4.7 Article

Technoeconomic analysis of a low CO2 emission dimethyl ether (DME) plant based on gasification of torrefied biomass

期刊

ENERGY
卷 35, 期 12, 页码 4831-4842

出版社

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.energy.2010.09.004

关键词

Biorefinery; Biofuel; Torrefication; Gasification; Syngas; CO2 capture

向作者/读者索取更多资源

Two models of a dimethyl ether (DME) fuel production plant were designed and analyzed in DNA and Aspen Plus. The plants produce DME by either recycle (RC) or once through (OT) catalytic conversion of a syngas generated by gasification of torrefied woody biomass. Torrefication is a mild pyrolysis process that takes place at 200-300 degrees C. Torrefied biomass has properties similar to coal, which enables the use of commercially available coal gasification processing equipment. The DME plants are designed with focus on lowering the total CO2 emissions from the plants; this includes e.g. a recycle of a CO2 rich stream to a CO2 capture plant, which is used in the conditioning of the syngas. The plant models predict energy efficiencies from torrefied biomass to DME of 66% (RC) and 48% (OT) (LHV). If the exported electricity is included, the efficiencies are 71% (RC) and 64% (OT). When accounting for energy loss in torrefaction, the total efficiencies are reduced to 64% (RC) and 58% (OT). The two plants produce DME at an estimated cost of $11.9/GJ(LHV) (RC) and $12.9/GJ(LHV) (OT). If a credit is given for storing the CO2 captured, the future costs may become as low as $5.4/GJ(LHV) (RC) and $3.1/GJ(LHV) (OT). (C) 2010 Elsevier Ltd. All rights reserved.

作者

我是这篇论文的作者
点击您的名字以认领此论文并将其添加到您的个人资料中。

评论

主要评分

4.7
评分不足

次要评分

新颖性
-
重要性
-
科学严谨性
-
评价这篇论文

推荐

暂无数据
暂无数据