CN216522597U - Auxiliary temperature control device for vacuum deacidification of chlorinated plasticizer - Google Patents

Auxiliary temperature control device for vacuum deacidification of chlorinated plasticizer Download PDF

Info

Publication number
CN216522597U
CN216522597U CN202122919312.0U CN202122919312U CN216522597U CN 216522597 U CN216522597 U CN 216522597U CN 202122919312 U CN202122919312 U CN 202122919312U CN 216522597 U CN216522597 U CN 216522597U
Authority
CN
China
Prior art keywords
cooling water
circulating pump
cooler
acid absorption
pipeline
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.)
Active
Application number
CN202122919312.0U
Other languages
Chinese (zh)
Inventor
叶活动
张津
陈芎严
陈志锋
郑茂书
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.)
FUJIAN ZHISHANG BIOMASS MATERIALS CO LTD
Original Assignee
FUJIAN ZHISHANG BIOMASS MATERIALS 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 FUJIAN ZHISHANG BIOMASS MATERIALS CO LTD filed Critical FUJIAN ZHISHANG BIOMASS MATERIALS CO LTD
Priority to CN202122919312.0U priority Critical patent/CN216522597U/en
Application granted granted Critical
Publication of CN216522597U publication Critical patent/CN216522597U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

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

Abstract

The utility model discloses a vacuum deacidification auxiliary temperature control device for chlorinated plasticizers, which comprises a cooling water circulating pump 1, a cooling water pool 2, a cooler 3, an absorption tower 4, an acid absorption tank 5 and an acid absorption circulating pump 6, wherein the cooling water pool is communicated with the cooling water circulating pump; an inlet pipeline of the cooling water circulating pump 1 is connected with a water outlet of the cooling water pool 2, an outlet pipeline of the cooling water circulating pump 1 is connected with a cooling water inlet of the cooler 3, and a cooling water outlet of the cooler 3 is connected back to the cooling water pool 2 through a pipeline; an inlet pipeline of the acid absorption circulating pump 6 is connected with a discharge hole of the acid absorption tank 5, an outlet pipeline of the acid absorption circulating pump 6 is connected with a feed hole of the absorption tower 4, a discharge hole of the absorption tower 4 is connected with a feed hole of the cooler 3, and a discharge hole of the cooler 3 is connected with a feed hole of the acid absorption tank 5. The vacuum deacidification method has the advantages of less alkali liquor consumption and low production cost.

Description

Auxiliary temperature control device for vacuum deacidification of chlorinated plasticizer
Technical Field
The utility model relates to the technical field of production devices of bio-ester plasticizers of organic chemical products, in particular to an auxiliary temperature control device for vacuum deacidification of chlorinated plasticizers.
Background
In the vacuum deacidification process during the production of chlorinated plasticizer, hydrogen chloride and water are converted into hydrochloric acid in an absorption tower, but the hydrogen chloride is large in amount and small in water amount compared with hydrogen chloride, the water temperature can be rapidly increased by heat emitted in the absorption process, the hydrogen chloride is absorbed unfavorably due to overhigh temperature, part of the hydrogen chloride cannot be absorbed, and is finally neutralized by alkali in a tail gas system, so that the alkali liquor consumption is increased, and the production cost is increased.
Disclosure of Invention
The utility model aims to provide a chlorinated plasticizer vacuum deacidification auxiliary temperature control device which is low in vacuum deacidification alkali liquor consumption and low in production cost.
In order to realize the purpose, the chlorinated plasticizer vacuum deacidification auxiliary temperature control device comprises a cooling water circulating pump 1, a cooling water pool 2, a cooler 3, an absorption tower 4, an acid absorption tank 5 and an acid absorption circulating pump 6; an inlet pipeline of the cooling water circulating pump 1 is connected with a water outlet of the cooling water pool 2, an outlet pipeline of the cooling water circulating pump 1 is connected with a cooling water inlet of the cooler 3, and a cooling water outlet of the cooler 3 is connected back to the cooling water pool 2 by a pipeline; the inlet pipeline of the acid absorption circulating pump 6 is connected with the discharge port of the acid absorption tank 5, the outlet pipeline of the acid absorption circulating pump 6 is connected with the feed port of the absorption tower 4, the discharge port of the absorption tower 4 is connected with the feed port of the cooler 3, and the discharge port of the cooler 3 is connected with the feed port of the acid absorption tank 5.
The chlorinated plasticizer vacuum deacidification auxiliary temperature control device with the structure has the following technical characteristics and beneficial effects: firstly, the chlorinated plasticizer vacuum deacidification auxiliary temperature control device with the structure can better control the acid temperature in the deacidification process of the chlorinated plasticizer, prevent partial hydrogen chloride from being completely absorbed and neutralized by alkali in a tail gas system due to overhigh temperature, reduce alkali liquor consumption and reduce production cost; secondly, simple structure, low manufacturing and maintenance cost, convenient and reliable use.
Drawings
FIG. 1 is a schematic structural diagram of an auxiliary temperature control device for vacuum deacidification of chlorinated plasticizers in the present invention.
Reference numerals: the device comprises a cooling water circulating pump 1, a cooling water pool 2, a cooler 3, an absorption tower 4, an acid absorption tank 5 and an acid absorption circulating pump 6.
Detailed Description
The chlorinated plasticizer vacuum deacidification auxiliary temperature control device of the utility model is further explained in detail with the accompanying drawings and the specific embodiment.
As shown in fig. 1, the chlorinated plasticizer vacuum deacidification auxiliary temperature control device of the present invention comprises a cooling water circulating pump 1, a cooling water pool 2, a cooler 3, an absorption tower 4, an acid absorption tank 5, and an acid absorption circulating pump 6; an inlet pipeline of the cooling water circulating pump 1 is connected with a water outlet of the cooling water pool 2, an outlet pipeline of the cooling water circulating pump 1 is connected with a cooling water inlet of the cooler 3, and a cooling water outlet of the cooler 3 is connected back to the cooling water pool 2 by a pipeline; the inlet pipeline of the acid absorption circulating pump 6 is connected with the discharge port of the acid absorption tank 5, the outlet pipeline of the acid absorption circulating pump 6 is connected with the feed port of the absorption tower 4, the discharge port of the absorption tower 4 is connected with the feed port of the cooler 3, and the discharge port of the cooler 3 is connected with the feed port of the acid absorption tank 5.
During operation, the cooling water circulating pump 1 and the acid absorption circulating pump 6 are firstly started, the temperature of acid is increased in the acid absorption process, the acid is cooled by the cooler 3, and the cooled acid returns to the acid absorption tank 5.

Claims (1)

1. A chlorinated plasticizer vacuum deacidification auxiliary temperature control device is characterized in that: the device comprises a cooling water circulating pump (1), a cooling water pool (2), a cooler (3), an absorption tower (4), an acid absorption tank (5) and an acid absorption circulating pump (6); an inlet pipeline of the cooling water circulating pump (1) is connected with a water outlet of the cooling water pool (2), an outlet pipeline of the cooling water circulating pump (1) is connected with a cooling water inlet of the cooler (3), and a cooling water outlet of the cooler (3) is connected back to the cooling water pool (2) through a pipeline; the inlet pipeline of the acid absorption circulating pump (6) is connected with the discharge port of the acid absorption tank (5), the outlet pipeline of the acid absorption circulating pump (6) is connected with the feed port of the absorption tower (4), the discharge port of the absorption tower (4) is connected with the feed port of the cooler (3), and the discharge port of the cooler (3) is connected with the feed port of the acid absorption tank (5).
CN202122919312.0U 2021-11-25 2021-11-25 Auxiliary temperature control device for vacuum deacidification of chlorinated plasticizer Active CN216522597U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202122919312.0U CN216522597U (en) 2021-11-25 2021-11-25 Auxiliary temperature control device for vacuum deacidification of chlorinated plasticizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202122919312.0U CN216522597U (en) 2021-11-25 2021-11-25 Auxiliary temperature control device for vacuum deacidification of chlorinated plasticizer

Publications (1)

Publication Number Publication Date
CN216522597U true CN216522597U (en) 2022-05-13

Family

ID=81532234

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202122919312.0U Active CN216522597U (en) 2021-11-25 2021-11-25 Auxiliary temperature control device for vacuum deacidification of chlorinated plasticizer

Country Status (1)

Country Link
CN (1) CN216522597U (en)

Similar Documents

Publication Publication Date Title
CN105112100A (en) Continuous production technique of chlorinated paraffin
CN205603586U (en) Crop straw enzymolysis tank
CN201543388U (en) Spray-type rapid high-efficiency copper dissolving system
CN216522597U (en) Auxiliary temperature control device for vacuum deacidification of chlorinated plasticizer
CN202193613U (en) Device for recycling dilute hydrochloric acid from tail gas containing hydrogen chloride gas
CN101654264B (en) Special device for continuously preparing light magnesium carbonate by low-pressure pyrolysis
CN203833860U (en) Production device for epoxy plasticizer
CN210366984U (en) System for tower continuous method production sodium hypochlorite
CN101624707B (en) Highly integrated fuel gas generator device without discharging any waste liquor
CN220824647U (en) Tail gas treatment device in chlorinated plasticizer production
CN211988632U (en) Energy-concerving and environment-protective type tert-butyl reation kettle for catechol production
CN2910893Y (en) Equipment for producing sodium hypochlorite
CN210410328U (en) Water glass dissolves waste heat recovery device
CN201357034Y (en) Adipic acid argon, nitrate and waste gas recovery system
CN216389266U (en) Outer groove circulation photovoltaic wet process groove type device
CN115463519B (en) Method and system for producing nitrososulfuric acid with high efficiency
CN204788013U (en) From mending water cooling tower circulating device
CN214635216U (en) Tail gas treatment device in chloro fatty acid methyl ester production
CN103819732A (en) Production device and method for epoxy plasticizer
CN214159099U (en) Recovery device for tail water of magnesium produced by concentrated nitric acid
CN203820663U (en) Production system of 2-chlorine-4-nitrotoluene
CN201574125U (en) Production equipment for naphthalene sulfonate water-reducing admixture
CN219942323U (en) Byproduct hydrogen chloride separating tower
CN219539474U (en) Double-circulation OSLO crystallizer
CN219424378U (en) Carbon source environmental protection production facility

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant