CN1776300A - Condensate water recovery device for condenser - Google Patents
Condensate water recovery device for condenser Download PDFInfo
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- CN1776300A CN1776300A CN 200510126132 CN200510126132A CN1776300A CN 1776300 A CN1776300 A CN 1776300A CN 200510126132 CN200510126132 CN 200510126132 CN 200510126132 A CN200510126132 A CN 200510126132A CN 1776300 A CN1776300 A CN 1776300A
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- condenser
- recovery device
- condensed water
- water recovery
- condensate water
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Abstract
Characters of water recovery arrangement are that there is drainage channel corresponding to each cooling pipe placed in horizontal or declining position inside condenser. The drainage channel is in slant state. Advantages are: reducing condensed water to be vaporized for second time so as to lower resistance of the fume extraction system, make flow of fume more swimmingly and reasonably; eliminating induced draft fan etc. equipment for forcing fume extraction so as to save relevant power and cost; smaller installation space. The invention saves cost of fuel gas, and reduces environmental pollution.
Description
Technical field
The present invention relates to a kind of improvement technology of Boiler Used Coldly condenser, particularly relate to retracting device the condensed water of condenser.
Background technology
The combustion natural gas boiler is used in a large number at present, can produce a large amount of steam behind the combustion of natural gas, can produce the steam of 1.55KG after the completing combustion of every standard cubic meter natural gas, if these water vapor condensations Cheng Shui, can emit the heat of 3700KJ, account for the combustion of natural gas heat release sensible heat part 10%, use condenser can reclaim this part heat, thereby improved the service efficiency of boiler.In actual applications, the about 10.3NM3 of 1NM3 combustion of natural gas production theory exhaust gas volumn (approximately 12.5KG), with excess air coefficient 1.3 is example, produces flue gas 14NM3 (approximately 16.6KG), gets 200 ℃ of flue-gas temperatures and is reduced to 70 ℃, emit the about 1600KJ of physics sensible heat, the water vapour condensation rate gets 50%, emits the about 1850KJ of the latent heat of vaporization, amounts to heat release 3450KJ, be 10% of natural gas low heat valve approximately, can save gas fuel nearly 11%.
Boiler is that present most widely used energy source terminal utilize technology, also is the main source of pollutant emission in the atmosphere.The pollutant that discharges in the combustion process, as: sulfur dioxide (SO
2) and nitrogen oxide (NO
x) can cause some areas acid rain after entering atmosphere: carbon dioxide (CO
2) and methane (CH
4) the isothermal chamber gas purging, will cause global warming.The climate change that global warming causes is the significant challenge that the whole world faces, and improving energy conversion and utilization ratio and controlling combustion process better is to reduce the major measure of atmospheric emission.
Generation along with condensed water in the flue gas, nuisance in the flue gas such as nitrogen oxide, carbon monoxide, halogenated compound etc. can be dissolved in the condensed water, thereby the nuisance that enters atmosphere is reduced in a large number, the discharge standard of Pekinese's gas fired-boiler is nitrogen oxide≤200mg/kwh, carbon monoxide≤80ppm/m, and flue gas is by behind the condenser, nitrogen oxide is less than 60mg/kwh, carbon monoxide is generally less than 10ppm/m, so the use of condenser can significantly reduce the discharging of nuisance.
Generally speaking, the cigarette direction of advancing of condenser both domestic and external is all selected to go out under enterprising, promptly firing flue gas that natural gas or oil burning boiler produce enters from the top of condenser, discharge from the bottom of condenser, and the condensed water that produces in condenser is also freely dropped onto the bottom of condenser by the top of condenser, because the very fast from top to bottom reduction of flue-gas temperature, the condensed water of generation just can not form double evaporation-cooling in the drippage process from the top down, and condensation effect obtains fine assurance.But install the boiler room of condenser additional for the preparation of having built up, because flue is all installed from bottom to top, so want to install additional the trend that existing condenser just must change flue, such one is that transformation is pretty troublesome, and main is not transform the space, and a lot of boiler rooms have lost the transformation apparatus meeting: in addition, because after flue gas flows from the top down, must make progress again and flow, its resistance is will more former trend from bottom to top a lot of greatly, also can't normally move after causing a lot of boiler improvements.If discharge and flue gas is made into enter top from the bottom of condenser, then can reduce the condenser occupation space is installed, reduce to install the resistance that condenser causes, but flue gas upwards flows from the bottom, the condensed water that produces in condenser but drips downwards from top, and because of the bottom is the import of flue gas, the cigarette temperature is very high, condensed water can produce double evaporation-cooling, seriously reduces the efficient of condenser.
Summary of the invention
The condensate water recovery device that the purpose of this invention is to provide a kind of condenser, adopt flue to install from bottom to top to solve, flue gas enters the problem that the timely discharge of condensed water the condenser of formula structure is discharged on top from the bottom of condenser, to improve the efficient of condenser.
The condensate water recovery device of condenser of the present invention, it comprises: a corresponding with it rhone is all arranged under each the root level of condenser inside or tilted-putted cooling tube, described rhone is skewed, to form one group of condensed water drain tank structure that two ends have difference in height.
The condensate water recovery device of condenser as described above is connected with a condensed water main respectively at the low side with several condensation gutters below one deck cooling tube; Described low side with one deck condensation gutter is successively the arrangement that reduces in the horizontal direction, the condensed water main be the incline direction setting after it is communicated with respectively, low side one side of condensed water main is connected with vertical condensate draining pipe respectively again.
The condensate water recovery device of aforesaid condenser, the V-shaped structure of described condensation gutter.
The condensate water recovery device of aforesaid condenser, described condensation gutter semicircular in shape or circular arc.
The present invention has following advantage and good effect: because the fine queueing problem that solves condensed water, reduced the double evaporation-cooling of condensed water to greatest extent, what make that condenser has been realized flue gas goes out on advancing down, make the flow process of flue gas more smooth and easy rationally, the resistance of whole smoke evacuation system is littler, avoid installing additional the forced fume exhaust measure of equipment such as air-introduced machine, also just saved corresponding electric power input; Because installing space is littler, making has had the possibility that this energy saver of condenser is installed in the boiler room that condenser can't be installed originally simultaneously.Thus, the one, can save a large amount of combustion gas expenses for the user, the 2nd, reduce exhaust gas discharging, reduced environmental pollution, the 3rd, for society has saved a large amount of fuel.
Description of drawings
Fig. 1 is the structure front view of condensate water recovery device of the present invention.
Fig. 2 is the A-A cutaway view of Fig. 1.
The specific embodiment
Fig. 1 is that condensate water recovery device is installed on the structural representation in the condenser.In Fig. 1, the flue gas that the burning of combustion natural gas boiler produces enters from condenser smoke inlet 10, and the top exhanst gas outlet 1 from condenser after each cooling tube 3 surperficial heat releases of condenser inside is discharged.Cooling water enters first water cavity 4 from cooling water inlet pipe 6, enters the cooling water outlet pipe 8 outflow condensers of second water cavity 12, the 3rd water cavity 7, the 4th water cavity 11, the 5th water cavity 9 successively by cooling tube.Heat and water vapor condensation liberated heat that cooling water absorbs in the flue gas by cooling tube 3; Flue gas is in cooling tube 3 surperficial heat releases, steam in the flue gas is in cooling tube 3 surface condensations, the condensing drip that produces that condenses drops in the condensation gutter 2, flows into condensed water arterial drainages 5 by condensation gutter 2 again, by condensed water arterial drainage 5 condensed water is entered neutralization pond.
Each root level of flue gas condenser or tilted-putted cooling tube all have a corresponding with it rhone 2 for 3 times, be consistent on the vertical direction, in the horizontal direction each rhone 3 all tilt and direction identical so that the condensed water that rhone 3 receives is discharged to the low side of each rhone.The low side of each of described horizontal direction layer rhone 3 can be communicated with arterial drainage 5 in the mode that reduces successively again, forms to have the arterial drainage syndeton at an angle of inclination (drop).The low side that forms each arterial drainage 5 by above-mentioned connected mode is communicated with vertically disposed condensate draining pipe 13 again, referring to Fig. 2.Fall in the corresponding rhone 3 at the condensing drip that the cooling tube surface produces, be expelled in the condensate draining pipe 13 after by arterial drainage 5 these condensing drips being concentrated again, be discharged to outside the condenser at last.
Claims (4)
1, a kind of condensate water recovery device of condenser, it is characterized in that it comprises: a corresponding with it rhone is all arranged under each the root level of condenser inside or tilted-putted cooling tube, described rhone is skewed, to form one group of condensed water drain tank structure that two ends have difference in height.
2, the condensate water recovery device of condenser as claimed in claim 1 is characterized in that: be connected with a condensed water main respectively at the low side with several condensation gutters below one deck cooling tube; Described low side with one deck condensation gutter is successively the arrangement that reduces in the horizontal direction, the condensed water main be the incline direction setting after it is communicated with respectively, low side one side of condensed water main is connected with vertical condensate draining pipe respectively again.
3, the condensate water recovery device of condenser as claimed in claim 1 is characterized in that: the V-shaped structure of described condensation gutter.
4, the condensate water recovery device of condenser as claimed in claim 1 is characterized in that: described condensation gutter semicircular in shape or circular arc.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB200510126132XA CN100400964C (en) | 2005-11-30 | 2005-11-30 | Condensate water recovery device for condenser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB200510126132XA CN100400964C (en) | 2005-11-30 | 2005-11-30 | Condensate water recovery device for condenser |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1776300A true CN1776300A (en) | 2006-05-24 |
| CN100400964C CN100400964C (en) | 2008-07-09 |
Family
ID=36765952
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB200510126132XA Expired - Fee Related CN100400964C (en) | 2005-11-30 | 2005-11-30 | Condensate water recovery device for condenser |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100400964C (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100552290C (en) * | 2007-07-11 | 2009-10-21 | 泉州市天龙环境工程有限公司 | Condensation water recovery system |
| CN106196214A (en) * | 2016-08-08 | 2016-12-07 | 叶安生 | Cooking fume condensation purifier |
| CN112551844A (en) * | 2020-12-13 | 2021-03-26 | 西安国祯环保工程有限公司 | Gravity turning plate device with condensate water recovery function for sludge treatment tower |
| CN115814579A (en) * | 2023-02-13 | 2023-03-21 | 轻准(杭州)科技有限公司 | Based on electron condensing steam-gas separation device |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2377477Y (en) * | 1998-06-12 | 2000-05-10 | 胡斌 | Heat exchanger assembly having condensed exhaust-heat heat-exchanger |
| JP2003294382A (en) * | 2002-04-04 | 2003-10-15 | Toyo Radiator Co Ltd | Heat exchanger |
| CN1611903A (en) * | 2003-10-30 | 2005-05-04 | 乐金电子(天津)电器有限公司 | Heat exchanger with drain groove |
| CN2738190Y (en) * | 2004-10-28 | 2005-11-02 | 王予意 | Water vapour condensation heat exchanger |
-
2005
- 2005-11-30 CN CNB200510126132XA patent/CN100400964C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100552290C (en) * | 2007-07-11 | 2009-10-21 | 泉州市天龙环境工程有限公司 | Condensation water recovery system |
| CN106196214A (en) * | 2016-08-08 | 2016-12-07 | 叶安生 | Cooking fume condensation purifier |
| CN106196214B (en) * | 2016-08-08 | 2018-03-27 | 叶安生 | Cooking fume condensation purifier |
| CN112551844A (en) * | 2020-12-13 | 2021-03-26 | 西安国祯环保工程有限公司 | Gravity turning plate device with condensate water recovery function for sludge treatment tower |
| CN115814579A (en) * | 2023-02-13 | 2023-03-21 | 轻准(杭州)科技有限公司 | Based on electron condensing steam-gas separation device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100400964C (en) | 2008-07-09 |
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| Date | Code | Title | Description |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: BEIJING NORTHERN SHANGDA ENERGY CONSERVATION EQUIP Free format text: FORMER OWNER: WANG XIAOWEI Effective date: 20090821 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20090821 Address after: Room 111, Heng Tong Building, No. 4, Huayuan Road, Beijing, Haidian District Patentee after: Beijing North samdar energy saving equipment Co. Ltd. Address before: Beijing City, Haidian District No. 48 Zhichun Road Yingdu building C block 3 unit 12 layer Patentee before: Wang Xiaowei |
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| DD01 | Delivery of document by public notice |
Addressee: Beijing North samdar energy saving equipment Co. Ltd. Document name: Notification that Application Deemed not to be Proposed |
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| DD01 | Delivery of document by public notice |
Addressee: Beijing North samdar energy saving equipment Co. Ltd. Document name: Notification of Termination of Patent Right |
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| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080709 Termination date: 20131130 |