CN201701787U - Demister - Google Patents

Demister Download PDF

Info

Publication number
CN201701787U
CN201701787U CN2010202014218U CN201020201421U CN201701787U CN 201701787 U CN201701787 U CN 201701787U CN 2010202014218 U CN2010202014218 U CN 2010202014218U CN 201020201421 U CN201020201421 U CN 201020201421U CN 201701787 U CN201701787 U CN 201701787U
Authority
CN
China
Prior art keywords
demister
flange
shell
gas
reaction
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
CN2010202014218U
Other languages
Chinese (zh)
Inventor
张超
马晓丽
何晓芳
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN2010202014218U priority Critical patent/CN201701787U/en
Application granted granted Critical
Publication of CN201701787U publication Critical patent/CN201701787U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The utility model discloses a demister, belonging to chemical equipment and solving the defects that in the prior art, as ethyl acetate synthetization reaction is carried out by an etherification method, a rectifying tower body is easy to be corroded and is added with burden. The demister comprises a shell, wherein the top, the middle part and the bottom of the shell are respectively provided with a gas outlet, a synthesis gas inlet and a liquid outlet which are respectively provided with an upper flange, an intermediate flange and a lower flange; the inner upper part of the shell is provided with a whirling plate; and the whirling plate consists of a retaining cylinder, the inner side of the retaining cylinder is provided with a blade, and the outer side thereof is distributed with distribution rings. The demister is mainly used for gas and liquid separation during the process of ethyl acetate synthetization reaction with the method.

Description

Demister
Technical field
The utility model belongs to a kind of chemical production equipment, specifically, relates in particular to a kind of demister.
Background technology
In the reaction of esterification process synthesis for ethyl acetate, reacted gas enters rectifying column, reacted product is separated, owing to the big quantity of fluid of carrying under one's arms in the uprising gas that enters rectifying column, this part liquid for the reaction incomplete material, acid content is very high, enter rectifying column after, cause the tower body corrosion easily, and can increase the weight of the load of rectifying column.At present, also there is not a kind of equipment can effectively weaken the load that the burn into of the tower body of rectifying column is alleviated rectifying column.
Summary of the invention
When solving the reaction of esterification process synthesis for ethyl acetate in the prior art, the defective that is easy to cause the corrosion of rectifying column tower body and increases the weight of the rectifying column burden, the utility model provides a kind of demister.
The utility model is achieved through the following technical solutions:
A kind of demister comprises housing, and the top of housing, middle part and bottom are respectively equipped with gas vent, synthesis gas inlet and liquid outlet, is respectively equipped with upper flange, middle flange and lower flange on gas vent, synthesis gas inlet and the liquid outlet; The top of enclosure interior is provided with the eddy flow plate; Described eddy flow plate comprises the retaining tube, and retaining tube inboard is provided with blade, and the outside is provided with distribution rings.
Described distribution rings can be uniformly distributed in the retaining tube outside.
Compared with prior art, the beneficial effects of the utility model are: after reacted gas enters housing by middle flange, because the centrifugal action of eddy flow plate comes gas and fluid separation applications, thereby reach the purpose of gas-liquid separation, alleviated the load of later separation equipment; Liquid after being convenient to separate enters reaction system once more and participates in reaction, has improved the conversion ratio of reaction; Simple in structure, simple for production, convenient maintenance, maintenance.
Description of drawings
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the front view of eddy flow plate of the present utility model;
Fig. 3 is the vertical view of eddy flow plate of the present utility model.
The specific embodiment
The utility model is described in further detail below in conjunction with accompanying drawing:
Upper flange in the drawings, 1; 2, blade; 3, retaining tube; 4, distribution rings; 5, housing; 6, lower flange; 7, middle flange; 8, gas vent; 9, synthesis gas inlet; 10, liquid outlet.
A kind of demister comprises housing 5, and the top of housing 5, middle part and bottom are respectively equipped with gas vent 8, synthesis gas inlet 9 and liquid outlet 10, is respectively equipped with upper flange 1, middle flange 7 and lower flange 6 on gas vent 8, synthesis gas inlet 9 and the liquid outlet 10; The top of housing 5 inside is provided with the eddy flow plate; Described eddy flow plate comprises retaining tube 3, and retaining tube 3 inboards are provided with blade 2, and the outside is evenly distributed with distribution rings 4.
In use, reacted synthesis gas enters housing 5 inside by synthesis gas inlet 9, passes through the eddy flow plate then; At eddy flow plate place, because action of centrifugal force makes gas and fluid separation applications come, the gas after the separation is discharged through gas vent 8, and liquid is discharged through liquid outlet 10, thereby reaches the purpose of gas-liquid separation.

Claims (2)

1. a demister comprises housing, and the top of housing, middle part and bottom are respectively equipped with gas vent, synthesis gas inlet and liquid outlet, is respectively equipped with upper flange, middle flange and lower flange on gas vent, synthesis gas inlet and the liquid outlet; It is characterized in that: the top of enclosure interior is provided with the eddy flow plate; Described eddy flow plate comprises the retaining tube, and retaining tube inboard is provided with blade, and the outside is provided with distribution rings.
2. demister according to claim 1 is characterized in that: described distribution rings is uniformly distributed in the retaining tube outside.
CN2010202014218U 2010-05-18 2010-05-18 Demister Expired - Lifetime CN201701787U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010202014218U CN201701787U (en) 2010-05-18 2010-05-18 Demister

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010202014218U CN201701787U (en) 2010-05-18 2010-05-18 Demister

Publications (1)

Publication Number Publication Date
CN201701787U true CN201701787U (en) 2011-01-12

Family

ID=43438931

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010202014218U Expired - Lifetime CN201701787U (en) 2010-05-18 2010-05-18 Demister

Country Status (1)

Country Link
CN (1) CN201701787U (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103721442A (en) * 2012-10-12 2014-04-16 沈阳芯源微电子设备有限公司 Structure for removing bubbles in liquid
CN105413317A (en) * 2015-12-09 2016-03-23 深圳市瑞升华科技股份有限公司 Liquid spray foam remover applied to rectifying tower
CN105536300A (en) * 2016-01-31 2016-05-04 长沙今朝科技股份有限公司 Gas-liquid separation device, gas-liquid separation method and filling machine
CN106220500A (en) * 2016-08-17 2016-12-14 泰兴金江化学工业有限公司 A kind of ethyl acetate production energy-saving equipment
CN106478415A (en) * 2016-08-17 2017-03-08 泰兴金江化学工业有限公司 A kind of ethyl acetate energy-saving processing technique
KR101768466B1 (en) 2016-12-29 2017-08-23 정석엔지니어링 주식회사 Apparatus for removing odor using turbo blower

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103721442A (en) * 2012-10-12 2014-04-16 沈阳芯源微电子设备有限公司 Structure for removing bubbles in liquid
CN105413317A (en) * 2015-12-09 2016-03-23 深圳市瑞升华科技股份有限公司 Liquid spray foam remover applied to rectifying tower
CN105536300A (en) * 2016-01-31 2016-05-04 长沙今朝科技股份有限公司 Gas-liquid separation device, gas-liquid separation method and filling machine
CN106220500A (en) * 2016-08-17 2016-12-14 泰兴金江化学工业有限公司 A kind of ethyl acetate production energy-saving equipment
CN106478415A (en) * 2016-08-17 2017-03-08 泰兴金江化学工业有限公司 A kind of ethyl acetate energy-saving processing technique
CN106478415B (en) * 2016-08-17 2019-01-18 泰兴金江化学工业有限公司 A kind of ethyl acetate energy-saving processing technique
KR101768466B1 (en) 2016-12-29 2017-08-23 정석엔지니어링 주식회사 Apparatus for removing odor using turbo blower

Similar Documents

Publication Publication Date Title
CN201701787U (en) Demister
CN103007862A (en) Gas-liquid stirring reactor for synthesizing acrylic acid and ester through acetylene carbonylation method
CN202643806U (en) Leaching tank
CN202968431U (en) Composite tower for separating intermediate products dimethyl oxalate and methanol in industrial production of ethylene glycol
CN202490455U (en) Vacuum buffer tank
CN203971583U (en) A kind of Despumation device of acetate production use
CN202143807U (en) Foam destroyer used for producing acetate
CN202199146U (en) External circular reaction side-discharge rectification apparatus in composite structure
CN201551868U (en) Ammonium sulfate crystallizer
CN210012834U (en) Continuous esterification production device for waste oil
CN104474743B (en) A kind of device being continuously separated biodiesel and glycerine
CN203417535U (en) Acid mist sedimentation device
CN202785265U (en) Lifting device of grain stillage distillation cylinder
CN202555255U (en) Variable-diameter tower reactor capable of carrying out continuous reaction
CN104353329B (en) Methanol separator
CN202666662U (en) Waste gas absorption device
CN104084108B (en) A kind of esterification reaction tower
CN202942707U (en) Three-leg type jacket suction filter
CN203021485U (en) System for continuously producing ethyl butyrate
CN204219958U (en) Flue gas cleaner
CN212407125U (en) Fan guiding device
CN202909709U (en) Vacuum charging reaction kettle
CN202819488U (en) High-efficiency fermentation tank for yoghurt
CN203513651U (en) Biodiesel esterification reactor
CN202460204U (en) Gas and liquid separator for esterification

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CX01 Expiry of patent term

Granted publication date: 20110112

CX01 Expiry of patent term