CN110043918B - Adjacent furnace heating starting system with air heater - Google Patents

Adjacent furnace heating starting system with air heater Download PDF

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Publication number
CN110043918B
CN110043918B CN201910314430.3A CN201910314430A CN110043918B CN 110043918 B CN110043918 B CN 110043918B CN 201910314430 A CN201910314430 A CN 201910314430A CN 110043918 B CN110043918 B CN 110043918B
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China
Prior art keywords
condensate water
communicated
pipeline
unit
waterway pipeline
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CN201910314430.3A
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CN110043918A (en
Inventor
潘存华
彭志福
刘进峰
李德
周福
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Datang Boiler Pressure Vessel Examination Center Co Ltd
East China Electric Power Test Institute of China Datang Corp Science and Technology Research Institute Co Ltd
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Datang Boiler Pressure Vessel Examination Center Co Ltd
East China Electric Power Test Institute of China Datang Corp Science and Technology Research Institute Co Ltd
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Priority to CN201910314430.3A priority Critical patent/CN110043918B/en
Publication of CN110043918A publication Critical patent/CN110043918A/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L15/00Heating of air supplied for combustion
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Air Supply (AREA)

Abstract

The invention discloses an adjacent furnace heating starting system with a heater, which comprises: the two units comprise a low-temperature coal economizer, a condensate water heater, an air preheater and a condensate water tank, wherein the low-temperature coal economizer is communicated with the condensate water tank through a first waterway pipeline, the low-temperature coal economizer is communicated with the condensate water heater through a second waterway pipeline, the condensate water heater is communicated with the condensate water tank through a third waterway pipeline, the condensate water heater is communicated with the air preheater through a supply pipeline, the first waterway pipeline of the two units is communicated with the seventh waterway pipeline, the third waterway pipeline of the two units is communicated with the eighth waterway pipeline, and the high-temperature closed water heating heater heated by the low-temperature coal economizer is utilized during operation of the unit A, so that the first and second air temperatures of the inlet of the unit A air preheater are improved, the heating cost of the air preheater is saved, the high-temperature closed water heating heater of the unit A is utilized during starting of the unit B, and the starting cost of the unit B is reduced.

Description

Adjacent furnace heating starting system with air heater
Technical Field
The invention relates to the technical field of waste heat utilization, in particular to an adjacent furnace heating starting system with a heater.
Background
In recent years, along with the continuous rising of international oil prices and the aggravation of global warming trend, energy conservation and emission reduction become the public consensus, and the starting time of a unit and the starting mode of the unit are shortened and optimized, so that the method also becomes the focus of attention of investors. The boiler starting system is arranged for the ultra-supercritical unit and the once-through boiler so as to ensure the safety of the unit during low-load operation, realize the cold state and hot state flushing of the boiler, save working medium and heat and meet the requirements of starting the boiler in different states. However, the process is long in duration, and a large amount of fuel oil and fire coal are consumed. In order to effectively save the fuel consumption of the starting ignition of the boiler, a plurality of domestic projects at present consider adopting plasma ignition, micro-oil ignition and other ignition modes, but even so, a certain amount of fuel is required to be consumed.
Disclosure of Invention
Based on the technical problems in the background technology, the invention provides a neighboring furnace heating starting system with a heater;
the invention provides a neighboring furnace heating starting system with a heater, which comprises the following components: a first unit and a second unit;
the first unit comprises a first low-temperature economizer, a first condensate water heater, a first air preheater and a first condensate water tank, wherein the first low-temperature economizer is communicated with the first condensate water tank through a first waterway pipeline, the first low-temperature economizer is communicated with the first condensate water heater through a second waterway pipeline, the first condensate water heater is communicated with the first condensate water tank through a third waterway pipeline, and the first condensate water heater is communicated with the first air preheater through a first air supply pipeline;
the second unit comprises a second low-temperature economizer, a second condensate water heater, a second air preheater and a second condensate water tank, wherein the second low-temperature economizer is communicated with the second condensate water tank through a fourth waterway pipeline, the second low-temperature economizer is communicated with the second condensate water heater through a fifth waterway pipeline, the second condensate water heater is communicated with the second condensate water tank through a sixth waterway pipeline, and the second condensate water heater is communicated with the second air preheater through a second air supply pipeline;
the second waterway pipeline is communicated with the fifth waterway pipeline through a seventh waterway pipeline, and the third waterway pipeline is communicated with the sixth waterway pipeline through an eighth waterway pipeline.
Preferably, the seventh waterway pipeline is provided with a first regulating valve, and the eighth waterway pipeline is provided with a second regulating valve.
Preferably, the first water channel pipeline is provided with a first booster valve, and the fourth water channel pipeline is provided with a second booster valve.
In the invention, in the normal working stage of the A unit (one unit of the first unit or the second unit), the high-temperature closed water heating air heater heated by the low-temperature coal economizer of the A unit is utilized, so that the first air temperature and the second air temperature of the air preheater of the A unit are improved, the advantage of flue gas waste heat utilization of the low-temperature coal economizer is fully exerted, and when the B unit (the other unit of the first unit or the second unit) is in the starting stage, the A unit utilizes the high-temperature closed water heating air heater heated by the low-temperature coal economizer to heat the B unit, so that the time from the ignition of the B unit to the integral coordinated operation of the B unit can be shortened, the fuel consumption during the starting of the B unit can be reduced, the starting cost of the B unit can be reduced, and the method has obvious effects of relieving transverse cracks of a water cooling wall and over-fast heating rate.
Drawings
Fig. 1 is a schematic structural diagram of an adjacent furnace heating start system with a heater according to the present invention.
Detailed Description
In the first figure, 1-first unit, 11-first low-temperature economizer, 12-first condensate heater, 13-first air preheater, 14-first condensate water tank, 15-first water channel pipeline, 16-second water channel pipeline, 17-third water channel pipeline and 18-first air supply pipeline; 2-second units, 21-second low-temperature economizers, 22-second condensate water heaters, 23-second air pre-heaters, 24-second condensate water tanks, 25-fourth waterway pipelines, 26-fifth waterway pipelines, 27-sixth waterway pipelines and 28-second air supply pipelines; 3-seventh water channel pipeline, 4-eighth water channel pipeline.
Referring to fig. 1, the adjacent furnace heating start system with a heater provided by the invention comprises: a first unit and a second unit;
the first unit comprises a first low-temperature economizer, a first condensate water heater, a first air preheater and a first condensate water tank, wherein the first low-temperature economizer is communicated with the first condensate water tank through a first waterway pipeline, the first low-temperature economizer is communicated with the first condensate water heater through a second waterway pipeline, the first condensate water heater is communicated with the first condensate water tank through a third waterway pipeline, and the first condensate water heater is communicated with the first air preheater through a first air supply pipeline;
the second unit comprises a second low-temperature economizer, a second condensate water heater, a second air preheater and a second condensate water tank, wherein the second low-temperature economizer is communicated with the second condensate water tank through a fourth waterway pipeline, the second low-temperature economizer is communicated with the second condensate water heater through a fifth waterway pipeline, the second condensate water heater is communicated with the second condensate water tank through a sixth waterway pipeline, and the second condensate water heater is communicated with the second air preheater through a second air supply pipeline;
the second waterway pipeline is communicated with the fifth waterway pipeline through a seventh waterway pipeline, and the third waterway pipeline is communicated with the sixth waterway pipeline through an eighth waterway pipeline; the seventh waterway pipeline is provided with a first regulating valve, and the eighth waterway pipeline is provided with a second regulating valve; the first water channel pipeline is provided with a first booster valve, and the fourth water channel pipeline is provided with a second booster valve.
In the specific scheme, cold condensate water in a condensate water tank of a turbine side of an A unit (one of a first unit or a second unit) is heated by hot flue gas of a low-temperature coal economizer of the A unit, high-temperature closed water flowing out of the low-temperature coal economizer can flow into a condensate water heating air heater of the A unit, cold air entering the condensate water heating air heater is preheated and flows back, so that the temperature of first air and second air of the air preheater of the A unit is improved, the energy consumption of the air preheater of the A unit is reduced through waste heat utilization, the energy consumption of the B unit (one of the first unit or the second unit) at a starting stage can be reduced through the utilization of waste heat, the high-temperature closed water flowing out of the low-temperature coal economizer can enter the condensate water heating air heater of the B unit at a starting stage, the required parameters are achieved by means of the high-temperature closed water of the A unit, after the adjacent boiler is heated, a phase change area of a water cooling wall is greatly advanced, the thermal uniformity is extremely good, the transverse generation probability is reduced, the starting speed is greatly improved, the ignition time is shortened, the ignition time is shortened, the boiler is not has a fire-tube is greatly shortened, the fire-crack is prevented from being started, the boiler is greatly, the fire-down, the boiler is not has a fire-down valve is started, and the boiler is provided with a fire valve, the fire valve is greatly and the fire-down, the fire valve is opened, the fire valve is and the water, the fire valve is opened, the boiler is opened and the water and the boiler is opened and the water.
The foregoing is only a preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art, who is within the scope of the present invention, should make equivalent substitutions or modifications according to the technical scheme of the present invention and the inventive concept thereof, and should be covered by the scope of the present invention.

Claims (1)

1. An adjacent furnace heating start system with a heater, which is characterized by comprising: a first unit and a second unit;
the first unit comprises a first low-temperature economizer, a first condensate water heater, a first air preheater and a first condensate water tank, wherein the first low-temperature economizer is communicated with the first condensate water tank through a first waterway pipeline, the first low-temperature economizer is communicated with the first condensate water heater through a second waterway pipeline, the first condensate water heater is communicated with the first condensate water tank through a third waterway pipeline, and the first condensate water heater is communicated with the first air preheater through a first air supply pipeline;
the second unit comprises a second low-temperature economizer, a second condensate water heater, a second air preheater and a second condensate water tank, wherein the second low-temperature economizer is communicated with the second condensate water tank through a fourth waterway pipeline, the second low-temperature economizer is communicated with the second condensate water heater through a fifth waterway pipeline, the second condensate water heater is communicated with the second condensate water tank through a sixth waterway pipeline, and the second condensate water heater is communicated with the second air preheater through a second air supply pipeline;
the second waterway pipeline is communicated with the fifth waterway pipeline through a seventh waterway pipeline, and the third waterway pipeline is communicated with the sixth waterway pipeline through an eighth waterway pipeline;
the seventh waterway pipeline is provided with a first regulating valve, and the eighth waterway pipeline is provided with a second regulating valve;
the first water channel pipeline is provided with a first booster valve, and the fourth water channel pipeline is provided with a second booster valve.
CN201910314430.3A 2019-04-18 2019-04-18 Adjacent furnace heating starting system with air heater Active CN110043918B (en)

Priority Applications (1)

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CN201910314430.3A CN110043918B (en) 2019-04-18 2019-04-18 Adjacent furnace heating starting system with air heater

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Application Number Priority Date Filing Date Title
CN201910314430.3A CN110043918B (en) 2019-04-18 2019-04-18 Adjacent furnace heating starting system with air heater

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CN110043918B true CN110043918B (en) 2024-04-02

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Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4558227A (en) * 1983-06-14 1985-12-10 Hitachi, Ltd. Method of controlling operation of thermoelectric power station
DE8915497U1 (en) * 1989-06-03 1990-08-16 Vießmann, Hans, Dr., 3559 Battenberg boiler
CN102305413A (en) * 2011-07-28 2012-01-04 中国电力工程顾问集团西南电力设计院 Exhaust gas waste heat recovery and emission reduction comprehensive application system for coal-fired boiler in thermal power plant
CN104296121A (en) * 2014-09-25 2015-01-21 黑龙江宏宇电站设备有限公司 Power station boiler neighbor machine steam heating starting device and warm starting method
CN204460172U (en) * 2015-01-14 2015-07-08 陕西万方节能科技股份有限公司 A kind of pulverized-coal fired boiler adjacent stove heating coil start up system
CN205137410U (en) * 2015-11-23 2016-04-06 李东民 Tuber pipe contact heating device of coal -fired pulverized coal boiler unit neighbour stove heat
CN205245218U (en) * 2015-12-31 2016-05-18 神华集团有限责任公司 Boiler system
CN106051805A (en) * 2016-06-24 2016-10-26 福建龙净环保股份有限公司 Waste heat recovery system and method with discharged smoke waste heat as heat source of air heater
CN207268458U (en) * 2017-08-01 2018-04-24 中国大唐集团科学技术研究院有限公司火力发电技术研究所 The system for preventing ammonium hydrogen sulfate from blocking air preheater after SCR denitration transformation
CN207422196U (en) * 2017-11-16 2018-05-29 山西崇光发电有限责任公司 A kind of CFB units combine afterheat utilizing system
CN210035568U (en) * 2019-04-18 2020-02-07 中国大唐集团科学技术研究院有限公司华东电力试验研究院 Adjacent furnace heating starting system with air heater

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4558227A (en) * 1983-06-14 1985-12-10 Hitachi, Ltd. Method of controlling operation of thermoelectric power station
DE8915497U1 (en) * 1989-06-03 1990-08-16 Vießmann, Hans, Dr., 3559 Battenberg boiler
CN102305413A (en) * 2011-07-28 2012-01-04 中国电力工程顾问集团西南电力设计院 Exhaust gas waste heat recovery and emission reduction comprehensive application system for coal-fired boiler in thermal power plant
CN104296121A (en) * 2014-09-25 2015-01-21 黑龙江宏宇电站设备有限公司 Power station boiler neighbor machine steam heating starting device and warm starting method
CN204460172U (en) * 2015-01-14 2015-07-08 陕西万方节能科技股份有限公司 A kind of pulverized-coal fired boiler adjacent stove heating coil start up system
CN205137410U (en) * 2015-11-23 2016-04-06 李东民 Tuber pipe contact heating device of coal -fired pulverized coal boiler unit neighbour stove heat
CN205245218U (en) * 2015-12-31 2016-05-18 神华集团有限责任公司 Boiler system
CN106051805A (en) * 2016-06-24 2016-10-26 福建龙净环保股份有限公司 Waste heat recovery system and method with discharged smoke waste heat as heat source of air heater
CN207268458U (en) * 2017-08-01 2018-04-24 中国大唐集团科学技术研究院有限公司火力发电技术研究所 The system for preventing ammonium hydrogen sulfate from blocking air preheater after SCR denitration transformation
CN207422196U (en) * 2017-11-16 2018-05-29 山西崇光发电有限责任公司 A kind of CFB units combine afterheat utilizing system
CN210035568U (en) * 2019-04-18 2020-02-07 中国大唐集团科学技术研究院有限公司华东电力试验研究院 Adjacent furnace heating starting system with air heater

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