IP Library Granted Patent US 8,658,321
Granted Patent B2
US 8,658,321 · App. 13/681,584 · Granted Feb 25, 2014

Desulfurization system and method for desulfurizing a fuel stream

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Quick Facts
Patent No.
US 8,658,321
App. No.
13/681,584
Granted
Feb 25, 2014
Kind
B2
Abstract

A method for producing a substantially desulfurized a hydrocarbon fuel stream at temperatures less than 100° C. The method includes providing a nondesulfurized fuel cell hydrocarbon fuel stream that may include water and passing the fuel stream sequentially through a zeolite Y adsorbent and a selective sulfur adsorbent. The zeolite Y adsorbent may be exchanged with copper ions. The method produces a substantially desulfurized hydrocarbon fuel stream containing less than 50 ppb sulfur.

Claims (6)

1. A sulfur adsorbent system for use in removing sulfur from a hydrocarbon used in a fuel cell processing train, the sulfur adsorbent system comprising a zeolite Y adsorbent ion exchanged with a cation selected from the group consisting of Cu, Ag, Mn, Mg, Fe, Ca, Ce, La, Sr, Pr, Nd, and mixtures thereof and a selective sulfur adsorbent, wherein the sulfur adsorbent system is configured such that the hydrocarbon sequentially passes through both the zeolite Y adsorbent and then the selective sulfur adsorbent placed together in the sulfur adsorbent system at a temperature below 100° C. and wherein the desulfurization within that sulfur adsorbent system is performed substantially not by chemical desulfurization processes.

2. The sulfur adsorbent system of claim 1 , wherein the zeolite Y comprises a copper exchanged zeolite Y.

3. The sulfur adsorbent system of claim 1 , wherein the selective sulfur adsorbent comprise one or more manganese compounds combined with a metal compound selected from iron compounds, copper compounds, and mixture of iron and copper compounds.

4. The sulfur adsorbent system of claim 1 further comprising controlling the temperature of the feed stream while passing through the zeolite Y adsorbent and the selective sulfur adsorbent to below about 60° C.

5. The sulfur adsorbent system of claim 1 , wherein the hydrocarbon feed stream further comprises water.

6. The sulfur adsorbent system of claim 1 further comprising an inlet for conveying the hydrocarbon containing sulfur to the zeolite Y adsorbent and selective sulfur adsorbent and an outlet for passing a desulfurized hydrocarbon downstream in the fuel cell processing train.

Assignments (3)
CONFIRMATORY DEED OF ASSIGNMENT EFFECTIVE DEC. 31, 2017 Recorded Sep 14, 2021
From: CLARIANT CORPORATION
To: CLARIANT INTERNATIONAL LTD
Reel/Frame 057499/0988 →
MERGER Recorded Jan 8, 2014
From: SUD-CHEMIE INC.
To: CLARIANT CORPORATION
Reel/Frame 031914/0466 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 20, 2012
From: RATNASAMY, CHANDRA; WAGNER, JON P.; SPIVEY, R. STEVE; ANFANG, HANS-GEORG
To: SUD-CHEMIE INC.
Reel/Frame 029326/0914 →