CN206435184U - A kind of polycarboxylate superplasticizer mother liquor production system - Google Patents
A kind of polycarboxylate superplasticizer mother liquor production system Download PDFInfo
- Publication number
- CN206435184U CN206435184U CN201720078616.XU CN201720078616U CN206435184U CN 206435184 U CN206435184 U CN 206435184U CN 201720078616 U CN201720078616 U CN 201720078616U CN 206435184 U CN206435184 U CN 206435184U
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- Prior art keywords
- retort
- metering head
- pipeline
- finished product
- tank
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Abstract
The utility model discloses a kind of polycarboxylate superplasticizer mother liquor production system, including：Pure water groove, organic acid tank, A hoppers and the B hoppers being placed in bottom production space；A material retort, blending tank and the finished product retort being placed in the production space of intermediate layer；The A material metering head tank and B material metering head tanks being placed in the production space of upper strata, A material metering head tank and B the material metering head tank are arranged at intervals；Finished product retort expects the underface of metering head tank and B material metering head tanks located at A, each finished product retort is connected with an A material metering head tank and a B material metering head tank respectively, multiple finished pots are additionally provided with bottom production space, finished pot is located at the underface of finished product retort.The utility model has the advantage that：It is whole system compact conformation, rationally distributed, floor space can be greatlyd save.Raw material mixing is abundant, and automaticity is high, can improve production efficiency, the quality of production of product is can guarantee that again.
Description
Technical field
The utility model is related to chemical equipment technical field, and system is produced more particularly, to a kind of polycarboxylate superplasticizer mother liquor
System.
Background technology
Water reducer is a kind of under conditions of maintaining concrete slump constant, outside the concrete that can reduce mixing water amount
Plus agent.Belong to anion surfactant mostly, there is lignosulfonates, naphthalene sulphonate formaldehyde polymer etc..The life of water reducer
Need to use reactor, raw material storage tank etc. during production, connected between raw material storage tank and reactor by pipeline, in raw material storage tank
Raw material entered in reactor and reacted by pipeline.
Utility model content
The purpose of this utility model is that there is provided a kind of simple and compact for structure, layout in order to make up the deficiencies in the prior art
Rational polycarboxylate superplasticizer mother liquor production system.
In order to reach the purpose of this utility model, technical scheme is as follows：
A kind of polycarboxylate superplasticizer mother liquor production system, it is characterised in that including：
Pure water groove, organic acid tank, A hoppers and the B hoppers being placed in bottom production space；
A material retort, blending tank and the finished product retort being placed in the production space of intermediate layer；
The A material metering head tank and B material metering head tanks being placed in the production space of upper strata, the A material metering head tank and B
Material metering head tank is arranged at intervals；
Finished product retort expects the underface of metering head tank and B material metering head tanks, each finished product retort difference located at A
Connected with an A material metering head tank and a B material metering head tank, multiple finished pots be additionally provided with bottom production space,
Finished pot is located at the underface of finished product retort.
Preferably, pure water groove expects that retort and blending tank are connected with A respectively by pipeline, and organic acid tank passes through pipeline
Connected with A material retort, A expects that A material are delivered in A hoppers by retort by pipeline and A material conveying pumps, and blending tank passes through pipeline
B material are delivered in B hoppers with B material conveying pumps.
Preferably, the A in the A hoppers expects that the A material feeding pumps by pipeline and on pipeline are delivered to A material meterings
In head tank, the B in B hoppers expects that the B material feeding pumps by pipeline and on pipeline are delivered in B material metering head tanks.
Preferably, the bottom of finished product retort is provided with into by pipeline with being connected at the top of finished pot on the pipeline of connection
Product delivery pump.
Preferably, the bottom of finished product retort is also connected by pipeline with blending tank top.
Preferably, pure water groove is also connected by pipeline with finished product retort top.
The utility model has the advantage that：
It is whole system compact conformation, rationally distributed, floor space can be greatlyd save.Raw material mixing is abundant, automaticity
Height, can improve production efficiency, and the quality of production of product is can guarantee that again.
Brief description of the drawings
Fig. 1 is the structural representation of this practical polycarboxylate superplasticizer mother liquor production system.
Embodiment
The utility model is further described with reference to embodiment, but protection domain of the present utility model not only office
It is limited to embodiment.
With reference to shown in Fig. 1, a kind of polycarboxylate superplasticizer mother liquor production system, in the production space for being respectively placed in three layers, most
Bottom can be walked about between the superiors by stair.Wherein being placed in bottom production space 300 has pure water groove 101, organic acid
Groove 102, A hoppers 103 and B hoppers 104；Being placed in intermediate layer production space 200 has A to expect retort 1, blending tank 3 and finished product
Retort 4；Being placed in upper strata production space 100 has A material metering head tank 5 and B material metering head tanks 6, and the A material metering is high
Position groove 5 and B material metering head tanks 6 are arranged at intervals, and an A material metering head tank 5 and a B material metering head tank 6 coordinate
It is used together.
Finished product retort 4 expects the underface of metering head tank and B material metering head tanks, each finished product retort point located at A
Do not connected with an A material metering head tank and a B material metering head tank, A material metering head tank and B material metering head tank difference
It will be reacted in A material and B material feeding finished products retort 4.Multiple finished pots 107 are additionally provided with bottom production space 300, into
Product tank 107 is located at the underface of finished product retort, and reacted finished product is delivered in finished pot 107 by finished product delivery pump 109,
Finished product in finished pot 107 dispatches from the factory finally by the conveying of finished product pump 110 to be used.
Pure water groove 101 expects that retort 1, blending tank 3 and finished product react by the pure water pump 111 on pipeline and pipeline and A
The top of tank 4 is connected, and conveys pure water into each retort.Organic acid tank 102 expects that the top of retort 1 is connected by pipeline with A
And expect to convey organic acid in retort 1 to A.A expects that retort 1 will react obtained A material the bottom of from by pipeline and A material conveying pumps 11
Portion is delivered in A hoppers 103, and blending tank 3 will react obtained B by pipeline and B material conveying pumps 31 and expect that being delivered to B from bottom expects
In groove 104.Raw material adds A from top by raw materials pump 36 and expected in retort 1, therefore the reactant of A material retort 1 has original
Material, pure water and organic acid.
A of the A material by pipeline and on pipeline in A hoppers 103 expects that feeding pump 34 is delivered to A material metering head tanks
In 5, B of the B material by pipeline and on pipeline in B hoppers 104 expects that feeding pump 35 is delivered in B material metering head tanks 6.
A expects and B material are delivered in finished product retort 4 from A material metering head tank 5 and B material metering head tanks 6 respectively and carry out end reaction shape
Into finished product.
The bottom of finished product retort 4 is connected by pipeline with the top of finished pot 107, and is provided with the pipeline connected
Product delivery pump 109.The bottom of finished product retort 4 is also connected by pipeline with the top of blending tank 3, and finished product retort 4 is with mixing
Close and finished product delivery pump 109 is also installed on the pipeline that tank 3 is connected, therefore, the material into blending tank 3 is pure water and finished product, is mixed
Close tank 3 even directly to communicate with one of finished pot 107, finished product is used after mixing with pure water again, can play well
Adjustment effect.
Finally it should be noted that：Above example only not limits the utility model and retouched to illustrate the utility model
The technical scheme stated, therefore, although this specification the utility model is had been carried out with reference to each above-mentioned embodiment it is detailed
Illustrate, still, it will be understood by those within the art that, still the utility model can be modified or equally replaced
Change, and technical scheme that all do not depart from spirit and scope of the present utility model and its improvement, it all should cover new in this practicality
In the right of type.
Claims (6)
1. a kind of polycarboxylate superplasticizer mother liquor production system, it is characterised in that including：
Pure water groove (101), organic acid tank (102), A hoppers (103) and the B hoppers being placed in bottom production space (300)
(104)；
A material retort (1), blending tank (3) and the finished product retort (4) being placed in intermediate layer production space (200)；
The A material metering head tanks (5) and B material metering head tanks (6) being placed in upper strata production space (100), the A material metering are high
Position groove and B material metering head tanks are arranged at intervals；
Finished product retort expects the underface of metering head tank and B material metering head tanks located at A, and each finished product retort is respectively with one
Individual A material metering head tank and a B material metering head tank connection, are additionally provided with multiple finished pots (107) in bottom production space,
Finished pot is located at the underface of finished product retort.
2. polycarboxylate superplasticizer mother liquor production system according to claim 1, it is characterised in that pure water groove passes through pipeline point
Do not connected with A material retort (1) and blending tank (3), organic acid tank expects that retort is connected by pipeline with A, A material retort
A material are delivered in A hoppers (103) by pipeline and A material conveying pumps (11), blending tank (3) passes through pipeline and B material conveying pumps
(31) B material are delivered in B hoppers (104).
3. polycarboxylate superplasticizer mother liquor production system according to claim 2, it is characterised in that in the A hoppers (103)
A material expect that feeding pump (34) is delivered in A material metering head tanks by pipeline and A on pipeline, in B hoppers (104)
B material expect that feeding pump (35) is delivered in B material metering head tanks by pipeline and B on pipeline.
4. polycarboxylate superplasticizer mother liquor production system according to claim 2, it is characterised in that the bottom of finished product retort
By pipeline with being connected at the top of finished pot, finished product delivery pump is installed on the pipeline of connection.
5. polycarboxylate superplasticizer mother liquor production system according to claim 4, it is characterised in that the bottom of finished product retort
Also by pipeline with being connected at the top of blending tank.
6. polycarboxylate superplasticizer mother liquor production system according to claim 2, it is characterised in that pure water groove also passes through pipeline
With being connected at the top of finished product retort.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720078616.XU CN206435184U (en) | 2017-01-20 | 2017-01-20 | A kind of polycarboxylate superplasticizer mother liquor production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720078616.XU CN206435184U (en) | 2017-01-20 | 2017-01-20 | A kind of polycarboxylate superplasticizer mother liquor production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206435184U true CN206435184U (en) | 2017-08-25 |
Family
ID=59635088
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720078616.XU Expired - Fee Related CN206435184U (en) | 2017-01-20 | 2017-01-20 | A kind of polycarboxylate superplasticizer mother liquor production system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206435184U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113171732A (en) * | 2021-03-22 | 2021-07-27 | 中船重工（邯郸）派瑞特种气体有限公司 | Dangerous liquid feeding system and method |
-
2017
- 2017-01-20 CN CN201720078616.XU patent/CN206435184U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113171732A (en) * | 2021-03-22 | 2021-07-27 | 中船重工（邯郸）派瑞特种气体有限公司 | Dangerous liquid feeding system and method |
| CN113171732B (en) * | 2021-03-22 | 2022-05-17 | 中船(邯郸)派瑞特种气体股份有限公司 | Dangerous liquid feeding system and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170825 Termination date: 20190120 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |