CN105037729B - A kind of device that silicone oil is prepared using hexamethyldisiloxane - Google Patents

A kind of device that silicone oil is prepared using hexamethyldisiloxane Download PDF

Info

Publication number
CN105037729B
CN105037729B CN201510523771.3A CN201510523771A CN105037729B CN 105037729 B CN105037729 B CN 105037729B CN 201510523771 A CN201510523771 A CN 201510523771A CN 105037729 B CN105037729 B CN 105037729B
Authority
CN
China
Prior art keywords
reaction kettle
storage tank
low molecule
connect
hexamethyldisiloxane
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
CN201510523771.3A
Other languages
Chinese (zh)
Other versions
CN105037729A (en
Inventor
张丹丹
陈海平
苗刚
欧阳辉
汪民康
刘亚伟
肖能成
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.)
Hubei Xingrui Silicon Material Co Ltd
Original Assignee
Hubei Xingrui 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 Hubei Xingrui Chemical Co Ltd filed Critical Hubei Xingrui Chemical Co Ltd
Priority to CN201510523771.3A priority Critical patent/CN105037729B/en
Publication of CN105037729A publication Critical patent/CN105037729A/en
Application granted granted Critical
Publication of CN105037729B publication Critical patent/CN105037729B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Silicon Polymers (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

The present invention relates to a kind of devices that silicone oil is prepared using hexamethyldisiloxane, including raw material storage tank, reaction kettle, packed tower, impeller pump, condenser, low molecule storage tank, raw material storage tank at the top of feed pipe and reaction kettle by connecting, reactor bottom is connect through conveying pipeline with rotary discharge valve, rotary discharge valve divides two-way after being connect with impeller pump, circulation loop is formed with being connect at the top of reaction kettle again after being connect all the way with packed tower, all the way directly circulation loop is formed with being connect at the top of reaction kettle.The covering device is suitable for the scale-up that hexamethyldisiloxane prepares silicone oil, simple and feasible, solves the problems, such as that laboratory amplification condition is limited, the production for hexamethyldisiloxane provides application test device.

Description

A kind of device that silicone oil is prepared using hexamethyldisiloxane
Technical field
The present invention relates to a kind of application test amplifying devices, and in particular to a kind of hexamethyldisiloxane prepares answering for silicone oil With experiment amplifying device.
Background technology
Low viscosity methyl-silicone oil uses DMC and hexamethyldisiloxane(Abbreviation MM)It is urged in storng-acid cation exchange resin It is prepared under change effect, but for the hexamethyldisiloxane of trial production, in order to which it is examined to prepare the qualification of silicone oil, removes Outside the lab scale of laboratory, need to be verified using experiment is further amplified.
Invention content
To solve the above problems, the present invention provides the application apparatus that a kind of hexamethyldisiloxane prepares silicone oil.
The specific technical solution of the present invention is as follows:
A kind of device that silicone oil is prepared using hexamethyldisiloxane, including raw material storage tank, reaction kettle, packed tower, rotor Pump, condenser, low molecule storage tank, raw material storage tank at the top of feed pipe and reaction kettle by connecting, and reactor bottom is through conveying pipeline Connect with rotary discharge valve, rotary discharge valve divides two-way after being connect with impeller pump, after being connect all the way with packed tower again with reaction kettle Top connects, and forms circulation loop, directly forms circulation loop with being connect at the top of reaction kettle all the way.
It is connect at the top of the reaction kettle through conveying pipeline with condenser overhead, condenser bottom is stored up through conveying pipeline and low molecule Tank connects.
Both ends install filter cloth and card additional on the inside of the packed tower, and filter cloth is set on the inside of card.
A kind of device that silicone oil is prepared using hexamethyldisiloxane, workflow are:Reaction kettle is vacuumized so that Raw material storage tank metering DMC enters through feed pipe in reaction kettle, stops vacuumizing, and to reaction kettle heating stirring, low molecule is stored up Tank vacuumizes, and DMC dehydrations, low molecule enters low molecule storage tank by condenser, after dehydrating amount reaches a certain level, stops taking out true Sky, reaction kettle feed inlet manually add in needed for MM, be stirred, heating preheating, be then turned on reaction kettle by impeller pump with The circulation loop that packed tower is formed, the DMC mixed and MM are squeezed into packed tower, are reacted certain time, and timing sampling measures Silicon oil viscosity after viscosity reaches required standard, closes the circulation loop.Reaction kettle is opened to follow self by what impeller pump was formed Loop back path vacuumizes low molecule storage tank, reaction kettle heating, carries out de- low, after de- low amounts reaches a certain level, stops taking off It is low.Reaction is completed.
Advantages of the present invention:The scale-up of silicone oil is prepared suitable for hexamethyldisiloxane, it is simple and feasible, solve reality The problem of room amplification condition is limited is tested, the production for hexamethyldisiloxane provides application test device.
Description of the drawings
Structure diagram of the attached drawing for the present invention.
In figure:1- raw material storage tanks, 2- reaction kettles, 3- packed towers, 4- impeller pumps, 5- condensers, 6- low molecule storage tanks, 7- rotations Turn discharge valve, section A-A, B-B are:8- cards.
Specific embodiment
The invention will be further described below in conjunction with the accompanying drawings.
As shown in the figure, a kind of device that silicone oil is prepared using hexamethyldisiloxane, including raw material storage tank, reaction kettle, is filled out Expect tower, impeller pump, condenser, low molecule storage tank, raw material storage tank at the top of feed pipe and reaction kettle by connecting, reactor bottom It is connect through conveying pipeline with rotary discharge valve, rotary discharge valve divides two-way after being connect with impeller pump, after being connect all the way with packed tower again With being connect at the top of reaction kettle, circulation loop is formed, directly forms circulation loop with being connect at the top of reaction kettle all the way.
It is connect at the top of the reaction kettle through conveying pipeline with condenser overhead, condenser bottom is stored up through conveying pipeline and low molecule Tank connects.
Both ends install filter cloth and card additional on the inside of the packed tower, and filter cloth is set on the inside of card.

Claims (1)

  1. A kind of 1. method that silicone oil is prepared using hexamethyldisiloxane, which is characterized in that including raw material storage tank(1)、
    Reaction kettle(2), packed tower(3), impeller pump(4), condenser(5), low molecule storage tank(6), raw material storage tank(1)Pass through charging Pipeline and reaction kettle(2)Top connects, reaction kettle(2)Bottom is through conveying pipeline and rotary discharge valve(7)Connection, rotary discharge valve (7)With impeller pump(4)Divide two-way after connection, all the way with packed tower(3)After connection again with reaction kettle(2)Top connects, and formation follows Loop back path, all the way directly and reaction kettle(2)Top connects, and forms circulation loop;Reaction kettle(2)Top is through conveying pipeline and condenser (5)Top connects, condenser(5)Bottom is through conveying pipeline and low molecule storage tank(6)Connection;Packed tower(3)Inside both ends install filter additional Cloth and card(8), filter cloth is set to card(8)Inside;
    Concrete technology is vacuumizes reaction kettle so that raw material storage tank metering DMC enters through feed pipe in reaction kettle, stops taking out Vacuum to reaction kettle heating stirring, vacuumizes low molecule storage tank, DMC dehydrations, and low molecule enters low molecule by condenser and stores up Tank after dehydrating amount reaches a certain level, stops vacuumizing, and in MM needed for the artificial addition of reaction kettle feed inlet, is stirred, heats up Preheating is then turned on the circulation loop that reaction kettle is formed by impeller pump and packed tower, the DMC mixed and MM is squeezed into filler It in tower, reacts certain time, timing sampling measures silicon oil viscosity, after viscosity reaches required standard, closes the circulation loop, beats Open the circulation loop that reaction kettle is formed self by impeller pump, low molecule storage tank vacuumized, reaction kettle heating, carry out it is de- low, After de- low amounts reaches a certain level, stop de- low, reaction completion.
CN201510523771.3A 2015-08-25 2015-08-25 A kind of device that silicone oil is prepared using hexamethyldisiloxane Active CN105037729B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510523771.3A CN105037729B (en) 2015-08-25 2015-08-25 A kind of device that silicone oil is prepared using hexamethyldisiloxane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510523771.3A CN105037729B (en) 2015-08-25 2015-08-25 A kind of device that silicone oil is prepared using hexamethyldisiloxane

Publications (2)

Publication Number Publication Date
CN105037729A CN105037729A (en) 2015-11-11
CN105037729B true CN105037729B (en) 2018-06-26

Family

ID=54444727

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510523771.3A Active CN105037729B (en) 2015-08-25 2015-08-25 A kind of device that silicone oil is prepared using hexamethyldisiloxane

Country Status (1)

Country Link
CN (1) CN105037729B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107778488B (en) * 2017-11-16 2020-07-21 湖北兴瑞硅材料有限公司 Low molecular remover and method for producing methyl silicone oil with viscosity of 30-1000000cs

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0031063A2 (en) * 1979-12-21 1981-07-01 Bayer Ag Process for the preparation of equilibrated organopolysiloxane products
CN102643431A (en) * 2012-05-04 2012-08-22 浙江恒业成有机硅有限公司 Method for preparing low viscosity dimethyl silicone oil
CN203393077U (en) * 2013-07-31 2014-01-15 嘉兴联合化学有限公司 Terminal epoxy-based polysiloxane production system
CN104193997A (en) * 2014-08-21 2014-12-10 湖北兴发化工集团股份有限公司 Method and device for preparing high-boiling silicon oil
CN204395970U (en) * 2014-12-19 2015-06-17 仪征市新源新材料科技有限公司 A kind of novel energy-conserving automated production silicone oil reactor

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0031063A2 (en) * 1979-12-21 1981-07-01 Bayer Ag Process for the preparation of equilibrated organopolysiloxane products
CN102643431A (en) * 2012-05-04 2012-08-22 浙江恒业成有机硅有限公司 Method for preparing low viscosity dimethyl silicone oil
CN203393077U (en) * 2013-07-31 2014-01-15 嘉兴联合化学有限公司 Terminal epoxy-based polysiloxane production system
CN104193997A (en) * 2014-08-21 2014-12-10 湖北兴发化工集团股份有限公司 Method and device for preparing high-boiling silicon oil
CN204395970U (en) * 2014-12-19 2015-06-17 仪征市新源新材料科技有限公司 A kind of novel energy-conserving automated production silicone oil reactor

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
Silicone fluid manufacture;Reuben Gutoff,等;《Industrial and Engineering Chemistry》;19571130;第49卷(第11期);第1807-1811页 *
碱催化制备低黏度甲基硅油和乙烯基硅油;李恩,等;《有机硅材料》;20131130;第27卷(第6期);第441-443页 *

Also Published As

Publication number Publication date
CN105037729A (en) 2015-11-11

Similar Documents

Publication Publication Date Title
CN206906203U (en) A kind of high-temperature high-pressure reaction kettle device for overcritical sour gas Water-rock interaction
CN103831075B (en) A kind of electric motor built-in hypergravity swinging bed device and application thereof
CN203187662U (en) Lab culture medium preparing and split charging device
CN209597189U (en) A kind of Low-viscosity high-flash-point waterborne polyurethane water shutoff material production equipment
CN103766205B (en) The bottled medium preparation method of roxburgh anoectochilus terminal bud and packaging device thereof
CN105037729B (en) A kind of device that silicone oil is prepared using hexamethyldisiloxane
CN107778488A (en) A kind of de- low molecule device and the method that production viscosity is 30 1000000cs methyl-silicone oils
CN101764070B (en) Resin adhesive vacuum encapsulation device and process thereof
CN103149122B (en) Steel-making calcium activated analyser in calcium system auxiliary agent
CN104807821A (en) Swing reaction device for evaluating performance of hydrate inhibitors
CN104263219B (en) A kind of new polyturethane waterproofing paint process units and technique thereof
CN206660668U (en) A kind of nitrogen charging polymer deaerating plant
CN206591061U (en) A kind of polycarboxylic acids process units
CN205659681U (en) A apparatus for producing for resin is synthetic
CN201526806U (en) Continuous liquid supply device
CN206184050U (en) Bubble system is arranged to substrate glue
CN205346806U (en) Printing ink partial shipment system
CN112903959B (en) Simulation experiment method and device for supercritical/subcritical static water rock reaction
CN2885828Y (en) Sol feeder device
CN109224930A (en) A kind of fire foam process units
CN206508941U (en) Analytical instrument gaseous mixture air distributing device
CN203033752U (en) Separating funnel with stirrer for adjusting and displaying temperature
CN207221388U (en) A kind of highly effective and safe chemical industry extraction separation device
CN201572622U (en) Novel thermostatting diaphragm emulsifier
CN205556857U (en) Automatic liquid supplementation device of polycrystal making herbs into wool

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CP03 Change of name, title or address
CP03 Change of name, title or address

Address after: 443007 No. 66-2 Ting Ting Road, Ting Ting District, Yichang, Hubei

Patentee after: Hubei Xingrui silicon material Co., Ltd.

Address before: 443006 No. 29 Changjiang Road, Ting Ting District, Yichang, Hubei

Patentee before: HUBEI XINGRUI CHEMICAL CO., LTD.