CN201648306U - Tar separating device - Google Patents

Tar separating device Download PDF

Info

Publication number
CN201648306U
CN201648306U CN2009202586888U CN200920258688U CN201648306U CN 201648306 U CN201648306 U CN 201648306U CN 2009202586888 U CN2009202586888 U CN 2009202586888U CN 200920258688 U CN200920258688 U CN 200920258688U CN 201648306 U CN201648306 U CN 201648306U
Authority
CN
China
Prior art keywords
tar
oil storage
storage tank
centrifugal separator
fractionating tower
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 - Lifetime
Application number
CN2009202586888U
Other languages
Chinese (zh)
Inventor
李志国
王红波
李卫光
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.)
Baoshun Technology Co., Ltd.
Original Assignee
HENAN BAOSHUO TAR CHEMICAL CO Ltd
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 HENAN BAOSHUO TAR CHEMICAL CO Ltd filed Critical HENAN BAOSHUO TAR CHEMICAL CO Ltd
Priority to CN2009202586888U priority Critical patent/CN201648306U/en
Application granted granted Critical
Publication of CN201648306U publication Critical patent/CN201648306U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Centrifugal Separators (AREA)

Abstract

The utility model discloses a tar separating device which comprises a fractionating tower. The fractionating tower is communicated with an oil storage tank through a pipeline; a centrifugal separator is arranged between the fractionating tower and the oil storage tank and respectively communicated with an oil residue collecting tank, a water collecting tank and the oil storage tank; and an oil storage groove is also arranged between the centrifugal separator and the fractionating tower. By adopting the technical scheme, the utility model has the following advantages that after raw tar is processed by the centrifugal separator, the deslagging and dewatering efficiency is high, and the product quality is improved, for example, the tar has high quality, less impurities, short separating time and high processing efficiency; and after the tar is processed by the centrifugal separator, the water and slag content is less, therefore, the high-purity tar is subjected to a subsequent process, so that the load of a tubular furnace in the subsequent process is reduced, coal gas is saved, and the failure rate of equipment in the subsequent process also can be reduced, thereby prolonging the maintenance time.

Description

The tar separation device
Technical field
The equipment of the utility model coal tar enterprise relates to a kind of equipment of separating tar specifically.
Background technology
The coal-tar middle oil separation natural method commonly used of coal tar chemical enterprise is separated at present, is about to crude oil and pours storage tank into, and through natural sedimentation layering in 10-28 hour, the upper strata was a water, and the middle level is a tar, and lower floor is the dregs of fat, and pipeline is connected on the middle level then, is delivered to subsequent processing.But there is following shortcoming in this structure: 1, tar stock processing back bits are many, moisture content big, influence amount of finish and quality product.2, increase back operation tube furnace load, saving coal gas, reduced the spoilage of tube furnace.
Summary of the invention
The purpose of this utility model just is to overcome above-mentioned deficiency a kind of tar separation device is provided.
The purpose of this utility model can be achieved through the following technical solutions:
A kind of tar separation device comprises separation column, and separation column is communicated with storage tank by pipeline, is provided with separating centrifuge between separation column and storage tank, and separating centrifuge is communicated with dregs of fat receiving tank, water collecting groove and storage tank respectively.
Above-mentioned tar separation device also is provided with oil storage vessel between separating centrifuge and separation column.
Adopt technique scheme, the utility model has following advantage: after using whizzer, raw tar takes off slag, dehydration rate height, improve the quality of products, as quality of coke tar, impurity is few, disengaging time is short, improve working (machining) efficiency, be both by the moisture dregginess of the tar behind the separating centrifuge for a short time, highly purified like this tar enters the postorder operation, reduce the load of tube furnace in the postorder operation, save coal gas, can also reduce the spoilage of equipment in the postorder operation, prolong the maintenance number of times.
Description of drawings
Accompanying drawing is the utility model structural representation.
Embodiment
A kind of as shown in drawings tar separation device, comprise separation column 1, separation column 1 is communicated with storage tank 3 by pipeline 2, is provided with separating centrifuge 4 between separation column 1 and storage tank 3, and separating centrifuge 4 is communicated with dregs of fat receiving tank 5, water collecting groove 6 and storage tank 3 respectively.
Preferred version of the present utility model is also to be provided with oil storage vessel 7 between separating centrifuge 4 and separation column 1, the raw material that comes out from separation column is in entering oil storage vessel, after the natural sedimentation layering, first isolating tar is obtained more highly purified tar by separating centrifuge.

Claims (2)

1. a tar separation device comprises separation column, and separation column is communicated with storage tank by pipeline, it is characterized in that: be provided with separating centrifuge between separation column and storage tank.
2. tar separation device according to claim 1 is characterized in that: also be provided with oil storage vessel between separating centrifuge and separation column.
CN2009202586888U 2009-12-01 2009-12-01 Tar separating device Expired - Lifetime CN201648306U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009202586888U CN201648306U (en) 2009-12-01 2009-12-01 Tar separating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009202586888U CN201648306U (en) 2009-12-01 2009-12-01 Tar separating device

Publications (1)

Publication Number Publication Date
CN201648306U true CN201648306U (en) 2010-11-24

Family

ID=43113535

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2009202586888U Expired - Lifetime CN201648306U (en) 2009-12-01 2009-12-01 Tar separating device

Country Status (1)

Country Link
CN (1) CN201648306U (en)

Similar Documents

Publication Publication Date Title
CN102284354B (en) Coarse slime separating process
EP1797236A4 (en) Method for separating lignin from a lignin containing liquid/slurry
CN104263397B (en) A kind of resinous shale wholegrain level sorting enrichment oil matrix technique
UA96268C2 (en) Methods for removal of carboxylic and/or phosphoric admixtures in plant for the production of silicon
CN101774879B (en) Method for simultaneously extracting high-purity beta-methylnaphthalene and indole from coal tar
CN107020201B (en) Thickener underflow coarse slime recovery system
CN110899001A (en) Two-stage flotation process for difficult-to-float coal slime
CN102774817A (en) Process for recovery and purification of hexagonal boron nitride in cubic boron nitride synthetic tailings
CN201648306U (en) Tar separating device
CN102274786A (en) Coal slime two-stage flotation process with granularity smaller than 0.5mm
CN106631682B (en) Device and method for separating water from 2-chloro-1, 2-tetrafluoropropane
MY176577A (en) Process for extracting carboxylic acids produced by anaerobic fermentation from fermentable biomass
CN101817527B (en) Method for refining and purifying electronic-grade silane in polysilicon production process
CN103466873A (en) Method for processing sewage with high-concentration phenol and ammonia
CN102896036A (en) Three-section four-product heavy media coal preparation process
CN103894277B (en) Main coal separation sludge-water secondary flotation technology for middings crushing and dissociation dense medium cyclone
WO2017191364A1 (en) Method and system
CN203159556U (en) System for preparing PTA/PET based on pyrolysis and gasification device
CN102311753B (en) Method for deep cut of crude oil
CN111467873B (en) Methyl siloxane dehydration and impurity removal process and equipment
CN205635422U (en) Device for separating isopropanol from water-containing acetone hydrogenation product
CN203853144U (en) Secondary floatation system of slime water primarily separated by heavy medium cyclone for crushing and dissociating middlings
CN207793117U (en) A kind of improved refining of crude phenol system
CN107573219A (en) A kind of improved refining of crude phenol system and method
CN102059174A (en) Cleaned coal dehydration process and equipment combination for realizing same

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee

Owner name: BAOSHUN TECHNOLOGY CO., LTD.

Free format text: FORMER NAME: HENAN BAOSHUO TAR CHEMICAL CO., LTD.

CP01 Change in the name or title of a patent holder

Address after: 455141, Henan County, Anyang Province copper Town Court Village

Patentee after: Baoshun Technology Co., Ltd.

Address before: 455141, Henan County, Anyang Province copper Town Court Village

Patentee before: Henan Baoshuo Tar Chemical Co., Ltd.

CX01 Expiry of patent term

Granted publication date: 20101124

CX01 Expiry of patent term