CN214763414U - Evaporation condensation system for recovery system - Google Patents
Evaporation condensation system for recovery system Download PDFInfo
- Publication number
- CN214763414U CN214763414U CN202022791040.6U CN202022791040U CN214763414U CN 214763414 U CN214763414 U CN 214763414U CN 202022791040 U CN202022791040 U CN 202022791040U CN 214763414 U CN214763414 U CN 214763414U
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- Prior art keywords
- heat exchanger
- condensation
- communicated
- recovery system
- water
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- 238000009833 condensation Methods 0.000 title claims abstract description 40
- 230000005494 condensation Effects 0.000 title claims abstract description 40
- 238000011084 recovery Methods 0.000 title claims abstract description 22
- 238000001704 evaporation Methods 0.000 title claims abstract description 14
- 230000008020 evaporation Effects 0.000 title claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 36
- 239000000498 cooling water Substances 0.000 claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 36
- 238000005086 pumping Methods 0.000 claims description 6
- 239000010865 sewage Substances 0.000 claims description 6
- 230000001502 supplementing effect Effects 0.000 claims description 2
- 238000000605 extraction Methods 0.000 abstract description 5
- 230000008676 import Effects 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- 239000002826 coolant Substances 0.000 description 2
- 239000002173 cutting fluid Substances 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000003020 moisturizing effect Effects 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000009931 harmful effect Effects 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to an evaporation condensing system for recovery system includes condensation heat exchanger (1), cartridge pressure transmitter (1.1) and temperature changer (1.2) on the inlet pipeline of the cooling water runner of condensation heat exchanger (1), the import and the vapor source of the condensation gas runner of condensation heat exchanger (1) are linked together, the export of the condensation gas runner of condensation heat exchanger (1) communicates to the top of liquid collecting box (2), has a evacuating device's extraction opening to communicate to the top of liquid collecting box (2) through the pipeline; tuning fork level gauges (2.1) are inserted in the upper portion and the lower portion of the side wall of the liquid collecting box (2). The utility model relates to an evaporation condensing system for recovery system, it adopts the vacuum extraction mode can effectual improvement condensation effect, avoids causing the pollution to the environment.
Description
Technical Field
The utility model relates to an evaporation condensing system for recovery system belongs to environmental protection recovery plant technical field.
Background
At present, in occasions such as semiconductor cutting, the water content of a lubricating coolant such as mortar influences the cutting quality, so that the water content needs to be adjusted, and the water content is generally adjusted by adopting physical adsorption and distillation dehydration modes; however, the physical adsorption method has low efficiency and low loss of cutting fluid, and the distillation dehydration method lacks a special condensing system to treat distilled water vapor, so that the water vapor carrying the solvent such as cutting fluid is directly discharged to the outside, which not only wastes resources, but also has adverse effect on the environment.
Disclosure of Invention
An object of the utility model is to overcome above-mentioned not enough, provide an evaporation condensing system for recovery system, it adopts the vacuum extraction mode can effectual improvement condensation effect, avoids causing the pollution to the environment.
The purpose of the utility model is realized like this:
an evaporation and condensation system for a recovery system comprises a condensation heat exchanger, wherein a pressure transmitter and a temperature transformer are inserted on an inlet pipeline of a cooling water flow channel of the condensation heat exchanger, an inlet of the condensation gas flow channel of the condensation heat exchanger is communicated with a water vapor source, an outlet of the condensation gas flow channel of the condensation heat exchanger is communicated to the top of a liquid collecting tank, and an air suction port of a vacuum pumping device is communicated to the top of the liquid collecting tank through a pipeline; tuning fork level gauges are inserted in the upper portion and the lower portion of the side wall of the liquid collecting box.
The utility model relates to an evaporation condensing system for recovery system, the leakage fluid dram of the lateral wall lower part of collection liquid case communicates to the import of electronic blow-down valve through the pipeline, the export of electronic blow-down valve is carried outward through the delivery pump.
The utility model relates to an evaporative condensation system for recovery system, evacuating device includes two water ring vacuum pumps, and two water ring vacuum pumps's extraction opening communicates to liquid collecting tank through manual valve respectively, and two water ring vacuum pumps's coolant outlet communicates to coil pipe heat exchanger's top inlet behind manual valve respectively, coil pipe heat exchanger's bottom liquid outlet communicates to two water ring vacuum pumps's cooling water import respectively behind manual valve, and is provided with a drain that is linked together with shell side passageway bottom coil pipe heat exchanger, has concatenated electronic blowoff valve on this drain is to the pipeline of external connection.
The utility model relates to an evaporation condensing system for recovery system has concatenated electric control valve and manual control valve respectively on the water inlet of coil pipe heat exchanger's cooling water coil pipe and the delivery port.
The utility model relates to an evaporation condensing system for recovery system, it has temperature transmitter to peg graft on the pipeline that coil pipe heat exchanger bottom liquid outlet and water ring vacuum pump's cooling water inlet are connected.
The utility model relates to an evaporation condensing system for recovery system, it has a moisturizing pipe to peg graft at coil pipe heat exchanger's top, and this moisturizing pipe is linked together with the shell side passageway.
Compared with the prior art, the beneficial effects of the utility model are that:
the utility model discloses a vapor liquefaction after the condensation heat exchanger will distill and guarantee through the evacuating device who links to each other with the collection liquid case that vapor can channel into the condensation heat exchanger smoothly to avoid causing harmful effects to the environment.
Drawings
Fig. 1 is a schematic structural view of an evaporation and condensation system for a recovery system of the present invention.
Wherein:
the device comprises a condensation heat exchanger 1, a liquid collecting tank 2, an electric discharge valve 3 and a delivery pump 4;
a pressure transmitter 1.1 and a temperature changer 1.2;
a tuning fork liquid level meter 2.1;
a water ring vacuum pump 101, a coil heat exchanger 102, a liquid level meter 103, an electric blowdown valve 104 and a temperature transmitter 105.
Detailed Description
Referring to fig. 1, the utility model relates to an evaporation condensing system for recovery system, include condensation heat exchanger 1, cartridge pressure transmitter 1.1 and temperature changer 1.2 on the inlet pipeline of the cooling water runner of condensation heat exchanger 1, the import of the condensation gas runner of condensation heat exchanger 1 is linked together with the vapor source, the export of the condensation gas runner of condensation heat exchanger 1 communicates to the top of header tank 2, has a vacuum extractor's extraction opening to communicate to the top of header tank 2 through the pipeline; tuning fork liquid level meters 2.1 are inserted in the upper part and the lower part of the side wall of the liquid collecting box 2;
further, a liquid outlet at the lower part of the side wall of the liquid collecting tank 2 is communicated to an inlet of an electric discharge valve 3 through a pipeline, and an outlet of the electric discharge valve 3 is discharged to a recovery device through a delivery pump 4;
preferably, the signal lines of the two tuning fork level gauges 2.1 are connected with the control end of the delivery pump 4, the signal lines of the two tuning fork level gauges 2.1 are connected with the control end of the electric drain valve 3, so as to realize automatic control of the liquid level, when the liquid level exceeds the tuning fork level gauge 2.1 positioned at a high position, the tuning fork level gauge 2.1 sends a signal to enable the electric drain valve 3 and the delivery pump 4 to open liquid discharge, and when the liquid level is lower than the tuning fork level gauge 2.1 positioned at a low position, the tuning fork level gauge 2.1 sends a signal to enable the electric drain valve 3 and the delivery pump 4 to stop liquid discharge;
furthermore, the vacuum pumping device comprises two water ring vacuum pumps 101, the pumping outlets of the two water ring vacuum pumps 101 are respectively communicated with the liquid collecting tank 2 through manual valves, the cooling water outlets of the two water ring vacuum pumps 101 are respectively communicated with the top liquid inlet of the coil pipe heat exchanger 102 through manual valves, the bottom liquid outlet of the coil pipe heat exchanger 102 is respectively communicated with the cooling water inlets of the two water ring vacuum pumps 101 through manual valves, the bottom of the coil pipe heat exchanger 102 is provided with a sewage discharge outlet communicated with a shell pass channel, and the pipeline externally connected with the sewage discharge outlet is connected with an electric sewage discharge valve 104 in series; thereby facilitating the pollution discharge of the cooling water of the water ring vacuum pump 101 and ensuring the quality of the cooling water;
preferably, level meters 103 are respectively inserted in the upper part and the lower part of the shell wall of the coil heat exchanger 102, the control lines of the two level meters 103 are connected with the control end of an electric blowdown valve 104, and when the water level of cooling water for a water ring vacuum pump 101 extruded into the shell pass flow channel of the coil heat exchanger 102 is higher than the level meter 103 located at a high position, the electric blowdown valve 104 is opened to start tapping; when the drain is to a level below the level gauge 103, which is at a low level, the motorized blowoff valve 104 is closed.
Further, a water inlet and a water outlet of the cooling water coil of the coil heat exchanger 102 are respectively connected in series with an electric control valve and a manual control valve;
furthermore, a temperature transmitter 105 is inserted into a pipeline connecting a liquid outlet at the bottom of the coil heat exchanger 102 and a cooling water inlet of the water ring vacuum pump 101, and is used for monitoring the temperature of cooling water entering the water ring vacuum pump 101;
furthermore, a water supplementing pipe is inserted into the top of the coil pipe heat exchanger 102 and communicated with the shell pass channel, so that cooling water can be supplemented to the water ring vacuum pump 101 conveniently;
when the cooling device is used, cooling water in the water ring vacuum pump 101 enters the shell pass channel of the coil heat exchanger 102, and cooling water is introduced into the coil in the coil heat exchanger 102 to cool the cooling water in the shell pass channel.
In addition: it should be noted that the above-mentioned embodiment is only a preferred embodiment of the present patent, and any modification or improvement made by those skilled in the art based on the above-mentioned conception is within the protection scope of the present patent.
Claims (6)
1. An evaporation and condensation system for a recovery system is characterized in that: the device comprises a condensation heat exchanger (1), wherein a pressure transmitter (1.1) and a temperature transformer (1.2) are inserted on an inlet pipeline of a cooling water flow channel of the condensation heat exchanger (1), an inlet of a condensation gas flow channel of the condensation heat exchanger (1) is communicated with a water vapor source, an outlet of the condensation gas flow channel of the condensation heat exchanger (1) is communicated to the top of a liquid collecting tank (2), and an air suction port of a vacuum pumping device is communicated to the top of the liquid collecting tank (2) through a pipeline; tuning fork level gauges (2.1) are inserted in the upper portion and the lower portion of the side wall of the liquid collecting box (2).
2. An evaporative condensation system for a recovery system as set forth in claim 1, wherein: and a liquid outlet at the lower part of the side wall of the liquid collecting box (2) is communicated to an inlet of the electric discharge valve (3) through a pipeline, and an outlet of the electric discharge valve (3) is externally conveyed through the conveying pump (4).
3. An evaporative condensation system for a recovery system as set forth in claim 1, wherein: the vacuum pumping device comprises two water ring vacuum pumps (101), wherein the air pumping ports of the two water ring vacuum pumps (101) are communicated to a liquid collecting tank (2) through manual valves respectively, cooling water outlets of the two water ring vacuum pumps (101) are communicated to a top liquid inlet of a coil pipe heat exchanger (102) through the manual valves respectively, a bottom liquid outlet of the coil pipe heat exchanger (102) is communicated to a cooling water inlet of the two water ring vacuum pumps (101) through the manual valves respectively, a sewage draining port communicated with a shell pass channel is arranged at the bottom of the coil pipe heat exchanger (102), and an electric sewage draining valve (104) is connected to an externally connected pipeline in series through the sewage draining port.
4. An evaporative condensation system for a recovery system as set forth in claim 3, wherein: the water inlet and the water outlet of a cooling water coil of the coil heat exchanger (102) are respectively connected with an electric control valve and a manual control valve in series.
5. An evaporative condensation system for a recovery system as set forth in claim 3, wherein: a temperature transmitter (105) is inserted on a pipeline connecting a liquid outlet at the bottom of the coil heat exchanger (102) and a cooling water inlet of the water ring vacuum pump (101).
6. An evaporative condensation system for a recovery system as set forth in claim 3, wherein: and a water supplementing pipe is inserted into the top of the coil heat exchanger (102) and is communicated with the shell pass channel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022791040.6U CN214763414U (en) | 2020-11-27 | 2020-11-27 | Evaporation condensation system for recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022791040.6U CN214763414U (en) | 2020-11-27 | 2020-11-27 | Evaporation condensation system for recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214763414U true CN214763414U (en) | 2021-11-19 |
Family
ID=78709858
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202022791040.6U Active CN214763414U (en) | 2020-11-27 | 2020-11-27 | Evaporation condensation system for recovery system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214763414U (en) |
-
2020
- 2020-11-27 CN CN202022791040.6U patent/CN214763414U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: An evaporative condensation system for a recovery system Effective date of registration: 20220922 Granted publication date: 20211119 Pledgee: Jiangsu Jiangyin Rural Commercial Bank Co.,Ltd. high tech Zone sub branch Pledgor: JIANGYIN DONGWEI RENEWABLE RESOURCES TECHNOLOGY Co.,Ltd. Registration number: Y2022320010539 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20231023 Granted publication date: 20211119 Pledgee: Jiangsu Jiangyin Rural Commercial Bank Co.,Ltd. high tech Zone sub branch Pledgor: JIANGYIN DONGWEI RENEWABLE RESOURCES TECHNOLOGY Co.,Ltd. Registration number: Y2022320010539 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: An evaporative condensation system for recycling systems Effective date of registration: 20231025 Granted publication date: 20211119 Pledgee: Jiangsu Jiangyin Rural Commercial Bank Co.,Ltd. high tech Zone sub branch Pledgor: JIANGYIN DONGWEI RENEWABLE RESOURCES TECHNOLOGY Co.,Ltd. Registration number: Y2023980062692 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right |