CN201264988Y - Positive and reverse flame biomass gas-carbon cogeneration producer - Google Patents
Positive and reverse flame biomass gas-carbon cogeneration producer Download PDFInfo
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- CN201264988Y CN201264988Y CNU2008201857854U CN200820185785U CN201264988Y CN 201264988 Y CN201264988 Y CN 201264988Y CN U2008201857854 U CNU2008201857854 U CN U2008201857854U CN 200820185785 U CN200820185785 U CN 200820185785U CN 201264988 Y CN201264988 Y CN 201264988Y
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- 239000002028 Biomass Substances 0.000 title claims abstract description 38
- 229910052799 carbon Inorganic materials 0.000 title claims description 8
- 238000002309 gasification Methods 0.000 claims abstract description 57
- 238000003763 carbonization Methods 0.000 claims abstract description 43
- 239000003610 charcoal Substances 0.000 claims abstract description 9
- 239000007789 gas Substances 0.000 claims description 30
- 238000004519 manufacturing process Methods 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 3
- 238000002485 combustion reaction Methods 0.000 abstract description 14
- 238000000034 method Methods 0.000 abstract description 13
- 238000009835 boiling Methods 0.000 abstract description 5
- 239000000126 substance Substances 0.000 abstract description 4
- 230000008929 regeneration Effects 0.000 abstract description 2
- 238000011069 regeneration method Methods 0.000 abstract description 2
- 239000010903 husk Substances 0.000 description 3
- 241000209094 Oryza Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 235000013399 edible fruits Nutrition 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000005429 filling process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
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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
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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Abstract
本实用新型涉及一种正反火生物质气炭联产发生炉,同时还涉及相应的气炭联产方法,属于能源再生利用技术领域。该发生炉包括气化炉和炭化室;气化炉的上部为反火气化炉膛,下部为正火气化炉膛;反火气化炉膛底部透过反火炉排与正火气化炉膛的连通;正火气化炉膛与炭化室紧邻,并经通道与炭化室连通。使用时将生物质分别加入后点燃,使反火气化炉膛产生的可燃气体透过反火炉排,与正火气化炉膛产生的可燃气体混合,由通道进入炭化室。最终可以抽取透过炭化室内生物质的可燃气体,并得到生物质炭。本实用新型可以提高可燃气体的气化强度和热值,同时避免出现沸腾燃烧导致的过燃,既得到了符合要求的高热值可燃气体,又可以获得取代木炭的炭化物质。
The utility model relates to a generator for cogeneration of biomass gas and charcoal with positive and negative fires, and also relates to a corresponding method for cogeneration of gas and charcoal, belonging to the technical field of energy regeneration and utilization. The generator includes a gasification furnace and a carbonization chamber; the upper part of the gasification furnace is a reverse-fired gasification furnace, and the lower part is a normalized gasification furnace; the bottom of the reverse-fired gasification furnace is connected to the normalized gasification furnace through the reverse-fired grate; The furnace is adjacent to the carbonization chamber and communicates with the carbonization chamber through a channel. When in use, the biomass is added separately and then ignited, so that the combustible gas generated by the backfiring gasification furnace passes through the backfiring grate, mixes with the combustible gas generated by the normalizing gasification furnace, and enters the carbonization chamber through the channel. Finally, the combustible gas passing through the biomass in the carbonization chamber can be extracted to obtain biochar. The utility model can improve the gasification intensity and calorific value of the combustible gas, avoid over-combustion caused by boiling combustion at the same time, obtain combustible gas with high calorific value meeting the requirements, and obtain carbonized substances replacing charcoal.
Description
技术领域 technical field
本实用新型涉及一种生物质气炭联产发生炉,尤其是一种正反火生物质气炭联产发生炉,属于能源再生利用技术领域。The utility model relates to a biomass gas-carbon co-production generator, in particular to a forward-back fire biomass gas-carbon co-production generator, which belongs to the technical field of energy regeneration and utilization.
背景技术 Background technique
生物质通常包括秸秆、薪柴、稻壳、果壳等农林废弃物。对这些生物质进行合理的处理利用,不仅有利于环境保护,还可以获得宝贵的能源。因此引起了人们的关注。Biomass usually includes agricultural and forestry waste such as straw, firewood, rice husk, and fruit shell. Reasonable treatment and utilization of these biomass is not only beneficial to environmental protection, but also can obtain valuable energy. Therefore, it has attracted people's attention.
传统的生物质处理方法是沸腾式燃烧,即将生物质置于发生炉之类的设施内进行不完全燃烧,从而产生可以利用的一氧化碳等可燃气体以及炭化物质。沸腾式燃烧的缺点是容易过燃。通过不断改进,出现了可以实现分层燃的正火发生炉。这种发生炉的结构特征是含氧气流从生物质底部进入,自下而上经过生物质,其风压低于生物质的总重,因此生物质不会因助燃气流过大、燃烧过旺而沸腾。其优点是容易控制所需的不完全燃烧,气化强度和生成的燃气热值均比较高,其缺点是生成的燃气不仅温度较高而且含有较多灰分,需要冷却洗净处理,结果耗费了水资源,还会引起二次污染。The traditional biomass treatment method is boiling combustion, that is, the biomass is placed in a facility such as a generator for incomplete combustion, thereby producing combustible gases such as carbon monoxide and carbonized substances that can be used. The disadvantage of boiling combustion is that it is easy to overburn. Through continuous improvement, a normalizing furnace that can realize stratified combustion has appeared. The structural feature of this generator is that the oxygen-containing flow enters from the bottom of the biomass, passes through the biomass from bottom to top, and its wind pressure is lower than the total weight of the biomass. boiling. The advantage is that it is easy to control the required incomplete combustion, and the gasification intensity and the calorific value of the generated gas are relatively high. Water resources can also cause secondary pollution.
检索发现,申请号为200510040840.1的中国专利申请公开了一种反火生物质炭化燃气发生方法,实现该方法的发生炉结构特点是助燃气流从生物质上部进入,自上而下经过生物质。由于助燃气流对灰分有抑制作用,因此这种方法产生的燃气通常不用洗净处理,但其生物质燃气和生成生物质炭化产品。反火生物质炭化燃气发生炉,其气化强度和生成的燃气热值往往不及正火发生法。The search found that the Chinese patent application with application number 200510040840.1 discloses a gas generation method for carbonization of counterfired biomass. The structural feature of the generator for realizing this method is that the gas-supporting gas flow enters from the upper part of the biomass and passes through the biomass from top to bottom. Because the combustion-supporting gas flow has an inhibitory effect on ash, the gas produced by this method usually does not need to be cleaned, but the biomass gas and biomass carbonization products are generated. The gasification intensity and the calorific value of the generated gas of the reverse-fired biomass carbonization gas-fired furnace are often lower than those of the normalized method.
实用新型内容 Utility model content
本实用新型的目的在于:针对上述现有技术存在的缺点或不足,提出一种气化强度和生成的燃气热值高、并且无需进行冷却和洗净处理的正反火生物质气炭联产发生炉。The purpose of this utility model is to propose a kind of positive and negative fire biomass gas-carbon cogeneration with high gasification intensity and high calorific value of the generated gas without cooling and cleaning treatment in view of the shortcomings or deficiencies of the above-mentioned prior art furnace.
为了达到以上目的,本实用新型的正反火生物质气炭联产发生炉包括气化炉和炭化室(或称干馏室);所述气化炉的上部为反火气化炉膛,下部为正火气化炉膛;所述反火气化炉膛底部透过反火炉排与正火气化炉膛的连通;所述正火气化炉膛底部的正火炉排下设有出灰口和进气口;所述正火气化炉膛与炭化室紧邻,并经通道与炭化室连通;所述炭化室底部的炭化炉排下设有出炭口和出气口;所述正火气化炉膛的进气口外接鼓风机,所述炭化室的出气口外接抽风机。In order to achieve the above purpose, the forward and reverse fire biomass gas-char co-production generator of the present utility model includes a gasification furnace and a carbonization chamber (or carbonization chamber); the upper part of the gasification furnace is a reverse fire gasification furnace, and the lower part is a normal fire gasification furnace; the bottom of the reverse fire gasification furnace communicates with the normalizing gasification furnace through the reverse fire grate; the normalizing grate at the bottom of the normalizing gasification furnace is provided with an ash outlet and an air inlet; the normalizing gas The carbonization furnace is next to the carbonization chamber, and communicates with the carbonization chamber through a channel; a carbonization outlet and a gas outlet are provided under the carbonization grate at the bottom of the carbonization chamber; the air inlet of the normalizing gasification furnace is externally connected with a blower, and the The air outlet of the chamber is externally connected with an exhaust fan.
使用时,利用生物质气炭联产的方法包括以下步骤:When in use, the method for utilizing biomass gas and charcoal cogeneration comprises the following steps:
第一步、将生物质分别加入反火气化炉膛、正火气化炉膛和炭化室;In the first step, biomass is added to the backfire gasification furnace, normalizing gasification furnace and carbonization chamber respectively;
第二步、点燃正火气化炉膛和反火气化炉膛中的生物质;The second step is to ignite the biomass in the normalizing gasification furnace and the backfiring gasification furnace;
第三步、启动鼓风机和抽风机,使反火气化炉膛产生的可燃气体透过反火炉排,与正火气化炉膛产生的可燃气体混合,由通道进入炭化室;The third step is to start the blower and exhaust fan, so that the combustible gas generated by the backfire gasification furnace passes through the backfire grate, mixes with the combustible gas generated by the normalizing gasification furnace, and enters the carbonization chamber through the channel;
第四步、由炭化室的出气口抽取透过炭化室内生物质的可燃气体,输送到所需处;The fourth step is to extract the combustible gas passing through the biomass in the carbonization chamber from the gas outlet of the carbonization chamber, and transport it to the desired place;
第五步、待炭化室内生物质炭化后,打开炭化室的出炭口取出。Step 5: After the biomass is carbonized in the carbonization chamber, open the carbon outlet of the carbonization chamber and take it out.
上述过程中,通过调控鼓风机和抽风机的风量,宜将反火气化炉膛内的燃烧温度控制在300-400℃,正反火气化炉膛的燃烧温度控制在400-500℃。In the above process, by adjusting the air volume of the blower and exhaust fan, it is advisable to control the combustion temperature in the reverse fire gasification furnace at 300-400°C, and the combustion temperature in the reverse fire gasification furnace at 400-500°C.
本实用新型的上述过程中,由于将正火与反火燃烧有机结合,因此得以借助正火燃烧提高反火可燃气体的气化强度和热值,同时借助反火可燃气体抑制正火燃烧的势头,避免出现沸腾燃烧导致的过燃;此外,上述过程借助炭化室内生物质,使混合后的正反火可燃气体得到过滤和冷却,而生物质本身在此过程中被炭化;结果,既得到了符合要求的高热值可燃气体,又可以获得取代木炭的炭化物质。由此可见,上述技术方案十分合理的实现了实用新型目的。In the above process of the utility model, due to the organic combination of normalizing and backfiring combustion, the gasification intensity and calorific value of the backfiring combustible gas can be improved by means of normalizing combustion, and the momentum of normalizing combustion can be suppressed by the backfiring combustible gas , to avoid over-combustion caused by boiling combustion; in addition, the above-mentioned process uses the biomass in the carbonization chamber to filter and cool the mixed positive and negative fire combustible gases, and the biomass itself is carbonized in this process; The required combustible gas with high calorific value can also obtain carbonized substances instead of charcoal. This shows that above-mentioned technical scheme has realized utility model purpose quite reasonably.
附图说明 Description of drawings
下面结合附图对本实用新型作进一步的说明。Below in conjunction with accompanying drawing, the utility model is further described.
图1为本实用新型一个优选实施例的结构示意图。Fig. 1 is a schematic structural diagram of a preferred embodiment of the present invention.
具体实施方式 Detailed ways
实施例一Embodiment one
本实施例的正反火生物质气炭联产发生炉如图1所示,气化炉的上部为反火气化炉膛7,下部为正火气化炉膛36。反火气化炉膛顶部为反火加料口1(兼做反火进气口),底部透过反火炉排39与正火气化炉膛的连通。反火炉排39支撑在其支架38上,上面安置反火炉耙40。正火气化炉膛侧壁设有加料口37和防爆口35,底部的正火炉排29上安置正火炉耙30,下部的刮灰器28下设有出灰口26和进气口25。炭化室11与正火气化炉膛紧邻,并经通道10与正火气化炉膛连通。炭化室的侧壁设有加料口9、防爆口14,底部的炭化炉排20上安置炭化炉耙19,下部的刮灰器21下设有出炭口24和出气口23。反火气化炉膛7、正火气化炉膛36和炭化室11内分别装有外置电机带动的垂向转轴33、2和15,转轴上部装有水平旋转的平料器3,用于控制填充生物质的量并保持其均匀平整。正火气化炉膛的进气口25外接鼓风机,炭化室的出气口23外接抽风机。The forward-backfire biomass gas-char cogeneration generator of this embodiment is shown in FIG. 1 , the upper part of the gasifier is the reverse-
采用该设备实现正反火生物质气炭联产方法包括以下步骤:The method of using the equipment to realize the combined production of biomass gas and charcoal by forward and backward fire includes the following steps:
第一步、将秸秆、薪柴、稻壳、果壳之类的农林废弃物作为生物质去杂后,水分控制在10-15%,分别由加料口加入反火气化炉膛、正火气化炉膛和炭化室;The first step is to use agricultural and forestry waste such as straw, firewood, rice husk, and fruit husk as biomass to remove impurities, control the water content at 10-15%, and add the reverse fire gasification furnace and normal fire gasification furnace through the feeding port respectively. and carbonization chamber;
第二步、用明火点燃正火气化炉膛和反火气化炉膛中的生物质;The second step is to ignite the biomass in the normal fire gasification furnace and the reverse fire gasification furnace with an open flame;
第三步、启动鼓风机和抽风机,使反火气化炉膛产生的可燃气体(CO、H2、CH4、CmHn等)透过反火炉排,与正火气化炉膛产生的可燃气体混合,由通道进入炭化室;The third step is to start the blower and exhaust fan, so that the combustible gases (CO, H 2 , CH 4 , CmHn, etc.) Enter the carbonization chamber;
第四步、由炭化室的出气口抽取透过炭化室内生物质的可燃气体,输送到储气罐等所需处;The fourth step is to extract the combustible gas passing through the biomass in the carbonization chamber from the gas outlet of the carbonization chamber, and transport it to the required place such as the gas storage tank;
第五步、炭化室内生物质在过滤冷却可燃气体的同时,释放出其中有助于进一步提高可燃气体热值的挥发份而被干馏,之后被炭化,打开炭化室的出炭口取出即可得到生物质炭,用于取代传统的木炭。The fifth step, while the biomass in the carbonization chamber is filtering and cooling the combustible gas, it releases volatile matter which helps to further increase the calorific value of the combustible gas, and is then carbonized. Open the carbonization outlet of the carbonization chamber and take it out to get Biochar, used to replace traditional charcoal.
实验证明,本实施例的气化强度可达150-300kg/m2h,比传统设备的气化强度提高20%以上,获得的可燃气体热值超过5000-6000KJ/m3,比现有技术明显提高,产生的生物质炭是木炭的理想取代品,既节能,又环保。Experiments have proved that the gasification intensity of this embodiment can reach 150-300kg/m 2 h, which is more than 20% higher than that of traditional equipment, and the calorific value of combustible gas obtained exceeds 5000-6000KJ/m 3 , which is higher than that of the prior art Significantly improved, the biochar produced is an ideal substitute for charcoal, which is energy-saving and environmentally friendly.
除上述实施例外,本实用新型还可以有其他实施方式。凡采用等同替换或等效变换形成的技术方案,均落在本实用新型要求的保护范围。In addition to the above embodiments, the utility model can also have other implementations. All technical solutions formed by equivalent replacement or equivalent transformation fall within the scope of protection required by the utility model.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104949105A (en) * | 2015-07-24 | 2015-09-30 | 重庆巴洛克新能源有限公司 | Automatically controlled biomass combustion system |
| CN104990066A (en) * | 2015-07-24 | 2015-10-21 | 重庆巴洛克新能源有限公司 | Automatic control multi-stage biomass burning system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104949105A (en) * | 2015-07-24 | 2015-09-30 | 重庆巴洛克新能源有限公司 | Automatically controlled biomass combustion system |
| CN104990066A (en) * | 2015-07-24 | 2015-10-21 | 重庆巴洛克新能源有限公司 | Automatic control multi-stage biomass burning system |
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