CN101381646A - Handling arrangement for recovering and utilizing organic solid rubbish - Google Patents
Handling arrangement for recovering and utilizing organic solid rubbish Download PDFInfo
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- CN101381646A CN101381646A CNA2008101991839A CN200810199183A CN101381646A CN 101381646 A CN101381646 A CN 101381646A CN A2008101991839 A CNA2008101991839 A CN A2008101991839A CN 200810199183 A CN200810199183 A CN 200810199183A CN 101381646 A CN101381646 A CN 101381646A
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- charing
- pressure cylinder
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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Abstract
The invention discloses a treatment device for recycling of organic solid garbage, which belongs to the technical field of garbage recovery and treatment devices. The treatment device for recycling of the organic solid garbage comprises a drying section (1), a pressurization section (2), and a high-temperature carbonization section (3) which are orderly connected. With the structure, the device, by changing organic domestic garbage into carbon coal for recycling, realizes the complete recycling of domestic garbage, particularly solid matters of the domestic garbage, avoids the pollution to the environment, and transforms waste into fuel with economic value at the same time. The device is suitable for sustainable production, and has the advantages of high production efficiency, low treatment cost, and low energy consumption.
Description
Technical field
The invention belongs to the technical field of refuse reclamation treatment unit, specifically be meant the treatment unit that a kind of organic solid rubbish is recycled.
Background technology
At present, application of city life garbage is big public hazards of harm social economy Sustainable development, also is unique a kind of potential resources that is increasing on the earth.How scientificlly and effectively to handle the application of city life garbage of contaminated soil, water body, atmosphere, damage to the environment quality and HUMAN HEALTH, reasonably utilize recyclable or reproducible resource in the rubbish, realizing the target of application of city life garbage minimizing, innoxious and recycling treatment, is emphasis, the focus environmental protection problem that countries in the world are very paid close attention to and puted forth effort to study.Be protection existent environment of people and ecotope, the processing of rubbish is more and more important.Along with the raising of rapid economic development, people's material and cultural life, bigger variation is all taking place in domestic refuse aspect the quality and quantity two in recent years.Past rubbish is based on food and organic waste, the present then plastics that rolled up stationery and be difficult to decompose.Life refuse processing method mainly contains landfill method, burning method and recycling method at present.The shortcoming of burying the method for filling out is that sanitary fill is rolled, bury capping, take a large amount of soils, because various plastic garbages account for 40-60% (the application of city life garbage total amount is more than 70%), can not rot for many years, the soil that landfill is crossed rubbish generally can not use as ploughing; Burning method can cause topsoil, must handle the remaining rubbish in burning back; The recycling method is comparatively ideal waste disposal method, as domestic refuse being formed methane or, being made into fertilizer etc., but can producing remaining rubbish by heap fermentation, all reach the environment that causes secondary pollution easily over a long time, infringement eco-environmental quality and HUMAN HEALTH.The processing of existing organic waste also has by the mode of charing to be undertaken, but the carbonizing apparatus complex structure, production efficiency is low, and energy consumption is also higher.
Summary of the invention
The object of the present invention is to provide a kind of organic domestic waste can the recycling, can protect environment, can obtain the treatment unit of the organic solid rubbish recycling of economic benefit again.
For solving the problems of the technologies described above, the technical solution used in the present invention is: the treatment unit that organic solid rubbish is recycled is characterized in that comprising the dryer section, pressurized segment and the high temperature carbonization section that are linked in sequence.Described dryer section mainly by drying cylinder, be arranged on drying heater on the drying cylinder, wet pumping unit, rotationally be arranged on pushing ram in the drying cylinder, drive the motor that pushing ram rotates and form, the head end of drying cylinder is provided with opening for feed, tail end is provided with discharge port, pushing ram is provided with axially extended screw-blade, the external diameter of screw-blade and the internal diameter of drying cylinder adapt, and the inlet of wet pumping unit is connected in the drying cylinder.Described pressurized segment mainly is made up of the pressure thruster that adds pressure cylinder and be arranged in the input terminus that adds pressure cylinder, the described input terminus that adds pressure cylinder connects discharge port, and the sectional area of internal space that adds the output terminal of pressure cylinder little by little dwindles along the direction of propulsion of pressure thruster.Described high temperature carbonization section mainly is made up of charing tube, the charing well heater, the water cooler that are arranged on the charing tube, the input terminus of described charing tube is connected on the output terminal that adds pressure cylinder, the sectional area of the internal space of charing tube is long-pending identical with the inner section of the input port that adds pressure cylinder, and water cooler is arranged on the output terminal of charing tube.
When the present invention works, organic waste after pulverizing is put into from the opening for feed of dryer section, drying heater heats to strengthen the evaporation of moisture the organic waste in the drying cylinder, wet pumping unit is extracted the steam that produces out, the electric motor driving pushing ram rotates, and screw-blade and then rotates, and the organic waste in the drying cylinder can be promoted from head end toward tail end, also stir organic waste when promoting, improve drying efficiency.Also can realize the control of degree of drying when dry by adjusting drying temperature or exsiccant time.When organic rubbish enter along discharge port add in the pressure cylinder after, pressure thruster pushes away organic waste toward the output terminal that adds pressure cylinder, because the sectional area of the internal space of output terminal little by little dwindles just compacted compacting constantly of organic waste.After the compacted compacting of organic waste, pressure thruster pushes organic waste in the internal space of charing tube, this moment, organic waste still kept compacted condition, the charing well heater can heat the organic waste in the charing tube, organic waste high temperature and with the isolated condition of air under formed the charcoal coal by charing, the temperature of control charing well heater and the fltting speed of pressure thruster are the temperature and time of may command charing.From the output of the output terminal of charing tube, can lower the temperature to the charcoal coal after the charing by water cooler under the effect of pressure thruster for the charcoal coal, prevents spontaneous combustion behind its ingress of air.
Owing to adopted above-mentioned structure, the present invention utilizes by organic domestic waste being become the charcoal coal again, realization is to the particularly thorough recycling of its solids of domestic refuse, solved pollution to environment, simultaneously refuse is transformed into the fuel of economically valuable, suitable the continuing of the present invention produces, and has the production efficiency height, processing cost is low, advantage of low energy consumption.
Description of drawings
Fig. 1 is the sectional view of the treatment unit of organic solid rubbish recycling;
Fig. 2 is the sectional view of another embodiment of pressurized segment;
Fig. 3 is the front view of screw-blade, groove, washer;
Fig. 4 is the sectional view along A among Fig. 3-A line;
Fig. 5 is the sectional view of another state of Fig. 4.
Comprise among the figure: dryer section 1, pressurized segment 2, high temperature carbonization section 3, discharging section 4, drying cylinder 10, drying heater 11, wet pumping unit 12, pushing ram 13, motor 14, opening for feed 15, discharge port 16, screw-blade 17, groove 18, slide block 19, washer 20, add pressure cylinder 21, interior pillar stiffener 22, pressurization pushing ram 23, pressurization motor 24, pressurization screw-blade 25, piston 26, pressing machine 27, charing tube 31, charing well heater 32, water cooler 33, vacuum fan 34.
Embodiment
Below in conjunction with accompanying drawing the specific embodiment of the present invention is described in further detail, but does not constitute any limitation of the invention.
As shown in Figure 1, the treatment unit that organic solid rubbish of the present invention is recycled comprises the dryer section 1, pressurized segment 2 and the high temperature carbonization section 3 that are linked in sequence.
Described dryer section 1 mainly by drying cylinder 10, be arranged on drying heater 11 on the drying cylinder 10, wet pumping unit 12, rotationally be arranged on pushing ram 13 in the drying cylinder 10, drive the motor 14 that pushing ram 13 rotates and form.The drying cylinder 10 of embodiment is three sections among the figure, and each section horizontal parallel setting and end to end can provide longer drying distance taking under the equal length spatial condition like this.Drying cylinder 10 is made by thermal conduction good metal materials such as iron and steel, and the head end top of each section drying cylinder 10 is provided with opening for feed 15, and the tail end bottom is provided with discharge port 16.Drying heater 11 can be nichrome wire, is arranged on the Lower Half of drying cylinder 10, can the organic waste in the drying cylinder 10 be heated during the nichrome wire energising.The two ends of pushing ram 13 are located in the axis hole at drying cylinder 10 two ends rotationally, also can be provided with bearing between axis hole and the pushing ram 13 to reduce friction, and the motor shaft of the outer end of pushing ram 13 and motor 14 is in transmission connection.Pushing ram 13 is provided with axially extended screw-blade 17, and the internal diameter of the external diameter of screw-blade 17 and drying cylinder 10 adapts.The inlet of wet pumping unit 12 is connected in each section drying cylinder 10.During dryer section 1 work, organic waste after pulverizing is put into from the opening for feed 15 of drying cylinder 10, during the nichrome wire energising organic waste in the drying cylinder 10 is heated to strengthen the evaporation of moisture, wet pumping unit 12 is extracted the steam that produces out, motor 14 drives pushing ram 13 and rotates, screw-blade 17 and then rotates, organic waste in the drying cylinder 10 can be promoted from head end toward tail end, also stir organic waste when promoting, improve drying efficiency, also can realize the control of degree of drying when dry by adjusting drying temperature or exsiccant time.
Described pressurized segment 2 mainly is made up of the pressure thruster that adds pressure cylinder 21 and be arranged in the input terminus that adds pressure cylinder 21, adding pressure cylinder 21 is made by firm material such as iron and steel, the described input terminus that adds pressure cylinder 21 connects discharge port 16, the sectional area of internal space that adds the output terminal of pressure cylinder 21 little by little dwindles along the direction of propulsion of pressure thruster, when organic rubbish enter add in the pressure cylinder 21 after, pressure thruster pushes away organic waste toward the output terminal that adds pressure cylinder 21, because the sectional area of the internal space of output terminal little by little dwindles, just compacted compacting constantly of organic waste.
Described high temperature carbonization section 3 mainly is made up of charing tube 31, the charing well heater 32, the water cooler 33 that are arranged on the charing tube 31.The input terminus of described charing tube 31 is connected on the output terminal that adds pressure cylinder 21, and charing tube 31 can directly be extended to form by the end that adds pressure cylinder 21, and the sectional area of the internal space of charing tube 31 is long-pending identical with the inner section of the input port that adds pressure cylinder 21.Charing well heater 32 can be nichrome wire, can adopt the mode of winding to be arranged on charing tube 31 peripheries, and water cooler 33 is arranged on the output terminal of charing tube 31.After the compacted compacting of organic waste, pressure thruster pushes organic waste in the internal space of charing tube 31, this moment, organic waste still kept compacted condition, the nichrome wire energising can be heated the organic waste in the charing tube 31, organic waste high temperature and with the isolated condition of air under formed the charcoal coal by charing, the temperature of control charing well heater 32 and the fltting speed of pressure thruster are the temperature and time of may command charing.From the output of the output terminal of charing tube 31, can lower the temperature to the charcoal coal after the charing by water cooler 33 under the effect of pressure thruster for the charcoal coal, prevents spontaneous combustion behind its ingress of air.
Described add be provided with in the pressure cylinder 21 in pillar stiffener 22, add pressure cylinder 21 and interior pillar stiffener 22 formed spatial sectional areas little by little dwindle.Interior pillar stiffener 22 can be formed from steel, and is shaped as taper, and the little rear end of front end is big, and it is fixed on and adds in the pressure cylinder 21.Interior pillar stiffener 22 is with to add pressure cylinder 21 coaxial, and to form a cross section be the annular space to interior pillar stiffener 22 with adding pressure cylinder 21, and this structure is convenient to organic waste is evenly exerted pressure.The end of interior pillar stiffener 22 is cylindric, it extends in the charing tube 31, and the difference of the internal diameter of the external diameter of pillar stiffener 22 and charing tube 31 is chosen lessly for good in this section, and organic waste forms the one deck that approaches by this space like this, be convenient to the conduction of heat, to improve the efficient of charing.Charing well heater 32 can be arranged on charing tube 31 peripheries and the interior pillar stiffener 22, heats simultaneously from the two sides like this, and heating efficiency is higher, and charing rate is fast.
Described pressure thruster is by being arranged on the pressurization pushing ram 23 that adds in the pressure cylinder 21 rotationally, driving the pressurization motor 24 that pressurization pushing ram 23 rotates and form, pressurization pushing ram 23 is provided with axially extended pressurization screw-blade 25, the external diameter of pressurization screw-blade 25 adapts with the internal diameter that adds pressure cylinder 21, add pressure cylinder 21 and be provided with axis hole, pressurization pushing ram 23 passes in the axis hole, and pressurization pushing ram 23 outer ends are connected with the motor shaft of pressurization motor 24.When pressurization motor 24 drives 23 rotations of pressurization pushing ram, pressurization screw-blade 25 rotates in adding pressure cylinder 21, organic waste enters pressurization screw-blade 25 and adds in the space between the pressure cylinder 21 from the import that adds pressure cylinder 21 input terminuss, pressurization screw-blade 25 pushes add organic waste to pressure cylinder 21 output terminals, and the pressure thruster of this kind structure is convenient to work continuously.
As shown in Figure 2, described pressure thruster is made up of pressing machine 27 that also can axially movable piston 26, driven plunger 26 move in adding pressure cylinder 21, and pressing machine 27 can be selected hydropress or pneumatic press for use, and the external diameter of piston 26 adapts with the internal diameter that adds pressure cylinder 21.Pressing machine 27 driven plunger 26 axially move in adding pressure cylinder 21 during work, when piston 26 when adding the output terminal of pressure cylinder 21, organic waste enters into piston 26 front ends and adds in the space between the output terminal of pressure cylinder 21 from the import that adds pressure cylinder 21 input terminuss, pressing machine 27 driven plunger 26 advance organic waste to the output terminal that adds pressure cylinder 21, organic waste stopped to enter and added pressure cylinder 21 this moment, piston 26 is got back to when adding the output end position of pressure cylinder 21, organic waste enters from the import that adds pressure cylinder 21 input terminuss again, and so forth.
As shown in Figure 3, Figure 4, offer on the described screw-blade 17 roughly along pushing ram 13 radial slots 18, be provided with slidably slide block 19 in the groove 18, be fixed with the washer 20 that when slide block 19 is in groove 18 outer ends, can reach outside screw-blade 15 outers on the slide block 19, wherein slide block 19 can be selected screw for use, washer 20 can adopt steel plate, and both can be spirally connected or weld.Because drying cylinder 10 and screw-blade 17 can produce the phenomenon of expanding with heat and contract with cold when temperature variation is big, the internal diameter of screw-blade 17 and drying cylinder 10 can not be good cooperate, as cooperate the tension may be stuck, cooperated Song Youhui to make residual a part of organic waste on the wall of drying cylinder 10.After adopting above-mentioned structure, when pushing ram 13 rotated, washer 20 can slide along groove 18 under the effect of gravity, and when groove 18 is horizontal when above, slide block 19 can fall into the end of groove 18 near pushing ram 13 axle center.As shown in Figure 5, when groove 18 is horizontal when following, it is the outer end away from the end in pushing ram 13 axle center that slide block 19 can fall into groove 18, and this moment, washer 20 can reach outside screw-blade 15 outers, washer 20 just can touch the inner-wall surface of drying cylinder 10, strikes off the organic waste that remains on the inner-wall surface.
The output terminal of described charing tube 31 is circumscribed with vacuum fan 34, and vacuum fan 34 can be taken gas the charcoal coal of exporting from the output terminal of charing tube 31 away and make his usefulness in addition, as the use that acts as a fuel.
Described drying heater 11 is connected to dry temperature controller, and the heating intensity that dry temperature controller is used for detecting the temperature of drying cylinder 10 and controls drying heater 11 is to realize drying temperature control.
Described charing well heater 32 is connected to the charing temperature controller, and the heating intensity that dry temperature controller is used for detecting the temperature of charing tube 31 and controls charing well heater 32 is to realize drying temperature control.
The outside of described drying cylinder 10 or charing tube 31 is provided with thermal insulation layer, and thermal insulation layer can adopt asbestos or other thermostable heat insulation materials, and thermal insulation layer can be incubated drying cylinder 10 or charing tube 31, prevents that heat scatters and disappears, and improves the energy service efficiency.
Described water cooler 33 is the water pipe that is arranged on the output terminal of charing tube 31, water pipe is made by thermal conduction good metal material, circulation cycle water in the water pipe, water pipe can or be located in the output terminal of charing tube 31 around the outside wall surface of charing tube 31 output terminals, the charcoal coal that water pipe forms after to charing is lowered the temperature, prevent spontaneous combustion behind its ingress of air, also can be used as his usefulness after the water in the water pipe is heated, to save the energy.
Motor described in the present invention also can be selected for use as other power set such as oil engines.
Claims (10)
1. the treatment unit that organic solid rubbish is recycled is characterized in that comprising the dryer section (1), pressurized segment (2) and the high temperature carbonization section (3) that are linked in sequence, wherein:
Described dryer section (1) mainly by drying cylinder (10), be arranged on drying heater (11) on the drying cylinder (10), wet pumping unit (12), rotationally be arranged on pushing ram (13) in the drying cylinder (10), drive the motor (14) that pushing ram (13) rotates and form, the head end of drying cylinder (10) is provided with opening for feed (15), tail end is provided with discharge port (16), pushing ram (13) is provided with axially extended screw-blade (17), the internal diameter of the external diameter of screw-blade (17) and drying cylinder (10) adapts, and the inlet of wet pumping unit (12) is connected in the drying cylinder (10);
Described pressurized segment (2) mainly is made up of the pressure thruster that adds pressure cylinder (21) and be arranged in the input terminus that adds pressure cylinder (21), the described input terminus that adds pressure cylinder (21) connects discharge port (16), and the sectional area of internal space that adds the output terminal of pressure cylinder (21) little by little dwindles along the direction of propulsion of pressure thruster;
Described high temperature carbonization section (3) mainly is made up of charing tube (31), the charing well heater (32), the water cooler (33) that are arranged on the charing tube (31), the input terminus of described charing tube (31) is connected on the output terminal that adds pressure cylinder (21), the sectional area of the internal space of charing tube (31) is long-pending identical with the inner section of the input port that adds pressure cylinder (21), and water cooler (33) is arranged on the output terminal of charing tube (31).
2. the treatment unit of recycling according to the described organic solid rubbish of claim 1, it is characterized in that: described adding, be provided with interior pillar stiffener (22) in the pressure cylinder (21), add pressure cylinder (21) and the formed spatial sectional area of interior pillar stiffener (22) little by little dwindles, the end of interior pillar stiffener (22) extends in the charing tube (31).
3. the treatment unit of recycling according to the described organic solid rubbish of claim 1, it is characterized in that: described pressure thruster is by being arranged on the pressurization pushing ram (23) that adds in the pressure cylinder (21) rotationally, driving the pressurization motor (24) that pressurization pushing ram (23) rotates and form, pressurization pushing ram (23) is provided with axially extended pressurization screw-blade (25), and the external diameter of pressurization screw-blade (25) adapts with the internal diameter that adds pressure cylinder (21).
4. according to the treatment unit of the described organic solid rubbish recycling of claim 1, it is characterized in that: described pressure thruster is by can axially movable piston (26), the mobile pressing machine (27) of driven plunger (26) forming in adding pressure cylinder (21).
5. the treatment unit of recycling according to each described organic solid rubbish in the claim 1 to 4, it is characterized in that: offer on the described screw-blade (17) roughly along pushing ram (13) radial slot (18), be provided with slidably slide block (19) in the groove (18), be fixed with the washer (20) that when slide block (19) is in groove (18) outer end, can reach outside screw-blade (15) outer on the slide block (19).
6. according to the treatment unit of each described organic solid rubbish recycling in the claim 1 to 4, it is characterized in that: the output terminal of described charing tube (31) is circumscribed with vacuum fan (34).
7. according to the treatment unit of each described organic solid rubbish recycling in the claim 1 to 4, it is characterized in that: described drying heater (11) is connected to dry temperature controller.
8. according to the treatment unit of each described organic solid rubbish recycling in the claim 1 to 4, it is characterized in that: described charing well heater (32) is connected to the charing temperature controller.
9. according to the treatment unit of each described organic solid rubbish recycling in the claim 1 to 4, it is characterized in that: the outside of described drying cylinder (10) or charing tube (31) is provided with thermal insulation layer.
10. according to the treatment unit of each described organic solid rubbish recycling in the claim 1 to 4, it is characterized in that: described water cooler (33) is the water pipe that is arranged on the output terminal of charing tube (31).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200810199183A CN101381646B (en) | 2008-10-16 | 2008-10-16 | Handling arrangement for recovering and utilizing organic solid rubbish |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200810199183A CN101381646B (en) | 2008-10-16 | 2008-10-16 | Handling arrangement for recovering and utilizing organic solid rubbish |
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| Publication Number | Publication Date |
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| CN101381646A true CN101381646A (en) | 2009-03-11 |
| CN101381646B CN101381646B (en) | 2012-09-12 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN200810199183A Expired - Fee Related CN101381646B (en) | 2008-10-16 | 2008-10-16 | Handling arrangement for recovering and utilizing organic solid rubbish |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102173084A (en) * | 2011-03-18 | 2011-09-07 | 四川洪春福环保设备有限公司 | Fuel forming machine |
| CN102660306A (en) * | 2012-05-09 | 2012-09-12 | 李海明 | Reflux rotating household garbage pyrolysis carbonization furnace system and garbage disposal process |
| CN103484137A (en) * | 2012-06-12 | 2014-01-01 | 丁泽明 | Carbonizing apparatus and carbonizing method for waste solid organic matters |
| CN106623369A (en) * | 2017-01-11 | 2017-05-10 | 深圳市科鸿环保新能源科技有限公司 | Household garbage harmless treatment and energy source conversion electricity generation equipment |
| CN107597805A (en) * | 2017-09-29 | 2018-01-19 | 江苏绿尚环保科技有限公司 | A kind of solid refuse recycling and processing device |
| CN109277395A (en) * | 2018-09-27 | 2019-01-29 | 金庆波 | A kind of environmental protection recyclable device and its working method |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000104082A (en) * | 1998-09-30 | 2000-04-11 | Kawasaki Steel Corp | Method and apparatus for producing refuse derived solid fuel |
| CN2376349Y (en) * | 1999-05-27 | 2000-05-03 | 金春植 | Equipment for treating refuse |
| CN1277628C (en) * | 2001-12-18 | 2006-10-04 | 张庆陆 | Method for recovering hydrazine hydrate continuous distillation salt mud |
| KR100736267B1 (en) * | 2006-03-31 | 2007-07-06 | 김현수 | The system for sterilizing and recycling of organic waste by using the saturated and overheated vapor |
| CN101157090B (en) * | 2006-08-19 | 2012-10-24 | 倪国森 | Refuse classification recovering and recovery resourceful process system |
| CN201301309Y (en) * | 2008-10-16 | 2009-09-02 | 练其辉 | Treatment device for recycling organic solid waste |
-
2008
- 2008-10-16 CN CN200810199183A patent/CN101381646B/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102173084A (en) * | 2011-03-18 | 2011-09-07 | 四川洪春福环保设备有限公司 | Fuel forming machine |
| CN102660306A (en) * | 2012-05-09 | 2012-09-12 | 李海明 | Reflux rotating household garbage pyrolysis carbonization furnace system and garbage disposal process |
| CN102660306B (en) * | 2012-05-09 | 2013-12-04 | 李海明 | Reflux rotating household garbage pyrolysis carbonization furnace system and garbage disposal process |
| CN103484137A (en) * | 2012-06-12 | 2014-01-01 | 丁泽明 | Carbonizing apparatus and carbonizing method for waste solid organic matters |
| CN103484137B (en) * | 2012-06-12 | 2014-11-19 | 丁泽明 | Carbonizing apparatus and carbonizing method for waste solid organic matters |
| CN106623369A (en) * | 2017-01-11 | 2017-05-10 | 深圳市科鸿环保新能源科技有限公司 | Household garbage harmless treatment and energy source conversion electricity generation equipment |
| CN107597805A (en) * | 2017-09-29 | 2018-01-19 | 江苏绿尚环保科技有限公司 | A kind of solid refuse recycling and processing device |
| CN109277395A (en) * | 2018-09-27 | 2019-01-29 | 金庆波 | A kind of environmental protection recyclable device and its working method |
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|---|---|
| CN101381646B (en) | 2012-09-12 |
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Address after: 516211, No. 2, Kaesong Avenue, freshwater Town, Huiyang District, Guangdong, Huizhou Patentee after: Qi Hui Lian Address before: 511515 room 9, 301 South Hospital, No. 18, Xincheng District, Guangdong, Qingyuan Patentee before: Qi Hui Lian |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120912 Termination date: 20211016 |
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| CF01 | Termination of patent right due to non-payment of annual fee |