Agarose hydrolysis by two-stage enzymatic process and bioethanol production from the hydrolysate

2016 ◽  
Vol 51 (6) ◽  
pp. 759-764 ◽  
Author(s):  
Young Bin Seo ◽  
Juyi Park ◽  
In Young Huh ◽  
Soon-Kwang Hong ◽  
Yong Keun Chang
2010 ◽  
Vol 18 (5) ◽  
pp. 837-842 ◽  
Author(s):  
Fubao SUN ◽  
Zhonggui MAO ◽  
Jianhua ZHANG ◽  
Hongjian ZHANG ◽  
Lei TANG ◽  
...  

2011 ◽  
Vol 48 (2) ◽  
pp. 143-147 ◽  
Author(s):  
Qisi Zhu ◽  
Tie Li ◽  
Yonghua Wang ◽  
Bo Yang ◽  
Yongjun Ma

2014 ◽  
Vol 16 (2) ◽  
pp. 65 ◽  
Author(s):  
Saniha Adini ◽  
Endang Kusdiyantini ◽  
Anto Budiharjo

The Indonesia needs of Bioethanol were 390.000 kL in 2012, but the local ethanol production only able to cover less than 4% from the needed. The high demand of the bioethanol encourage for another innovation in ethanol production more efficient and effectively. Seaweeds and the residual pulp of Gracilaria sp. could be useful as substrate for bioethanol production, because of the high amount of polysaccharide, cellulose and galactan type. Unfortunately, this cellulose and galactan had through the saccharification process first, before they can be used as substrates in bioethanol production. This study examined the difference between two saccharification process which are acid hydrolisis using H2SO4 1% and enzymatic process using Aspergillus niger on the use seaweed and the residual pulp of Gracilaria sp. for bioethanol production. Bioethanol production been conducted for 5 days and in each 24 hour, the sampling for cell number variable, reduction sugar amount variable, and medium fermentation pH variable had been retrieved. The ethanol amount calculation in the last incubation phase conducted using distillate fermentation spesific gravity methode. The highest ethanol was obtained 5,50%  by treatment using seaweed medium with acid hydrolisis. The anova analysis result showed that interaction between medium variable and hydrolisis didn’t have signifficant influence toward ethanol product. It showed that seaweed and the residual pulp of Gracilaria sp. had same quality and they can be useful as main component of bioethanol production which are hydrolisis by enzymatic or acid hydrolisis.   Key Words :  Gracilaria sp., the residual pulp, saccharification, reducing sugar, ethanol


Author(s):  
A B Arif ◽  
A Budiyanto ◽  
W Diyono ◽  
M Hayuningtyas ◽  
T Marwati ◽  
...  

Author(s):  
Kęstutis Venslauskas ◽  
Kęstutis Navickas ◽  
Marja Nappa ◽  
Petteri Kangas ◽  
Revilija Mozūraitytė ◽  
...  

This study evaluates the possibility of recovery of high-quality valuable fish oil and proteins from fish co-streams by traditional means or a combination of several technologies. A techno-economically feasible and sustainable zero-waste process is needed for full utilisation of this co-stream’s potential. This study aims to determine the energy efficiency and economic feasibility of four different zero-waste bio-refineries based on salmon filleting co-streams. The study covers four concepts: (I) biogas and fertiliser production from salmon co-streams, (II) fish silage production, (III) thermal processing of salmon co-streams for producing oil, protein concentrate, and meal, and (IV) novel two-stage thermal and enzymatic process for producing high-quality oil and protein hydrolysate, while the solid residue is converted to biogas and fertilisers. Monte Carlo simulation is used to evaluate uncertainties in economic evaluation. The results show that the two-stage processing of fish co-streams leads to recovery of both high-quality marine oil and proteins, showing the largest profitability and return on investment during the economic analysis. It is a more tempting option than the currently used thermal treatment or traditional silage processes. The possibility of producing food-grade fish protein hydrolysate is the biggest benefit here. Concepts studied are examples of zero-waste processing of bioproducts and illustrate the possibilities and benefits of fully utilising the different fractions of fish as fillets, oil, protein, fertilisers, and energy production.


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