CN209173924U - A kind of stearate quantitative proportioning reaction process units - Google Patents
A kind of stearate quantitative proportioning reaction process units Download PDFInfo
- Publication number
- CN209173924U CN209173924U CN201821555632.4U CN201821555632U CN209173924U CN 209173924 U CN209173924 U CN 209173924U CN 201821555632 U CN201821555632 U CN 201821555632U CN 209173924 U CN209173924 U CN 209173924U
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- China
- Prior art keywords
- storage tank
- utility
- stearate
- control system
- model
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- 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.)
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Abstract
The utility model discloses a kind of stearate quantitative proportioning reaction process units, including liquid alkaline storage tank, stearic acid storage tank, brine reservoir, reaction kettle and control system, the liquid alkaline storage tank, stearic acid storage tank, brine reservoir pass through setting conveyance conduit and are connected to reaction kettle, and suction pump, flowmeter and pneumatic operated valve are fixedly installed on each conveyance conduit, suction pump, flowmeter and pneumatic operated valve are electrically connected with control system, and water tank and storage salt cellar are fixedly connected with outside the brine reservoir.The utility model structure is simple and convenient to operate, and the utility model is fed intake using automatic ration, can not only save stearic acid slice packaging and transportation cost, to reduce the cost of stearate, and artificial, reduction labor intensity can be reduced, and average reduction daily 2 is artificial；The utility model can be improved working efficiency, reduce ingredient and Manual material feeding time, increase product yield about 30%, while loss caused by can reduce because of charge ratio mistake.
Description
Technical field
The utility model relates to stearate technical field of processing equipment, and in particular to a kind of stearate quantitative proportioning is anti-
Answer process units.
Background technique
It is mostly manual operation in the process of production stearate, stearic acid is weighed by determining packet quantity, and liquid alkaline passes through people
It pours into reaction kettle, is passed through after manually weighing with salt, dissolution is driven into reaction kettle after work operation.There is weighing number in manual operation
Amount inaccuracy, the case where leading to abnormal reaction, waste raw material；Water can not be accurately used in course of dissolution, and energy consumption is caused to waste；It is stearic
Acid, which needs to send again after liquid slice packaging to kieserohalosylvite workshop, re-melts use, and salt water needs repeatedly to dissolve in use
Ingredient wastes time, man power and material.High labor cost in entire process, the case where there are energy consumption and material consumption wastes, easily
There is the link of operation error.
Utility model content
The purpose of this utility model is that it is in view of the drawbacks of the prior art and insufficient, a kind of stearate quantitative proportioning is provided
React process units.
A kind of stearate quantitative proportioning reaction life that in order to achieve the above purposes, the technical solution adopted by the utility model is:
Device is produced, innovative point is: including liquid alkaline storage tank, stearic acid storage tank, brine reservoir, reaction kettle and control system, the liquid
Alkali storage tank, stearic acid storage tank, brine reservoir pass through setting conveyance conduit and are connected to reaction kettle, and solid on each conveyance conduit
Suction pump, flowmeter and pneumatic operated valve are set surely, and suction pump, flowmeter and pneumatic operated valve are electrically connected with control system, the salt
Water tank and storage salt cellar are fixedly connected with outside water storage tank.
Further, the control system includes PLC control system and touch operation screen.
After adopting the above structure, the utility model has the beneficial effect that
The utility model structure is simple and convenient to operate, and the utility model is fed intake using automatic ration, can not only be saved hard
Resin acid slice packaging and transportation cost to reduce the cost of stearate, and can reduce artificial, reduction labor intensity,
And average reduction 2 daily is manually；The utility model can be improved working efficiency, reduce ingredient and Manual material feeding time, increase
Product yield about 30%, while loss caused by can reduce because of charge ratio mistake.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Description of symbols:
1 liquid alkaline storage tank, 2 stearic acid storage tanks, 3 brine reservoirs, 4 reaction kettles, 5 conveyance conduits, 6 suction pumps, 7 flowmeters, 8 gas
Dynamic valve, 9 water tanks, 10 storage salt cellars.
Specific embodiment
The utility model will be further described below with reference to the accompanying drawings.
In order to make the purpose of the utility model, technical solutions and advantages more clearly understood, below in conjunction with attached drawing and specifically
Embodiment, the present invention will be further described in detail.It should be appreciated that the specific embodiments described herein are only used
To explain the utility model, it is not used to limit the utility model.
Referring to Fig. 1, a kind of stearate quantitative proportioning reaction process units, including liquid alkaline storage tank 1, stearic acid storage tank 2, salt
Water storage tank 3, reaction kettle 4 and control system, liquid alkaline storage tank 1, stearic acid storage tank 2, brine reservoir 3 pass through setting conveyance conduit 5
It is connected to reaction kettle 4, and suction pump 6, flowmeter 7 and pneumatic operated valve 8 is fixedly installed on each conveyance conduit 5, suction pump 6, stream
Meter 7 and pneumatic operated valve 8 are electrically connected with control system, and water tank 9 and storage salt cellar 10 are fixedly connected with outside brine reservoir 3.Liquid
Alkali is directly from external input to liquid alkaline storage tank 1；Stearic acid is directly inputted into stearic acid storage tank 2, transports again without slice packaging
Kieserohalosylvite workshop；Quantitative Yan Heshui is delivered in brine reservoir 3 is stirred according to production needs by water tank 9 and storage salt cellar 10
It is stand-by afterwards, in use, being fed intake by control system automatic ration.
Control system includes PLC control system and touch operation screen.It can be by the way that liquid alkaline storage be respectively set in touch operation screen
Tank 1, stearic acid storage tank 2, in brine reservoir 3 raw material usage amount, while in process of production to suction pump, flowmeter and pneumatic
Valve carries out chain control, accomplishes quantitative feeding and is automatically stopped charging.
The above is merely intended for describing the technical solutions of the present application, but not for limiting the present application, those of ordinary skill in the art couple
The other modifications or equivalent replacement that the technical solution of the utility model is made, without departing from technical solutions of the utility model
Spirit and scope should all cover in the scope of the claims of the utility model.
Claims (2)
1. a kind of stearate quantitative proportioning reacts process units, it is characterised in that: including liquid alkaline storage tank, stearic acid storage tank, salt
Water storage tank, reaction kettle and control system, the liquid alkaline storage tank, stearic acid storage tank, brine reservoir pass through setting conveyance conduit with
Reaction kettle connection, and suction pump, flowmeter and pneumatic operated valve are fixedly installed on each conveyance conduit, suction pump, flowmeter are gentle
Dynamic valve is electrically connected with control system, and water tank and storage salt cellar are fixedly connected with outside the brine reservoir.
2. a kind of stearate quantitative proportioning according to claim 1 reacts process units, it is characterised in that: the control
System includes PLC control system and touch operation screen.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821555632.4U CN209173924U (en) | 2018-09-21 | 2018-09-21 | A kind of stearate quantitative proportioning reaction process units |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821555632.4U CN209173924U (en) | 2018-09-21 | 2018-09-21 | A kind of stearate quantitative proportioning reaction process units |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209173924U true CN209173924U (en) | 2019-07-30 |
Family
ID=67360122
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821555632.4U Expired - Fee Related CN209173924U (en) | 2018-09-21 | 2018-09-21 | A kind of stearate quantitative proportioning reaction process units |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209173924U (en) |
-
2018
- 2018-09-21 CN CN201821555632.4U patent/CN209173924U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20191125 Address after: Room 102-2, floor 1, block a, building 2, No. 58, Baozhen South Road, Baozhen, Chongming District, Shanghai 202157 (Shanghai Baozhen economic community) Patentee after: Shanghai Chaoling daily chemical products Co.,Ltd. Address before: 226000 No. 1 Dingxin East Road, Dingyan Town, Rugao City, Nantong City, Jiangsu Province Patentee before: NANTONG NOBILE CHEMICALS TECHNOLOGY CO.,LTD. |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190730 Termination date: 20210921 |