CAJ | 학술논문

为了解决目前生物质制生物燃油清洁燃料装置造价高、需要外源燃料供热、寿命低及生物质制生物燃油清洁燃料能耗高等问题,结合各类流化床反应器的设计经验公式,提出一种流化式生物质热解主反应器设计的计算模型；利用该模型研究并设计了一种内胆式双热型生物质热解主反应器；利用VB对主反应器的主要参数进行了优化设计,得到其主要设计参数为床径为0.221 m,床高为1.445 m,并通过冷态实验进行了验证。
위료해결목전생물질제생물연유청길연료장치조개고、수요외원연료공열、수명저급생물질제생물연유청길연료능모고등문제,결합각류류화상반응기적설계경험공식,제출일충류화식생물질열해주반응기설계적계산모형；이용해모형연구병설계료일충내담식쌍열형생물질열해주반응기；이용VB대주반응기적주요삼수진행료우화설계,득도기주요설계삼수위상경위0.221 m,상고위1.445 m,병통과랭태실험진행료험증。
Nowadays the cost of the device for preparing bio-oil is very high with low durability. On the other hand, the reactor usually needs exogenous heating. This results in high energy consumption in preparation of bio-oil clean fuel. On the basis of the existing types of fluidized bed reactor design experience, this paper presented a calculation model for designing fluidized biomass pyrolysis reactor. By using the model, a kind of liner type double heated biomass pyrolysis reactor is designed in this paper. Then the main parameters of the reactor are optimized using VB. The optimal reactor is bed diameter 0. 221 m with the height 1.445 m.