Process simulation of bio-ethanol production from empty fruit bunch via acid hydrolysis pretreatment

2018 ◽  
Author(s):  
L.K. Bhullar ◽  
Z.A. Putra ◽  
M.R. Bilad ◽  
N.A. Hadi ◽  
M.D. Hakim
Keyword(s):  
Ethanol Production ◽  
Acid Hydrolysis ◽  
Process Simulation ◽  
Empty Fruit Bunch

Optimization studies on acid hydrolysis of oil palm empty fruit bunch fiber for production of xylose

2007 ◽  
Vol 98 (3) ◽  
pp. 554-559 ◽  
Author(s):  
S.H.A. Rahman ◽  
J.P. Choudhury ◽  
A.L. Ahmad ◽  
A.H. Kamaruddin
Keyword(s):  
Acid Hydrolysis ◽  
Oil Palm ◽  
Empty Fruit Bunch ◽  
Hydrolysis Of

Process Simulation and Economic Analysis of Rhamnolipid Production by Pseudomonas aeruginosa Using Oil Palm Empty Fruit Bunch as Substrate

2021 ◽  
Vol 104 ◽  
pp. 103-112
Author(s):  
Andrea Gilang Fauzi ◽  
Cut Nanda Sari ◽  
Andre Fahriz Perdana Harahap ◽  
Muhammad Yusuf Arya Ramadhan ◽  
Misri Gozan
Keyword(s):  
Pseudomonas Aeruginosa ◽  
Oil Palm ◽  
Process Simulation ◽  
Production Cost ◽  
Economic Assessment ◽  
Industrial Applications ◽  
Empty Fruit Bunch ◽  
Rhamnolipid Production ◽  
Surfactant Production ◽  
Purification Methods

Surfactants are amphiphilic molecules that have been used in widely used as emulsifier and cleaning agent in various industries. These broad industrial applications made the global surfactant production increased annually. In 2020, the amount of global surfactant production estimated would reach more than 24 million per year. However, the currently used surfactants are synthetically produced from chemical or petroleum-derived products, so it is often toxic and non-biodegradable. Rhamnolipids are “surfactant like” molecules produced by Pseudomonas aeruginosa, which could be alternatives for more environmentally friendly surfactants. The use of rhamnolipids is quite limited due to its expensive production cost. The production cost of rhamnolipid could be reduced using by agro-industrial by-product as a substrate. One of the abundant agro-industrial by-products in Indonesia that can be used as a substrate for rhamnolipid production is Oil Palm Empty Fruit Bunch (OPEFB). This study employed SuperPro Designer v9.5 to performed process simulation and economic assessment of rhamnolipid production using OPEFB as a substrate through two different purification methods, which are solvent extraction and chromatography adsorption. Based on the process simulation that has been done, the process that used adsorption chromatography purification methods more efficient in terms of the usage of the feedstock and energy. The economic assessment also showed that these methods were more profitable and economically attractive, with the value of NPV 11.400.000 USD, IRR 11,64%, and Payback Period 6,21 years.

scholarly journals Acid hydrolysis optimization of cocoa pod shell using response surface methodology approach toward ethanol production

2018 ◽  
Vol 52 (6) ◽  
pp. 581-587
Author(s):  
Vinayaka B. Shet ◽  
Nisha sanil ◽  
Manasa Bhat ◽  
Manasa Naik ◽  
Leah Natasha Mascarenhas ◽  
...  
Keyword(s):  
Response Surface Methodology ◽  
Ethanol Production ◽  
Acid Hydrolysis ◽  
Response Surface

scholarly journals Techno-Economic Implications of Fed-Batch Enzymatic Hydrolysis

Processes ◽  
2019 ◽  
Vol 7 (11) ◽  
pp. 847 ◽  
Author(s):  
Ellen Argo ◽  
Deepak R. Keshwani
Keyword(s):  
Enzymatic Hydrolysis ◽  
Ethanol Production ◽  
Process Simulation ◽  
Cellulosic Ethanol ◽  
Production Cost ◽  
Simulation Software ◽  
Labor Costs ◽  
Fed Batch ◽  
Capital Costs ◽  
Plant Capacity

Fed-batch enzymatic hydrolysis has the potential to improve the overall process of converting cellulosic biomass into ethanol. This paper utilizes a process simulation approach to identify and quantify techno-economic differences between batch and fed-batch enzymatic hydrolysis in cellulosic ethanol production. The entire process of converting corn stover into ethanol was simulated using SuperPro Designer simulation software. The analysis was conducted for a plant capacity of 2000 metric tons of dry biomass per day. A literature review was used to identify baseline parameters for the process. The sensitivity of the ethanol production cost to changes in sugar conversion efficiency, plant capacity, biomass cost, power cost, labor cost, and enzyme cost was evaluated using the process simulation. For the base scenario, the ethanol unit production cost was approximately $0.10/gallon lower for fed-batch hydrolysis. The greatest differences were seen in facilities costs, labor costs, and capital costs. Using a fed-batch operation decreased facilities costs by 41%, labor costs by 21%, and capital costs by 15%. The sensitivity analysis found that cost of biomass had the greatest effect on ethanol production cost, and in general, the results support the proposition that fed-batch enzymatic hydrolysis does improve the techno-economics of cellulosic ethanol production.

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