CN102225419A - Garbage reduction equipment - Google Patents

Garbage reduction equipment Download PDF

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Publication number
CN102225419A
CN102225419A CN2011101583494A CN201110158349A CN102225419A CN 102225419 A CN102225419 A CN 102225419A CN 2011101583494 A CN2011101583494 A CN 2011101583494A CN 201110158349 A CN201110158349 A CN 201110158349A CN 102225419 A CN102225419 A CN 102225419A
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CN
China
Prior art keywords
gasification
reduction equipment
waste reduction
drying
primary tank
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CN2011101583494A
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Chinese (zh)
Inventor
李康敏
罗媚
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Individual
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Individual
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Priority to CN2011101583494A priority Critical patent/CN102225419A/en
Publication of CN102225419A publication Critical patent/CN102225419A/en
Priority to CN 201220194822 priority patent/CN202606487U/en
Priority to CN2012101341108A priority patent/CN102699012A/en
Pending legal-status Critical Current

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Abstract

The invention relates to garbage reduction equipment which comprises a control system, and a lifting and charging system, a conveying and drying system, a gasifying system, a discharging system and a gasified and purifying system that are electrically connected with the control system, as well as a final assembly operation room, wherein all the systems are arranged in the final assembly operation room, the gasifying system consists of a main container, and a gas chamber used for storing positive pressure gas is arranged on the outer wall of the main container and communicated with the inner cavity of the main container at least one through hole. The garbage reduction equipment has mobility, can be fast assembled and transported, thus being not required for occupying permanently fixed place; the final assembly operation room is built on the basis of the dimension of a standard container, thus realizing the standardization and modularization during designing, manufacturing and transporting processes; and the gas chamber used for storing positive pressure gas is arranged on the outer wall of the main container and communicated with the inner cavity of the main container, thus realizing that air in the main container is stirred and aerated so as to greatly improve garbage reduction with maximum proportion of 95%.

Description

A kind of waste reduction equipment
Technical field
The present invention relates to a kind of technology of garbage disposal field, more specifically, relate to a kind of waste reduction equipment.
Background technology
Rapid expansion along with Increase of population and city size, the processing of municipal refuse is subjected to people's attention more and more, but objectively because the scale of garbage disposal and the development that scope lags behind the city to a certain extent, a large amount of house refuses has little time effective disposal, so that causes serious environmental problem day by day.People adopt the mode disposal of refuse of digging pit landfill or building destructor plant at the periphery in city usually at present, but landfill does not almost have the processing of essence to rubbish, it is except meeting takies a large amount of land resource, mode that also can be by polluted underground water or loss gas by landfill material pollutes the health of last harm humans to people's living environment; The infusion of financial resources that destructor plant needs is big, the construction period is long and set up, and in case build finish after, if need resettlement because of other conditions change, its process will be very difficult, not have mobility, so only be applicable to usually large scale rubbish is handled.And for areas such as some remote cities and towns, factory, heavy construction building site, rural areas, the rubbish of some is also made in these areas on the one hand, the demand that refuse treatment plant is had reality, on the other hand because its geographical position is more remote, if these rubbish are all transported to remote large-scale destructor plant to be handled, its cost will be too high, unlikely obtains implementing; In addition, post-processed for some natural calamities or accident, often also follow a large amount of garbage-cleanings, such as cleaning of the scene behind earthquake, the tsunami and rebuilding in disaster-hit areas, these situations have not only required refuse treatment plant on the scene, and the timeliness of marching into the arena and handling of refuse treatment plant all there is extremely strong susceptibility, existing trash processing way can not satisfy above-mentioned requirements at all, based on above reason, people are detachable to some, mobility strong and the high refuse treatment plant of treatment effeciency have urgent demand.
Summary of the invention
Purpose of the present invention overcomes the deficiencies in the prior art exactly, and a kind of waste reduction equipment is provided, and the primary clustering of this equipment all is integrated in the general assembly operating room, dismounting and transportation easily, and mobility is very strong; Simultaneously, the general assembly operating room is based on container, also realized the standardization and the modularization of design, manufacturing, transportation.
In order to reach above purpose, by the following technical solutions:
A kind of waste reduction equipment, comprise control system and the lifting charging system that is electrically connected with control system, carry drying system, gasification system, the gentle gasification cleaning system of discharge system, also comprise the general assembly operating room, above-mentioned each system integration is installed in the general assembly operating room, wherein:
Promote charging system and be used to promote pretreated rubbish to carrying drying system;
Carry drying system to be used for rubbish is carried out drying and it is conveyed into primary tank;
Gasification system is used for rubbish to the drying decrement that gasifies;
Discharge system is used to discharge the residue through after the gasification decrement;
Gasification gas cleaning system is used for the steam of the gasification gas of gasification system generation and the generation of rubbish drying is purified.
Further, the outer wall of described primary tank is provided with the air chamber that is used to store barotropic gas, and described air chamber is communicated with by at least one through hole with the inner chamber of primary tank.
Further, the aperture of described through hole is between 1mm~20mm.
Again further, the air pressure of described air chamber is between 100Pa~2000Pa.
In order to form liquid mist reaction, described gasification system is provided with the spray reaction shower nozzle in primary tank, and described spray reaction shower nozzle is communicated with the container that is used for carrying liquid, and described liquid can resolve into combustion-supporting gas when being heated to more than 100 ℃ temperature.
Further, described conveying drying system is provided with the movable passageway that is used to shift rubbish, described movable passageway is connected to form circulating conveyer belt in turn by the exotic material head and the tail, and an end of described conveyer belt connects the lifting charging system, and the other end extends into primary tank.
Further, the gasification gas that described gasification system produces is discharged by the feeding space at described movable passageway place, simultaneously sending material is carried out heat drying.
In order to make the gasification gas can qualified discharge, described gasification gas cleaning system comprises re-heat heat build-up reactor, the gentle gasification washing system of combination dust pelletizing system that connects in turn, described re-heat heat build-up reactor is provided with heater, and described heater can make the temperature of re-heat heat build-up reactor be higher than 850 degree.
Further, described general assembly operating room is provided with the multifunction gate that is used to operate and overhaul waste reduction equipment in its sidewall, and the top of described multifunction gate flexibly connects by rotating shaft and general assembly operating room.
Further, described general assembly operating room is that inside dimension is respectively the TEU (Twenty-foot Equivalent Unit) of 5.69m*2.13m*2.18m or 11.8m*2.13m*2.18m or 13.58m*2.34m*2.71m or is the combination cabinet of minimum dimension unit with above TEU (Twenty-foot Equivalent Unit).
Compared with prior art, beneficial effect of the present invention is:
Each system integration of waste reduction equipment is installed in the general assembly operating room, makes equipment possess mobility, realized the fast assembling-disassembling and the transfer of equipment, need not to take permanent fixed venue, solved problems such as addressing, change of address difficulty; The structure of general assembly operating room is of a size of the basis with TEU (Twenty-foot Equivalent Unit), has realized standardization and the modularization of equipment in design, manufacturing, transportation; Outer wall at primary tank is provided with the air chamber that is used to store malleation that is communicated with the primary tank inner chamber, has realized the air in the primary tank is stirred and local oxygenation, and waste reduction efficient is improved greatly, and maximum decrement ratio can reach 95%; Simultaneously, the heat energy gasification is equipped with sprays the solution that can be decomposed into combustion-supporting gas by the spray reaction shower nozzle in primary tank, realized the purification to air when improving efficiency of combustion.
Description of drawings
Fig. 1 is the front view of waste reduction equipment of the present invention.
Fig. 2 is the vertical view of waste reduction equipment of the present invention.
Fig. 3 is the container dodge gate schematic diagram that is used for fixing waste reduction equipment of the present invention.
Fig. 4 is the process chart of waste reduction equipment of the present invention work.
Fig. 5 is the conveying drying system schematic diagram of waste reduction equipment of the present invention.
Fig. 6 is the formation schematic diagram of the sharp-pointed winddorn of waste reduction equipment of the present invention.
Among the figure: 1-promotes charging system; 2-re-heat heat build-up reactor; The 3-control system; 4-makes up dust pelletizing system; 5-gasification gas cleaning system; 6-takes out air-introduced machine; 7-gasification gas exhaust system; 71-gasification gas floss hole; 8-carries drying system; The 81-conveyer belt; The 9-heating system; The 10-discharge system; 11-general assembly operating room; The 12-gasification system; The 120-primary tank; The 121-air chamber; The sharp-pointed winddorn of 122-; 13-general assembly operating room bottom surface; 14-spray reaction shower nozzle; The 15-through hole; The 16-multifunction gate; The 17-portable hopper.
The specific embodiment
Below in conjunction with drawings and the specific embodiments, the present invention made further specify:
Referring to Fig. 1, Fig. 2, a kind of waste reduction equipment of the present invention, comprise control system 3 and the lifting charging system 1 that is electrically connected with control system 3, carry drying system 8, gasification system 12, discharge system 10 gentle gasification cleaning systems, also comprise general assembly operating room 11, above-mentioned each system integration is installed in the general assembly operating room 11, wherein:
Promote charging system 1 and be used to promote pretreated rubbish to carrying drying system 8;
Carry drying system 8 to be used for rubbish is carried out drying and it is conveyed into primary tank 120;
Gasification system 12 is used for rubbish to the drying decrement that gasifies;
Discharge system 10 is used to discharge the residue through after the gasification decrement;
Gasification gas cleaning system 5 is used for the steam of the gasification gas of gasification system 12 generations and the generation of rubbish drying is purified.
Gasification system 12 includes primary tank 120, the outer wall of primary tank 120 is provided with the air chamber 121 that is used to store barotropic gas, above-mentioned air chamber 121 is communicated with by at least one through hole 15 with the inner chamber of primary tank 120, wherein air chamber 121 is connected with air compression plant, the air pressure of described air chamber 121 is between 100Pa~2000Pa, the aperture of through hole 15 is between 1mm~20mm, gasification system 11 also is provided with spray reaction shower nozzle 14 in primary tank 120, this spray reaction shower nozzle 14 is communicated with the container that is used for carrying liquid, described liquid can resolve into combustion-supporting gas when being heated to more than 100 ℃ temperature, carry drying system 8 also to be provided with the movable passageway that is used to shift rubbish, this movable passageway is connected to form circulating conveyer belt 81 in turn by the exotic material head and the tail, one end of conveyer belt 81 connects lifting charging system 1, the other end extends into primary tank 120, in order to make full use of the heat of gasification gas, the gasification gas that gasification system 12 produces is discharged by the feeding space at above-mentioned movable passageway place, gasification gas cleaning system comprises the re-heat heat build-up reactor 2 that connects in turn, combination dust pelletizing system 4 gentle gasification washing systems 5, described re-heat heat build-up reactor 2 is provided with heater, and described heater can make the temperature of re-heat heat build-up reactor 2 be higher than 850 degree.
Realize fast assembling-disassembling and transfer in order to make waste reduction equipment of the present invention, adopt at present general TEU (Twenty-foot Equivalent Unit) as the general assembly operating room, for example, inside dimension is set is respectively 5.69m*2.13m*2.18m (20 chi), (11.8m*2.13m*2.18m 40 chi), the ISO freight container of (13.58m*2.34m*2.71m 45 chi) or other sizes or be that the combination cabinet of minimum dimension unit is as the general assembly operating room with above TEU (Twenty-foot Equivalent Unit), wherein the work of waste reduction equipment the time partly is above standard the parts of Container Dimensions (as portable hopper 17, gasification gas floss hole 71 etc.) all be designed to quick-detachable movable part, and reserved the relevant position in general assembly operating room bottom surface 13 for it.When shipment, can carry out integral hoisting to general assembly operating room 11, transhipment is convenient; Wait to unload in place after, with portable hopper 17, gasification gas floss hole 71 movable parts such as grade splice the fixing operation of can starting shooting again, easy and simple to handle, simultaneously because general assembly operating room 11 is standard size, so nature and existing vehicles compatibility also help to allow the miscellaneous part of waste reduction equipment realize standardization, modular production simultaneously.Referring to Fig. 3, in order to give waste reduction equipment reservation operations and the maintenance room of being fixed in the general assembly operating room 11, general assembly operating room 11 is provided with multifunction gate 16 in its sidewall, the top of this multifunction gate 16 flexibly connects by rotating shaft and general assembly operating room 11 bodies, these multifunction gate 16 closures can make 11 sealings of general assembly operating room, unlatching can be each operation position the space is provided, and also has the function of sun-shading rain-proof simultaneously concurrently.
Based on above structure, referring to Fig. 4, waste reduction equipment of the present invention, its course of work is divided into following steps:
1, rubbish screening: the house refuse of collecting is carried out sorting by the refuse classification system, to plastics, metal, the inorganic matter otherwise processed such as (as earth) of sieving out, with main component is that organic part is transferred to waste reduction device processes of the present invention, for the latter, concrete will putting into respectively or together through the changing food waste of press filtration with through the garden garbage of pulverizing exactly promotes charging system 1.
2, pan feeding: promoting charging system 1 is that organic rubbish quantitatively promotes and renders to the conveying drying system 8 from material receiving port with above-mentioned main component, referring to Fig. 5, carry drying system 8 to comprise that mainly connects a movable passageway that promotes charging system 1 and gasification system 12, this movable passageway constitutes circulating conveyer belt 81 by exotic material, above-mentioned exotic material is preferably metal bracelet (plate) in this specific embodiment, during the work of waste reduction equipment, conveyer belt 81 is sent pending thing into primary tank 120 by the adjustable translational speed of per minute 1~300cm, because of its good conductive force, conveyer belt 81 is about to self heat through primary tank 120 time and reaches 60~500 ℃, it continues to accept and carry rubbish on the one hand when returning back to material receiving port, utilize the opposed rubbish thereon of waste heat of metallic object itself to dry on the other hand, circulation and so forth can as often as possible be removed near the moisture in the conveyer belt part rubbish.Simultaneously, because the circulation passage of the gasification gas that the feeding space at movable passageway place also is simultaneously a gasification system 12 to produce, and its temperature of gasification gas that flows out primary tank 120 is generally 150~850 ℃, so with above process synchronously, the rubbish of movable passageway middle and upper part is air-dry by the waste heat of gasification gas, two combine, and can reduce the water content of pending thing in course of conveying and remove the part percolate, and this design has reduced the energy consumption of gasification and guaranteed that the gasification decrement of rubbish is more abundant; By above-mentioned movable passageway, thing to be processed is transmitted and enters primary tank 120.
3, gasification decrement: referring to Fig. 6, be positioned at the air chamber 121 of primary tank 120 outer walls and primary tank 120 inner chambers separately by refractory layer, owing to have the different through hole of big measuring angle 15 on the refractory layer, when air compression plant feeds malleation in air chamber 121, gas permeation through hole 15 in the air chamber 121 enters the lower primary tank of air pressure 120 inner chambers and forms the jet that length is 100~1000mm (being sharp-pointed winddorn 122), this sharp-pointed winddorn 122 stirs air on the one hand, make air and treat that vapour fully contacts, can enter each corner of primary tank 120 inner chambers on the other hand, realized local oxygenation, made gasification more abundant.(necessary minimum air capacity claims theoretical combustion air during fuel completing combustion under ideal conditions at excess air coefficient, the required air capacity of fuel completing combustion or imperfect combustion is the Actual combustion air capacity under physical condition, excess air coefficient m=Actual combustion air capacity/theoretical combustion air) less than under 1 the condition, the dynamically quick decrement of pending rubbish, and the gas of generation is more fully decomposed.Form synchronously with sharp-pointed winddorn 122, after rubbish enters primary tank 120, spray reaction shower nozzle 14 beginnings sprayed solution in primary tank 120 inner chambers that primary tank 120 is equipped with, the heat of meeting this solution promptly resolves into combustion-supporting gas and helps to carry out gasification reaction, because of the difference of solution formula also can realize catharsis to gasification gas, in practice, the efficiency of dust collection of hydrojet mist can reach 25-65% in primary tank 120, and gasification gas purification efficiency can reach 20%-60%.
In order to make reaction more abundant, gasification makes temperature be controlled to be 250 ℃-850 ℃ by control system 3 and heating system 9, and oxygen concentration is controlled to be 1%-7%, and the environment of object being treated is more suitable in carrying out reduction reaction.In addition, according to the characteristics of object being treated, also can determine the decrement ratio of rubbish in the various objectives of comprehensive utilization or security landfill, this decrement ratio can be regulated between 50%-95%.Normally say, need landfill as residue, the temperature that then raises also increases oxygen concentration, makes gasification more abundant; Need fully utilize as residue, then corresponding reduction gasification temperature is suitably controlled the decrement ratio.
4, discharging: the residue main component after the gasification decrement is a simple substance carbon, this part material can directly be discharged through discharge system 10, residue after the eliminating as required can be to its comprehensive utilization or outward transport landfill, as the garden garbage mainly formed by the residual branch of plant, dust etc. after gasification system 12 processing, can become well-behaved garden fertilizer, entering the afforestation comprehensive utilization, do not need landfill disposal, can not cause secondary pollution.
5, gasification gas purifies: by the control to excess air coefficient and correlative factor in the gasification decrement process, every cubic metre of handled thing handling through gasification abatement system 12 produces tolerance and is about 200-2500m 3/ h, flow velocity 0.5-8m/s, the vapor mixing that this portion gas and drying garbage produce is after purified by gasification gas cleaning system.Because of above gas based on steam and carbon dioxide, so carrying out combined gasifying gas to it, this equipment purifies, specifically, gasification gas cleaning system comprises that again the re-heat heat build-up reactor 2, combination dust pelletizing system 4, the gasification air purge that connect in turn wash system's 5 several sections; Wherein, re-heat heat build-up reactor 2 is provided with heater the gasification gas that produces in the primary tank 120 is heated once more, make gas reach uniform temperature (>850 ℃) and stop certain hour to reach the purpose that the pernicious gas that makes in the gas more thoroughly decomposes, heater can make electricity consumption or fuel as the energy; Combination dust pelletizing system 4 places are provided with the filter screen that is used for dust removal by filtration, can remove most of solid particle in the gasification gas; Be provided with the material that active carbon etc. has adsorptivity in the gasification gas cleaning system 5, can further remove the toxic gas in the gasification gas.After purifying, still have the gasification gas of temperature at first to carry out circulating and recovering, these gases are extracted into air exhauster 6 and carry the pending thing of drying system 8 heating, redundance gas then enters into gasification gas exhaust system 7 qualified discharges, has promptly finished the gasification decrement treatment to rubbish to this.
Certainly; should be understood that; the disclosed content of above specific embodiment only is a part preferred version of the present invention; every based on technical scheme of the present invention, technical spirit according to the invention, belong to those skilled in the art and need not to carry out the enforcement that creative work can obtain and all should belong to protection scope of the present invention.

Claims (10)

1. waste reduction equipment, comprise control system and the lifting charging system that is electrically connected with control system, carry drying system, gasification system, the gentle gasification cleaning system of discharge system, it is characterized in that, also comprise the general assembly operating room, above-mentioned each system integration is installed in the general assembly operating room, wherein:
Promote charging system and be used to promote pretreated rubbish to carrying drying system;
Carry drying system to be used for rubbish is carried out drying and it is conveyed into primary tank;
Gasification system is used for rubbish to the drying decrement that gasifies;
Discharge system is used to discharge the residue through after the gasification decrement;
Gasification gas cleaning system is used for the steam of the gasification gas of gasification system generation and the generation of rubbish drying is purified.
2. waste reduction equipment as claimed in claim 1 is characterized in that described gasification system includes primary tank, and the outer wall of described primary tank is provided with the air chamber that is used to store barotropic gas, and described air chamber is communicated with by at least one through hole with the inner chamber of primary tank.
3. waste reduction equipment as claimed in claim 2 is characterized in that the aperture of described through hole is between 1mm~20mm.
4. waste reduction equipment as claimed in claim 2 is characterized in that described air chamber is connected with air compression plant, and the air pressure of described air chamber is between 100Pa~2000Pa.
5. waste reduction equipment as claimed in claim 2, it is characterized in that, described gasification system is provided with the spray reaction shower nozzle in primary tank, described spray reaction shower nozzle is communicated with the container that is used for carrying liquid, and described liquid can resolve into combustion-supporting gas when being heated to more than 100 ℃ temperature.
6. waste reduction equipment as claimed in claim 1, it is characterized in that, described conveying drying system is provided with the movable passageway that is used to shift rubbish, described movable passageway is connected to form circulating conveyer belt in turn by the exotic material head and the tail, one end of described conveyer belt connects the lifting charging system, and the other end extends into primary tank.
7. waste reduction equipment as claimed in claim 6 is characterized in that, the gasification gas that described gasification system produces is discharged by the feeding space at described movable passageway place, simultaneously sending material is carried out heat drying.
8. waste reduction equipment as claimed in claim 1, it is characterized in that, described gasification gas cleaning system comprises re-heat heat build-up reactor, the gentle gasification washing system of combination dust pelletizing system that connects in turn, described re-heat heat build-up reactor is provided with heater, and described heater can make the temperature of re-heat heat build-up reactor be higher than 850 degree.
9. waste reduction equipment as claimed in claim 1 is characterized in that, described general assembly operating room is provided with the multifunction gate that is used to operate and overhaul waste reduction equipment in its sidewall, and the top of described multifunction gate flexibly connects by rotating shaft and general assembly operating room.
10. waste reduction equipment as claimed in claim 1, it is characterized in that described general assembly operating room is that inside dimension is respectively the TEU (Twenty-foot Equivalent Unit) of 5.69m*2.13m*2.18m or 11.8m*2.13m*2.18m or 13.58m*2.34m*2.71m or is the combination cabinet of minimum dimension unit with above TEU (Twenty-foot Equivalent Unit).
CN2011101583494A 2011-06-14 2011-06-14 Garbage reduction equipment Pending CN102225419A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
CN2011101583494A CN102225419A (en) 2011-06-14 2011-06-14 Garbage reduction equipment
CN 201220194822 CN202606487U (en) 2011-06-14 2012-05-03 Garbage conversion reduction processing device
CN2012101341108A CN102699012A (en) 2011-06-14 2012-05-03 Garbage diversion reduction treatment process as well as equipment implementing same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011101583494A CN102225419A (en) 2011-06-14 2011-06-14 Garbage reduction equipment

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CN102225419A true CN102225419A (en) 2011-10-26

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CN2011101583494A Pending CN102225419A (en) 2011-06-14 2011-06-14 Garbage reduction equipment
CN 201220194822 Expired - Fee Related CN202606487U (en) 2011-06-14 2012-05-03 Garbage conversion reduction processing device
CN2012101341108A Pending CN102699012A (en) 2011-06-14 2012-05-03 Garbage diversion reduction treatment process as well as equipment implementing same

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Application Number Title Priority Date Filing Date
CN 201220194822 Expired - Fee Related CN202606487U (en) 2011-06-14 2012-05-03 Garbage conversion reduction processing device
CN2012101341108A Pending CN102699012A (en) 2011-06-14 2012-05-03 Garbage diversion reduction treatment process as well as equipment implementing same

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102699012A (en) * 2011-06-14 2012-10-03 李康敏 Garbage diversion reduction treatment process as well as equipment implementing same
CN103480631A (en) * 2013-09-18 2014-01-01 李康敏 Catering industry and garden biomass waste resource recycling and comprehensive utilization process
CN104148372A (en) * 2014-07-25 2014-11-19 李英军 Pretreatment device and pretreatment method for volume reduction and dehumidification of garbage

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WO2014067908A2 (en) * 2012-11-02 2014-05-08 Robert Stöcklinger Device and method for obtaining at least one pure substance from biological waste or biomass
CN106281996B (en) * 2015-05-15 2018-10-19 常州益优新能源有限公司 Modularized bioreactor for handling organic waste

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Publication number Priority date Publication date Assignee Title
JP3896750B2 (en) * 2000-01-14 2007-03-22 松下電工株式会社 Garbage disposal equipment
JP2005349282A (en) * 2004-06-09 2005-12-22 Inax Corp Garbage treatment apparatus
CN1301807C (en) * 2004-08-06 2007-02-28 北京厨房设备集团公司 Domestic refuse sorting and treating system and treating process thereof
CN101036916A (en) * 2007-04-24 2007-09-19 大连理工大学 Domestic waste comprehensive treatment technology based on the pre-processing
CN101979921B (en) * 2010-10-13 2012-07-04 上海泰欣环保设备成套有限公司 Process for spraying and treating percolate
CN102225419A (en) * 2011-06-14 2011-10-26 李康敏 Garbage reduction equipment

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102699012A (en) * 2011-06-14 2012-10-03 李康敏 Garbage diversion reduction treatment process as well as equipment implementing same
CN103480631A (en) * 2013-09-18 2014-01-01 李康敏 Catering industry and garden biomass waste resource recycling and comprehensive utilization process
CN103480631B (en) * 2013-09-18 2016-05-11 李康敏 Food and drink gardens biomass castoff resources circulation comprehensive utilization process
CN104148372A (en) * 2014-07-25 2014-11-19 李英军 Pretreatment device and pretreatment method for volume reduction and dehumidification of garbage
CN104148372B (en) * 2014-07-25 2016-09-21 李英军 A kind of rubbish volume reduction dehumidification pretreatment unit and preprocess method

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Open date: 20111026