CN203949521U - A kind of highly-efficient glass heat exchanger - Google Patents
A kind of highly-efficient glass heat exchanger Download PDFInfo
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- CN203949521U CN203949521U CN201420386395.9U CN201420386395U CN203949521U CN 203949521 U CN203949521 U CN 203949521U CN 201420386395 U CN201420386395 U CN 201420386395U CN 203949521 U CN203949521 U CN 203949521U
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- condenser
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- cooling water
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Abstract
The utility model discloses a kind of highly-efficient glass heat exchanger, it is characterized in that glass condenser (5) comprises at least two joint condenser tower joints (5-1), the cooling water intake (5-3) of adjacent condenser coil (5-2) is connected with cooling water water return outlet (5-4), glass condenser (5) passes through elbow, tetrafluoro hose connector (1), straight pipe, valve connects respectively tail gas outlet (8), condensed fluid refluxing opening (9) again, glass condenser (5) connects respectively sewage draining exit (10) by valve, liquid backflow mouth (11), liquid backflow mouth (11) is by threeway, tetrafluoro hose connector connects respectively import (13), gas feed (12), gas feed (12) connects glass condenser (5), the utility model installing/dismounting is safeguarded flexible, reduce warehousing pressure, cost-saving, improve condensation efficiency, reduce energy resource consumption and material loss, economical and practical, save installing space, safe and reliable.
Description
Technical field:
The utility model relates to a kind of heat exchanger, relates in particular to a kind of highly-efficient glass heat exchanger.
Background technology:
Glass heat interchanger is due to compact conformation, volume is little, visual in image, physicochemical property is stable, and antiseptic property is superior, simple installation, and every internode adopts cone-shaped flange mouth to connect, and assembling flexibly, can be assembled by " series connection " or " parallel connection " mode, meet the needs of different film-cooled heats, be therefore widely used in the chemical process such as cooling, the backflow, extraction, purification of chemical process.At present, existing glass heat interchanger gas vent and liquid backflow mouth share import and export, when liquid backflow amount greatly or not solidifying gas flow is large, often can cause gas, liquid convection, liquid splash, when serious, can in the tower joint of glass condenser, there is " bumping " phenomenon of " rushing tower ", there is very large danger, and the outlet of glass heat interchanger directly connects vacuum line, phenomenon that liquid " bumping " " rushes tower " can cause liquid material directly to be taken out of cooling system by vacuum when serious, enter vacuum system, not only reduce condensation efficiency, cause serious material loss waste, and can contaminated vacuum system etc. reaction fixed gas system for handling.Therefore conventional glass condenser is only applicable to the distillation of a small amount of chemical material, and the condensing reflux that reaction temperature is lower, reactant liquor evaporation capacity is little operation.
The purpose of this utility model be to overcome the deficiency of above-mentioned prior art and provide a kind of installing/dismounting safeguard flexible, reduce warehousing pressure, cost-saving, improve condensation efficiency, reduce energy resource consumption and material loss, economical and practical, save installing space, safe and reliable highly-efficient glass heat exchanger.
utility model content:
The purpose of this utility model can reach by following measure: a kind of highly-efficient glass heat exchanger, it comprises glass condenser, it is characterized in that glass condenser comprises at least two joint condenser tower joints, every joint condenser Ta Jienei is equipped with condenser coil, one end of condenser coil is provided with cooling water intake, the other end is provided with cooling water water return outlet, wherein the cooling water intake of the condenser coil between adjacent condenser tower joint is connected with cooling water water return outlet, elbow is passed through in the upper end of glass condenser, tetrafluoro hose connector, straight pipe connecting tee, the side of threeway connects tail gas outlet by valve, the lower end of threeway connects condensed fluid refluxing opening again by valve, the lower end connecting tee of glass condenser, the lower end of threeway connects sewage draining exit by valve, the side of threeway connects liquid refluxing opening, liquid backflow mouth connecting tee, the side of threeway connects import by tetrafluoro hose connector, bend pipe is passed through in the upper end of threeway, tetrafluoro hose connector connects gas feed, gas feed connects glass condenser.
The utility model can produce following good effect compared with the prior art: the utility model has designed the unique and superior tetrafluoro combination that is flexible coupling, use tetrafluoro to be flexible coupling and connect combination by each section, reduce the impact of vibration on instrument, pipeline, installing/dismounting is safeguarded flexible, accessory is of less types and can be general, reduce warehousing pressure, save entreprise cost; Increase gas feed, made gas rising passway not take condenses return flow line; For avoid overheated gas have little time condensation " rush tower " run material, increase condensed fluid refluxing opening again, go out the tower joint of glass condenser once there be liquid, can receive reuse, solve the problem that the gas-liquid convection problem of common condenser and " bumping " " rush tower " and run material, improve condensation efficiency, reduced energy resource consumption and material loss waste; The potential safety hazard of having avoided common condenser gas-liquid convection and " bumping " " to rush tower " bringing, the essential safety of implement device; Increased sewage draining exit, daily as sewage draining exit, in emergency circumstances or if desired (while having little time to reflux such as a large amount of condensed fluids), can open sewage draining exit for subsequent use by liquid guide flow to reaction system.Can increase or reduce according to practical effect the tower joint number of glass condenser, economical and practical, saving installing space; Only take convection problem and " bumping " race material problem that a reactor mouth position has solved high-efficiency condensation backflow and common condenser, avoid simple raising condensation efficiency and taken too much still mouth position, can, by measured response still still mouth position for other processing arrangements, not affect process pipe designing requirement.
Brief description of the drawings:
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention: the detailed description of the invention of the present utility model below in conjunction with accompanying drawing elaborates:
Embodiment: a kind of highly-efficient glass heat exchanger (referring to Fig. 1), it comprises glass condenser 5, glass condenser 5 comprises that at least two joint condenser tower joint 5-1(the present embodiment are two joints), in every joint condenser tower joint 5-1, be equipped with condenser coil 5-2, one end of condenser coil 5-2 is provided with cooling water intake 5-3, the other end is provided with cooling water water return outlet 5-4, and wherein the cooling water intake 5-3 of the condenser coil 5-2 between adjacent condenser tower joint 5-1 is connected by bend pipe 5-5 with cooling water water return outlet 5-4.The upper end connecting bend 3 of glass condenser 5, elbow 3 connects horizontal straight pipe 6 by tetrafluoro hose connector 1, laterally straight pipe 6 connects vertical straight siphunculus 7 by elbow 3, vertical straight siphunculus 7 connecting tees 2, the side of threeway 2 connects tail gas outlet 8 by valve 4, and the lower end of threeway 2 connects condensed fluid refluxing opening 9 again by valve 4.The lower end connecting tee 2 of glass condenser 5, the lower end of threeway 2 connects sewage draining exit 10 by valve 4, the side of threeway 2 connects liquid refluxing opening 11, liquid backflow mouth 11 connecting tees 2, the side of threeway 2 connects import 13 by tetrafluoro hose connector 1, the upper end bridge piece 3 of threeway 2, bend pipe 3 connects gas feed 12 by tetrafluoro hose connector 1, and gas feed 12 connects glass condenser 5.
When use, in reaction system, Yin Wendu is higher, exceed the boiling point of material and make reaction mass flash to overheated gas, enter in the cavity of glass condenser 5 through import 13, gas feed 12, simultaneously in the condenser coil 5-2 of recirculated cooling water in cooling water intake 5-3 enters the cavity of glass condenser 5, in the cavity of overheated gas process glass condenser time, carry out heat exchange with the cooling water as cold-producing medium in condenser coil 5-2 in the mode of cross-flow, non-direct contact.The overheated gas of material is emitted heat in heat exchanging process, and interior can reduction is condensed into gradually liquid state, in liquid backflow mouth 11 Returning reacting systems in the cavity of glass condenser.In heat exchanging process, absorb the cooling water of amount of heat, interior can increasing, temperature raises, then continues circulation through circulation, and heat is taken away.
Claims (1)
1. a highly-efficient glass heat exchanger, it comprises glass condenser (5), it is characterized in that glass condenser (5) comprises at least two joint condenser tower joints (5-1), in every joint condenser tower joint (5-1), be equipped with condenser coil (5-2), one end of condenser coil (5-2) is provided with cooling water intake (5-3), the other end is provided with cooling water water return outlet (5-4), wherein the cooling water intake (5-3) of the condenser coil (5-2) between adjacent condenser tower joint (5-1) is connected with cooling water water return outlet (5-4), the upper end of glass condenser (5) is by elbow (3), tetrafluoro hose connector (1), straight pipe connecting tee (2), the side of threeway (2) connects tail gas outlet (8) by valve (4), the lower end of threeway (2) connects condensed fluid refluxing opening (9) by valve (4) again, the lower end connecting tee (2) of glass condenser (5), the lower end of threeway (2) connects sewage draining exit (10) by valve (4), the side of threeway (2) connects liquid refluxing opening (11), liquid backflow mouth (11) connecting tee (2), the side of threeway (2) connects import (13) by tetrafluoro hose connector (1), the upper end of threeway (2) is by bend pipe (3), tetrafluoro hose connector (1) connects gas feed (12), gas feed (12) connects glass condenser (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420386395.9U CN203949521U (en) | 2014-07-14 | 2014-07-14 | A kind of highly-efficient glass heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420386395.9U CN203949521U (en) | 2014-07-14 | 2014-07-14 | A kind of highly-efficient glass heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203949521U true CN203949521U (en) | 2014-11-19 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420386395.9U Active CN203949521U (en) | 2014-07-14 | 2014-07-14 | A kind of highly-efficient glass heat exchanger |
Country Status (1)
| Country | Link |
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| CN (1) | CN203949521U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104745307A (en) * | 2015-03-10 | 2015-07-01 | 王世军 | Rose cell sap distilling device |
-
2014
- 2014-07-14 CN CN201420386395.9U patent/CN203949521U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104745307A (en) * | 2015-03-10 | 2015-07-01 | 王世军 | Rose cell sap distilling device |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |