Nothing Special   »   [go: up one dir, main page]

CN2504256Y - Combined degreaser - Google Patents

Combined degreaser Download PDF

Info

Publication number
CN2504256Y
CN2504256Y CN 01208713 CN01208713U CN2504256Y CN 2504256 Y CN2504256 Y CN 2504256Y CN 01208713 CN01208713 CN 01208713 CN 01208713 U CN01208713 U CN 01208713U CN 2504256 Y CN2504256 Y CN 2504256Y
Authority
CN
China
Prior art keywords
oil
hydroecium
horizontal
container
less
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.)
Expired - Fee Related
Application number
CN 01208713
Other languages
Chinese (zh)
Inventor
黄松
潘峰
孙河生
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.)
HUAYOU HUIBOPU SCIENCE AND TECHNOLOGY Co Ltd BEIJING
Original Assignee
HUAYOU HUIBOPU SCIENCE AND TECHNOLOGY Co Ltd BEIJING
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 HUAYOU HUIBOPU SCIENCE AND TECHNOLOGY Co Ltd BEIJING filed Critical HUAYOU HUIBOPU SCIENCE AND TECHNOLOGY Co Ltd BEIJING
Priority to CN 01208713 priority Critical patent/CN2504256Y/en
Application granted granted Critical
Publication of CN2504256Y publication Critical patent/CN2504256Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Cyclones (AREA)
  • Removal Of Floating Material (AREA)

Abstract

A composite oil remover is a horizontal cylindrical container which reduces the oil content in sewage to less than 50mg/L from less than 1000mg/L. The oil remover consists of a horizontal steel-made cylindrical contained and a vortex separator arranged on the top of the container. The interior of the cylinder body is provided with two stages of lipophilic coalescence fillers and a set of slant boards. Coming water enters the vortex separator first to remove the majority of the contained oil, and then enters the cylindrical container to remove the residual oil in the oil-containing sewage after successively passing through each filler stage. Flocculants are thrown in at the outlet of the vortex separator with a dosage of less than or equal to 100mg/L. The detailed structure is shown in the attached drawing.

Description

The combined oil removing device
The utility model relates to a kind of oil field oily(waste)water oil eliminator, is applicable to that handling oil water-mass density difference is greater than 0.05g/cm 3Oily(waste)water.
The widely used oily(waste)water oleaginousness that makes has three kinds by the method that 1000mg/L reduces to below the 50mg/L on the oil field at present, and the one, hydrocyclone oil removing, the 2nd, big jar oil removing, the 3rd, swash plate oil removing.Though hydrocyclone oil removing treatment capacity is bigger, pressure reduction is bigger, and general pressure drop is greater than 0.2Mpa; Though the two kinds of deoiling method pressure drops in back are less, but consumption of chemical agent is 200~400mg/L nearly, for addressing this problem, common way is that branch is handled oily(waste)water for several sections, though technical indicator can reach requirement, consumption of chemical agent also can be reduced to about 100mg/L, has the technical process complexity, construction investment is higher, the problem that the maintenance management workload is bigger.
The purpose of this utility model is that a kind of improved combined oil removing device will be provided, and it can make sewage with oil be reduced to below the 50mg/L by 1000mg/L, and pressure drop only is 0.1Mpa, can also make consumption of chemical agent be lower than 100mg/L.
The purpose of this utility model is achieved in that the combined oil removing device is made up of a horizontal steel cylindrical vessel and a vertical swirler, and swirler utilizes the pressure drop of 0.1Mpa that sewage with oil is reduced to about 100mg/L by 1000mg/L; The oil eliminator main part makes sewage with oil be reduced to below the 50mg/L by 100mg/L in 15 minutes time of oily(waste)water stop.
The utility model suitably reduces the length of cyclone pipe small cone section, increases the internal diameter of small cone section, and pressure drop is controlled in the 0.1Mpa, and oil-containing is reduced to below the 100mg/L by 1000mg/L; The coalescent pack of secondary lipophilic is set in the oil eliminator main body and one group of swash plate is used to make sewage with oil to reduce to below the 50mg/L from 100mg/L, the chemical agent spin current device bottom of playing throwing out adds in the low oily(waste)water, rather than chemical agent joins oil-containing and reaches in the sewage of 1000mg/L as common sedimentation removes oil tank, therefore can reduce the consumption of chemical agent significantly.
The concrete structure of utility model is provided by Fig. 1.
Describe the details and the working process of the combined oil removing device that the utility model proposes in detail below in conjunction with Fig. 1.
The sewage of oil-containing 1000mg/L enters swirler (8) from inlet (1), and tangentially enter swirler, the effusive oil of swirler enters oil header through communicating pipe (7), the sewage that oil-containing is lower than 100mg/L enters horizontal container (16) through aqueduct (12), sewage is after entering swash plate group (11) oil removing after the firsts and seconds lipophilic coalescent pack (9) (10), enter hydroecium (13) through aqueduct (6), flow out oil eliminator through water outlet (4).The isolating oil of oil eliminator flows into grease chamber (14) with the isolated oil of swirler and flows out oil eliminator through oil export (5).Flocculation agent adds from dosing mouth (2), and fluid level transmitter mouth (3) is arranged on the hydroecium middle part.Aqueduct (6) upper end that is provided with in the hydroecium (13) is equipped with water-oil interface setter (15), by the liquid level difference of its adjustable fuel-economizing hydroecium, thereby guarantees the stable of the interior water-oil interface of horizontal container, makes oily water separation reach design objective.

Claims (2)

1, a kind of horizontal oil eliminator is made up of steel Horizontal Cylindrical Tank and a degreaser cyclone installing above, it is characterized in that the oil outlet pipe of the isolated oil of swirler by top enters the oil trap in the horizontal container; Be provided with the coalescent pack of secondary lipophilic and one group of swash plate in the horizontal container; Be provided with grease chamber and hydroecium in the horizontal container, the grease chamber links to each other with the aqueduct of hydroecium by the bottom, is provided with liquor-level regulator in the hydroecium.
2, oil eliminator according to claim 1 is characterized in that the water-oil interface setter system in the hydroecium constitutes by one section moving casing of increase and corresponding regulating mechanism on aqueduct.
CN 01208713 2001-03-04 2001-03-04 Combined degreaser Expired - Fee Related CN2504256Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 01208713 CN2504256Y (en) 2001-03-04 2001-03-04 Combined degreaser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 01208713 CN2504256Y (en) 2001-03-04 2001-03-04 Combined degreaser

Publications (1)

Publication Number Publication Date
CN2504256Y true CN2504256Y (en) 2002-08-07

Family

ID=33628783

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 01208713 Expired - Fee Related CN2504256Y (en) 2001-03-04 2001-03-04 Combined degreaser

Country Status (1)

Country Link
CN (1) CN2504256Y (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101559292B (en) * 2009-05-12 2011-04-20 上海西恩化工设备有限公司 Oil removing technique by filtration method
CN103043747A (en) * 2013-01-09 2013-04-17 中国天辰工程有限公司 Oil-water separator
CN106186387A (en) * 2015-04-29 2016-12-07 中国石油化工股份有限公司 A kind of separation equipment and method for separating and processing
CN107381851A (en) * 2017-08-04 2017-11-24 上海米素环保科技有限公司 A kind of production separator and its separation method for offshore gas field platform production water process
CN107381914A (en) * 2017-08-04 2017-11-24 华东理工大学 A kind of offshore gas field platform production method for treating water and its device
CN109553241A (en) * 2017-09-27 2019-04-02 中国石油化工股份有限公司 A kind of oil-contained waste water treatment device and method

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101559292B (en) * 2009-05-12 2011-04-20 上海西恩化工设备有限公司 Oil removing technique by filtration method
CN103043747A (en) * 2013-01-09 2013-04-17 中国天辰工程有限公司 Oil-water separator
CN103043747B (en) * 2013-01-09 2014-09-24 中国天辰工程有限公司 Oil-water separator
CN106186387A (en) * 2015-04-29 2016-12-07 中国石油化工股份有限公司 A kind of separation equipment and method for separating and processing
CN106186387B (en) * 2015-04-29 2019-06-18 中国石油化工股份有限公司 A kind of separation equipment and method for separating and processing
CN107381851A (en) * 2017-08-04 2017-11-24 上海米素环保科技有限公司 A kind of production separator and its separation method for offshore gas field platform production water process
CN107381914A (en) * 2017-08-04 2017-11-24 华东理工大学 A kind of offshore gas field platform production method for treating water and its device
WO2019024915A1 (en) * 2017-08-04 2019-02-07 华东理工大学 Offshore gas field platform produced water treatment method and device
CN110759566A (en) * 2017-08-04 2020-02-07 华东理工大学 Production water treatment method for offshore gas field platform
CN110759566B (en) * 2017-08-04 2022-11-11 华东理工大学 Production water treatment method for offshore gas field platform
CN109553241A (en) * 2017-09-27 2019-04-02 中国石油化工股份有限公司 A kind of oil-contained waste water treatment device and method
CN109553241B (en) * 2017-09-27 2021-10-29 中国石油化工股份有限公司 Oily sewage treatment device and method

Similar Documents

Publication Publication Date Title
CN201217639Y (en) Integrated waste water treatment device
CN100579917C (en) Three-phase cyclone separator and cleaning treatment system for oil-containing water
CN101094812A (en) Wastewater treatment plant
CN202343009U (en) Kitchen oil and water separation device
CN102786167A (en) Laboratory wastewater treating device
CN201333428Y (en) Oil-removing sand-removing separator
CN204265551U (en) A kind of cyclone air-flotation tripping device of tar ammonia
CN2504256Y (en) Combined degreaser
CN208900092U (en) A kind of online eddy flow is set except being fixedly mounted with
CN110668570B (en) High-efficiency granular sludge anaerobic tower reactor
CN210001675U (en) Oil-water separation system
CN201686526U (en) Emergency oil pool
CN201882993U (en) Oily sewage settling treatment device
CN111573871A (en) Closed oily sewage treatment device and process
CN207468254U (en) Tank in a kind of tank
CN202968270U (en) Water treatment device of oil water separator
CN207175535U (en) A kind of separator for oily water
CN210559511U (en) Oily sewage pure physical water quality modification system
CN212334813U (en) Closed oily sewage treatment plant
CN204996173U (en) Containment structure of thickened sludge hydroextractor
CN212327480U (en) Tar ammonia water separator
CN209307464U (en) The device of oil slick in earth solution is removed in Rare-Earth Extraction Process
CN208471608U (en) A kind of cyclone air-flotation combination unit
CN2560410Y (en) Cyclone hydraulic separating, automatic tall-oil collecting and discharging combination apparatus
RU2567309C1 (en) Surge-vessel - separator

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee