CN213375210U - Phenyl chlorosilane synthesis reaction gas condensing device - Google Patents
Phenyl chlorosilane synthesis reaction gas condensing device Download PDFInfo
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- CN213375210U CN213375210U CN202021808912.9U CN202021808912U CN213375210U CN 213375210 U CN213375210 U CN 213375210U CN 202021808912 U CN202021808912 U CN 202021808912U CN 213375210 U CN213375210 U CN 213375210U
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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
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Abstract
The utility model relates to a phenyl chlorosilane synthesis reaction gas condensing equipment, including heat exchanger and conduction oil level groove, heat exchanger divide into first heat exchange area and second heat exchange area, be provided with the closing plate between first heat exchange area and the second heat exchange area, be connected through the connecting pipe between first heat exchange area and the second heat exchange area, install the flow valve on the connecting pipe, first folding pipe has been distributed in the first heat exchange area, the outer wall in first heat exchange area is passed at the both ends of first folding pipe, the outer wall in second heat exchange area has been distributed to the second folding pipe in the second heat exchange area, the outer wall in second heat exchange area is passed at second folding pipe both ends, first heat exchange area is located the upper portion in second heat exchange area, first heat exchange area passes through the pipeline and is connected with conduction oil level groove. The utility model discloses the problem of the temperature that has avoided direct gas pipe and liquid's heat exchange to bring is difficult to control uses a cooling arrangement to reach the purpose of gas liquefaction and liquid heating simultaneously.
Description
Technical Field
The utility model relates to a chemical industry high temperature gas condenser equipment technical field, concretely relates to phenyl chlorosilane synthesis reaction gas condensing equipment.
Background
In the chemical industry field at present, a water cooling mode is generally adopted in a gas condensation mode, the cost is low, and the efficiency is high. However, when high-temperature gas with the temperature of more than 200 ℃ is cooled, the requirement on water quality is high, when water with general water quality condenses high-temperature liquid, cooling water at the inlet of a high-temperature gas condenser can be partially gasified, so that a pipe wall or the inner wall of a shell at the position is greatly scaled, the heat exchange efficiency is reduced, production stop is directly caused in severe cases, and when a water-cooled condenser is adopted, the heat of a cooled substance enters circulating water and is directly diffused into the atmosphere from a water cooling tower, and the reaction heat generated by the reaction cannot be recycled.
SUMMERY OF THE UTILITY MODEL
For solving the problem that exists among the prior art, the utility model provides a phenyl chlorosilane synthesis reaction gas condensing equipment, specific technical scheme is as follows:
the utility model provides a phenyl chlorosilane synthesis reaction gas condensing equipment, includes heat exchanger (1) and conduction oil tank (2), heat exchanger (1) divide into first heat exchange district (101) and second heat exchange district (102), be provided with between first heat exchange district (101) and second heat exchange district (102) closing plate (103), first heat exchange district (101) and second heat exchange district (102) between be connected through connecting pipe (3), connecting pipe (3) on install flow valve (4), first heat exchange district (101) in distribute first folding pipe (5), the both ends of first folding pipe (5) pass the outer wall of first heat exchange district (101), second heat exchange district (102) in distribute second folding pipe (6), second folding pipe (6) both ends pass the outer wall of second heat exchange district (102),
the first heat exchange area (101) is positioned at the upper part of the second heat exchange area (102), and the first heat exchange area (101) is connected with the heat conducting oil level groove (2) through a pipeline.
Furthermore, a spraying pipeline (7) is arranged on the top surface of the first heat exchange area (101), a plurality of spray heads (8) are arranged on the spraying pipeline (7), and the spray heads (8) extend into the first heat exchange area (101) and are connected with the top surface wall of the first heat exchange area (101) in a sealing mode.
Furthermore, a liquid outlet (9) is formed in the bottom surface of the second heat exchange area (102), the liquid outlet (9) is connected with a circulating pump (10) through a pipeline, and the circulating pump (10) is connected with the bottom surface of the heat conduction oil level groove (2) through a pipeline, so that circulation of heat conduction oil is realized.
Furthermore, the first heat exchange area (101) and the second heat exchange area (102) are respectively provided with a temperature detector (11), the temperature detectors (11) are electrically connected with a display screen (12) arranged at a lower part, so that the temperature is monitored, and the working conditions of a flow valve and a circulating pump are adjusted according to the displayed temperature, so that the speed and the efficiency of heat exchange are controlled.
The utility model has the advantages that: the utility model provides a cooling device uses the cooling oil to cool off, has also avoided the problem that the temperature that direct gas pipe and the heat exchange of liquid brought is difficult to the control, has used a cooling arrangement to reach the purpose of gas liquefaction and liquid heating simultaneously to it is extravagant to reduce the energy.
Drawings
Fig. 1 is a schematic structural diagram of a phenyl chlorosilane synthesis reaction gas condensing device according to an embodiment of the present invention.
The system comprises a heat exchanger 1, a heat conducting oil level tank 2, a first heat exchange area 101, a second heat exchange area 102, a connecting pipe 3, a flow valve 4, a first folding pipe 5, a second folding pipe 6, a spraying pipeline 7, a spray head 8, a liquid outlet 9, a circulating pump 10, a temperature detector 11 and a display screen 12.
The specific implementation mode is as follows:
in order to deepen understanding of the present invention, the following detailed description is made on the embodiments of the present invention with reference to the accompanying drawings.
It should be understood that the structure, ratio, size and the like shown in the drawings attached to the present specification are only used for matching with the content disclosed in the specification, so as to be known and read by those skilled in the art, and are not used for limiting the limit conditions that the present invention can be implemented, so that the present invention has no technical essential meaning, and any structure modification, ratio relationship change or size adjustment should still fall within the scope that the technical content disclosed in the present invention can cover without affecting the function that the present invention can produce and the purpose that the present invention can achieve.
Examples
With reference to figure 1 of the drawings,
a condensation device for phenylchlorosilane synthesis reaction gas comprises a heat exchanger 1 and a heat conducting oil level tank 2, wherein the heat exchanger 1 is divided into a first heat exchange area 101 and a second heat exchange area 102, a sealing plate 103 is arranged between the first heat exchange area 101 and the second heat exchange area 102, the first heat exchange area 101 is connected with the second heat exchange area 102 through a connecting pipe 3, a flow valve 4 is installed on the connecting pipe 3, first folding pipes 5 are distributed in the first heat exchange area 101, two ends of each first folding pipe 5 penetrate through the outer wall of the first heat exchange area 101, second folding pipes 6 are distributed in the second heat exchange area 102, two ends of each second folding pipe 6 penetrate through the outer wall of the second heat exchange area 102,
the first heat exchange area 101 is located at the upper part of the second heat exchange area 102, and the first heat exchange area 101 is connected with the conduction oil level tank 2 through a pipeline.
Further, a spray pipe 7 is arranged on the top surface of the first heat exchange area 101, a plurality of spray heads 8 are arranged on the spray pipe 7, and the spray heads 8 extend into the first heat exchange area 101 and are connected with the top surface wall of the first heat exchange area 101 in a sealing mode.
Further, a liquid outlet 9 is formed in the bottom surface of the second heat exchange area 102, the liquid outlet 9 is connected with a circulating pump 10 through a pipeline, and the circulating pump 10 is connected with the bottom surface of the heat conduction oil level groove 2 through a pipeline, so that circulation of heat conduction oil is realized.
Further, the first heat exchange area 101 and the second heat exchange area 102 are respectively provided with a temperature detector 11, the temperature detector 11 is electrically connected with a display screen 12 installed at a low position, so that the temperature is monitored, and the working conditions of a flow valve and a circulating pump are adjusted according to the displayed temperature, thereby controlling the speed and efficiency of heat exchange.
The technical means disclosed by the scheme of the utility model is not limited to the technical means disclosed by the technical means, but also comprises the technical scheme consisting of the equivalent replacement of the technical features. The present invention is not to be considered as the best thing, and belongs to the common general knowledge of the technicians in the field.
Claims (4)
1. The utility model provides a phenyl chlorosilane synthesis reaction gas condensing equipment, characterized in that, includes heat exchanger (1) and conduction oil level groove (2), heat exchanger (1) divide into first heat exchange district (101) and second heat exchange district (102), be provided with between first heat exchange district (101) and second heat exchange district (102) closing plate (103), first heat exchange district (101) and second heat exchange district (102) between be connected through connecting pipe (3), connecting pipe (3) on install flow valve (4), first heat exchange district (101) in distribute first folding pipe (5), the both ends of first folding pipe (5) pass the outer wall of first heat exchange district (101), second heat exchange district (102) in distribute second folding pipe (6), second folding pipe (6) both ends pass the outer wall of second heat exchange district (102),
the first heat exchange area (101) is positioned at the upper part of the second heat exchange area (102), and the first heat exchange area (101) is connected with the heat conducting oil level groove (2) through a pipeline.
2. The phenylchlorosilane synthesis reaction gas condensing unit as claimed in claim 1, wherein a spray pipe (7) is arranged on the top surface of the first heat exchange area (101), a plurality of spray heads (8) are arranged on the spray pipe (7), and the spray heads (8) extend into the first heat exchange area (101) and are hermetically connected with the top surface wall of the first heat exchange area (101).
3. The phenylchlorosilane synthesis reaction gas condensing device as claimed in claim 1, wherein a liquid outlet (9) is formed in the bottom surface of the second heat exchange area (102), the liquid outlet (9) is connected with a circulating pump (10) through a pipeline, and the circulating pump (10) is connected with the bottom surface of the heat-conducting oil level tank (2) through a pipeline, so that the circulation of heat-conducting oil is realized.
4. The phenylchlorosilane synthesis reaction gas condensing device as claimed in claim 1, wherein the first heat exchange area (101) and the second heat exchange area (102) are respectively provided with a temperature detector (11), and the temperature detectors (11) are electrically connected with a display screen (12) arranged at a lower position to realize temperature monitoring.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021808912.9U CN213375210U (en) | 2020-08-26 | 2020-08-26 | Phenyl chlorosilane synthesis reaction gas condensing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021808912.9U CN213375210U (en) | 2020-08-26 | 2020-08-26 | Phenyl chlorosilane synthesis reaction gas condensing device |
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| Publication Number | Publication Date |
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| CN213375210U true CN213375210U (en) | 2021-06-08 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202021808912.9U Active CN213375210U (en) | 2020-08-26 | 2020-08-26 | Phenyl chlorosilane synthesis reaction gas condensing device |
Country Status (1)
| Country | Link |
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| CN (1) | CN213375210U (en) |
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2020
- 2020-08-26 CN CN202021808912.9U patent/CN213375210U/en active Active
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