CN214763383U - Circulation evaporation reaction kettle system - Google Patents
Circulation evaporation reaction kettle system Download PDFInfo
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- CN214763383U CN214763383U CN202022791057.1U CN202022791057U CN214763383U CN 214763383 U CN214763383 U CN 214763383U CN 202022791057 U CN202022791057 U CN 202022791057U CN 214763383 U CN214763383 U CN 214763383U
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- reaction kettle
- outlet
- communicated
- evaporation
- valve
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 48
- 238000001704 evaporation Methods 0.000 title claims abstract description 34
- 230000008020 evaporation Effects 0.000 title claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000007788 liquid Substances 0.000 claims abstract description 6
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 230000008054 signal transmission Effects 0.000 claims description 3
- 125000004122 cyclic group Chemical group 0.000 claims 6
- 230000018044 dehydration Effects 0.000 abstract description 4
- 238000006297 dehydration reaction Methods 0.000 abstract description 4
- 238000004821 distillation Methods 0.000 abstract description 3
- 239000000463 material Substances 0.000 description 4
- 230000005611 electricity Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000004570 mortar (masonry) Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 239000002173 cutting fluid Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000008676 import 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
- 238000011084 recovery Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
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Abstract
The utility model relates to a circulation evaporation reaction kettle system, a feed inlet (1.2) is arranged on the side wall of the lower part of a reaction kettle (1), a vapor outlet (1.3) is arranged at the highest position of an arc-shaped top cover at the top part of the reaction kettle (1), and a temperature transmitter (1.5) is inserted in the lower part of the side wall of the reaction kettle (1); a discharge port at the bottom of the reaction kettle (1) is communicated with an inlet of a three-way valve (103) through a liquid outlet valve (102) and a delivery pump (2), an outlet of the three-way valve (103) is communicated with an inlet of a medium flow channel of the evaporation heat exchanger (3), a pipeline communicated with the outlet of the medium flow channel of the evaporation heat exchanger (3) is inserted into one end in the reaction kettle (1) and is connected with a shower head (5) with a downward nozzle; a water vapor outlet (1.3) at the top of the reaction kettle (1) is communicated to the negative pressure condenser (4) through a pipeline. The utility model relates to a circulation evaporation reation kettle system, it adopts the distillation dehydration mode to realize the quick adjustment to the moisture content.
Description
Technical Field
The utility model relates to a circulation evaporation reation kettle system, it can be used to adjust cutting fluid moisture content, belongs to environmental protection recovery plant technical field.
Background
In the past, in the occasion of semiconductor cutting and the like, the water content of a lubricating coolant such as mortar affects the cutting quality, therefore, the water content needs to be adjusted, and when the water content is higher, the conventional dehydration method adopts physical adsorption, but the physical adsorption method has low efficiency and has small loss to cutting liquid and the like, so a brand new dehydration system is needed to solve the problems.
Disclosure of Invention
An object of the utility model is to overcome the aforesaid not enough, provide a circulation evaporation reation kettle system, it adopts the distillation dehydration mode to realize the quick adjustment to the moisture content.
The purpose of the utility model is realized like this:
a circulating evaporation reaction kettle system comprises a reaction kettle, wherein limit switches are respectively inserted at the upper part and the lower part of the side wall of the reaction kettle, a feed inlet is formed in the side wall of the lower part of the reaction kettle, a steam outlet is formed in the highest position of an arc-shaped top cover at the top of the reaction kettle, and a temperature transmitter is inserted at the lower part of the side wall of the reaction kettle;
a discharge port at the bottom of the reaction kettle is communicated to an inlet of a three-way valve through a liquid outlet valve and a delivery pump, an outlet of the three-way valve is communicated to an inlet of a medium flow channel of the evaporation heat exchanger, and a pipeline communicated with an outlet of the medium flow channel of the evaporation heat exchanger is inserted into one end of the reaction kettle and connected with a shower head with a downward nozzle; and a water vapor outlet at the top of the reaction kettle is communicated to a negative pressure condenser through a pipeline.
The utility model relates to a circulation evaporation reation kettle system, be provided with flange connection dish on the vapor outlet at reation kettle top.
The utility model relates to a circulation evaporation reation kettle system, a governing valve has concatenated on evaporation heat exchanger's the steam runner import.
The utility model relates to a circulation evaporation reation kettle system, the governing valve is temperature regulating valve.
The utility model relates to a circulation evaporation reation kettle system, reation kettle's lateral wall upper portion is pegged graft and is had a broken empty valve.
The utility model relates to a circulation evaporation reation kettle system, the last pump that has concatenated of charge-in pipeline on reation kettle's the feed inlet, two limit switch all are connected with the control end electricity of pump.
The utility model relates to a circulation evaporation reation kettle system, it has the negative pressure changer to peg graft on reation kettle's the top arc top cap, and the signal transmission line of negative pressure changer is connected with an alarm device looks electricity.
Compared with the prior art, the beneficial effects of the utility model are that:
the utility model discloses a circulation distillation mode realizes the regulation to the moisture content, and realizes the contactless circulation heating to materials such as mortar through the heat exchanger, and safe and reliable and energy consumption are lower, have positive environmental protection benefit.
Drawings
Fig. 1 is a schematic diagram of a circulation evaporation reaction kettle system of the utility model.
Wherein:
the device comprises a reaction kettle 1, a delivery pump 2, an evaporation heat exchanger 3, a negative pressure condenser 4 and a shower head 5;
a limit switch 1.1, a feed inlet 1.2, a vapor outlet 1.3, a negative pressure transmitter 1.4 and a temperature transmitter 1.5;
a vacuum breaking valve 101, a liquid outlet valve 102, a three-way valve 103 and a regulating valve 104.
Detailed Description
Referring to fig. 1, the utility model relates to a circulation evaporation reaction kettle system, which comprises a reaction kettle 1, wherein limit switches 1.1 are respectively inserted into the upper part and the lower part of the side wall of the reaction kettle 1, a feed inlet 1.2 is arranged on the side wall of the lower part of the reaction kettle 1, a steam outlet 1.3 is arranged at the highest position of an arc top cover at the top of the reaction kettle 1, and a temperature transmitter 1.5 is inserted into the lower part of the side wall of the reaction kettle 1;
a discharge port at the bottom of the reaction kettle 1 is communicated with an inlet of a three-way valve 103 through a liquid outlet valve 102 and a delivery pump 2, an outlet of the three-way valve 103 is communicated with an inlet of a medium flow channel of the evaporation heat exchanger 3, a pipeline communicated with an outlet of the medium flow channel of the evaporation heat exchanger 3 is inserted into one end of the reaction kettle 1, and a shower head 5 with a downward nozzle is connected with the pipeline; a water vapor outlet 1.3 at the top of the reaction kettle 1 is communicated to a negative pressure condenser 4 through a pipeline;
further, a flange connecting disc is arranged on a water vapor outlet 1.3 at the top of the reaction kettle 1;
further, an adjusting valve 104 is connected in series to an inlet of the steam flow channel of the evaporation heat exchanger 3, preferably, the adjusting valve 104 is a temperature adjusting valve, and the opening degree can be automatically adjusted according to the temperature;
further, an air break valve 101 is inserted into the upper portion of the side wall of the reaction kettle 1, and when the water content of the material in the reaction kettle 1 reaches the standard, vacuum negative pressure is released through the air break valve 101, so that normal material conveying is facilitated;
further, a feed pipeline on a feed port 1.2 of the reaction kettle 1 is connected with a delivery pump in series, and two limit switches 1.1 are electrically connected with a control end of the delivery pump, so that automatic material level control is realized conveniently;
further, a negative pressure transmitter 1.4 is inserted on the arc-shaped top cover at the top of the reaction kettle 1, and a signal transmission line of the negative pressure transmitter 1.4 is electrically connected with an alarm device, so that when the condition that the pressure in the reaction kettle 1 is too low or too high is detected, an alarm can be given in time;
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 (7)
1. A circulation evaporation reation kettle system which characterized in that: the reaction kettle comprises a reaction kettle (1), wherein limit switches (1.1) are respectively inserted at the upper part and the lower part of the side wall of the reaction kettle (1), a feeding hole (1.2) is formed in the side wall of the lower part of the reaction kettle (1), a steam outlet (1.3) is formed in the highest position of an arc-shaped top cover at the top of the reaction kettle (1), and a temperature transmitter (1.5) is inserted at the lower part of the side wall of the reaction kettle (1);
a discharge port at the bottom of the reaction kettle (1) is communicated with an inlet of a three-way valve (103) through a liquid outlet valve (102) and a delivery pump (2), an outlet of the three-way valve (103) is communicated with an inlet of a medium flow channel of the evaporation heat exchanger (3), a pipeline communicated with the outlet of the medium flow channel of the evaporation heat exchanger (3) is inserted into one end in the reaction kettle (1) and is connected with a shower head (5) with a downward nozzle; a water vapor outlet (1.3) at the top of the reaction kettle (1) is communicated to the negative pressure condenser (4) through a pipeline.
2. A cyclic evaporation reactor system according to claim 1, wherein: and a flange connecting disc is arranged on a steam outlet (1.3) at the top of the reaction kettle (1).
3. A cyclic evaporation reactor system according to claim 1, wherein: and an adjusting valve (104) is connected in series with the steam runner inlet of the evaporation heat exchanger (3).
4. A cyclic evaporation reactor system according to claim 3, wherein: the regulating valve (104) is a temperature regulating valve.
5. A cyclic evaporation reactor system according to claim 1, wherein: an air break valve (101) is inserted into the upper part of the side wall of the reaction kettle (1).
6. A cyclic evaporation reactor system according to claim 1, wherein: a feed pipeline on a feed port (1.2) of the reaction kettle (1) is connected with a delivery pump in series, and the two limit switches (1.1) are electrically connected with the control end of the delivery pump.
7. A cyclic evaporation reactor system according to claim 1, wherein: the top arc-shaped top cover of the reaction kettle (1) is inserted with a negative pressure transmitter (1.4), and a signal transmission line of the negative pressure transmitter (1.4) is electrically connected with an alarm device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022791057.1U CN214763383U (en) | 2020-11-27 | 2020-11-27 | Circulation evaporation reaction kettle system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022791057.1U CN214763383U (en) | 2020-11-27 | 2020-11-27 | Circulation evaporation reaction kettle system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214763383U true CN214763383U (en) | 2021-11-19 |
Family
ID=78709871
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202022791057.1U Active CN214763383U (en) | 2020-11-27 | 2020-11-27 | Circulation evaporation reaction kettle system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214763383U (en) |
-
2020
- 2020-11-27 CN CN202022791057.1U patent/CN214763383U/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 | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A Circulating Evaporation Reactor 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 |
|
| PC01 | Cancellation 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 |
|
| PE01 | Entry into force 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: A Circulating Evaporation Reactor System 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 |