CN209052607U - The system of microchannel treated rubber captax sodium salt solution - Google Patents

The system of microchannel treated rubber captax sodium salt solution Download PDF

Info

Publication number
CN209052607U
CN209052607U CN201821734050.2U CN201821734050U CN209052607U CN 209052607 U CN209052607 U CN 209052607U CN 201821734050 U CN201821734050 U CN 201821734050U CN 209052607 U CN209052607 U CN 209052607U
Authority
CN
China
Prior art keywords
channel mixer
sodium salt
microchannel
micro
captax
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
CN201821734050.2U
Other languages
Chinese (zh)
Inventor
孙风娟
王秀猛
朱军
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.)
Kemai Chemical Co Ltd
Original Assignee
Kemai 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 Kemai Chemical Co Ltd filed Critical Kemai Chemical Co Ltd
Priority to CN201821734050.2U priority Critical patent/CN209052607U/en
Application granted granted Critical
Publication of CN209052607U publication Critical patent/CN209052607U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Landscapes

  • Extraction Or Liquid Replacement (AREA)

Abstract

The utility model belongs to rubber accelerator preparation field, and in particular to a kind of system of microchannel treated rubber captax sodium salt solution, the alkali fusion reaction kettle, multipole microchannel mixed cell and liquid separation unit for being used to mix thick M and liquid alkaline including sequential connection;The multipole microchannel mixed cell includes high temperature section micro-channel mixer, counterflow heat exchange section micro-channel mixer and the low-temperature zone micro-channel mixer being linked in sequence;Oil Guide heater and the high temperature section micro-channel mixer are connected as it and provide thermal medium;Refrigerator and the low-temperature zone micro-channel mixer are connected as it and provide cooling medium.Micro-channel mixer is used in this system, will heat up mass transfer, cooling liquid separation, low-temperature oxidation, counterflow heat exchange, multitple extraction combination, energy conservation and environmental protection, occupied area is small, and extraction efficiency is high.This system structure is simple, does not generate technique waste water, and no risk of explosion realizes comprehensive utilization of energy, and cost substantially reduces, and belongs to environmentally protective process system.

Description

The system of microchannel treated rubber captax sodium salt solution
Technical field
The utility model belongs to rubber accelerator preparation field, and in particular to a kind of microchannel treated rubber captax sodium The system of salting liquid.
Background technique
2 one mercaptobenzothiazoler of thiofide (MBT), abbreviation M are widely used a kind of logical in rubber industry With type promotor.The salting liquid formed with sodium hydroxide solution dissolution M, abbreviation M sodium salt.The M purity that high-pressure process is synthesized Lower, impure (being referred to as resin) is more, referred to as thick M.Existing M sodium salt production technology: thick M extracts through soda acid WATER-WASHING METHOD or solvent It follows the example of after purification is M, then with sodium hydroxide solution dissolves to form M sodium salt, in which: soda acid WATER-WASHING METHOD includes: thick M alkali soluble+air lift+ The processes such as oxidation+acidification+drying+pneumatic conveying drying;Solvent extraction includes: thick M high-temperature digestion+crystallisation by cooling+drying+air-flow is dry The processes such as dry.The shortcomings that soda acid WATER-WASHING METHOD: soda acid dosage is big, can generate a large amount of brine waste, and post-processing difficulty is big.Solvent extraction Following the example of is more novel processing method at present, advantage be do not generate technique waste water, the disadvantage is that: be related in production process Band solvent dries, the processes such as pneumatic conveying drying, and protection is improper to will cause peculiar smell, or even has risk of explosion.Therefore providing one kind can Overcoming the system of defect in the prior art becomes urgent problem to be solved.
Utility model content
The purpose of this utility model is to provide the systems of microchannel treated rubber captax sodium salt solution.
In order to achieve the above object, the utility model adopts the following technical solutions:
A kind of system of microchannel treated rubber captax sodium salt solution is used to mix thick M and liquid including sequential connection Alkali fusion reaction kettle, multipole microchannel mixed cell and the liquid separation unit of alkali;The multipole microchannel mixed cell includes suitable High temperature section micro-channel mixer, counterflow heat exchange section micro-channel mixer and the low-temperature zone micro-channel mixer of sequence connection;Oil Guide Heater and the high temperature section micro-channel mixer are connected as it and provide thermal medium;Refrigerator and the low-temperature zone microchannel Mixer is connected as it and provides cooling medium.
The upper end solvent portion of the liquid separation unit is returned by the counterflow heat exchange section micro-channel mixer and solvent Receive kettle connection;The lower end sodium salt part of the liquid separation unit is connect with multiple centrifugation liquid separation units;The centrifugation liquid separation list Member includes the micro-channel mixer being linked in sequence and dispenser to realize the centrifuge separation again of sodium salt.
The centrifugation liquid separation unit is 1-3.
The upper end solvent portion of the dispenser is connect with the high temperature section micro-channel mixer realizes solvent again It utilizes.
The refrigerator and the micro-channel mixer are connected as it and provide cooling medium.
The solvent recovery kettle is connect by condenser with fluid reservoir;The refrigerator is connected as it with condenser and mentions For cooling medium;The Oil Guide heater and solvent recovery kettle is connected as it and provides heat medium.
The fluid reservoir and the micro-channel mixer are connected as it and provide extractant.
The alkali fusion reaction kettle surface is provided with insulating layer.
Compared with prior art, the utility model has the beneficial effects that
Using the purification M sodium salt system of the utility model, high temperature product is continuously squeezed into alkali fusion with room temperature lye and is reacted In kettle, agitating device makes solid dissolve rapidly to thick M sodium salt.It is mixed that thick M sodium salt and extract liquor squeeze into high temperature section microchannel simultaneously Clutch, the high-speed impact in micro-channel mixer using the biggish heat exchange area in microchannel and material, realization are rapidly heated, high speed Mass transfer.Using micro-channel mixer temperature descending section, it is organic that solubility of the reduction impurity resin in sodium salt enters more resins Xiang Zhong, while the ratio of dissolving each other of sodium salt phase and solvent phase is reduced, subsequently into liquid separation unit, by organic solvent phase and salt water phase point From.As preference, the low-temperature solvent after separation mutually passes through counterflow heat exchange section micro-channel mixer and mixes with the high temperature before separating Liquid heat exchange, high-temperature extraction solvent out are mutually directly entered solvent recovery kettle, realize comprehensive utilization of energy.Recovered solvent enters Solvent enters fluid reservoir by condenser, recycling.The extractant of low temperature sodium salt recycling after separation is extracted, and is mentioned High effect of extracting.The system has liquid holdup small, and occupied area is small, and security and stability is high, economical environment-protective, no technique waste water row It puts, continuous production is high-efficient, high degree of automation.
Detailed description of the invention
Fig. 1 is the overall structure diagram of the utility model.
Specific embodiment
In order to make those skilled in the art more fully understand the technical solution of the utility model, with reference to the accompanying drawing The utility model is described in further detail with most preferred embodiment.
The system that Fig. 1 shows a kind of microchannel treated rubber captax sodium salt solution is used to mix including sequential connection Alkali fusion reaction kettle 1, multipole microchannel mixed cell and the liquid separation unit of thick M and liquid alkaline;The multipole microchannel mixes single Member includes that the high temperature section micro-channel mixer 2, counterflow heat exchange section micro-channel mixer 3 and low-temperature zone microchannel being linked in sequence mix Clutch 4;Oil Guide heater 10 and the high temperature section micro-channel mixer are connected as it and provide thermal medium;Refrigerator 6 with it is described Low-temperature zone micro-channel mixer be connected as its provide cooling medium.The alkali fusion reaction kettle surface is provided with insulating layer.
The upper end solvent portion of the liquid separation unit 4 passes through the counterflow heat exchange section micro-channel mixer 3 and solvent Kettle 9 is recycled to be connected to;The lower end sodium salt part of the liquid separation unit is connect with multiple centrifugation liquid separation units;The centrifugation liquid separation Unit includes the micro-channel mixer 11 being linked in sequence and dispenser 12 to realize the two-stage centrifugal separation of sodium salt or more Grade separation.The centrifugation liquid separation unit is 1-3.
The upper end solvent portion of the dispenser 12 is connect with the high temperature section micro-channel mixer 2 realizes solvent It recycles.The refrigerator and the micro-channel mixer are connected as it and provide cooling medium.
The solvent recovery kettle is connect by condenser 9 with fluid reservoir 8;The refrigerator and condenser is connected as it Cooling medium is provided;The Oil Guide heater and solvent recovery kettle is connected as it and provides heat medium.The fluid reservoir 9 with The micro-channel mixer 11 is connected as it and provides extractant.
The system of a kind of microchannel treated rubber captax sodium salt solution provided by the utility model, by soda acid WATER-WASHING METHOD It is combined with solvent method, dissolves thick M to form salting liquid with liquid alkaline, then is mixed by microchannel with extractant and M- sodium salt solution Clutch extracts away the resin impurity in M- sodium salt, so that the M sodium salt of purification be made.Micro-channel mixer is used in this system, It will heat up mass transfer, cooling liquid separation, low-temperature oxidation, counterflow heat exchange, multitple extraction combination, energy conservation and environmental protection, occupied area is small, extraction It takes high-efficient.This system structure is simple, does not generate technique waste water, and no risk of explosion realizes comprehensive utilization of energy, and cost drops significantly It is low, belong to environmentally protective process system.
The above content is only the preferred embodiment of the utility model, for those of ordinary skill in the art, according to this reality With novel thought, there will be changes in the specific implementation manner and application range, and the content of the present specification should not be construed as Limitations of the present invention.

Claims (8)

1. a kind of system of microchannel treated rubber captax sodium salt solution, which is characterized in that be used to mix including sequential connection Close the alkali fusion reaction kettle, multistage microchannel mixed cell and liquid separation unit of thick M and liquid alkaline;The multistage microchannel mixes single Member includes high temperature section micro-channel mixer, counterflow heat exchange section micro-channel mixer and low-temperature zone the microchannel mixing of sequential series Device;Oil Guide heater and the high temperature section micro-channel mixer are connected as it and provide thermal medium;Refrigerator and the low temperature Section micro-channel mixer is connected as it and provides cooling medium.
2. the system of treated rubber captax sodium salt solution in microchannel according to claim 1, which is characterized in that described The upper end solvent portion of liquid separation unit be connected to by the counterflow heat exchange section micro-channel mixer with solvent recovery kettle;It is described The lower end sodium salt part of liquid separation unit connect with multiple centrifugation liquid separation units;The centrifugation liquid separation unit includes being linked in sequence Micro-channel mixer and dispenser to realize the centrifuge separation again of sodium salt.
3. the system of treated rubber captax sodium salt solution in microchannel according to claim 2, which is characterized in that described Centrifugation liquid separation unit be 1-3.
4. the system of treated rubber captax sodium salt solution in microchannel according to claim 2, which is characterized in that described Dispenser upper end solvent portion connect with the high temperature section micro-channel mixer realize solvent recycling.
5. the system of treated rubber captax sodium salt solution in microchannel according to claim 2, which is characterized in that described Refrigerator and the micro-channel mixer be connected as its and cooling medium be provided.
6. the system of treated rubber captax sodium salt solution in microchannel according to claim 2, which is characterized in that described Solvent recovery kettle connect with fluid reservoir by condenser;The refrigerator and condenser is connected as it and provides cooling medium; The Oil Guide heater and solvent recovery kettle is connected as it and provides heat medium.
7. the system of treated rubber captax sodium salt solution in microchannel according to claim 6, which is characterized in that described Fluid reservoir and the micro-channel mixer be connected as its and extractant be provided.
8. the system of treated rubber captax sodium salt solution in microchannel according to claim 1, which is characterized in that described Alkali fusion reaction kettle surface be provided with insulating layer.
CN201821734050.2U 2018-10-24 2018-10-24 The system of microchannel treated rubber captax sodium salt solution Active CN209052607U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201821734050.2U CN209052607U (en) 2018-10-24 2018-10-24 The system of microchannel treated rubber captax sodium salt solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821734050.2U CN209052607U (en) 2018-10-24 2018-10-24 The system of microchannel treated rubber captax sodium salt solution

Publications (1)

Publication Number Publication Date
CN209052607U true CN209052607U (en) 2019-07-02

Family

ID=67051435

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201821734050.2U Active CN209052607U (en) 2018-10-24 2018-10-24 The system of microchannel treated rubber captax sodium salt solution

Country Status (1)

Country Link
CN (1) CN209052607U (en)

Similar Documents

Publication Publication Date Title
CN101654305B (en) Process for changing phenolic nitrate effluent into useful material by extracting, evaporating, crystallizing and coupling
CN101955211A (en) Method for extracting lithium carbonate from lepidolite
CN102329253B (en) Reaction apparatus for resorcinol neutralization reaction section and reaction technology thereof
CN100418884C (en) Process for raising producing aluminium oxide circulating efficiency by Bayer process
CN105967415B (en) A kind of beta naphthal high-concentration organic substance wastewater process for reclaiming with high salt and system
CN102558077B (en) Process system capable of continuously producing methylbenzotriazole (TTA) and production method
CN102557085A (en) Method for producing cesium salt and rubidium salt based on zero discharge and continuous extraction
CN102602953A (en) Method for preparing high borosilicate glass industry-level boric acid by utilizing salt lake lithium-extracting mother solution
CN104649898B (en) A kind of solvent method continuous carbonization produces beta naphthal, the method and device of coproduction 2,3 acid
CN101780994A (en) High-efficiency extraction agent and method for extracting H acid waste liquid
CN105503530A (en) Multi-effect thermal coupling rectification production apparatus and technological method of alkali process sodium methoxide preparation
CN105503664B (en) A kind of method of three monomers production technology wastewater utilization
CN109810159A (en) A kind of method that allocholic acid yield can be improved from duck bile
CN203794645U (en) Device for extracting lithium carbonate from spodumene
CN209052607U (en) The system of microchannel treated rubber captax sodium salt solution
CN209052606U (en) The system of treated rubber captax sodium salt solution
CN111186950B (en) High-yield seawater desalination system and operation method
CN111777495B (en) Method for separating solid mixture of sodium phenolate and sodium hydroxide and extracting, separating and recovering phenol from toluene
CN103897734A (en) Energy-saving efficient resin-removing method and device for coarse lignite wax
CN104743586A (en) Joint production method of alkali leaching of aluminium in Bayer red mud and aluminium oxide decomposed mother liquid evaporation for salt elimination
CN103804238A (en) Method of recovering 2-sodium naphthalenesulfonate from 2-isonaphthol production wastewater
CN102276438A (en) Production method of 1,5(1,8)-diphenoxy anthraquinone
CN102732370B (en) Pilot test method for extracting soybean oil by using aqueous enzymatic method
CN206467170U (en) The double kettle cross backflow reaction systems of L alanine isopropyl esters hydrochloride
CN203295403U (en) Device system used for extracting and refining azophenylene in RT base waste

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant