Biomass pretreatment process
The process for the treatment of ligno-cellulosic biomass comprises the steps of: A) Soaking a ligno-cellulosic biomass feedstock in vapor or liquid water or mixture thereof in the temperature range of 100 to 210° C. for 1 minute to 24 hours to create a soaked biomass containing a dry content and a first liquid; B) Separating at least a portion of the first liquid from the soaked biomass to create a first liquid stream and a first solid stream; wherein the first solid stream comprises the soaked biomass; and C) Steam exploding the first solid stream to create a steam exploded stream comprising solids and a second liquid.
1. A process for the treatment of ligno-cellulosic biomass comprising the steps of:
A) soaking a ligno-cellulosic biomass feedstock in a low temperature soaking step in a liquid comprised of water at a temperature in the range of 25 to 100° C. for 1 minute to 24 hours and the low temperature soaking step is followed by a separation step to separate at least a portion of the liquid from the low temperature soaked ligno-cellulosic biomass;
B) soaking a lingo-cellulosic biomass feedstock in vapor or liquid water or mixture thereof in the temperature range of 145 to 165° C. for a time within the range selected from the group consisting of 1 minute to 24 hours, 1 minute to 6 hours, 1 minute to 4 hours, 1 minute to 3 hours, 1 minute to 2.5 hours, and 1 minute to 2.0 hours to create a soaked biomass containing a dry content and a first liquid;
C) separating at least a portion of the first liquid from the soaked biomass to create a first liquid stream and a first solid stream; wherein the first solid stream comprises the soaked biomass;
D) steam exploding the first solid stream to create a steam exploded stream comprising solids and a second liquid;
E) washing the steam exploded stream with at least a third liquid to create a third liquid stream;
F) purifying the third liquid stream to create a second purified liquid stream by removing at least a portion of at least one inhibitor selected from the group consisting of acetic acid, formic acid, levulinic acid, furfural, 5-HMF and phenolic compounds; and
G) combining the second purified liquid stream with at least a portion of the steam exploded stream.
2. The process according to claim 1 , wherein the combination of the second purified liquid stream with at least a portion of the steam exploded stream is done after at least a portion of the steam exploded stream has been hydrolyzed.
3. The process according to claim 1 , wherein the process comprises a further step of combining at least a portion of the liquid of the first liquid stream with at least a portion of the steam exploded stream.
4. The process according to claim 3 , wherein the combination of the liquid of the first liquid stream with at least a portion of the steam exploded stream is done after at least a portion of the steam exploded stream has been hydrolyzed.
5. A process for the treatment of ligno-cellulosic biomass comprising the steps of:
A) soaking a ligno-cellulosic biomass feedstock in a low temperature soaking step in a liquid comprised of water at a temperature in the range of 25 to 100° C. for 1 minute to 24 hours and the low temperature soaking step is followed by a separation step to separate at least a portion of the liquid from the low temperature soaked ligno-cellulosic biomass;
B) soaking a lingo-cellulosic biomass feedstock in vapor or liquid water or mixture thereof in the temperature range of 145 to 165° C. for a time within the range selected from the group consisting of 1 minute to 24 hours, 1 minute to 6 hours, 1 minute to 4 hours, 1 minute to 3 hours, 1 minute to 2.5 hours, and 1 minute to 2.0 hours to create a soaked biomass containing a dry content and a first liquid;
C) separating at least a portion of the first liquid from the soaked biomass to create a first liquid stream and a first solid stream; wherein the first solid stream comprises the soaked biomass;
D) steam exploding the first solid stream to create a steam exploded stream comprising solids and a second liquid;
E) combining at least a portion of the liquid of the first liquid stream with at least a portion of the steam exploded stream; and
F) purifying the first liquid stream to create a first purified liquid stream by removing at least a portion of at least one inhibitor selected from the group consisting of acetic acid, formic acid, levulinic acid, furfural, 5-HMF and phenolic compounds prior to combining the first liquid stream with at least a portion of the steam exploded stream.
6. The process according to claim 5 , wherein the combining with at least a portion of the steam exploded stream is done after at least a portion of the steam exploded stream has been hydrolyzed.
7. The process according to claim 5 , wherein the process comprises a further step of combining at least a portion of the liquid of the first liquid stream with at least a portion of the steam exploded stream.
8. The process according to claim 7 , wherein the combination of the first liquid stream with at least a portion of the steam exploded stream is done after at least a portion of the steam exploded stream has been hydrolyzed.
9. A process for the treatment of ligno-cellulosic biomass comprising the steps of:
A) soaking a ligno-cellulosic biomass feedstock in a low temperature soaking step in a liquid comprised of water at a temperature in the range of 25 to 100° C. for 1 minute to 24 hours and the low temperature soaking step is followed by a separation step to separate at least a portion of the liquid from the low temperature soaked ligno-cellulosic biomass;
B) soaking a lingo-cellulosic biomass feedstock in vapor or liquid water or mixture thereof in the temperature range of 145 to 165° C. for a time within the range selected from the group consisting of 1 minute to 24 hours, 1 minute to 6 hours, 1 minute to 4 hours, 1 minute to 3 hours, 1 minute to 2.5 hours, and 1 minute to 2.0 hours to create a soaked biomass containing a dry content and a first liquid;
C) separating at least a portion of the first liquid from the soaked biomass to create a first liquid stream and a first solid stream; wherein the first solid stream comprises the soaked biomass;
D) steam exploding the first solid stream to create a steam exploded stream comprising solids and a second liquid wherein at least some of the second liquid in the steam exploded stream is separated from the steam exploded stream to create a second liquid stream;
E) combining at least a portion of the liquid of the first liquid stream with at least a portion of the steam exploded stream; and
F) purifying the first liquid stream to create a first purified liquid stream by removing at least a portion of at least one inhibitor selected from the group consisting of acetic acid, formic acid, levulinic acid, furfural, 5-HMF and phenolic compounds prior to combining the first liquid stream with at least a portion of the steam exploded stream.
10. The process according to claim 9 , wherein the combination of the first liquid stream with at least a portion of the steam exploded stream is done after at least a portion of the steam exploded stream has been hydrolyzed.
11. The process according to claim 9 , wherein the steam exploded stream is washed with at least a third liquid to create a third liquid stream.
12. The process according to claim 11 , wherein the third liquid stream is purified and then combined with at least a portion of the steam exploded stream.
13. The process according to claim 12 , wherein the combination of the third liquid stream with at least a portion of the steam exploded stream is done after at least a portion of the steam exploded stream has been hydrolyzed.