CN205424934U - Device of solid wastes material of many function processing - Google Patents
Device of solid wastes material of many function processing Download PDFInfo
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- CN205424934U CN205424934U CN201620108520.9U CN201620108520U CN205424934U CN 205424934 U CN205424934 U CN 205424934U CN 201620108520 U CN201620108520 U CN 201620108520U CN 205424934 U CN205424934 U CN 205424934U
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Abstract
The utility model discloses a device of solid wastes material of many function processing, including the pyrolysis gasifier, it includes furnace body, flue gas stoving case, and the furnace body top is equipped with the combustible gas expansion box, and the combustible gas expansion box is the intercommunication bottom the furnace body, furnace body upper portion is equipped with the combustible gas contact tube, and the combustible gas contact tube is connected with condensing equipment, and condensing equipment is connected with the combustible gas expansion box, the furnace body lower part is equipped with the inside contact tube of flue gas, and flue gas stoving case is connected with exhaust -heat boiler, exhaust -heat boiler is connected with flue gas water washing system, and exhaust -heat boiler is connected with sludge drying equipment, flue gas water washing system is connected with the effluent water sump, and flue gas water washing system is connected with the chimney, and condensing equipment is connected with the effluent water sump, the effluent water sump is connected with can be with the water oil separating system of tar and separation of water. The utility model discloses a solid wastes material, burning can thoroughly be handled completely to the device, make smoke and dust discharge to reach standard to has the sludge treatment ability simultaneously.
Description
Technical field
This utility model belongs to field of environment protection equipment, is specifically related to the device of a kind of multi-functional process solid waste.
Background technology
Along with adding of Chinese society doctrine new countryside construction paces is busy, beautiful rural construction is just adding fast speed and is catching up with forward, during building beautiful rural, based on residents in rural community and the process of the solid waste of domestic sludge, is the most increasingly subject to people's attention.At present, the method for process is still based on burying method.Because lacking wholesale fund input and landfill yard is built lack of standardization, cause a large amount of external wave of garbage leachate in landfill yard and pollute underground (table) water source, severely impacted the healthy of periphery villager.Under state revenue and expenditure is supported; although having built incinerator and the gasification furnace of a part of small-scale; but incinerator and gasification furnace technology do not pass a test, process not thoroughly, incomplete combustion, flue dust not qualified discharge etc.; cause again air and surrounding enviroment are polluted, receive the serious obstruction of local villager.
And, at present in order to process incinerator and the gasification furnace function singleness of rubbish, not there is the function simultaneously processing mud, say, that process solid refuse and to process mud be two incoherent techniques, be the different equipment of two sets yet.Owing to the two incoherent equipment of set each work, it is impossible to collaborative so that some emissions each produced can not mutually utilize, and causes energy waste.
Technical term is explained as follows:
Oxide layer and reducing zone: the artificial invisible layer divided according to reaction principle, is the known technology of prior art.
Utility model content
For the problems referred to above, this utility model aims to provide one can thoroughly process solid waste, burning completely, makes flue dust qualified discharge, and has the device of the multi-functional process solid waste of Treatment of Sludge ability simultaneously.
This utility model solves the technical scheme of problem: the device of a kind of multi-functional process solid waste, including pyrolysis gasification furnace, this pyrolysis gasification furnace includes that body of heater, two ends are fixed on the flue gas drying case of upper of furnace body inwall, described body of heater top is provided with combustible gas expansion box, and this combustible gas expansion box is connected with bottom of furnace body by the combustion-supporting conduit of combustible gas；
Upper of furnace body is provided with combustible gas delivery line, and this combustible gas delivery line connects condensing unit, and condensing unit outfan is connected with combustible gas expansion box by pipeline；
Described lower portion of furnace body is provided with the internal delivery line of the flue gas connected with flue gas drying case input, the outfan of described flue gas drying case connects, by the first flue gas delivery line, the boiler that has surplus heat, described waste heat boiler is connected by the second flue gas delivery line gas fume washing system, and waste heat boiler is connected by steam delivery line sludge drying device；
Described gas fume washing system is connected by pipeline cesspool, and gas fume washing system connects chimney, and condensing unit is connected with cesspool by condenser sewage delivery line；
The outfan of described cesspool is connected by sewage delivery line the oil-water separation system that can be separated by tar with water.
Concrete, described sludge drying device includes the condensed water water tank that the dewatered sludge storage tank that sewage sludge feed mechanism, drying baker are connected by dewatered sludge delivery line is connected by steam condensate (SC) pipe with drying baker with drying baker.
Further, being provided with sealing radiator around furnace body outer wall, this sealing radiator connects water inlet pipe and outlet pipe, and connecting between water inlet pipe and outlet pipe has plate type heat exchanger, plate type heat exchanger outfan is connected with waste heat boiler by moisturizing water pipe, and condensed water water tank is connected with moisturizing water pipe.
In this further improved plan, the setting of sealing radiator, and it is contacted with waste heat boiler generation, the heat that pyrolysis gasification furnace is distributed can be salvaged, be equivalent to the water to entering in waste heat boiler preheat so that the water in waste heat boiler can gasify faster, has saved the energy.
Concrete, described condensing unit includes first-stage condenser, secondary condenser, is provided with air-introduced machine between secondary condenser and combustible gas expansion box.
Concrete, described gas fume washing system includes one-level gas fume washing tower, secondary smoke water scrubber, is connected by flue gas connecting tube between two-stage gas fume washing tower；
Described secondary smoke water scrubber outfan is connected with chimney, is provided with air-introduced machine between secondary smoke water scrubber and chimney.
Described oil-water separation system includes oil water separator, the scrapper conveyor being positioned at oil water separator top, micro-nano bubble generator, is positioned at the micro-nano bubble of oil water separator and dives and penetrate tar holding vessel and the clean water tank that head is connected with oil water separator outfan.Use micro-nano bubble generator and bubble to dive and penetrate head, oil-water separation and speed can be improved, quickly, effectively, up hill and dale by oil, water separate.
Described clean water tank is connected with one-level gas fume washing tower and secondary smoke water scrubber respectively by pipeline, and pipeline is provided with water pump.So, the clean aquiform stool obtained can recycle.
Further, described lower portion of furnace body is provided with fresh air inlet, is disposed with aerator at fresh air inlet, and described bottom of furnace body is provided with the horizontal conveying worm for slagging tap and longitudinal spiral conveyer.
Further, the outfan of described longitudinal spiral conveyer connects brick making system, and this brick making system includes the brickmaking machine that the pulverizer that the magnetic separator that the screening machine that clinker elevator is connected is connected with screening machine is connected with magnetic separator is connected with pulverizer with clinker elevator；Described magnetic separator is also associated with metal collection case, and screening machine is the most also connected with brickmaking machine.
Above-mentioned brick making system, oil-water separation system are the equipment having in prior art.
Operation principle of the present utility model is:
A rubbish is poured in pyrolysis gasification furnace by (), heat that rubbish is transmitted by furnace wall and flue gas drying case on pyrolysis gasification furnace top and by transpiring moisture and dry；
B rubbish that () dried enters in the middle part of pyrolysis gasification furnace under gravity, and in stove, middle portion temperature controls at 400 DEG C-600 DEG C, and the Organic substance in rubbish is pyrolyzed in this temperature range and generates main by CO, CH4、H2, Hydrocarbon constitute fuel gas, this part fuel gas together with steam from combustible gas delivery line discharge, enter into condensing unit, combustible gas and water vapor mixture body in condensing unit through condensation and wash rice goes out water vapour；
It is stripped of the fuel gas of water vapour and is directed to combustible gas expansion box, then by combustible gas combustion-supporting conduit, combustible gas imported to pyrolysis gasification furnace internal oxidation layer and carry out burning and combustion-supporting；
(c) through pyrolysis after Organic substance carbon residue and mixture of inorganic substance under gravity, enter into reducing zone and the oxide layer of middle and lower part in pyrolysis gasification furnace, carry out the chemical reaction of state of absorbing heat at reducing zone, carried out smouldering in oxide layer and release amount of heat；
D the high-temperature flue gas generated after () burning, enters into flue gas drying case through flue gas inner conduit, enters into waste heat boiler by the first flue gas delivery line the most again；
E (), to being passed through water in waste heat boiler, enters into the high-temperature flue gas of waste heat boiler and water heat exchange from flue gas drying case and be cooled, the flue gas after cooling imports to gas fume washing system by the second flue gas delivery line, and the flue gas after washing is from smoke stack emission；
F mud is delivered in sludge drying device by (), the high temperature saturated vapor provided by waste heat boiler and mud noncontact heat exchange, mud absorbs saturated vapor liberated heat and heated and dry, then carries out pyrolytic gasification in dewatered sludge is transported to pyrolysis gasification furnace；
G water and tar mixed liquor condensed device sewage delivery line that condensing unit is discharged by () are extracted in cesspool, the sewage in cesspool is extracted into oil-water separation system, carries out the separation of tar and water；And carry out pyrolytic gasification process in tar is transported to pyrolysis gasification furnace.
Remarkable result of the present utility model is:
Having garbage disposal and two kinds of functions of Treatment of Sludge the most simultaneously, overlap incoherent equipment by conventional art two and connect, one-machine-multi-function, energy waste is low.
2. in processing house refuse or sludge process, it is not necessary to house refuse is classified, sort, screen, the early stage process such as crush, the most effectively.Solve the key technical problem such as rural solid waste thing incinerator and gasification furnace processes not thoroughly, incomplete combustion, flue dust not qualified discharge.
3. the flue gas that waste heat boiler is discharged, by can direct qualified discharge after two-stage washing cooling.
4. the lime-ash stayed after organic matter pyrolysis gasification can carry out brickmaking, it is achieved that twice laid, functional diversities.
In sum, this device can the most thoroughly, effectively, environmental protection dispose house refuse and mud, the discharge of flue gas energy stably reaching standard, and without sewage discharge and secondary pollution, is county, villages (towns), village's house refuse and the ideal equipment of sludge treatment.
Accompanying drawing explanation
The utility model is described in further detail below in conjunction with the accompanying drawings.
Fig. 1 is structural representation of the present utility model.
In figure: 1-pyrolysis gasification furnace；2-bell；3-body of heater；4-sealing radiator；5-outlet pipe；6-water inlet pipe；The internal delivery line of 7-flue gas；8-flue gas drying case；9-the first flue gas delivery line；10-flame observation port；11-fresh air inlet；The horizontal conveying worm of 12-；13-longitudinal spiral conveyer；14-aerator；15-combustible gas delivery line；16-first-stage condenser；The cold doubtful device of 17-bis-grades；18-air-introduced machine；19-combustible gas expansion box；The combustion-supporting conduit of 20-combustible gas；21-clinker elevator；22-screening machine；23-magnetic separator；24-pulverizer；25-brickmaking machine；26-metal collection case；27-water pump；28-plate type heat exchanger；29-waste heat boiler；30-steam delivery line；31-drying baker；32-sewage sludge feed mechanism；34-steam condensate (SC) pipe；35-condensed water water tank；36-water pump；37-moisturizing water pipe；38-dewatered sludge delivery line；39-dewatered sludge storage tank；40-the second flue gas delivery line；41-one-level gas fume washing tower；42-flue gas connecting tube；43-secondary smoke water scrubber；44-air-introduced machine；45-chimney；46-pipeline；47-condenser sewage delivery line；48-cesspool；49-pipeline；50-sewage delivery line；51-sewage pump；52-rubbing board machine；53-oil water separator；The micro-nano bubble generator of 54-；The micro-nano bubble of 55-is latent penetrates head；56-tar holding vessel；57-clean water delivery line；58-clean water tank；59-water pump；60-bubble.
Detailed description of the invention
As shown in Figure 1, a kind of device of multi-functional process solid waste, including pyrolysis gasification furnace 1, this pyrolysis gasification furnace 1 includes that body of heater 3, two ends are fixed on the flue gas drying case 8 of body of heater 3 upper inside wall, described body of heater 3 top is provided with combustible gas expansion box 19, and this combustible gas expansion box 19 is connected bottom body of heater 3 by the combustion-supporting conduit of combustible gas 20.
Body of heater 3 top is provided with combustible gas delivery line 15, and this combustible gas delivery line 15 connects condensing unit, and condensing unit outfan is connected with combustible gas expansion box 19 by pipeline.Described condensing unit includes first-stage condenser 16, secondary condenser 17, is provided with air-introduced machine 18 between secondary condenser 17 and combustible gas expansion box 19.
Described body of heater 3 bottom is provided with the internal delivery line 7 of the flue gas connected with flue gas drying case 8 input, and the outfan of described flue gas drying case 8 connects, by the first flue gas delivery line 9, the boiler 29 that has surplus heat.Described waste heat boiler 29 is connected by the second flue gas delivery line 40 gas fume washing system.
Waste heat boiler 29 is connected by steam delivery line 30 sludge drying device.Described sludge drying device includes the condensed water water tank 35 that the dewatered sludge storage tank 39 that sewage sludge feed mechanism 32, drying baker 31 are connected by dewatered sludge delivery line 38 is connected by steam condensate (SC) pipe 34 with drying baker 31 with drying baker 31.
Described gas fume washing system is connected by pipeline 49 cesspool 48, and gas fume washing system connects chimney 45.Condensing unit is connected with cesspool 48 by condenser sewage delivery line 47.
Described gas fume washing system includes one-level gas fume washing tower 41, secondary smoke water scrubber 43, is connected by flue gas connecting tube 42 between two-stage gas fume washing tower.Described secondary smoke water scrubber 43 outfan is connected with chimney 45, is provided with air-introduced machine 44 between secondary smoke water scrubber 43 and chimney 45.
The outfan of described cesspool 48 is connected by sewage delivery line 50 oil-water separation system that can be separated by tar with water.Described oil-water separation system includes oil water separator 53, is positioned at the scrapper conveyor 52 on oil water separator 53 top, micro-nano bubble generator 54, is positioned at the micro-nano bubble of oil water separator and dives and penetrate the 55 tar holding vessel 56 being connected with oil water separator 53 outfan and a clean water tank 58.Described clean water tank 58 is connected with one-level gas fume washing tower 41 and secondary smoke water scrubber 43 respectively by pipeline 46, and pipeline 46 is provided with water pump 59.
Being provided with sealing radiator 4 around body of heater 3 outer wall, this sealing radiator 4 connects water inlet pipe 6 and outlet pipe 5, and connecting between water inlet pipe 6 and outlet pipe 5 has plate type heat exchanger 28.Plate type heat exchanger 28 outfan is connected with waste heat boiler 29 by moisturizing water pipe 37, and condensed water water tank 35 is connected with moisturizing water pipe 37.
Described body of heater 3 bottom is provided with fresh air inlet 11, is disposed with aerator 14 at fresh air inlet 11.Air inlet 11 is arranged over bottom body of heater 3 described in flame observation port 10 being provided with the horizontal conveying worm 12 for slagging tap and longitudinal spiral conveyer 13.
The outfan of described longitudinal spiral conveyer 13 connects brick making system, and this brick making system includes the brickmaking machine 25 that the pulverizer 24 that the magnetic separator 23 that the screening machine 22 that clinker elevator 21 is connected is connected with screening machine 22 is connected with magnetic separator 23 is connected with pulverizer 24 with clinker elevator 21；Described magnetic separator 23 is also associated with metal collection case 26, and screening machine 22 is the most also connected with brickmaking machine 25.
The operation principle of the present embodiment is:
A () opens bell 2, poured into by rubbish in pyrolysis gasification furnace 1, covers bell 2.Heat that rubbish is transmitted by furnace wall and flue gas drying case 8 on pyrolysis gasification furnace 1 top and by transpiring moisture and dry；
B rubbish that () dried enters in the middle part of pyrolysis gasification furnace 1 under gravity, and in stove, middle portion temperature controls at 400 DEG C-600 DEG C, and the Organic substance in rubbish is pyrolyzed in this temperature range and generates main by CO, CH4、H2, Hydrocarbon constitute fuel gas, this part fuel gas is discharged from combustible gas delivery line 15 together with steam under air-introduced machine 18 acts on, enter into first-stage condenser 16, through condensation, wash rice goes out most of water vapor in first-stage condenser 16 for combustible gas and water vapor mixture body, then enter back in secondary condenser 17 and again condense, and wash rice goes out remaining water vapour；
It is stripped of the fuel gas of water vapour and is directed to combustible gas expansion box 19, then by the combustion-supporting conduit of combustible gas 20, combustible gas imported to pyrolysis gasification furnace 1 internal oxidation layer and carry out burning and combustion-supporting；
(c) through pyrolysis after Organic substance carbon residue and mixture of inorganic substance under gravity, enter into reducing zone and the oxide layer of middle and lower part in pyrolysis gasification furnace 1, carry out the chemical reaction of state of absorbing heat at reducing zone, carried out smouldering in oxide layer and release amount of heat；
The oxygen that smouldering needs is provided by aerator 14, and is uniformly distributed entrance by fresh air inlet 11.Mixture all becomes lime-ash after layer is smouldered.Utilizing horizontal conveying worm 12 to be discharged to by lime-ash in longitudinal spiral conveyer 13, lime-ash is discharged by recycling longitudinal spiral conveyer 13；
From longitudinal spiral conveyer Ash water out to clinker elevator 21, utilize clinker elevator 21 by Ash water to screening machine 22, the minus sieve powder that screening machine 22 sieves is transported to brickmaking machine 25 and carries out brickmaking.Screening machine oversize is transported to magnetic separator 23, sub-elects metallics and send into metal collection case 26.The grey solid impurity particle of magnetic separation is transported to pulverizer 24 pulverize, the Ash water pulverized is carried out brickmaking to brickmaking machine 25；
D the high-temperature flue gas generated after () burning, enters into flue gas drying case 8 through flue gas inner conduit 7, enters into waste heat boiler 29 by the first flue gas delivery line 9 the most again；
E water at low temperature is pumped into sealing radiator from water inlet pipe 6 by water pump 27 by (), discharge from outlet pipe 5 after utilizing the temperature in pyrolysis gasification furnace 1 heated, and the hot water of outlet pipe 5 flows into plate type heat exchanger 28 and carries out heat exchange with the cold water entering heat exchanger.After cold water is heated by plate type heat exchanger 28, it is pumped in waste heat boiler 29 under water pump 36 acts on.Enter into the high-temperature flue gas of waste heat boiler 29 and water heat exchange from flue gas drying case 8 and be cooled, flue gas after cooling imports to one-level gas fume washing tower 41 by the second flue gas delivery line 40, secondary smoke water scrubber 43 is imported to again by flue gas connecting tube 42, flue gas after two-stage is washed, under air-introduced machine 44 acts on, discharges from chimney 45；
F () will be sent into drying baker 31 from sewage sludge feed mechanism 32, the high temperature saturated vapor provided by waste heat boiler 29 and mud noncontact heat exchange, mud absorbs saturated vapor liberated heat and is heated and dries, and the mud dried is directed to dewatered sludge storage tank 39 by dewatered sludge delivery line 38.Pyrolytic gasification is carried out in the dewatered sludge in dewatered sludge storage tank 39 is transported to pyrolysis gasification furnace 1 again；
High temperature saturated vapor in drying baker 31 is condensed and passes through steam condensate (SC) pipe 34 and imports in condensed water water tank 35, and the water in condensed water water tank 35 also can be pumped into waste heat boiler 29 by water pump 36 and carry out re-evaporation；
G water and tar mixed liquor condensed device sewage delivery line 47 that first-stage condenser 16 and secondary condenser 17 are discharged by () are extracted in cesspool 48, and through sewage delivery line 50 and sewage pump 51, the sewage in cesspool 48 is extracted into oil-water separation system；
Micro-nano bubble generator 54 in this system produces a large amount of diameter and is fed in oil water separator 53 at 50 μm bubbles below 60, bubble.Bubble 60 is penetrated 55 and is uniformly spread in oil mixing with water liquid and attach tar by micro-nano bubble is latent and upwards float, and tar quickly takes to liquid level, and under rubbing board machine 52 acts on, the tar that will float over liquid level is discharged, and is transported in tar storage tank 56；
Then carry out pyrolytic gasification process in the tar in tar storage tank 56 is transported to pyrolysis gasification furnace 1, the clean water separating tar is derived water pipe 57 by clean water and imports in clean water tank 58.Clean water in clean water tank 58 is extracted into repetitive cycling in one-level gas fume washing tower 41 and secondary smoke water scrubber 43 by water pump 59 and uses.
Claims (9)
1. the device of a multi-functional process solid waste, it is characterized in that: include pyrolysis gasification furnace (1), this pyrolysis gasification furnace (1) includes that body of heater (3), two ends are fixed on the flue gas drying case (8) of body of heater (3) upper inside wall, described body of heater (3) top is provided with combustible gas expansion box (19), and this combustible gas expansion box (19) is connected with body of heater (3) bottom by the combustion-supporting conduit of combustible gas (20)；
Body of heater (3) top is provided with combustible gas delivery line (15), and this combustible gas delivery line (15) connects condensing unit, and condensing unit outfan is connected with combustible gas expansion box (19) by pipeline；
Described body of heater (3) bottom is provided with the internal delivery line (7) of the flue gas connected with flue gas drying case (8) input, the outfan of described flue gas drying case (8) connects, by the first flue gas delivery line (9), the boiler (29) that has surplus heat, described waste heat boiler (29) is connected by the second flue gas delivery line (40) gas fume washing system, and waste heat boiler (29) is connected by steam delivery line (30) sludge drying device；
Described gas fume washing system is connected by pipeline (49) cesspool (48), and gas fume washing system connects chimney (45), and condensing unit is connected with cesspool (48) by condenser sewage delivery line (47)；
The outfan of described cesspool (48) is connected by sewage delivery line (50) the oil-water separation system that can be separated by tar with water.
The device of multi-functional process solid waste the most according to claim 1, it is characterised in that: described sludge drying device includes the condensed water water tank (35) that the dewatered sludge storage tank (39) that sewage sludge feed mechanism (32), drying baker (31) are connected by dewatered sludge delivery line (38) is connected by steam condensate (SC) pipe (34) with drying baker (31) with drying baker (31).
The device of multi-functional process solid waste the most according to claim 2, it is characterized in that: be provided with sealing radiator (4) around body of heater (3) outer wall, the upper connection of this sealing radiator (4) has water inlet pipe (6) and outlet pipe (5), connect between water inlet pipe (6) and outlet pipe (5) and have plate type heat exchanger (28), plate type heat exchanger (28) outfan is connected with waste heat boiler (29) by moisturizing water pipe (37), and condensed water water tank (35) is connected with moisturizing water pipe (37).
The device of multi-functional process solid waste the most according to claim 1, it is characterized in that: described condensing unit includes first-stage condenser (16), secondary condenser (17), is provided with air-introduced machine (18) between secondary condenser (17) and combustible gas expansion box (19).
The device of multi-functional process solid waste the most according to claim 1, it is characterized in that: described gas fume washing system includes one-level gas fume washing tower (41), secondary smoke water scrubber (43), connected by flue gas connecting tube (42) between two-stage gas fume washing tower；
Described secondary smoke water scrubber (43) outfan is connected with chimney (45), is provided with air-introduced machine (44) between secondary smoke water scrubber (43) and chimney (45).
The device of multi-functional process solid waste the most according to claim 1, it is characterised in that: described oil-water separation system includes oil water separator (53), is positioned at the scrapper conveyor (52) on oil water separator (53) top, micro-nano bubble generator (54), is positioned at that the micro-nano bubble of oil water separator (53) is latent penetrates tar holding vessel (56) and the clean water tank (58) that head (55) is connected with oil water separator (53) outfan.
The device of multi-functional process solid waste the most according to claim 6, it is characterized in that: described clean water tank (58) is connected with one-level gas fume washing tower (41) and secondary smoke water scrubber (43) respectively by pipeline (46), and pipeline (46) is provided with water pump (59).
The device of multi-functional process solid waste the most according to claim 1, it is characterized in that: described body of heater (3) bottom is provided with fresh air inlet (11), fresh air inlet (11) place is disposed with aerator (14), and described body of heater (3) bottom is provided with the horizontal conveying worm (12) for slagging tap and longitudinal spiral conveyer (13).
The device of multi-functional process solid waste the most according to claim 8, it is characterized in that: the outfan of described longitudinal spiral conveyer (13) connects brick making system, and this brick making system includes the brickmaking machine (25) that the pulverizer (24) that the magnetic separator (23) that the screening machine (22) that clinker elevator (21) is connected is connected with screening machine (22) is connected with magnetic separator (23) is connected with pulverizer (24) with clinker elevator (21)；Described magnetic separator (23) is also associated with metal collection case (26), and screening machine (22) is the most also connected with brickmaking machine (25).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620108520.9U CN205424934U (en) | 2016-02-03 | 2016-02-03 | Device of solid wastes material of many function processing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620108520.9U CN205424934U (en) | 2016-02-03 | 2016-02-03 | Device of solid wastes material of many function processing |
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| Publication Number | Publication Date |
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| CN205424934U true CN205424934U (en) | 2016-08-03 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201620108520.9U Withdrawn - After Issue CN205424934U (en) | 2016-02-03 | 2016-02-03 | Device of solid wastes material of many function processing |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105546548A (en) * | 2016-02-03 | 2016-05-04 | 湖南鹞翔环保能源科技有限公司 | Multifunctional solid waste treatment device and solid waste treatment method thereof |
-
2016
- 2016-02-03 CN CN201620108520.9U patent/CN205424934U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105546548A (en) * | 2016-02-03 | 2016-05-04 | 湖南鹞翔环保能源科技有限公司 | Multifunctional solid waste treatment device and solid waste treatment method thereof |
| CN105546548B (en) * | 2016-02-03 | 2017-08-04 | 湖南鹞翔环保能源科技有限公司 | A kind of device and its solid waste substance treating method of multi-functional processing solid waste |
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Granted publication date: 20160803 Effective date of abandoning: 20170804 |