CN203284365U - Full-automatic continuous polymer manufacturing plant - Google Patents
Full-automatic continuous polymer manufacturing plant Download PDFInfo
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- CN203284365U CN203284365U CN2013201441835U CN201320144183U CN203284365U CN 203284365 U CN203284365 U CN 203284365U CN 2013201441835 U CN2013201441835 U CN 2013201441835U CN 201320144183 U CN201320144183 U CN 201320144183U CN 203284365 U CN203284365 U CN 203284365U
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Abstract
The utility model discloses a full-automatic continuous polymer manufacturing plant and mainly relates to manufacturing equipment for polycarboxylic acid concrete water reducer. The full-automatic continuous polymer manufacturing plant comprises a monomer pretreatment kettle, a plurality of automatic temperature control reaction kettles, a feeding tank, a neutralization kettle and an end product tank, all connected with one another through an automatic transport system to form the full-automatic continuous manufacturing plant. The full-automatic continuous polymer manufacturing plant, provided by the utility model, is equipped with the monomer pretreatment kettle, monomer dissolution control is facilitated, and a certain amount of monomer can be stored for the convenience of continuous manufacturing, so that the efficiency of manufacturing and preparing polycarboxylic acid water reducer is increased, and the manpower is effectively saved.
Description
Technical field
The utility model discloses a kind of full-automatic continuous polymer production equipment, by International Patent Classification (IPC) (IPC), divides and belongs to Chemicals productive experiment device technique field, relates generally to the production of polycarboxylic acid series water reducing agent.
Background technology
Polycarboxylate water-reducer is a kind of important kind in concrete admixture, and polycarboxylate water-reducer is generally take the derivative of polyoxyethylene glycol and unsaturated carboxylic acid as main raw material, through free radical polymerization, forms.Industrial installation generally comprises polyreaction tank and simple material titration apparatus two portions composition at present; There is following defect in production equipment:
1, need more manpower to be engaged in the interpolation of the solid raw materials such as polyether monomer;
2, need the workman in shifts, not so can't produce continuously.
Summary of the invention
For the deficiencies in the prior art, the utility model provides a kind of full-automatic continuous polymer production equipment, is applicable to the polycarboxylate water-reducer manufacture.
For achieving the above object, the utility model is achieved through the following technical solutions:
A kind of full-automatic continuous polymer production equipment, comprise monomer pre-treatment still, more than one temperature automatically controlled reactor, charging stock tank, neutralization tank and finished pot, wherein:
Monomer pre-treatment still, it is dissolving and the premixed container of monomer in polyreaction;
Temperature automatically controlled reactor, it provides the polyreaction place, and each reactor can be according to different reaction process design reaction times and temperature;
Charging stock tank, it is used for accommodating additive, and this additive is the aqueous solution of a certain amount of initiator and other reagent, and is added to as requested in temperature automatically controlled reactor;
Neutralization tank, add neutralization reagent and be added on request in temperature automatically controlled reactor in it;
Finished pot, it is connected to hold the final polymerisate of storage with temperature automatically controlled reactor;
Described monomer pre-treatment still, each temperature automatically controlled reactor, charging stock tank, neutralization tank and finished pot are connected to form full automatic continuous producing apparatus by automatic conveying system.
Further, described automatic conveying system comprises the automatization conveying of starting material, pre-treatment monomer and polymkeric substance finished product, and it is comprised of so that automatically control the conveying of material a plurality of T-valve that coordinate with each reactor and container tank, a plurality of flow pump, a plurality of starting material conveying belt and a conventional pump.
Further, e Foerderanlage all is with in the upper and lower of described monomer pre-treatment still, and mixing of monomer solution is convenient to mechanical stirring mechanism in its inside.
Further, the stock liquid of described monomer pre-treatment still and charging stock tank first is delivered to temperature automatically controlled reactor and carries out insulation reaction, and the neutralization reagent in neutralization tank is delivered in reactor as required by T-valve and flow pump again.
A kind of full-automatic continuous polymer production equipment of the utility model, monomer pre-treatment still wherein are the operations such as the dissolving of monomer in polyreaction and pre-mixing; Temperature automatically controlled reactor can provide the polyreaction place, can be according to no reaction process design reaction times and temperature; Automatic conveying system comprises starting material, and the automatization of pre-treatment monomer and polymkeric substance finished product is carried; Charging stock tank can add the aqueous solution of a certain amount of initiator and other reagent, by automatic conveying system, according to certain production technique, adds in temperature automatically controlled reactor; Neutralization tank can add the neutralising fluid reagent such as liquid caustic soda, by automatic conveying system, according to certain production technique, adds in temperature automatically controlled reactor.All with e Foerderanlage, inner with temperature control system and stirring system in temperature automatically controlled reactor upper and lower.
Due to the utilization of technique scheme, the utility model is compared and is had following advantages and effect with existing operative technique:
1, the utility model is full-automatic continuous polymer production equipment, has monomer pre-treatment still, not only facilitates the dissolving of monomer to control, and can store a certain amount of monomer, is convenient to continuous production and application;
2, the utility model, due to automatic conveying system and automatic temperature-controlled reactor, is convenient to the realization of the production automation.
Description of drawings
Fig. 1 is the utility model structural representation.
Embodiment
The utility model is described in further detail below in conjunction with accompanying drawing:
Embodiment: see also Fig. 1, a kind of full-automatic continuous polymer production equipment, have monomer conveying belt A, monomer pre-treatment still B, temperature automatically controlled reactor C1, C2 ..., deionization delivery system D, charging stock tank E, neutralization tank F, charging stock tank raw material conveying belt G, neutralization tank raw material conveying belt H, finished pot I.S1, S2, S3, S4, S5, S6, S7, S8 ... for program control T-valve, P1, P2 ... for flow pump, Pn is conventional pump.
During use, first use monomer conveying belt A that a certain amount of monomer is added monomer pre-treatment still B, adjust simultaneously T-valve S1, make a certain amount of deionized water add pre-treatment still B; Simultaneously, add a certain amount of raw material toward charging stock tank and neutralization tank; Starting agitator makes monomer fully dissolve mixing again; Then adjust delivery system, a certain amount of deionized water is added C1, C2 , by certain production technique, adjust delivery system again, the raw material in monomer pre-treatment still B and charging stock tank E is entered reactor C1, C2 according to a certain percentage Then, by certain processing sequence insulation reaction; Then, adjust delivery system the material of neutralization tank is added reactor C1, C2 ... in, and stir; Finally, adjust e Foerderanlage, transport material to finished pot I.Like this, a collection of material is just produced complete.Then repeat top step and just can carry out the production of the second batch of material.Perhaps monomer pre-treatment still, charging stock tank and neutralization tank are enough large, can omit the step that adds raw material.
The utility model is full-automatic design continuously, has improved the efficiency of polycarboxylate water-reducer manufacture, has effectively saved the labor force, has improved labor force's added value.
The above record, only for utilizing the embodiment of this origination techniques content, modification, variation that any those skilled in the art use this creation to do, all belong to the scope of the claims that this creation is advocated, and be not limited to those disclosed embodiments.
Claims (5)
1. a full-automatic continuous polymer production equipment, is characterized in that comprising monomer pre-treatment still, more than one temperature automatically controlled reactor, charging stock tank, neutralization tank and finished pot, wherein:
Monomer pre-treatment still, it is dissolving and the premixed container of monomer in polyreaction;
Temperature automatically controlled reactor, it provides the polyreaction place, and each reactor can be according to different reaction process design reaction times and temperature;
Charging stock tank, it is used for accommodating additive, and is added to as requested in temperature automatically controlled reactor;
Neutralization tank, add neutralization reagent and be added on request in temperature automatically controlled reactor in it;
Finished pot, it is connected to hold the final polymerisate of storage with temperature automatically controlled reactor;
Described monomer pre-treatment still, each temperature automatically controlled reactor, charging stock tank, neutralization tank and finished pot are connected to form full automatic continuous producing apparatus by automatic conveying system.
2. full-automatic continuous polymer production equipment according to claim 1, it is characterized in that: described automatic conveying system comprises the automatization conveying of starting material, pre-treatment monomer and polymkeric substance finished product, and it is comprised of so that automatically control the conveying of material a plurality of T-valve that coordinate with each reactor and container tank, a plurality of flow pump, a plurality of starting material conveying belt and a conventional pump.
3. full-automatic continuous polymer production equipment claimed in claim 1, it is characterized in that: e Foerderanlage all is with in the upper and lower of described monomer pre-treatment still, and mixing of monomer solution is convenient to mechanical stirring mechanism in its inside.
4. full-automatic continuous polymer production equipment claimed in claim 1, it is characterized in that: the stock liquid of described monomer pre-treatment still and charging stock tank first is delivered to temperature automatically controlled reactor and carries out insulation reaction, and the neutralization reagent in neutralization tank is delivered in reactor as required by T-valve and flow pump again.
5. the described full-automatic continuous polymer production equipment of one of claim 1 to 4 is characterized in that: described temperature automatically controlled reactor upper and lower is all with e Foerderanlage, and is inner with temperature control system and stirring system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013201441835U CN203284365U (en) | 2013-03-27 | 2013-03-27 | Full-automatic continuous polymer manufacturing plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013201441835U CN203284365U (en) | 2013-03-27 | 2013-03-27 | Full-automatic continuous polymer manufacturing plant |
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| CN203284365U true CN203284365U (en) | 2013-11-13 |
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| CN2013201441835U Expired - Lifetime CN203284365U (en) | 2013-03-27 | 2013-03-27 | Full-automatic continuous polymer manufacturing plant |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103769030A (en) * | 2014-02-20 | 2014-05-07 | 枣庄市荣宝莱建材科技发展有限公司 | Automatic production equipment for polycarboxylate superplasticizer |
| CN103980435A (en) * | 2014-05-22 | 2014-08-13 | 武汉华轩高新技术有限公司 | Functionalized regulating and controlling system for production of polycarboxylate water reducer |
| CN103980436A (en) * | 2014-05-22 | 2014-08-13 | 武汉华轩高新技术有限公司 | Efficient and low-energy-consumption pretreatment system for polycarboxylic acid production |
| CN110128579A (en) * | 2019-04-13 | 2019-08-16 | 复旦大学 | High pass weight polymers library is automatically synthesized apparatus and method |
-
2013
- 2013-03-27 CN CN2013201441835U patent/CN203284365U/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103769030A (en) * | 2014-02-20 | 2014-05-07 | 枣庄市荣宝莱建材科技发展有限公司 | Automatic production equipment for polycarboxylate superplasticizer |
| CN103769030B (en) * | 2014-02-20 | 2015-07-15 | 枣庄市荣宝莱建材科技发展有限公司 | Automatic production equipment for polycarboxylate superplasticizer |
| CN103980435A (en) * | 2014-05-22 | 2014-08-13 | 武汉华轩高新技术有限公司 | Functionalized regulating and controlling system for production of polycarboxylate water reducer |
| CN103980436A (en) * | 2014-05-22 | 2014-08-13 | 武汉华轩高新技术有限公司 | Efficient and low-energy-consumption pretreatment system for polycarboxylic acid production |
| CN103980436B (en) * | 2014-05-22 | 2016-08-24 | 武汉华轩高新技术有限公司 | A kind of high-efficiency low energy consumption polycarboxylic acids produces pretreatment system |
| CN103980435B (en) * | 2014-05-22 | 2016-09-28 | 武汉华轩高新技术有限公司 | A kind of functionalization regulator control system produced for polycarboxylate water-reducer |
| CN110128579A (en) * | 2019-04-13 | 2019-08-16 | 复旦大学 | High pass weight polymers library is automatically synthesized apparatus and method |
| CN110128579B (en) * | 2019-04-13 | 2021-08-20 | 复旦大学 | Automatic synthesis device and method for high-throughput polymer library |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20131113 |
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| CX01 | Expiry of patent term |