CN204611798U - A kind of employing hydronic dried slag removing equipment of low temperature neat stress and furnace cinder cooling device thereof - Google Patents
A kind of employing hydronic dried slag removing equipment of low temperature neat stress and furnace cinder cooling device thereof Download PDFInfo
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- CN204611798U CN204611798U CN201520142436.4U CN201520142436U CN204611798U CN 204611798 U CN204611798 U CN 204611798U CN 201520142436 U CN201520142436 U CN 201520142436U CN 204611798 U CN204611798 U CN 204611798U
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Abstract
The one that the utility model provides adopts the hydronic dried slag removing equipment of low temperature neat stress and furnace cinder cooling device thereof, comprises dry-type slag extractor body (9), cooling device (8) and control system (10).This dry-type slag extractor comprises furnace cinder cooling device, the cooling medium of natural wind as slag and slag drying machine is substituted using the low temperature neat stress after flue gas desulfur device, and according to boiler main, reheater temperature, pressure in slag temperature and furnace hopper bottom and slag extractor, the low temperature neat stress amount of slag drying machine is sent in automatic adjustment, thus avoid a large amount of amorphous natural wind to enter burner hearth affecting normal burning tissues, while realizing cooled slag and slag drying machine, improve the economy of unit operation.
Description
Technical field
The utility model belongs to field of electrical equipment, and particularly one adopts the hydronic dried slag removing equipment of low temperature neat stress and furnace cinder cooling device thereof.
Background technology
Dried slag removing technology is the technology adopting the slag of a kind of special steel band (conveyer belt) conveying after Air flow.The course of work of this technology is that appropriate natural wind is under the effect of combustion chamber draft, enter from dry-type slag extractor bottom, the slag fallen in steel band and boiler larynx mouth area adverse current cooling steel band top and aditus laryngis, by the cooling of furnace slag of high temperature to the cold slag that can directly store and transport, and heat is sent into burner hearth.Compared with the wet type dreg removing system of extensive use, dried slag removing technology has the following advantages: 1, using natural wind as cold slag medium, do not need cooling water, can using water wisely and water treatment system investment; The slag of 2, discharging is dry slag but not wet slag, and the activity of slag is not destroyed, and is conducive to the comprehensive utilization of slag; 3, the radiant heat of the heat of slag and boiler throat can be recycled in stove by cooling air again, reduces the imperfect combustion loss in slag, thus reduces the heat loss of boiler, improves boiler efficiency.In recent years, what require along with energy-saving and emission-reduction improves constantly the popularization with dry-type slag extractor production domesticization, and the power plant of the domestic 1000MW of comprising unit has nearly hundreds coal-burning boiler to adopt Dry Slag Removal System.
At present, the dry bottom ash handling system of domestic installation is many introduces from Italian MAGALDI company and German CB-DRYCON company.Also there are corresponding dried slag removing patented technology in Japan and Britain, such as patent No. JP-A-63-6319 and GB1357276.In recent years more domestic companies it is also proposed the dried slag removing technology (such as patent No. CN1050178C, CN2459550Y and CN100443801C) with independent intellectual property right, and some power plant are applied at home.Analyze and find: these technology all adopt surrounding air as the cooling medium of slag and slag drying machine above, and the cooling air volume entering slag drying machine is all uncontrollable, changes with combustion chamber draft.For new-built unit, though can consider leaking out of slag drying machine and leave certain surplus during boiler combustion system design, the cooling air quantity due to Dry Slag Removal System is that air force depends on combustion chamber draft according to the design of boiler EIAJ; And different load lower hearth negative pressure substantially constant, namely under different load, slag drying machine inleakage is substantially identical, causes the air leak rate of air curtain of slag drying machine under middle-low load far above design load thus.A large amount of amorphous air directly enters burner hearth through slag drying machine and the air quantity entered in burner hearth through burner can be caused to reduce, thus affect the tissue of stove combustion, cause furnace flame off-centring, superheater, reheater overtemperature are serious, spray water flux is large, and unit operation economy reduces.In addition, large quantity of air directly enters burner hearth without air preheater, and air preheater heat transfer effect is deteriorated, and exhaust gas temperature raises, and causes boiler efficiency to reduce.Wet type dreg removing system being changed to the unit of Dry Slag Removal System, is that value is lower, under after changing Dry Slag Removal System into, the problems referred to above not only come across middle-low load, also very outstanding under high loads according to the design of wet type dreg removing system because furnace bottom that boiler is initial leaks out.
Natural wind is adopted to cool the problem caused for Dry Slag Removal System, Chinese patent 00209485.1 and patent 200920073690.8 propose a kind of method controlling slag drying machine cold air amount, namely on ventilating opening, install one piece of baffle plate additional, utilize the aperture of combustion chamber draft regulating fender, thus the air quantity that control is bled in burner hearth.Patent 200920312413.8 it is also proposed one can remote-operated throttle setting, can control by operated from a distance the cold air amount entering slag drying machine, but undeclaredly using which kind of parameter regulates as feedback.Patent 200610011273.1 proposes the differential pressure of two pressure vacuum gauges on slag drying machine as feedback, the aperture of adjustment steam-operating baffle door, thus controls the cold air amount entering burner hearth.Patent 200920283916.7,201020197028.6,201120268617.3 and 201110094523.3 also all relates to a kind of method, device and the control principle that regulate slag drying machine cooling air volume.Can be found by above-mentioned analysis, existing patented technology all adopts natural wind cooling to cause the technical thought of problem using the cold air amount controlling to enter slag drying machine as solving Dry Slag Removal System.
Utility model content
Utility model object: the purpose of this utility model is some row problems that solution Dry Slag Removal System adopts natural wind cooled slag to cause, provides a kind of and is applicable to the furnace cinder cooling device of dry-type slag extractor and comprises the dry-type slag extractor of furnace cinder cooling device.
Technical scheme: the utility model provides a kind of dry-type slag extractor comprising furnace cinder cooling device, comprises dry-type slag extractor body (9), cooling device (8) and control system (10), described dry-type slag extractor body (9) comprises housing (9-1) and is located at shutoff door (9-3) in housing (9-1), grid (9-4), conveyer belt (9-2) and cleaning chain (9-5) from top to bottom successively, described cooling device (8) comprises net fume flow control valve (8-2), neat stress temperature regulates bypass (8-3), neat stress blower fan bypass (8-4), one group of low temperature neat stress spout (8-6) and the neat stress blower fan (8-1) connected successively, low temperature neat stress pipeline (8-5), described one group of low temperature neat stress spout (8-6) is connected by valve (8-7) with low temperature neat stress pipeline (8-5) respectively, described net fume flow control valve (8-2) is located on low temperature neat stress pipeline (8-5), neat stress temperature regulates bypass (8-3) one end to be connected with neat stress blower fan (8-1), the other end is connected with chimney or directly connects air, neat stress blower fan bypass (8-4) two ends are connected with neat stress blower fan (8-1) two ends respectively, described one group of low temperature neat stress spout (8-6) is located at housing (9-1) both sides respectively, temperature sensor, pressure sensor that described control system (10) comprises neat stress air-blower control unit (10-6) and is connected with neat stress air-blower control unit (10-6) respectively, temperature sensor, pressure sensor are located in housing (9-1).
As improvement, the quantity of described low temperature neat stress spout (8-6) is 3 layers, is arranged in housing (9-1) from top to bottom; Comprise first order low temperature neat stress spout (8-6-1), second level low temperature neat stress spout (8-6-2) and third level low temperature neat stress spout (8-6-3); Described first order low temperature neat stress spout (8-6-1) is located at shutoff door (9-3) top, described second level low temperature neat stress spout (8-6-2) is located between grid (9-4) and conveyer belt (9-2), and described third level low temperature neat stress spout (8-6-3) is located between conveyer belt (9-2) and cleaning chain (9-5).
As further improvement, the quantity of described temperature sensor is 3 layers, and the quantity of described pressure sensor is 2 layers; Described control system (10) comprises neat stress air-blower control unit (10-6) and the first order temperature sensor (10-1) be connected with neat stress air-blower control unit (10-6) respectively and first order pressure sensor (10-2), second level temperature sensor (10-3) and second level pressure sensor (10-4), third level pressure sensor (10-5); Described first order temperature sensor (10-1) and first order pressure sensor (10-2) are located near first order low temperature neat stress spout (8-6-1), described second level temperature sensor (10-3) and second level pressure sensor (10-4) are located near second level low temperature neat stress spout (8-6-2), and described third level pressure sensor (10-5) is located near third level low temperature neat stress spout (8-6-3).
Improve as another kind, described low temperature neat stress spout (8-6) comprises low temperature neat stress wind-distributing pipe (8-6-4) and low temperature neat stress nozzle hood (8-6-5).
The utility model additionally provides a kind of furnace cinder cooling device being applicable to dry-type slag extractor, comprises cooling device (8) and control system (10), described cooling device (8) comprises net fume flow control valve (8-2), neat stress temperature regulates bypass (8-3), neat stress blower fan bypass (8-4), one group of low temperature neat stress spout (8-6) and the neat stress blower fan (8-1) connected successively, low temperature neat stress pipeline (8-5), described one group of low temperature neat stress spout (8-6) is connected by valve (8-7) with low temperature neat stress pipeline (8-5) respectively, described net fume flow control valve (8-2) is located on low temperature neat stress pipeline (8-5), neat stress temperature regulates bypass (8-3) one end to be connected with neat stress blower fan (8-1), neat stress blower fan bypass (8-4) two ends are connected with neat stress blower fan (8-1) two ends respectively, described one group of low temperature neat stress spout (8-6) is located at the housing both sides of dry-type slag extractor respectively, temperature sensor, pressure sensor that described control system (10) comprises neat stress air-blower control unit (10-6) and is connected with neat stress air-blower control unit (10-6) respectively, temperature sensor, pressure sensor are located in the housing of dry-type slag extractor.
The utility model additionally provides a kind of method of the cooling of furnace slag to dry-type slag extractor, comprises the following steps:
(1) neat stress after desulfurization delivers to dry-type slag extractor place through blower fan, and point three layers of feeding dry-type slag extractor are inner, and the low temperature neat stress amount of three layers of low temperature neat stress spout regulates according to the temperature and pressure of slag drying machine inside;
(2) the neat stress amount in dry-type slag extractor of entering, according to pressure in boiler main, reheater temperature and slag temperature, furnace hopper bottom and slag extractor, regulates neat stress blower fan or neat stress temperature to regulate the low temperature neat stress amount sending into dry-type slag extractor automatically; The adjustment of neat stress temperature regulates bypass to realize by adjustment neat stress temperature, by mixing the cold flue gas in chimney or the neat stress temperature in ambient, cool air adjustment feeding slag drying machine.
Beneficial effect: the dry-type slag extractor that the utility model provides comprises furnace cinder cooling device, the cooling medium of natural wind as slag and slag drying machine is substituted using the low temperature neat stress after flue gas desulfur device, and according to boiler main, reheater temperature, pressure in slag temperature and boiler furnace hopper bottom and slag extractor, the low temperature neat stress amount of slag drying machine is sent in automatic adjustment, thus avoid a large amount of amorphous natural wind to enter burner hearth affecting normal burning tissues, while realizing cooled slag and slag drying machine, improve the economy of unit operation.
Specifically, the utility model has following outstanding advantage relative to prior art:
(1) the utility model proposes and substitute the cooling medium of cold air as Dry Slag Removal System using the low temperature neat stress after desulfurizer, effectively can solve some row problems that Dry Slag Removal System adopts natural wind cooled slag to cause, can under the prerequisite of requirement meeting the cooling of Dry Slag Removal System lime-ash, meet the air distribution requirement of burner primary and secondary air and air preheater heat transfer requirements simultaneously, improve the economy of unit operation.Neat stress temperature after desulfurization, generally at 40 ~ 50 DEG C, is delivered to dry slag extractor place through blower fan extraction and can be cooled to less than 30 DEG C.In addition, the specific heat capacity of flue gas is higher than air, and by cooling of furnace slag at identical temperature, required exhaust gas volumn is less.Therefore, adopt in the neat stress cooled slag principle after desulfurization feasible.
(2) the utility model proposes in low temperature neat stress classification feeding slag drying machine, and wind-distributing pipe is set at the dry-type slag extractor bottom, strengthening cooling of furnace slag effect, simultaneously, adopt blower fan quantitative for low temperature neat stress controlled classification to be sent in slag drying machine, and wind-distributing pipe is set at the dry-type slag extractor bottom, can under the condition not affecting combustion chamber draft, realize the object of " little neat stress amount, good cooling effect ", efficiently solve the uncontrollable difficult problem of Dry Slag Removal System cooling air.
(3) in order to control the low temperature neat stress amount entered in slag drying machine, proposing the driving force using blower fan as cooling medium, substituting combustion chamber draft, while guarantee cooling of furnace slag effect, heat exchange in adjustment stove.
(4) equipment that the utility model proposes have structure simple, implement convenient, be applicable to the advantage of existing Dry Slag Removal System transformation.
Accompanying drawing explanation
Fig. 1 is the dry-type slag extractor cooling of furnace slag method and Plant arrangement schematic diagram that the utility model proposes;
Fig. 2 is that in slag drying machine, neat stress spout in the second level arranges schematic diagram;
Fig. 3 is that in slag drying machine, third level neat stress spout arranges schematic diagram;
Fig. 4 is that longitudinal schematic diagram arranged by dry-type slag extractor cooling system;
Wherein, 1, boiler; 2, SCR denitration system; 3, air preheater; 4, deduster; 5, air-introduced machine; 6, desulfurizing tower; 7, chimney; 8-1, neat stress blower fan; 8-2, net fume flow control valve; 8-3, neat stress temperature regulate bypass; 8-4, the bypass of neat stress blower fan; 8-5, low temperature neat stress pipeline; 8-6 low temperature neat stress spout, 8-6-1, first order low temperature neat stress spout; 8-6-2, second level low temperature neat stress spout 8-6-3 third level low temperature neat stress spout, 8-6-4, low temperature neat stress wind-distributing pipe; 8-6-5, low temperature neat stress nozzle hood; 8-7, low temperature neat stress spout valve; 9, dry-type slag extractor body; 9-1, dried slag removing engine housing; 9-2, conveyer belt; 9-3, shutoff door; 9-4, grid; 9-5, cleaning chain; 10-1, first order temperature sensor; 10-2, first order pressure sensor; 10-3, second level temperature sensor; 10-4, second level pressure sensor; 10-5, third level pressure sensor; 10-6, neat stress air-blower control unit.
Detailed description of the invention
Comprise the dry-type slag extractor of furnace cinder cooling device, see Fig. 1 to 4, comprise dry-type slag extractor body 9, cooling device 8 and control system 10.
Dry-type slag extractor body 9 comprises housing 9-1 and is located at shutoff door 9-3, grid 9-4 in housing 9-1, conveyer belt 9-2 and cleaning chain 9-5 from top to bottom successively;
Cooling device 8 comprises net fume flow control valve 8-2, neat stress temperature regulates bypass 8-3, neat stress blower fan bypass 8-4, one group of low temperature neat stress spout 8-6 and the neat stress blower fan 8-1 connected successively, low temperature neat stress pipeline 8-5, the neat stress that cooled slag uses utilizes neat stress blower fan 8-1 to extract from desulfurizing tower 6 exhaust pass, one group of low temperature neat stress spout 8-6 is connected by valve 8-7 with low temperature neat stress pipeline 8-5 respectively, net fume flow control valve 8-2 is located on low temperature neat stress pipeline 8-5, neat stress temperature regulates bypass 8-3 one end to be connected with neat stress blower fan 8-1, neat stress temperature regulates the other end of bypass 8-3 to regulate neat stress temperature by the flue gas or natural wind extracting lower temperature from chimney or environment, for regulating the neat stress temperature entered in slag drying machine, neat stress blower fan bypass 8-4 two ends are connected with neat stress blower fan 8-1 two ends respectively, one group of low temperature neat stress spout 8-6 is located at housing 9-1 both sides respectively.The quantity of low temperature neat stress spout 8-6 is 3 layers, is arranged in housing 9-1 from top to bottom; Comprise first order low temperature neat stress spout 8-6-1, second level low temperature neat stress spout 8-6-2 and third level low temperature neat stress spout 8-6-3; First order low temperature neat stress spout 8-6-1 is located at above shutoff door 9-3, and second level low temperature neat stress spout 8-6-2 is located between grid 9-4 and conveyer belt 9-2, and third level low temperature neat stress spout 8-6-3 is located between conveyer belt 9-2 and cleaning chain 9-5.Low temperature neat stress spout 8-6 comprises low temperature neat stress wind-distributing pipe 8-6-4 and third level low temperature neat stress nozzle hood 8-6-5.
Temperature sensor, pressure sensor that control system 10 comprises neat stress air-blower control unit 10-6 and is connected with neat stress air-blower control unit 10-6 respectively, temperature sensor, pressure sensor are located in housing 9-1.The quantity of temperature sensor is 3 layers, and the quantity of pressure sensor is 2 layers; Control system 10 comprises neat stress air-blower control unit 10-6 and the first order temperature sensor 10-1 be connected with neat stress air-blower control unit 10-6 respectively and first order pressure sensor 10-2, second level temperature sensor 10-3 and second level pressure sensor 10-4, third level pressure sensor 10-5; First order temperature sensor 10-1 and first order pressure sensor 10-2 is located near first order low temperature neat stress spout 8-6-1, second level temperature sensor 10-3 and second level pressure sensor 10-4 is located near the low temperature neat stress spout 8-6-2 of the second level, and third level pressure sensor 10-5 is located near third level low temperature neat stress spout 8-6-3.The neat stress amount entered in slag drying machine regulates according to temperature sensor and pressure sensor measured value.
During use, dry-type slag extractor body 9, boiler 1, SCR denitration system 2, air preheater 3, deduster 4, air-introduced machine 5, desulfurizing tower 6, cooling device 8 are in turn connected into ring, and chimney 7 regulates bypass 8-3 to be connected with desulfurizing tower 6 and neat stress temperature.In running, the neat stress after desulfurization is delivered to slag drying machine through blower fan and is punished three layers of feeding slag drying machines inside, and the low temperature neat stress amount of three layers of spout regulates according to the temperature and pressure of slag drying machine inside.The neat stress amount in slag drying machine of entering is according to boiler main, reheater temperature, and pressure in slag temperature and furnace hopper bottom and slag extractor, regulates neat stress blower fan or neat stress temperature to regulate the low temperature neat stress amount sending into slag drying machine automatically.The adjustment of neat stress temperature regulates bypass to realize by adjustment neat stress temperature, by mixing the cold flue gas in chimney or the neat stress temperature in ambient, cool air adjustment feeding slag drying machine in right amount.
Claims (5)
1. adopt the hydronic dried slag removing equipment of low temperature neat stress, it is characterized in that: comprise dry-type slag extractor body (9), cooling device (8) and control system (10), described dry-type slag extractor body (9) comprises housing (9-1) and is located at shutoff door (9-3) in housing (9-1), grid (9-4), conveyer belt (9-2) and cleaning chain (9-5) from top to bottom successively, described cooling device (8) comprises net fume flow control valve (8-2), neat stress temperature regulates bypass (8-3), neat stress blower fan bypass (8-4), one group of low temperature neat stress spout (8-6) and the neat stress blower fan (8-1) connected successively, low temperature neat stress pipeline (8-5), described one group of low temperature neat stress spout (8-6) is connected by valve (8-7) with low temperature neat stress pipeline (8-5) respectively, described net fume flow control valve (8-2) is located on low temperature neat stress pipeline (8-5), neat stress temperature regulates bypass (8-3) one end to be connected with neat stress blower fan (8-1), neat stress blower fan bypass (8-4) two ends are connected with neat stress blower fan (8-1) two ends respectively, described one group of low temperature neat stress spout (8-6) is located at housing (9-1) both sides respectively, temperature sensor, pressure sensor that described control system (10) comprises neat stress air-blower control unit (10-6) and is connected with neat stress air-blower control unit (10-6) respectively, temperature sensor, pressure sensor are located in housing (9-1).
2. one according to claim 1 adopts the hydronic dried slag removing equipment of low temperature neat stress, it is characterized in that: the quantity of described low temperature neat stress spout (8-6) is 3 layers, is arranged in housing (9-1) from top to bottom; Comprise first order low temperature neat stress spout (8-6-1), second level low temperature neat stress spout (8-6-2) and third level low temperature neat stress spout (8-6-3); Described first order low temperature neat stress spout (8-6-1) is located at shutoff door (9-3) top, described second level low temperature neat stress spout (8-6-2) is located between grid (9-4) and conveyer belt (9-2), and described third level low temperature neat stress spout (8-6-3) is located between conveyer belt (9-2) and cleaning chain (9-5).
3. one according to claim 2 adopts the hydronic dried slag removing equipment of low temperature neat stress, and it is characterized in that: the quantity of described temperature sensor is 3 layers, the quantity of described pressure sensor is 2 layers; Described control system (10) comprises neat stress air-blower control unit (10-6) and the first order temperature sensor (10-1) be connected with neat stress air-blower control unit (10-6) respectively and first order pressure sensor (10-2), second level temperature sensor (10-3) and second level pressure sensor (10-4), third level pressure sensor (10-5); Described first order temperature sensor (10-1) and first order pressure sensor (10-2) are located near first order low temperature neat stress spout (8-6-1), described second level temperature sensor (10-3) and second level pressure sensor (10-4) are located near second level low temperature neat stress spout (8-6-2), and described third level pressure sensor (10-5) is located near third level low temperature neat stress spout (8-6-3).
4. one according to claim 1 adopts the hydronic dried slag removing equipment of low temperature neat stress, it is characterized in that: described low temperature neat stress spout (8-6) comprises low temperature neat stress wind-distributing pipe (8-6-4) and low temperature neat stress nozzle hood (8-6-5).
5. be applicable to a furnace cinder cooling device for dry-type slag extractor, it is characterized in that: comprise cooling device (8) and control system (10), described cooling device (8) comprises net fume flow control valve (8-2), neat stress temperature regulates bypass (8-3), neat stress blower fan bypass (8-4), one group of low temperature neat stress spout (8-6) and the neat stress blower fan (8-1) connected successively, low temperature neat stress pipeline (8-5), described one group of low temperature neat stress spout (8-6) is connected by valve (8-7) with low temperature neat stress pipeline (8-5) respectively, described net fume flow control valve (8-2) is located on low temperature neat stress pipeline (8-5), neat stress temperature regulates bypass (8-3) one end to be connected with neat stress blower fan (8-1), neat stress blower fan bypass (8-4) two ends are connected with neat stress blower fan (8-1) two ends respectively, described one group of low temperature neat stress spout (8-6) is located at the housing both sides of dry-type slag extractor respectively, temperature sensor, pressure sensor that described control system (10) comprises neat stress air-blower control unit (10-6) and is connected with neat stress air-blower control unit (10-6) respectively, temperature sensor, pressure sensor are located in the housing of dry-type slag extractor.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104832930A (en) * | 2015-03-13 | 2015-08-12 | 国电科学技术研究院 | Slag cooling device applicable to dry slag discharge machines and application thereof |
| CN108534159A (en) * | 2018-04-28 | 2018-09-14 | 河南禾力能源股份有限公司 | A kind of automatic pressure regulating device of Industrial Boiler deslagging air compressor machine |
| CN110287561A (en) * | 2019-06-14 | 2019-09-27 | 国电南京电力试验研究有限公司 | One kind stopping standby burner low-temperature flue gas cooling system and its Parameters design |
| CN116576476A (en) * | 2023-07-11 | 2023-08-11 | 江苏大恒环境技术有限公司 | Furnace bottom dry ash discharging device of furnace-pan integrated salt-containing waste liquid incinerator |
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2015
- 2015-03-13 CN CN201520142436.4U patent/CN204611798U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104832930A (en) * | 2015-03-13 | 2015-08-12 | 国电科学技术研究院 | Slag cooling device applicable to dry slag discharge machines and application thereof |
| CN104832930B (en) * | 2015-03-13 | 2017-01-18 | 国电科学技术研究院 | Slag cooling device applicable to dry slag discharge machines and application thereof |
| CN108534159A (en) * | 2018-04-28 | 2018-09-14 | 河南禾力能源股份有限公司 | A kind of automatic pressure regulating device of Industrial Boiler deslagging air compressor machine |
| CN108534159B (en) * | 2018-04-28 | 2023-08-08 | 河南禾力能源有限公司 | Automatic pressure regulating device of air compressor for slag discharge of industrial boiler |
| CN110287561A (en) * | 2019-06-14 | 2019-09-27 | 国电南京电力试验研究有限公司 | One kind stopping standby burner low-temperature flue gas cooling system and its Parameters design |
| CN110287561B (en) * | 2019-06-14 | 2023-05-26 | 国能南京电力试验研究有限公司 | Low-temperature flue gas cooling system of standby combustor and parameter design method thereof |
| CN116576476A (en) * | 2023-07-11 | 2023-08-11 | 江苏大恒环境技术有限公司 | Furnace bottom dry ash discharging device of furnace-pan integrated salt-containing waste liquid incinerator |
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