生物质气化联合循环发电技术的探讨

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。     

生物质整体气化联合循环发电系统的发展现状

文章介绍了生物质整体气化联合循环发电系统（RIGCC）搜其关键技术和设备，阐述了目前出现的大型生物质整体气化联合循环发电系统示范工程的工艺过程和运行经验，对我国发展BIGCC技术的可行性进行了分析，并提出目前需要解决的关键技术问题。     

生物质气化耦合燃煤发电技术的应用

生物质气化耦合燃煤发电技术是生物质资源利用的重要发展方向。根据生物质气化耦合燃煤发电技术的原理,进行生物质气化耦合燃煤发电的实际应用,研究该技术在应用过程中存在的一些问题及对策,说明生物质气化耦合燃煤发电是生物质高效和经济的应用途径之一。     

中国生物质能利用技术评价

本文针对目前我国已有的生物质能利用技术进行技术评价,主要有生物质燃烧技术(包括炉灶燃烧技术、锅炉燃烧发电技术和生物质型煤技术)、生物质气化技术(包括生物质气化技术、生物质气化发电技术)和生物质热裂解液化技术。本文在阐述我国生物质能源开发利用的意义的基础上,综述了上述各种技术发展现状与近年来的应用情况,对我国生物质能利用技术的发展有参考价值。     

浅谈生物质气化在发电技术应用

随着经济的发展,世界各国电力需求猛增,电力供应日益紧张,在这种环境下,通过气化发电技术,把生物质能转化为电能,既能大规模处理生物质废料,又能提供电力,具有明显的社会和经济效益。介绍了生物质气化发电技术的国内外发展现状,着重讲述了生物质气化发电技术的原理、特点和分类,以及各类生物质气化发电技术的特点,分析了生物质气化发电技术的社会效益及应用前景。指出在我国这样一个农业大国应该大力发展生物质气化发电技术。     

生物质能应用技术现状及发展趋势

综述了国内外生物质能应用技术现状，包括生物质捆包直燃供热技术、生物质成型燃料供热技术、生物质直燃发电技术、生物质气化多联产技术、生物质气化产碳耦合供热技术、生物质气化耦合大型燃煤锅炉技术，以及生物质气化制氢、NH₃及甲醇技术，为生物质能进一步利用提供方向。     

生物质发电技术发展探讨

联系生物质发电技术的发展趋势,分别对生物质直接燃烧发电技术、生物质与煤混合直燃发电技术和生物质气化发电技术进行深入分析,并对比生物质直燃技术和生物质气化技术的优劣势。     

我国生物质发电产业现状及建议

生物质发电是目前发展最成熟、规模最大的生物质能利用技术,通过利用生物质燃烧或转化技术实现可燃气体的燃烧发电。文章叙述了我国发展生物质发电产业的意义,概括和总结了国内外在生物质直燃发电、混燃发电和气化发电方面的现状和经验,指出我国生物质发电产业所面临的挑战,最后提出了有关生物质发电产业的商业化建议。     

生物质流化床气化技术应用研究现状

按所得产品不同,可将生物质气化技术分为制氢、发电和合成液体燃料3大类。文章介绍了生物质流化床水蒸气气化制氢、催化气化制氢和超临界水气化制氢的工艺特点;分析了生物质流化床气化发电的技术、经济可行性;简述了生物质流化床气化合成液体燃料的研究现状;指出气化产出气化学当量比调变、焦油去除问题和合成气净化是生物质流化床气化技术应用的主要瓶颈,认为定向气化是今后研究的主要方向。     

生物质气化发电机技术（1）气化发电的工作原理及工艺流程

１气化发电工作原理生物质气化发电技术的基本原理是把生物质转化为可燃气,再利用可燃气推动燃气发电设备进行发电。它既能解决生物质难于燃用而且分布分散的缺点,又可以充分发挥燃气发电技术设备紧凑而且污染少的优点,所以气化发电是生物质能最有效最洁净的利用方法之一。气化发电过程包括３个方面：一是生物质气化,把固体生物质转化为气体燃料;二是气体净化,气化出来的燃气都含有一定的杂质,包括灰分、焦炭和焦油等,需经过净化系统把杂质除去,以保证燃气发电设备的正常运行;三是燃气发电,利用燃气轮机或燃气内燃机进行发电,有…     

Simulation of a new biomass integrated gasification combined cycle (BIGCC) power generation system using Aspen Plus: Performance analysis and energetic assessment

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.     

Systems analysis of integrating biomass gasification with pulp and paper production - Effects on economic performance, CO2 emissions and energy use

This paper evaluates system aspects of biorefineries based on biomass gasification integrated with pulp and paper production. As a case the Billerud Karlsborg mill is used. Two biomass gasification concepts are considered: BIGDME (biomass integrated gasification dimethyl ether production) and BIGCC (biomass integrated gasification combined cycle). The systems analysis is made with respect to economic performance, global CO₂ emissions and primary energy use. As reference cases, BIGDME and BIGCC integrated with district heating are considered. Biomass gasification is shown to be potentially profitable for the mill. The results are highly dependent on assumed energy market parameters, particularly policy support. With strong policies promoting biofuels or renewable electricity, the calculated opportunity to invest in a gasification-based biorefinery exceeds investment cost estimates from the literature. When integrated with district heating the BIGDME case performs better than the BIGCC case, which shows high sensitivity to heat price and annual operating time. The BIGCC cases show potential to contribute to decreased global CO₂ emissions and energy use, which the BIGDME cases do not, mainly due to high biomass demand. As biomass is a limited resource, increased biomass use due to investments in gasification plants will lead to increased use of fossil fuels elsewhere in the system.     

生物质气化技术面临的挑战及技术选择

生物质气化可实现低品位生物质能的深层次利用,不同地区、不同行业有不同的能源需求和产业结构,应合理选择生物质气化技术。固定床气化技术针对的是中小规模应用,该技术存在的问题包括焦油含量高、规模小、机械化和自动化程度较低、发电效率低等。流化床气化技术针对的是中等及以上规模应用,目前需要解决的问题是热效率低,发电效率低,需要开发高气化效率和无焦油的燃气型气化炉、低热值燃气轮机、高效燃气净化系统,以便采用BIGCC技术。沼气技术是一项生物质综合高效清洁利用的多联产工艺,目前急需开发高效高浓度厌氧消化的沼气发酵工艺和配套的集成设备,培育和筛选高效沼气发酵微生物菌群,简化沼气净化工序,解决沼液、沼渣的利用难题等。生物质快速热解技术是一种高温处理过程,其最大的优点是产物生物油易于储存运输,不存在产品规模和消费的地域限制问题。从工艺特点、经济效益和规模化生产来看,沼气技术更适合处理高含水的养殖业粪便,快速热解技术更适合农作物秸秆的规模化转化,燃气型气化技术更适合社区生活垃圾和农林产品加工废弃物的处理。     

Reducing life cycle greenhouse gas emissions of corn ethanol by integrating biomass to produce heat and power at ethanol plants

A life-cycle assessment (LCA) of corn ethanol was conducted to determine the reduction in the life-cycle greenhouse gas (GHG) emissions for corn ethanol compared to gasoline by integrating biomass fuels to replace fossil fuels (natural gas and grid electricity) in a U.S. Midwest dry-grind corn ethanol plant producing 0.19 hm³ y⁻¹ of denatured ethanol. The biomass fuels studied are corn stover and ethanol co-products [dried distillers grains with solubles (DDGS), and syrup (solubles portion of DDGS)]. The biomass conversion technologies/systems considered are process heat (PH) only systems, combined heat and power (CHP) systems, and biomass integrated gasification combined cycle (BIGCC) systems. The life-cycle GHG emission reduction for corn ethanol compared to gasoline is 38.9% for PH with natural gas, 57.7% for PH with corn stover, 79.1% for CHP with corn stover, 78.2% for IGCC with natural gas, 119.0% for BIGCC with corn stover, and 111.4% for BIGCC with syrup and stover. These GHG emission estimates do not include indirect land use change effects. GHG emission reductions for CHP, IGCC, and BIGCC include power sent to the grid which replaces electricity from coal. BIGCC results in greater reductions in GHG emissions than IGCC with natural gas because biomass is substituted for fossil fuels. In addition, underground sequestration of CO₂ gas from the ethanol plant’s fermentation tank could further reduce the life-cycle GHG emission for corn ethanol by 32% compared to gasoline.     

户用型下吸式生物质气化炉性能研究

由于生物质能具有储量大、环境友好等特点,生物质气化技术尤其是户用型气化技术在我国农村应用值得研究。论文在建立下吸式户用型气化系统上,研究了不同生物质原料的气化性能,如对温度分布、气化效率、燃气热值、燃气产量等,并进行了焦油脱除效率的研究。结果表明,该炉型的气化效率可达70％,燃气热值达到6MJ／m3,燃气中焦油含量降低至20mg／m3。     

Aspen Plus simulation of biomass integrated gasification combined cycle systems at corn ethanol plants

Biomass integrated gasification combined cycle (BIGCC) systems and natural gas combined cycle (NGCC) systems are employed to provide heat and electricity to a 0.19 hm³ y⁻¹ (50 million gallon per year) corn ethanol plant using different fuels (syrup and corn stover, corn stover alone, and natural gas). Aspen Plus simulations of BIGCC/NGCC systems are performed to study effects of different fuels, gas turbine compression pressure, dryers (steam tube or superheated steam) for biomass fuels and ethanol co-products, and steam tube dryer exhaust treatment methods. The goal is to maximize electricity generation while meeting process heat needs of the plant. At fuel input rates of 110 MW, BIGCC systems with steam tube dryers provide 20–25 MW of power to the grid with system thermal efficiencies (net power generated plus process heat rate divided by fuel input rate) of 69–74%. NGCC systems with steam tube dryers provide 26–30 MW of power to the grid with system thermal efficiencies of 74–78%. BIGCC systems with superheated steam dryers provide 20–22 MW of power to the grid with system thermal efficiencies of 53–56%. The life-cycle greenhouse gas (GHG) emission reduction for conventional corn ethanol compared to gasoline is 39% for process heat with natural gas (grid electricity), 117% for BIGCC with syrup and corn stover fuel, 124% for BIGCC with corn stover fuel, and 93% for NGCC with natural gas fuel. These GHG emission estimates do not include indirect land use change effects.