IP Library Granted Patent US 11,198,093
Granted Patent B2
US 11,198,093 · App. 16/331,162 · Granted Dec 14, 2021

Method for cleaning viscose production off-gases and catalysts for use in the method

Inventors: Niklas Bengt Jakobsson (Kågeröd, SE); Peter Bo Olsen (Hørsholm, DK); Per Aggerholm Sørensen (Kgs. Lyngby, DK); Anders Theilgaard Madsen (Copenhagen S, DK)
Assignee: HALDOR TOPSØE A/S
B01D53/8612B01D53/002B01D53/04B01D53/501B01D53/75B01J21/08B01J23/22C01B17/0426C01B17/0434C01B17/56D01F13/02B01D2251/304B01D2251/404B01D2251/604B01D2251/606B01D2253/102B01D2255/207B01D2255/209B01D2255/2027B01D2255/20723B01D2255/30B01D2257/30B01D2257/304Y02P70/62
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Quick Facts
Patent No.
US 11,198,093
App. No.
16/331,162
Granted
Dec 14, 2021
Kind
B2
Abstract

A method for cleaning an off-gas from viscose production, essentially containing H 2 S and CS 2 , comprises passing the gas through a catalytic reactor containing a direct oxidation type catalyst, such as V 2 O 5 on silica, to convert H 2 S in the gas to elemental sulfur, SO 2 or mixtures thereof, either via the oxygen present in the gas or via oxygen added to the gas stream. Elemental sulfur and SO 2 are removed from the effluent gas from the catalytic reactor, and the unconverted CS 2 is recycled to the viscose production process.

Claims (9)

1. A method for cleaning off-gases from viscose production, said off-gases containing air and sulfur components, including H 2 S and CS 2 , comprising:

passing the off-gas through a catalytic reactor containing a direct oxidation type catalyst to convert H 2 S in the off-gas to elemental sulfur and SO 2 , either via oxygen present in the gas or via oxygen added to the gas stream,

removing elemental sulfur and SO 2 from the effluent gas from the catalytic reactor, and

recycling an amount of unconverted CS 2 to the viscose production process,

wherein the elemental sulfur is removed in a condenser and the SO 2 is removed in a caustic scrubber.

2. The method according to claim 1 , wherein the CS 2 is absorbed and concentrated in a regenerative activated carbon filter downstream from the caustic scrubber, and the absorbed CS 2 is desorbed and returned as a raw material to a viscose production plant.

3. The method according to claim 2 , wherein the absorbed CS 2 is desorbed and returned, optionally after being upconcentrated, as a raw material to the viscose production plant.

4. The method according to claim 1 , wherein the off-gas from viscose production contains H 2 S in a concentration of 200 to 2000 ppm and CS 2 in a concentration of 200 to 1000 ppm.

5. The method according to claim 1 , wherein the operation temperature of the catalytic reactor is in the range from 100 to 300° C.

Assignments (2)
CHANGE OF NAME Recorded Oct 30, 2023
From: HALDOR TOPSØE A/S
To: TOPSOE A/S
Reel/Frame 065565/0685 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 28, 2019
From: JAKOBSSON, NIKLAS BENGT; OLSEN, PETER BO; SØRENSEN, PER AGGERHOLM; MADSEN, ANDERS THEILGAARD
To: HALDOR TOPSØE A/S
Reel/Frame 049289/0605 →
Priority Claims (1)
DK PA 2016 00593 · Oct 6, 2016 · national
Continuity (1)
Related Publication 20190255484A1 · Aug 22, 2019