IP Library Granted Patent US 8,383,050
Granted Patent B2
US 8,383,050 · App. 12/892,449 · Granted Feb 26, 2013

Device and method for pressure and flow control in parallel reactors

Inventors: Alfred Haas (Eppelheim, DE); Wolfgang Strehlau (Dossenheim, DE); Armin Brenner (Eppelheim, DE); Oliver Koechel (Bubenheim, DE); Markus Friess (Lindenberg, DE); Torsten Zech (Heidelberg, DE)
Assignee: HTE AG
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 8,383,050
App. No.
12/892,449
Granted
Feb 26, 2013
Kind
B2
Abstract

A method and a device for the parallel study of chemical reactions in at least two spatially separated reaction spaces is provided. A device for the parallel study of chemical reactions includes at least the following components: (a) at least two spatially separated reaction spaces; (b) on the reaction space input side, at least one common educt feed for the reaction spaces according to (a); (d) on the reaction space output side, at least one connection per reaction space to at least one holding gas feed common to all the reaction spaces, or subsets of them; (e) on the reaction space output side, and downstream of the connection to the holding gas feed according to (d) in the product flow direction, at least one restrictor per reaction space.

Claims (31)

1. A method for the controlled discharge of product fluid out of a high pressure end separation unit that is part of a device for the processing or testing of at least one chemical reaction, comprising at least the following steps:

(i) opening of a discharge valve triggered by the signal of a level sensor in at least one separation unit;

(ii) discharging of the product fluid from the at least one separation unit, via said discharge valve, into at least one collecting area;

(iii) closing of said discharge valve, triggered by a signal corresponding to a change in pressure and/or a change in fluid flow; and

(iv) directing gaseous product flow through the collecting area.

2. The method according to claim 1 , wherein the gaseous product from the high pressure end separation unit is directed into the low pressure end separation unit by means of a dip pipe or a tube.

3. The method according to claim 1 , wherein the gaseous product coming from the low pressure end separation unit is directed to an analysis system.

4. A device for the processing or testing of at least one chemical reaction, comprising at least one unit for the controlled discharge of product fluid out of at least one high pressure end fluid separation unit, wherein said fluid separation unit is in fluid connection, via a discharge valve, with a collecting area that is at a lower pressure than the high pressure fluid separation unit, wherein the device comprises the following components:

(a) at least two spatially separated reaction spaces;

(b) on the reaction space input side, at least one common educt feed for the reaction spaces according to (a), or for subsets of them;

(c) on the reaction space output side, at least one connection per reaction space to at least one holding gas feed common to all the reaction spaces, or subsets of them; and

(d) on the reaction space output side, and downstream of the connection to the holding gas feed according to (c) in the product flow direction, at least one restrictor per reaction space.

5. The device according to claim 4 , wherein the volume of each of the reaction spaces is in the range of from 0.1 ml to 50 ml.

6. The device according to claim 4 , wherein the reaction spaces are designed as reaction channels, and each of them has an inset for holding solids.

7. The device according to claim 4 , wherein the common holding gas feed comprises at least the following components:

(i) at least one supply unit for the holding gas,

(ii) at least one flow meter,

(iii) at least one pressure controller.

8. The device according to claim 4 , wherein all or subsets of the reaction spaces are connected via a connection, which is hermetic up to at least 20 bar, to a holding gas feed common to all the reaction spaces, or subsets of them.

9. The device according to claim 4 , wherein the common control fluid feed comprises at least the following components:

(i) at least one supply unit for the control fluid,

(ii) at least one mass flow controller,

(iii) downstream, relative to the flow direction of the control fluid, of the mass flow controller, one restrictor per connection of the control fluid feed to the reaction spaces.

10. The device according to claim 4 , wherein the connections intended to lead from the control fluid feed to the reaction spaces are brought together at a node/mixing point with the connections attached to the reaction spaces on the reaction space output side for discharging the products.

11. The device according to claim 10 , wherein the nodes/mixing points for feeding the control fluid are downstream, relative to the flow direction of the control fluid, of the restrictors of the control fluid feed, and also upstream, relative to the flow direction of the product/products, of the restrictors on the reaction space output side.

12. A device for the processing or testing of at least one chemical reaction, comprising at least one unit for the controlled discharge of product fluid out of at least one high pressure end fluid separation unit, wherein said fluid separation unit is in fluid connection, via a discharge valve, with a collecting area that is at a lower pressure than the high pressure fluid separation unit, wherein the device comprises the following components:

(a) at least two spatially separated reaction spaces;

(b) on the reaction space input side, at least one common educt feed for the reaction spaces according to (a), or for subsets of them;

(c) on the reaction space output side, at least one connection per reaction space to at least one holding gas feed common to all the reaction spaces;

(d) on the reaction space output side, at least one connection per reaction space to at least one control fluid feed common to all the reaction spaces; and

(e) on the reaction space output side, and downstream of the connection to the holding gas feed according to (c) and the connection to the control fluid feed according to (d) in the product flow direction, at least one restrictor per reaction space.

Assignments (2)
CHANGE OF NAME Recorded Sep 16, 2014
From: HTE AG
To: HTE GMBH THE HIGH THROUGHPUT EXPERIMENTATION COMPANY
Reel/Frame 033753/0685 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 25, 2012
From: HAAS, ALFRED; STREHLAU, WOLFGANG; BRENNER, ARMIN; KOECHEL, OLIVER; FRIESS, MARKUS; ZECH, TORSTEN
To: HTE AG
Reel/Frame 029192/0645 →
Continuity (3)
Division 12424744 · Apr 16, 2009
Division 10583753
Related Publication 20110014718A1 · Jan 20, 2011