Gas-fed fermentation reactors, systems and processes utilizing gas/liquid separation vessels
Reactors, systems and processes for the production of biomass by culturing microorganisms in aqueous liquid culture medium circulating inner loop reactor which utilize nonvertical pressure reduction zones are described. Recovery and processing of the culture microorganisms to obtain products, such as proteins or hydrocarbons is described.
1. A process for stimulating production of biomass comprising:
flowing through a loop section of a loop reactor, a multi-phase mixture of a gas and a liquid culture medium;
introducing a nutrient into the multi-phase mixture;
flowing the multi-phase mixture of a gas and a liquid culture medium through a substantially vertical upflow zone after flowing the multi-phase mixture through the loop section of a loop reactor;
flowing the multi-phase mixture of a gas and a liquid culture medium from the substantially vertical upflow zone into an inlet side section of a gas/liquid separation vessel of the loop reactor via a bend having a radius of curvature between 0.5 to 3 times a diameter of the vertical upflow zone;
separating the multi-phase mixture of a gas and a liquid culture medium into a gas phase and a liquid phase in the gas/liquid separation vessel by:
flowing the multi-phase mixture of a gas and a liquid culture medium into a lower portion of the gas/liquid separation vessel through the inlet side section of the gas/liquid separation vessel, the inlet side section of the gas/liquid separation vessel having a shape of an oblique conical frustum and having an increasing diameter in a direction of flow of the multi-phase mixture through the inlet side section; and
flowing the multi-phase mixture through an intermediate section located between an outlet side section of the gas/liquid separation vessel and the inlet side section of the gas/liquid separation vessel, the intermediate section having a constant diameter; and
removing the liquid phase from an outlet of the gas/liquid separation vessel and delivering the removed liquid phase to an inlet of the loop section.
2. The process of claim 1 , wherein delivering the removed liquid phase to the inlet of the loop section includes flowing the removed liquid phase through a conduit of non-increasing diameter.
3. The process of claim 1 , wherein separating the multi-phase mixture of a gas and a liquid culture medium into a gas phase and a liquid phase in the gas/liquid separation vessel further comprises flowing the multi-phase mixture through the inlet side section and the intermediate section of the gas/liquid separation vessel, wherein the inlet side section and the intermediate section include a lowermost edge that lie on a common plane.
4. The process of claim 1 , wherein the nutrients include a C 1 compound.
5. The process of claim 4 , wherein the C 1 compound is methane.
6. The process of claim 1 , further comprising flowing the multi-phase mixture of a gas and a liquid culture medium through a substantially vertical downflow zone before flowing the multi-phase mixture through the loop section of a loop reactor.
7. The process of claim 1 , wherein a lowermost edge of each of the intermediate section, the outlet side section and the inlet side section of the gas/liquid separation vessel contact a common plane.
8. The process of claim 1 , wherein flowing the multi-phase mixture of a gas and a liquid culture medium into a lower portion of the gas/liquid separation vessel through the inlet side section of the gas/liquid separation vessel having a shape of an oblique conical frustum includes flowing the multi-phase mixture of a gas and a liquid culture medium through the inlet side section of the gas/liquid separation vessel having a shape of an oblique conical frustum including a cone angle that ranges between 5 to 30°.
9. The process of claim 1 , wherein the gas/liquid separation vessel has a longitudinal axis and the inlet side section has a length L a measured along the longitudinal axis of the gas/liquid separation vessel, L a being greater than a length L i of the intermediate section measured along the longitudinal axis of the gas/liquid separation vessel.
10. The process of claim 9 , wherein the longitudinal axis of the gas/liquid separation vessel includes a horizontal centerline of the intermediate section.
11. The process of claim 1 , wherein the gas/liquid separation vessel includes a longitudinal axis that lies in a horizontal plane.
12. The process of claim 1 , wherein the separating the multi-phase mixture of a gas and a liquid culture medium into a gas phase and a liquid phase in the gas/liquid separation vessel further includes flowing the multi-phase mixture through the inlet side section and the intermediate section and contacting the multi-phase mixture with a flow guide in the inlet side section and the intermediate section.
13. The process of claim 12 , wherein the flow guide is a v-shaped vertical baffle.
14. The process of claim 12 , wherein the flow guide includes two or more vertical baffles.
15. The process of claim 14 , wherein the two are more vertical baffles are two or more parallel vertical baffles.
16. The process of claim 1 , wherein the flowing a multi-phase mixture through a loop section of a loop reactor includes flowing the multi-phase mixture through the loop section having an inner diameter between about 20 cm to 3 meters.
17. The process of claim 1 , further comprising recycling a portion of the gas phase to the loop section.
18. The process of claim 1 , further comprising returning the liquid phase to the gas/liquid separation vessel.
19. The process of claim 1 , wherein pressure within a headspace of the gas/liquid separation vessel ranges from 0.2 to about 0.6 bars.
20. The process of claim 1 , wherein pressure at a beginning of the substantially vertical upflow zone ranges from about 1.0 to about 3.0 bars.
21. The process of claim 1 , wherein pressure at an outlet of the substantially vertical upflow zone ranges from about 0.2 bars to about 0.6 bars.
22. The process of claim 1 , wherein pressure drop across the substantially vertical upflow zone ranges from about 1.0 bars to about 2.3 bars.
23. A process for stimulating production of biomass comprising:
flowing through a substantially horizontal section of a loop reactor, a multi-phase mixture of a gas and a liquid culture medium;
introducing a nutrient into the multi-phase mixture;
flowing the multi-phase mixture of a gas and a liquid culture medium through a substantially vertical upflow zone after flowing the multi-phase mixture through the substantially horizontal section of a loop reactor;
flowing the multi-phase mixture of a gas and a liquid culture medium from the substantially vertical upflow zone into an inlet side section of a gas/liquid separation vessel of the loop reactor via a bend having a radius of curvature between 0.5 to 3 times a diameter of the vertical upflow zone;
separating the multi-phase mixture of a gas and a liquid culture medium into a gas phase and a liquid phase in the gas/liquid separation vessel by:
flowing the multi-phase mixture of a gas and a liquid culture medium into a lower portion of the gas/liquid separation vessel through the inlet side section of the gas/liquid separation vessel, the inlet side section of the gas/liquid separation vessel having a shape of an oblique conical frustum and having an increasing diameter in a direction of flow of the multi-phase mixture through the inlet side section; and
flowing the multi-phase mixture through an intermediate section located between an outlet side section of the gas/liquid separation vessel and the inlet side section of the gas/liquid separation vessel, the intermediate section having a constant diameter; and
removing the liquid phase from an outlet of the gas/liquid separation vessel and delivering the removed liquid phase to an inlet of the substantially horizontal section.
24. The process of claim 23 , wherein delivering the removed liquid phase to the inlet of the substantially horizontal section includes flowing the removed liquid phase through a conduit of non-increasing diameter.
25. The process of claim 23 , wherein flowing the multi-phase mixture of a gas and a liquid culture medium into a lower portion of the gas/liquid separation vessel through an inlet side section of the gas/liquid separation vessel having a shape of an oblique conical frustum includes flowing the multi-phase mixture of a gas and a liquid culture medium through the inlet side section of the gas liquid separation vessel having a shape of an oblique conical frustum including a cone angle that ranges between 5 to 30°.
26. The process of claim 23 , wherein the gas/liquid separation vessel has a longitudinal axis and the inlet side section has a length L a measured along the longitudinal axis of the gas/liquid separation vessel, L a being greater than a length L i of the intermediate section measured along the longitudinal axis of the gas/liquid separation vessel.
27. The process of claim 26 , wherein the ratio of L a /L i is between 0.08 to 0.2.
28. The process of claim 26 , wherein length L i of the intermediate section is between 2 to 8 meters.
29. The process of claim 23 , wherein the flowing the multi-phase mixture through the intermediate section includes flowing the multi-phase mixture through the intermediate section and the intermediate section has a diameter D that is between 2 to 8 meters.
30. The process of claim 23 , wherein the gas/liquid separation vessel includes a longitudinal axis that lies in a horizontal plane.
31. The process of claim 23 , wherein the nutrients include a C 1 compound.
32. The process of claim 23 , wherein the flowing a multi-phase mixture through the substantially horizontal section of the loop reactor includes flowing the multi-phase mixture through the substantially horizontal section of the loop reactor that has a section having a larger cross-sectional area and a section having a smaller cross-sectional area, the larger cross-sectional area being at most three times the smaller cross-sectional area.