CN104728826A - Constant temperature economizer - Google Patents
Constant temperature economizer Download PDFInfo
- Publication number
- CN104728826A CN104728826A CN201510122659.9A CN201510122659A CN104728826A CN 104728826 A CN104728826 A CN 104728826A CN 201510122659 A CN201510122659 A CN 201510122659A CN 104728826 A CN104728826 A CN 104728826A
- Authority
- CN
- China
- Prior art keywords
- economizer
- constant temperature
- temperature
- heat exchanger
- external heat
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
Landscapes
- Chimneys And Flues (AREA)
Abstract
A constant temperature economizer comprises an economizer body, the economizer body is externally connected with a down pipe to form a closed cycle, an external heat exchanger is arranged on a circulating pipeline, when water is adopted as a circulating medium in the down pipe, a vacuum pump is arranged on the external heat exchanger to control operating pressure between 50, 000 Pa and 80, 000 Pa, the wall temperature of the economizer body is maintained between 80 DEG C and 95 DEG C, and ethyl alcohol can be directly adopted as a circulating medium in the down pipe. The wall temperature of the economizer is maintained between 80 DEG C and 95 DEG C constantly, low-temperature corrosion does not occur, the flow rate of working media in a heating surface is low, resistance is small, and no in-line pump is needed; the flow rate of flue gas is designed to be lower than 7 m/s, and the abrasion rate of the heating surface is low; the temperature of the flue gas is reduced, specific resistance of flying ash is lowered, the dust collection area of a bag deduster is enlarged, the dust removal efficiency of electricity and the dust removal efficiency of bags are both improved, flue gas waste heat is used for heating heat supply network water, cold air and condensed water, the waste heat is made full use of, and economical efficiency is remarkably improved.
Description
Technical field
The invention belongs to Thermal Power Generation Industry fume afterheat and utilize technology, particularly a kind of constant temperature economizer.
Background technology
Owing to using the impact of the factor such as coal type change and air preheater air leakage, coal-fired plant boiler exhaust gas temperature, often higher than design load, provides space for fume afterheat utilizes.
For response national energy-saving environmental protection policy, flue-gas temperature needs to be reduced to about 90 DEG C, and one side Mist heat recovering as far as possible, reduces fly ash resistivity on the other hand, improves bag dedusting specific dust collection area, improves efficiency of dust collection, form low temperature dedusting technology.
Empirically exhaust gas temperature often rises 10 DEG C, and boiler efficiency declines about 0.5%, and standard coal consumption is risen about 2g/ (kWh).Flue gas cooling working medium is generally water, and fume afterheat can be divided into three kinds of forms for the working medium heated: heat supply network recirculated water, one or two cold wind and condensate water.
At present, coal-burning power plant solves high fume temperature, and the general technical scheme adopted has high-temperature economizer and low-level (stack-gas) economizer.
Before high-temperature economizer is generally arranged in air preheater, direct heating boiler feed water, fume afterheat utilization ratio is the highest, is limited to back-end ductwork space and exhaust gas temperature in actual items transformation, the layout of high-temperature economizer needs COMPREHENSIVE CALCULATING air preheater operating condition, prevents cold section of air preheater from cold end corrosion occurring.Therefore, when general exhaust gas temperature is more than 200 DEG C, suggestion adopts high-temperature economizer.
After low-level (stack-gas) economizer is generally arranged in air preheater, in actual items transformation, space is enough.Be divided into open circulation and closed cycle by circulation form, whatsoever circulation form, the inlet water temperature of low-level (stack-gas) economizer is generally 70-85 DEG C, and outlet water temperature is generally designed to 120-130 DEG C, and wall temperature of heated surface increases.
The shortcoming of low-level (stack-gas) economizer is:
(1) counter-flow arrangement, heat transfer temperature difference is little;
(2) inlet water temperature (70-85 DEG C) is low, and during actual motion, with load and coal type change, inlet water temperature regulation and control are difficult, there is the risk of low-temperature zone cold end corrosion;
(3) for preventing cold end corrosion, heating surface material will elect Ni-based ND steel as, and material cost is high, and does not fundamentally solve the problem of cold end corrosion;
(4) the open circulation water yield is large, thermal power plant unit is existed to the problem of condensing capacity deficiency, and it is large that closed cycle exists water circulating pump power, runs the problem that power consumption is high.
Summary of the invention
In order to overcome the shortcoming of above-mentioned prior art, the object of the present invention is to provide a kind of constant temperature economizer, wall temperature of heated surface is constant remains on some numerical value between 80-95 DEG C, economizer generation cold end corrosion is prevented from design source, thus avoid the problems referred to above that conventional economizer occurs, when general flue-gas temperature is reduced to below 110 DEG C, fly ash resistivity declines obviously, dust collection efficiency improves, for minimizing boiler exhaust gas heat loss, raising boiler dusting efficiency and equipment dependability are significant; The more important thing is that fume afterheat is fully utilized, the approach of utilization is very extensive, can be used for heat-setting water, heat supply network recirculated water, cold wind etc., also can increase heating area, and the two income of Social benefit and economic benefit, market application foreground is wide.
To achieve these goals, the technical solution used in the present invention is:
Constant temperature economizer, comprises economizer body 1, and the external down-comer 2 of economizer body 1 forms closed cycle, and on circulation line, be provided with external heat exchanger 3, external heat exchanger 3 is provided with vavuum pump 4.
In this situation, described circulation line does not need arrange tubing pump, adopt water as circulatory mediator in down-comer 2, described external heat exchanger 3 is arranged vavuum pump 4 operating pressure is regulated and controled between 5-8 ten thousand Pa, economizer body 1 wall temperature is kept above more than acid dew point 10-15 DEG C, and described acid dew point is according to using coal and actual test SO
3cubage obtains.
Described economizer body 1 wall temperature remains between 80-95 DEG C.
The another kind of form of constant temperature economizer, comprises economizer body 1, it is characterized in that, the external down-comer 2 of economizer body 1 forms closed cycle, and on circulation line, be provided with external heat exchanger 3.That is, no longer need to arrange vavuum pump 4
In this situation, in described down-comer 2, adopt ethanol as circulatory mediator.
The heating surface of economizer body 1 of the present invention adopts spiral fin coil, and horizontal or vertical layout, former rows that described spiral fin coil enters at flue gas select stainless steel, and all the other select ordinary carbon steel.
Compared with prior art, the wall temperature of economizer of the present invention is constant to be remained between 80-95 DEG C, there is not cold end corrosion, and refrigerant flow rate is low in heating surface, resistance is little, does not need to arrange tubing pump, design cigarette speed is lower than 7m/s, heating surface wear speed is low, and equipment dependability improves, and fume afterheat is fully utilized.
Accompanying drawing explanation
Fig. 1 is the structural representation of the embodiment of the present invention one.
Fig. 2 is the structural representation of the embodiment of the present invention two.
Detailed description of the invention
Embodiments of the present invention are described in detail below in conjunction with drawings and Examples.
Embodiment one
As shown in Figure 1, constant temperature economizer, comprises economizer body 1, and the external down-comer 2 of economizer body 1 forms closed cycle, and on circulation line, be provided with external heat exchanger 3 and vavuum pump 4.In the present embodiment, water is as circulatory mediator, and endless form is closed cycle, Operation system setting closed cycle water pump and external heat exchanger 3, arrange vavuum pump 4 on external heat exchanger 3 top, by vavuum pump 4, system pressure is adjusted to 5-8 ten thousand Pa, economizer body 1 wall temperature remains between 80-95 DEG C.Ensure that any point wall temperature is higher than more than acid dew point 10-15 DEG C, and cold end corrosion does not occur, external heat exchanger can be used for heating cold wind, heat supply network recirculated water, condensate water etc.
The present embodiment adopts water as circulatory mediator, is regulated and controled between 5-8 ten thousand Pa by closed system operating pressure, thus realize constant wall temperature by vavuum pump.
Embodiment two
As shown in Figure 2, constant temperature economizer, comprises economizer body 1, and the external down-comer 2 of economizer body 1 forms closed cycle, and on circulation line, be provided with external heat exchanger 3.Ethanol is as circulatory mediator, endless form is closed cycle, external heat exchanger 3 top is without the need to arranging vavuum pump, system running pressure is normal pressure, ethanol vapourizing temperature is at ambient pressure 83 DEG C, and therefore economizer body 1 wall temperature remains on 83 DEG C, and external circulating system needs configuration cycles water pump, the heat that external cooling water and ethanol medium absorb carries out heat exchange, reaches the object that fume afterheat utilizes.
The present embodiment adopts the circulatory mediator that vapourizing temperature is low, and as ethanol, its normal pressure vapourizing temperature is 83 DEG C, thus realizes constant wall temperature.
Constant temperature economizer surface of the present invention can adopt spiral fin coil, and level, vertically layout, material can use ordinary carbon steel pipe, can ensure lower cost.In design process, should first according to using coal and actual test SO
3content, calculates acid dew point, and the standard being greater than acid dew point 10-15 DEG C according to wall temperature, designs the economizer of constant wall temperature, make run duration cold end corrosion not occur all the time.
After constant temperature economizer of the present invention is arranged in air preheater, compare Conventional cryogenic economizer, it has constant wall temperature, and the method that constant wall temperature realizes has two kinds, i.e. above-described embodiment one and embodiment two, finally reaches the object that flue-gas temperature is reduced to about 90 DEG C.
Creativeness of the present invention:
The environmental protection standard of new promulgation requires that all fired power generating unit soot emissions are lower than 20mg/Nm
3, key area soot emissions are lower than 5mg/Nm
3.Adopt wet-esp to be a kind of feasible program, replacement scheme builds low low temp. electric dedusting technology in addition, then connects wet desulphurization, also dust concentration can be reduced to 3-10mg/Nm
3low low temp. electric dedusting technology requires that exhaust gas temperature is reduced to about 90 DEG C, therefore, fume afterheat utilizes the reliability of equipment most important, Conventional cryogenic economizer is in operation and there is a lot of problem, as cold end corrosion, stifled ash and leakage etc., often cause economizer to stop transport, the long period reliability service problem resolving economizer is the key of low cryogenic technique.Constant temperature economizer of the present invention is exactly the invention solving this key technology.
In 300MW unit for, Conventional cryogenic economizer is for preventing cold end corrosion, wearing and tearing etc., the Ni-based ND corrosion resisting steel of heating surface material selection, heating surface direct cost about 7,000,000 yuan, and constant temperature economizer of the present invention has constant wall temperature control ability, heating surface adopts ordinary carbon steel thus, and heating surface direct cost about saves more than 1,000,000 yuan.
For expanding the approach that fume afterheat utilizes, the heat of Natural Circulation, by external heat exchanger and other working medium heat exchange, because system is Natural Circulation, saves the water circulating pump of forced circulation, runs power consumption low, and operation and maintenance cost about save 1/6.Operating cost is low, remarkable in economical benefits.
In structured design process, relate to following two aspect problems:
(1) system running pressure adjustment
When adopting water as circulatory mediator, adjustment System operating pressure is one of main feature of the present invention, vavuum pump can by between pressure adjusting to 5-8 ten thousand Pa, when pressure is 50,000 Pa, corresponding vapourizing temperature is 80 DEG C, and when pressure is 80,000 Pa, vapourizing temperature is 95 DEG C, adjustable between 80-95 DEG C, applied range.
When adopting ethanol as circulatory mediator, normal pressure runs, and the vapourizing temperature of ethanol is 83 DEG C, also can ensure that heating surface cold end corrosion does not occur, and does not need to arrange vavuum pump.
(2) circulatory mediator is selected
System is closed cycle, and therefore, circulatory mediator can be selected, and the present invention have selected the common water of nature and ethanol.
Therefore, in its work progress, first Calculation of Hydrodynamic should be carried out, next selects cooling medium, and the medium of Chang Xuan is divided into water and ethanol, finally according to design needs, determine the exhaust gas temperature that cooling medium and needs reach, and then certainty annuity operating pressure and wall temperature, the wall temperature of design needs higher than more than flue gas acid dew point 10-15 DEG C, ensures never cold end corrosion to occur.
Economizer material selection ordinary carbon steel, for preventing the anterior heating surface wear of flow of flue gas, former row can be designed to stainless steel tube again.
Claims (9)
1. constant temperature economizer, comprise economizer body (1), it is characterized in that, economizer body (1) external down-comer (2) forms closed cycle, and on circulation line, be provided with external heat exchanger (3), external heat exchanger (3) is provided with vavuum pump (4).
2. constant temperature economizer according to claim 1, is characterized in that, described circulation line not need arrange tubing pump.
3. constant temperature economizer according to claim 1 or 2, it is characterized in that, adopt water as circulatory mediator in described down-comer (2), described external heat exchanger (3) is arranged vavuum pump (4) by operating pressure regulation and control between 5-8 ten thousand Pa, economizer body (1) wall temperature is kept above more than acid dew point 10-15 DEG C.
4. constant temperature economizer according to claim 3, it is characterized in that, described economizer body (1) wall temperature remains between 80-95 DEG C.
5. constant temperature economizer according to claim 3, is characterized in that, described acid dew point is according to using coal and actual test SO
3cubage obtains.
6. constant temperature economizer, comprises economizer body (1), it is characterized in that, economizer body (1) external down-comer (2) forms closed cycle, and on circulation line, be provided with external heat exchanger (3).
7. constant temperature economizer according to claim 6, is characterized in that, adopts ethanol as circulatory mediator in described down-comer (2).
8. constant temperature economizer according to claim 1 or 6, is characterized in that, the heating surface of described economizer body (1) adopts spiral fin coil, horizontal or vertical layout.
9. constant temperature economizer according to claim 7, it is characterized in that, former rows that described spiral fin coil enters at flue gas select stainless steel, and all the other select ordinary carbon steel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510122659.9A CN104728826A (en) | 2015-03-19 | 2015-03-19 | Constant temperature economizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510122659.9A CN104728826A (en) | 2015-03-19 | 2015-03-19 | Constant temperature economizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104728826A true CN104728826A (en) | 2015-06-24 |
Family
ID=53452980
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510122659.9A Pending CN104728826A (en) | 2015-03-19 | 2015-03-19 | Constant temperature economizer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104728826A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105180144A (en) * | 2015-08-14 | 2015-12-23 | 中国能源建设集团广东省电力设计研究院有限公司 | Boiler flue gas waste heat recovery system |
| CN107504477A (en) * | 2016-06-14 | 2017-12-22 | 天津华赛尔传热设备有限公司 | A kind of pressure regulation heat-exchange system of low-level (stack-gas) economizer |
| CN109404879A (en) * | 2018-11-23 | 2019-03-01 | 北京米能科技有限公司 | A kind of small-sized DC boiler and its start and run water round-robin method |
Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5743199A (en) * | 1980-08-27 | 1982-03-11 | Hirakawa Tekkosho:Kk | Vacuum heat exchanger having temperature control unit |
| FR2554571A1 (en) * | 1983-11-04 | 1985-05-10 | Inst Francais Du Petrole | Method of heat exchange between a hot and cold fluid using a fluid mixture as the heat-carrying medium and producing a circulation of the heat-carrying medium by capillary attraction |
| CN1236876A (en) * | 1998-05-25 | 1999-12-01 | 中国船舶工业总公司第七研究院第七一一研究所 | Heat pipe type of coal saver resisting corrosion effectively |
| CN201715544U (en) * | 2010-08-20 | 2011-01-19 | 熊亚东 | Flue gas waste heat recovery system |
| CN201897411U (en) * | 2010-10-22 | 2011-07-13 | 青岛新能源科技有限公司 | Variable-pressure temperature-regulation waste heat recycling device |
| CN102410549A (en) * | 2011-11-10 | 2012-04-11 | 王海波 | Composite phase change heat exchange system for flue gas heat recovery of boiler |
| CN102410527A (en) * | 2011-11-10 | 2012-04-11 | 王海波 | Composite phase change heat exchanger for recovering waste heat of boiler flue gas |
| CN102435083A (en) * | 2011-12-15 | 2012-05-02 | 大连熵立得传热技术有限公司 | Split heat pipe heat exchanger with controllable heat pipe wall temperature |
| CN202734630U (en) * | 2012-08-11 | 2013-02-13 | 云南丰普科技有限公司 | Split type variable-conductance heat pipe |
| CN102997262A (en) * | 2011-09-19 | 2013-03-27 | 上海康洪精密机械有限公司 | System for improving utilization grade of flue gas afterheat |
| CN103486898A (en) * | 2013-09-13 | 2014-01-01 | 中国科学院工程热物理研究所 | Automatic safe control device of industrial waste heat recovery system |
| CN204678310U (en) * | 2015-03-19 | 2015-09-30 | 中国华能集团清洁能源技术研究院有限公司 | Constant temperature economizer |
-
2015
- 2015-03-19 CN CN201510122659.9A patent/CN104728826A/en active Pending
Patent Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5743199A (en) * | 1980-08-27 | 1982-03-11 | Hirakawa Tekkosho:Kk | Vacuum heat exchanger having temperature control unit |
| FR2554571A1 (en) * | 1983-11-04 | 1985-05-10 | Inst Francais Du Petrole | Method of heat exchange between a hot and cold fluid using a fluid mixture as the heat-carrying medium and producing a circulation of the heat-carrying medium by capillary attraction |
| CN1236876A (en) * | 1998-05-25 | 1999-12-01 | 中国船舶工业总公司第七研究院第七一一研究所 | Heat pipe type of coal saver resisting corrosion effectively |
| CN201715544U (en) * | 2010-08-20 | 2011-01-19 | 熊亚东 | Flue gas waste heat recovery system |
| CN201897411U (en) * | 2010-10-22 | 2011-07-13 | 青岛新能源科技有限公司 | Variable-pressure temperature-regulation waste heat recycling device |
| CN102997262A (en) * | 2011-09-19 | 2013-03-27 | 上海康洪精密机械有限公司 | System for improving utilization grade of flue gas afterheat |
| CN102410549A (en) * | 2011-11-10 | 2012-04-11 | 王海波 | Composite phase change heat exchange system for flue gas heat recovery of boiler |
| CN102410527A (en) * | 2011-11-10 | 2012-04-11 | 王海波 | Composite phase change heat exchanger for recovering waste heat of boiler flue gas |
| CN102435083A (en) * | 2011-12-15 | 2012-05-02 | 大连熵立得传热技术有限公司 | Split heat pipe heat exchanger with controllable heat pipe wall temperature |
| CN202734630U (en) * | 2012-08-11 | 2013-02-13 | 云南丰普科技有限公司 | Split type variable-conductance heat pipe |
| CN103486898A (en) * | 2013-09-13 | 2014-01-01 | 中国科学院工程热物理研究所 | Automatic safe control device of industrial waste heat recovery system |
| CN204678310U (en) * | 2015-03-19 | 2015-09-30 | 中国华能集团清洁能源技术研究院有限公司 | Constant temperature economizer |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105180144A (en) * | 2015-08-14 | 2015-12-23 | 中国能源建设集团广东省电力设计研究院有限公司 | Boiler flue gas waste heat recovery system |
| CN107504477A (en) * | 2016-06-14 | 2017-12-22 | 天津华赛尔传热设备有限公司 | A kind of pressure regulation heat-exchange system of low-level (stack-gas) economizer |
| CN109404879A (en) * | 2018-11-23 | 2019-03-01 | 北京米能科技有限公司 | A kind of small-sized DC boiler and its start and run water round-robin method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102305413B (en) | Exhaust gas waste heat recovery and emission reduction comprehensive application system for coal-fired boiler in thermal power plant | |
| CN204739568U (en) | Energy saving and emission reduction system that horizontal phase transition heat exchanger and prefix type hydrophily formula GGH unite | |
| CN207422196U (en) | A kind of CFB units combine afterheat utilizing system | |
| CN102330968A (en) | Two-stage flue gas heat exchanger system applied to thermal power plant | |
| CN109668165B (en) | Hot secondary air and flue gas waste heat utilization system and thermal generator set | |
| CN104964265A (en) | Energy-saving emission reduction system and energy-saving emission reduction method of horizontal type phase change heat exchanger and front-arrangement type water medium type GGH combined | |
| CN105180146A (en) | Multi-stage smoke waste heat recovery and comprehensive utilization system for combined heat and power plant | |
| CN102031999A (en) | Thermal power generator set with high-efficient circulating system | |
| CN109737446A (en) | A kind of recycling of power plant boiler smoke discharging residual heat and flue gas disappear white system | |
| CN102607010A (en) | Composite phase-change heat exchange system | |
| CN104848238A (en) | Electric dust removal heat exchange system | |
| CN113268887B (en) | Optimal heat source determining system and method for boiler air heater of coal electric unit | |
| CN104676622A (en) | Flue gas treatment system and flue gas reheating method based on fluoroplastic heat exchanger | |
| CN205332168U (en) | Waste heat comprehensive recovery utilization system of thermal power factory | |
| CN104728826A (en) | Constant temperature economizer | |
| CN204042853U (en) | Steam boiler waste heat reclaims and system for deoxidizing by heat power | |
| CN101261008B (en) | Liquid phase intermediate medium heat exchanging type heat exchanger | |
| CN203836943U (en) | Low-temperature coal economizer of 300MW circulating fluidized bed boiler | |
| CN206919053U (en) | A kind of surplus heat collection device for boiler smoke | |
| CN105674315A (en) | Double-circuit and double-circulation heat exchanging system | |
| CN204678310U (en) | Constant temperature economizer | |
| CN205388305U (en) | Novel low temperature second grade economizer | |
| CN204756887U (en) | High -efficient hot media water system of circulating fluidized bed boiler | |
| CN105674238B (en) | Wind-heat recover and the united energy-saving and emission-reduction system of fume afterheat depth retracting device and energy-saving and emission-reduction method | |
| CN204962712U (en) | System is used multipurposely in multistage recovery of cogeneration of heat and power power plant flue gas waste heat |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20150624 |
|
| RJ01 | Rejection of invention patent application after publication |