CN205607235U - Hot media water tubular heat exchanger control system - Google Patents
Hot media water tubular heat exchanger control system Download PDFInfo
- Publication number
- CN205607235U CN205607235U CN201620105192.7U CN201620105192U CN205607235U CN 205607235 U CN205607235 U CN 205607235U CN 201620105192 U CN201620105192 U CN 201620105192U CN 205607235 U CN205607235 U CN 205607235U
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- heat medium
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- medium water
- regulating valve
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 118
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 63
- 239000003546 flue gas Substances 0.000 claims abstract description 63
- 230000001105 regulatory effect Effects 0.000 claims abstract description 49
- 239000007789 gas Substances 0.000 claims abstract description 47
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000010438 heat treatment Methods 0.000 claims description 19
- 239000003795 chemical substances by application Substances 0.000 claims description 15
- 230000033228 biological regulation Effects 0.000 abstract description 13
- 239000000428 dust Substances 0.000 abstract description 10
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 230000003020 moisturizing effect Effects 0.000 abstract 2
- 239000012717 electrostatic precipitator Substances 0.000 abstract 1
- 235000019504 cigarettes Nutrition 0.000 description 18
- 238000013461 design Methods 0.000 description 14
- 238000005260 corrosion Methods 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 4
- 239000000779 smoke Substances 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 238000013517 stratification Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 239000003500 flue dust Substances 0.000 description 2
- 229910052602 gypsum Inorganic materials 0.000 description 2
- 239000010440 gypsum Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000017531 blood circulation Effects 0.000 description 1
- 230000004087 circulation Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000012716 precipitator Substances 0.000 description 1
- 230000007115 recruitment Effects 0.000 description 1
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- Chimneys And Flues (AREA)
Abstract
The utility model relates to a hot media water tubular heat exchanger control system, including gas cooler, flue gas heater, hot media water moisturizing case, hot media water pump, hot media water steam heater, a passageway hot media water water inlet regulating valve, B passageway hot media water water inlet regulating valve, hot media water bypass regulation valve and steam control valve, hot media water moisturizing case links to each other with flue gas heater and hot media water pump, and A passageway hot media water water inlet regulating valve and B passageway hot media water water inlet regulating valve are connected respectively to the hot media water pump, and A passageway hot media water water inlet regulating valve and B passageway hot media water water inlet regulating valve connect a set of gas cooler respectively, and two sets of gas coolers link to hot media water hot media water 2, hot media water steam heater reconnection to flue gas heater. The beneficial effects of the utility model are that: control flue gas cooler outlet's that can be fine flue -gas temperature maintains certain within range, the better dust collection efficiency that assurance electrostatic precipitator is high.
Description
Technical field
This utility model patent relates to control system, particularly relates to a kind of heat medium water pipe heat exchanger control system.
Background technology
For solving " gypsum rain " problem that coal-burning power plant the most generally exists, and it is the tightest preferably to meet flue gas pollutant
The emission request of lattice, typically arranges heat medium water pipe heat exchanger, and it includes gas cooler and flue gas heater.It can reach
Three below purpose: before gas cooler is arranged on dry electrostatic cleaner, is lowered into the flue-gas temperature of electric cleaner, respectively
Plant the temperature of control entrance electric cleaner under operating mode and maintain in certain scope, it is ensured that the efficiency of dust collection that electric cleaner is higher；
After flue gas heater is arranged in wet electrical dust precipitator, transmit heat by heat medium water medium, compared with swinging GGH, will not
Cause smoke spillage, more preferably ensure desulfurization and dust removing effects；Being utilized by fume afterheat, lifting enters the flue-gas temperature of chimney,
" gypsum rain " problem of solution.
In the unit starting stage, ignition of the boiler produces flue gas SO2、SO3And flue gas water smoke, if gas cooler and flue gas add
Hot device water temperature is less than flue-gas temperature, can cause gas cooler and flue gas heater tube wall condensation, corrosion, cool down because of flue gas simultaneously
Environment dust concentration residing for device is higher, easily makes flue dust stick, dust stratification and fouling, affects heat-transfer surface and deteriorates.At compressor emergency shutdown
Process, is similar to the unit starting stage, and flue-gas temperature, less than flue gas dew point temperature, brings corrosion to gas cooler.At machine
Group normal course of operation in, need ensure matchmaker's waterpipe type heat exchanger under various operating modes the flue-gas temperature of electric cleaner entrance one
In the range of Ding, need to ensure that the flue-gas temperature of flue gas heater outlet reaches to design requirement under various operating modes, needs to ensure respectively
Plant the heat-transfer surface of gas cooler and flue gas heater under operating mode not occur because of the low dust stratification caused of heat exchanger tube wall temperature and corrosion.
Utility model content
The purpose of this utility model is to overcome prior art not enough, provides a kind of rational in infrastructure, meets the heating agent water pipe of requirements
Formula Heat Exchanger Control System.
For achieving the above object, this utility model have employed techniques below scheme:
Heat medium water pipe heat exchanger control system, including gas cooler, flue gas heater, heat medium water water supply tank, heating agent water pump,
Heat medium water steam heater, A channel heat medium water inlet regulating valve, channel B heat medium water inlet regulating valve, heat medium water bypass valve
And steam control valve, described heat medium water water supply tank is connected with flue gas heater and heating agent water pump, and heating agent water pump connects A channel respectively
Heat medium water inlet regulating valve and channel B heat medium water inlet regulating valve, A channel heat medium water inlet regulating valve and channel B heat medium water enter
Water regulating valve connects one group of gas cooler respectively, and two groups of gas coolers are connected to heat medium water steam heater, and described heat medium water steams
Vapour heater is then connected to flue gas heater, is additionally provided with heat medium water bypass regulation between heating agent water pump and heat medium water steam heater
Valve.
As preferably: described heat medium water steam heater is provided with vapour source and steam control valve.
The beneficial effects of the utility model are:
1, the flue-gas temperature that can well control gas cooler outlet under the various operating condition of unit maintains in certain scope
In, preferably ensure the efficiency of dust collection that electric cleaner is high.
2, under the various operating condition of unit, it is ensured that the cigarette temperature of flue gas heater outlet reaches to design requirement.
3, under the various operating condition of unit, the tube wall temperature of heat medium water pipe heat exchanger is at utmost ensured, it is to avoid flue gas cools down
Device and the condensation of flue gas heater pipe wall of heat exchange pipe and corrosion.
4, the flue dust come because of the environment dust concentration higher band residing for gas cooler can be avoided to stick, dust stratification and fouling, impact is changed
Hot side also deteriorates.
Accompanying drawing explanation
Fig. 1 is this utility model structural representation；
Description of reference numerals: heat medium water water supply tank 1, heating agent water pump 2, A channel heat medium water inlet regulating valve 3, channel B heating agent
Water inlet regulating valve 4, heat medium water bypass valve 5, gas cooler 6, heat medium water steam heater 7, flue gas heater 8,
Vapour source 9, steam control valve 10.
Detailed description of the invention
Below in conjunction with embodiment, this utility model is described further.The explanation of following embodiment is only intended to help and understands this reality
With novel.It should be pointed out that, for those skilled in the art, in the premise without departing from this utility model principle
Under, it is also possible to this utility model is carried out some improvement and modification, and these improve and modification also falls into this utility model claim
Protection domain in.
Outside the heat medium water pipe heat exchanger smoke abatement Gas Cooler 6 of the present embodiment and flue gas heater 8, it is made up of following aid system:
Heat medium water water charging system, capital equipment includes heat medium water water supply tank 1, heat medium water blood circulation, capital equipment include heating agent water pump 2,
Heat medium water steam heating system, capital equipment includes heat medium water steam heater 7 and corresponding adjusting control valve door, mainly includes
A channel heat medium water inlet regulating valve 3, channel B heat medium water inlet regulating valve 4, heat medium water bypass valve 5 and steam control valve
10 compositions such as grade.
1 system signal with reference to the accompanying drawings, in unit starting, the different phase running and stop transport, heat medium water pipe heat exchanger is taked not
Same control model.
In the unit starting stage, unit air-introduced machine completes the upper water conservancy project of heat medium water pipe heat exchanger and makees before starting.Before ignition of the boiler
Preheating heat medium water, carries out tube wall intensification to gas cooler 6 and flue gas heater 8.Before ignition of the boiler, gas cooler
6 and flue gas heater 8 in heat medium water together circulate intensification, now gas cooler 6 exit water temperature is minimum, makes this point
Water temperature is higher than flue gas acid dew point, can control the heating agent water temperature lower limit of whole system well.Standard-sized sheet A channel inlet regulating valve 3 can be passed through
With channel B inlet regulating valve 4, fully closed heat medium water bypass valve 5, heat medium water bypass valve 5 is according to gas cooler 6
Outlet heat medium water temperature gradually adjusts and follows the tracks of, until temperature reaches design load.After ignition of the boiler, when flue-gas temperature is relatively low,
Heat medium water and flue gas will occur heat exchange, and flue gas will take away partial heat, when the heating capacity of heat medium water steam heater 7 is enough,
Use gas cooler 6 and flue gas heater 8 to circulate intensification simultaneously；Heating capacity at heat medium water steam heater 7 has in limited time,
Gas cooler 6 being isolated, it is ensured that the tube wall temperature of flue gas heater 8, now flue gas heater 8 exit water temperature is minimum,
This water temperature should be made higher than flue gas acid dew point, can control heat medium water temperature lower limit well.By fully closed A channel inlet regulating valve 3 and B
Passage inlet regulating valve 4, standard-sized sheet heat medium water bypass valve 5, and gradually adjust heat medium water according to flue gas heater 8 exit water temperature
The aperture of bypass valve 5 is also followed the tracks of, until temperature reaches design load.
The most warmed up to normally at unit normal operating phase, gas cooler 6 and flue gas heater 8 heat medium water.Flue gas cools down
Device 6 exports cigarette temperature and rises, then open big A channel inlet regulating valve 3 and channel B inlet regulating valve 4, turns down heat medium water bypass and adjusts
Joint valve 5；Gas cooler 6 exports cigarette temperature and declines, then turn down A channel inlet regulating valve 3 and channel B inlet regulating valve 4,
Opening big heat medium water bypass valve 5, major control gas cooler 6 exports cigarette temperature in design load scope.Flue gas heater 8 goes out
Mouth cigarette temperature rises, then turn down steam control valve 10；Otherwise anti-then, control flue gas heater 8 export cigarette temperature in scope of design.
In the unit outage stage, standard-sized sheet heat medium water bypass valve 5, fully closed A channel inlet regulating valve 3 and channel B water inlet are adjusted
Joint valve 4, heating agent water pump 2 runs, and keeps the circulation of other system beyond smoke abatement Gas Cooler 6.Increase steam control valve 10 to open
Degree, flue gas heater 8 heat medium water passes through steam heating and thermal insulation, and gas cooler 6 heat medium water then synchronizes to decline with cigarette temperature, until
Boiler flameout.In the stages of not stopping transport such as generator set desulfurization absorption tower recirculation pumps, control flue gas heater 8 exports heating agent water temperature and is higher than
Flue gas dew point temperature.The non-ignition phase of boiler in air flowing, keeps flue gas heater 8 to export heat medium water temperature and is slightly above cigarette
Temperature.
Illustrate in conjunction with accompanying drawing 1 system, to heat medium water pipe heat exchanger system, mainly take following control thinking:
By A channel inlet regulating valve 3, channel B inlet regulating valve 4 and heat medium water bypass valve 5, regulate heat medium water flow
The flue-gas temperature that gas cooler exports is controlled at certain temperature range；In the case of unit underload, pass through steam control valve
The magnitude of recruitment of 10 regulation auxiliary steams, controls flue gas heater 8 exit gas temperature and reaches design load or control gas cooler
6 leaving water temperatures reach design load.Native system configuration logic is mainly the design of the regulating loop of 4 regulation valves.State respectively such as
Under:
Heat medium water bypass valve 5:
First as gas cooler 6 regulates control, mainly controls the maximum caloric receptivity that gas cooler 6 can be accomplished,
I.e. when A channel inlet regulating valve 3 and channel B inlet regulating valve 4 standard-sized sheet, gas cooler 6 reaches maximum caloric receptivity.It is opened
Following principle is followed in degree setting: unit at full capacity time, heat medium water bypass valve 5 is fully closed, gas cooler 6 can be exported cigarette
Temperature control is below flue gas dew point temperature.During minimum load, A channel inlet regulating valve 3 and channel B inlet regulating valve 4 are fully closed,
Heat medium water bypass valve 5 standard-sized sheet, makes gas cooler 6 export cigarette temperature and is maintained at more than flue gas acid dew point temperature.Owing to A leads to
The control object of road inlet regulating valve 3 and channel B inlet regulating valve 4 is also that gas cooler 6 exports cigarette temperature, for avoiding the occurrence of
There is " intersect confusion " phenomenon with heat medium water bypass valve 5 in A channel inlet regulating valve 3 and channel B inlet regulating valve 4,
When the initial stage of carrying out debugs, the valve position of heat medium water bypass valve 5 regulates with unit load as foundation.
A channel inlet regulating valve 3 and channel B inlet regulating valve 4:
Second as gas cooler 6 regulates control, mainly controls unit gas cooler 6 under different load operating mode
Outlet cigarette temperature is in reasonable interval, and the regulation of relative first is the finest.When its regulation can not meet system condition, need to coordinate
Heat medium water bypass valve 5 regulates gas cooler performance.
A channel inlet regulating valve 3 and channel B inlet regulating valve 4 mainly export the closed loop regulation of cigarette temperature with gas cooler 6,
By regulation A channel inlet regulating valve 3 and the aperture of channel B inlet regulating valve 4, it is ensured that gas cooler 6 exports cigarette Wen Da
To design load.For the hysteresis avoiding whole system to regulate, it is simultaneously introduced unit load and gas cooler 6 exports the actual measurement of cigarette temperature
The temperature difference of value and setting value is as feedforward.
Steam control valve 10:
In the different phase of unit load, steam control valve 10 exports cigarette temperature according to flue gas heater 8, flue gas heater 8 exports
Water temperature, heat medium water steam heater 7 inlet water temperature use different controlled plants.3 closed loop regulations of major design: with flue gas
Heater 8 exports the closed loop regulation of cigarette temperature, and it is mainly by regulation steam control valve 10 aperture, it is ensured that flue gas heater 8 exports
Cigarette temperature reaches design load, regulates with the closed loop of gas cooler 6 exit water temperature, and it is mainly by regulation steam control valve 10 aperture,
Ensure that gas cooler 6 exit water temperature reaches design load；Regulating with the closed loop of flue gas heater 8 exit water temperature, it mainly passes through
Regulation steam control valve 10 aperture, it is ensured that flue gas heater 8 exit water temperature reaches design load.
This utility model is applied at Zhejiang Zhe Nengjiahua electricity generating corporation, Ltd #3 unit～#8 unit, controls respond well.
Claims (2)
- null1. a heat medium water pipe heat exchanger control system，It is characterized in that: include gas cooler (6)、Flue gas heater (8)、Heat medium water water supply tank (1)、Heating agent water pump (2)、Heat medium water steam heater (7)、A channel heat medium water inlet regulating valve (3)、Channel B heat medium water inlet regulating valve (4)、Heat medium water bypass valve (5) and steam control valve (10)，Described heat medium water water supply tank (1) is connected with flue gas heater (8) and heating agent water pump (2)，Heating agent water pump (2) connects A channel heat medium water inlet regulating valve (3) and channel B heat medium water inlet regulating valve (4) respectively，A channel heat medium water inlet regulating valve (3) and channel B heat medium water inlet regulating valve (4) connect one group of gas cooler (6) respectively，Two groups of gas coolers (6) are connected to heat medium water steam heater (7)，Described heat medium water steam heater (7) is then connected to flue gas heater (8)，Heat medium water bypass valve (5) it is additionally provided with between heating agent water pump (2) and heat medium water steam heater (7).
- Heat medium water pipe heat exchanger control system the most according to claim 1, it is characterised in that: described heat medium water steam heater (7) is provided with vapour source (9) and steam control valve (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620105192.7U CN205607235U (en) | 2016-02-01 | 2016-02-01 | Hot media water tubular heat exchanger control system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620105192.7U CN205607235U (en) | 2016-02-01 | 2016-02-01 | Hot media water tubular heat exchanger control system |
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| Publication Number | Publication Date |
|---|---|
| CN205607235U true CN205607235U (en) | 2016-09-28 |
Family
ID=56960388
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620105192.7U Active CN205607235U (en) | 2016-02-01 | 2016-02-01 | Hot media water tubular heat exchanger control system |
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| Country | Link |
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| CN (1) | CN205607235U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105571381A (en) * | 2016-02-01 | 2016-05-11 | 浙江天地环保工程有限公司 | Control system and method for heat medium water pipe type heat exchanger |
| CN107023815A (en) * | 2017-04-25 | 2017-08-08 | 广东电网有限责任公司电力科学研究院 | The temprature control method of the indirect flue gas heat-exchange unit of 600MW coal-burning boilers |
| CN114110600A (en) * | 2021-11-08 | 2022-03-01 | 西安交通大学 | Heat storage quick start type garbage pyrolysis gasification system and method thereof |
-
2016
- 2016-02-01 CN CN201620105192.7U patent/CN205607235U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105571381A (en) * | 2016-02-01 | 2016-05-11 | 浙江天地环保工程有限公司 | Control system and method for heat medium water pipe type heat exchanger |
| CN107023815A (en) * | 2017-04-25 | 2017-08-08 | 广东电网有限责任公司电力科学研究院 | The temprature control method of the indirect flue gas heat-exchange unit of 600MW coal-burning boilers |
| CN107023815B (en) * | 2017-04-25 | 2019-04-12 | 广东电网有限责任公司电力科学研究院 | The temprature control method of the indirect flue gas heat-exchange unit of 600MW coal-burning boiler |
| CN114110600A (en) * | 2021-11-08 | 2022-03-01 | 西安交通大学 | Heat storage quick start type garbage pyrolysis gasification system and method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: Hangzhou City, Zhejiang province 310012 Huaxing Road No. 99 (Hangzhou Neusoft business building) Co-patentee after: ZHEJIANG ZHENENG WENZHOU POWER GENERATION CO.,LTD. Patentee after: Zhejiang Tiandi Environmental Protection Technology Co.,Ltd. Address before: Hangzhou City, Zhejiang province 310012 Huaxing Road No. 99 (Hangzhou Neusoft business building) Co-patentee before: ZHEJIANG ZHENENG WENZHOU POWER GENERATION Co.,Ltd. Patentee before: ZHEJIANG TIANDI ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. |
|
| CP03 | Change of name, title or address |
Address after: 310012 99 Huaxing Road, Xihu District, Hangzhou, Zhejiang (Hangzhou Neusoft business building) Patentee after: Zhejiang Zheneng Technology Environmental Protection Group Co.,Ltd. Country or region after: China Patentee after: ZHEJIANG ZHENENG WENZHOU POWER GENERATION CO.,LTD. Address before: No.99, Huaxing Road, Hangzhou City, Zhejiang Province (Hangzhou Neusoft venture building) Patentee before: Zhejiang Tiandi Environmental Protection Technology Co.,Ltd. Country or region before: China Patentee before: ZHEJIANG ZHENENG WENZHOU POWER GENERATION CO.,LTD. |