CN105537233A - Harmless treatment and recycling system for oily garbage - Google Patents
Harmless treatment and recycling system for oily garbage Download PDFInfo
- Publication number
- CN105537233A CN105537233A CN201510926689.5A CN201510926689A CN105537233A CN 105537233 A CN105537233 A CN 105537233A CN 201510926689 A CN201510926689 A CN 201510926689A CN 105537233 A CN105537233 A CN 105537233A
- Authority
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- China
- Prior art keywords
- oil
- gas
- reactor
- combustion chamber
- reaction kettle
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 28
- 238000004064 recycling Methods 0.000 title claims description 14
- 239000007789 gas Substances 0.000 claims abstract description 67
- 239000003546 flue gas Substances 0.000 claims abstract description 25
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 24
- 238000006243 chemical reaction Methods 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000002485 combustion reaction Methods 0.000 claims abstract description 17
- 239000003054 catalyst Substances 0.000 claims abstract description 14
- 238000004140 cleaning Methods 0.000 claims abstract description 13
- 230000005540 biological transmission Effects 0.000 claims abstract description 11
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 8
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 8
- 239000001257 hydrogen Substances 0.000 claims abstract description 8
- 238000012545 processing Methods 0.000 claims description 21
- 239000007921 spray Substances 0.000 claims description 13
- 238000001179 sorption measurement Methods 0.000 claims description 12
- 230000003197 catalytic effect Effects 0.000 claims description 10
- 238000009413 insulation Methods 0.000 claims description 9
- 239000000779 smoke Substances 0.000 claims description 9
- 239000002351 wastewater Substances 0.000 claims description 8
- 238000005253 cladding Methods 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 238000003860 storage Methods 0.000 claims description 6
- 230000003014 reinforcing effect Effects 0.000 claims description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 3
- 238000005859 coupling reaction Methods 0.000 claims description 2
- 239000007788 liquid Substances 0.000 abstract description 8
- 238000007599 discharging Methods 0.000 abstract description 4
- 238000011084 recovery Methods 0.000 abstract description 3
- 239000006229 carbon black Substances 0.000 abstract description 2
- 239000002518 antifoaming agent Substances 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 9
- 238000009833 condensation Methods 0.000 description 7
- 230000005494 condensation Effects 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 244000144977 poultry Species 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 244000144972 livestock Species 0.000 description 5
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- 239000013530 defoamer Substances 0.000 description 4
- 239000002283 diesel fuel Substances 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 4
- 238000006477 desulfuration reaction Methods 0.000 description 3
- 230000023556 desulfurization Effects 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000003500 flue dust Substances 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 239000004115 Sodium Silicate Substances 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- 201000010099 disease Diseases 0.000 description 2
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 238000005461 lubrication Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- 235000017550 sodium carbonate Nutrition 0.000 description 2
- 235000019795 sodium metasilicate Nutrition 0.000 description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 2
- 229910052911 sodium silicate Inorganic materials 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- 241000282898 Sus scrofa Species 0.000 description 1
- 241000519996 Teucrium chamaedrys Species 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000009970 fire resistant effect Effects 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000000693 micelle Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Treating Waste Gases (AREA)
- Processing Of Solid Wastes (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
The invention relates to a harmless treatment system for oily garbage. The system is characterized in that a reaction device comprises a horizontal reaction kettle, and the reaction kettle is provided with a spiral rotating plate and an inner wall cleaning device; a feed opening is formed in one end of the reaction kettle, an oil gas outlet is formed in the other end of the reaction kettle, and a transmission device is arranged at the oil gas outlet end; the oil gas outlet is connected with a gas recovery device; a flue gas outlet in the upper end of a heat-insulating housing is connected with a flue gas treatment device; and an ash discharging chute is arranged the bottom in a position near the oil gas outlet, the reaction kettle is directly heated by a combustion chamber, and one end of the combustion chamber is connected with the gas recovery device. According to the system, the garbage is smashed and heated at a high temperature in the reaction kettle and reacts under the action of a non-hydrogen catalyst, an antifoaming agent and a flocculant to generate a great amount of gas and oily liquid, the gas and the oily liquid are condensed and subjected to oil-water separation so that oil is separated from the gas and the oily liquid and is recycled, and residues generated after the reaction can also be used for making carbon black. Therefore, the whole system saves energy, protects the environment and improves the living environment of residents.
Description
Art
The present invention relates to a kind of refuse disposal system, belong to technical field of environment protection equipment, especially a kind of greasy dirt rubbish processing to be harmless and recycling system.
Background technology
Along with the development of China's economy, industrial production obtains extensive development, but industrial production brings the industrial refuses such as a large amount of air-borne dust pollutions, sewage and solid waste.As produced some discarded object being stained with greasy dirt and rubbish in machine components manufactory etc., these rubbish are often directly poured on roadside or are transported to other vacant lot, cause very large pollution to environment.The midget plant that particularly distance living area is nearer, the various greasy dirt rubbish of discharge have a strong impact on resident's normal life.
In addition, China is livestock and poultry cultivation big country, and cultivation scale is at the forefront in the world.In the process of livestock culture, because the reason such as weather, epidemic disease exists certain death rate.The process place that the livestock and poultry of these death are not fixed, usually directly abandon roadside, or dispose by the mode of burying, these methods all can not reach complete harmless treatment, have a strong impact on living environment.For the poultry of death, need to carry out harmless treatment timely, avoid pestilence, environmental pollution even epidemic disease poultry come into the market.
Summary of the invention
For the defect of above-mentioned prior art and the technical problem of existence, the present invention devises a kind of greasy dirt rubbish processing to be harmless and recycling system, solves because of current industrial refuse, livestock and poultry garbage disposal is improper and the environmental problem caused and the harm brought.The present invention can carry out harmless treatment to industrial refuse, livestock and poultry rubbish etc. containing greasy dirt rubbish; be conducive to environmental protect; and manufacture lubrication wet goods be can be used for the oil reclaimed in garbage disposal; the solid residue of discharging can be used for making carbon black; reach the effect of discarded object recycling; drastically increase resource utilization, for environmental protection and social development provide a power.
The technical solution adopted for the present invention to solve the technical problems is: a kind of greasy dirt rubbish processing to be harmless and recycling system, comprise transmission device, reaction unit, flue gas processing device, gas recycling device; Described reaction unit comprises horizontal reacting still, the insulation cladding that described reactor is provided with spiral flap, cleaning device for inner wall and is enclosed in outside reactor, and described spiral flap and cleaning device for inner wall are fixed on reactor inwall; Described reactor one end is provided with charging aperture, and the other end is provided with oil gas vent, and described oil gas vent end is provided with transmission device; Described oil gas vent connects gas concentration unit; Be provided with safety valve between described oil gas vent and gas concentration unit, the automatic vent when air pressure reaches certain value, prevent air pressure too high; Described insulation cladding upper end exhanst gas outlet connects flue gas processing device; Reaction unit is provided with combustion chamber near the bottom of charging aperture one end, and bottom oil gas vent, be provided with ash chute, reactor is directly heated in combustion chamber, and one end, described combustion chamber connects gas concentration unit;
Described flue gas processing device comprises flue gas cleaner, smoke filter, spray column and adsorption tower, and described flue gas cleaner, smoke filter, spray column and adsorption tower are connected successively; Described adsorption tower afterbody is connected a blower fan, accelerates air flowing, is provided with activated carbon, alundum (Al2O3) can carry out desulfurization and drying to the sulphur-containing substance contained in flue gas and moisture in described adsorption tower; Be provided with in described spray column spray equipment can remove burning produce most of flue dust simultaneously to flue gas carry out cooling process; Waste gas after flue gas processing device process is pure pollution-free;
Described gas concentration unit comprises catalytic tower, settling tank, condenser, negative pressure device, oil water separator, gas purifier; Described catalytic tower, settling tank, condenser, negative pressure device, oil water separator, gas purifier are connected successively; The combustion chamber of described gas purifier one end coupled reaction still; Described oil water separator is connected with oil storage tank and wastewater disposal basin, described oil storage tank and wastewater disposal basin parallel connection; Described catalytic tower is connected with oil gas vent, is provided with catalyst in described catalytic tower, and described catalyst is non-hydrogen catalyst, described non-hydrogen catalyst can reduce the condensation point of distillate, make the heavy content of wax diesel oil of high condensation point be converted into the light diesel fuel of low condensation point, catalyst strength is high, active good;
Related content in technique scheme is explained as follows:
Described reactor inside is provided with spiral flap, and flap height is 20-30 centimetre, and rotating shaft runs through charging aperture and oil gas vent, and described oil gas vent end is provided with transmission device, and described transmission device comprises motor and driving-belt; Be the sleeve pipe of connection rotating shaft outside the pipeline of oil gas vent end, drive rotating shaft to rotate by the driving-belt on Electric Machine Control sleeve pipe, thus make the rubbish in reactor rub, fully react; Described reactor near charging aperture one end bottom be combustion chamber, directly heat reactor, in gas purifier final gas out, understand some not liquid gas, be connected to combustion chamber by pipeline, recycle as part of fuel; Ash chute is provided with, for discharging inner remaining solid residue after completion of the reaction bottom the other end of described reactor;
Cleaning device for inner wall is provided with in described reactor, described cleaning device for inner wall is fixed on reactor inwall by two stands, arc heat-resisting reinforcing bar is provided with in the middle of described support, described arc heat-resisting reinforcing bar is hinged in the middle of support, intermediate portion is arranged with balancing weight, when reactor rotates, balancing weight drives arc reinforcing bar to rotate scraping inwall, reaches the effect of cleaning inwall, prevents encrustation;
Insulation cladding top outside described reactor is provided with smoke discharge tube road, connect flue gas processing device, comprise and mainly contain spray equipment, the flue gas cleaner of water seal tank composition, pipeline in the middle of flue gas cleaner and smoke filter is equipped with blower fan, flue gas passes through spray equipment successively under fan action, most of flue dust that removing burning produces, enter smoke filter again, upper end is open type, fire resistant filter material is equipped with in its inside, as asbestos filter etc., then spray column is entered, after-treatment can be carried out to most of flue dust that burning produces by being provided with spray equipment in described spray column, finally enter adsorption tower again, be provided with activated carbon in described adsorption tower, alundum (Al2O3) can carry out desulfurization and drying to the sulphur-containing substance contained in flue gas and moisture, the waste gas after flue gas processing device process is pure pollution-free,
In system operation, by disposed waste and appropriate sodium metasilicate, soda ash, non-hydrogen catalyst, defoamer, flocculant together from charging aperture, described defoamer suppresses to produce bubble in reactor, remove the impurity and foreign material that are overflowed from oil gas vent by bubble, thus the thermal insulation layer between elimination fluid, increase heat transfer effect; Described flocculant makes the suspended particulates loss of stability in waste water, the inter coagulation of micelle thing phase makes particulate increase, form floccule body, alumen ustum, floccule body is grown up and namely depart from aqueous phase precipitation under gravity after certain volume, thus a large amount of suspensions in removal exhaust gas oil stain, eliminate the thermal insulation layer between fluid simultaneously, increase heat transfer effect; Described non-hydrogen catalyst can reduce the condensation point of distillate, and make the heavy content of wax diesel oil of high condensation point be converted into the light diesel fuel of low condensation point, catalyst strength is high, active good; Rubbish in reactor carries out pyrolysis under the effect of non-hydrogen catalyst, defoamer and flocculant, produces a large amount of gas, enters into gas treatment equipment; First can through settling tank, wherein entrained solid particle drops wherein thereupon, more successively through condenser and oil water separator, the oil in gas is separated recycling; Be provided with negative pressure device between described condenser and oil water separator, form negative pressure, be conducive to gas, liquid communication, to eventually pass through in the gas of gas purifier process due to containing not liquid gas, it is directly introduced combustion chamber as fuel utilization;
Relevant device in whole treatment system and everywhere pipeline are all provided with the instrument such as thermometer, Pressure gauge, in operation, check operating mode at any time, guarantee normal operation.
Compared to existing technology, the beneficial effect of the greasy dirt rubbish processing to be harmless system related to of the present invention is:
1, simple in equipment, cost is low, effective, is convenient to industrialization;
2, rubbish reaches innoxious requirement after treatment, is conducive to environmental protection, well improves urban residents'
Periphery living environment;
3, can be used for manufacture lubrication wet goods to the oil reclaimed in garbage disposal, the solid residue of discharge can be used for making charcoal
Black, whole processing procedure energy-conserving and environment-protective, reach waste recovery, improve resource utilization.
Accompanying drawing explanation
Fig. 1 is system flow chart of the present invention.
In figure: 1, reactor, 2, insulation cladding, 3, combustion chamber, 4, oil-out, 5, catalytic tower, 6, settling tank, 7, condenser, 8, negative pressure device, 9, oil water separator, 10, gas purifier, 11, wastewater disposal basin, 12, oil storage tank, 13, flue gas cleaner, 14, smoke filter, 15, spray column, 16, adsorption tower, 17, blower fan, 18, ash chute, 19, charging aperture, 20, transmission device, 21, cleaning plant, 22, spiral flap.
Detailed description of the invention
Below in conjunction with accompanying drawing, the specific embodiment of the present invention is elaborated, illustrate advantage of the present invention and the outstanding contributions relative to prior art further, understandable, following embodiment is only the detailed description to the better embodiment of the present invention, should not be interpreted as any restriction to technical solution of the present invention.
As shown in Figure 1, rubbish, appropriate sodium metasilicate, soda ash, non-hydrogen catalyst, defoamer, the flocculants such as greasy dirt rubbish and dead pig are together added from charging aperture 19 and starts combustion chamber 3, reactor 1 is heated to about 300 degree, along with temperature raises, the gas that reaction produces and oily liq go out 4 by oil gas gradually and accelerate complete reaction by catalytic tower 5, enter settling tank 6 again, wherein entrained solid particle drops and to precipitate in water, residual gas and oily liq successively by condenser 7, negative pressure device 8, oil water separator 9, gas purifier 10.
In condenser 7, the oily liq of condensation enters into oil water separator 9, the oil separated by the row of conduits on oil water separator 9 top to oil storage tank 12; Be connected with wastewater disposal basin 11 bottom oil water separator 8, collect the waste water of discharging; Remaining gas is from the row of conduits on oil water separator 9 top to gas purifier 10, pipeline inserts below the liquid level of water in gas purifier 10, not liquid gas is contained, through row of conduits in combustion chamber 3, as the part of fuel of combustion chamber 3 in the gas that gas purifier 10 is finally discharged.
The flue gas produced in reactor 1 is introduced into flue gas cleaner 13 through pipeline, flow through smoke filter 14 again, and then undertaken lowering the temperature and dedusting by spray column 15, finally carry out desulfurization and drying by adsorption tower 16 pairs of flue gases, wherein blower fan 17 accelerates air flowing, and gas is after treatment environment friendly and pollution-free.
Reactor 3 is subject to transmission device 20 driven rotary when heating simultaneously, insulation cladding 2 keeps fixing, and when reactor 3 rotates, rubbish rubs, fully reflects by the spiral flap 22 on reactor 3 inwall, simultaneously cleaning device for inner wall 21 is swiped reactor 3 inwall, reaches the effect of cleaning, de-sludging.
Solid residue is expelled to ash chute 18 by reactor 3 after completion of the reaction.
Claims (6)
1. greasy dirt rubbish processing to be harmless and a recycling system, comprises transmission device, reaction unit, flue gas processing device, gas concentration unit; Described reaction unit comprises horizontal reacting still, the insulation cladding that described reactor is provided with spiral flap, cleaning device for inner wall and is enclosed in outside reactor, and described spiral flap and cleaning device for inner wall are fixed on reactor inwall; Described reactor one end is provided with charging aperture, and the other end is provided with oil gas vent, and described oil gas vent end is provided with transmission device; Described oil gas vent connects gas concentration unit; Be provided with safety valve between described oil gas vent and gas concentration unit, the automatic vent when air pressure reaches certain value, prevent air pressure too high; Described insulation cladding upper end exhanst gas outlet connects flue gas processing device; Reaction unit is provided with combustion chamber near the bottom of charging aperture one end, and bottom oil-out, be provided with ash chute, reactor is directly heated in combustion chamber, and one end, described combustion chamber connects gas concentration unit.
2. a kind of greasy dirt rubbish processing to be harmless according to claim 1 and recycling system, its special type is: described flue gas processing device comprises flue gas cleaner, smoke filter, spray column and adsorption tower, and described flue gas cleaner, smoke filter, spray column and adsorption tower are connected successively; Described adsorption tower afterbody is connected a blower fan; Activated carbon, alundum (Al2O3) is provided with in described adsorption tower.
3. a kind of greasy dirt rubbish processing to be harmless according to claim 1 and recycling system, its special type is: described gas concentration unit comprises catalytic tower, settling tank, condenser, negative pressure device, oil water separator, gas purifier; Described catalytic tower, settling tank, condenser, negative pressure device, oil water separator, gas purifier are connected successively; The combustion chamber of described gas purifier one end coupled reaction still; Described oil water separator is connected with oil storage tank and wastewater disposal basin, described oil storage tank and wastewater disposal basin parallel connection; Described catalytic tower is connected with oil-out, is provided with catalyst in described catalytic tower, and described catalyst is non-hydrogen catalyst.
4. a kind of greasy dirt rubbish processing to be harmless according to claim 1 and recycling system, its special type is: described reactor inside is provided with spiral flap, flap height is 20-30 centimetre, rotating shaft runs through charging aperture and oil gas vent, described oil gas vent end is provided with transmission device, and described transmission device comprises motor and driving-belt; Be the sleeve pipe of connection rotating shaft outside the pipeline of oil gas vent end, drive rotating shaft to rotate by the driving-belt on Electric Machine Control sleeve pipe.
5. a kind of greasy dirt rubbish processing to be harmless according to claim 1 and recycling system, its special type is: be provided with cleaning device for inner wall in described reactor, described cleaning device for inner wall is fixed on reactor inwall by two stands, arc heat-resisting reinforcing bar is provided with in the middle of described support, described arc heat-resisting reinforcing bar is hinged in the middle of support, and intermediate portion is arranged with balancing weight.
6. a kind of greasy dirt rubbish processing to be harmless according to claim 1 and recycling system, its special type is: the relevant device in described whole treatment system and everywhere pipeline are all provided with the instrument such as thermometer, Pressure gauge, check operating mode at any time in operation, guarantee normal operation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510926689.5A CN105537233B (en) | 2015-12-14 | 2015-12-14 | A kind of greasy dirt rubbish processing to be harmless and recycling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510926689.5A CN105537233B (en) | 2015-12-14 | 2015-12-14 | A kind of greasy dirt rubbish processing to be harmless and recycling system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105537233A true CN105537233A (en) | 2016-05-04 |
| CN105537233B CN105537233B (en) | 2018-04-06 |
Family
ID=55817061
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510926689.5A Active CN105537233B (en) | 2015-12-14 | 2015-12-14 | A kind of greasy dirt rubbish processing to be harmless and recycling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105537233B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106994461A (en) * | 2017-04-12 | 2017-08-01 | 黄嘉铭 | A kind of environment-friendly and energy-efficient animals with diseases innocent treatment equipment and its method |
| CN110259399A (en) * | 2019-06-25 | 2019-09-20 | 成都华寰环保科技有限公司 | Base oil recovery process and its device in a kind of drilling well oil-base mud landwaste |
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| JPH09279171A (en) * | 1996-04-10 | 1997-10-28 | Nippon Steel Corp | Purification of oil-containing thermal decomposition gas |
| CN102001803A (en) * | 2010-10-29 | 2011-04-06 | 唐山南光实业有限公司 | Rotary oil-containing sludge treatment device |
| CN102220152A (en) * | 2010-04-16 | 2011-10-19 | 华南再生资源（中山）有限公司 | Reactor wall scraper |
| CN203791334U (en) * | 2014-05-09 | 2014-08-27 | 代全光 | Oil contamination garbage innocent treatment system |
| CN104789251A (en) * | 2015-05-05 | 2015-07-22 | 湖南奔骥环保能源科技有限责任公司 | External-rotation and internal-turning full-automatic continuous cracking and refining device |
-
2015
- 2015-12-14 CN CN201510926689.5A patent/CN105537233B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH09279171A (en) * | 1996-04-10 | 1997-10-28 | Nippon Steel Corp | Purification of oil-containing thermal decomposition gas |
| CN102220152A (en) * | 2010-04-16 | 2011-10-19 | 华南再生资源（中山）有限公司 | Reactor wall scraper |
| CN102001803A (en) * | 2010-10-29 | 2011-04-06 | 唐山南光实业有限公司 | Rotary oil-containing sludge treatment device |
| CN203791334U (en) * | 2014-05-09 | 2014-08-27 | 代全光 | Oil contamination garbage innocent treatment system |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106994461A (en) * | 2017-04-12 | 2017-08-01 | 黄嘉铭 | A kind of environment-friendly and energy-efficient animals with diseases innocent treatment equipment and its method |
| CN110259399A (en) * | 2019-06-25 | 2019-09-20 | 成都华寰环保科技有限公司 | Base oil recovery process and its device in a kind of drilling well oil-base mud landwaste |
| CN110259399B (en) * | 2019-06-25 | 2024-02-06 | 成都华寰环保科技有限公司 | Process and device for recovering base oil from drilling oil-based mud cuttings |
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| Publication number | Publication date |
|---|---|
| CN105537233B (en) | 2018-04-06 |
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