EP2411734A1 - Système permettant de diminuer des émissions et d'améliorer le rendement énergétique de systèmes de combustion de combustibles fossiles et de biocarburant - Google Patents

Système permettant de diminuer des émissions et d'améliorer le rendement énergétique de systèmes de combustion de combustibles fossiles et de biocarburant

Info

Publication number
EP2411734A1
EP2411734A1 EP10755371A EP10755371A EP2411734A1 EP 2411734 A1 EP2411734 A1 EP 2411734A1 EP 10755371 A EP10755371 A EP 10755371A EP 10755371 A EP10755371 A EP 10755371A EP 2411734 A1 EP2411734 A1 EP 2411734A1
Authority
EP
European Patent Office
Prior art keywords
water
evaporator
burner
housing
flue
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP10755371A
Other languages
German (de)
English (en)
Other versions
EP2411734A4 (fr
Inventor
Fadi Eldabbagh
Luc Mandeville
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Publication of EP2411734A1 publication Critical patent/EP2411734A1/fr
Publication of EP2411734A4 publication Critical patent/EP2411734A4/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D12/00—Other central heating systems
    • F24D12/02—Other central heating systems having more than one heat source
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23D—BURNERS
    • F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/46—Details, e.g. noise reduction means
    • F23D14/68—Treating the combustion air or gas, e.g. by filtering, or moistening
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23L—SUPPLYING 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
    • F23L15/00—Heating of air supplied for combustion
    • F23L15/04—Arrangements of recuperators
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23L—SUPPLYING 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
    • F23L7/00—Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam
    • F23L7/002—Supplying water
    • F23L7/005—Evaporated water; Steam
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23N—REGULATING OR CONTROLLING COMBUSTION
    • F23N5/00—Systems for controlling combustion
    • F23N5/003—Systems for controlling combustion using detectors sensitive to combustion gas properties
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H9/00—Details
    • F24H9/20—Arrangement or mounting of control or safety devices
    • F24H9/2007—Arrangement or mounting of control or safety devices for water heaters
    • F24H9/2035—Arrangement or mounting of control or safety devices for water heaters using fluid fuel
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2200/00—Heat sources or energy sources
    • F24D2200/16—Waste heat
    • F24D2200/18—Flue gas recuperation
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Definitions

  • the present invention concerns a water heater system wherein the amount of water and the temperature of the air are closed loop controlled for reducing NOx production.
  • a water heater system comprising: a hot water boiler having top, bottom and side walls; a flue connected to the top wall; a burner secured to a side wall of the first housing; a combustible feeder connected to the burner; an evaporator having a housing comprising an outlet, heat exchange elements located in the housing and a water discharge device spaced above the heat exchange elements, wherein the evaporator provides a source of humid air to the burner for increasing the combustion products dew point and to reduce NOx emissions when burned; and a heat recovery system connected to the flue wherein the heat is used for heating water used by the water discharge device.
  • the water heater system further comprises a flue gas analyzer connected to the flue and to the outlet of the evaporator for measuring the level of at least one of CO 2 , thermal and fuel NOx and H 2 O and for measuring the temperature and water content at the outlet of the evaporator; and a controller for analyzing the values obtained from the flue gas analyzer, wherein if at least one of these values, alone or in combination, indicates a sub-optimal combustion condition, the controller adjust the operation parameters of the water heater system to reach optimal combustion condition.
  • the heat recovery system is a source of hot water such as an indirect economizer.
  • the right amount of water is taken from the heat recovery system based on controller output.
  • other types of heat recovery systems would be suitable for the present invention and that water could be heated separately from the heat coming from the heat recovery system.
  • This system could be used replacing the hot water boiler with other types of heating device such as steam boilers and cogen units.
  • Figure 1 is a simplified schematic diagram of the system of an embodiment of the present invention.
  • the invention relates to a water heater system in which hot water from a heat recovery system is used to warm and humidify a flow of intake air to the burner.
  • the objectives are to reduce energy consumption and to reduce flame temperature so thermal and fuel NOx" s will be reduced.
  • An advantage of the present invention is that the amount of water and the temperature of the air are closed loop controlled to the maximum level before negative effects appear.
  • the nitrogen bound in the fuel is released as a free radical, and ultimately forms free N2, or NO.
  • Fuel NOx can contribute as much as 50% of total emissions when burning oil and as much as 80% when burning coal.
  • By humidifying the combustion air we are significantly reducing the amount of fuel bound NOx converted to free N 2 or NO.
  • the objective of the system is to ensure that the moisture content of the combustion air of coal, oil or any biomass burner air is kept at maximum practical level because the water vapor in the combustion air creates conditions that improve gasification.
  • Gasification is a process that converts solid carbonaceous materials (coal, petroleum products, or biomass) by thermochemical reactions into a fuel gas known as syngas, which is rich in hydrogen and carbon moNOxide.
  • the process needs to operate with an oxidizer (air, oxygen, steam or a combination) under sub-conditions. However, usually air and steam mixture are commonly used oxidizer in industry. Then, the syngas can be directly fired into gas turbines or boilers. The overall process is done in several processes and zones:
  • the pyrolysis process occurs as the solid carbonaceous material heats up (302- 1292°F) in the absence of oxygen to release volatiles (tar, hydrogen, and carbon moNOxide) and produce char.
  • volatiles tar, hydrogen, and carbon moNOxide
  • the weight loss of the solid materials depends on its volatiles content and also on the operating conditions.
  • C represents the carbon-containing solid and/or char.
  • the aim is to use the gasification air humidification to enhance the overall gasification process, hence increasing the quantity and the high heating value of the generated syngas.
  • the flame temperature is estimated from the flue gas temperature.
  • the CO level is measured from the flue gas. If the flue gas temperature goes below a predetermined value, while maintaining the CO concentration at the limit of 400 PPM, it is an indication that the combustion process is adversely affected by the high water content of the combustion air.
  • control system In parallel to controlling these two output parameters, the control system will monitor the following input parameters:
  • control system When temperature or CO content of the flue gas indicates sub-optimal combustion conditions, the control system will change the above inputs (points 1 to 3) to reestablish optimal combustion conditions.
  • the commands of the control system will be based on the level of these 3 input parameters, according to the following priorities.
  • the system (10) comprises an evaporator (20) having a vertical cylindrical housing (22). Heat exchange elements (24) are provided inside the housing (22). Water is sprayed through a water discharge device (26) on top of the heat exchange elements (24) and drop down the housing (22). The humidified air is evacuated by an outlet (28) to reach the burner (38) of the hot water boiler (30). The downward flow of hot water exchanges heat with the upward flow of air provided by an air inlet (29).
  • Various techniques can be used to improve heat exchange performance like packing, number of spraying head, size of the water particulates, etc.
  • the hot water boiler (30) comprises top and bottom walls (32) (34) and side walls (36) and the burner (38) is secured to one of the side walls (36).
  • a combustible feeder (39) is attached to the burner (38) for providing the combustible needed.
  • the hot water boiler (30) further comprises a flue (40) for evacuating the flue gas.
  • a heat recovery system (42) which is an indirect economizer and is used as a source of hot water.
  • the flue gas then passes through a flue gas analyzer (50) which measures the level of CO 2 , thermal and fuel NOx, H 2 O and any other parameter of the flue gas. It also measure the temperature and water content at the outlet (28) of the evaporator (20).
  • the flue gas analyzer (50) is connected to a controller (60).
  • the controller (60) uses the information from the flue gas analyzer (50) to determine the proper amount of hot water to feed to the evaporator (20), based on water temperature, and quality of the combustion.
  • the control algorithm fuzzy logic or else keeps in optimal operating conditions for maximum energy savings, reducing pollutant emissions, with the maximum amount in the air without reducing burner efficiency.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Regulation And Control Of Combustion (AREA)
  • Air Supply (AREA)

Abstract

La présente invention se rapporte à un système de chauffe-eau comprenant : une chaudière à eau chaude ayant des parois supérieure, inférieure et latérales ; un tube de fumée raccordé à la paroi supérieure ; un brûleur fixé à une paroi latérale de la première carrosserie ; un dispositif d'alimentation en combustible raccordé au brûleur ; un évaporateur ayant un logement, le logement comprenant un orifice de sortie, des éléments échangeurs de chaleur situés dans le logement et un dispositif d'évacuation d'eau espacé au-dessus des éléments échangeurs de chaleur, l'évaporateur offrant une source d'air humide au brûleur pour augmenter le point de rosée du produit de combustion et pour réduire l'émission de NOx lorsqu'il est brûlé ; et un système de récupération de chaleur raccordé au tube de fumée, la chaleur étant utilisée pour chauffer l'eau utilisée par le dispositif d'évacuation d'eau.
EP10755371.1A 2009-03-26 2010-03-26 Système permettant de diminuer des émissions et d'améliorer le rendement énergétique de systèmes de combustion de combustibles fossiles et de biocarburant Withdrawn EP2411734A4 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US16361809P 2009-03-26 2009-03-26
PCT/CA2010/000463 WO2010108281A1 (fr) 2009-03-26 2010-03-26 Système permettant de diminuer des émissions et d'améliorer le rendement énergétique de systèmes de combustion de combustibles fossiles et de biocarburant

Publications (2)

Publication Number Publication Date
EP2411734A1 true EP2411734A1 (fr) 2012-02-01
EP2411734A4 EP2411734A4 (fr) 2014-12-17

Family

ID=42780114

Family Applications (1)

Application Number Title Priority Date Filing Date
EP10755371.1A Withdrawn EP2411734A4 (fr) 2009-03-26 2010-03-26 Système permettant de diminuer des émissions et d'améliorer le rendement énergétique de systèmes de combustion de combustibles fossiles et de biocarburant

Country Status (7)

Country Link
US (1) US20120085339A1 (fr)
EP (1) EP2411734A4 (fr)
JP (1) JP5653996B2 (fr)
CN (1) CN102439359A (fr)
BR (1) BRPI1014209A2 (fr)
CA (1) CA2756557A1 (fr)
WO (1) WO2010108281A1 (fr)

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CN103449488B (zh) * 2012-05-31 2016-04-13 沈阳铝镁设计研究院有限公司 降低氢氧化铝焙烧过程能量消耗的方法
CN103574580B (zh) * 2013-11-15 2015-07-01 神华集团有限责任公司 一种火电机组NOx排放监控方法及系统
EP3290794A1 (fr) * 2016-09-05 2018-03-07 Technip France Procédé permettant de réduire les émissions de nox
CN107238092A (zh) * 2017-06-12 2017-10-10 清华大学 燃煤锅炉排烟超低温冷凝热回收及进风加湿的方法与装置
US11441199B2 (en) 2019-04-25 2022-09-13 Les Équipements Lapierre Inc. Controller of the release of energy of a combustion of biomass, system provided with such a controller, kit for assembling the same, and corresponding methods of assembling, operating and use associated thereto
US11624097B2 (en) * 2020-05-14 2023-04-11 Les Equipements Lapierre Inc. Evaporator system, kit for assembling the same, and corresponding methods of assembling, operating and use associated thereto

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US5967137A (en) * 1997-03-27 1999-10-19 Societe En Commandite Gaz Metropolitain High efficiency direct-contact high temperature water heater
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CN102439359A (zh) 2012-05-02
EP2411734A4 (fr) 2014-12-17
US20120085339A1 (en) 2012-04-12
BRPI1014209A2 (pt) 2016-04-05
JP2012521530A (ja) 2012-09-13
CA2756557A1 (fr) 2010-09-30
JP5653996B2 (ja) 2015-01-14
WO2010108281A1 (fr) 2010-09-30

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