Shekhawat Dushyant, Jackson James E, Miller Dennis J
Department of Chemical Engineering and Materials Science, 2527 Engineering Building, Michigan State University, East Lansing, MI 48824, USA.
Bioresour Technol. 2006 Jan;97(2):342-7. doi: 10.1016/j.biortech.2005.02.036. Epub 2005 Apr 25.
A complete process model and economic analysis has been developed for itaconic acid production via catalytic condensation of dimethyl succinate and formaldehyde. The process model is based on experimental yields and selectivities obtained for the condensation reaction and on recovery schemes for itaconic acid developed in our laboratory. For an 18 million kg/yr (40 million lb/yr) itaconic acid production facility with a 10-year lifetime, the model predicts a capital investment of $40 million and an itaconic acid selling price of $2.34/kg ($1.06/lb) to achieve 30% annual return on investment. Feedstock cost is the largest contributor to the price of itaconic acid; succinate conversion and selectivity to the intermediate citraconic acid therefore most strongly influence process economics. Results of these analyses indicate that itaconic acid can be produced catalytically from succinic acid and formaldehyde at lower cost than via the current fungal fermentation route.
通过丁二酸二甲酯与甲醛的催化缩合生产衣康酸,已开发出完整的工艺模型和经济分析方法。该工艺模型基于缩合反应的实验产率和选择性,以及我们实验室开发的衣康酸回收方案。对于一个年产能1800万千克(4000万磅)、寿命为10年的衣康酸生产装置,该模型预测资本投资为4000万美元,衣康酸售价为2.34美元/千克(1.06美元/磅),以实现30%的年投资回报率。原料成本是衣康酸价格的最大组成部分;因此,琥珀酸转化率和中间产物柠康酸的选择性对工艺经济性影响最大。这些分析结果表明,通过催化方法由琥珀酸和甲醛生产衣康酸的成本低于目前的真菌发酵路线。