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EP1695009A1 - Chaudiere a gazeification pour combustibles solides, en particulier des bottes de paille, presentant des valeurs d'echappement optimisees - Google Patents

Chaudiere a gazeification pour combustibles solides, en particulier des bottes de paille, presentant des valeurs d'echappement optimisees

Info

Publication number
EP1695009A1
EP1695009A1 EP04789949A EP04789949A EP1695009A1 EP 1695009 A1 EP1695009 A1 EP 1695009A1 EP 04789949 A EP04789949 A EP 04789949A EP 04789949 A EP04789949 A EP 04789949A EP 1695009 A1 EP1695009 A1 EP 1695009A1
Authority
EP
European Patent Office
Prior art keywords
combustion chamber
combustion
gasification
cylindrical
ash
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.)
Granted
Application number
EP04789949A
Other languages
German (de)
English (en)
Other versions
EP1695009B1 (fr
Inventor
Christian Herlt
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.)
Herlt Christain
Original Assignee
Herlt Christain
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 Herlt Christain filed Critical Herlt Christain
Publication of EP1695009A1 publication Critical patent/EP1695009A1/fr
Application granted granted Critical
Publication of EP1695009B1 publication Critical patent/EP1695009B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23BMETHODS OR APPARATUS FOR COMBUSTION USING ONLY SOLID FUEL
    • F23B5/00Combustion apparatus with arrangements for burning uncombusted material from primary combustion
    • F23B5/04Combustion apparatus with arrangements for burning uncombusted material from primary combustion in separate combustion chamber; on separate grate
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23BMETHODS OR APPARATUS FOR COMBUSTION USING ONLY SOLID FUEL
    • F23B7/00Combustion techniques; Other solid-fuel combustion apparatus
    • F23B7/002Combustion techniques; Other solid-fuel combustion apparatus characterised by gas flow arrangements
    • F23B7/005Combustion techniques; Other solid-fuel combustion apparatus characterised by gas flow arrangements with downdraught through fuel bed and grate
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • F23G5/0276Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage using direct heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/32Incineration of waste; Incinerator constructions; Details, accessories or control therefor the waste being subjected to a whirling movement, e.g. cyclonic incinerators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/10Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of field or garden waste or biomasses
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2900/00Special features of, or arrangements for incinerators
    • F23G2900/50002Burning with downwards directed draft through the waste mass

Definitions

  • Gasification boiler for solid fuels especially for straw bales, with optimized exhaust gas values
  • the invention relates to a gasification boiler for the combustion of solid fuels, especially straw bales, for heating purposes and hot water production.
  • the invention is characterized by optimal combustion and ash separation. This ensures that the prescribed exhaust gas values are adhered to.
  • the filling shaft has the shape of a double cone with gas outflow openings and a fuel ring channel in the extension. This is to achieve a uniform burn-up and simple construction.
  • DE PS 3617146 shows a special air supply for the primary air in order to achieve a good fuel gas / air mixture.
  • the blower is mounted on the filling door and feeds outside air into three levels of the fuel shaft.
  • the solution in DE PS 3718022 contains two air supply levels in the fuel shaft and one to the combustion chamber. Particularly good gasification is to be achieved with the recirculation of exhaust gas.
  • the straw straw bale fuel has special requirements. There is the problem of uniform gasification, which is hindered by charring of the outer layers. A high content of unburned small components and a low ash melting point have an unfavorable effect on the exhaust gas values and contaminate the heat exchange surfaces (DE OS 41 34 754).
  • the object of the invention is to carry out the combustion even of small parts as completely as possible and to separate the ashes from the fuel gas almost completely before the heat exchangers.
  • the fuel and gasification chamber has recesses on the side next to the grate arranged in the center and the combustion chamber. Coarse particles collect in these, while only the fine particles with the fuel gas are carried into the combustion chamber. The coarse parts can outgas in the wells and do not burden the gas flow. After the combustion is complete, the remaining ash can be removed from there.
  • a cylindrical combustion chamber designed as an additional structural unit is connected to the outlet of the combustion chamber. This post-combustion chamber significantly increases the combustion time, which means that small parts and partially oxidized gases are completely burned. The tangential introduction of the fuel gas acts like a cyclone, so that more ash collects on the floor. This can be removed through a lid.
  • a cylindrical, ash separator designed as an additional structural unit is connected to the combustion chamber.
  • the remaining ash components are removed from the flue gas.
  • the subsequent heat exchanger is no longer loaded with ash.
  • the interaction of the three structural features thus results in more complete combustion, improved ash separation and thus lower exhaust gas pollution.
  • the maintenance and service life of the heat exchanger are also improved.
  • FIG. 1 shows a gasification boiler in front view in section
  • Figure 2 shows the side view of the entire heating system in
  • Figure 3 is a plan view of the entire heating system.
  • a fuel and gasification chamber 1 and a lying, cylindrical combustion chamber 3 are arranged in a housing.
  • a filling door for the straw bale and two doors for ash removal are attached to the front.
  • At the lower vertex of the fuel and gasification chamber 1 there is a longitudinal slot in the floor, which extends over the entire depth.
  • a grate 2 is embedded in this.
  • Below the grate 2 there are gas nozzles which open into a combustion chamber 6. This consists of pipe sections made of refractory concrete, which are guided in a steel pipe.
  • the fuel and gasification chamber 1 has depressions 4 parallel to the grate 2 and combustion chamber 3. These are half-shell-shaped. In the end area, the wall has a door for removal of ashes.
  • the boiler with fuel and gasification chamber 1 and combustion chamber 3 is designed as a structural unit.
  • the downstream combustion chamber 5, ash separator 6 and heat exchanger are combined into a further structural unit by a frame 10.
  • Combustion chamber 5 and Aseheabscheider 6 have a vertical, cylindrical housing.
  • the walls of the housings are insulated, at the top they are closed by a bowl-shaped cover.
  • a pipe is centrally located in the ash separator in the upper area and a circular baffle (8) is attached below it in such a way that an annular opening for the ash deposit remains on the outer wall.
  • the subsequent heat exchangers are arranged in a vertical flue gas outlet.
  • the combustion gases have a rotational movement due to a forced air fan in the fuel and gasification chamber 1.
  • the loose, heavy particles of the firing material collect in the outer, lateral recesses 4 and burn out there completely.
  • Light floating particles are entrained with the fuel gas flow and completely burned in the combustion chamber 5 at the latest.
  • the ash separator 6 the ash is separated several times. When the gas flows in, the ash particles are pressed against the inner wall and fall downward when deflected by the guide plate 8.
  • the ash is removed through the upper covers 7, 9 and a door in the bottom area of the ash separator 6.
  • the gas stream cleaned in this way is passed over the heat exchangers.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Thermal Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Solid-Fuel Combustion (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Air Supply (AREA)
  • Combustion Of Fluid Fuel (AREA)
  • Incineration Of Waste (AREA)
  • Gasification And Melting Of Waste (AREA)
EP04789949A 2003-10-16 2004-10-07 Chaudiere a gazeification pour combustibles solides, en particulier des bottes de paille, presentant des valeurs d'echappement optimisees Expired - Lifetime EP1695009B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10349365A DE10349365A1 (de) 2003-10-16 2003-10-16 Vergaserheizkessel für feste Brennstoffe, insbesondere für Strohballen, mit optmierten Abgaswerten
PCT/DE2004/002240 WO2005040680A1 (fr) 2003-10-16 2004-10-07 Chaudiere a gazeification pour combustibles solides, en particulier des bottes de paille, presentant des valeurs d'echappement optimisees

Publications (2)

Publication Number Publication Date
EP1695009A1 true EP1695009A1 (fr) 2006-08-30
EP1695009B1 EP1695009B1 (fr) 2009-01-14

Family

ID=34442221

Family Applications (1)

Application Number Title Priority Date Filing Date
EP04789949A Expired - Lifetime EP1695009B1 (fr) 2003-10-16 2004-10-07 Chaudiere a gazeification pour combustibles solides, en particulier des bottes de paille, presentant des valeurs d'echappement optimisees

Country Status (18)

Country Link
US (1) US8261677B2 (fr)
EP (1) EP1695009B1 (fr)
JP (1) JP2007508518A (fr)
KR (1) KR100916684B1 (fr)
CN (1) CN100520179C (fr)
AT (1) ATE421071T1 (fr)
AU (1) AU2004284144B9 (fr)
BR (1) BRPI0415593B1 (fr)
CA (1) CA2542676C (fr)
DE (2) DE10349365A1 (fr)
DK (1) DK1695009T3 (fr)
EA (1) EA008320B1 (fr)
EC (1) ECSP066567A (fr)
ES (1) ES2322363T3 (fr)
NZ (1) NZ547146A (fr)
UA (1) UA80782C2 (fr)
WO (1) WO2005040680A1 (fr)
ZA (1) ZA200603850B (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2419050C1 (ru) * 2010-01-18 2011-05-20 Дмитрий Георгиевич Крылов Теплогенератор, работающий на соломе

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DE102006052345B4 (de) * 2006-11-07 2009-04-23 Herlt, Christian, Dipl.-Ing. Verfahren und Vorrichtung zur Verminderung der Feinstaubbildung bei der thermischen Vergasung von halmartiger und stückiger Biomasse in Form von Ballen
DE102007054114A1 (de) * 2007-11-10 2009-05-20 Iht Innovative Heiztechnik Gmbh Heizkessel für die Verbrennung von festem Brennstoff
WO2009129762A1 (fr) * 2008-04-22 2009-10-29 Christian Herlt Procédé et dispositif de réduction de micropoussières dans les gaz d'échappement lors de la gazéification thermique de biomasse de type chaume ou fragmentaire
CN104235858B (zh) * 2014-07-11 2016-07-06 浙江三联环保科技股份有限公司 一种二次燃烧系统
CN108253445B (zh) * 2018-02-23 2024-04-05 辽宁众缘节能锅炉有限公司 一种捆状秸秆锅炉的控制系统
CN109163323A (zh) * 2018-09-06 2019-01-08 黑龙江赫尔特生物质能源发展有限公司 多功能汇集式后燃烧系统
CN109370650A (zh) * 2018-11-21 2019-02-22 黑龙江赫尔特生物质能源发展有限公司 一种低尘排放和更稳定燃气成分的整捆式生物质气化装置
RU2721057C1 (ru) * 2019-10-18 2020-05-15 Юрий Викторович Яковлев Теплогенерирующая установка для нагрева воздуха в технологических целях с использованием в качестве топлива отходов сельского хозяйства, в том числе тюкованной и рулонной соломы
CN110701602A (zh) * 2019-11-19 2020-01-17 中国农业科学院农业环境与可持续发展研究所 一种自动补料分级层燃秸秆捆烧锅炉
CN111298582B (zh) * 2020-03-30 2024-06-28 黑龙江赫尔特生物质能源发展有限公司 用生物质净化含尘烟气的方法和装置
CN111336533A (zh) * 2020-03-30 2020-06-26 黑龙江赫尔特生物质能源发展有限公司 用于固体燃料烟气多级后燃烧的方法与装置

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RU2419050C1 (ru) * 2010-01-18 2011-05-20 Дмитрий Георгиевич Крылов Теплогенератор, работающий на соломе

Also Published As

Publication number Publication date
AU2004284144A1 (en) 2005-05-06
ES2322363T3 (es) 2009-06-19
NZ547146A (en) 2008-07-31
AU2004284144B2 (en) 2008-09-18
BRPI0415593B1 (pt) 2015-11-24
CA2542676C (fr) 2010-12-07
UA80782C2 (en) 2007-10-25
ECSP066567A (es) 2006-10-17
CN1867800A (zh) 2006-11-22
JP2007508518A (ja) 2007-04-05
DE502004008888D1 (de) 2009-03-05
WO2005040680A1 (fr) 2005-05-06
US20090107421A1 (en) 2009-04-30
EA008320B1 (ru) 2007-04-27
ATE421071T1 (de) 2009-01-15
US8261677B2 (en) 2012-09-11
KR100916684B1 (ko) 2009-09-11
DE10349365A1 (de) 2005-05-19
AU2004284144B9 (en) 2008-09-25
EP1695009B1 (fr) 2009-01-14
BRPI0415593A (pt) 2007-01-02
KR20060090250A (ko) 2006-08-10
EA200600734A1 (ru) 2006-10-27
ZA200603850B (en) 2007-04-25
CN100520179C (zh) 2009-07-29
CA2542676A1 (fr) 2005-05-06
DK1695009T3 (da) 2009-05-11

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