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在集成生物柴油工艺中,将酶法酯化与传统的碱性酯交换结合。

Combining enzymatic esterification with conventional alkaline transesterification in an integrated biodiesel process.

机构信息

Novozymes, Krogshoejvej 36, 2880 Bagsvaerd, Denmark.

出版信息

Appl Biochem Biotechnol. 2011 Apr;163(7):918-27. doi: 10.1007/s12010-010-9095-9. Epub 2010 Sep 28.

Abstract

An integrated biodiesel process that combines enzymatic esterification and alkaline transesterification is suggested. With focus on the enzymatic step, the paper provides proof of concept and suggestions for further process development. Hence, palm fatty acid distillate (PFAD) has been enzymatically converted to fatty acid methyl esters in a two-step process using the immobilized lipase Novozym 435 in packed-bed columns. With only a small excess of methanol, the first reaction stage could reduce the free fatty acid (FFA) content from 85% to 5%. After removal of water by simple phase separation, it was possible to lower the FFA content to 2.5% in a second reaction stage. Both reaction stages are relatively fast with suggested reaction times of 15 min in column 1 (productivity 10 kg/kg/h) and 30 min in column 2 (productivity 5 kg/kg/h), resulting in 15% FFA after column 1 and 5% FFA after column 2. A lifetime study indicated that approximately 3,500 kg PFAD/kg Novozym 435 can be treated in the first reaction stage before the enzyme has become fully inactivated. With further optimization, the enzymatic process could be a real alternative to today's sulfuric acid catalyzed process.

摘要

本文提出了一种将酶法酯化和碱性酯交换相结合的集成生物柴油工艺。重点关注酶法步骤,为进一步的工艺开发提供了概念验证和建议。因此,使用固定化脂肪酶 Novozym 435 在填充床柱中,通过两步法将棕榈脂肪酸馏分(PFAD)酶法转化为脂肪酸甲酯。只需甲醇稍微过量,第一反应阶段就可以将游离脂肪酸(FFA)含量从 85%降低到 5%。简单的相分离除去水后,在第二反应阶段可以将 FFA 含量降低到 2.5%。两个反应阶段都相对较快,在第 1 根柱子中的建议反应时间为 15 分钟(生产率为 10kg/kg/h),在第 2 根柱子中的建议反应时间为 30 分钟(生产率为 5kg/kg/h),因此第 1 根柱子后 FFA 含量为 15%,第 2 根柱子后 FFA 含量为 5%。寿命研究表明,在酶完全失活之前,大约可以用 3500kg PFAD/kg Novozym 435 处理第一反应阶段。通过进一步优化,该酶法工艺可能成为当今硫酸催化工艺的真正替代方法。

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