CN206793675U - A kind of intermediate for producing high collapse-preventing type polyether monomer to pretreatment feeding-distribution device - Google Patents
A kind of intermediate for producing high collapse-preventing type polyether monomer to pretreatment feeding-distribution device Download PDFInfo
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- CN206793675U CN206793675U CN201720699770.9U CN201720699770U CN206793675U CN 206793675 U CN206793675 U CN 206793675U CN 201720699770 U CN201720699770 U CN 201720699770U CN 206793675 U CN206793675 U CN 206793675U
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- pipeline
- cooling water
- measuring tank
- reaction kettle
- main reaction
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Abstract
A kind of intermediate for producing high collapse-preventing type polyether monomer be the utility model is related to pretreatment feeding-distribution device, including middle measuring tank A, middle measuring tank B, pre-process kettle, valve, instrument, vacuum pipe, exhaust pipe, nitrogen pipeline, remove main reaction kettle pipeline A, jet chimney A, cooling water return pipeline A, jet chimney B, cooling water return pipeline B, steam condensate (SC) pipeline A, recirculated cooling water water supply pipeline, steam condensate (SC) pipeline B, recirculated cooling water water supply pipeline, remove main reaction kettle pipeline B, remove main reaction kettle pipeline C, it is characterized in that middle measuring tank A, middle measuring tank B is connected with pretreatment kettle, the beneficial effects of the utility model are, the utility model can be quicker, more efficiently distribute material, it is added significantly to the production efficiency of polyether monomer.
Description
Technical field
The manufacture of high collapse-preventing type polyether monomer production equipment is the utility model is related to, specifically a kind of high protect of production is collapsed
The intermediate of type polyether monomer to pretreatment feeding-distribution device.
Background technology
Polyether monomer is mainly used in building trade, as the primary raw material of concrete additive, by development for many years
The increasing market share is won with the characteristic of high water reducing rate, by years development from lipid to ethers, adaptability is also more next
Better.
Because the gap of various regions sand material and binder materials is larger, slump loss in actual production is caused to be difficult to
Keeping, polyether monomer currently on the market is mainly used to produce the water reducer of high water reducing rate, but for the sand materials such as Beijing ratio
Poor construction market must just add special guarantor agent of collapsing and be adjusted.
The content of the invention
Technical problem to be solved in the utility model is overcome the deficiencies in the prior art, there is provided one kind produces high collapse-preventing type
The intermediate of polyether monomer is to pretreatment feeding-distribution device, and technical scheme is used by the utility model solves its technical problem:
Structure of the present utility model includes middle measuring tank A, middle measuring tank B, pretreatment kettle, valve, instrument, vacuum pipe, tail gas
Pipeline, nitrogen pipeline, go main reaction kettle pipeline A, jet chimney A, cooling water return pipeline A, jet chimney B, circulation cold
But water water return pipeline B, steam condensate (SC) pipeline A, recirculated cooling water water supply pipeline, steam condensate (SC) pipeline B, circulating cooling are waterborne
Waterpipe, remove main reaction kettle pipeline B, remove main reaction kettle pipeline C, it is characterised in that middle measuring tank A, middle measuring tank B with it is pre-
Handle kettle connection.
A kind of intermediate for producing high collapse-preventing type polyether monomer to pretreatment feeding-distribution device, it is characterised in that centre meter
Vacuum pipe, exhaust pipe are set on measuring tank A and middle measuring tank B, nitrogen pipeline, remove main reaction kettle pipeline A, is pre-processed on kettle
Jet chimney A, cooling water return pipeline A, jet chimney B, cooling water return pipeline B, steam condensate (SC) pipe are set
Road A, recirculated cooling water water supply pipeline, steam condensate (SC) pipeline B, recirculated cooling water water supply pipeline, remove main reaction kettle pipeline B, go
Main reaction kettle pipeline C, each pipeline are controlled and monitored with instrument by valve.
Pretreating process flow:First deionized water is squeezed into reactor by meter, then NaOH solid state powders are led to
Cross screw feeder to be slowly added in reactor, and be stirred continuously, control temperature is made between 80 DEG C~90 DEG C by vavuum pump
Vacuum state is in kettle, 99% methallyl alcohol of barreled is squeezed into head tank with pump, is added by meter in reactor,
It is stirred continuously, methallyl alcohol, NaOH and input amount mol ratio are 30: 1, methallyl alcohol and NaOH reaction methallyl sodium alkoxide
And water, in terms of methallyl alcohol, up to 98%, reaction generation water and raw material deionized water pass through reactivity as water vapor
Vavuum pump is constantly deviate from, and reaction is carried out to the right, methallyl alcohol is fully reacted generation methallyl sodium alkoxide, reaction with NaOH
After end, the solution is sent into polymerization reaction kettle by solution based on methallyl sodium alkoxide by pump in kettle.
The beneficial effects of the utility model are that the utility model more quick, more efficient can distribute material, significantly increase
The production efficiency of polyether monomer is added.
Brief description of the drawings
Fig. 1:The utility model embodiment structural representation.
Fig. 2:The utility model embodiment pretreatment reaction equation.
In figure:Middle measuring tank A1, middle measuring tank B2, pretreatment kettle 3, valve 4, instrument 5, vacuum pipe 6, offgas duct
Road 7, nitrogen pipeline 8, go main reaction kettle pipeline A9, jet chimney A10, cooling water return pipeline A11, jet chimney B12,
Cooling water return pipeline B13, steam condensate (SC) pipeline A14, recirculated cooling water water supply pipeline 15, steam condensate (SC) pipeline
B16, recirculated cooling water water supply pipeline 17, remove main reaction kettle pipeline B18, remove main reaction kettle pipeline C19.
Embodiment
It is described with reference to make the utility model detailed description in detail below.As shown in drawings, it is of the present utility model
Structure include middle measuring tank A1, middle measuring tank B2, pretreatment kettle 3, valve 4, instrument 5, vacuum pipe 6, exhaust pipe 7,
Nitrogen pipeline 8, go main reaction kettle pipeline A9, jet chimney A10, cooling water return pipeline A11, jet chimney B12, circulation
CWR road B13, steam condensate (SC) pipeline A14, recirculated cooling water water supply pipeline 15, steam condensate (SC) pipeline B16, follow
Ring cooling water water supply pipeline 17, remove main reaction kettle pipeline B18, remove main reaction kettle pipeline C19, it is characterised in that middle measuring tank
A1, middle measuring tank B2 are connected with pretreatment kettle 3.
A kind of intermediate for producing high collapse-preventing type polyether monomer to pretreatment feeding-distribution device, it is characterised in that centre meter
Vacuum pipe 6, exhaust pipe 7 are set on measuring tank A1 and middle measuring tank B2, nitrogen pipeline 8, remove main reaction kettle pipeline A9, pre- place
Manage and jet chimney A10, cooling water return pipeline A11, jet chimney B12, cooling water return pipeline are set on kettle
B13, steam condensate (SC) pipeline A14, recirculated cooling water water supply pipeline 15, steam condensate (SC) pipeline B16, recirculated cooling water upper hose
Road 17, remove main reaction kettle pipeline B18, remove main reaction kettle pipeline C19, each pipeline is controlled and monitored with instrument 5 by valve 4.
Embodiment described above is only that preferred embodiment of the present utility model is described, not to this practicality
New spirit and scope are defined, on the premise of the utility model design conception is not departed from, ordinary skill in this area
The all variations and modifications that technical staff makes to the technical solution of the utility model, protection model of the present utility model all should be fallen into
Enclose, the claimed technology contents of the utility model, all recorded in detail in the claims.
Claims (2)
1. a kind of intermediate for producing high collapse-preventing type polyether monomer to pretreatment feeding-distribution device, including middle measuring tank A (1), in
Between measuring tank B (2), pretreatment kettle (3), valve (4), instrument (5), vacuum pipe (6), exhaust pipe (7), nitrogen pipeline (8),
Go main reaction kettle pipeline A (9), jet chimney A (10), cooling water return pipeline A (11), jet chimney B (12), circulation cold
But water water return pipeline B (13), steam condensate (SC) pipeline A (14), recirculated cooling water water supply pipeline (15), steam condensate (SC) pipeline B
(16), recirculated cooling water water supply pipeline (17), remove main reaction kettle pipeline B (18), remove main reaction kettle pipeline C (19), its feature exists
It is connected in middle measuring tank A (1), middle measuring tank B (2) with pretreatment kettle (3).
2. a kind of intermediate for producing high collapse-preventing type polyether monomer according to claim 1 to pretreatment feeding-distribution device, its
It is characterised by middle measuring tank A (1) with setting vacuum pipe (6), exhaust pipe (7), nitrogen pipeline on middle measuring tank B (2)
(8) main reaction kettle pipeline A (9), is removed, pre-processes and jet chimney A (10), cooling water return pipeline A (11) is set on kettle, steamed
Steam pipe road B (12), cooling water return pipeline B (13), steam condensate (SC) pipeline A (14), recirculated cooling water water supply pipeline
(15), steam condensate (SC) pipeline B (16), recirculated cooling water water supply pipeline (17), remove main reaction kettle pipeline B (18), go main reaction
Kettle pipeline C (19), each pipeline are controlled and monitored by valve (4) and instrument (5).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720699770.9U CN206793675U (en) | 2017-06-12 | 2017-06-12 | A kind of intermediate for producing high collapse-preventing type polyether monomer to pretreatment feeding-distribution device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201720699770.9U CN206793675U (en) | 2017-06-12 | 2017-06-12 | A kind of intermediate for producing high collapse-preventing type polyether monomer to pretreatment feeding-distribution device |
Publications (1)
Publication Number | Publication Date |
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CN206793675U true CN206793675U (en) | 2017-12-26 |
Family
ID=60747201
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201720699770.9U Expired - Fee Related CN206793675U (en) | 2017-06-12 | 2017-06-12 | A kind of intermediate for producing high collapse-preventing type polyether monomer to pretreatment feeding-distribution device |
Country Status (1)
Country | Link |
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CN (1) | CN206793675U (en) |
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2017
- 2017-06-12 CN CN201720699770.9U patent/CN206793675U/en not_active Expired - Fee Related
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Legal Events
Date | Code | Title | Description |
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GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171226 Termination date: 20200612 |
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CF01 | Termination of patent right due to non-payment of annual fee |