CN202898175U - Oil field oily sludge resourceful treatment device - Google Patents
Oil field oily sludge resourceful treatment device Download PDFInfo
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- CN202898175U CN202898175U CN201220476934.9U CN201220476934U CN202898175U CN 202898175 U CN202898175 U CN 202898175U CN 201220476934 U CN201220476934 U CN 201220476934U CN 202898175 U CN202898175 U CN 202898175U
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- sludge
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- 239000010802 sludge Substances 0.000 title claims abstract description 41
- 238000000605 extraction Methods 0.000 claims abstract description 54
- 239000003921 oil Substances 0.000 claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000010779 crude oil Substances 0.000 claims abstract description 19
- 239000002904 solvent Substances 0.000 claims abstract description 18
- 238000005191 phase separation Methods 0.000 claims abstract description 16
- 239000007790 solid phase Substances 0.000 claims abstract description 8
- 239000012071 phase Substances 0.000 claims abstract description 7
- 239000007791 liquid phase Substances 0.000 claims abstract description 4
- 238000005188 flotation Methods 0.000 claims description 16
- 239000003795 chemical substances by application Substances 0.000 claims description 11
- 238000004064 recycling Methods 0.000 claims description 10
- 230000015556 catabolic process Effects 0.000 claims description 8
- 238000006731 degradation reaction Methods 0.000 claims description 7
- 239000002699 waste material Substances 0.000 claims description 6
- 238000000926 separation method Methods 0.000 abstract description 7
- 238000004821 distillation Methods 0.000 abstract description 6
- 239000000047 product Substances 0.000 abstract description 6
- 239000010865 sewage Substances 0.000 abstract description 4
- 239000013589 supplement Substances 0.000 abstract 2
- 238000006065 biodegradation reaction Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 14
- 239000007788 liquid Substances 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 239000000839 emulsion Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 238000002955 isolation Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000012188 paraffin wax Substances 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 102100033429 Glutamine-fructose-6-phosphate aminotransferase [isomerizing] 1 Human genes 0.000 description 1
- 101710165608 Glutamine-fructose-6-phosphate aminotransferase [isomerizing] 1 Proteins 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000002054 inoculum Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 230000011218 segmentation Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 239000011877 solvent mixture Substances 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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- Treatment Of Sludge (AREA)
Abstract
The utility model relates to a resource treatment device for oily sludge in an oil field; the hoister is connected with a vibrating rotary screen, and the vibrating rotary screen is connected with single-arm multi-paddle extraction equipment; the single-arm multi-paddle extraction equipment is connected with the separation settling tank; the solid phase outlet of the separation settling tank is connected with the flow curtain type extraction tower; the liquid phase outlet of the separation settling tank is connected with the two-phase separation tank; an oil phase outlet of the two-phase separation tank is connected with the reduced pressure distillation tower, and a water phase outlet of the two-phase separation tank is connected with the electric floating system; an extractant outlet of the reduced pressure distillation tower is connected with a solvent supplement tank, a crude oil outlet of the reduced pressure distillation tower is connected with a crude oil finished product tank, and the solvent supplement tank is connected with the single-arm multi-paddle extraction equipment and the flow curtain type extraction tower; an oily sewage outlet of the sludge tank is connected with an electric floating system, and an oil residue outlet of the electric floating system is connected with a flow curtain type extraction tower; the water phase outlet of the electric floating system is connected with the water treatment system, and the solid phase outlet of the flow curtain type extraction tower is connected with the biodegradation system; the oil content of the silt processed by the device reaches the national stacking standard.
Description
Technical field
The utility model relates to a kind of Sludge in Oilfields processing equipment for recycling.
Background technology
The source of oil sludge mainly is the sandy oil-containing sludge that produces in the Oil extraction process, the sandy oil-containing sludge that contains sandy oil-containing sludge and the generation of refinery's Sewage treatment systems of oil field gathering and transportation process generation.These oil sludges also contain the stratum silt that carries in the Produced Liquid except containing crude oil, the flco that forms in the sewage treatment process of disposing polluted water in oil station, corrosive pipeline product, heavy metal salt and paraffin, gum asphalt etc., and certain moisture content.
The oily sludge that produces in the Oil extraction process is mainly derived from Ground Processing System, and the oily sludge that produces in the oil extraction-generated waste water treating processes is added flco that the water purification agent that adds in the dirty water decontamination handles forms etc. and formed oily sludge.
The oil field gathering and transportation process produces oil tank that oily sludge is mainly derived from block station, joint station, slurry tank, Water Tank, oil trap bed mud, oil product storage tank when storing oil product, a small amount of mechanical impurity in the oil product, the grains of sand, earth, heavy metal salt and the heavy components such as paraffin and bituminous matter are deposited on tank bottom, form tank bottom oil sludge.The blowdown of slurry tank, secondary settlement tank, well-flushing water withdrawing can also can produce oily sludge in addition.
By analysis these oily sludges form different, usually oil length between 10%～60%, the solids 10-60% such as silt, and water 15-60%.In the situation that petroleum resources growing tension and environmental problem are on the rise, the crude oil in the efficient recovery oil sludge has not only been saved valuable petroleum resources, and has eliminated environmental pollution.
Relatively the method for processing oily sludge commonly used has at present: solidify and bury, burn hot washing method, solvent extration, chemical demulsification method, solid-liquid isolation method, pyrolysis method etc.But wherein many methods all exist some problems, are not suitable for very much for practical application.Power consumption greatly, easily produces secondary pollution such as burning method, the crude resources waste; Biological treatment need last length, and same crude resources also can not get recycling; Chemical demulsification method need add emulsion splitter and heating in addition to the serious oily sludge of emulsification, and aftertreatment is difficult, also produces secondary pollution simultaneously; Solid-liquid isolation method is low for the crude oil recovery rate that contains innage, with serious pollution oily sludge; The pyrolysis method facility investment is high.
Solvent extraction is the effective ways that reclaim crude oil, and the body refuse after the extraction more easily reaches the national standard of landfill or stacking, but and the crude resources of efficient recovery preciousness, thereby draw its people's concern.Patent CN1526797A uses extraction process and reclaim oil fuel from oily sludge, and this patent adopts general extraction tower, and when the oily sludge layering was slower, the diluted acid that needs to add 1-3% carried out breakdown of emulsion, can cause the corrosion of equipment and the secondary pollution of environment.
The utility model content
The purpose of this utility model provides a kind of Sludge in Oilfields processing equipment for recycling, oily sludge is after extraction, sedimentation, separation, fractionation, crude oil is recycled, the solvent reclamation reuse, and solid slag can reach the GB4284-84 effluent standard after biological degradation is processed.
Sludge in Oilfields processing equipment for recycling described in the utility model comprises lift, vetivert rotary screen, many oars of single armed extraction equipment, separate and subside tank, two phase separation pot, stream curtain formula extraction tower, electro-flotation system, vacuum still, sludge sump, biological degradation system, solvent makeup tank and crude oil finished pot; Lift is positioned at the sludge sump top, is connected with vetivert rotary screen, and the outlet that vetivert rotary screen is positioned at the bottom is connected with the entrance of many oars of single armed extraction equipment; The outlet of many oars of single armed extraction equipment is connected with the separate and subside tank; The solid phase outlet of separate and subside tank is connected with the entrance of stream curtain formula extraction tower; The liquid-phase outlet of separate and subside tank is connected with two phase separation pot; The oil phase outlet of two phase separation pot is connected with the vacuum still entrance, and the water outlet of two phase separation pot is connected with the electro-flotation system; The outlet of vacuum still extraction agent is connected with the solvent makeup tank, and the vacuum still crude exports are connected with the crude oil finished pot, and the solvent makeup tank is connected with the extraction agent entrance that is connected curtain formula extraction tower with many oars of single armed extraction equipment; The oily(waste)water outlet of sludge sump is connected with the electro-flotation system, and the dregs of fat outlet of electro-flotation system is connected with the entrance of stream curtain formula extraction tower; The water outlet of electro-flotation system is connected with water treatment system, and the solid phase outlet of stream curtain formula extraction tower is connected with the biological degradation system.
Sludge in Oilfields processing equipment for recycling described in the utility model:
One cover sludge pretreatment equipment, its core is vetivert rotary screen, is contained in ratchel and foreign material in the mud by this equipment rough segmentation.
One cover single armed many oars extraction equipment, its core is the many oars of single armed and extraction agent, the shear agitation effect by the many oars of single armed and extraction agent makes silt, crude oil solvent mixture and sewage three-phase settlement separate.It is equipped with settlement separation tank, solvent makeup tank and robot control system(RCS).
One cover is processed the stream curtain formula extraction equipment of shale oily sludge, the shale oily sludge is after many oars of single armed extracting system separates, because the close greasy filth of proportion and crude oil can't pass through gravity separation, only have by behind stream curtain formula extracting system and the extraction agent mixing, washing, make mud up to standard.
One cover crude separation, solvent reclaiming equipment, nucleus equipment is vacuum still, since from crude oil and extractant mixture after shale and chiltern separate, must valuable crude resources be separated with valuable extraction agent by vacuum distillation technique, crude oil is defeated outward as finished product.Solvent cycle is usefulness again, reduces running cost.Auxiliary facility has the integrated heating of solvent makeup tank, crude oil finished pot and distillation tower, cools off, vacuumizes facility and robot control system(RCS).Do not select the air distillation reason to have two: one so only select underpressure distillation, reduce the light constituent quantity of distillate that cut point reduces energy consumption, reduces crude oil; The 2nd, reduce the loss of solvent.
With the auxiliary material that contains biological inoculum with process after waste residue admix certain hour in proportion after, this waste residue is innoxious to reach national agricultural emission standard.
Sludge in Oilfields processing equipment for recycling described in the utility model.Silt particle oil-containing after this device is processed reach national stacking standard (＜3000mg/kg).
Description of drawings
Fig. 1 Sludge in Oilfields processing equipment for recycling schematic diagram.
Embodiment
Unit type lift GFL-1, vetivert rotary screen GFSS-1, many oars of single armed extraction equipment GFAT-1, three phase separation tank GFSD-1, stream curtain formula extraction tower GFFT-1, the GFEF-1 of electro-flotation system, vacuum still GFDT-1 patent equipment manufacturer all are Beijing Green Fei Deke skill Development Co., Ltd.
Sludge in Oilfields processing equipment for recycling described in the utility model comprises lift, vetivert rotary screen, many oars of single armed extraction equipment, separate and subside tank, two phase separation pot, stream curtain formula extraction tower, electro-flotation system, vacuum still, sludge sump, biological degradation system, solvent makeup tank and crude oil finished pot; Lift is positioned at the sludge sump top, is connected with vetivert rotary screen, and the outlet that vetivert rotary screen is positioned at the bottom is connected with the entrance of many oars of single armed extraction equipment; The outlet of many oars of single armed extraction equipment is connected with the separate and subside tank; The solid phase outlet of separate and subside tank is connected with the entrance of stream curtain formula extraction tower; The liquid-phase outlet of separate and subside tank is connected with two phase separation pot; The oil phase outlet of two phase separation pot is connected with the vacuum still entrance, and the water outlet of two phase separation pot is connected with the electro-flotation system; The outlet of vacuum still extraction agent is connected with the solvent makeup tank, and the vacuum still crude exports are connected with the crude oil finished pot, and the solvent makeup tank is connected with the extraction agent entrance that is connected curtain formula extraction tower with many oars of single armed extraction equipment; The oily(waste)water outlet of sludge sump is connected with the electro-flotation system, and the dregs of fat outlet of electro-flotation system is connected with the entrance of stream curtain formula extraction tower; The water outlet of electro-flotation system is connected with water treatment system, and the solid phase outlet of stream curtain formula extraction tower is connected with the biological degradation system.
Claims (1)
1. a Sludge in Oilfields processing equipment for recycling comprises lift, vetivert rotary screen, many oars of single armed extraction equipment, separate and subside tank, two phase separation pot, stream curtain formula extraction tower, electro-flotation system, vacuum still, sludge sump, biological degradation system, solvent makeup tank and crude oil finished pot; It is characterized in that: lift is positioned at the sludge sump top, is connected with vetivert rotary screen, and the outlet that vetivert rotary screen is positioned at the bottom is connected with the entrance of many oars of single armed extraction equipment; The outlet of many oars of single armed extraction equipment is connected with the separate and subside tank; The solid phase outlet of separate and subside tank is connected with the entrance of stream curtain formula extraction tower; The liquid-phase outlet of separate and subside tank is connected with two phase separation pot; The oil phase outlet of two phase separation pot is connected with the vacuum still entrance, and the water outlet of two phase separation pot is connected with the electro-flotation system; The outlet of vacuum still extraction agent is connected with the solvent makeup tank, and the vacuum still crude exports are connected with the crude oil finished pot, and the solvent makeup tank is connected with the extraction agent entrance that is connected curtain formula extraction tower with many oars of single armed extraction equipment; The oily(waste)water outlet of sludge sump is connected with the electro-flotation system, and the dregs of fat outlet of electro-flotation system is connected with the entrance of stream curtain formula extraction tower; The water outlet of electro-flotation system is connected with water treatment system, and the solid phase outlet of stream curtain formula extraction tower is connected with the biological degradation system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220476934.9U CN202898175U (en) | 2012-09-18 | 2012-09-18 | Oil field oily sludge resourceful treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220476934.9U CN202898175U (en) | 2012-09-18 | 2012-09-18 | Oil field oily sludge resourceful treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202898175U true CN202898175U (en) | 2013-04-24 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201220476934.9U Expired - Lifetime CN202898175U (en) | 2012-09-18 | 2012-09-18 | Oil field oily sludge resourceful treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202898175U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103626366A (en) * | 2013-12-19 | 2014-03-12 | 中国石油大学(华东) | Treatment method for recycling oil-field oily sludge |
| CN104891756A (en) * | 2015-06-03 | 2015-09-09 | 温州大学 | Oil sludge recovery device and method based on sufficient stirring |
| CN105417909A (en) * | 2015-12-30 | 2016-03-23 | 哈尔滨工业大学 | Electrochemical biological coupling deep treatment method for oily sludge |
| CN105733640A (en) * | 2016-03-16 | 2016-07-06 | 中国石油大学(华东) | Treatment method of waste oil-based drilling fluid |
| CN106830119A (en) * | 2017-02-24 | 2017-06-13 | 长江大学 | The magnetic absorption processing unit of oil-polluted water |
| CN113233725A (en) * | 2021-06-24 | 2021-08-10 | 陕西延长石油（集团）有限责任公司 | Device and method for flotation and extraction coupling treatment of oily sludge |
| CN115466028A (en) * | 2022-10-14 | 2022-12-13 | 李怡珠 | Method for treating oil field oil sludge |
-
2012
- 2012-09-18 CN CN201220476934.9U patent/CN202898175U/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103626366A (en) * | 2013-12-19 | 2014-03-12 | 中国石油大学(华东) | Treatment method for recycling oil-field oily sludge |
| CN103626366B (en) * | 2013-12-19 | 2015-04-29 | 中国石油大学(华东) | Treatment method for recycling oil-field oily sludge |
| CN104891756A (en) * | 2015-06-03 | 2015-09-09 | 温州大学 | Oil sludge recovery device and method based on sufficient stirring |
| CN105417909A (en) * | 2015-12-30 | 2016-03-23 | 哈尔滨工业大学 | Electrochemical biological coupling deep treatment method for oily sludge |
| CN105733640A (en) * | 2016-03-16 | 2016-07-06 | 中国石油大学(华东) | Treatment method of waste oil-based drilling fluid |
| CN106830119A (en) * | 2017-02-24 | 2017-06-13 | 长江大学 | The magnetic absorption processing unit of oil-polluted water |
| CN113233725A (en) * | 2021-06-24 | 2021-08-10 | 陕西延长石油（集团）有限责任公司 | Device and method for flotation and extraction coupling treatment of oily sludge |
| CN115466028A (en) * | 2022-10-14 | 2022-12-13 | 李怡珠 | Method for treating oil field oil sludge |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130424 |
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| CX01 | Expiry of patent term |