TY - JOUR
T1 - Preliminary plant design of thermochemical conversion for rice straw-based second-generation bioethanol production in West Java
AU - Harahap, A. F.P.
AU - Arya Ramadhan, M. Y.
AU - Lee, W. C.
AU - Gozan, M.
N1 - Funding Information:
The authors gratefully acknowledge the funding by Universitas Indonesia through Hibah Pengabdian dan Pemberdayaan Masyarakat (PPM) grant (327/UN2.PPM/HKP.05.00/2020). The authors would like to thank W.W. Purwanto, Y. Muharam, T.S. Utami, A.A. Tanoyo, C. Harfian, D.P. Hallatu, E. Janitra and E. Firmansyah for the helpful suggestions regarding the design.
Publisher Copyright:
© Published under licence by IOP Publishing Ltd.
Copyright:
Copyright 2020 Elsevier B.V., All rights reserved.
PY - 2020/11/24
Y1 - 2020/11/24
N2 - Thermochemical conversion is selected in the design of a rice straw-based bioethanol production plant. This study examines the gasification and catalytic synthetic process technologies of rice straw into ethanol. The size of rice straw was reduced and dried before entering the gasification reactor to convert into syngas. The clean gas goes to the mixed alcohol synthesis process in a plug flow reactor with CuO/ZnO as a catalyst. The product is then purified through several separation methods, i.e., column distillation, stripping, and absorption. The controlled parameters for this plant are temperature, flow rate, pressure, level, and concentration. The paper describes the piping instrumentation diagram with a graphical representation of the equipment, piping, and instrumentation. A Heat Exchanger Network analysis achieves an efficiency of 34.4%. The electricity required is fulfilled by turbine expander for about 1,493 kW, and the rest of it is provided by PLN, besides an emergency generator sets. The capacity of this plant is 100,000 kL/year.
AB - Thermochemical conversion is selected in the design of a rice straw-based bioethanol production plant. This study examines the gasification and catalytic synthetic process technologies of rice straw into ethanol. The size of rice straw was reduced and dried before entering the gasification reactor to convert into syngas. The clean gas goes to the mixed alcohol synthesis process in a plug flow reactor with CuO/ZnO as a catalyst. The product is then purified through several separation methods, i.e., column distillation, stripping, and absorption. The controlled parameters for this plant are temperature, flow rate, pressure, level, and concentration. The paper describes the piping instrumentation diagram with a graphical representation of the equipment, piping, and instrumentation. A Heat Exchanger Network analysis achieves an efficiency of 34.4%. The electricity required is fulfilled by turbine expander for about 1,493 kW, and the rest of it is provided by PLN, besides an emergency generator sets. The capacity of this plant is 100,000 kL/year.
UR - http://www.scopus.com/inward/record.url?scp=85097557532&partnerID=8YFLogxK
U2 - 10.1088/1755-1315/599/1/012004
DO - 10.1088/1755-1315/599/1/012004
M3 - Conference article
AN - SCOPUS:85097557532
SN - 1755-1307
VL - 599
JO - IOP Conference Series: Earth and Environmental Science
JF - IOP Conference Series: Earth and Environmental Science
IS - 1
M1 - 012004
T2 - 2nd International Conference on Green Energy and Environment, ICoGEE 2020
Y2 - 8 October 2020
ER -