CN203479046U - Device for recycling condensate steam in process of production - Google Patents
Device for recycling condensate steam in process of production Download PDFInfo
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- CN203479046U CN203479046U CN201320518215.3U CN201320518215U CN203479046U CN 203479046 U CN203479046 U CN 203479046U CN 201320518215 U CN201320518215 U CN 201320518215U CN 203479046 U CN203479046 U CN 203479046U
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- steam
- storage tank
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- condensate
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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
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
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Abstract
The utility model provides a device for recycling condensate steam in the process of production. The device comprises a heat exchanger and a condensate storage tank, wherein the heat exchanger and the condensate storage tank are sequentially connected. The condensate storage tank is provided with a gas-liquid separator, and the gas-liquid separator is used for carrying out secondary condensation on steam escaped from the condensate storage tank. According to the recycling device, secondary condensation on condensate flowing out of the heat exchanger can be achieved, secondary recycling of heat of the condensate steam can be achieved, the steam can be recycled by 1.8ton/hour, and the energy-saving effect is obvious; in addition, complete recycling can be achieved, the investment is small, the configuration is simple, and the device is suitable for industrial production enterprises.
Description
Technical field
The utility model belongs to and in industrial production, utilizes Steam Heating material technical field, relate to a kind of steam that is applicable in enrichment facility that condensed water reclaims open system through heat exchange, condensed secondary recovery operative installations, particularly a kind of device of producing steam after middle recovery condensation.
Background technology
Condensation water recovery system in industrial production is divided into open system and closed system.The condensate storage of open system is open type, communicates with atmosphere.When condensed water enters condensate storage, pressure reduces suddenly, and water temperature, higher than boiling point corresponding to this pressure, produces a large amount of secondary flash steams, and residue condensate temperature is approximately 100 ℃, reclaims and uses secondary flash steam and condensed water, has certain energy-saving significance.Condensed water recovery technology in industry, relates generally to the recovery use of condensed water at present, secondary flash steam is set up to heat exchanger more and reclaim, and investment is large, increases maintenance cost.
Summary of the invention
The purpose of this utility model is to provide a kind of device of producing steam after middle recovery condensation, for the recovery of secondary flash steam, does not need to set up heat exchanger, reduces investment.
For achieving the above object, the technical scheme that the utility model adopts is: a kind of device of producing steam after middle recovery condensation, comprise the heat exchanger and the condensate liquid storage tank that are connected successively, on condensate liquid storage tank, gas-liquid separator is installed, the steam that gas-liquid separator is overflowed from condensate liquid storage tank for time condensation.
Described gas-liquid separator comprises the cylindrical shell of the hollow of vertical setting, and cylindrical shell bottom is respectively equipped with steam inlet and lower liquid mouth, and steam inlet and lower liquid mouth are communicated with condensate liquid storage tank respectively; Cylindrical shell upper end is vertically provided with the water-locator of tubular, and the lower end of water-locator is stretched in cylindrical shell.
The utility model retracting device adopts condensate liquid storage tank to carry out preliminary condensation to the steam in condensate liquid, by gas-liquid separator, remaining condensed steam being carried out to condensation more again reclaims, realizing the secondary recovery of condensed steam heat uses, energy-saving effect is obvious, can realize completely and reclaiming, and small investment, configuration are simply, are applicable to industrial production enterprise.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model retracting device.
Fig. 2 is the structural representation of gas-liquid separator in the utility model retracting device.
Fig. 3 is the structural representation of eddy flow perforated panel in the utility model retracting device.
Fig. 4 is the top view of Fig. 3.
In figure: 1. heat exchanger, 2. gas-liquid separator, 3. condensate liquid storage tank, 4. condensate liquid delivery pump, 5. cylindrical shell, 6. descend liquid mouth, 7. steam inlet, 8. water-locator, 9. baffle plate, 10. eddy flow perforated panel, 11. pressure relief openings, 12. fresh water (FW) entrances, 13. eddy flow perforated panel plate bodys, 14. whirl hole.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is elaborated.
As shown in Figure 1, the utility model retracting device, comprises the heat exchanger 1, condensate liquid storage tank 3 and the condensate liquid delivery pump 4 that are connected successively; Structure gas-liquid separator 2 is as shown in Figure 2 installed on condensate liquid storage tank 3, and gas-liquid separator 2 comprises the cylindrical shell 5 of the hollow of vertical setting, and cylindrical shell 5 lower sides are provided with steam inlet 7, and steam inlet 7 is communicated with condensate liquid storage tank 3; Cylindrical shell 5 lower ends are provided with lower liquid mouth 6, lower liquid mouth 6 is communicated with condensate liquid storage tank 3, and the upper end of cylindrical shell 5 is provided with fresh water (FW) entrance 12, the interior water-locator 8 that is vertically provided with tubular of fresh water (FW) entrance 12, the lower end of water-locator 8 is stretched in cylindrical shell 5, between the sidewall of water-locator 8 and fresh water (FW) entrance 12 sidewalls, has space; The sidewall of fresh water (FW) entrance 12 is provided with pressure relief opening 11.
In water-locator 8, be horizontally disposed with the baffle plate 9 of ring-type, baffle plate 9 is provided with structure eddy flow perforated panel 10 as shown in Figure 3 and Figure 4, eddy flow perforated panel 10 comprises tabular eddy flow perforated panel plate body 13, on eddy flow perforated panel plate body 13, be processed with several whirl hole 14, whirl hole 14 is bent tube type, and it is coaxial that same whirl hole 14 is positioned at the circular hole of eddy flow perforated panel plate body 13 both ends of the surface; , the plurality of whirl hole 14 is distributed in respectively on a plurality of concentric circles centered by eddy flow perforated panel plate body 13 axis, and the whirl hole 14 on each concentric circles is uniformly distributed, and the center of circle of all whirl hole 14 arc of curvature is all towards eddy flow perforated panel plate body 13 axis; And the quantity of the whirl hole 14 distributing on the larger concentric circles of radius is more than the quantity of the whirl hole 14 distributing on the less concentric circles of radius.On condensate liquid storage tank 3 sidewalls, set up overflow pipe, and cause trench; On gas-liquid separator 2, set up blow-down pipe, after preventing from cutting off the water supply, install superpressure.
The upper end of water-locator 8 is connected with fresh water (FW) conveying device, makes to connect one end that the condensate line of heat exchanger 1 and condensate liquid storage tank 3 stretches into condensate liquid storage tank 3 apart from the condensate liquid storage tank 3 about 800mm～1000mm in bottom.The steam producing in production forms condensed water after heat exchanger heat exchange, this condensed water flows into condensate liquid storage tank 3 through condensate line, because the pressure in condensate liquid storage tank 3 reduces suddenly, and the temperature of condensed water is higher than the corresponding boiling point of this pressure, thereby at a large amount of secondary flash steams of the interior generation of condensate storage tank 3, the secondary flash steam producing enters gas-liquid separator 2 by steam inlet 7, and flow from the bottom up in gas-liquid separator 2, now open fresh water (FW) conveying device, the lower fresh water (FW) of temperature (or condensate liquid) is sent into water-locator 8, the fresh water (FW) that enters water-locator 8 flows from top to bottom, during through eddy flow perforated panel 10, when making flow, whirl hole 14 produces rotation, the fresh water (FW) flowing out from whirl hole 14 is covering of the fan and sprays out from water-locator 8 lower ends, make part that cylindrical shell 5 is positioned at water-locator 8 lower ends all under the covering in these spurting current, to entering the steam of cylindrical shell 5, carry out time condensation, the condensed water that condensation forms drops to cylinder body bottom with the fresh water (FW) that enters cylindrical shell 5, by lower liquid mouth 6, flow into condensate liquid storage tank 3, solution temperature in condensate liquid storage tank 3 is about 50～70 ℃, by condensate liquid delivery pump 4, deliver to the production workshop section needing.
Condensate liquid tankful in condensate liquid storage tank 3, close in the situation of fresh water (FW), there will be the liquid hit phenomenon of steam and water, now by pressure relief opening 11, can discharge the superheated steam in cylindrical shell 5, prevent the interior superpressure that occurs of condensate liquid storage tank 3, cause condensate liquid storage tank 3 cell bodies to leak and damage.
Claims (6)
1. a device of producing steam after middle recovery condensation, comprise the heat exchanger (1) and the condensate liquid storage tank (3) that are connected successively, it is characterized in that, gas-liquid separator (2) is installed, the steam that gas-liquid separator (2) is overflowed from condensate liquid storage tank (3) for time condensation on condensate liquid storage tank (3).
2. in producing according to claim 1, reclaim the device of steam after condensation, it is characterized in that, described gas-liquid separator (2) comprises the cylindrical shell (5) of the hollow of vertical setting, cylindrical shell (5) bottom is respectively equipped with steam inlet (7) and lower liquid mouth (6), and steam inlet (7) and lower liquid mouth (6) are communicated with condensate liquid storage tank (3) respectively; Cylindrical shell (5) upper end is vertically provided with the water-locator (8) of tubular, and the lower end of water-locator (8) is stretched in cylindrical shell (5).
3. in producing according to claim 2, reclaim the device of steam after condensation, it is characterized in that, described cylindrical shell (5) upper end is provided with fresh water (FW) entrance (12), and water-locator (8) is positioned at fresh water (FW) entrance (12), between water-locator (8) sidewall and fresh water (FW) entrance (12) sidewall, has space.
4. the device that reclaims steam after condensation in producing according to claim 3, is characterized in that, the sidewall of described fresh water (FW) entrance (12) is provided with pressure relief opening (11).
5. according to the device that reclaims steam after condensation in producing described in claim 2 or 3, it is characterized in that, in described water-locator (8), be provided with eddy flow perforated panel (10), eddy flow perforated panel (10) comprises tabular eddy flow perforated panel plate body (13), on eddy flow perforated panel plate body (13), be processed with the whirl hole (14) of several bent tube types, the circular hole at same whirl hole (14) two ends is coaxial; The plurality of whirl hole (14) is distributed on a plurality of concentric circles centered by eddy flow perforated panel plate body (13) axis, whirl hole on each concentric circles (14) is uniformly distributed, and the center of all whirl hole (14) arc of curvature is all towards eddy flow perforated panel plate body (13) axis; And the quantity of the whirl hole (14) distributing on the larger concentric circles of radius is more than the quantity of the whirl hole (14) distributing on the less concentric circles of radius.
6. according to the device that reclaims steam after condensation in producing described in claim 1 or 2, it is characterized in that, described condensate liquid storage tank (3) is connected with condensate liquid delivery pump (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320518215.3U CN203479046U (en) | 2013-08-16 | 2013-08-16 | Device for recycling condensate steam in process of production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320518215.3U CN203479046U (en) | 2013-08-16 | 2013-08-16 | Device for recycling condensate steam in process of production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203479046U true CN203479046U (en) | 2014-03-12 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320518215.3U Expired - Fee Related CN203479046U (en) | 2013-08-16 | 2013-08-16 | Device for recycling condensate steam in process of production |
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| Country | Link |
|---|---|
| CN (1) | CN203479046U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106959036A (en) * | 2017-05-07 | 2017-07-18 | 丁新平 | A kind of steam and hot water thermal energy storage device |
| CN107606965A (en) * | 2017-09-29 | 2018-01-19 | 广西信发铝电有限公司 | A kind of condenser system |
-
2013
- 2013-08-16 CN CN201320518215.3U patent/CN203479046U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106959036A (en) * | 2017-05-07 | 2017-07-18 | 丁新平 | A kind of steam and hot water thermal energy storage device |
| CN107606965A (en) * | 2017-09-29 | 2018-01-19 | 广西信发铝电有限公司 | A kind of condenser system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140312 Termination date: 20150816 |
|
| EXPY | Termination of patent right or utility model |