NaHSO4催化椰子油皂脚油酯化降酸工艺优化

以椰子油皂脚油为原料的生物柴油酯化效率与催化剂和结合反应装置的操作方法有关。以硫酸氢钠为催化剂结合设计的反应装置,对高酸值椰子油皂脚油进行预酯化反应研究。通过单因子试验探讨适用于反应装置的反应条件,并讨论不同的操作方式对反应速率和反应进程的影响。结果表明:最佳条件为:反应温度105℃,甲醇通入流速为0.825 mL/min,催化剂用量为5.0%,反应2 h下转化率>95%。催化剂重复使用9次后转化率78.15%;改变操作方法,0.1 MPa条件下反应,采用通入甲醇1.32 mL/min反应30 min,后常压条件下通入甲醇量0.825 mL/min,反应30 min,椰子油皂脚油酸值由106变为1.2 mg/g,转化率98.9%,并可缩短酯化时间1 h,油脂成品满足酯交换工序要求。精制的生物柴油成品所测试的技术指标符合德国现行生物柴油标准(DIN V 51606)。

Optimization of sodium bisulfate catalyzed esterification of soapstock of coconut oil to deacidification

Biodiesel is a fatty acid alkyl ester derived from renewable feedstocks such as plant oils, animal fats or waste oils by transesterification with short-chain alcohols and catalyst. It has attracted attention in the past decades as an alternative and sustainable energy source. The esterification efficiency of biodiesel using soapstock of coconut oil as raw material is related to catalyst and the operation method binding reaction device. Heterogeneous catalyst has the general advantages of easy separation, medium and reusability. In this paper, esterification of biodiesel with soapstock of coconut oil was studied using sodium bisulfate as catalyst on self-designed reaction device. First, the reaction conditions suitable for the device were studied through single factor experiments. Then, the effects of different operation modes on the reaction rate and process were researched. It indicated that proper operation method plays a key role in acid reduction of low grade oil. At the beginning, the results showed that the optimum conditions were as follows:When the reaction temperature was 105 ℃, the methanol flow rate was 0.825 m L/min, catalyst dosage was 5.0% and more than 95% esterification rate was obtained after 2 hours. Meanwhile, under this condition esterification rate was 78.15% after 9 times of catalyst reuse. The high stability can be recognized, which strengthen the target that to reduce the cost of produce through the reuse of catalyst. At last, esterification rate was 98.9%, and esterification time was shortened by 1 hour when changed the operation approaches by the amount of methanol was injected at 1.32 mL/min for 30 min under pressure condition, subsequently the amount of methanol was injected at 0.825 mL/min for 30 min under normal pressure condition. We are happy to see that the acid value of the coconut oil soap foot oil reduced from 106 to 1.2 mg/g using this operation method. This means that we have successfully reduced the acid value of high acid value oil and the oil met the requirements of the subsequent ester exchange process. The raw material of low acid oil can be transformed into biodiesel by transesterification and biodiesel was being tested technical indicators met the current German biodiesel standards(DIN V 51606) after transesterification.