CN207734641U - A kind of crystallizing tank of energy uniform decrease in temperature - Google Patents
A kind of crystallizing tank of energy uniform decrease in temperature Download PDFInfo
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- CN207734641U CN207734641U CN201721861865.2U CN201721861865U CN207734641U CN 207734641 U CN207734641 U CN 207734641U CN 201721861865 U CN201721861865 U CN 201721861865U CN 207734641 U CN207734641 U CN 207734641U
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- temperature
- inlet pipe
- outlet pipe
- heat exchanger
- temperature lowering
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Abstract
The utility model provides a kind of crystallizing tank of energy uniform decrease in temperature, including crystallizing tank, chuck, temperature lowering water inlet pipe, temperature lowering water outlet pipe, chuck be located in crystallization tank wall, it is characterised in that：Further include recirculated water inlet pipe, recirculated water outlet pipe and heat exchanger, two water routes built in heat exchanger are connected to by recirculated water inlet pipe and recirculated water outlet pipe between chuck and a wherein water route for heat exchanger, pipeline pump is provided in the recirculated water outlet pipe；Temperature lowering water inlet pipe and temperature lowering water outlet pipe are respectively communicated with another water route of heat exchanger, are arranged on temperature lowering water inlet pipe and start diaphragm valve.The utility model can make the material uniform decrease in temperature in crystallizing tank, avoid crystallizing uneven or even the phenomenon that lump.
Description
Technical field
The utility model belongs to field of chemical equipment, and in particular to a kind of crystallizing tank of energy uniform decrease in temperature.
Background technology
Crystallizing tank is widely used in chemical pharmaceutical industry, especially a kind of glucose crystallization tank, production process
It needs gradual gradient cooling cooling to promote the generation of glucose crystallization, the outer wall covering in glucose crystallization tank is usually used
Cooling water is directly passed through chuck and crystallized in the space between tank wall, carries out gradient by way of manual operation by chuck
Cooling.But the flow of manual operation temperature lowering water is not often accomplished to accurately control, and can not ensure that temperature-fall period gradient carries out, usually
Occur that crystallization is uneven, and crystalline particle problem not of uniform size influences product quality, or even makes to adhere to Portugal on the inner wall of crystallizing tank
Grape sugar lumps, it is difficult to clear up, it is necessary to which clear tank processing caking seriously affects production efficiency.
Invention content
The technical problems to be solved in the utility model is：Overcome the deficiencies of the prior art and provide it is a kind of can uniform decrease in temperature
Crystallizing tank can make the material uniform decrease in temperature in crystallizing tank, avoid crystallizing uneven or even the phenomenon that lump.
Technical solution adopted by the utility model to solve its technical problems is：A kind of crystallizing tank of energy uniform decrease in temperature, packet
Crystallizing tank, chuck, temperature lowering water inlet pipe, temperature lowering water outlet pipe are included, chuck be located in crystallization tank wall, it is characterised in that：Further include following
Between a wherein water route for ring water inlet pipe, recirculated water outlet pipe and heat exchanger, two water routes built in heat exchanger, chuck and heat exchanger
It is connected to recirculated water outlet pipe by recirculated water inlet pipe, pipeline pump is provided in the recirculated water outlet pipe；Temperature lowering water inlet pipe and cooling
Water outlet pipe is respectively communicated with another water route of heat exchanger, is arranged on temperature lowering water inlet pipe and starts diaphragm valve.
Preferably, temperature instrumentation is set on recirculated water inlet pipe or recirculated water outlet pipe.
Compared with prior art, the utility model has the beneficial effects that：
1. adding a heat exchanger, circulation waterway, recirculated water are connected between chuck and a wherein water route for heat exchanger
Road setting pipeline pump, i.e., form a circulation waterway, circulation waterway recycle stream under the action of pipeline pump on the outside of crystallizing tank
It is dynamic；Temperature lowering water is penetrated through in another water route of heat exchanger, by temperature lowering water to circulating water cooling in heat exchanger.Temperature lowering water into
Pneumatic diaphragm control valve is set on water pipe, the flow of temperature lowering water can be regulated and controled by the temperature gradient of restriction, so as to recirculated water
Gradient cooling avoids the drawbacks of manual operation can not accurately control, and ensures that crystallization is uniform, improves product quality；Due to cycle
The uniform decrease in temperature successively that water is stablized prevents glucose crystallization on crystallization top tank structure, without clear tank processing caking, improves production effect
Rate.
2. temperature instrumentation is arranged on circulating water pipeline, the circulating water temperature of crystallization tank wall can be monitored in time, is contributed to
Control the cooling extent of crystallizing tank.
Description of the drawings
Fig. 1 is the utility model principle figure.
In figure label for：
1 crystallizing tank；2 heat exchangers；3 recirculated water inlet pipes；4 recirculated water outlet pipes；5 pneumatic diaphragm control valves；6 pipeline pumps；7 folders
Set；8 temperature lowering water inlet pipes；9 temperature lowering water outlet pipes；10 temperature instrumentations.
Specific implementation mode
Embodiment below in conjunction with the accompanying drawings is described further the utility model：A kind of crystallizing tank of energy uniform decrease in temperature, packet
Include crystallizing tank 1, chuck 7, temperature lowering water inlet pipe 8, temperature lowering water outlet pipe 9, chuck 7 be located in 1 outer wall of crystallizing tank, further include recirculated water into
Between a wherein water route for pipe 3, recirculated water outlet pipe 4 and heat exchanger 2, two water routes built in heat exchanger 2, chuck 7 and heat exchanger 2
It is connected to recirculated water outlet pipe 4 by recirculated water inlet pipe 3, i.e., in the interior water route with heat exchanger 2 of the chuck 7 of 1 outer wall of crystallizing tank
Between form a circulation waterway, pipeline pump 6 is provided in recirculated water outlet pipe 4, on recirculated water inlet pipe 3 or recirculated water outlet pipe 4
Temperature instrumentation 10 is set.
Temperature lowering water inlet pipe 8 and temperature lowering water outlet pipe 9 are respectively communicated with another water route of heat exchanger 2, are arranged on temperature lowering water inlet pipe 8
Pneumatic diaphragm control valve 5.
The operation principle and the course of work of the utility model：
First, the injection cycle in a wherein water route for heat exchanger 2, recirculated water inlet pipe 3, recirculated water outlet pipe 4, chuck 7
Water, under the action of pipeline pump 6, recirculated water is circulated around the outer wall of crystallizing tank 1, and temperature instrumentation is arranged on circulation waterway
10, the circulating water temperature of circulation 1 outer wall of crystallizing tank can be learnt in time.Temperature lowering water is another from 8 inflow heat exchanger 2 of temperature lowering water inlet pipe
Water route, then flowed out by temperature lowering water outlet pipe 9, i.e., temperature lowering water circulates along another water route of heat exchanger 2, is set along temperature lowering water inlet pipe 8
Set pneumatic diaphragm control valve 5, the flow of energy Auto-matching temperature and temperature lowering water.Temperature lowering water and recirculated water are realized in heat exchanger 2
Heat exchange regulates and controls pneumatic diaphragm control valve 5 according to the temperature value of temperature instrumentation 10, and the flow of temperature lowering water matches adjusting therewith, from
And recirculated water gradient uniformity is made to cool down, it realizes the uniform decrease in temperature to crystallizing tank 1, promotes crystallization uniform, glucose is avoided to lump.
Heat exchanger 2, pipeline pump 6 and pneumatic diaphragm control valve 5 belong to the prior art, repeat no more.
The above descriptions are merely preferred embodiments of the present invention, is not to make other forms to the utility model
Limitation, any person skilled in the art is changed or is modified as possibly also with the technology contents of the disclosure above equivalent
The equivalent embodiment of variation.But it is every without departing from the content of the technical scheme of the utility model, the technology according to the utility model is real
Any simple modification, equivalent variations and remodeling, still fall within the guarantor of technical solutions of the utility model made by confrontation above example
Protect range.
Claims (2)
1. a kind of crystallizing tank of energy uniform decrease in temperature, including crystallizing tank, chuck, temperature lowering water inlet pipe, temperature lowering water outlet pipe, chuck be located in
Crystallize tank wall, it is characterised in that：Further include recirculated water inlet pipe, recirculated water outlet pipe and heat exchanger, two water routes built in heat exchanger,
It is connected to by recirculated water inlet pipe and recirculated water outlet pipe between chuck and a wherein water route for heat exchanger, in the recirculated water outlet pipe
It is provided with pipeline pump；Temperature lowering water inlet pipe and temperature lowering water outlet pipe are respectively communicated with another water route of heat exchanger, are set on temperature lowering water inlet pipe
Set startup diaphragm valve.
2. a kind of crystallizing tank of energy uniform decrease in temperature according to claim 1, it is characterised in that：In recirculated water inlet pipe or cycle
Temperature instrumentation is set in water outlet pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721861865.2U CN207734641U (en) | 2017-12-27 | 2017-12-27 | A kind of crystallizing tank of energy uniform decrease in temperature |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721861865.2U CN207734641U (en) | 2017-12-27 | 2017-12-27 | A kind of crystallizing tank of energy uniform decrease in temperature |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207734641U true CN207734641U (en) | 2018-08-17 |
Family
ID=63120186
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721861865.2U Active CN207734641U (en) | 2017-12-27 | 2017-12-27 | A kind of crystallizing tank of energy uniform decrease in temperature |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207734641U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109341551A (en) * | 2018-11-06 | 2019-02-15 | 东旭（昆山）显示材料有限公司 | A kind of optical spacer height-measuring machine |
-
2017
- 2017-12-27 CN CN201721861865.2U patent/CN207734641U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109341551A (en) * | 2018-11-06 | 2019-02-15 | 东旭（昆山）显示材料有限公司 | A kind of optical spacer height-measuring machine |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 255000 Shuangfeng Industrial Park, Zichuan District, Zibo City, Shandong Province Patentee after: Luwei Pharmaceutical Group Co.,Ltd. Address before: 255000 Shuangfeng Industrial Park, Zichuan District, Zibo City, Shandong Province Patentee before: SHANDONG LUWEI PHARMACEUTICAL Co.,Ltd. |