CN105352339B - A kind of evaporative condenser for chemical industry - Google Patents
A kind of evaporative condenser for chemical industry Download PDFInfo
- Publication number
- CN105352339B CN105352339B CN201510491091.8A CN201510491091A CN105352339B CN 105352339 B CN105352339 B CN 105352339B CN 201510491091 A CN201510491091 A CN 201510491091A CN 105352339 B CN105352339 B CN 105352339B
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- cooling cylinder
- heater
- cooling
- heat exchanger
- exchanger tube
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- 239000000126 substance Substances 0.000 title claims abstract description 14
- 238000001816 cooling Methods 0.000 claims abstract description 49
- 239000004744 fabric Substances 0.000 claims abstract description 8
- 230000002093 peripheral effect Effects 0.000 claims abstract description 4
- 239000000498 cooling water Substances 0.000 abstract description 7
- 239000007788 liquid Substances 0.000 abstract description 4
- 230000005611 electricity Effects 0.000 abstract description 3
- 238000012423 maintenance Methods 0.000 abstract description 3
- 238000003912 environmental pollution Methods 0.000 abstract description 2
- 238000009510 drug design Methods 0.000 abstract 1
- 238000009833 condensation Methods 0.000 description 6
- 230000005494 condensation Effects 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses a kind of evaporative condensers for chemical industry, belong to field of chemical equipment, it mainly solves to use shell and tube indirect condenser at present, the heat exchange area that condenser needs is big, consumption of cooling-water is big, also need other vacuum pump to extract incoagulable gas, the high problem of power consumption, heater is connect with cooling cylinder, the heater is set to the bottom of entire cooling cylinder, enter after being heated by heater cooling in container in cooling cylinder, cooling cylinder is columnar structured, there is container inside cooling cylinder, cooling cylinder top peripheral interval cloth shows heat exchanger tube, the heat exchanger tube combines together with cooling cylinder, heater adds thermogenetic gas to absorb heat by heat exchanger tube to be condensed into liquid and be placed in container, column is spliced with cooling cylinder periphery.The present invention has rational design, in the case where same operating condition heat exhaust, reduces electricity consumption, water-saving, while having that occupied area is small, and low noise is free from environmental pollution, long service life and simple and convenient for maintenance.
Description
Technical field
The present invention relates to a kind of evaporative condensers for chemical industry, belong to field of chemical equipment.
Background technique
Existing widely used condenser has shell and tube indirect condenser, multi-layer porous board-like direct condenser etc..Currently, making
When with shell and tube indirect condenser, the material drop carried secretly in secondary steam will not pollute cooling water, be suitble to material corrosion strong
Occasion, but condenser need heat exchange area it is big, bulky, structure is complicated, and consumption of cooling-water is big, it is also necessary in addition configure
For vacuum pump to extract incoagulable gas, power consumption is high.Multi-layer porous board-like direct condenser uses cooling water and secondary steam
Direct condensation by contact, condensation effect is preferable, but on porous plate aperture aperture it is smaller, blocking is easy when long period of operation.This is directly
It is easy to cause liquid flooding or cooling water back-mixing into vaporization chamber when condenser counter-current operation, the effect that condensation is not achieved and vacuumizes
Fruit, it is also desirable to which vacuum pump extracts fixed gas.
Summary of the invention
When the present invention for shell and tube indirect condenser is used at present, the heat exchange area that condenser needs is big, bulky,
Structure is complicated, and consumption of cooling-water is big, it is also necessary to which in addition for vacuum pump to extract incoagulable gas, power consumption is high.Multilayer is more
Orifice-plate type direct condenser uses cooling water and the direct condensation by contact of secondary steam, and the aperture of aperture is smaller on porous plate, for a long time
The problem of blocking is easy when operation, devises a kind of evaporative condenser for chemical industry.
The technical scheme adopted by the invention to solve the technical problem is that:
A kind of evaporative condenser for chemical industry, structure include: heat exchanger tube, cooling cylinder, column, container, heater；Add
Hot device is connect with cooling cylinder, and the heater is set to the bottom of entire cooling cylinder, is entered in cooling cylinder after being heated by heater
It is cooling in container, realize condensation operation, cooling cylinder be it is columnar structured, have container inside cooling cylinder, the container is placed in cooling
Cylinder is internal be it is columnar structured, cooling cylinder top peripheral interval cloth shows heat exchanger tube, and the heat exchanger tube permeates with cooling cylinder
Body, heater add thermogenetic gas to absorb heat by heat exchanger tube to be condensed into liquid and be placed in container, and the water for absorbing heat steams
Hair is vapor, and column is spliced with cooling cylinder periphery.
Column interval cloth is listed in the lower periphery of cooling cylinder, is integrated with cooling cylinder splicing, the ring in radial position
Around arrangement.
The interval Boulez heat exchanger tube have very high evaporation efficiency, while may be implemented in cooling cylinder container cooling cylinder and
The small temperature difference heat exchange of heat exchanger tube, has very high heat exchange efficiency.
Compared with prior art, the beneficial effects of the present invention are:
1. novel and unique of the present invention, rationally, structure is simple, and in the case where same operating condition heat exhaust, weight saving subtracts for design
Few electricity consumption, it is water-saving, while having that occupied area is small, easy for installation, low noise is free from environmental pollution, long service life and maintenance
The advantages that easy, being widely used in industrial, chemical industry is the ideal energy-efficient product of environmental protection, it more adapts to water quality inferiority, water resource lacks
Work area uses.
2. the configuration of the present invention is simple, component technological is good, and material is cheap, low manufacture cost, and energy energy conservation subtracts material, answers
It is wide with property.
Detailed description of the invention
Fig. 1 is entirety sectional view of the present invention.
In figure: 1 heat exchanger tube, 2 cooling cylinders, 3 columns, 4 containers, 5 heaters.
Specific embodiment
A kind of evaporative condenser for chemical industry as shown in Figure 1:, structure include: heat exchanger tube 1, cooling cylinder 2, column 3,
Container 4, heater 5；Heater 5 is connect with cooling cylinder 2, and the heater 5 is set to the bottom of entire cooling cylinder 2, passes through heating
Device 5 enters cooling in container 4 in cooling cylinder 2 after heating, realize condensation operation, cooling cylinder 2 be it is columnar structured, in cooling cylinder 2
There is a container 4 in portion, the container 4 be placed in inside cooling cylinder 2 be it is columnar structured, 2 top peripheral interval cloth of cooling cylinder shows heat exchange
Pipe 1, the heat exchanger tube 1 combine together with cooling cylinder 2, and heater 5 plus thermogenetic gas are cold by the absorption heat of heat exchanger tube 1
It congeals into liquid to be placed in container 4, the water evaporation for absorbing heat is vapor, and column 3 is spliced with 2 periphery of cooling cylinder；It is described
Column 3 is spaced the lower periphery that cloth is listed in cooling cylinder 2, is integrated with the splicing of cooling cylinder 2, around arrangement in radial position；Institute
Stating interval Boulez heat exchanger tube 1 has very high evaporation efficiency, while cooling cylinder 2 and heat exchanger tube may be implemented in 2 container 4 of cooling cylinder
1 small temperature difference heat exchange, has very high heat exchange efficiency.
A kind of evaporative condenser for chemical industry, is fixed on the ground using column 3 described in the present embodiment, is spaced cloth
The cylindricality column 3 of column keeps condenser more firm, and novel and unique of the present invention, rationally, structure is simple, in same operating condition heat extraction for design
In the case where amount, weight saving reduces electricity consumption, water-saving, while having that occupied area is small, and easy for installation, low noise does not pollute
Environment, long service life and simple and convenient for maintenance, being widely used in industrial, chemical industry is the ideal energy-efficient product of environmental protection, it is more suitable
The work area for answering water quality inferiority, water resource to lack uses, and the configuration of the present invention is simple, component technological is good, and material is cheap, production
At low cost, energy energy conservation subtracts material, and application is wide.
The above description is merely a specific embodiment, those skilled in the art the invention discloses
In range, the variation that can be readily occurred in should all be covered within the protection scope of invention.
Claims (2)
1. a kind of evaporative condenser for chemical industry, structure include: heat exchanger tube (1), cooling cylinder (2), column (3), container (4),
Heater (5)；It is characterized in that: heater (5) is connect with cooling cylinder, the heater (5) is set to the bottom of entire cooling cylinder (2)
Portion, cooling cylinder be it is columnar structured, it is columnar structured, cooling cylinder (2) top peripheral inside cooling cylinder that the container (4), which is placed in,
Interval cloth is shown heat exchanger tube (1), and the heat exchanger tube (1) combines together with cooling cylinder.
2. a kind of evaporative condenser for chemical industry according to claim 1, characterized in that pillar (3) interval cloth is listed in
The lower periphery of cooling cylinder (2) is integrated, around arrangement in radial position with cooling cylinder (2) splicing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510491091.8A CN105352339B (en) | 2015-08-11 | 2015-08-11 | A kind of evaporative condenser for chemical industry |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510491091.8A CN105352339B (en) | 2015-08-11 | 2015-08-11 | A kind of evaporative condenser for chemical industry |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105352339A CN105352339A (en) | 2016-02-24 |
| CN105352339B true CN105352339B (en) | 2019-04-23 |
Family
ID=55328354
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510491091.8A Active CN105352339B (en) | 2015-08-11 | 2015-08-11 | A kind of evaporative condenser for chemical industry |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105352339B (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2562864Y (en) * | 2002-07-05 | 2003-07-30 | 中国石化集团巴陵石油化工有限责任公司 | Polymerization still |
| CN101380561A (en) * | 2008-09-26 | 2009-03-11 | 浙江大学 | Large membrane wall gas-phase reactor with high pressure steam as by-product |
| CN202762434U (en) * | 2012-09-13 | 2013-03-06 | 青州市坤伟工贸有限公司 | Reaction kettle with cooling coil for producing N-cyclohexy-2-benzothiazole sulfenamid (CBS) |
| CN203540491U (en) * | 2013-11-18 | 2014-04-16 | 福建省邵武市永晶化工有限公司 | Reactor for preparing antimony pentafluoride |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4330307A (en) * | 1980-04-07 | 1982-05-18 | Coury Glenn E | Method of separating a noncondensable gas from a condensable vapor |
| US20030133857A1 (en) * | 2002-01-12 | 2003-07-17 | Saudi Basic Industries Corporation | Multiphase polymerization reactor |
| CN2616537Y (en) * | 2002-05-13 | 2004-05-19 | 大连铁道学院 | Organic compound synthesizing apparatus |
| CN101643389B (en) * | 2009-08-25 | 2012-05-02 | 上海化工研究院 | Methanol synthesizer |
| CN201684606U (en) * | 2010-05-12 | 2010-12-29 | 汕头市微补植物营养科技有限公司 | Reactor with temperature detector |
| CN202700115U (en) * | 2012-08-03 | 2013-01-30 | 梅晓锋 | Novel distilling device |
-
2015
- 2015-08-11 CN CN201510491091.8A patent/CN105352339B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2562864Y (en) * | 2002-07-05 | 2003-07-30 | 中国石化集团巴陵石油化工有限责任公司 | Polymerization still |
| CN101380561A (en) * | 2008-09-26 | 2009-03-11 | 浙江大学 | Large membrane wall gas-phase reactor with high pressure steam as by-product |
| CN202762434U (en) * | 2012-09-13 | 2013-03-06 | 青州市坤伟工贸有限公司 | Reaction kettle with cooling coil for producing N-cyclohexy-2-benzothiazole sulfenamid (CBS) |
| CN203540491U (en) * | 2013-11-18 | 2014-04-16 | 福建省邵武市永晶化工有限公司 | Reactor for preparing antimony pentafluoride |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105352339A (en) | 2016-02-24 |
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