This application claims priority from Taiwan Patent Application No. 098136802, filed in the Taiwan Patent Office on Oct. 30, 2009, and incorporates the Taiwan patent application in its entirety by reference.
This present disclosure relates to increase the ethanol concentration from the conversion the lignocelluloses. In particular, it related to a designed process for integrating the C5 sugar fermentation and the cellulose-to-ethanol process under an operative mode of simultaneous saccharification and fermentation process (SSF). It is efficient for increasing the final ethanol concentration in the broth of fermentor.
Increasing the consumption of petroleum has results in the necessity for developing novel liquid biofuel. Among them, the Bioethanol has been considered as one of the most significant liquid biofuel, which could be blend with gasoline to reduce the use of fossil fuel and then decrease the emission of CO2 and air pollutants.
Today, bioethanol is almost produced via fermentation process. According to the source of feedstock, the bioethanol is classified starch-based, cane sugar-based, and cellulosic ethanol. The feedstock of starch-based and cane sugar-based ethanol is mainly obtained from grain and sugarcane. The cellulosic ethanol is made from composition of cellulose and hemicelluloses in plant and agricultural waste. It is important to note that bioethanol from grain or sugarcane is usually considered to be very practicable and the process could give high ethanol concentration in broth due high ethanol concentration produced. However, the lignocellulosic materials have shown the advantages of low cost, diverse and no competition with food crops. Consequently, lignocellulosic material is potentially considered as the feedstock for bioethanol production.
The cellulosic ethanol process is related to a heterogeneous reaction between solid and liquid phase. If increasing the solid content in process, the high solid content often make the delivery and agitation of pretreated solid residues difficult. The poor substrate fluidity usually results in the mass transfer limitation, and then causes the conversion efficiency to be decreased as well as the sugar concentration produced in process. Therefore, the cellulosic ethanol concentration from the broth of fermentation process is generally lower than that in cane sugar-based and starch-based process. When the broth with low ethanol concentration is purified to hydrous ethanol concentration by distillation, the energy consumption of distillation will be greatly increased. Thus, the ethanol concentration in broth is generally proposed to be above 4% for reducing the energy consumption of ethanol distillation.
The lignocellulosic feedstock is mainly composed of 60%˜80% cellulose and hemicelluloses and 15-25% lignin. The hemicelluloses first converted to pentose by pretreatment process, and then the mono-sugar released could be fermented into ethanol. For pretreatment technologies of hemicelluloses hydrolysis, the thermal chemical pretreatment such as dilute acid hydrolysis and acid-catalyzed steam hydrolysis is usually used in cellulosic ethanol process. During these pretreatment technologies, constant solid and liquid content is mixed with 1˜3% (w/w) diluted sulfuric acid under high temperature and pressure conditions. The liquid is called hydrolysate after pretreatment reaction. The fermentation inhibitors such as furfural, hydroxylmethyl furfural (HMF) or organic acid is produced along as the release of xylose. These inhibitors often show toxic and inhibitive to fermented organism and further reduce the ethanol productivity. Therefore, the furfural of hydrolysate from pretreatment reaction is often removed by overliming process. Then the detoxified hydrolysate is available to be fermented by organism.
After the pretreatment, the solid residues which contain long chain cellulose is needed to be hydrolyzed to monosugar (C6H10O5)n+nH2O→nC6H12O6) by dilute acid, concentrated acid or enzyme. Now, usage of celluase for hydrolysis of cellulose is a major tendency. Traditionally, the biochemical process of cellulose-to-ethanol could be: (1) separate/sequential hydrolysis and fermentation (SHF), as shown in
The main purpose of the present disclosure is to provide a method to increase lignocellosic ethanol concentration in broth. The pretreated solid residues are mixed with ethanol-containing broth from the fermentation of xylose hydrolysate and then performed under the process of simultaneous saccharification and fermentation (SSF) for converting cellulose to ethanol.
The second purpose of the present disclosure is to obtain a final ethanol concentration above 4% (w/w) or at least 1.8 times in comparison of that from traditional SHF process.
The third purpose of the present disclosure is to reduce 50% usage of water in the fermentation process by replacing water with ethanol broth from xylose fermentation.
To achieve the above purposes, the present disclosure is a method to increase lignocellosic ethanol concentration in broth, comprising steps of: (a) obtaining a xylose hydrolysate and a solid residue from the pretreatment of lignocellulosic materials; (b) the ethanol-containing broth is obtained from the fermentation of the xylose hydrolysate by adding Pichia Stipitis; and (c) mixing the broth from xylose fermentation with the solid residue is performed under the simultaneous saccharification and fermentation (SSF) process by adding Saccharomyces Cerevisiae and cellulase.
The present disclosure will be better understood from the following detailed description of the preferred embodiment according to the present disclosure, taken in conjunction with the accompanying drawings, in which
The following description of the preferred embodiment is provided to understand the features and the structures of the present disclosure.
Under the present disclosure, the xylose hydrolysate and pretreted solid residuse which was used in all examples with rice straw by dilute acid steam explsion pretreatment method. The xylose hydrolysate was dealt with overliming method to remove furfural and then was fermented by Pichia stipitis in 5 L fermentor. The fermentaion was controlled in 30° C. at pH6 with 100 rpm agition. The incoulation ratio is 1:5(v/v) (incoulted volume:fermention volume).
Number | Date | Country | Kind |
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098136802 | Oct 2009 | TW | national |