CN106608706A - Resource utilization method of oily sludge through innocent treatment - Google Patents
Resource utilization method of oily sludge through innocent treatment Download PDFInfo
- Publication number
- CN106608706A CN106608706A CN201610452563.3A CN201610452563A CN106608706A CN 106608706 A CN106608706 A CN 106608706A CN 201610452563 A CN201610452563 A CN 201610452563A CN 106608706 A CN106608706 A CN 106608706A
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- Prior art keywords
- oil
- oily sludge
- solid
- water
- solid slag
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- 239000010802 sludge Substances 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims abstract description 34
- 239000003921 oil Substances 0.000 claims abstract description 51
- 239000007787 solid Substances 0.000 claims abstract description 29
- 239000002893 slag Substances 0.000 claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000004033 plastic Substances 0.000 claims abstract description 17
- 229920003023 plastic Polymers 0.000 claims abstract description 17
- 239000007790 solid phase Substances 0.000 claims abstract description 15
- 238000003795 desorption Methods 0.000 claims abstract description 14
- BXLNWOAYQXBHCY-UHFFFAOYSA-N diphenylsilylidene(diphenyl)silane Chemical compound C1=CC=CC=C1[Si](C=1C=CC=CC=1)=[Si](C=1C=CC=CC=1)C1=CC=CC=C1 BXLNWOAYQXBHCY-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000005191 phase separation Methods 0.000 claims abstract description 10
- 239000010865 sewage Substances 0.000 claims abstract description 10
- 238000010438 heat treatment Methods 0.000 claims abstract description 9
- 239000003517 fume Substances 0.000 claims abstract description 6
- 239000012535 impurity Substances 0.000 claims abstract description 5
- 238000003756 stirring Methods 0.000 claims abstract description 3
- 238000004140 cleaning Methods 0.000 claims abstract 2
- 238000000197 pyrolysis Methods 0.000 claims description 13
- 238000005516 engineering process Methods 0.000 claims description 11
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 6
- 239000003546 flue gas Substances 0.000 claims description 6
- 239000008187 granular material Substances 0.000 claims description 5
- 238000000465 moulding Methods 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 5
- 238000005406 washing Methods 0.000 claims description 5
- 230000003311 flocculating effect Effects 0.000 claims description 4
- 239000000356 contaminant Substances 0.000 claims description 3
- 230000026676 system process Effects 0.000 claims description 3
- 238000005496 tempering Methods 0.000 claims description 3
- 239000002671 adjuvant Substances 0.000 claims description 2
- 238000001311 chemical methods and process Methods 0.000 claims description 2
- 238000001914 filtration Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 claims description 2
- 238000006386 neutralization reaction Methods 0.000 claims description 2
- 238000000746 purification Methods 0.000 claims description 2
- 238000005201 scrubbing Methods 0.000 claims description 2
- 238000004062 sedimentation Methods 0.000 claims description 2
- 230000011218 segmentation Effects 0.000 claims description 2
- 239000007921 spray Substances 0.000 claims description 2
- 238000004064 recycling Methods 0.000 abstract description 4
- 230000003750 conditioning effect Effects 0.000 abstract 3
- 239000011449 brick Substances 0.000 abstract 1
- 239000002245 particle Substances 0.000 abstract 1
- 238000007670 refining Methods 0.000 abstract 1
- 239000002689 soil Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 2
- 241000772415 Neovison vison Species 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
- B01D46/023—Pockets filters, i.e. multiple bag filters mounted on a common frame
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/10—Treatment of sludge; Devices therefor by pyrolysis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B33/00—Clay-wares
- C04B33/02—Preparing or treating the raw materials individually or as batches
- C04B33/13—Compounding ingredients
- C04B33/132—Waste materials; Refuse; Residues
- C04B33/1321—Waste slurries, e.g. harbour sludge, industrial muds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/60—Production of ceramic materials or ceramic elements, e.g. substitution of clay or shale by alternative raw materials, e.g. ashes
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/40—Valorisation of by-products of wastewater, sewage or sludge processing
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Hydrology & Water Resources (AREA)
- Water Supply & Treatment (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- Ceramic Engineering (AREA)
- Health & Medical Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Analytical Chemistry (AREA)
- Dispersion Chemistry (AREA)
- Biomedical Technology (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Treatment Of Sludge (AREA)
Abstract
The invention discloses a resource utilization method of oily sludge through innocent treatment. The resource utilization method comprises the steps of conducting sorting, supplying heat, conducting conditioning and separating, recycling plastic, performing three-phase separation, performing TPDS (pyrolyzation and desorption), utilizing solid slag, treating fume and sewage and performing automatic controlling. The process flow comprises the steps of sorting the oily sludge, conducting cleaning with hot water and conducting refining, wherein the sorted oily sludge particles are less than 2 mm; granulating cleaned-out plastic impurities and then performing recycling; preheating the sorted oily sludge, then conducting conditioning, namely conducting dosing, and heating while stirring, and performing oil, water and solid three-phase separation after conditioning; sending separated oil to an oil tank to be stored and allowing water to enter a sewage treatment system to be treated so as to be recycled or discharged to reach the standard, and performing TPDS (pyrolyzation and desorption) treatment on solid phase which still contains a small amount of oil, so that the oil in the solid phase is desorbed and separated out; and recycling the oil in the oil tank, and allowing the solid slag to enter a solid slag curing unit, and performing forming so as to make bricks. Finally, the oil content of the solid slag is less than or equal to 0.3%, and the moisture content is less than or equal to 1%.
Description
Technical field
The present invention relates to a kind of process for treating oil-containing sludge, specifically a kind of oily sludge harmless treatment recycling side
Method.
Background technology
Oily sludge refer to the oil that the mink cell focuses and soil, water etc. such as crude oil, various product oils, residual oil mix and formed,
Soil, water, or even the mixture of other pollutant such as it is blended with.If directly discharged without processing, substantial amounts of soil is not only taken up
Ground, it also containing substantial amounts of heavy metal and antibacterial, can produce the severe contamination that stench causes water body, soil and air.Mesh
The front treatment technology to oily sludge has a lot, related according to the requirement of minimizing, innoxious, resource and comprehensive utilization
Processing method is summed up mainly to be had：Solidification technology, incineration treatment technology, biological restoration treatment technology, solvent extraction
Treatment technology, chemico-heating wash treatment technology, pyrolysis processing technology etc..
The big multiprocessing of existing contained Mud Treatment Technology is not thorough, and solid slag oil content is higher, and hot washing device can produce substantial amounts of dirt
Water, it is quenched during introduce demulsifier and surfactant, problem of environmental pollution can be brought, easily cause secondary pollution, Gu
It is difficult after change to recover soil characteristic.
The content of the invention
It is an object of the invention to provide a kind of oily sludge harmless treatment resource utilization method, to solve above-mentioned background skill
The problem proposed in art.
For achieving the above object, the present invention provides following technical scheme：
The invention discloses a kind of oily sludge harmless treatment resource utilization method.Including sorting, heat supply, quenched separation,
Plastic reclaimed, three phase separation, TPDS (pyrolysis desorption), solid slag is utilized, fume treatment, sewage disposal, is automatically controlled.
Its technological process is：Oily sludge is sorted first, hot water is cleaned and refined.Oily sludge granule is less than 2mm after sorting.
Reclaim after the plastic contaminant pelletize for washing out.Oily sludge after sorting enters hardening and tempering process, dosing, heating after preheating
Stir simultaneously, it is quenched after oily sludge carry out oil, water, solid three phase separation.The oil isolated sends into oil tank storage.Separate
The water for going out enters reuse or qualified discharge after sewage disposal system process.The solid phase isolated still contains a small amount of oil, solid phase
Process via TPDS (pyrolysis desorption), the oil in solid phase is desorbed and is separated.The oil of generation is reclaimed into oil tank,
Solid slag oil content≤0.3% of generation, moisture content≤1%, solid slag enters solid slag solidified cell, molding brickmaking.TPDS (heat
Solution desorption) and it is plastic reclaimed during generation flue gas enter flue gas processing device.State IV standards discharge is reached after treatment.
Final solid slag oil content≤0.3% is capable of achieving using the technological process of the present invention.
As further scheme of the invention：Characterized in that, described sort process, to oily sludge rough segmentation is carried out, in
Point, impurity to be separated after subdivision, the oily sludge granule after process is less than 2mm.The impurity isolated enters plastics again
Raw technique.
As further scheme of the invention：Described heating unit, to the technique such as sorting, quenched heat is provided.
As further scheme of the invention：Described is quenched, dosing, heating, sludge is carried out by physical chemistry method quenched.
As further scheme of the invention：Described is plastic reclaimed, reclaims after the plastic granulating for washing out.
As further scheme of the invention：Described three phase separation, the mechanical separation to water, oil and solid phase.Solid phase contains
There are a small amount of oil, moisture content≤40%.
As further scheme of the invention：Described TPDS (pyrolysis desorption), using pyrolysis desorption technology, by oil-containing
Oil content in sludge is desorbed and separates, solid slag oil content≤0.3% after process, moisture content≤1%.
As further scheme of the invention：Described solid slag is utilized, plus adjuvant molding brickmaking.
As further scheme of the invention：Described fume treatment, gas enters sack cleaner, acid-base neutralization and spray
After scrubbing tower purification, qualified discharge.
As further scheme of the invention：Described sewage disposal, sewage Jing flocculating sedimentatioies, air supporting are further gone in eliminating water
Reuse after a small amount of oil, tail water reaches discharge standard Jing after flocculating sedimentation, air supporting, filtration.
Description of the drawings
Fig. 1 is oily sludge harmless treatment resource utilization method process chart.
Specific embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clearly and completely
Description, it is clear that described embodiment is only a part of embodiment of the invention, rather than the embodiment of whole.Based on this
Embodiment in invention, the every other enforcement that those skilled in the art are obtained under the premise of creative work is not made
Example, belongs to the scope of protection of the invention.
Fig. 1 is referred to, in the embodiment of the present invention, an a kind of oily sludge harmless treatment resource utilization method.Including point
Pick, heat supply, quenched separation, plastic reclaimed, three phase separation, TPDS (pyrolysis desorption), solid slag is utilized, fume treatment,
Sewage disposal, automatically control.Its technological process is：Oily sludge is sorted first, hot water is cleaned and refined.Point
Rear oily sludge granule is picked less than 2mm.Reclaim after the plastic contaminant pelletize for washing out.Oily sludge after sorting is through preheating
Enter hardening and tempering process afterwards, dosing, heating are stirred simultaneously, it is quenched after oily sludge carry out oil, water, solid three phase separation.Point
The oil for separating out sends into oil tank storage.The water isolated enters reuse or qualified discharge after sewage disposal system process.Isolate
Solid phase still contain a small amount of oil, solid phase is processed via TPDS (pyrolysis desorption), by the oil desorption in solid phase and is separated
Out.The oil of generation is reclaimed into oil tank, solid slag oil content≤0.3% of generation, moisture content≤1%, and solid slag is solid into solid slag
Change unit, molding brickmaking.TPDS (pyrolysis desorption) and it is plastic reclaimed during the flue gas of generation enter flue gas processing device.
State IV standards discharge is reached after treatment.
Final solid slag oil content≤0.3% is capable of achieving using the technological process of the present invention.
It is obvious to a person skilled in the art that the invention is not restricted to the details of above-mentioned one exemplary embodiment, and do not carrying on the back
In the case of the spirit or essential attributes of the present invention, the present invention can be in other specific forms realized.Therefore, no matter from
From the point of view of which point, embodiment all should be regarded as exemplary, and be nonrestrictive, the scope of the present invention is by appended power
Profit is required rather than described above is limited, it is intended that all in the implication and scope of the equivalency of claim by falling
Change is included in the present invention.Any reference in claim should not be considered as and limit involved claim.
Moreover, it will be appreciated that although this specification is been described by according to embodiment, not each embodiment is only included
One independent technical scheme, this narrating mode of description is only that for clarity, those skilled in the art should be by
Description as an entirety, the technical scheme in each embodiment can also Jing it is appropriately combined, forming those skilled in the art can
With the other embodiment for understanding.
Claims (10)
1. a kind of oily sludge harmless treatment resource utilization method.Including sorting, heat supply, quenched separation are plastic reclaimed,
Three phase separation, TPDS (pyrolysis desorption), solid slag is utilized, fume treatment, sewage disposal, is automatically controlled.Its technique stream
Cheng Wei：Oily sludge is sorted first, hot water is cleaned and refined.Oily sludge granule is less than 2mm after sorting.Cleaning
Reclaim after the plastic contaminant pelletize for going out.Oily sludge after sorting enters hardening and tempering process after preheating, and dosing, heating are simultaneously
Stirring, it is quenched after oily sludge carry out oil, water, solid three phase separation.The oil isolated sends into oil tank storage.Isolate
Water enters reuse or qualified discharge after sewage disposal system process.The solid phase isolated still contain a small amount of oil, solid phase via
TPDS (pyrolysis desorption) is processed, and the oil content in solid phase is desorbed and is separated.The oil of generation is reclaimed into oil tank, is produced
Solid slag oil content≤0.3%, moisture content≤1%, solid slag enter solid slag solidified cell, molding brickmaking.(pyrolysis is de- for TPDS
It is attached) and it is plastic reclaimed during produce flue gas enter flue gas processing device.State IV standards discharge is reached after treatment.
Final solid slag oil content≤0.3% is capable of achieving using the technological process of the present invention.
2. sort process according to claim 1, it is characterised in that rough segmentation is carried out to oily sludge, in point, after subdivision
Separate with impurity, the oily sludge granule after process is less than 2mm.The impurity isolated enters plastic reclaimed technique.
3. heat supply according to claim 1, it is characterised in that the preheating to the technique and oily sludge such as sorting, quenched is carried
Heating load.
4. it is according to claim 1 quenched, it is characterised in that dosing, heating, sludge is adjusted by physical chemistry method
Matter.
5. it is according to claim 1 plastic reclaimed, it is characterised in that to reclaim after the plastic granulating for washing out.
6. three phase separation according to claim 1, it is characterised in that the mechanical separation to water, oil and solid phase.Solid phase contains
Oily a small amount of oil, moisture content≤60%.
7. TPDS according to claim 1 (pyrolysis desorption), it is characterised in that on the basis of own pyrolysis charring technology,
Oil content in oily sludge is desorbed and is separated, solid slag oil content≤0.3% after process, moisture content≤1%.
8. solid slag according to claim 1 is utilized, it is characterised in that plus adjuvant molding brickmaking.
9. fume treatment according to claim 1, it is characterised in that gas enters sack cleaner, acid-base neutralization and spray
After scrubbing tower purification, qualified discharge.
10. water process according to claim 1, it is characterised in that water Jing flocculating sedimentatioies, air supporting are further gone out a small amount of in water
Oil after reuse, tail water reaches discharge standard Jing after flocculating sedimentation, air supporting, filtration.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610452563.3A CN106608706A (en) | 2016-06-21 | 2016-06-21 | Resource utilization method of oily sludge through innocent treatment |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201610452563.3A CN106608706A (en) | 2016-06-21 | 2016-06-21 | Resource utilization method of oily sludge through innocent treatment |
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| CN106608706A true CN106608706A (en) | 2017-05-03 |
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| CN201610452563.3A Pending CN106608706A (en) | 2016-06-21 | 2016-06-21 | Resource utilization method of oily sludge through innocent treatment |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107151088A (en) * | 2017-07-21 | 2017-09-12 | 浙江宜可欧环保科技有限公司 | The processing method of oily sludge on offshore platform |
| CN108585398A (en) * | 2018-07-12 | 2018-09-28 | 上海呈策环保科技有限公司 | A kind of method and its apparatus system of processing oily sludge |
| CN108640655A (en) * | 2018-06-07 | 2018-10-12 | 四川农业大学 | A method of energy conservation and environmental protection construction material is prepared by municipal sludge |
| CN108996859A (en) * | 2018-08-30 | 2018-12-14 | 广西博世科环保科技股份有限公司 | High concentration petroleum sludge green cleaning-thermal desorption integrated technology processing method and processing system |
| CN109652119A (en) * | 2019-01-26 | 2019-04-19 | 沧州信昌化工股份有限公司 | Sump oil/aging oil treatment equipment |
| CN110395861A (en) * | 2019-08-29 | 2019-11-01 | 宜兴市创新环保有限公司 | A method of it is granulated using oily sludge |
| CN111299294A (en) * | 2020-03-27 | 2020-06-19 | 武汉集斯广宜环保科技有限公司 | Comprehensive treatment system and method for oily waste |
| CN112744990A (en) * | 2020-12-04 | 2021-05-04 | 陕西欧菲德环保科技有限公司 | Harmless treatment system and treatment process for ground oil sludge |
| CN113121074A (en) * | 2019-12-30 | 2021-07-16 | 中国石油天然气股份有限公司 | Method and system for thermal fine washing-multiphase separation of thick oil sludge |
| CN113562946A (en) * | 2021-09-07 | 2021-10-29 | 山东河轩环保科技有限公司 | Quality change process for treating sludge by using oil shale oil refining furnace |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102039301A (en) * | 2010-09-30 | 2011-05-04 | 昆明理工大学 | Oily sludge recycling and innocent comprehensive treatment process |
| CN102180575A (en) * | 2011-03-31 | 2011-09-14 | 濮阳市天地人环保工程技术有限公司 | Processing method for centralized treatment and reclamation of oil-containing sludge |
| CN104341081A (en) * | 2013-07-30 | 2015-02-11 | 麦王环境技术股份有限公司 | Harmless treatment method for separation and recovery of oily sludge |
-
2016
- 2016-06-21 CN CN201610452563.3A patent/CN106608706A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102039301A (en) * | 2010-09-30 | 2011-05-04 | 昆明理工大学 | Oily sludge recycling and innocent comprehensive treatment process |
| CN102180575A (en) * | 2011-03-31 | 2011-09-14 | 濮阳市天地人环保工程技术有限公司 | Processing method for centralized treatment and reclamation of oil-containing sludge |
| CN104341081A (en) * | 2013-07-30 | 2015-02-11 | 麦王环境技术股份有限公司 | Harmless treatment method for separation and recovery of oily sludge |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107151088A (en) * | 2017-07-21 | 2017-09-12 | 浙江宜可欧环保科技有限公司 | The processing method of oily sludge on offshore platform |
| CN108640655A (en) * | 2018-06-07 | 2018-10-12 | 四川农业大学 | A method of energy conservation and environmental protection construction material is prepared by municipal sludge |
| CN108640655B (en) * | 2018-06-07 | 2020-11-24 | 四川农业大学 | Method for preparing energy-saving and environment-friendly building material from municipal sludge |
| CN108585398A (en) * | 2018-07-12 | 2018-09-28 | 上海呈策环保科技有限公司 | A kind of method and its apparatus system of processing oily sludge |
| WO2020041917A1 (en) * | 2018-08-30 | 2020-03-05 | 广西博世科环保科技股份有限公司 | Green cleaning-thermal desorption integrated technology treatment method and system for high-concentration petroleum sludge |
| CN108996859A (en) * | 2018-08-30 | 2018-12-14 | 广西博世科环保科技股份有限公司 | High concentration petroleum sludge green cleaning-thermal desorption integrated technology processing method and processing system |
| CN109652119A (en) * | 2019-01-26 | 2019-04-19 | 沧州信昌化工股份有限公司 | Sump oil/aging oil treatment equipment |
| CN110395861A (en) * | 2019-08-29 | 2019-11-01 | 宜兴市创新环保有限公司 | A method of it is granulated using oily sludge |
| CN113121074A (en) * | 2019-12-30 | 2021-07-16 | 中国石油天然气股份有限公司 | Method and system for thermal fine washing-multiphase separation of thick oil sludge |
| CN111299294A (en) * | 2020-03-27 | 2020-06-19 | 武汉集斯广宜环保科技有限公司 | Comprehensive treatment system and method for oily waste |
| CN111299294B (en) * | 2020-03-27 | 2023-04-18 | 武汉集斯广宜环保科技有限公司 | Comprehensive treatment system and method for oily waste |
| CN112744990A (en) * | 2020-12-04 | 2021-05-04 | 陕西欧菲德环保科技有限公司 | Harmless treatment system and treatment process for ground oil sludge |
| CN113562946A (en) * | 2021-09-07 | 2021-10-29 | 山东河轩环保科技有限公司 | Quality change process for treating sludge by using oil shale oil refining furnace |
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