Feed control in conversion of biomass into hydrocarbon fuels and chemicals
The present disclosure relates to processes for producing hydrocarbon fuels from lignocellulosic biomass. A process may include introducing biomass to a pretreatment system, and a first separation system forming a pentose-rich stream and a pentose-lean stream. The pentose-lean stream may be introduced to a hydrolysis system forming a hydrolysate and the hydrolysate introduced to a second separation system forming a hexose-rich stream and a lignin stream. Additionally, at least one of the pentose-rich stream or the hexose-rich stream may be introduced to a bioreactor containing microorganisms configured to produce hydrocarbon fuels. Additionally, the present disclosure also relates to systems for the production of hydrocarbon fuels. A system may include a pretreatment system, a first separation system, a hydrolysis system, a second separation system, and one or more bioreactors. Alternatively a system may include a pretreatment system, a hydrolysis system, a sugar separation system, and one or more bioreactors.
1. A process for producing hydrocarbon fuels from lignocellulosic biomass, the process comprising:
introducing biomass to a pretreatment system to form a pretreatment effluent;
introducing the pretreatment effluent to a hydrolysis system to form a hydrolysate;
introducing the hydrolysate to a sugar separation system to form a pentose-rich stream, a hexose-rich stream, and a lignin stream;
introducing the pentose-rich stream to a first bioreactor containing first microorganisms configured to produce hydrocarbon fuels;
introducing the hexose-rich stream to a second bioreactor containing second microorganisms configured to produce hydrocarbon fuels, the second microorganisms being the same or different than the first microorganisms, an initial feed rate of the pentose-rich stream to the first bioreactor being different than an initial feed rate of the hexose-rich stream to the second bioreactor;
adjusting the initial feed rate of the pentose-rich stream to the first bioreactor with increase of time on stream; and
adjusting the initial feed rate of the hexose-rich stream to the second bioreactor with increase of time on stream.
2. The process of claim 1 , further comprising concentrating the pentose-rich stream to a sugar concentration of 40 wt % to 60 wt %.
3. The process of claim 1 , further comprising concentrating the hexose-rich stream to a sugar concentration of 40 wt % to 60 wt %.
4. The process of claim 1 , further comprising purifying the pentose-rich stream.
5. The process of claim 1 , further comprising purifying the hexose-rich stream.
6. The process of claim 1 , wherein the microorganisms are configured to produce the hydrocarbon fuels by converting pentose or hexose into a fatty acid ester, wherein the hydrocarbon fuels comprise at least one of fatty acid methyl ester or fatty acid ethyl ester.
7. The process of claim 1 , wherein introducing at least one pentose-rich-stream or the hexose-rich stream to the bioreactor comprises introducing the pentose-rich stream to the bioreactor at an initial rate higher than an initial rate of introducing the hexose-rich stream to the bioreactor.
8. The process of claim 1 , wherein introducing the at least one of the pentose-rich stream or the hexose-rich stream to a bioreactor comprises introducing the hexose-rich stream at a rate that increases with increase of time on stream.
9. The process of claim 1 , wherein introducing the at least one of the pentose-rich stream or the hexose-rich stream to a bioreactor comprises introducing the pentose-rich stream at a rate that declines with increase of time on stream.