CN205628807U - Starch milk pipe clearance system - Google Patents
Starch milk pipe clearance system Download PDFInfo
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- CN205628807U CN205628807U CN201620203091.3U CN201620203091U CN205628807U CN 205628807 U CN205628807 U CN 205628807U CN 201620203091 U CN201620203091 U CN 201620203091U CN 205628807 U CN205628807 U CN 205628807U
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- starch
- starch milk
- latex dust
- centrifugal pump
- water supply
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Abstract
The utility model belongs to the technical field of bioengineering, especially, relate to a starch milk pipe clearance system. Including the starch milk jar, liquefaction regulation jar and centrifugal pump, starch milk jar and liquefaction are adjusted all through starch milk pipe intercommunication between jar and the centrifugal pump, the lower extreme of starch milk pipe is equipped with the compressed gas pipeline, the upper end of starch milk pipe still is equipped with water supply line, the centrifugal pump exit is equipped with the pneumatic valve, all be equipped with the pneumatic valve on compressed gas pipeline and the water supply line. The utility model discloses a mutually supporting, adjusting between compressed gas pipeline, water supply line and the pneumatic valve that starch milk guan shangjia established can weather and thoroughly clear up remaining emulsion and precipitate on the starch milk inside pipe wall fast, has reached simultaneously and has not reduced starch milk concentration, has improved fructose output, has practiced thrift the effect of water resource.
Description
Technical field
This utility model belongs to technical field of bioengineering, particularly relates to a kind of starch latex dust cleaning system.
Background technology
In fructose produces, needing to be provided starch milk by starch workshop, starch milk needs after being transported to fructose workshop
Carrying out a point tank and regulate its parameter, when its point of tank, starch milk pipeline is to connect starch milk tank and liquefaction regulation tank
Tie, but easily cause starch milk during the conveying of point tank and be interrupted conveying, starch milk easily precipitates, and causes shallow lake
Powder blocking of mammary tube, reduces production efficiency, too increases workload.
In prior art, major part uses tap water to be rinsed starch latex dust, because pipeline is oversize, rinses and uses
The water yield is relatively big, causes the starch concentration in liquefaction regulation tank to reduce, increases evaporation, the workload concentrated,
Reduce fructose yield, add energy consumption, waste water resource simultaneously.
Utility model content
This utility model is low for the above-mentioned efficiency existed when clearing up starch latex dust, cleaning is the most thorough and traditional
The problems such as the drawback brought during cleaning, propose a kind of reasonable in design, with low cost and can quickly dry up and thorough
The emulsion remained on end cleaning starch milk inside pipe wall and precipitate, reach not reduce starch concentration, improve
Fructose yield, has saved the effect of water resource.
In order to achieve the above object, the technical solution adopted in the utility model is, this utility model provides one
Kind of starch latex dust cleaning system, including starch milk tank, liquefaction regulation tank and centrifugal pump, described starch milk tank with
All being connected by starch latex dust between liquefaction regulation tank and centrifugal pump, the lower end of described starch latex dust is provided with pressure
Contracting feed channel, the upper end of described starch latex dust is additionally provided with water supply pipe, is provided with gas at described outlet of centrifugal pump
Dynamic valve, described compressed gas pipeline and water supply pipe are equipped with pneumatic operated valve.
As preferably, described compressed gas pipeline and water supply pipe all with starch latex dust connecing.
As preferably, described pneumatic operated valve is that PLC controls pneumatic operated valve.
As preferably, described starch latex dust is stainless steel pipes.
As preferably, the inlet of described centrifugal pump is connected by starch latex dust with the liquid outlet of starch milk tank.
Compared with prior art, advantage of the present utility model and good effect are,
This utility model passes through between compressed gas pipeline, water supply pipe and the pneumatic operated valve added on starch latex dust
Coordinate, regulate, it is possible to quickly dry up and thoroughly clear up emulsion and the precipitate of residual on starch milk inside pipe wall,
Reach not reduce starch concentration, improve fructose yield, also a saving the effect of water resource.
Accompanying drawing explanation
In order to be illustrated more clearly that the technical scheme of this utility model embodiment, in embodiment being described below
The required accompanying drawing used is briefly described, it should be apparent that, the accompanying drawing in describing below is this practicality
Some novel embodiments, for those of ordinary skill in the art, are not paying creative work
Under premise, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
The structural representation of the starch latex dust cleaning system that Fig. 1 provides for embodiment 1；
In the most each figure, 1, starch milk tank；2, centrifugal pump；3, liquefaction regulation tank；4, starch latex dust；
5, water supply pipe；6, compressed gas pipeline；7, centrifugal pump pneumatic operated valve；8, water supply pipe pneumatic operated valve；
9, compressed gas pipeline pneumatic operated valve.
Detailed description of the invention
In order to be more clearly understood that above-mentioned purpose of the present utility model, feature and advantage, below in conjunction with attached
This utility model is described further by figure and embodiment.It should be noted that in the case of not conflicting,
Feature in embodiments herein and embodiment can be mutually combined.
Elaborate a lot of detail in the following description so that fully understanding this utility model, but,
This utility model can be different from other modes described here with employing to be implemented, therefore, and this utility model
It is not limited to the restriction of the specific embodiment of description described below.
Embodiment 1, as it is shown in figure 1, the present embodiment provides a kind of starch latex dust cleaning system, including starch milk
Tank 1, liquefaction regulation tank 3, centrifugal pump 2, between starch milk tank 1, centrifugal pump 2 and liquefaction regulation tank 3 all
Being connected by starch latex dust 4, the inlet of centrifugal pump 2 is connected with the liquid outlet of starch milk tank 1, centrifugal pump
The liquid outlet of 2 is connected with one end of centrifugal pump pneumatic operated valve 7, the other end of centrifugal pump pneumatic operated valve 7 and starch milk
One end of pipe 4 connects, and one end of compressed gas pipeline 6 is connected with one end of compressed gas pipeline pneumatic operated valve 9, pressure
The other end of contracting feed channel pneumatic operated valve 9 and starch latex dust 4 also connect, one end of water supply pipe 5 and tap water
One end of conduit pipe pneumatically valve 8 connects, and the other end of water supply pipe pneumatic operated valve 8 and starch latex dust 4 also connect.
By the setting of compressed gas pipeline 6, compressed gas is utilized to be blown clean by starch latex dust 4 inwall starch emulsion,
Instead of the original flow process directly using tap water to be rinsed such that it is able to quickly dry up and thoroughly clear up shallow lake
The emulsion remained on powder latex dust inwall and precipitate, reached not reduce starch concentration, improves fructose and produces
Amount, also a saving the effect of water resource.
In the present embodiment, owing to starch latex dust 4 internal feed liquid temperature is higher, pressure is relatively big, uses common
The person is easily damaged by Valve controlling, and security reliability is relatively low, therefore in the present embodiment, pneumatic operated valve uses PLC
Controlling, the PLC pneumatic operated valve used is the most commercially available, therefore does not retouches detailed
State its structure.
In the present embodiment, in order to make starch latex dust 4 have good resistance to compression, a shock resistance, therefore starch
Latex dust 4 is stainless steel pipes.
In the present embodiment, water supply pipe 5 and compressed gas pipeline 6 all with starch latex dust 4 connecing, so
Can conveniently use PLC pneumatic operated valve to carry out coordinating, regulating, can fully control tap water and compressed gas turnover,
Facilitate the cleaning of starch latex dust.
During specific works, the starch milk in starch milk tank 1 is beaten to liquefaction regulation tank 3 by centrifugal pump 2, when
When starch milk reaches the liquid level of liquefaction regulation tank 3, send signal, close centrifugal pump 2, simultaneously close off centrifugal
Pump pneumatic operated valve 7, opens compressed gas pipeline pneumatic operated valve 9, and compressed gas enters starch latex dust and closes pressure after 4,3～8 seconds
Contracting feed channel pneumatic operated valve 9, opens water supply pipe pneumatic operated valve 8, and tap water enters starch latex dust 4,2～5 seconds
Rear closedown water supply pipe pneumatic operated valve 8, then open compressed gas pipeline pneumatic operated valve 9, compressed gas enters starch latex dust
Close compressed gas pipeline pneumatic operated valve 9, the signal of centrifugal pump 2 to be launched such as now after 4,3～8 seconds, receive from
After heart pump 2 enabling signal, open centrifugal pump pneumatic operated valve 7, restart centrifugal pump 2 and be operated, under entrance
One circulation process.
By above-mentioned embodiment, it is possible to quickly dry up and thoroughly clear up the emulsion of residual on starch milk inside pipe wall
And precipitate, reach not reduce starch concentration, improve fructose yield, save the effect of water resource.
The above, be only preferred embodiment of the present utility model, is not that this utility model is made it
The restriction of its form, any those skilled in the art possibly also with the disclosure above technology contents in addition
Change or be modified as the Equivalent embodiments of equivalent variations and be applied to other field, but every without departing from this practicality
New technique plan content, according to technical spirit of the present utility model above example is made any simply
Amendment, equivalent variations and remodeling, still fall within the protection domain of technical solutions of the utility model.
Claims (5)
1. a starch latex dust cleaning system, including starch milk tank, liquefaction regulation tank and centrifugal pump, starch milk
All connected by starch latex dust between tank with liquefaction regulation tank and centrifugal pump, it is characterised in that described starch milk
The lower end of pipe is provided with compressed gas pipeline, and the upper end of described starch latex dust is additionally provided with water supply pipe, described centrifugal
It is provided with pneumatic operated valve at pump discharge, described compressed gas pipeline and water supply pipe are equipped with pneumatic operated valve.
Starch latex dust the most according to claim 1 cleaning system, it is characterised in that described compression gas pipe
Road and water supply pipe all with starch latex dust connecing.
Starch latex dust the most according to claim 2 cleaning system, it is characterised in that described pneumatic operated valve is
PLC controls pneumatic operated valve.
Starch latex dust the most according to claim 3 cleaning system, it is characterised in that described starch latex dust
For stainless steel pipes.
Starch latex dust the most according to claim 4 cleaning system, it is characterised in that described centrifugal pump
Inlet is connected by starch latex dust with the liquid outlet of starch milk tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620203091.3U CN205628807U (en) | 2016-03-16 | 2016-03-16 | Starch milk pipe clearance system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620203091.3U CN205628807U (en) | 2016-03-16 | 2016-03-16 | Starch milk pipe clearance system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205628807U true CN205628807U (en) | 2016-10-12 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620203091.3U Active CN205628807U (en) | 2016-03-16 | 2016-03-16 | Starch milk pipe clearance system |
Country Status (1)
| Country | Link |
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| CN (1) | CN205628807U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109907087A (en) * | 2019-02-21 | 2019-06-21 | 沈剑武 | A kind of food production high pressure powder blower with cleaning removal function |
| CN116689412A (en) * | 2023-08-09 | 2023-09-05 | 琥崧智能装备(太仓)有限公司 | Lithium iron phosphate pipeline cleaning system and cleaning control method thereof |
-
2016
- 2016-03-16 CN CN201620203091.3U patent/CN205628807U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109907087A (en) * | 2019-02-21 | 2019-06-21 | 沈剑武 | A kind of food production high pressure powder blower with cleaning removal function |
| CN109907087B (en) * | 2019-02-21 | 2021-03-02 | 浙江子午线质量标准化研究有限公司 | Food production high-pressure powder sprayer with cleaning and dehumidifying functions |
| CN116689412A (en) * | 2023-08-09 | 2023-09-05 | 琥崧智能装备(太仓)有限公司 | Lithium iron phosphate pipeline cleaning system and cleaning control method thereof |
| CN116689412B (en) * | 2023-08-09 | 2023-10-27 | 琥崧智能装备(太仓)有限公司 | Lithium iron phosphate pipeline cleaning system and cleaning control method thereof |
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| GR01 | Patent grant |