Process for producing a bio-product
It is disclosed a process for producing a bio-product from a ligno-cellulosic biomass, wherein the ligno-cellulosic biomass, a gas and steam are introduced in a pressurized reactor operated in a continuous manner at conditions to have a vapor head space. In the pressurized reactor, the vapor head space is maintained at a vapor head space temperature and at a pressure which is at least 1 bar greater than a pure steam equilibrium pressure at the vapor head space temperature. The ligno-cellulosic biomass is then refined by rapidly releasing the pressure while discharging the ligno-cellulosic biomass from the pressurized reactor assembly to create a pre-treated ligno-cellulosic biomass, which is then hydrolyzed and converted to the bio-product. Preferably, at least a portion of the gas is air entrapped in the ligno-cellulosic biomass and it is introduced into the pressurized reactor as part of the ligno-cellulosic biomass. In a preferred embodiment, the lignocellulosic biomass is subjected to a soaking step and an aeration step prior to being introduced into the pressurized reactor, without any xylans separation step.
1. A process for producing a bio-product from a ligno-cellulosic biomass comprised of a total amount of xylans, a total amount of glucans, a total amount of lignin, and water, wherein the process comprises the steps of:
a. introducing the ligno-cellulosic biomass, a total amount of gas, and steam into a pressurized reactor of a pressurized reactor assembly operated in a continuous manner at conditions to have a vapor head space in the pressurized reactor, wherein a portion of the steam condenses on the ligno-cellulosic biomass within the pressurized reactor;
b. maintaining the ligno-cellulosic biomass in the pressurized reactor at a ligno-cellulosic biomass pressure greater than 10 bar for a residence time from 0.5 minutes to 120 minutes, at a vapor head space temperature in a range of 130° C. to 230° C., wherein the ligno-cellulosic biomass pressure is at least 1 bar greater than a pure steam equilibrium pressure at the vapor head space temperature;
c. refining the ligno-cellulosic biomass by rapidly releasing the ligno-cellulosic biomass pressure while discharging the ligno-cellulosic biomass from the pressurized reactor assembly to create a pre-treated ligno-cellulosic biomass;
d. hydrolyzing at least a portion of the glucans to an amount of glucose; and
e. converting at least a portion of the amount of glucose to the bio-product.
2. The process of claim 1 , wherein the ligno-cellulosic biomass further comprises an entrapped air, and at least a portion of the gas is entrapped air introduced into the pressurized reactor as part of the ligno-cellulosic biomass.
3. The process of claim 1 , wherein the process further comprises a xylans separation step, wherein less than 15% of the total amount of xylans are separated from the ligno-cellulosic biomass prior to introduction into the pressurized reactor.
4. The process of claim 2 , wherein the process further comprises a xylans separation step, wherein less than 15% of the total amount of xylans are separated from the ligno-cellulosic biomass prior to introduction into the pressurized reactor.
5. The process of claim 1 , wherein the process does not comprise a xylans separation step prior to introduction into the pressurized reactor.
6. The process of claim 2 , wherein the process does not comprise a xylans separation step prior to introduction into the pressurized reactor.
7. The process of claim 1 , wherein the process further comprises a soaking step, wherein the ligno-cellulosic biomass is soaked in a liquid comprised of water prior to introducing the ligno-cellulosic biomass into the pressurized reactor.
8. The process of claim 2 , wherein the process further comprises a soaking step, wherein the ligno-cellulosic biomass is soaked in a liquid comprised of water prior to introducing the ligno-cellulosic biomass into the pressurized reactor.
9. The process of claim 3 , wherein the process further comprises a soaking step, wherein the ligno-cellulosic biomass is soaked in a liquid comprised of water prior to introducing the ligno-cellulosic biomass into the pressurized reactor.
10. The process of claim 5 , wherein the process further comprises a soaking step, wherein the ligno-cellulosic biomass is soaked in a liquid comprised of water prior to introducing the ligno-cellulosic biomass into the pressurized reactor.
11. The process of claim 7 , wherein the process further comprises an aeration step, wherein the ligno-cellulosic biomass is aerated after the soaking step by exposing the ligno-cellulosic biomass to air.
12. The process of claim 8 , wherein the process further comprises an aeration step, wherein the ligno-cellulosic biomass is aerated after the soaking step by exposing the ligno-cellulosic biomass to air.
13. The process of claim 9 , wherein the process further comprises an aeration step, wherein the ligno-cellulosic biomass is aerated after the soaking step by exposing the ligno-cellulosic biomass to air.
14. The process of claim 10 , wherein the process further comprises an aeration step, wherein the ligno-cellulosic biomass is aerated after the soaking step by exposing the ligno-cellulosic biomass to air.
15. The process of claim 1 , wherein the ligno-cellulosic biomass is compressed at a compression temperature in a range of 25° C. to less than 100° C. prior to introducing the ligno-cellulosic biomass into the pressurized reactor.
16. The process of claim 1 , wherein the pressurized reactor has a pressurized reactor volume and the vapor head space has a vapor head space volume which is between 5% and 80% of the pressurized reactor volume.
17. The process of claim 1 , wherein the ligno-cellulosic biomass pressure is selected so that the refining step steam explodes the ligno-cellulosic biomass.
18. The process of claim 1 , wherein the vapor head space temperature and the residence time are controlled so that more than 65% of the total amount of xylans are recovered in the pre-treated ligno-cellulosic biomass.
19. The process of claim 1 , wherein the ligno-cellulosic biomass pressure is controlled so that the pre-treated ligno-cellulosic biomass comprises an amount of accessible glucans and the amount of accessible glucans in the pre-treated ligno-cellulosic biomass relative to the total amount of glucans in the pre-treated ligno-cellulosic biomass is greater than 80%.