CN214250679U - Spiral plate type heat exchanger for pigment processing process - Google Patents
Spiral plate type heat exchanger for pigment processing process Download PDFInfo
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- CN214250679U CN214250679U CN202023181692.4U CN202023181692U CN214250679U CN 214250679 U CN214250679 U CN 214250679U CN 202023181692 U CN202023181692 U CN 202023181692U CN 214250679 U CN214250679 U CN 214250679U
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- organic liquid
- heat exchanger
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- steam inlet
- condensed water
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Abstract
The utility model discloses a spiral plate heat exchanger for pigment processing process, which comprises a steam inlet, wherein the upper end of the steam inlet is fixedly provided with an exhaust port, the right end of the steam inlet is fixedly provided with an organic liquid outlet, the upper end of the organic liquid outlet is fixedly provided with an organic liquid inlet, the lower end of the steam inlet is fixedly provided with a condensed water outlet, the lower end of the organic liquid outlet is fixedly provided with a drain outlet, organic liquid is led in through the organic liquid inlet, the organic liquid flows spirally in the heat exchanger, the condensed water and the organic liquid are kept horizontally parallel, the condensed water and the organic liquid synchronously flow in the spiral heat exchanger, the flowing time of the condensed water and the organic liquid is increased, the steam heat can be greatly absorbed by the condensed water and the organic liquid, then the condensed water is led out through the condensed water outlet, the organic liquid is led out from the organic liquid outlet, and the cooled steam is led out through the exhaust port, the drain can discharge the inside spot of heat exchanger, the inside clean and tidy degree of guarantee heat exchanger.
Description
Technical Field
The utility model relates to a heat exchanger correlation technique field specifically is a spiral plate heat exchanger that pigment course of working used.
Background
The heat exchanger (heat exchanger) is a device for transferring partial heat of hot fluid to cold fluid, also called heat exchanger, and plays an important role in chemical industry, petroleum industry, power industry, food industry and other industrial production, and the heat exchanger can be used as heater, cooler, condenser, evaporator and reboiler in chemical industry production, and has wide application.
Most heat exchangers have low working efficiency at present, and when partial heat of hot fluid is transferred to cold fluid, the heat is easy to lose greatly, so that the heat received by the cold fluid is reduced.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a spiral plate heat exchanger that pigment course of working used to solve the problem that proposes among the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme:
the utility model provides a spiral plate heat exchanger that pigment course of working used, includes steam inlet, the fixed gas vent that is provided with in steam inlet upper end, the fixed organic liquid outlet that is provided with of steam inlet right-hand member, the fixed organic liquid import that is provided with in organic liquid outlet upper end, the fixed comdenstion water export that is provided with of steam inlet lower extreme, the fixed drain that is provided with of organic liquid outlet lower extreme.
Preferably, the steam inlet and the organic liquid outlet are in parallel symmetry.
Preferably, the sewage draining exit and the exhaust port are both arranged outside the heat exchanger, and the sewage draining exit and the exhaust port are perpendicular to the heat exchanger.
Preferably, the condensate water outlet fixedly connected with the lower end of the heat exchanger is rectangular in shape and structure, and the condensate water outlet and the heat exchanger are vertically installed.
Preferably, the condensed water outlet and the organic liquid inlet are kept horizontally parallel.
Preferably, the steam inlet and the organic liquid outlet are symmetrically arranged.
Compared with the prior art, the beneficial effects of the utility model are that: leading-in hot steam through steam inlet, through the leading-in organic liquid of organic liquid import, organic liquid is the heliciform flow in the heat exchanger, the comdenstion water keeps the level parallel with organic liquid, the comdenstion water flows with organic liquid in the inside synchronization of heat exchanger that is the heliciform, it is long when having increased comdenstion water and organic liquid flow, let the steam heat can be absorbed by comdenstion water and organic liquid by a wide margin, the export of rethread condensate water is derived, organic liquid is derived from organic liquid export, refrigerated steam passes through the gas vent and derives, the inside spot of heat exchanger can be discharged to the drain, guarantee the inside finishment of heat exchanger.
Drawings
Fig. 1 is a schematic front view of a spiral plate heat exchanger used in the pigment processing process of the present invention;
fig. 2 is a schematic view of a top view structure of a spiral plate heat exchanger used in the pigment processing process.
In the figure: 1. a steam inlet; 2. a condensed water outlet; 3. an organic liquid inlet; 4. an organic liquid outlet; 5. a sewage draining outlet; 6. and (7) an exhaust port.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-2, the present invention provides a technical solution: the utility model provides a spiral plate heat exchanger that pigment course of working used, includes steam inlet 1, the fixed gas vent 6 that is provided with in 1 upper end of steam inlet, the fixed organic liquid export 4 that is provided with of 1 right-hand member of steam inlet, the fixed organic liquid import 3 that is provided with in 4 upper ends of organic liquid export, the fixed comdenstion water export 2 that is provided with of 1 lower extreme of steam inlet, the fixed drain 5 that is provided with of 4 lower extremes of organic liquid export.
The steam inlet 1 and the organic liquid outlet 4 are kept in parallel symmetry.
The sewage draining exit 5 and the exhaust port 6 are both arranged outside the heat exchanger, and the sewage draining exit 5 and the exhaust port 6 are perpendicular to the heat exchanger.
The condensate outlet 2 fixedly connected with the lower end of the heat exchanger is rectangular in shape, and the condensate outlet 2 and the heat exchanger are vertically installed.
The condensed water outlet 2 and the organic liquid inlet 3 are kept horizontally parallel.
The steam inlet 1 and the organic liquid outlet 4 are symmetrically arranged.
What need explain, the utility model relates to a spiral plate heat exchanger that pigment course of working used, through 1 leading-in hot steam of steam inlet, through 3 leading-in organic liquids of organic liquid import, organic liquid is the heliciform in the heat exchanger and flows, the comdenstion water keeps the level parallel with organic liquid, the comdenstion water flows with organic liquid in the inside synchronization of heat exchanger that is the heliciform, it is long when comdenstion water and organic liquid flow have been increased, let the steam heat can be absorbed by comdenstion water and organic liquid by a wide margin, rethread condensation water export 2 derives, organic liquid is derived from organic liquid outlet 4, refrigerated steam passes through gas vent 6 and derives, the inside spot of heat exchanger can be discharged to drain 5, the inside finishment of guarantee heat exchanger.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. The utility model provides a spiral plate heat exchanger that pigment course of working used which characterized in that: the device comprises a steam inlet (1), wherein an exhaust port (6) is fixedly arranged at the upper end of the steam inlet (1), an organic liquid outlet (4) is fixedly arranged at the right end of the steam inlet (1), an organic liquid inlet (3) is fixedly arranged at the upper end of the organic liquid outlet (4), a condensed water outlet (2) is fixedly arranged at the lower end of the steam inlet (1), and a sewage draining outlet (5) is fixedly arranged at the lower end of the organic liquid outlet (4).
2. A spiral plate heat exchanger for a pigment processing process according to claim 1, wherein: the steam inlet (1) and the organic liquid outlet (4) are kept in parallel symmetry.
3. A spiral plate heat exchanger for a pigment processing process according to claim 1, wherein: and the sewage draining port (5) and the exhaust port (6) are arranged outside the heat exchanger, and the sewage draining port (5) and the exhaust port (6) are vertically arranged with the heat exchanger.
4. A spiral plate heat exchanger for a pigment processing process according to claim 3, wherein: the condensate outlet (2) fixedly connected with the lower end of the heat exchanger is rectangular in shape and structure, and the condensate outlet (2) and the heat exchanger are vertically installed.
5. A spiral plate heat exchanger for a pigment processing process according to claim 1, wherein: the condensed water outlet (2) and the organic liquid inlet (3) are kept horizontally parallel.
6. A spiral plate heat exchanger for a pigment processing process according to claim 1, wherein: the steam inlet (1) and the organic liquid outlet (4) are symmetrically arranged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202023181692.4U CN214250679U (en) | 2020-12-25 | 2020-12-25 | Spiral plate type heat exchanger for pigment processing process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202023181692.4U CN214250679U (en) | 2020-12-25 | 2020-12-25 | Spiral plate type heat exchanger for pigment processing process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214250679U true CN214250679U (en) | 2021-09-21 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202023181692.4U Active CN214250679U (en) | 2020-12-25 | 2020-12-25 | Spiral plate type heat exchanger for pigment processing process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214250679U (en) |
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2020
- 2020-12-25 CN CN202023181692.4U patent/CN214250679U/en active Active
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