Development of Innovative Methanol Synthesis Process Based on Self-Heat Recuperation

被引:4
作者
Kansha, Yasuki [1 ]
Ishizuka, Masanori [1 ]
Tsutsumi, Atsushi [1 ]
机构
[1] Univ Tokyo, Inst Ind Sci, Collaborat Res Ctr Energy Engn, Meguro Ku, Tokyo 1538505, Japan
来源
16TH INTERNATIONAL CONFERENCE ON PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION (PRES'13) | 2013年 / 35卷
关键词
FIXED-BED REACTOR; TECHNOLOGY; DESIGN;
D O I
10.3303/CET1335006
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
In recent years, the demand for methanol will continue increasing. As well as other chemical processes, many methanol synthesis processes have reactant recycle system with product separation due to the low conversion ratio of the reactor. For this product separation from reactant recycle stream, a gas-liquid separator or distillation process has often been used. However, this gas-liquid separator and distillation processes are well known as an energy intensive process. Thus, many chemical engineers and investigators have been managing to produce a catalyst which achieves high conversion from reactant to production in the reactor for whole process optimization. In contrast, authors have developed self-heat recuperation technology based on exergy recuperation, in which whole process heat is utilized without any additional heat, leading to the reduction of energy requirement in several chemical processes. In this research, we developed an innovative integrated process design method based on self-heat recuperation for methanol synthesis process from energy saving point of view.
引用
收藏
页码:37 / 42
页数:6
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