中文摘要：

固体热载体加热生物质是生物质热解制取生物油的工艺手段之一。为解决固体热载体间接加热方式升温慢、效率低问题,设计了一种流化床生物质燃烧的热烟气直接加热固体热载体装置,分析了其结构与原理,开展了固体热载体升温性能和流化床燃烧器的燃烧特性试验研究,并对试验结果进行了热平衡分析。结果表明：流化床高温烟气加热陶瓷球热载体的平均热能利用率为66.3%,流化床燃烧生物质粉产生的高温烟气能够满足热载体加热装置对热源的需求,热载体加热器内的热量传递方式主要是对流换热。陶瓷球热载体与加热器内高温烟气的对流传热系数为475 W/（m^2·℃）。研究对结果对解决生物质热解液化技术中的固体热载体加热升温关键问题具有重要指导意义。

英文摘要：

Biomass is one of environment friendly and renewable resources, which is considered as an ideally clean energy. In general, the development and utilization of biomass energy aim at converting the solid agricultural and forestry wastes into gaseous, solid or liquid fuels by physical or chemical processing methods. Solid heat carrier heating biomass is one of the process means of preparing bio-oil from biomass pyrolysis. In order to solve the indirect heating slow and low efficiency problems of solid heat carrier heating, a solid heat carrier heating device heated by high temperature flue gas which was generated by fluidized bed combustor was designed, and its structure and principle were analyzed, including high temperature flue gas generator, feeder of ceramic ball, heat carrier heat exchanger, built-in baffle, data acquisition and control system. The device could carry out the solid heat carrier heating performance and the combustion characteristic of fluidized bed combustor. Furthermore, the heat balance analysis of test results was performed. Biomass powder fuel was conducted on proximate analysis, ultimate analysis and determination of low calorific value, the results showed that the biomass powder fuel was a kind of clean energy. By conducting tests of biomass powder fuel combustion on high temperature gas generating apparatus to determine optimum powder concentration was 240 g/m^3. The fluidized bed combustion furnace temperature changes were analyzed under optimal wind powder concentration, which indicated that biomass powder burning had ideal effect, the burner could be continuous, stable producing high temperature flue gas. By studying the temperature variation during the heat exchange process of ceramic balls and high temperature flue gas, the convective heat transfer coefficient of ceramic ball and high temperature flue gas and the heat utilization efficiency of the device were obtained. The convection heat transfer coefficient between ceramic balls and the high temperature flue gas was calculated and