CN103132935A - Staged vacuum drying treatment process and treatment device for oilfield drilling cuttings - Google Patents

Staged vacuum drying treatment process and treatment device for oilfield drilling cuttings Download PDF

Info

Publication number
CN103132935A
CN103132935A CN201310057482XA CN201310057482A CN103132935A CN 103132935 A CN103132935 A CN 103132935A CN 201310057482X A CN201310057482X A CN 201310057482XA CN 201310057482 A CN201310057482 A CN 201310057482A CN 103132935 A CN103132935 A CN 103132935A
Authority
CN
China
Prior art keywords
vacuum
temperature
drilling cuttings
vacuum desiccator
oil
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
Application number
CN201310057482XA
Other languages
Chinese (zh)
Other versions
CN103132935B (en
Inventor
王宗明
乔莎莎
谭宁宁
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
China University of Petroleum East China
Original Assignee
China University of Petroleum East China
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by China University of Petroleum East China filed Critical China University of Petroleum East China
Priority to CN201310057482.XA priority Critical patent/CN103132935B/en
Publication of CN103132935A publication Critical patent/CN103132935A/en
Application granted granted Critical
Publication of CN103132935B publication Critical patent/CN103132935B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Drying Of Solid Materials (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention relates to a staged vacuum drying treatment process and a treatment device for oilfield drilling cuttings. During auxiliary heating, the inside of a dryer is pumped to reach different levels of vacuum degrees by a vacuum set, water and diesel in the oilfield drilling cuttings are sequentially vaporized by staged vacuuming, vapor is liquefied by a condenser, the water containing a small amount of oil is recovered to a water storage tank, the diesel containing a small amount of water is recovered to an oil storage tank for reserve, the drilling cuttings are discharged after dried, and a heating system is automatically started or stopped as needed. By the aid of the drying treatment process and the drying treatment device, the oil-based drilling cuttings can be dried to such a degree that the water content is lower than 0.1% and the oil content is lower than 0.3%, and the drilling cuttings can be maximally reduced and directly discharged. The treatment device can respectively recover the diesel and the water by the aid of the same condenser under a staged vacuum condition, a huge fractionating tower is omitted, and the device is compact in structure, simple and convenient to operate, high in drilling cuttings treatment efficiency, fine in environmental performance and suitable for harmless treatment of the oil-based drilling cuttings on an open sea or deep sea drilling platform.

Description

Oil drilling drilling cuttings classification vacuum drying treatment technique and treating apparatus
Technical field
The present invention relates to oil drilling oil-contained drilling cuttings classification vacuum drying treatment technique and implement this technique treating apparatus used; belong to the oil field environment-protection field; the drying and other treatment that can be used for oil-contained drilling cuttings or oily sludge is particularly suitable for the harmless treatment of oil base drilling cuttings on the offshore boring island of off-lying sea or deep-sea zone.
Background technology
At present, oil base drilling fluid is widely used in drilling technology, and the oil that is used as continuous phase in the water-in-oil type drilling fluid is called base oil, and the base oil that the most generally uses is diesel oil (China's No. zero diesel oil commonly used).In oil-based drilling mud, diesel oil often surpasses 50% as the concentration by volume of additive, and water is evenly dispersed in diesel oil as necessary component, and its water content is generally 10~60%.The drilling cuttings that produces during drilling well may contain and surpass 7.5% oil, oil-contained drilling cuttings directly discharges, serious environment pollution will be caused, affect the water source of drinking water, affect soil and animal and plant growth, even directly jeopardize human health and life security, so the use of a series of relevant laws and regulations restriction oil base drilling fluids and the discharging of oil-contained drilling cuttings have been formulated in countries in the world.
The oil base drilling cuttings need to carry out strict processing, can not advanced treating during offshore drilling, pass through often preliminary treatment, and then transport land back and carry out again advanced treating.Drill cutting treatment method commonly used has drier to take off dry method, hot fractionating process, re-injection method, hot water washing etc. at present.After drier takes off dry process, the comprehensive oil-containing mass fraction of drilling cuttings higher than 4.8%, can not directly discharge; The drilling cuttings crude quality mark that hot fractionating process was processed is lower than 1%, but the method equipment is complicated, operating condition is harsh, mostly is professional treatment factory and uses; Landwaste re-injection method be with drilling cuttings by grinding and sieve and add appropriate seawater and thickening agent, select the injection of suitable stratum, this technical finesse is thorough, but cost is very high, often exceeds the ability to bear of drilling team.Displacement efficiency is very high for hot water washing (also claiming the thermal desorption method), but occupation area of equipment is large, and water consumption is large, and can cause secondary pollution.
Great development along with sea oil drilling and production; the oil pollution problem of ocean also grows in intensity; the drilling cuttings pretreatment often adopts centrifuge to carry out preliminary mummification on ocean platform; screen drum and rotary drum serious wear during the operation of this kind centrigugal swing dryer; application life is short, and it is not high enough to discharge the drilling cuttings mass dryness fraction, therefore at present in the urgent need to a kind of compact conformation, oil base drill chip innocent treating apparatus easy and simple to handle; can directly arrange the sea after making disposal of cuttings, satisfy the demand of deep-sea or off-lying sea drilling well.
Summary of the invention
The present invention is mainly the deficiency for existing drill cutting treatment method, a kind of compact conformation, oil base drill chip innocent treatment process easy and simple to handle is provided and implements the treating apparatus of this treatment process.The key issue that solves is to form at a lower temperature the classification vacuum, moisture and oil product are vaporized in different phase, only just water and oil content can not liquefied with condenser, play the effect of separation, harsh high temperature fractionation process and huge fractionating column have been avoided, disposal of cuttings is thorough, and is simple to operate, good environmental protection.
Technical scheme of the present invention is achieved in that by auxiliary heating system and improves the drilling cuttings temperature, and with the vacuum unit, dryer inside is extracted into respectively the vacuum of different stage, utilize the classification vacuum that the moisture in the oil drilling drilling cuttings and diesel oil are vaporized successively, again by condenser with steam liquefied, the water that will contain respectively a small amount of oil is recovered to water tank, it is standby that the diesel oil that will contain a small amount of water is recovered to oil storage tank, effluxes after the drilling cuttings drying; System reduces the temperature that effluxes drilling cuttings by heat-obtaining, and keeps the temperature of water tank, reclaims heat.
Oil drilling drilling cuttings classification vacuum drying treatment device, it is characterized in that: comprise vacuum desiccator, heating system, temperature pick up, pressure sensor, vacuum unit, deduster, condenser, water tank, oil storage tank, heat-obtaining system, heating system comprises controller and heater, vacuum desiccator is the closed container that an inside is provided with agitator, vacuum desiccator top has temperature-measuring port, pressure tap and extraction opening, and the heat-obtaining system comprises water pump, valve and heat exchanging pipe; The heater cartridge of heating system is in vacuum desiccator, containing the liquid drilling cuttings is loaded in vacuum desiccator, the extraction opening of vacuum desiccator is connected with the deduster entrance, the deduster outlet is connected with the entrance of vacuum unit, the vacuum machine set outlet is connected with condenser, condenser is connected with oil storage tank with water tank respectively by valve, and heat-obtaining system one end is loaded in the dry device of dry vacuum, and the other end is loaded in water tank; The temperature-measuring port mounting temperature sensor of vacuum desiccator, temperature pick up is connected with the controller of heating system; The pressure tap setting pressure sensor of vacuum desiccator, pressure sensor is connected with the controller of vacuum unit.
Use the technique that described treating apparatus carries out oil drilling drilling cuttings classification vacuum drying treatment, it is characterized in that: airtight after the wet drilling bit of filling less than 2/3 volume in vacuum desiccator, heating system is opened, and the drilling cuttings temperature is higher than 0 ℃, the temperature pick up feedback signal, heating system is closed; If environment temperature is higher than 0 ℃, heating system does not start; Vacuum unit starting, the vacuum pressure in vacuum desiccator be less than 400Pa, the pressure sensor feedback signal, reduce vacuum unit flow, vacuum pressure is greater than 500Pa, the pressure sensor feedback signal, increase vacuum unit flow, keeping the vacuum desiccator internal pressure is 400~500Pa; The steam with solid impurity from the extraction of vacuum desiccator extraction opening, first remove solid impurity through deduster, enter again the vacuum unit, the steam that the vacuum machine set outlet is discharged, liquefy through the condenser pressure charging temperature reduction, when the vacuum desiccator internal pressure was 400~500Pa, the water tank inlet valve was opened, and condensate liquid enters water tank; When vacuum unit flow less than 0.1m 3During/min, the water tank inlet valve cuts out, and first order processing finishes; The oil storage tank inlet valve is opened, and beginning is processed in the second level; Heating system is opened, and in vacuum desiccator, temperature is higher than 150 ℃, and heating system is closed, and the interior temperature of vacuum desiccator 1 is lower than 100 ℃, and heating system starts, and keeping the interior temperature of vacuum desiccator is 100~150 ℃; The vacuum unit starting, the pressure sensor feedback signal, the corresponding adjusting of vacuum unit flow guarantees that vacuum pressure is 10~50Pa; The oil storage tank inlet valve is opened, and condensate liquid enters oil storage tank 10; When vacuum unit 5 flows less than 0.1m 3During/min, the vacuum unit is closed, and second level processing finishes; The heat-obtaining system opens, and in vacuum desiccator, temperature reduces, in vacuum desiccator temperature lower than 50 ℃, heat-obtaining system closing, vacuum desiccator discharging.
Vacuum desiccator is a closed container, and inside is provided with an agitator and is used for stirring drilling cuttings, prevents the drilling cuttings caking, accelerates dry run.Vacuum desiccator top has temperature-measuring port, pressure tap and extraction opening, the temperature-measuring port mounting temperature sensor, and pressure tap setting pressure sensor, extraction opening is connected with vacuum unit entrance.The heater of heating system can be steam-heating pipe, can be also microwave applicator.
The vacuum unit can be the above vacuum pump series connection of two-stage or two-stage, to reach required vacuum requirement.
Deduster can be chosen sack cleaner with removing the granule foreign that carries in steam, or with the strainer of filter core.
The heat-obtaining system comprises water pump, valve and heat exchanging pipe, and an end is packed in vacuum desiccator, and an end is packed in water tank, both reduced the temperature that effluxes drilling cuttings, reclaimed again waste heat, and reclaimed heat and be stored in water tank, the temperature that can keep water storage, and the initial temperature of raising water for heating.
Condenser adopts water at low temperature as cooling medium, the heat when condensing with recovered steam, and owing to adopting vacuum fractionation dry, oil and water share a condenser, and by opening corresponding valve, Jiang Shui and oil are stored in water tank and oil storage tank respectively.
Compared with prior art, the invention has the advantages that: the oil drilling drilling cuttings classification vacuum drying treatment technique and the treating apparatus that provide are simple to operate, apparatus structure is compact, saved huge fractionating column, disposal of cuttings efficient is high, good environmental protection, the oil base drilling cuttings can be dried to moisture content less than 0.1%, oil content is less than 0.3%, to reach drilling cuttings minimizing and the purpose that directly effluxes to greatest extent.
Coming further to illustrate in detail technological process of the present invention and treating apparatus below in conjunction with accompanying drawing consists of.
Description of drawings
Fig. 1 is oil drilling drilling cuttings classification vacuum drying treatment technique and treating apparatus schematic diagram.
Wherein 1 is vacuum desiccator, the 2nd, and heating system, the 3rd, temperature pick up, the 4th, pressure sensor, the 5th, vacuum unit, the 6th, deduster, the 7th, condenser, the 8th, oil storage tank inlet valve, the 9th, water tank inlet valve, the 10th, oil storage tank, the 11st, water tank, 12 heat-obtaining systems, the 1.1st, vacuum desiccator extraction opening, the 1.2nd, pressure tap, 1.3 be temperature-measuring port, 2.1 be heater, the 2.2nd, heating controller, the 5.1st, vacuum unit entrance, 5.2 be the vacuum machine set outlet, 5.3 be the vacuum machine group controller, the 6.1st, deduster material inlet, 6.2 deduster gas outlets.
The specific embodiment
Embodiment is as follows:
With reference to Fig. 1, temperature-measuring port 1.3 mounting temperature sensors 3 of vacuum desiccator 1, temperature pick up 3 is connected with heating controller 2.2, temperature pick up 3 signal feedback heating systems 2; The pressure tap 1.2 setting pressure sensors 4 of vacuum desiccator 1, pressure sensor 4 is connected with vacuum machine group controller 5.3, pressure sensor 4 signal feedback vacuum units 5; The heater 2.1 of heating system 2 is loaded in vacuum desiccator 1, vacuum desiccator extraction opening 1.1 is connected with the deduster material inlet 6.1 of deduster 6, deduster gas outlet 6.2 is connected with vacuum unit entrance 5.1, vacuum machine set outlet 5.2 is connected with condenser 7, condenser 7 is connected with the water tank inlet valve to be connected with water tank with oil storage tank 10 respectively by oil storage tank inlet valve 8 and is connected, heat-obtaining system 12 1 ends are loaded in vacuum desiccator 1, and the other end is loaded in water tank 11.
This embodiment is for the wet drilling bit that contains water and diesel oil, the main component of diesel oil is that C16 is to n-alkane, monocyclic naphthenes and the mononuclear aromatics of C20, the saturated vapour pressure of 60 ℃ of lower n-eicosanes is less than 0.1Pa, the hexadecane saturated vapor pressure is about 7Pa, saturated vapour pressure under 100 ℃ of n-eicosanes is less than 19Pa, the saturated vapour pressure of n-eicosane under 150 ℃ is 100Pa, and 0 ℃ of lower water saturation vapour pressure is greater than 600Pa.
Airtight after the wet drilling bit of the interior filling of vacuum desiccator 1 less than 2/3 volume, heating system 2 is opened, and the drilling cuttings temperature is higher than 0 ℃, temperature pick up 3 feedback signals, and heating system 2 is closed; If environment temperature is higher than 0 ℃, heating system 2 does not start.Vacuum unit 5 starts, and the vacuum pressure in vacuum desiccator 1 is 400Pa, pressure sensor 4 feedback signals, reduce vacuum unit 5 flows, vacuum pressure is greater than 500Pa, pressure sensor 4 feedback signals, increase vacuum unit 5 flows, keeping vacuum desiccator 1 internal pressure is 400~500Pa.The steam with solid impurity from 1.1 extractions of vacuum desiccator extraction opening, first remove solid impurity through deduster 6, enter again vacuum unit 5, the steam that vacuum machine set outlet 5.2 is discharged, liquefy through condenser 7 pressure charging temperature reductions, when vacuum desiccator 1 internal pressure was 400~500Pa, water tank inlet valve 9 was opened, and condensate liquid enters water tank 11.When vacuum unit 5 flows less than 0.1m 3During/min, water tank inlet valve 9 cuts out, and first order processing finishes.Oil storage tank inlet valve 8 is opened, and beginning is processed in the second level.Heating system 2 is opened, and the interior temperature of vacuum desiccator 1 is higher than 150 ℃, and heating system 2 is closed, and the interior temperature of vacuum desiccator 1 is lower than 100 ℃, and heating system 2 starts, and keeping the interior temperature of vacuum desiccator 1 is 100~150 ℃.Vacuum unit 5 starts, pressure sensor 4 feedback signals, and the 5 corresponding adjustings of flow of vacuum unit guarantee that vacuum pressure is 10~50Pa.Oil storage tank inlet valve 8 is opened, and condensate liquid enters oil storage tank 10.When vacuum unit 5 flows less than 0.1m 3During/min, vacuum unit 5 is closed, and second level processing finishes.Heat-obtaining system 12 opens, and the interior temperature of vacuum desiccator 1 reduces, and the interior temperature of vacuum desiccator 1 is lower than 50 ℃, and heat-obtaining system 12 closes, vacuum desiccator 1 discharging.A plurality of work periods are carried out in so intermittently operated, and the disposal of cuttings amount is greater than 10m 3/ h satisfies the online requirement of processing of drilling cuttings fully.
The above is the embodiment commonly used of this invention, and according to the difference of material handling character, any those skilled in the art can set different operating temperatures and operation vacuum level according to the technology contents of above-mentioned announcement, realize other embodiment of equivalence.

Claims (3)

1. oil drilling drilling cuttings classification vacuum drying treatment device, it is characterized in that: comprise vacuum desiccator, heating system, temperature pick up, pressure sensor, vacuum unit, deduster, condenser, water tank, oil storage tank, heat-obtaining system, heating system comprises controller and heater, vacuum desiccator is the closed container that an inside is provided with agitator, vacuum desiccator top has temperature-measuring port, pressure tap and extraction opening, and the heat-obtaining system comprises water pump, valve and heat exchanging pipe;
The heater cartridge of heating system is in vacuum desiccator, containing the liquid drilling cuttings is loaded in vacuum desiccator, the extraction opening of vacuum desiccator is connected with the deduster entrance, the deduster outlet is connected with the entrance of vacuum unit, the vacuum machine set outlet is connected with condenser, condenser is connected with oil storage tank with water tank respectively by valve, and heat-obtaining system one end is loaded in the dry device of dry vacuum, and the other end is loaded in water tank; The temperature-measuring port mounting temperature sensor of vacuum desiccator, temperature pick up is connected with the controller of heating system; The pressure tap setting pressure sensor of vacuum desiccator, pressure sensor is connected with the controller of vacuum unit.
2. treating apparatus as claimed in claim 1, it is characterized in that: the heater of described heating system is steam-heating pipe or microwave applicator.
3. use the technique that treating apparatus as claimed in claim 1 carries out oil drilling drilling cuttings classification vacuum drying treatment, it is characterized in that:
Airtight after the wet drilling bit of filling less than 2/3 volume in vacuum desiccator, heating system is opened, and the drilling cuttings temperature is higher than 0 ℃, the temperature pick up feedback signal, and heating system is closed; If environment temperature is higher than 0 ℃, heating system does not start;
Vacuum unit starting, the vacuum pressure in vacuum desiccator be less than 400Pa, the pressure sensor feedback signal, reduce vacuum unit flow, vacuum pressure is greater than 500Pa, the pressure sensor feedback signal, increase vacuum unit flow, keeping the vacuum desiccator internal pressure is 400~500Pa; The steam with solid impurity from the extraction of vacuum desiccator extraction opening, first remove solid impurity through deduster, enter again the vacuum unit, the steam that the vacuum machine set outlet is discharged, liquefy through the condenser pressure charging temperature reduction, when the vacuum desiccator internal pressure was 400~500Pa, the water tank inlet valve was opened, and condensate liquid enters water tank; When vacuum unit flow less than 0.1m 3During/min, the water tank inlet valve cuts out, and first order processing finishes;
The oil storage tank inlet valve is opened, and beginning is processed in the second level; Heating system is opened, and in vacuum desiccator, temperature is higher than 150 ℃, and heating system is closed, and the interior temperature of vacuum desiccator 1 is lower than 100 ℃, and heating system starts, and keeping the interior temperature of vacuum desiccator is 100~150 ℃; The vacuum unit starting, the pressure sensor feedback signal, the corresponding adjusting of vacuum unit flow guarantees that vacuum pressure is 10~50Pa; The oil storage tank inlet valve is opened, and condensate liquid enters oil storage tank 10; When vacuum unit 5 flows less than 0.1m 3During/min, the vacuum unit is closed, and second level processing finishes; The heat-obtaining system opens, and in vacuum desiccator, temperature reduces, in vacuum desiccator temperature lower than 50 ℃, heat-obtaining system closing, vacuum desiccator discharging.
CN201310057482.XA 2013-02-23 2013-02-23 Oil drilling drilling cuttings classification vacuum drying treatment technique and treating apparatus Expired - Fee Related CN103132935B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310057482.XA CN103132935B (en) 2013-02-23 2013-02-23 Oil drilling drilling cuttings classification vacuum drying treatment technique and treating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310057482.XA CN103132935B (en) 2013-02-23 2013-02-23 Oil drilling drilling cuttings classification vacuum drying treatment technique and treating apparatus

Publications (2)

Publication Number Publication Date
CN103132935A true CN103132935A (en) 2013-06-05
CN103132935B CN103132935B (en) 2015-07-29

Family

ID=48493320

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310057482.XA Expired - Fee Related CN103132935B (en) 2013-02-23 2013-02-23 Oil drilling drilling cuttings classification vacuum drying treatment technique and treating apparatus

Country Status (1)

Country Link
CN (1) CN103132935B (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014171839A1 (en) * 2013-04-19 2014-10-23 Trond Melhus Method and system for separation of oil and water from drilling mud
CN106219938A (en) * 2016-08-24 2016-12-14 李天舒 A kind of greasy filth or the processing method of mud
CN110201984A (en) * 2019-06-24 2019-09-06 中国石油集团川庆钻探工程有限公司工程技术研究院 A kind of oil-containing article microwave goes oil recovery apparatus and its application method
CN111577176A (en) * 2020-06-08 2020-08-25 浙江铂沣环保科技有限公司 Offshore oil and gas platform oil-based drilling fluid drilling cuttings while-drilling treatment system
CN113404451A (en) * 2021-02-04 2021-09-17 中国石油大学(北京) Method for rock debris reinjection layer selection based on logging information

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4747961A (en) * 1986-12-19 1988-05-31 Atlantic Richfield Company Method and system for treating drill cutting slurries and the like
US20090120846A1 (en) * 2005-11-16 2009-05-14 George Alexander Burnett Shale shakers with cartridge screen assemblies
CN101506464A (en) * 2006-10-04 2009-08-12 国民油井华高有限合伙公司 Method and apparatus for preparing drill cuttings for reinjection into a well
CN102187051A (en) * 2008-10-29 2011-09-14 丹尼尔·盖·波默洛 System and method for drying drill cuttings

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4747961A (en) * 1986-12-19 1988-05-31 Atlantic Richfield Company Method and system for treating drill cutting slurries and the like
US20090120846A1 (en) * 2005-11-16 2009-05-14 George Alexander Burnett Shale shakers with cartridge screen assemblies
CN101506464A (en) * 2006-10-04 2009-08-12 国民油井华高有限合伙公司 Method and apparatus for preparing drill cuttings for reinjection into a well
CN102187051A (en) * 2008-10-29 2011-09-14 丹尼尔·盖·波默洛 System and method for drying drill cuttings

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
张春雪等: "《油田钻井钻屑在线干化技术浅析》", 《石油矿场机械》 *
易绍金等: "《海上钻井含油钻屑处理技术》", 《中国海上油气(工程)》 *

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014171839A1 (en) * 2013-04-19 2014-10-23 Trond Melhus Method and system for separation of oil and water from drilling mud
CN106219938A (en) * 2016-08-24 2016-12-14 李天舒 A kind of greasy filth or the processing method of mud
CN106219938B (en) * 2016-08-24 2019-05-03 李天舒 A kind of processing method of greasy filth or sludge
CN110201984A (en) * 2019-06-24 2019-09-06 中国石油集团川庆钻探工程有限公司工程技术研究院 A kind of oil-containing article microwave goes oil recovery apparatus and its application method
CN110201984B (en) * 2019-06-24 2024-01-26 中国石油天然气集团有限公司 Microwave deoiling recovery device for oil-containing article and use method thereof
CN111577176A (en) * 2020-06-08 2020-08-25 浙江铂沣环保科技有限公司 Offshore oil and gas platform oil-based drilling fluid drilling cuttings while-drilling treatment system
CN113404451A (en) * 2021-02-04 2021-09-17 中国石油大学(北京) Method for rock debris reinjection layer selection based on logging information
CN113404451B (en) * 2021-02-04 2022-08-02 中国石油大学(北京) Method for rock debris reinjection layer selection based on logging information

Also Published As

Publication number Publication date
CN103132935B (en) 2015-07-29

Similar Documents

Publication Publication Date Title
CN103132935B (en) Oil drilling drilling cuttings classification vacuum drying treatment technique and treating apparatus
NO165576B (en) PROCEDURE FOR THE REMOVAL OF ORGANIC POLLUTIONS FROM PARTICULAR SOLIDS AND APPARATUS FOR IMPLEMENTATION OF THE PROCEDURE.
CN202898176U (en) Resourceful treatment device for sandy oil-containing sludge
CN204571890U (en) Discarded oil-base mud is with brill treating apparatus
CN111943464B (en) Method and system for treating perennial polluted sludge, waste residues or oil sand in natural oil deposit containing oil and water deeply
CN104046375A (en) Microwave-assisted supercritical CO2 extraction system and microwave-assisted supercritical CO2 extraction method for crude oil in oil sand
CN110395857A (en) The method and apparatus for handling oil-containing hydrous matter
CN101121571B (en) Method for treating well drilling waste liquid by diesel engine tail gas
CN103396830B (en) Device and method for dehydrating heavy sump oil
CN105921489A (en) Animal harmless treatment equipment and method
FI75360B (en) SAETT ATT AVVATTNA EN KAKA AV BIOMASS.
CN206553370U (en) A kind of sludge combined treatment device
CN101269380B (en) Method for removing oil-containing drill cuttings and oil component in oil polluted soil
CN106915891A (en) A kind of oil plant oily sludge is innoxious and processing method of resource
CN201648205U (en) Oil field oil sludge drying treatment combined device
CN205974231U (en) Oil plant contains oil sludge mummification and tail gas treatment integration processing system
CN205762913U (en) Animal innocent treatment equipment
CN111617562B (en) Oil-based drilling cutting thermal desorption volatile separation and collection system and process
CN212293437U (en) Oil-containing solid oil washing system
CN204369814U (en) Oil field dehydration oil removal plant
CN207987008U (en) A kind of mud pretreatment unit for dredger
CN207760285U (en) A kind of oil field dehydration degreasing unit
CN214192907U (en) Oily solid waste treatment device
CN218642684U (en) Oil-based rock debris extraction and oil extraction system
CN219098952U (en) Mud does not fall to ground pressure filtration equipment

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20150729

Termination date: 20160223