CN106090971A - A kind of combined steam flue gas MGGH system and method - Google Patents
A kind of combined steam flue gas MGGH system and method Download PDFInfo
- Publication number
- CN106090971A CN106090971A CN201610587174.1A CN201610587174A CN106090971A CN 106090971 A CN106090971 A CN 106090971A CN 201610587174 A CN201610587174 A CN 201610587174A CN 106090971 A CN106090971 A CN 106090971A
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- water
- flue gas
- steam
- heat exchanger
- smoke
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 61
- 239000003546 flue gas Substances 0.000 title claims abstract description 61
- MXWHMTNPTTVWDM-NXOFHUPFSA-N mitoguazone Chemical compound NC(N)=N\N=C(/C)\C=N\N=C(N)N MXWHMTNPTTVWDM-NXOFHUPFSA-N 0.000 title claims abstract description 30
- 238000000034 method Methods 0.000 title claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 86
- 239000007789 gas Substances 0.000 claims abstract description 40
- 239000000779 smoke Substances 0.000 claims abstract description 33
- 238000009833 condensation Methods 0.000 claims abstract description 14
- 230000005494 condensation Effects 0.000 claims abstract description 14
- 230000002209 hydrophobic effect Effects 0.000 claims abstract description 6
- 238000001556 precipitation Methods 0.000 claims abstract description 5
- 238000012546 transfer Methods 0.000 claims abstract description 4
- 235000019504 cigarettes Nutrition 0.000 claims description 16
- 238000010438 heat treatment Methods 0.000 claims description 11
- 238000011084 recovery Methods 0.000 claims description 9
- 238000006243 chemical reaction Methods 0.000 claims description 7
- 230000008676 import Effects 0.000 claims description 6
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 238000010521 absorption reaction Methods 0.000 claims description 3
- 230000008859 change Effects 0.000 claims description 3
- 239000003245 coal Substances 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- 238000013459 approach Methods 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 239000003517 fume Substances 0.000 abstract description 2
- 238000006477 desulfuration reaction Methods 0.000 description 9
- 230000023556 desulfurization Effects 0.000 description 9
- 230000003009 desulfurizing effect Effects 0.000 description 6
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 230000001932 seasonal effect Effects 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 230000006978 adaptation Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- 235000017550 sodium carbonate Nutrition 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 235000019738 Limestone Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 235000010216 calcium carbonate Nutrition 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 230000010148 water-pollination Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/08—Arrangements of devices for treating smoke or fumes of heaters
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Treating Waste Gases (AREA)
- Chimneys And Flues (AREA)
Abstract
A kind of combined steam flue gas MGGH system, on connection flue between boiler air preheater and cleaner unit, gas cooler is set, on connection flue between desulfurizer and chimney, smoke re-heater is set, the hot arc circulating water pipeline between gas cooler and smoke re-heater arranges supplementary heat exchanger；Circulating water pipeline and the terminal valve regulation system of connection are set between gas cooler, smoke re-heater, supplementary heat exchanger, supplementary heat exchanger is also connected be provided with steam inlet, hydrophobic outlet conduit, condensation water inlet pipeline, condense water exit conduit and control flow into steam or condense the valve transfer regulation system of water, achieve and electric precipitation gas approach temperature under various operating mode, can be automatically controlled, automatically control smoke stack emission temperature, there is while realizing fume emission environmental requirement the technique effect economized on coal, economize on water, reduce smoke discharge amount.
Description
Technical field
The present invention relates to a kind of thermal power plant minimum discharge MGGH (intermediate heat media flue gas heat-exchange unit: Media Gas-
GasHeater) energy-saving environmental protection device and method, belongs to thermal power plant's minimum discharge MGGH technical field.
Background technology
The minimum discharge problem of coal-fired plant boiler smoke evacuation has obtained country's attention, in developed area such as
The place such as the Yangtze River Delta, Zhujiang River triangle emits white cigarette to chimney and the most quite payes attention to.The leakage of the GGH system owing to using in the past causes
It is unable to reach minimum discharge, so the application of MGGH is more and more universal.
Flue gas desulfurization (Fluegasdesulfurization is called for short FGD).The lime-gypsum stone wet method cigarette of coal-fired flue-gas
Desulfurization technology is the desulfurization technology that current application is the widest, efficiency is the highest.For coal-burning power plant, considerably long in modern later
In period, FGD will be the main method controlling SO2 discharge.Flue gas desulfurization mainly has dry type flue gas desulfurizing and wet process of FGD
Two kinds.Wherein wet fuel gas desulfurizing technology flow process, form and mechanism are similar, mainly use limestone (CaCO3), Calx
(CaO) or the serosity such as sodium carbonate (Na2CO3) makees detergent, in reaction tower, flue gas is washed, thus remove in flue gas
SO2.This technique history of existing 50 years, after continuously improving and improving, Technical comparing is ripe, and has desulfurization effect
Rate high (90%～98%), unit capacity is big, and coal adaptability is strong, and operating cost is relatively low and the advantage such as side-product easily recovery.Also
Wet desulfurizing process just so that flue gas after desulfurization water capacity increases, these with saturated wet flue gas state from desulfurizing tower discharge into
Enter chimney and arrange the flue gas to air, cause grand chimney and emit white cigarette phenomenon.
Since saturated wet flue gas state can emit white cigarette from chimney discharge, then heating neat stress disengages it from saturation again
Discharge just can alleviate and emit white cigarette phenomenon, thus utilize the neat stress after the heating desulfurizing tower of the flue gas heat before desulfurizing tower, MGGH skill
Extensively arising at the historic moment of art.After solving the key technical problem of flue gas low-temperature corrosion, the economy of MGGH system seems
Important, how on the premise of reaching neat stress emission request, improve benefit of saving coal as far as possible and become as vast electric power skill
The target that art worker pursues
Existing MGGH (tubular type flue gas heat-exchange unit, hydrophily formula flue gas heat-exchange unit, tubular type GGH) system, uses auxiliary in winter to steam
The mode of vapour heating regulates flue-gas temperature, and whole system is when summer condition runs, and substantial amounts of smoke discharging residual heat enters with heat medium water
Desulfurization fume exhaust, the waste that assembly is meaningless.Meanwhile, before lacking regulation cleaner unit summer, gas cooler exports the means of cigarette temperature, presses
Heat exchange area bigger than normal need to be designed according to existing design with summer condition gas cooler, cause the waste of metal material, in the winter time
Under operating mode and be not suitable with.Meanwhile, need to control well the inlet flue gas temperature of cleaner unit, for electric dust collector, reduce flue-gas temperature, subtract
Lack flue gas volume flow, reduced the ratio resistance of dust, improve efficiency of dust collection, reduce dedusting power consumption.Cloth bag is removed
Dirt device, controls flue-gas temperature, prevents overtemperature flue gas from entering, it is ensured that the safety of device and reduce dedusting power consumption.Mesh
It is poor that front MGGH system adapts to seasonal variations ability to work.
Summary of the invention
The invention aims to solve the problem that existing MGGH adapts to seasonal variations ability.The present invention uses heating agent
Water uses auxiliary steam to heat winter, and summer heats the mode of low pressure condensation water, together with gas cooler, flue gas heater,
Solve the problem that existing power plant desulfurization exhaust gas temperature is low.
In order to solve above-mentioned technical problem, the technical scheme is that and provide a kind of combined steam flue gas MGGH system
System, the connection flue between boiler air preheater and cleaner unit arranges gas cooler, between desulfurizer and chimney
Connect and on flue, smoke re-heater is set, cleaner unit, air-introduced machine and desulfurization are set between gas cooler and smoke re-heater
Device, it is characterised in that on the hot arc circulating water pipeline between gas cooler and smoke re-heater, supplementary heat exchanger is set；
Circulating water pipeline and the terminal valve regulation system of connection are set between gas cooler, smoke re-heater, supplementary heat exchanger,
Supplementary heat exchanger is also connected be provided with steam inlet, hydrophobic outlet conduit, condensation water inlet pipeline, condense water out
Pipeline and control flow into steam or condense the valve transfer regulation system of water.
Also provide for the operation method of a kind of combined steam flue gas MGGH system, comprise the steps:
Cleaner unit import cigarette temperature is set as predetermined value, it is achieved low temp. electric dedusting；
Chimney emission temperature is set as predetermined value, eliminates and emit white cigarette phenomenon；
During winter operation, the supplementary heat exchanger in flue gas MGGH system accesses heat recovery steam to carry out utilizing steam concurrent heating to work
Pattern；
During summer operation, the supplementary heat exchanger in flue gas MGGH system accesses condensation water to carry out utilizing condensation water heat absorption work
Pattern；
When break down work or be not required to come into operation supplementary heat exchanger time, can by pipe valve open association bypass, open
The bypass valve in parallel of supplementary heat exchanger, do not come into operation this supplementary heat exchanger.
The present invention contrasts prior art a following beneficial effect: the invention provides combined steam flue gas MGGH system
System, it is achieved steam auxiliary heating and condense water heat absorption switch operating, it is ensured that various operating modes can offset variation of ambient temperature and
The unit load change impact on exhaust gas temperature, no matter how ambient temperature changes, no matter how unit load changes, real
Show and electric precipitation gas approach temperature under various operating mode, can have been automatically controlled, automatically controlled smoke stack emission temperature, realized flue gas
There is while discharge-ring guaranteed request the technique effect economized on coal, economize on water, reduce smoke discharge amount.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention
Wherein: cleaner unit 2, air-introduced machine 3, desulfurizer 4, chimney 9, gas cooler 1, smoke re-heater 5, water circulating pump
6, supplementary heat exchanger 7, low-pressure heater 8
Detailed description of the invention
For making the present invention become apparent, hereby with preferred embodiment, and accompanying drawing is coordinated to be described in detail below.
With reference to the accompanying drawings shown in 1, the present embodiment provides a kind of combined flue gas MGGH system, at boiler air preheater and cleaner unit
Between connection flue on gas cooler 1 is set, the connection flue between desulfurizer 4 and chimney arranges flue gas reheat
Device 5, the hot arc circulating water pipeline between gas cooler 1 and smoke re-heater 5 arranges supplementary heat exchanger 7, cold at flue gas
Cleaner unit 2, air-introduced machine 3 and desulfurizer 4 are but set between device 1 and smoke re-heater 5, at gas cooler 1 and flue gas reheat
On cold section of circulating water pipeline between device 5, frequency conversion water circulating pump 6 is set, by figure signal at gas cooler 1, smoke re-heater
5, circulating water pipeline and the terminal valve regulation system of connection are set between supplementary heat exchanger 7, supplementary heat exchanger 7 also connects
Connect and be provided with steam inlet, hydrophobic outlet conduit, condensation water inlet pipeline, condense water exit conduit and control to flow into steam
Or condense the valve transfer regulation system of water.
Also set up in parallel with supplementary heat exchanger on hot arc circulating water pipeline between gas cooler 1 with smoke re-heater 5
Bypass duct, utilize control valve to switch coming into operation or bypassing of supplementary heat exchanger.
Entrance point and the port of export at one-level low-pressure heater are drawn and are condensed water inlet pipeline, condensation water exit conduit, point
It is not connected to the steam inlet of supplementary heat exchanger and hydrophobic outlet conduit, utilizes control valve to control to switch into auxiliary
Heat exchanger add vapours or condense water.
By existing gas cooler, flue gas heater, supplementary heat exchanger system in access from low-pressure heater
Condensate line, can by supplementary heat exchanger change become utilize winter steam heating gas cooler, flue gas heater in
Heating agent recirculated water, utilizes the heating agent circulating water heating in gas cooler, flue gas heater to condense the seasonal adaptation of water summer
Heat exchanger.
A kind of combined steam flue gas MGGH operation method, comprises the steps:
Cleaner unit 2 import cigarette temperature is set as 90 DEG C (or between 85 DEG C-95 DEG C a certain require data), it is achieved low temperature
Electric precipitation；
Chimney emission temperature is set as 80 DEG C (or a certain required values), eliminates and emit white cigarette phenomenon；
During winter operation, follow according to gas cooler exit gas temperature (electric precipitation inlet flue gas temperature) regulation heat medium water system
The ring water yield, quantity of circulating water can be adjusted, according to smoke re-heater inlet water temperature (smoke re-heater by frequency conversion water circulating pump 6
Import and export cigarette temperature as feedforward) regulation heat recovery steam amount.Heat recovery steam can use inlet steam to regulate valve regulation.
During summer operation, according to smoke re-heater exit gas temperature (chimney inlet flue gas temperature) regulation heat medium water system circulation
The water yield, quantity of circulating water can be adjusted by frequency conversion water circulating pump 6, and according to gas cooler inlet water temperature, (gas cooler goes out
Mouth cigarette temperature is as feedforward) regulate the condensing water flow from low-pressure heater, low-pressure heater branch road condenses hydromining frequency conversion water
Pump and regulation valve mode regulate.
Spring and autumn or be not required to come into operation seasonal adaptation heat exchanger time, open the bypass valve in parallel of supplementary heat exchanger, do not come into operation
This supplementary heat exchanger.
When being embodied as, by detection gas cooler 1, the smoke entrance temperature of smoke re-heater 5, heat medium water, coagulate
Bear water the parameters such as out temperature, and by signal inputs such as flue-gas temperature flow, heat medium water flow temperature, condensing water flow temperature
In control system, control system controls the operating of whole system.
Smoke entrance flow, temperature and heat medium water according to gas cooler and smoke re-heater import and export flow, temperature
Degree, steam parameter, condensing water flow temperature, be automatically adjusted the heat recovery steam flow of access or from the condensation water of low-pressure heater
Flow, so that adapting with the heat needed for smoke re-heater, controls the heat medium water inlet temperature of smoke re-heater 5 95 simultaneously
About DEG C, it is ensured that enter the flue-gas temperature of chimney 10 at about 80 DEG C.
The steam flow entered is by carrying out valve regulated, and the condensing water flow from low-pressure heater passes through water inlet pipe water
Pump and valve regulated.
When break down work or be not required to come into operation supplementary heat exchanger time, can by pipe valve open association bypass, utilize
Bypass maintenance system in parallel is properly functioning.
Although the present invention is open as above with preferred embodiment, but it is not for limiting the present invention, any this area skill
Art personnel without departing from the spirit and scope of the present invention, can make possible variation and amendment, the therefore guarantor of the present invention
The scope of protecting should be defined in the range of standard with the claims in the present invention.
Claims (10)
1. a combined steam flue gas MGGH system, the connection flue between boiler air preheater and cleaner unit arranges flue gas
Cooler, the connection flue between desulfurizer and chimney arranges smoke re-heater, at gas cooler and flue gas reheat
Cleaner unit, air-introduced machine and desulfurizer are set between device, it is characterised in that the heat between gas cooler and smoke re-heater
On section circulating water pipeline, supplementary heat exchanger is set；Following of connection is set between gas cooler, smoke re-heater, supplementary heat exchanger
Ring waterpipe and terminal valve regulation system, be also connected with being provided with steam inlet, hydrophobic outlet on supplementary heat exchanger
Pipeline, condensation water inlet pipeline, condensation water exit conduit and control flow into the valve transfer of steam or condensation water and regulate system.
Combined steam flue gas MGGH system the most according to claim 1, it is characterised in that gas cooler and flue gas reheat
Also set up the bypass duct in parallel with supplementary heat exchanger on circulating water pipeline between device, utilize control valve to change to switch auxiliary
The coming into operation or bypassing of hot device.
Combined steam flue gas MGGH system the most according to claim 1, it is characterised in that at gas cooler with flue gas again
On cold section of circulating water pipeline between hot device, water circulating pump is set；Use variable frequency pump.
Combined steam flue gas MGGH system the most according to claim 1, it is characterised in that in entering of one-level low-pressure heater
Mouth end and the port of export are drawn and are condensed water inlet pipeline, condensation water exit conduit, are connected respectively to the steam inlet of supplementary heat exchanger
Pipeline and hydrophobic outlet conduit, utilize control valve to control to switch into adding vapours or condensing water of supplementary heat exchanger.
Combined steam flue gas MGGH system the most according to claim 4, it is characterised in that low-pressure heater branch road condenses water
Variable frequency pump and regulation valve mode is used to regulate.
6. an operation method for combined steam flue gas MGGH system, comprises the steps:
Cleaner unit import cigarette temperature is set as predetermined value, it is achieved low temp. electric dedusting；
Chimney emission temperature is set as predetermined value, eliminates and emit white cigarette phenomenon；
During winter operation, the supplementary heat exchanger in flue gas MGGH system accesses heat recovery steam to carry out utilizing steam concurrent heating Working mould
Formula；
During summer operation, the supplementary heat exchanger in flue gas MGGH system accesses condensation water to carry out utilizing condensation water heat absorption Working mould
Formula；
When break down work or be not required to come into operation supplementary heat exchanger time, can by pipe valve open association bypass, open auxiliary
Heat exchangers in parallel bypass valve, do not come into operation this supplementary heat exchanger.
The operation method of combined steam flue gas MGGH system the most according to claim 6, it is characterised in that winter operation
Time, regulating heat medium water system quantity of circulating water according to gas cooler exit gas temperature, quantity of circulating water can pass through frequency conversion recirculated water
Pump is adjusted, and regulates heat recovery steam amount according to smoke re-heater inlet water temperature.
The operation method of combined steam flue gas MGGH system the most according to claim 7, it is characterised in that the most further may be used
Utilize electric precipitation inlet flue gas temperature to regulate heat medium water system quantity of circulating water, utilize smoke re-heater to import and export cigarette temperature as feed-forward regulation
Heat recovery steam amount, heat recovery steam can use inlet steam to regulate valve regulation.
The operation method of combined steam flue gas MGGH system the most according to claim 6, it is characterised in that summer operation
Time, regulating heat medium water system quantity of circulating water according to smoke re-heater exit gas temperature, quantity of circulating water can pass through frequency conversion recirculated water
Pump is adjusted, and regulates the condensing water flow from low-pressure heater according to gas cooler inlet water temperature.
The operation method of combined steam flue gas MGGH system the most according to claim 9, it is characterised in that the most further
Available chimney inlet flue gas temperature regulation heat medium water system quantity of circulating water, utilizes gas cooler outlet cigarette temperature to coagulate as feed-forward regulation
Bearing water flow, low-pressure heater branch road condenses hydromining variable frequency pump and regulation valve mode regulates.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610587174.1A CN106090971A (en) | 2016-07-06 | 2016-07-06 | A kind of combined steam flue gas MGGH system and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610587174.1A CN106090971A (en) | 2016-07-06 | 2016-07-06 | A kind of combined steam flue gas MGGH system and method |
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| CN106090971A true CN106090971A (en) | 2016-11-09 |
Family
ID=57449338
Family Applications (1)
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| CN201610587174.1A Pending CN106090971A (en) | 2016-07-06 | 2016-07-06 | A kind of combined steam flue gas MGGH system and method |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106765265A (en) * | 2017-01-05 | 2017-05-31 | 东方电气集团东方锅炉股份有限公司 | A kind of low low temperature heat system of ultra-clean discharging fire coal unit open type |
| CN107120673A (en) * | 2017-05-11 | 2017-09-01 | 无锡华光新动力环保科技股份有限公司 | Low temperature SCR denitration and flue gas take off white device |
| CN107166417A (en) * | 2017-07-10 | 2017-09-15 | 都江电力设备厂 | A kind of new MGGH systems minimum wall temperature control method and system |
| CN107631289A (en) * | 2017-09-01 | 2018-01-26 | 中清源环保节能有限公司 | A kind of coal-burning power plant's heat supply initial station low temperature Mist heat recovering system |
| CN108224462A (en) * | 2018-03-02 | 2018-06-29 | 南京圣诺热管有限公司 | It is a kind of to eliminate white misty rain joint flue gas waste heat recovery system |
| CN113294799A (en) * | 2021-05-27 | 2021-08-24 | 东方电气集团东方锅炉股份有限公司 | Hot primary air and air-powder mixture heat exchange system |
| CN113654072A (en) * | 2021-08-10 | 2021-11-16 | 西安西热锅炉环保工程有限公司 | WGGH (WGGH) environment-friendly and energy-saving comprehensive utilization system, boiler system and operation method thereof |
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| CN104048307A (en) * | 2014-05-29 | 2014-09-17 | 舒少辛 | Smoke waste heat comprehensive utilization device and method |
| CN104566424A (en) * | 2015-01-12 | 2015-04-29 | 重庆中电节能技术服务有限公司 | Combined steam smoke MGGH system and flue gas treatment technology |
| CN204739568U (en) * | 2015-06-15 | 2015-11-04 | 杭州华电能源工程有限公司 | Energy saving and emission reduction system that horizontal phase transition heat exchanger and prefix type hydrophily formula GGH unite |
| CN206257687U (en) * | 2016-07-06 | 2017-06-16 | 大唐(北京)能源管理有限公司 | A kind of combined steam flue gas MGGH systems |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104048307A (en) * | 2014-05-29 | 2014-09-17 | 舒少辛 | Smoke waste heat comprehensive utilization device and method |
| CN104566424A (en) * | 2015-01-12 | 2015-04-29 | 重庆中电节能技术服务有限公司 | Combined steam smoke MGGH system and flue gas treatment technology |
| CN204739568U (en) * | 2015-06-15 | 2015-11-04 | 杭州华电能源工程有限公司 | Energy saving and emission reduction system that horizontal phase transition heat exchanger and prefix type hydrophily formula GGH unite |
| CN206257687U (en) * | 2016-07-06 | 2017-06-16 | 大唐(北京)能源管理有限公司 | A kind of combined steam flue gas MGGH systems |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106765265A (en) * | 2017-01-05 | 2017-05-31 | 东方电气集团东方锅炉股份有限公司 | A kind of low low temperature heat system of ultra-clean discharging fire coal unit open type |
| CN107120673A (en) * | 2017-05-11 | 2017-09-01 | 无锡华光新动力环保科技股份有限公司 | Low temperature SCR denitration and flue gas take off white device |
| CN107166417A (en) * | 2017-07-10 | 2017-09-15 | 都江电力设备厂 | A kind of new MGGH systems minimum wall temperature control method and system |
| CN107166417B (en) * | 2017-07-10 | 2023-04-14 | 中国电建集团都江电力设备有限公司 | Minimum wall temperature control method and system for MGGH system |
| CN107631289A (en) * | 2017-09-01 | 2018-01-26 | 中清源环保节能有限公司 | A kind of coal-burning power plant's heat supply initial station low temperature Mist heat recovering system |
| CN108224462A (en) * | 2018-03-02 | 2018-06-29 | 南京圣诺热管有限公司 | It is a kind of to eliminate white misty rain joint flue gas waste heat recovery system |
| CN113294799A (en) * | 2021-05-27 | 2021-08-24 | 东方电气集团东方锅炉股份有限公司 | Hot primary air and air-powder mixture heat exchange system |
| CN113654072A (en) * | 2021-08-10 | 2021-11-16 | 西安西热锅炉环保工程有限公司 | WGGH (WGGH) environment-friendly and energy-saving comprehensive utilization system, boiler system and operation method thereof |
| CN113654072B (en) * | 2021-08-10 | 2024-04-09 | 西安西热锅炉环保工程有限公司 | WGGH environment-friendly and energy-saving comprehensive utilization system, boiler system and operation method thereof |
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