IP Library Granted Patent US 8,657,921
Granted Patent B2
US 8,657,921 · App. 13/318,048 · Granted Feb 25, 2014

Shell and tube heat exchanger and method for removing volatile substances from a polymer solution

Inventors: Norbert Güntherberg (Speyer, DE); Rainer Bardon (Dannstadt-Schauernheim, DE); Hartmut Heinen (Ludwigshafen, DE); Michael Sauer (Hockenheim, DE); Ludger Leber (Dannstadt-Schauernheim, DE); Wolfgang Fischer (Walldorf, DE)
Assignee: Styrolution GmbH
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Quick Facts
Patent No.
US 8,657,921
App. No.
13/318,048
Granted
Feb 25, 2014
Kind
B2
Abstract

A shell-and-tube heat exchanger, for removing volatile substances from a polymer solution by degasification, includes a bundle of tubes arranged vertically and parallel to each other in a shell chamber through which a fluid heat-transfer medium flows. The upper end of each tube is fixed in an upper tube sheet and the lower end of each tube is fixed in a lower tube sheet, and the polymer solution flows through the tubes in the direction of gravity. One feature is that a multilayer woven wire fabric is attached to the top of the upper tube sheet. The finest meshed layer of the fabric has a mesh width of 50 μm to 1000 μm. The invention also relates to a method for removing volatile substances from a polymer solution by degasification in a shell-and-tube heat exchanger and use of the shell-and-tube heat exchanger.

Claims (14)

1. A shell-and-tube heat exchanger for removing volatile substances from a polymer solution by degassing, comprising:

a bundle of parallel vertical tubes arranged within a shell through which a fluid heat transfer medium flows, wherein each tube is fixed at its upper end in an upper tube plate and fixed at its lower end in a lower tube plate and wherein the polymer solution to be degassed flows through the tubes in the direction of gravity, and wherein a multilayer woven wire mesh comprises a finest-meshed layer with a mesh opening ranging from 50 μm to 1000 μm is installed on an upper side of the upper tube plate.

2. The shell-and-tube heat exchanger according to claim 1 , wherein the multilayer woven wire mesh further comprises a support layer having a mesh opening of from 1 mm to 15 mm and one or more further layers of which the finest-meshed layer has a mesh opening of from 50 μm to 1000 μm.

3. The shell-and-tube heat exchanger according to claim 1 , further comprising one or more additional layers each having a finest-meshed layer with a mesh opening of from 50 μm to 1000 μm.

4. The shell-and-tube heat exchanger according to claim 1 , wherein the finest-meshed layer of the multilayer woven wire mesh faces away from the upper tube plate.

5. The shell-and-tube heat exchanger according to claim 1 , wherein the tubes are provided with inlet nozzles and internal fittings for reducing the free cross section of the tubes.

6. The shell-and-tube heat exchanger according to claim 1 , wherein the tubes are provided with internal fittings for reducing the free cross section of the tubes.

7. The shell-and-tube heat exchanger according to claim 1 , wherein the tubes are provided with internal fittings for reducing the free cross section of the tubes.

8. The shell-and-tube heat exchanger according to claim 1 , wherein a perforated plate or a distributor plate is installed between the upper tube plate and the multilayer woven wire mesh.

9. A method of removing volatile substances from a polymer solution, comprising

providing a shell-and-tube heat exchanger according to claim 1 , wherein the shell-and-tube heat exchanger comprises a bundle of parallel vertical tubes within a shell through which a fluid heat transfer medium flows, wherein each vertical tube is fixed at its upper end in an upper tube plate and at its lower end in a lower tube plate;

flowing of polymer solution to be degassed through the vertical tubes in the direction of gravity; and

degassing the polymer solution by reducing the pressure and introducing heat within the vertical tubes.

10. The method according to claim 9 , further comprising removing remaining volatile substances from the polymer solution in a continuous degasser after degassing of the polymer solution in the shell-and-tube heat exchanger.

Assignments (4)
FIRST LIEN INTELLECTUAL PROPERTY SECURITY AGREEMENT Recorded Apr 30, 2021
From: INEOS STYROLUTION EUROPE GMBH
To: HSBC CORPORATE TRUSTEE COMPANY (UK) LIMITED
Reel/Frame 056103/0160 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 24, 2014
From: BASF SE; STYROLUTION GMBH
To: STYROLUTION EUROPE GMBH
Reel/Frame 034700/0165 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 4, 2013
From: BASF SE
To: STYROLUTION GMBH
Reel/Frame 031535/0349 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 26, 2012
From: GUNTHERBERG, NORBERT; BARDON, RAINER; HEINEN, HARTMUT; SAUER, MICHAEL; LEBER, LUDGER; FISCHER, WOLFGANG
To: BASF SE
Reel/Frame 027597/0886 →
Priority Claims (1)
EP 09159012 · Apr 29, 2009 · regional
Continuity (1)
Related Publication 20120132406A1 · May 31, 2012