CN217612964U - Chemical industry is high-efficient condenser device for distillation - Google Patents
Chemical industry is high-efficient condenser device for distillation Download PDFInfo
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- CN217612964U CN217612964U CN202221552735.1U CN202221552735U CN217612964U CN 217612964 U CN217612964 U CN 217612964U CN 202221552735 U CN202221552735 U CN 202221552735U CN 217612964 U CN217612964 U CN 217612964U
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- cooling chamber
- temperature water
- liquid separator
- water cooling
- low temperature
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Abstract
The utility model provides a chemical industry is high-efficient condenser device for distillation, the special card of phase lies in: the device comprises a normal-temperature water cooling chamber, a low-temperature water cooling chamber and a gas-liquid separator, wherein the normal-temperature water cooling chamber is arranged at the upper end of the low-temperature water cooling chamber, the gas-liquid separator is arranged at the lower end of the low-temperature water cooling chamber, and a first pore plate is arranged at the upper end of the normal-temperature water cooling chamber; the coil pipe is arranged in the low-temperature water cooling chamber, so that the temperature can be completely reduced, and the coil pipe does not overflow when all the coil pipe reaches a temperature below the boiling point of the coil pipe; the flow rate of the two-stage cooling water can be adjusted according to the boiling point of the organism by the two-stage cooling, so that the energy consumption is effectively saved; and the gas-liquid separator is integrated, so that the cost of the independent gas-liquid separator is saved, and the installation cost is also reduced.
Description
Technical Field
The utility model relates to a technical field is retrieved in the reation kettle distillation of chemical production in-process, specifically is a chemical industry distillation uses high-efficient condenser device.
Background
In the chemical production process, the organic solvent is distilled and recovered by a reaction kettle; the process has higher requirements on the condenser, and the speed and the recovery efficiency of the distillation process are two important indexes; currently, the recovery efficiency of the organic solvent is about 88% for the high boiling point (more than 80 ℃) and about 70% for the low boiling point (less than 60 ℃); a large amount of organic solvent gas which cannot be cooled is dissipated into the air, so that the environment is seriously polluted, and the safety and health of operators are influenced; and meanwhile, the method causes great waste to factories.
SUMMERY OF THE UTILITY MODEL
The utility model provides a technical problem provide a chemical industry is high-efficient condenser device for distillation to solve the problem that proposes in the above-mentioned background art.
The utility model provides a technical problem adopt following technical scheme to realize: the utility model provides a chemical industry is high-efficient condenser device for distillation which characterized in that: including normal atmospheric temperature water cooling chamber, low temperature water cooling chamber and vapour and liquid separator, normal atmospheric temperature water cooling chamber set up the upper end at the low temperature water cooling chamber, vapour and liquid separator set up the lower extreme at the low temperature water cooling chamber, the upper end of normal atmospheric temperature water cooling chamber be provided with first orifice plate, normal atmospheric temperature water cooling chamber and low temperature water cooling chamber between be provided with the second orifice plate, low temperature water cooling chamber lower extreme and vapour and liquid separator upper end between be provided with the third orifice plate.
Further, the upper end of normal atmospheric temperature water cooling chamber be provided with the material import, material import and stills distillation exit linkage, normal atmospheric temperature water cooling chamber one side top be provided with the circulating water shell side import, normal atmospheric temperature water cooling chamber one side below be provided with the circulating water shell side export, circulating water shell side import and circulating water access connection, circulating water shell side mouth be connected with the circulating water return opening.
Furthermore, one side top of low temperature water cooling chamber be provided with the refrigerated water import, low temperature water cooling chamber's opposite side below be provided with the refrigerated water export, the refrigerated water import be connected with low temperature water import, the refrigerated water export return connection with low temperature water.
Further, the lower extreme of vapour and liquid separator be provided with the material export, one side top of vapour and liquid separator be provided with vapour and liquid separator gas phase mouth, the material export with receive a jar mouth and be connected, vapour and liquid separator gas phase mouth and tail gas absorption mouth be connected.
Furthermore, a lifting lug is arranged on the second pore plate.
Furthermore, the room temperature water cooling chamber in be provided with the winding pipe, the low temperature water cooling chamber in be provided with the coiler.
Compared with the prior art, the beneficial effects of the utility model are that: the utility model can rapidly cool the organism gas by arranging the winding pipe in the normal temperature water cooling chamber, and the temperature difference between the two is controlled within 100 ℃, so that the device is not damaged by overlarge temperature difference; the coil pipe is arranged in the low-temperature water cooling chamber, so that the temperature can be completely reduced, and the coil pipe does not overflow when all the coil pipe reaches a temperature below the boiling point of the coil pipe; the flow rate of the two-stage cooling water can be adjusted according to the boiling point of the organism by the two-stage cooling, so that the energy consumption is effectively saved; and the gas-liquid separator is integrated, so that the cost of the independent gas-liquid separator is saved, and the installation cost is also reduced.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a schematic cross-sectional view of AA of the present invention.
Fig. 3 is a schematic cross-sectional view of BB surface of the present invention.
In the figure: 1-a normal temperature water cooling chamber; 2-a low-temperature water cooling chamber; 3-a gas-liquid separator; 4-a first orifice plate; 5-a second orifice plate; 6-third orifice plate; 7-lifting lugs; 8-material inlet; 9-material outlet; 10-inlet of shell pass of circulating water; 11-circulating water shell pass outlet; 12-chilled water inlet; 13-outlet of chilled water; 14-gas phase outlet for gas-liquid separation.
Detailed Description
In order to make the technical means, the creative features, the purpose and the efficacy of the present invention easily understood and appreciated, the present invention will be further explained with reference to the specific drawings, and in the description of the present invention, it should be noted that unless otherwise specified and limited, the terms "mounted", "connected" and "connected" should be understood broadly, for example, they may be fixed connection, detachable connection, or integrally connected, mechanically connected or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements.
As shown in fig. 1-3, a chemical industry is high-efficient condenser device for distillation, including normal atmospheric temperature water cooling chamber 1, low temperature water cooling chamber 2 and vapour and liquid separator 3, normal atmospheric temperature water cooling chamber 1 set up the upper end at low temperature water cooling chamber 2, vapour and liquid separator 3 set up the lower extreme at low temperature water cooling chamber 2, the upper end of normal atmospheric temperature water cooling chamber 1 be provided with first orifice plate 4, normal atmospheric temperature water cooling chamber 1 and low temperature water cooling chamber 2 between be provided with second orifice plate 5, 3 upper ends of low temperature water cooling chamber 2 lower extremes and vapour and liquid separator between be provided with third orifice plate 6.
Further, the upper end of normal temperature water cooling chamber 1 be provided with material import 8, material import 8 and stills distillation exit linkage, 1 one side top of normal temperature water cooling chamber be provided with circulating water shell side import 10, 1 one side below of normal temperature water cooling chamber be provided with circulating water shell side export, circulating water shell side import 10 and circulating water access connection, circulating water shell side mouth 11 be connected with the circulating water return opening.
Further, one side top of low temperature water cooling chamber 2 be provided with refrigerated water import 12, the opposite side below of low temperature water cooling chamber 2 be provided with refrigerated water export 13, refrigerated water import 12 and low temperature water access connection, refrigerated water export 13 and low temperature water return the mouth and be connected.
Further, the lower extreme of vapour and liquid separator 3 be provided with material export 9, one side top of vapour and liquid separator 3 be provided with vapour and liquid separator gas phase mouth 14, material export 9 with receive a jar mouth and be connected, vapour and liquid separator gas phase mouth 14 be connected with the tail gas absorption mouth.
Furthermore, a lifting lug 7 is arranged on the second orifice plate 5.
Further, the room temperature water cooling chamber 1 in be provided with the winding pipe for cool down rapidly, low temperature water cooling chamber 2 in be provided with the coil pipe for cool down once more.
The normal temperature water cooling chamber 1 of the utility model is made of stainless steel winding pipes, and the normal temperature water cooling chamber 1 is welded with the first orifice plate 4 and the second orifice plate 5 to form a closed structure; the organisms are initially cooled by the tube pass; circulating water is introduced from a circulating water shell pass inlet 10, flows out from a circulating water shell pass outlet 11 and flows away from the shell pass; the low-temperature water cooling chamber 2 is made of stainless steel coil pipes, and the low-temperature water cooling chamber 2 is connected with a chilled water inlet 12 and a chilled water outlet 13 to form a closed structure; the organisms cooled in the previous step move to the shell side and are further cooled; low-temperature water is introduced from a chilled water inlet 12, and flows out from a chilled water outlet 13 to enter a pipe pass; the organism reaches the gas-liquid separator after being cooled twice, and flows out from the material outlet 9, the utility model can rapidly cool the organism gas by arranging the winding pipe in the normal temperature water cooling chamber, and the two temperature differences are controlled within 100 ℃, so that the equipment cannot be damaged due to the overlarge temperature difference; the coil pipe is arranged in the low-temperature water cooling chamber, so that the temperature can be completely reduced, and the coil pipe does not overflow when all the coil pipe reaches a temperature below the boiling point of the coil pipe; the flow rate of the two-stage cooling water can be adjusted according to the boiling point of the organism by the two-stage cooling, so that the energy consumption is effectively saved; and the gas-liquid separator is integrated, so that the cost of the separate gas-liquid separator is saved, and the installation cost is also reduced.
The basic principles and the main features of the invention and the advantages of the invention have been shown and described above. It will be understood by those skilled in the art that the present invention is not limited to the above embodiments, and that the foregoing embodiments and descriptions are provided only to illustrate the principles of the present invention without departing from the spirit and scope of the present invention. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (6)
1. The utility model provides a chemical industry is high-efficient condenser device for distillation which characterized in that: including normal atmospheric temperature cooling chamber (1), low temperature cooling chamber (2) and vapour and liquid separator (3), normal atmospheric temperature cooling chamber (1) set up the upper end in low temperature cooling chamber (2), vapour and liquid separator (3) set up the lower extreme in low temperature cooling chamber (2), the upper end of normal atmospheric temperature cooling chamber (1) be provided with first orifice plate (4), normal atmospheric temperature cooling chamber (1) and low temperature cooling chamber (2) between be provided with second orifice plate (5), low temperature cooling chamber (2) lower extreme and vapour and liquid separator (3) upper end between be provided with third orifice plate (6).
2. The high-efficiency condenser device for chemical distillation as claimed in claim 1, wherein: the upper end of normal atmospheric temperature water cooling chamber (1) be provided with material import (8), material import (8) and stills distillation exit linkage, normal atmospheric temperature water cooling chamber (1) one side top be provided with circulating water shell side import (10), normal atmospheric temperature water cooling chamber (1) one side below be provided with the export of circulating water shell side, circulating water shell side import (10) and circulating water access connection, circulating water shell side mouth (11) return the mouth with the circulating water and be connected.
3. The high-efficiency condenser device for chemical distillation as claimed in claim 1, wherein: one side top of low temperature water cooling chamber (2) be provided with refrigerated water import (12), the opposite side below of low temperature water cooling chamber (2) be provided with refrigerated water export (13), refrigerated water import (12) be connected with low temperature water import, refrigerated water export (13) return mouthful with low temperature water and be connected.
4. The high-efficiency condenser device for chemical distillation as claimed in claim 1, wherein: the lower extreme of vapour and liquid separator (3) be provided with material export (9), one side top of vapour and liquid separator (3) be provided with vapour and liquid separator gas phase mouth (14), material export (9) be connected with receiving a jar mouth, vapour and liquid separator gas phase mouth (14) be connected with tail gas absorption mouth.
5. The high-efficiency condenser device for chemical distillation as claimed in claim 1, wherein: and a lifting lug (7) is arranged on the second pore plate (5).
6. The high-efficiency condenser device for chemical distillation as claimed in claim 1, wherein: the normal temperature water cooling chamber (1) in be provided with the winding pipe, low temperature water cooling chamber (2) in be provided with the coil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221552735.1U CN217612964U (en) | 2022-06-21 | 2022-06-21 | Chemical industry is high-efficient condenser device for distillation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221552735.1U CN217612964U (en) | 2022-06-21 | 2022-06-21 | Chemical industry is high-efficient condenser device for distillation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217612964U true CN217612964U (en) | 2022-10-21 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202221552735.1U Active CN217612964U (en) | 2022-06-21 | 2022-06-21 | Chemical industry is high-efficient condenser device for distillation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217612964U (en) |
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2022
- 2022-06-21 CN CN202221552735.1U patent/CN217612964U/en active Active
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