Process for the continuous production of cellulases by a filamentous fungus using a carbon substrate obtained from an acid pretreatment
US-9249402-B2 · Feb 2, 2016 · US
US11242549B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11242549-B2 |
| Application number | US-202016785599-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 8, 2020 |
| Priority date | Apr 17, 2019 |
| Publication date | Feb 8, 2022 |
| Grant date | Feb 8, 2022 |
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The present invention relates to a method for obtaining a high titer of enzyme mixture comprising cellulases, hemicellulases and β-glucosidases in reutilization of waste water generated during hot water extraction of lignocellulosic biomass or biorefinery waste water using Penicillium funiculosum MRJ-16 mutant strain. The cellulose or lignocellulosic biomass used in the fermentation process is selected from the group consisting of rice straw, wheat straw, corn stover, cotton stalk or a combination thereof. The enzyme mixture obtained by the present process is used for the saccharification of acid pretreated lignocellulosic biomass.
Opening claim text (preview).
We claim: 1. A method for obtaining an enzyme mixture comprising cellulases, hemicellulases and beta-glucosidases in re-utilization of waste water, the method comprising the steps of: (a) preparing fermentation media comprising 3-5 g/L ammonium sulfate, 4-6 g/L KH 2 PO 4 , 0.5-1 g/L MgSO 4 -7H 2 O, 2.5-5 g/L CaCO 3 , 2-3 g/L glycerol, 25-35 g/L corn steep solids, 25-40 g/L carbon source, 1-2 ml/L polysorbate 80, and waste water obtained during pre-treatment of lignocellulosic biomass or biorefinery waste water; (b) inoculating the media of step (a) with a liquid seed culture of Penicillium funiculosum MRJ-16 of Microbial Type Culture Collection (MTCC) Accession Number 25142; (c) fermenting the Penicillium funiculosum MRJ-16 culture of step (b) in an aerated fermenter; and (d) harvesting an enzyme mixture after centrifuging the fermented culture broth of step (c). 2. The method as claimed in claim 1 , wherein the waste water comprises waxes, proteins, phenolics and inhibitors. 3. The method as claimed in claim 2 , wherein the inhibitors in the waste water are organic acid, phenol, hydroxyl methyl furfural (HMF), formic acid, acetic acid and furfural. 4. The method as claimed in claim 1 , wherein the carbon source in the fermentation media of step (a) is selected from the group consisting of cellulose, acid pretreated lignocellulosic biomass, and a combination thereof. 5. The method as claimed in claim 1 , wherein the fermentation process is carried out at a temperature in the range of 25-35° C., pH in the range of 4-6, aeration in the range of 0.5-2.5 WM, and dissolved oxygen above 30%. 6. The method as claimed in claim 1 , wherein the fermentation is carried out for a time period of 80-110 hours. 7. The method as claimed in claim 4 , wherein the cellulose or lignocellulosic biomass is selected from the group consisting of rice straw, wheat straw, corn stover, cotton stalk, and a combination thereof. 8. The method as claimed in claim 1 , wherein the enzyme mixture obtained is used for the saccharification of acid pretreated lignocellulosic biomass.
produced by the action of a carbohydrase {(EC 3.2.x)}, e.g. by alpha-amylase {, e.g. by cellulase, hemicellulase} · CPC title
having a known sequence of two or more amino acids, e.g. glutathione · CPC title
Fungi isolates · CPC title
produced by the action of an alpha-1, 6-glucosidase, e.g. amylose, debranched amylopectin (non-biological hydrolysis of starch C08B30/00) · CPC title
Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis · CPC title
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