Behzadi Sam, Farid Mohammed M
Department of Chemical and Materials Engineering, University of Auckland, Private Bag, 92019 Auckland, New Zealand.
Bioresour Technol. 2009 Jan;100(2):683-9. doi: 10.1016/j.biortech.2008.06.037. Epub 2008 Jul 30.
A novel continuous reactor process has been developed for the production of biodiesel from fats and oils. The key feature of the process is its ability to operate continuously with a high reaction rate, potentially requiring less post reaction cleaning and product/reactant separation than currently established processes. This was achieved by atomising the heated oil/fat and then spraying it into a reaction chamber filled with methanol vapor in a counter current flow arrangement. This allows the continuous separation of product and the excess methanol stream in the reactor. The overall conversion based on a single cycle of this process has been between 50% and 96% of the feed stock materials. Conversions of 94-96% were achieved while operating with 5-7 g of sodium methoxide/L of methanol at methanol flow rate of 17.2 L/h and oil flow rate of 10 L/h. Additional variations in the reactant stoichiometry (i.e. reactant flow rates), catalyst type/concentration, and reaction temperature on the overall product conversion were investigated.
已开发出一种新型连续反应器工艺,用于从油脂生产生物柴油。该工艺的关键特性在于能够以高反应速率连续运行,与目前已确立的工艺相比,可能需要更少的反应后清洗以及产物/反应物分离操作。这是通过将加热后的油脂雾化,然后以逆流布置方式喷入充满甲醇蒸气的反应室来实现的。这使得在反应器中能够连续分离产物和过量的甲醇流。基于该工艺单个循环的总转化率在原料的50%至96%之间。在甲醇流速为17.2 L/h、油流速为10 L/h,使用5 - 7 g甲醇钠/L甲醇运行时,转化率达到了94 - 96%。还研究了反应物化学计量比(即反应物流速)、催化剂类型/浓度以及反应温度对总产物转化率的其他影响。