Process simulation of cassava cellulosic ethanol production with low to medium-pressure steam heat integration

被引:1
|
作者
Kamsuwan, Chaiyanan [1 ]
Tanprasert, Sorathan [1 ]
Nimmanterdwong, Prathana [1 ]
Piemjaiswang, Ratchanon [2 ]
Saencharee, Kanokporn [3 ]
Pumchumpol, Tanakorn [3 ]
Chalermsinsuwan, Benjapon [1 ,3 ,4 ]
机构
[1] Chulalongkorn Univ, Dept Chem Technol, Fuels Res Ctr, Fac Sci, Bangkok 10330, Thailand
[2] Chulalongkorn Univ, Environm Res Inst, Bangkok 10330, Thailand
[3] Integrated Res Ctr, 122 Moo 2 Thatoom Subdistrict, Si Maha Phot 25140, Prachin Buri, Thailand
[4] Chulalongkorn Univ, Ctr Excellence Petrochem & Mat Technol, Bangkok 10330, Thailand
关键词
Process simulation; Low to medium-pressure steam; Ethanol; Heat integration; Casava cellulosic;
D O I
10.1016/j.egyr.2023.04.246
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Energy demand tends to increase by 80% in 2050 due to the rapid growth of the global population. However, the energy resources rapidly decrease for responding to the global need. Many previous researchers suggest the ideas for solving this situation and the most interesting solution is the heat integration which intends to produce cost-effective energy with minimal impact on the environment. Energy integration thus should be noticeable for the industry process to minimize the loss along the industrial process. The ethanol production process is interested in this study because it can add value to agricultural products like cassava which is an industrial crop in several countries and produces ethanol products that can decrease the usage of gasoline. Here, the heat integration model was developed for the ethanol production process by using low to medium-pressure steam. For the simulation model, the ethanol production process used the cellulose content as the main inlet component to be easy for applicable corresponding to feed casava cellulosic substances. The process contained three sections including enzymatic hydrolysis, simultaneous saccharification fermentation (SSF), and fractional distillation. The quality and quantity of low to medium-pressure steam were investigated for maintaining the operation of the enzymatic hydrolysis reactor by varying steam pressure between 1-2 atm and steam temperature between 100-105 degrees C. The results achieved the methodology to find optimum conditions by the ratio between steam flow rate and product quantity. The best case could reduce 6.49% of the excessive usage of low to medium-pressure steam which pointed out the way to use the energy efficiently. (c) 2023 The Author(s). Published by Elsevier Ltd.
引用
收藏
页码:11 / 17
页数:7
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