CN101165409A - High-efficiency gas generator - Google Patents
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- CN101165409A CN101165409A CN 200710157614 CN200710157614A CN101165409A CN 101165409 A CN101165409 A CN 101165409A CN 200710157614 CN200710157614 CN 200710157614 CN 200710157614 A CN200710157614 A CN 200710157614A CN 101165409 A CN101165409 A CN 101165409A
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- 239000003245 coal Substances 0.000 claims abstract description 30
- 238000003860 storage Methods 0.000 claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 241000270708 Testudinidae Species 0.000 claims description 5
- 238000005192 partition Methods 0.000 claims description 5
- 239000007789 gas Substances 0.000 abstract description 71
- 238000010438 heat treatment Methods 0.000 abstract description 12
- 238000002485 combustion reaction Methods 0.000 abstract description 9
- 239000000428 dust Substances 0.000 abstract description 7
- 239000003034 coal gas Substances 0.000 abstract description 5
- 239000000779 smoke Substances 0.000 abstract description 5
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 abstract description 2
- 239000003830 anthracite Substances 0.000 abstract description 2
- 239000012530 fluid Substances 0.000 abstract description 2
- 238000000034 method Methods 0.000 abstract description 2
- 235000013311 vegetables Nutrition 0.000 abstract description 2
- 238000001514 detection method Methods 0.000 abstract 1
- 239000003915 liquefied petroleum gas Substances 0.000 abstract 1
- 238000012423 maintenance Methods 0.000 abstract 1
- 235000012054 meals Nutrition 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 description 6
- 238000006722 reduction reaction Methods 0.000 description 6
- 239000002956 ash Substances 0.000 description 5
- 238000002309 gasification Methods 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 238000003287 bathing Methods 0.000 description 3
- 239000000571 coke Substances 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000003763 carbonization Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 239000004484 Briquette Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Classifications
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- 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
- Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
- Y02E20/18—Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]
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- Solid-Fuel Combustion (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种煤气发生装置,特别是涉及一种能够提高产气量的高效煤气发生装置。The invention relates to a coal gas generator, in particular to a high-efficiency coal gas generator capable of increasing gas production.
背景技术Background technique
目前,城镇平房区及农村独居小楼,都用小型散烧煤炉取暖、烧饭、洗浴,小型餐馆、小型洗浴业也以散烧煤炉作为热源,即浪费能源,又严重污染环境,尤其北方地区所用能源中,煤占70%以上。为改善环境,大都推行清洁燃料和推广型煤来解决问题,但推行清洁燃料和型煤,成本比较高,难度也不小。众所周知,煤是十分复杂的固体物质,它的主要成份是碳以及少量氢、氮氧硫和无机灰分等。利用制水煤气的反应原理,在隔绝空气或缺氧的条件下,把煤加热到一定温度通入水蒸气,把固体的煤转化为气态的可燃物质,这类装置虽然以往也有,但由于致使煤气产量低,燃煤质量要求高,净化效果不好,难以满足使用要求。At present, small coal-fired stoves are used for heating, cooking, and bathing in bungalows in cities and towns and single-living small buildings in rural areas. Small restaurants and small bathing businesses also use coal-fired stoves as heat sources, which wastes energy and seriously pollutes the environment. Coal accounts for more than 70% of the energy used in the northern region. In order to improve the environment, most of them promote clean fuels and briquettes to solve the problem, but the cost of promoting clean fuels and briquettes is relatively high and the difficulty is not small. As we all know, coal is a very complex solid substance, and its main components are carbon and a small amount of hydrogen, nitrogen, oxygen, sulfur and inorganic ash. Utilizing the reaction principle of water gas production, under the conditions of isolation of air or lack of oxygen, the coal is heated to a certain temperature and water vapor is introduced to convert the solid coal into gaseous combustible substances. Low, high coal quality requirements, poor purification effect, difficult to meet the use requirements.
发明内容Contents of the invention
为解决上述问题,本发明的目的是提供一种既能直接燃用原煤,又能节能、减少污染、改善环境、产气量高的高效煤气发生装置。In order to solve the above problems, the object of the present invention is to provide a high-efficiency gas generator that can directly burn raw coal, save energy, reduce pollution, improve the environment, and have high gas production.
为了实现上述目的,本发明解决技术问题的技术方案包括煤气发生装置1、贮气罐18和燃烧器19,煤气发生装置1与贮气罐18相通,贮气罐18与燃烧器19相通,在煤气发生装置1内下部设有炉箅2,侧面设有蒸汽喷口4,其特征在于煤气发生装置1为圆台型。In order to achieve the above object, the technical solution of the technical problem of the present invention comprises
本发明还包括根据煤气发生装置1内温度、煤气浓度、湿度,控制进气阀27、鼓风机24、烟道关闭阀门16与加煤器6的自动控制装置。The present invention also includes an automatic control device for controlling the
所述的蒸汽喷口4上设有斜挡板5。The steam spout 4 is provided with an
本发明还包括龟板加热器25、它一端与热水管30相连、另一端与暖气片一端相连。The present invention also comprises
所述的炉箅2采用上拱梯式。Described
所述的贮气罐18内设有除焦油隔板28。The
所述的除焦油隔板28是垂直、平行交错排列的平板。The tar-removing
本发明与现有技术相比,具有如下效果:Compared with the prior art, the present invention has the following effects:
1、煤气发生装置在正常工作时,采取烟道关闭情况下密闭燃烧,不向大气排放烟尘。产生的混合煤气通过特制燃烧器燃烧,与管道煤气燃烧类似,混合煤气可视作清洁燃烧,能够明显改善环境,适合家庭、餐飮业、洗浴业、蔬菜暖棚取暖使用。1. When the gas generating device is working normally, it will burn in a sealed manner with the flue closed, and will not emit smoke and dust into the atmosphere. The mixed gas produced is burned by a special burner, which is similar to pipeline gas combustion. The mixed gas can be regarded as clean combustion and can significantly improve the environment. It is suitable for heating in households, restaurants, bathing industries, and vegetable greenhouses.
2、一次性投资小,操作简单,易于维修,能够替代型煤和石油液化气,改善居室和小型餐饮业环境,经济实用。2. The one-time investment is small, the operation is simple, and it is easy to maintain. It can replace briquette and petroleum liquefied gas, improve the environment of living room and small catering industry, and is economical and practical.
3、经权威部门检测,安全、卫生、方便、耐用。适用除无烟煤以外的各种煤种,并较常规小型散煤炉节煤近43%。3. Tested by the authoritative department, it is safe, hygienic, convenient and durable. It is suitable for all kinds of coal except anthracite, and saves coal by nearly 43% compared with conventional small-scale scattered coal furnaces.
附图说明Description of drawings
图1是本发明的结构示意图。图2是本发明的龟板加热器的结构示意图。图中:煤气发生装置1;炉箅;2;水夹套3;蒸汽喷口4;斜挡板5;加煤器6;煤斗7;蒸汽罐水位表8;水箱9水蒸汽加热罐10;水蒸汽加热罐排气阀11;出渣口12;烟道13;除尘器14;除尘阀1 5烟道关闭阀门16;贮气罐安全阀17;贮气罐18;燃烧器19;配风管20;配风阀21;残液排阀22;传感器23;鼓风机24;龟板加热器25;耐火炉衬26;进气阀27;除焦油隔板28冷水管29;热水管30。Fig. 1 is a structural schematic diagram of the present invention. Fig. 2 is a schematic structural view of the tortoise shell heater of the present invention. In the figure:
具体实施方式Detailed ways
下面结合附图对本发明进行详细说明。The present invention will be described in detail below in conjunction with the accompanying drawings.
如图1所示,本发明由煤气发生装置1、贮气罐18、燃烧器19、组成,其中煤气发生装置1与贮气罐18相通,贮气罐18与燃烧器19相通,在煤气发生装置1内下部设有炉箅2,侧面设有蒸汽喷口4、传感器23、加煤器6、上部设有水蒸汽加热罐10、烟道13,侧壁内侧设有耐火炉衬26,侧壁外测设有水夹套3。在外部还设有显示装置、鼓风机调速开关、煤气开关、燃烧器送风开关等。As shown in Figure 1, the present invention is made up of
煤气发生装置1采用圆台式结构,能够控制气化反应时产生的混合煤气主要成份一氧化碳和氢气在煤气发生装置1内继续氧化,而降低混合煤气可燃气体浓度,有利于控制产气,提高产气量;煤气发生装置1内设置自动控制装置,能够根据煤气发生装置1内的温度、煤气浓度、湿度,来控制进气阀27、鼓风机24、烟道关闭阀门16与加煤器6的动作;炉内蒸汽喷口4加斜挡板5,以防止煤粒堵塞蒸汽喷口4;加煤器6采取双层夹管旋转式加煤器,以防止加煤时冒烟及有效封闭加煤器6;燃烧器19采取风机附管通风,使煤气、空气在燃烧器混合室内充分混合,提高燃烧强度,增加火焰温度;为解决冬季连续取暖,本发明设有活动式龟板加热器25,其一端与热水管30相连,另一端与暖气片一端相连,暖气片另一端与冷气管29相连,将其放置在燃烧器19上加热以产生热水与暖气片进行循环取暖;炉箅2采用上拱梯式,使煤层形成中间薄,周围厚,有利于快燃烧,缩短产生煤气时间,以减少排放的烟尘量;贮气罐18内设垂直、平行交错排列的除焦油隔板28,有利于焦油煤气分离;烟道13上设有除尘器14,有助于防止启动时烟尘污染空气;贮气罐18设有贮气罐安全阀17,防止气压危险。The
首先,发生装置第一次点火时通过加煤器6加入少量木柴引火,再加入适量原煤,根据煤含硫量,将定量固硫剂,加入发生装置内。打开煤道13同时送入氧气,在煤气发生装置1下部形成氧化层,将氧化燃烧产生的热量供给上层原料完成化学反应,同时使水蒸汽加热罐10的水产生水蒸汽。自动控制装置接收传感器23发送的信号,根据煤气发生装置1内的温度、煤气浓度、湿度,来控制进气阀27、鼓风机24、烟道关闭阀门16与加煤器6的动作,进入工作状态,并将相应状态在显示装置上显示。First of all, when the generating device is ignited for the first time, a small amount of firewood is added through the
反应方程式: C+O2=CO2 2C+O2=2COReaction equation: C+O 2 =CO2 2C+O 2 =2CO
然后自动控制装置根据煤气发生装置1内的温度、湿度,打开进气阀27,通入水蒸汽,同时由氧化层产生的气体上升,在氧化层上部形成还原区。Then the automatic control device opens the
二氧化碳的还原反应: C+CO2=2COCarbon dioxide reduction reaction: C+CO 2 =2CO
水蒸汽的还原反应: C+H2O=CO+H2 Reduction reaction of water vapor: C+H 2 O=CO+H 2
氧化层和还原层生成的气体与气化剂中未反应的成分一起继续上升,加热上面的原料层,此时由于上升气流中不再含氧,原料实际处于无氧加热的干馏状态,这一料层称为干馏层。从干馏层下落的物料即为干馏产物半焦或焦炭,它们进入还原,氧化区域,在高温下,煤还会发生裂化反应和甲烷反应生成H2、CH4和其它烃等可燃气体。The gas generated from the oxidation layer and the reduction layer continues to rise together with the unreacted components in the gasification agent, heating the upper raw material layer. At this time, since the upward air flow no longer contains oxygen, the raw material is actually in a dry distillation state of anaerobic heating. The material layer is called the dry distillation layer. The material falling from the carbonization layer is the carbonization product semi-coke or coke, which enters the reduction and oxidation area. At high temperature, the coal will also undergo cracking reaction and methane reaction to generate combustible gases such as H 2 , CH 4 and other hydrocarbons.
煤气经过干燥后进入煤气发生装置1上部空间,经煤气发生装置1的煤气出口引出。Coal gas enters the upper space of
随着原料的不断燃烧和气化,逐渐形成炉渣、炉灰。在自身重力作用下,逐渐下降,由煤气发生装置1下部的炉箅2掉入炉坑,由出渣口12掏出,该煤气发生装置1的特点是气化与原料逆流,接触充分,氧化还原彻底,故炉灰挤成粉状,易除,充分利用自身产生的热量。可燃气逐层上升时,被上面料层过滤,故出口燃气灰分少,可动性好。With the continuous combustion and gasification of raw materials, slag and ash are gradually formed. Under the action of its own gravity, it gradually descends, falls into the furnace pit from the
煤气发生装置1出来的可燃气经贮气罐18除焦,除去煤气中的焦油、水气及灰颗粒等杂质,使杂质以液态流体形式由出焦口排出。净化后煤气即可使用。The combustible gas coming out of the
Claims (7)
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102585909A (en) * | 2012-03-08 | 2012-07-18 | 河南心连心化肥有限公司 | Coal water slurry gas making comprehensive utilization device |
| CN103666571A (en) * | 2013-11-26 | 2014-03-26 | 潘高峰 | Gas producer |
-
2007
- 2007-10-23 CN CN 200710157614 patent/CN101165409A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102585909A (en) * | 2012-03-08 | 2012-07-18 | 河南心连心化肥有限公司 | Coal water slurry gas making comprehensive utilization device |
| CN103666571A (en) * | 2013-11-26 | 2014-03-26 | 潘高峰 | Gas producer |
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