section, anaerobic fermentation is divided into hot fermentation (42-75 ℃), mesophilic digestion (20-42 ℃) and cold fermentation (5-20 ℃).The present invention adopts mesophilic digestion (37 ℃).
The biogas that produces after fermentation generates electricity after purified treatment, and the mud after fermentation separately deals with through sludge treating system.
Process domestic waste 300t, daily generation 2.6 ten thousand KWh through system's of the present invention day.The native system floor space is little, the valuable material utilization rate is high in non-secondary pollution, rubbish.
Claims (10)
1. the treatment system of a domestic waste, it comprises sorting system, pretreatment system and anaerobic fermentation system, it is characterized in that:
Sorting system comprises receiving cone, be positioned at the apron feeder of receiving cone bottom, evenly material toggling bag-breaking device and cylinder bag-broken screening machineifier, wherein, apron feeder is connected with the import of even material toggling bag-breaking device, evenly the outlet of material toggling bag-breaking device is connected with large part selection platform, and large part selection platform is connected with cylinder bag-broken screening machineifier; Cylinder bag-broken screening machineifier also is connected with pneumatic separation device and sorting platform, and wherein, the sorting platform is connected with pretreatment system;
Pretreatment system comprises that breaker, sand water separation device and the rubbish that is connected with the sorting platform receive bucket, and rubbish receives bucket and is connected with the sand water separation device with breaker by conveyer; Described sand water separation device inside is provided with deslagging spiral, grid, gas/water circle device and revolution crushing device; Described sand water separation device is connected with anaerobic fermentation system by elevator pump;
Anaerobic fermentation system comprises the homogeneous pond that is connected with elevator pump, and the homogeneous pond is connected with anaerobic digestor; Anaerobic digestor is connected with marsh gas purifying, electricity generation system and sludge storage pool respectively, and described sludge storage pool also is connected with mud and water treatment system.
2. according to the treatment system of domestic waste claimed in claim 1, it is characterized in that: be provided with bag-breaking device and screen cloth in described cylinder bag-broken screening machineifier, wherein, the sieve diameter of screen cloth is 60-90mm.
3. according to the treatment system of domestic waste claimed in claim 1, it is characterized in that: described pneumatic separation device is connected with light materials sorting platform and heavy substance sorting platform; Wherein, heavy substance sorting platform is connected with cylinder bag-broken screening machineifier with super power crusher by ferromagnetic deironing device successively.
4. according to the treatment system of domestic waste claimed in claim 1, it is characterized in that: be provided with ferromagnetic deironing device between described sorting platform and pretreatment system.
5. according to the treatment system of domestic waste claimed in claim 1, it is characterized in that: described breaker is divided into one-level disintegrating machine and secondary breaker, described sand water separation device is divided into one-level grit water separator and secondary grit water separator, wherein, rubbish receives bucket and is connected with the one-level disintegrating machine, and being connected with successively one-level grit water separator, secondary breaker, secondary grit water separator, described secondary grit water separator is connected with elevator pump.
6. according to the processing method of domestic waste claimed in claim 1, it is characterized in that: its operating procedure is
(1) municipal garbage is weighed, even material toggling after broken bag, the mode that combines by machine screening, selection by winnowing and artificial separation will load in mixture rubbish and classify;
(2) organic waste after choosing is through break process;
(3) material after fragmentation first dilutes, and dilution is processed by the spiral deslagging and removed water-bed heavy inorganic matter, removes the floating thing of the water surface through grid, and all the other organic materials are further broken through the revolution crushing device;
(4) the organic waste material of removing inorganic matter carries out intermediate temperature anaerobic fermentation.
7. according to the processing method of domestic waste claimed in claim 6, it is characterized in that: load in mixture rubbish in described step (1) and classify after sorting when processing, the labile organic compound part enters pretreatment workshop reception bucket after the belt conveyor magnetic separation; Brick and tile are sent to the organoclay workshop, concentrate and send landfill disposal; Combustible send combustion plant to focus on according to combustible; Plastics send the recovery of classifying of plastics segmentations workshop, and recyclable plastics is not processed as combustible; Recyclable rubbish send the regrowth workshop, sells as regenerant.
8. according to the processing method of domestic waste claimed in claim 6, it is characterized in that: through the further pulverizing after sorting and magnetic separation of weight that selection by winnowing obtains, and be back to cylinder bag-broken screening machineifier and again sieve in described step (1).
9. the processing method of the domestic waste of stating according to claim 6 is characterized in that: the water that in described step (3), the organic waste dilution is adopted is the recycle-water after water treatment system is processed through ammonia nitrogen removal.
10. the processing method of the domestic waste of stating according to claim 6, it is characterized in that: described step (4) digester charging solid content is 3-5%, and in tank, typical mean solids content is at 1.5-3%, and the time of staying, more than 22 days, the organic materials granularity was below 10mm.
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103350100A (en) * | 2013-08-02 | 2013-10-16 | 东莞市粤源包装有限公司 | Method for continuously filling domestic garbage by using landfill site filled with domestic garbage |
| CN103357651A (en) * | 2013-07-11 | 2013-10-23 | 陈解生 | Household waste treatment system and treatment method thereof |
| CN104498532A (en) * | 2015-01-09 | 2015-04-08 | 青岛绿色家园环境设备有限公司 | Process for producing methane by mixing and fermenting organic wastes |
| CN104607437A (en) * | 2014-12-10 | 2015-05-13 | 广东源盛生态环保科技有限公司 | House-refuse rapid processing method based on combination application of microbe and machinery |
| CN104690063A (en) * | 2015-01-05 | 2015-06-10 | 桑德环境资源股份有限公司 | Crushing and sorting method of domestic garbage |
| CN105886330A (en) * | 2014-12-11 | 2016-08-24 | 北京中科洁能环境工程技术有限公司 | Municipal domestic solid waste integrated treatment process system |
| CN106540875A (en) * | 2015-09-21 | 2017-03-29 | 天津德为环保工程设备有限公司 | A kind of broken bag method when new domestic waste is sieved |
| CN107511389A (en) * | 2017-07-24 | 2017-12-26 | 深圳市海吉星环保有限责任公司 | A kind of household waste hydraulic sorting and pulping process and processing system |
| CN107511388A (en) * | 2017-07-24 | 2017-12-26 | 深圳市海吉星环保有限责任公司 | A kind of organic perishable garbage anaerobic fermentation cogeneration of heat and power biogas slurry fertilizer manufacture and system |
| CN108144951A (en) * | 2018-01-05 | 2018-06-12 | 孙向夷 | A kind of mobile garbage specification processing system |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005288209A (en) * | 2004-03-31 | 2005-10-20 | Jfe Engineering Kk | Separation method of refuse and separation apparatus thereof |
| JP2007260538A (en) * | 2006-03-28 | 2007-10-11 | Toshiba Corp | Organic waste treatment system |
| CN102030567A (en) * | 2010-10-25 | 2011-04-27 | 赵泽明 | Processing method for comprehensive utilization of solid household refuse |
| CN102794293A (en) * | 2011-05-27 | 2012-11-28 | 北京昊业怡生科技有限公司 | Method for comprehensively treating municipal solid waste |
| CN203209417U (en) * | 2013-02-01 | 2013-09-25 | 青岛胶南绿茵环保科技有限公司 | Municipal household garbage treatment system |
-
2013
- 2013-02-01 CN CN201310041980.5A patent/CN103084380B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005288209A (en) * | 2004-03-31 | 2005-10-20 | Jfe Engineering Kk | Separation method of refuse and separation apparatus thereof |
| JP2007260538A (en) * | 2006-03-28 | 2007-10-11 | Toshiba Corp | Organic waste treatment system |
| CN102030567A (en) * | 2010-10-25 | 2011-04-27 | 赵泽明 | Processing method for comprehensive utilization of solid household refuse |
| CN102794293A (en) * | 2011-05-27 | 2012-11-28 | 北京昊业怡生科技有限公司 | Method for comprehensively treating municipal solid waste |
| CN203209417U (en) * | 2013-02-01 | 2013-09-25 | 青岛胶南绿茵环保科技有限公司 | Municipal household garbage treatment system |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103357651A (en) * | 2013-07-11 | 2013-10-23 | 陈解生 | Household waste treatment system and treatment method thereof |
| CN103350100A (en) * | 2013-08-02 | 2013-10-16 | 东莞市粤源包装有限公司 | Method for continuously filling domestic garbage by using landfill site filled with domestic garbage |
| CN103350100B (en) * | 2013-08-02 | 2015-02-25 | 广东源盛生态环保科技有限公司 | Method for continuously filling domestic garbage by using landfill site filled with domestic garbage |
| CN104607437A (en) * | 2014-12-10 | 2015-05-13 | 广东源盛生态环保科技有限公司 | House-refuse rapid processing method based on combination application of microbe and machinery |
| CN105886330A (en) * | 2014-12-11 | 2016-08-24 | 北京中科洁能环境工程技术有限公司 | Municipal domestic solid waste integrated treatment process system |
| CN104690063A (en) * | 2015-01-05 | 2015-06-10 | 桑德环境资源股份有限公司 | Crushing and sorting method of domestic garbage |
| CN104498532A (en) * | 2015-01-09 | 2015-04-08 | 青岛绿色家园环境设备有限公司 | Process for producing methane by mixing and fermenting organic wastes |
| CN106540875A (en) * | 2015-09-21 | 2017-03-29 | 天津德为环保工程设备有限公司 | A kind of broken bag method when new domestic waste is sieved |
| CN107511389A (en) * | 2017-07-24 | 2017-12-26 | 深圳市海吉星环保有限责任公司 | A kind of household waste hydraulic sorting and pulping process and processing system |
| CN107511388A (en) * | 2017-07-24 | 2017-12-26 | 深圳市海吉星环保有限责任公司 | A kind of organic perishable garbage anaerobic fermentation cogeneration of heat and power biogas slurry fertilizer manufacture and system |
| CN108144951A (en) * | 2018-01-05 | 2018-06-12 | 孙向夷 | A kind of mobile garbage specification processing system |
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