Method and apparatus for conversion of cellulosic material to ethanol
The present invention provides an apparatus and a method for conversion of cellulosic material, such as chopped straw and corn stover, and household waste, to ethanol and other products. The cellulosic material is subjected to continuous hydrothermal pre-treatment without addition of chemicals, and a liquid and a fiber fraction are produced. The fiber fraction is subjected to enzymatic liquefaction and saccharification. The method of the present invention comprises: performing the hydrothermal pre-treatment by subjecting the cellulosic material to at least one soaking operation, and conveying the cellulosic material through at least one pressurized reactor, and subjecting the cellulosic material to at least one pressing operation, creating a fiber fraction and a liquid fraction; selecting the temperature and residence time for the hydrothermal pretreatment, so that the fibrous structure of the feedstock is maintained and at least 80% of the lignin is maintained in the fiber fraction.
1. A method of continuous hydrothermal pretreatment of lignocellulosic biomass feedstock having an amount of lignin comprising:
(i). soaking of the lignocellulosic biomass feedstock having said amount of lignin in acetic acid containing liquid from a subsequent step of the hydrothermal pretreatment, followed by
(ii) continuous hydrothermal pretreatment within a pressurized pretreatment reactor at temperatures between 170 and 200° C.,
wherein the feedstock is cereal straw, corn stover or bagasse,
wherein, following soaking and pretreatment, the pretreated feedstock is subsequently subject to at least one pressing operation while it is still under pressure or after it has been unloaded from the pretreatment reactor to create a fibre fraction and a liquid fraction,
wherein temperature and residence time for hydrothermal pretreatment within the pretreatment reactor are selected at lower severity than that required for pretreatments that seek maximal removal of hemicellulose from the fibre fraction such that greater than 80% of said lignin amount remains in the fibre fraction following the at least one pressing operation,
further characterized in that the fibre fraction having greater than 80% of said lignin amount obtained following the at least one pressing operation is subsequently subject to enzymatic saccharification.
2. The method of claim 1 wherein saccharification is followed by fermentation.
3. The method of claim 1 wherein saccharification is conducted using a separate liquefaction step followed by simultaneous saccharification and fermentation.
4. The method of claim 1 wherein the feedstock is wheat straw.
5. The method of claim 1 further characterized by SSF of the liquefied fibre fraction to produce ethanol.
6. A method of continuous hydrothermal pretreatment of lignocellulosic biomass feedstock having an amount of lignin comprising:
(i). soaking of the lignocellulosic material having said amount of lignin, followed by
(ii). continuous pressurized hydrothermal pretreatment within a pressurized pretreatment reactor at temperatures between 170 and 200° C.,
wherein the feedstock is cereal straw, corn stover or bagasse,
wherein hydrothermal pretreatment is conducted without addition of acids, bases or other chemicals,
wherein, following soaking and pretreatment, the pretreated feedstock is subsequently subject to at least one pressing operation while it is still under pressure or after it has been unloaded from the pretreatment reactor to create a fibre fraction and a liquid fraction, and
wherein temperature and residence time for hydrothermal pretreatment within the pretreatment reactor are selected at lower severity than that required for pretreatments that seek maximal removal of hemicellulose from the fibre fraction such that greater than 80% of the said lignin remains in the fibre fraction following the at least one pressing operation,
further characterized in that the fibre fraction having greater than 80% of said lignin amount following the at least one pressing operation is subsequently subject to enzymatic saccharification.
7. The method of claim 6 wherein saccharification is followed by fermentation.
8. The method of claim 6 wherein saccharification is conducted using a separate liquefaction step followed by simultaneous saccharification and fermentation.
9. The method of claim 6 wherein the feedstock is wheat straw.