CN103923701A - Multistage jacketed chlorinated paraffin reaction tower - Google Patents

Multistage jacketed chlorinated paraffin reaction tower Download PDF

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Publication number
CN103923701A
CN103923701A CN201310603030.7A CN201310603030A CN103923701A CN 103923701 A CN103923701 A CN 103923701A CN 201310603030 A CN201310603030 A CN 201310603030A CN 103923701 A CN103923701 A CN 103923701A
Authority
CN
China
Prior art keywords
reaction tower
multistage
tower
jacketed
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.)
Pending
Application number
CN201310603030.7A
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Chinese (zh)
Inventor
刘新涛
姜维喜
陈剑英
卞福香
穆道旭
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.)
Dalian Lonsin New Materials Co Ltd
Original Assignee
Dalian Lonsin New 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 Dalian Lonsin New Materials Co Ltd filed Critical Dalian Lonsin New Materials Co Ltd
Priority to CN201310603030.7A priority Critical patent/CN103923701A/en
Publication of CN103923701A publication Critical patent/CN103923701A/en
Pending legal-status Critical Current

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Abstract

The invention relates to a multistage jacketed chlorinated reaction tower, and belongs to the field of paraffin processing equipment. The multistage jacketed chlorinated paraffin reaction tower includes a cylindrical tower body and end covers arranged at both ends of the tower body; the tower body is provided with at least two ring jackets and, each jacket is provided with at least a circulating liquid outlet and at least one circulating liquid inlet. According to the multistage jacketed chlorinated paraffin reaction tower, the multistage jackets are externally arranged on the reaction tower, the cooling effectiveness of the multistage jackets can be controlled when in use, so that materials in each part of the reaction tower can be fully reacted, and the production efficiency is improved.

Description

Multistage jacketed type clorafin reaction tower
Technical field
The present invention relates to a kind of multistage jacketed type clorafin reaction tower, belong to paraffin processing units field.
Background technology
Clorafin can be widely used as softening agent and because it well hinders for combustion property, can also be for plastics and rubber fire-retardant, the waterproof of fabric, fire proofing additive, the additive of coating, ink and withstand voltage lubricated oil additives.
The preparation method of clorafin comprises three kinds of thermal chlorination, catalysis method and photocatalytic methods at present.Above-mentioned three kinds of methods, in production process, all need the reaction heat that reaction is produced to take out of, at present comparatively conventional mode is to utilize pump etc. to force outer circulation the reactant in reactor, reactant in reaction tower exterior cooling is reinjected in reaction tower, though the method is effective, but, inject back the material heterogeneity in reaction tower, and iterative cycles wastes energy.In addition, due to progressively carrying out of reaction, will cause the viscosity of the reaction mass in reaction tower to increase from top to bottom, cause the material reaction speed of bottom to decline.
Summary of the invention
The object of this invention is to provide a kind of multistage jacketed type clorafin reaction tower.
A multistage jacketed type clorafin reaction tower, described reaction tower comprises cylindrical-shaped tower and is located at the end cap at tower body two ends; Described tower body is provided with at least two annular chucks, and described chuck is provided with at least one circulation fluid outlet and at least one circulation fluid entrance.
Described in multistage jacketed type clorafin reaction tower of the present invention, tower body is provided with three annular chucks, and described chuck is provided with a circulation fluid outlet and a circulation fluid entrance.
Described in multistage jacketed type clorafin reaction tower of the present invention, tower body outer wall is provided with preservative coat.
The preferred described reaction tower of multistage jacketed type clorafin reaction tower of the present invention comprises upper end cover and lower end cover.
The preferred described upper end cover of multistage jacketed type clorafin reaction tower of the present invention is provided with gas inlet, feeding mouth and pneumatic outlet.
The preferred described lower end cover of multistage jacketed type clorafin reaction tower of the present invention is provided with discharge opening.
Described in multistage jacketed type clorafin reaction tower of the present invention, annular chuck is in-built a heat-conducting medium.
Described in multistage jacketed type clorafin reaction tower of the present invention, heat-conducting medium is water.
Described in multistage jacketed type clorafin reaction tower of the present invention, chuck is provided with temperature sensing device.
Preferred technical scheme of the present invention is:
A multistage jacketed type clorafin reaction tower, described reaction tower comprises cylindrical-shaped tower and is located at the end cap at tower body two ends; Described reaction tower comprises upper end cover and lower end cover.Described upper end cover is provided with gas inlet, feeding mouth and pneumatic outlet.Described lower end cover is provided with discharge opening.Described chuck is provided with temperature sensing device.
Beneficial effect of the present invention: multistage jacketed type clorafin reaction tower provided by the invention, this reaction tower is provided with multistage chuck outward, during use, can control the cooling effectiveness of each chuck, thereby various piece material in reaction tower is fully reacted, enhance productivity.
Accompanying drawing explanation
Fig. 1 is a kind of schematic diagram of multistage jacketed type clorafin reaction tower;
Fig. 2 is chuck schematic cross-section.
Embodiment
Following non-limiting example can make the present invention of those of ordinary skill in the art's comprehend, but does not limit the present invention in any way.
Embodiment 1
A multistage jacketed type clorafin reaction tower, described reaction tower comprises cylindrical-shaped tower 1 and is located at the end cap at tower body 1 two ends; Described tower body 1 is provided with three annular chucks 2, and described chuck is provided with 3 and circulation fluid entrances 4 of a circulation fluid outlet.Described tower body 1 outer wall is provided with preservative coat.Described reaction tower comprises upper end cover 8 and lower end cover 10.Upper end cover 8 is provided with gas inlet 5, feeding mouth 6 and pneumatic outlet 7.Described lower end cover 10 is provided with discharge opening 9.In described annular chuck 2, water is housed.Described chuck 2 is provided with temperature sensing device.

Claims (9)

1. a multistage jacketed type clorafin reaction tower, is characterized in that: described reaction tower comprises cylindrical-shaped tower (1) and is located at the end cap at tower body (1) two ends; Described tower body (1) is provided with at least two annular chucks (2), and described chuck is provided with at least one circulation fluid outlet (3) and at least one circulation fluid entrance (4).
2. reaction tower according to claim 1, is characterized in that: described tower body (1) is provided with three annular chucks (2), and described chuck is provided with circulation fluid outlet (3) and a circulation fluid entrance (4).
3. reaction tower according to claim 1, is characterized in that: described tower body (1) outer wall is provided with preservative coat.
4. reaction tower according to claim 1, is characterized in that: described reaction tower comprises upper end cover (8) and lower end cover (11).
5. reaction tower according to claim 4, is characterized in that: described upper end cover (8) is provided with gas inlet (5), feeding mouth (6) and pneumatic outlet (7).
6. reaction tower according to claim 4, is characterized in that: described lower end cover (10) is provided with discharge opening (9).
7. reaction tower according to claim 1, is characterized in that: in described annular chuck (2), heat-conducting medium is housed.
8. reaction tower according to claim 7, is characterized in that: described heat-conducting medium is water.
9. reaction tower according to claim 1, is characterized in that: described chuck (2) is provided with temperature sensing device.
CN201310603030.7A 2013-11-22 2013-11-22 Multistage jacketed chlorinated paraffin reaction tower Pending CN103923701A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310603030.7A CN103923701A (en) 2013-11-22 2013-11-22 Multistage jacketed chlorinated paraffin reaction tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310603030.7A CN103923701A (en) 2013-11-22 2013-11-22 Multistage jacketed chlorinated paraffin reaction tower

Publications (1)

Publication Number Publication Date
CN103923701A true CN103923701A (en) 2014-07-16

Family

ID=51142103

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310603030.7A Pending CN103923701A (en) 2013-11-22 2013-11-22 Multistage jacketed chlorinated paraffin reaction tower

Country Status (1)

Country Link
CN (1) CN103923701A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105013407A (en) * 2015-07-27 2015-11-04 陕西延长石油集团氟硅化工有限公司 Organic fluorination reaction kettle device

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1033643A (en) * 1987-12-18 1989-07-05 楼存宝 Automatically circulation formula continuous processing is produced clorafin and chlorocarbon technology and main device
CN1424381A (en) * 2002-12-18 2003-06-18 宁波市镇海众利化工有限公司 Devices for continuously producing chlorinated paraffin
CN1843612A (en) * 2006-03-13 2006-10-11 江南大学 Multifunctional post-extraction tank for extracting biological reaction product
CN102936517A (en) * 2012-11-30 2013-02-20 大连隆星新材料有限公司 Device for preparing chloroparaffin

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1033643A (en) * 1987-12-18 1989-07-05 楼存宝 Automatically circulation formula continuous processing is produced clorafin and chlorocarbon technology and main device
CN1424381A (en) * 2002-12-18 2003-06-18 宁波市镇海众利化工有限公司 Devices for continuously producing chlorinated paraffin
CN1843612A (en) * 2006-03-13 2006-10-11 江南大学 Multifunctional post-extraction tank for extracting biological reaction product
CN102936517A (en) * 2012-11-30 2013-02-20 大连隆星新材料有限公司 Device for preparing chloroparaffin

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105013407A (en) * 2015-07-27 2015-11-04 陕西延长石油集团氟硅化工有限公司 Organic fluorination reaction kettle device

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Application publication date: 20140716