WO2010045858A1 - 水制氢燃料共烧炉 - Google Patents

水制氢燃料共烧炉 Download PDF

Info

Publication number
WO2010045858A1
WO2010045858A1 PCT/CN2009/074495 CN2009074495W WO2010045858A1 WO 2010045858 A1 WO2010045858 A1 WO 2010045858A1 CN 2009074495 W CN2009074495 W CN 2009074495W WO 2010045858 A1 WO2010045858 A1 WO 2010045858A1
Authority
WO
WIPO (PCT)
Prior art keywords
water
chamber
high temperature
fuel
separator
Prior art date
Application number
PCT/CN2009/074495
Other languages
English (en)
French (fr)
Inventor
李根均
Original Assignee
李柏林
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 李柏林 filed Critical 李柏林
Publication of WO2010045858A1 publication Critical patent/WO2010045858A1/zh

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/04—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of inorganic compounds, e.g. ammonia
    • C01B3/042—Decomposition of water
    • C01B3/045—Decomposition of water in gaseous phase
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24C—DOMESTIC STOVES OR RANGES ; DETAILS OF DOMESTIC STOVES OR RANGES, OF GENERAL APPLICATION
    • F24C9/00—Stoves or ranges heated by a single type of energy supply not covered by groups F24C3/00 - F24C7/00 or subclass F24B
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/16—Controlling the process
    • 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
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
    • 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
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency

Definitions

  • the invention relates to an energy-saving and environment-friendly water-based hydrogen fuel furnace, which is a device for co-firing to obtain ultra-high temperature, and belongs to the technical field of international patent classification F24C.
  • the cooker used in the prior art is an alcoholic liquid fuel cooker which burns alcohol or its vapor by heating and pressing a part of methanol into a gas. Combustion products are a serious hazard to humans and the environment. Moreover, the direct combustion of the alcohol causes severe corrosion of the burner parts, causing blockage of pipes such as carbon deposits, and insufficient combustion of the fuel.
  • the object of the present invention is to provide an ultra-high temperature device for co-firing an energy-saving and environmentally-friendly hydrogen fuel for improving combustion efficiency, energy saving, and pollution reduction.
  • An energy-saving and environment-friendly water-based hydrogen fuel co-firing to obtain an ultra-high temperature device which comprises an interconnected water tank, a water supply system and a water supply and pressure storage system, an interconnected water jacket, a steam generating chamber and a first-stage steam-water separator, and a second-stage steam-water separation
  • the pipeline is respectively connected to the first-stage steam-water separator and the gas supply pressure control system through a pipeline, and the gas supply pressure control system is connected by a pipeline to a catalyst chamber adjacent to the steam generating chamber and the first-stage steam-water separator, a water jacket, a steam generating chamber and a catalyst.
  • One side of the chamber is connected to the high temperature cracking chamber.
  • the front end of the high temperature cracking chamber is connected to the fuel burner head, and the rear end of the high temperature cracking chamber is connected to the swirl chamber.
  • the infrared control system is arranged at the rear of the device.
  • the fuel burner head is provided with a high temperature reheat distributor and a plurality of uniform gas nozzles.
  • the device of the invention can fully increase the calorific value of combustion, greatly improve the combustion efficiency, save energy and reduce emissions, reduce pollution, protect the environment, and benefit the country and the people.
  • the device of the invention comprises a water tank, a conveying pipe connected by each part, a water jacket, a first-stage steam separator, a second-stage steam separator, a catalyst chamber, a high-temperature water cracking device, a swirl chamber, an oxygen, a hydrogen nozzle, a coal burning, Fuel, gas furnace, gas, fuel control mechanism, air adjustment plate, water pump, water pipe pressure automatic control valve, water tank, water jacket water level gauge, water tank/water level automatic control mechanism, thermal insulation layer/insulation layer, water supply and pressure accumulation system, circuit And connecting seat, pressure gauge, connecting joint, nut, pressure self-protection device, bracket, high temperature reheat distributor, combustion coal exchange mechanism, oil vapor pressure mixed atomization combustion mechanism, furnace outer shell iron shell, etc.
  • the gas furnace may be an infrared ray, a blast nozzle, a vertical horizontal or a composite gas furnace.
  • Tap water can be injected into water by two methods: 1) directly injected into the water tank 1, and enters the water supply and pressure storage system 3 through the water supply system 2 to enter the water jacket 4, and the liquid level height is determined by infrared rays.
  • Control system 15 controls. 2) Directly supplied to the water supply and accumulator system through the pipeline. 3 After the pressure regulation control, it is sent to the water jacket 4 through the pipeline.
  • the gas, coal, and fuel burners 14 are heated and heated in the steam generating chamber 5 to boil to generate steam, and then enter the first-stage steam separator 6 through a plurality of vent holes, and then piped to the second-stage steam separator.
  • the remaining water flows back to the water jacket; the separated water vapor passes through the supply pressure control system 8 and the catalyst chamber 9 together with the catalytic gas generated by the heating, simultaneously enters the swirl chamber 10 to obtain uniform mixing, and then passes through
  • the pipeline is sent to the pyrolysis chamber 11 to be cracked into hydrogen and oxygen, and then the hydrogen and oxygen are sent to the high-temperature reheat distributor 12 in the furnace by the pipeline, and finally sprayed into the flame of the furnace through a plurality of gas nozzles 13 at this time.
  • the flame encounters hydrogen detonating and violently burning oxygen to help the fire, while at the same time generating more water vapor is split into hydrogen and oxygen and sent to the furnace to form a virtuous cycle, which makes the flame temperature in the furnace higher. Burning is more complete and more complete.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Air Supply (AREA)

Description

氷制氢燃料共烧炉 技术领域
本发明涉及一种节能环保水制氢燃料炉， 是一种共烧获得超高温的 装置， 属于国际专利分类 F24C技术领域。
背景技术
现有技术中使用的灶具为醇类液体燃料灶具， 通过打气加压， 或预 先将一部分甲醇加热成气体， 燃烧醇类或其蒸汽。 燃烧产物对人体和环 境都有严重的危害。 而且， 直接燃烧醇类对炉头部件产生严重的腐蚀， 造成积炭等管路堵塞， 不能充分燃烧燃料。
发明内容
本发明的目的， 在于提供一种提高燃烧效率、 节能减排、 降低污染 的节能环保水制氢燃料共烧获得超高温装置。
本发明的目的是通过以下技术方案实现的。
一种节能环保水制氢燃料共烧获得超高温装置， 它包括相互连接的 水箱、 供水系统和供水蓄压系统， 相互连接的水套、 蒸汽发生室和一级 汽水分离器， 二级汽水分离器通过管路分别连接一级汽水分离器和供气 压力控制系统， 供气压力控制系统由管路连接与蒸汽发生室和一级汽水 分离器邻接的催化剂室， 水套、 蒸汽发生室和催化剂室的一侧均与高温 裂解室连接， 高温裂解室的前端向外连接燃油炉头， 高温裂解室的后端 向外连接旋流室， 装置的后部设有红外线控制系统。
所述的燃油炉头中装有高温再热分配器， 以及数个均布的气体喷嘴。 本发明的装置可充分增加燃烧热值， 很大程度提高了燃烧效率， 节 能减排， 降低污染， 保护环境， 利国利民。
附图说明
附图为本发明的结构示意图。
图中： 1、 水箱， 2、 供水系统， 3、 供水蓄压系统， 4、 水套， 5、 蒸 汽发生室， 6、 一级汽水分离器， 7、 二级汽水分离器， 8、 供气压力控制 系统， 9、 催化剂室， 10、 旋流室， 1 1、 高温裂解室， 12、 高温再热分配 器， 1 3、 数个气体喷嘴， 14、 燃油炉头， 15、 红外线控制系统。 具体实施方式 本发明的装置中包括有水箱， 各部连接的输送管道， 水套、 一级汽 水分离器、 二级汽水分离器、 催化剂室、 高温水裂解装置、 旋流室、 氧， 氢气喷嘴， 燃煤、 燃油、 燃气炉， 燃气、 燃油控制机构、 空气调整板、 水泵、 自来水管压力自控阀、 水箱、 水套水位表、 水箱 /水位自控机构、 隔热保温层 /保温层及供水蓄压系统、 电路及连接座、压力表、连接接头、 螺母、 压力自保装置、 支架、 高温再热分配器、 燃烧换煤机构、 油汽压 力混合雾化燃烧机构、 炉的外罩铁壳等。 所述的燃气炉可以为红外线、 喷火嘴、 立卧式或复合式的燃气炉。
参见附图， 本发明系统的工作原理为： 自来水可分别通过二种方式 注水： 1 )直接注入水箱 1中， 经供水系统 2进入供水蓄压系统 3进入水 套 4 , 其液位高度由红外线控制系统 15控制。 2 )通过管道直供到供水蓄 压系统 3调压控制后经管道送进水套 4中。 由燃气、 燃煤、 燃油炉头 14 燃烧加温在蒸汽发生室 5 内至沸腾产生水蒸汽， 后经数个排气孔进入一 级汽水分离器 6 , 再由管道输送到二级汽水分离器 7内， 余水流回水套； 分离出来的水蒸汽经供气压力控制系统 8输送管道与催化剂室 9连同经 加温后产生的催化气体一起同时进入旋流室 10 , 得到均匀混合， 然后经 过管道送入高温裂解室 11裂解成氢气和氧气， 再由管道将氢气和氧气送 到炉膛中的高温再热分配器 12 ,最后经数个气体喷嘴 1 3喷向炉膛的火焰 中， 此时炉膛的火焰遇到了氢气开始爆燃并猛烈燃烧氧助火威， 与此同 时又产生更多的水蒸汽被裂解成氢气和氧气同样送到炉膛里， 形成良性 循环， 使炉中的火焰温度更高， 燃烧更充分， 更完全。

Claims

权利要求
1. 一种节能环保水制氢燃料共烧获得超高温装置， 其特征在于： 它包括 相互连接的水箱 （1)、 供水系统（2)和供水蓄压系统（3), 相互连接的 水套（ 4 )、 蒸汽发生室（ 5 )和一级汽水分离器（ 6 ), 二级汽水分离器（ 7 ) 通过管路分别连接一级汽水分离器（6)和供气压力控制系统（8 ), 供气 压力控制系统（ 8 )由管路连接与蒸汽发生室（ 5 )和一级汽水分离器（ 6 ) 邻接的催化剂室 （ 9 ), 水套（ 4 )、 蒸汽发生室 （ 5 )和催化剂室 （ 9 ) 的 一侧均与高温裂解室 （11 )连接， 高温裂解室 （11 ) 的前端向外连接燃 油炉头 （14 ), 高温裂解室 （11 ) 的后端向外连接旋流室 （10), 装置的 后部设有红外线控制系统（15)。
2. 根据权利要求 1所述的节能环保水制氢燃料共烧获得超高温装置， 其 特征在于： 所述的燃油炉头 （14 ) 中装有高温再热分配器（12), 以及数 个均布的气体喷嘴（13)。
PCT/CN2009/074495 2008-10-24 2009-10-19 水制氢燃料共烧炉 WO2010045858A1 (zh)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CNU2008201395376U CN201285080Y (zh) 2008-10-24 2008-10-24 一种节能环保水制氢燃料共烧获得超高温装置
CN200820139537.6 2008-10-24

Publications (1)

Publication Number Publication Date
WO2010045858A1 true WO2010045858A1 (zh) 2010-04-29

Family

ID=40950066

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2009/074495 WO2010045858A1 (zh) 2008-10-24 2009-10-19 水制氢燃料共烧炉

Country Status (2)

Country Link
CN (1) CN201285080Y (zh)
WO (1) WO2010045858A1 (zh)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111001421A (zh) * 2019-04-28 2020-04-14 蔡勇梅 一种水蒸气制氢催化剂及其制法、应用和燃烧装置

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201285080Y (zh) * 2008-10-24 2009-08-05 李根均 一种节能环保水制氢燃料共烧获得超高温装置
CN101614442B (zh) * 2009-08-17 2012-02-01 李根钧 一种高温水裂解气体与燃料混烧获取更高热效率的装置
CN101799179B (zh) * 2010-04-28 2011-04-06 李柏林 一种增能环保中餐灶
CN102095199B (zh) * 2010-12-09 2012-07-04 沈阳威德新能源有限公司 热激制氢燃烧机

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB720371A (en) * 1950-07-26 1954-12-15 Robert Von Linde Process for the production of a protective or controlled furnace atmosphere
CN2233050Y (zh) * 1995-08-25 1996-08-14 梁红光 红外燃气炉
CN1132843A (zh) * 1995-04-06 1996-10-09 丛选章 利用水分解作燃料的方法和装置
CN2349468Y (zh) * 1998-12-18 1999-11-17 李健德 燃气炉具水能助燃器
US20020071515A1 (en) * 2000-12-12 2002-06-13 Boardman Charles E. Systems and methods of producing hydrogen using a nuclear reactor
CN201285080Y (zh) * 2008-10-24 2009-08-05 李根均 一种节能环保水制氢燃料共烧获得超高温装置

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB720371A (en) * 1950-07-26 1954-12-15 Robert Von Linde Process for the production of a protective or controlled furnace atmosphere
CN1132843A (zh) * 1995-04-06 1996-10-09 丛选章 利用水分解作燃料的方法和装置
CN2233050Y (zh) * 1995-08-25 1996-08-14 梁红光 红外燃气炉
CN2349468Y (zh) * 1998-12-18 1999-11-17 李健德 燃气炉具水能助燃器
US20020071515A1 (en) * 2000-12-12 2002-06-13 Boardman Charles E. Systems and methods of producing hydrogen using a nuclear reactor
CN201285080Y (zh) * 2008-10-24 2009-08-05 李根均 一种节能环保水制氢燃料共烧获得超高温装置

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111001421A (zh) * 2019-04-28 2020-04-14 蔡勇梅 一种水蒸气制氢催化剂及其制法、应用和燃烧装置

Also Published As

Publication number Publication date
CN201285080Y (zh) 2009-08-05

Similar Documents

Publication Publication Date Title
WO2010045858A1 (zh) 水制氢燃料共烧炉
CN103644562A (zh) 组合式节能生物质燃料锅炉
WO2016206431A1 (zh) 用于生物质燃气工业热水器的燃烧器
CN202792512U (zh) 一种减小热能损失的新型工业锅炉
CN206191894U (zh) 氢混合燃气热水锅炉
CN205138229U (zh) 退火炉补燃余热锅炉
CN207936036U (zh) 一种高压燃烧注汽锅炉
CN102980186A (zh) 无压气化液体燃料燃烧器及燃烧炉具
CN113685850A (zh) 一种氢混节能灶
CN202057033U (zh) 节能蒸汽热水炉
CN102207332A (zh) 节能蒸汽热水炉
CN201764540U (zh) 一种返烧锅炉
CN105823040B (zh) 具有外置裂解管的高温裂解燃烧器
CN201531865U (zh) 节能环保蒸汽灶
CN103267273A (zh) 一种快速高效能蒸汽发生器(蒸汽锅炉)
CN2881436Y (zh) 燃气热水锅炉
CN214620116U (zh) 一种低压高温热源机
CN101368741A (zh) 多功能气化节能灶
CN203454133U (zh) 双预热型鼓风燃烧器
CN215176034U (zh) 环保型天然气炉
CN202973079U (zh) 无压气化液体燃料燃烧器及燃烧炉具
CN221424861U (zh) 一种高闪点液体燃料热能回收气化炉装置
CN201844549U (zh) 环保节能常压热水炉体
CN201373560Y (zh) 常压褐煤转气节能热水锅炉
CN201041378Y (zh) 一种醇基燃料用灶具

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 09821579

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 09821579

Country of ref document: EP

Kind code of ref document: A1