Method and apparatus for in situ product recovery

Patent metadata

Field	Value
Publication number	US-12023630-B2
Application number	US-202218046305-A
Country	US
Kind code	B2
Filing date	Oct 13, 2022
Priority date	Sep 5, 2017
Publication date	Jul 2, 2024
Grant date	Jul 2, 2024

Abstract

A method of obtaining a compound may include adding a substrate to a medium in a reactor, and reacting the substrate in the reactor to form the compound. A first stream is separated from the reaction liquid through a first membrane. A second stream is separated from the reaction liquid through a second membrane. The first membrane is a filtration membrane and the second membrane is configured for liquid-gas or liquid-liquid extraction The first membrane and the second membrane are at least partially immersed in the medium and are moved relative to the reactor during the separation steps.

First claim

The invention claimed is:

1. An apparatus, comprising:
a reactor, comprising a first reactor vessel, a substrate supply, a first outlet and a second outlet,
a filtration unit comprising a first membrane having a first surface communicating with the first reactor vessel and a second surface, opposite the first surface, communicating with the first outlet, and
a liquid-liquid or liquid-gas extraction unit comprising a second membrane having a third surface communicating with the first reactor vessel and a fourth surface, opposite the third surface, communicating with the second outlet,
wherein the liquid-liquid or liquid-gas extraction unit is configured to apply a pressure difference between the third surface and the fourth surface, comprising applying a partial vacuum at the fourth surface, such that a liquid compound from the first reactor vessel is recovered through a corresponding vapor at the fourth surface,
wherein the first membrane and the second membrane are arranged inside the first reactor vessel,
wherein the first membrane and the second membrane are arranged to move relative to the first reactor vessel, and
wherein the first membrane is a microfiltration, ultrafiltration, or nanofiltration membrane, and the second membrane is a membrane for pervaporation or liquid-liquid extraction.

2. The apparatus of claim 1 , wherein the pressure difference is a first pressure difference, and the filtration unit is configured to apply a second pressure difference between the first surface and the second surface, the second pressure difference being configured to generate a permeate flow from the first surface to the second surface.

3. The apparatus of claim 1 , comprising a first support frame and a second support frame associated with the first membrane and the second membrane respectively, wherein the first and second support frames are pivotally arranged relative to the first reactor vessel.

4. The apparatus of claim 3 , wherein the first membrane and the second membrane are fixedly attached to the respective first and second support frame.

5. The apparatus of claim 3 , comprising:
a pair of pivot axes fixedly arranged to the first reactor vessel, wherein the first and second support frames are configured to turn on a respective one of the pivot axes.

6. The apparatus of claim 3 , comprising:
a common pivot axis fixedly arranged to the first reactor vessel, wherein the first and second support frames are configured to turn on the common pivot axis.

7. The apparatus of claim 1 , wherein the first membrane and the second membrane are configured to turn on respective pivot axes relative to the reactor, wherein the respective pivot axes are each arranged in a fixed position relative to the reactor.

8. The apparatus of claim 1 , wherein the first membrane and the second membrane are configured to turn on a common pivot axis relative to the reactor, wherein the common pivot axis is arranged in a fixed position relative to the reactor.

9. The apparatus of claim 1 , comprising a third membrane unit arranged in the first reactor vessel, wherein the third membrane unit is configured to operate as a membrane contactor.

10. The apparatus of claim 9 , wherein the third membrane unit is configured to operate at a partial vacuum pressure between 75 mbar and 500 mbar at a permeate side of a membrane of the third membrane unit.

11. The apparatus of claim 9 , wherein the third membrane unit comprises a vacuum pump and a condenser downstream of the vacuum pump.

12. The apparatus of claim 9 , wherein the third membrane unit comprises membranes arranged on a support frame, wherein the support frame is arranged pivotally relative to the first reactor vessel.

13. The apparatus of claim 9 , wherein the third membrane unit comprises membranes arranged on a support frame, wherein the support frame is arranged fixed relative to the first reactor vessel.

14. The apparatus of claim 13 , wherein the third membrane unit is configured as a filtration unit, a liquid-liquid extraction unit or a liquid-gas extraction unit.

15. The apparatus of claim 1 , wherein the reactor comprises a second reactor vessel arranged downstream of the first reactor vessel and a further membrane unit arranged in the second reactor vessel.

16. An apparatus, comprising:
a reactor, comprising a first reactor vessel, a substrate supply, a first outlet and a second outlet;
a filtration unit comprising a first membrane having a first surface communicating with the first reactor vessel and a second surface, opposite the first surface, communicating with the first outlet; and
a liquid-liquid or liquid-gas extraction unit comprising a second membrane having a third surface communicating with the first reactor vessel and a fourth surface, opposite the third surface, communicating with the second outlet;
wherein the liquid-liquid or liquid-gas extraction unit is configured to apply a first pressure difference between the third surface and the fourth surface, comprising applying a partial vacuum at the fourth surface, such that a liquid compound from the first reactor vessel is recovered through a corresponding vapor at the fourth surface;
wherein the first membrane and the second membrane are arranged inside the first reactor vessel, and the first membrane and the second membrane are arranged to move relative to the first reactor vessel;
wherein the filtration unit is configured to apply a second pressure difference between the first surface and the second surface, the second pressure difference being configured to generate a permeate flow from the first surface to the second surface; and
wherein the first pressure difference is different than the second pressure difference.

Assignees

• Vito Nv

Inventors

• Van Hecke Wouter
• Elslander Helmut
• Vanbroekhoven Karolien
• De Wever Helene
• Beckers Herman

Classifications

• B01D61/3621

  comprising multiple pervaporation steps · CPC title

• C12M47/10

  Separation or concentration of fermentation products (bioreactors combined with means for distillation or extraction of liquid fuel C12M43/02) · CPC title

• C12M29/04

  Filters; Permeable or porous membranes or plates, e.g. dialysis · CPC title

• B01D2325/10

  Catalysts being present on the surface of the membrane or in the pores · CPC title

• B01D2319/06

  Use of membranes of different materials or properties within one module · CPC title