生物质粉复合气化燃烧系统Biomass powder composite gasification combustion system
技术领域Technical field
本发明涉及生物质燃烧技术,具体为一种生物质粉复合气化燃烧系统。The invention relates to a biomass burning technology, in particular to a biomass powder composite gasification combustion system.
背景技术Background technique
新能源技术作为二十一世纪世界经济发展中最具影响的技术之一,人类最终将依靠新能源产业的发展来解决全球的能源危机和环境污染问题,实现可持续发展。国家鼓励的可再生能源中,最大一块就是生物质能的发电和利用,我国拥有丰富的生物质能资源,据测算,我国理论生物质能资源为50亿吨左右。目前,可供利用开发的生物质能资源主要为生物质废弃物,包括农作物秸秆、谷壳、薪柴、工业有机废弃物和城市固体有机垃圾等。面对经济发展中如影随形的高消耗、高污染和资源环境约束问题,近年来,中国开始寻求经济增长模式的全面转变,走节约型发展道路。循环经济是一种以资源的高效利用和循环利用为核心,以″减量化、再利用、资源化″为原则,以低消耗、低排放、高效率为基本特征,符合可持续发展理念的经济增长模式,是对″大量生产、大量消费、大量废弃″的传统增长模式的根本变革。生物质能是一个重要的能源,预计到下世纪,世界能源消费的40%来自生物质能,我国有丰富的生物质能资源,我国农村能源的70%是生物质,仅农村秸杆每年总量达6亿多吨。随着经济的发展,人们生活水平的提高,环境保护意识的加强,对生物质能的合理、高效开发利用,必然愈来 愈受到人们的重视。As one of the most influential technologies in the world economic development in the 21st century, new energy technologies will eventually rely on the development of new energy industries to solve global energy crisis and environmental pollution problems and achieve sustainable development. Among the renewable energy sources encouraged by the state, the largest one is the generation and utilization of biomass energy. China has abundant biomass energy resources. According to estimates, China's theoretical biomass energy resources are about 5 billion tons. At present, the biomass energy resources available for development are mainly biomass waste, including crop straw, chaff, fuelwood, industrial organic waste and municipal solid organic waste. In the face of the high consumption, high pollution and resource and environmental constraints in economic development, in recent years, China has begun to seek a comprehensive transformation of the economic growth model and take a conservation-oriented development path. The circular economy is based on the efficient use and recycling of resources, with the principle of “reduction, reuse and resource utilization”, with low consumption, low emission and high efficiency as the basic characteristics, in line with the concept of sustainable development. The economic growth model is a fundamental change in the traditional growth model of “mass production, mass consumption, and mass abandonment”. Biomass energy is an important energy source. It is estimated that in the next century, 40% of the world's energy consumption comes from biomass energy. China has abundant biomass energy resources. 70% of China's rural energy is biomass, and only rural straw is always used every year. The amount reached more than 600 million tons. With the development of the economy, the improvement of people's living standards, the strengthening of environmental protection awareness, and the rational and efficient development and utilization of biomass energy, it is increasingly attracting people's attention.
目前,生物质粉的燃烧效率比较低下,如果不进一步提升效率,就很难商业化、产业化推广。At present, the combustion efficiency of biomass powder is relatively low. If the efficiency is not further improved, it will be difficult to commercialize and industrialize.
发明内容Summary of the invention
为了克服现有技术提及的缺点,本发明提供一种生物质粉复合气化燃烧系统。In order to overcome the disadvantages mentioned in the prior art, the present invention provides a biomass powder composite gasification combustion system.
本发明解决其技术问题所采用技术方案为:生物质粉复合气化燃烧系统,包括立式布置的混合塔以及横式布置的燃烧炉,所述混合塔的顶部中心处设有生物质粉入口,所述混合塔的底部连接所述燃烧炉的上端中部处,所述燃烧炉的底部设有往复炉排,所述燃烧炉的前侧设有热风出口;所述混合塔内还设有均流腔,所述生物质粉入口连通所述均流腔,所述均流腔的侧壁上均设有若干通孔,所有所述通孔连通所述混合塔的内腔,所述混合塔的侧壁由上至下还依次间隔设有一次风入口管、石油焦粉入口管和二次风入口管,所述一次风入口管连通所述均流腔,所述石油焦粉入口管和二次风入口管连通所述混合塔的内腔。The technical solution adopted by the present invention to solve the technical problem is: a biomass powder composite gasification combustion system, comprising a vertically arranged mixing tower and a horizontally arranged combustion furnace, wherein the mixing tower has a biomass powder inlet at the top center a bottom of the mixing tower is connected to a middle portion of an upper end of the combustion furnace, a bottom of the combustion furnace is provided with a reciprocating grate, a front side of the burning furnace is provided with a hot air outlet; and the mixing tower is further provided with a hot air outlet a flow chamber, the biomass powder inlet is connected to the current sharing chamber, and a sidewall of the current sharing chamber is provided with a plurality of through holes, all of the through holes communicating with the inner cavity of the mixing tower, the mixing tower The side wall is further provided with a primary air inlet pipe, a petroleum coke powder inlet pipe and a secondary air inlet pipe from top to bottom, wherein the primary air inlet pipe communicates with the current sharing cavity, the petroleum coke powder inlet pipe and A secondary air inlet conduit communicates with the interior of the mixing tower.
所述一次风入口管的注入方向与所述生物质粉入口的注入方向相垂直,所述石油焦粉入口管的注入方向与所述均流腔的外侧壁相切,所述二次风入口管的注入方向与所述一次风入口管的注入方向呈相对或相垂直设置。The injection direction of the primary air inlet pipe is perpendicular to the injection direction of the biomass powder inlet, and the injection direction of the petroleum coke powder inlet pipe is tangent to the outer sidewall of the current sharing cavity, and the secondary air inlet The injection direction of the tube is opposite or perpendicular to the injection direction of the primary air inlet tube.
所述一次风入口管、石油焦粉入口管和二次风入口管处均设有仅容许朝所述混合塔内部注入的单向阀。The primary air inlet pipe, the petroleum coke powder inlet pipe, and the secondary air inlet pipe are each provided with a check valve that allows only injection into the interior of the mixing tower.
所述混合塔的底部呈漏斗状。The bottom of the mixing tower is funnel shaped.
所述混合塔内还安装有匀风板,所述匀风板置于所述混合塔内的下部,所述匀风板上均匀开设有若干匀风孔。A homogenizing plate is further disposed in the mixing tower, and the uniformizing plate is disposed in a lower portion of the mixing tower, and the uniformizing plate is uniformly provided with a plurality of uniform air holes.
所述通孔的孔径为50~60mm,所述匀风孔的孔径为80~100mm。The through hole has a diameter of 50 to 60 mm, and the uniform hole has a diameter of 80 to 100 mm.
本发明的有益效果是:本设计的生物质粉复合气化燃烧系统,结构简单,通过在混合塔的顶部注入生物质粉,侧面的一次风入口管、石油焦粉入口管和二次风入口管依次切向注入一次风、石油焦粉和二次风,生物质粉在一次风的鼓吹下,在均流腔内形成旋风,然后通过均流腔侧壁的通孔均匀地喷入混合塔内,再与石油焦粉和二次风形成旋流式混合,使得进入燃烧炉内的生物质粉燃烧气化效率得以大大提高。The beneficial effects of the invention are: the biomass powder composite gasification combustion system of the design has a simple structure, by injecting biomass powder on the top of the mixing tower, the primary air inlet pipe on the side, the petroleum coke powder inlet pipe and the secondary air inlet. The tube injects the primary wind, the petroleum coke powder and the secondary air in turn, and the biomass powder forms a cyclone in the uniform flow chamber under the blowing of the primary air, and then uniformly sprays into the mixing tower through the through holes of the side wall of the equalization chamber. Inside, the cyclone mixing with the petroleum coke powder and the secondary air is formed, so that the combustion efficiency of the biomass powder entering the combustion furnace is greatly improved.
附图说明DRAWINGS
图1为本发明的整体结构主视图;Figure 1 is a front elevational view of the overall structure of the present invention;
图2为本发明的混合塔结构俯视图。Figure 2 is a plan view showing the structure of the mixing tower of the present invention.
具体实施方式Detailed ways
下面结合附图对本发明进行进一步的说明。The invention will now be further described with reference to the accompanying drawings.
如图1和图2所示,生物质粉复合气化燃烧系统,包括立式布置的混合塔1以及横式布置的燃烧炉2,所述混合塔1的顶部中心处设有生物质粉入口11,所述混合塔1的底部连接所述燃烧炉2的上端中部处,所述燃烧炉2的前侧设有热风出口21,所述燃烧炉2的底部设有往复炉排22,往复炉排22的末端设有 螺旋排渣装置23;所述混合塔1内还设有均流腔3,所述生物质粉入口11连通所述均流腔3,所述均流腔3的侧壁上均设有若干通孔31,所有所述通孔31连通所述混合塔1的内腔,所述混合塔1的侧壁由上至下还依次间隔设有一次风入口管12、石油焦粉入口管13和二次风入口管14,所述一次风入口管12连通所述均流腔3,所述石油焦粉入口管13和二次风入口管14连通所述混合塔1的内腔。As shown in FIG. 1 and FIG. 2, the biomass powder composite gasification combustion system comprises a vertically arranged mixing tower 1 and a horizontally arranged combustion furnace 2, and a biomass powder inlet is arranged at the top center of the mixing tower 1. 11. The bottom of the mixing tower 1 is connected to the middle of the upper end of the combustion furnace 2, the front side of the combustion furnace 2 is provided with a hot air outlet 21, and the bottom of the combustion furnace 2 is provided with a reciprocating grate 22, a reciprocating furnace The end of the row 22 is provided with a spiral slagging device 23; the mixing tower 1 is further provided with a current sharing chamber 3, the biomass powder inlet 11 is connected to the current sharing chamber 3, and the side wall of the current sharing chamber 3 Each of the through holes 31 is connected to the inner cavity of the mixing tower 1, and the side wall of the mixing tower 1 is sequentially spaced from top to bottom with a primary air inlet pipe 12 and petroleum coke. a powder inlet pipe 13 and a secondary air inlet pipe 14, the primary air inlet pipe 12 communicating with the equalizing chamber 3, the petroleum coke powder inlet pipe 13 and the secondary air inlet pipe 14 communicating with the inside of the mixing tower 1 Cavity.
所述一次风入口管12的注入方向与所述生物质粉入口11的注入方向相垂直,所述石油焦粉入口管13的注入方向与所述均流腔3的外侧壁相切,而且石油焦粉入口管13的数量可以设置为多个,呈以所述混合塔1的圆心为中心圆周分布;所述二次风入口管14的注入方向与所述一次风入口管11的注入方向呈相对或相垂直设置。The injection direction of the primary air inlet pipe 12 is perpendicular to the injection direction of the biomass powder inlet 11, the injection direction of the petroleum coke powder inlet pipe 13 is tangent to the outer side wall of the current sharing cavity 3, and the oil The number of the coke powder inlet tubes 13 may be set to be plural, distributed around the center of the center of the mixing tower 1; the injection direction of the secondary air inlet tubes 14 and the injection direction of the primary air inlet tubes 11 are Relative or vertical setting.
所述一次风入口管12、石油焦粉入口管13和二次风入口管14处均设有仅容许朝所述混合塔1内部注入的单向阀15。The primary air inlet pipe 12, the petroleum coke powder inlet pipe 13, and the secondary air inlet pipe 14 are each provided with a check valve 15 that allows only injection into the interior of the mixing tower 1.
所述混合塔1的底部呈漏斗状。The bottom of the mixing tower 1 has a funnel shape.
所述混合塔1内还安装有匀风板4,所述匀风板4置于所述混合塔1内的下部,所述匀风板4上均匀开设有若干匀风孔41。The mixing tower 1 is further provided with a uniform wind plate 4, which is placed in a lower portion of the mixing tower 1, and a plurality of uniform air holes 41 are evenly opened on the uniform air plate 4.
所述通孔31的孔径为50~60mm,所述匀风孔41的孔径为80~100mm。The through hole 31 has a diameter of 50 to 60 mm, and the uniform hole 41 has a hole diameter of 80 to 100 mm.
以上所述者,仅为本发明的较佳实施例而已,当不能以此限定本发明实施的范围,即大凡依本发明申请专利范围及发明 说明内容所作的简单等效变化与修饰,皆仍属本发明专利涵盖的范围内。The above is only the preferred embodiment of the present invention, and the scope of the invention is not limited thereto, that is, the simple equivalent changes and modifications made by the scope of the invention and the description of the invention are still It is within the scope of the patent of the present invention.