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生物质气化发电技术讲座(3)生物质焦油裂解技术 总被引:12,自引:1,他引:12
1生物质焦油的特性生物质气化的目标是得到尽可能多的可燃气体产物。但在气化过程中,焦炭和焦油都是不可避免的副产物。焦油在高温时呈气态,与可燃气体完全混合,而在低温(一般低于200℃)时凝结为液态。对于燃气需要降温利用的情况(如燃气用于内燃机发电时),焦油的分离问题显得尤为重要。焦油的存在对生物质气化及其利用会产生不利的影响。首先它降低了气化炉气化效率,气化气中焦油产物的能量一般占总能量的5%~15%,这部分能量在低温时难以与可燃气体一道被利用,大部分被浪费;其次焦油在低温时凝结为液态,容易和水、焦炭等结合在一起,堵塞输… 相似文献
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由中科院广州能源研究所承担的国家“十五”863项目“生物质气化发电优化系统及其示范工程”,已开发出适合我国国情的生物质中小型气化发电系统。该技术采用CFB气化炉和多级气体净化装置,配置多台200-400kW的气体燃料内燃发电机组用谷壳、木屑、稻草等多种生物质作原料来发电。 相似文献
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生物质气化发电技术讲座(4)生物质燃气净化技术 总被引:1,自引:0,他引:1
生物质气化燃气含有各种各样的杂质,杂质的主要成分列在表1中。各种杂质的含量与原料特性、气化炉的形式关系很大。燃气净化的目标就是要根据气化工艺的特点,设计合理有效的杂质去除工艺,保证后部气化发电设备不会因杂质的存在而导致其磨损腐蚀和污染等问题。(1)燃气高温过滤生物质气化燃气含有大量的微小的焦炭颗粒和灰,由于焦炭的密度和直径都很小,一般旋风分离器难以去除,即使用非常高效的旋风分离器,燃气中的颗粒含量也很难降到5~30g/m3。在这种情况下,比较好的净化方法是过滤。由于焦油在表1燃气中各种杂质的特性杂质种类典型成分可能… 相似文献
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由中科院广州能源研究所承担的国家“十五”期间863项目的生物质气化发电优化系统及其示范工程.已开发出适合我国国情的生物质中小型气化发电系统。该技术采用CFB气化炉和多级气体净化装置,配置多台200~400kW的气体燃料内燃发电机组,用谷壳木屑、稻草等多种生物质作原料来发电。 相似文献
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生物质气化发电技术讲座(5)生物质燃气发电技术 总被引:2,自引:1,他引:2
生物质燃气的特点是热值低(4~6MJ/m3)、杂质含量高,所以生物质燃气发电技术虽然与天然气发电技术、煤气发电技术的原理一样,但它有更多的独特性,对发电设备的要求与其他燃气发电设备也有较大的差别。1低热值燃气内燃机发电技术气体内燃机是常用的燃气发电设备之一,燃气内燃机都要求有强制点火系统,点火系统的设计必须根据燃气燃烧速度等进行调整。燃气内燃机的有效热效率ηe和有效燃气消耗率ge是衡量发动机经济性能的重要指标。在内燃机中各性能参数存在下面的关系:Ne=k1MbQηege=Mb/Ne=k2/ηeQNi=Ne+Nmηe=ηmηi式中:Ne,Ni,Nm——… 相似文献
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生物质气化发电技术的现状及发展趋势 总被引:1,自引:0,他引:1
欧训民 《能源技术(上海)》2009,30(2):84-85
简要介绍了国内外生物质气化发电技术的研究现状及发展趋势。生物质气化发电技术在发达国家已受到广泛重视,生物质联合循环发电技术(BIGCC)利用外燃机燃用生物质气,可避免高温气化气的除尘除焦难题,是一种比较先进的生物质能利用技术。根据我国国情,引进大型BIGCC并采用内燃机代替燃气轮机,是解决我国生物质气化发电规模化发展的有效手段之一。 相似文献
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本文阐述了国内外BIGCC生物质气化联合循环发电技术的发展概况和关键技术,介绍了生物质和煤共同气化的特性,为我国生物质气化联合循环发电技术的商业化运行提供了指导。 相似文献
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使用Aspen Plus软件对以Fe_2O_3为载氧体的生物质化学链气化系统进行模拟,分析温度、压力、载氧体与生物质摩尔比、水蒸气与生物质摩尔比等因素对合成气制备的影响;对不同生物质的气化条件进行优化;将气化制得的合成气通入M701F燃气轮机中发电,考察系统的发电效率。结果表明:常压下,不同生物质气化的优化温度均在740℃左右,此时制备的合成气冷煤气效率较高;提高反应压力有利于系统热量自平衡,但合成气的冷煤气效率降低;载氧体与生物质摩尔比的优化值与生物质中氧碳摩尔比呈负相关,且达到优化值时,气化环境中氧碳摩尔比在1.25左右;水蒸气通入气化系统后冷煤气效率可提高15.00%~20.00%,主要原因为H_2的产量显著增加,通入水蒸气后的气化环境的氧碳比在1.4左右时,制备合成气的冷煤气效率较高;系统的发电效率在30.00%~37.00%,高于生物质发电效率。 相似文献
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生物质能发电技术分析 总被引:5,自引:0,他引:5
在不可再生能源濒临枯竭,环境污染日益加剧的今天,生物质能源替代化石能源利用的研究和开发,已成为国内外学者研究和关注的热点。介绍了国内外生物质能的主要转化利用技术,分析了生物质直接燃烧发电技术和气化发电技术,提出了符合能量梯级利用原则的生物质能发电方式,将是生物质能利用的主要形式。 相似文献
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Miaomiao Niu Jun Xie Shaohua Liang Liheng Liu Liang Wang Yu Peng 《International Journal of Hydrogen Energy》2021,46(43):22356-22367
A new biomass integrated gasification combined cycle (BIGCC), which featured an innovative two-stage enriched air gasification system coupling a fluidized bed with a swirl-melting furnace, was proposed and built for clean and efficient biomass utilization. The performance of biomass gasification and power generation under various operating conditions was assessed using a comprehensive Aspen Plus model for system optimization. The model was validated by pilot-scale experimental data and gas turbine regulations, showing good agreement. Parameters including oxygen percentage of enriched air (OP), gasification temperature, excess air ratio and compressor pressure ratio were studied for BIGCC optimization. Results showed that increase OP could effectively improve syngas quality and two-stage gasification efficiency, enhancing the gas turbine inlet and outlet temperature. The maximum BIGCC fuel utilization efficiency could be obtained at OP of 40%. Increasing gasification temperature showed a negative effect on the two-stage gasification performance. For efficient BIGCC operation, the excess air ratio should be below 3.5 to maintain a designed gas turbine inlet temperature. Modest increase of compressor pressure ratio favored the power generation. Finally, the BIGCC energy analysis further proved the rationality of system design and sufficient utilization of biomass energy. 相似文献
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Jong Jun Lee Young Sik Kim Kyu Sang Cha Tong Seop Kim Jeong L. Sohn Yong Jin Joo 《Applied Energy》2009
An IGCC (integrated gasification combined cycle) plant consists of a power block and a gasifier block, and a smooth integration of these two parts is important. This work has analyzed the influences of the major design options on the performance of an IGCC plant. These options include the method of integrating a gas turbine with an air separation unit and the degree of nitrogen supply from the ASU to the gas turbine combustor. Research focus was given to the effect of each option on the gas turbine operating condition along with plant performance. Initially, an analysis adopting an existing gas turbine without any modifications of its components was performed to examine the influence of two design options on the operability of the gas turbine and performance of the entire IGCC plant. It is shown that a high integration degree, where much of the air required at the air separation unit is supplied by the gas turbine compressor, can be a better option considering both the system performance and operation limitation of the gas turbine. The nitrogen supply enhances system performance, but a high supply ratio can only be acceptable in high integration degree designs. Secondly, the modifications of gas turbine components to resume the operating surge margin, such as increasing the maximum compressor pressure ratio by adding a couple of stages and increasing turbine swallowing capacity, were simulated and their effects on system performance were examined. Modification can be a good option when a low integration degree is to be adopted, as it provides a considerable power increase. 相似文献
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A thermodynamic analysis of a Biomass Integrated Gasification Combined Cycle (BIGCC) plant has been performed based on energy and exergy balances in a proposed configuration. Combustion of supplementary biomass fuel is considered using the oxygen available in the gas turbine (GT) exhaust. The effects of pressure and temperature ratios of the GT system and the amount of fuel burned in the supplementary firing chamber on the thermal and exergetic efficiencies of the plant have been investigated. The plant efficiencies increase with the increase in both pressure and temperature ratios; however, the latter has a stronger influence than the former. Supplementary firing of biomass increases the plant efficiencies of a BIGCC plant till an optimum level of degree of firing. The other technical issues related to supplementary firing, like ash fusion in the furnace and exhaust heat loss maintaining a minimum pinch point temperature difference are accounted and finally a set of optimum plant operating parameters have been identified. The performance of a 50 MWe plant has been analyzed with the optimum operating parameters to find out equipment rating and biomass feed rates. Exergetic efficiencies of different plant equipments are evaluated to localize the major thermodynamic irreversibilities in the plant. 相似文献