IP Library Granted Patent US 9,393,537
Granted Patent B2
US 9,393,537 · App. 14/810,807 · Granted Jul 19, 2016

Jet loop reactor having nanofiltration

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Quick Facts
Patent No.
US 9,393,537
App. No.
14/810,807
Granted
Jul 19, 2016
Kind
B2
Abstract

The invention relates to a device for the continuous, homogeneous-catalysis reaction of a liquid with a gas and optionally an additional fluid, wherein the device comprises at least one reactor having an external liquid circulation driven by a pump, and wherein the device has at least one membrane separation stage that preferably holds back the homogeneous catalyst. The aim of the invention is to specify a device that allows homogeneous-catalysis gas/liquid phase reactions, in particular hydroformylations, which operate with membrane separation of the catalyst to be performed economically at an industrially relevant scale. Said aim is achieved in that a jet loop reactor is provided as the reactor, and that the pump and the membrane separation stage are arranged in the same external liquid circuit.

Claims (32)

1. A device, comprising:

a reactor having a pump-driven external liquid circuit; and

a membrane separation stage configured to retain a homogeneous catalyst,

wherein

the reactor is a jet loop reactor,

the pump and membrane separation stage are configured in the same external liquid circuit, and

a permeate-side free volume is in the membrane separation stage, wherein a free volume is at least 0.3 dm 3 per m 2 of a membrane surface.

2. The device of claim 1 ,

wherein

the pump is equipped structurally long-term pumping of fluids which comprise liquid and gaseous phases.

3. The device of claim 2 ,

wherein

the pump is a peripheral impeller pump.

4. The device of claim 1 , wherein a permeate-side gas discharge is configured downstream of the membrane separation stage.

5. The device of claim 1 ,

wherein

a heat exchanger adapted for heating or cooling a feed or a permeate of the membrane separation stage is arranged in the external liquid circuit.

6. The device of claim 1 ,

wherein

a tubular reaction space extends in the jet loop reactor, into which a jet nozzle adapted for injecting liquid into the reaction space and a suction tube adapted for extracting gas by suction both open out, and on which is a baffle plate-shielded takeoff adapted for the external liquid circuit.

7. The device of claim 1 , wherein a bypass conduit which is arranged in the external liquid circuit is parallel to the jet loop reactor or to the membrane separation stage.

8. The device of claim 1 ,

comprising

a multiplicity of jet loop reactors that are connectable in parallel and have a shared external liquid circuit, wherein the membrane separation stage is arranged within the shared external liquid circuit.

9. The device of claim 8 ,

wherein

the membrane separation stage comprises a multiplicity of membranes that are connectable in parallel in such a manner that an entire active membrane surface area of the membrane separation stage is adjustable by connecting and disconnecting the membranes.

10. The device of claim 1 , wherein the device is suitable for carrying out a homogeneous-catalytic reaction.

11. The device of claim 1 , wherein a heat exchanger adapted for heating or cooling a teed or a permeate of the membrane separation stage is arranged in the external liquid circuit, upstream of the membrane separation stage.

12. The device of claim 1 , wherein the free volume is at least 0.5 dm 3 per m 2 of a membrane surface.

13. The device of claim 1 , wherein the membrane separation stage comprises at least one membrane having a molecular weight cutoff in the range of 150 g/mol to less than 1000 g/mol.

14. The device of claim 13 , wherein the free volume is at least 0.5 dm 3 per m 2 of a membrane surface.

Assignments (2)
CONFIRMATORY ASSIGNMENT Recorded Nov 6, 2023
From: EVONIK OPERATIONS GMBH
To: EVONIK OXENO GMBH & CO. KG
Reel/Frame 065463/0144 →
CHANGE OF NAME Recorded Jan 31, 2020
From: EVONIK DEGUSSA GMBH
To: EVONIK OPERATIONS GMBH
Reel/Frame 051765/0166 →