IP Library Granted Patent US 8,702,910
Granted Patent B2
US 8,702,910 · App. 12/323,191 · Granted Apr 22, 2014

Multi-stage sulfur removal system and process for a fuel system

Inventors: Kandaswamy Duraiswamy (Huntington Beach, CA); Richard Root Woods (Irvine, CA)
Assignee: Intelligent Energy, Inc.
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Quick Facts
Patent No.
US 8,702,910
App. No.
12/323,191
Granted
Apr 22, 2014
Kind
B2
Abstract

A system for producing an auxiliary fuel stream containing a low concentration of sulfur compounds from a primary fuel stream includes a first separation stage to separate a portion of a primary fuel stream into a first vapor permeate stream and a first retentate stream, a first separation stage partial condenser connected to the first vapor permeate stream condensing a portion of the first vapor permeate stream into a first liquid stage stream and a first vapor stage stream, and a second separation stage partial condenser condensing a portion of the first vapor stage stream into a second liquid stage. The stream may then be processed through a sorbent bed to effectively remove the sulfur compounds.

Claims (25)

1. A system for producing a fuel stream containing a low concentration of undesirable compounds from a primary fuel stream, the system comprising:

a first separation stage to separate a portion of a primary fuel stream into a first vapor permeate stream and a first retentate stream;

a first separation stage partial condenser connected to the first vapor permeate stream condensing a portion of the first vapor permeate stream into a first liquid stage stream and a first vapor stage stream;

a second separation stage partial condenser condensing a portion of the first vapor stage stream into a second liquid stage;

a second separation stage for separating the second liquid stage stream into a second vapor permeate stream and a second retentate stream; and

a mixer to mix the first retentate stream and the second vapor permeate stream and returning the mixture to the primary fuel stream.

2. The system of claim 1 further comprising a polishing filter connected to the second retentate stream.

3. The system of claim 1 , wherein the second separation stage comprises a sulfur selective membrane maintained within a predetermined pervaporation temperature range and a predetermined pervaporation vacuum range operable to pass the second liquid stage stream into a second vapor permeate stream and a second retentate stream.

4. The system of claim 1 further comprising a polishing filter receiving the second stage retentate stream and producing the auxiliary fuel stream therefrom.

5. A system for producing an auxiliary fuel stream containing a low concentration of undesirable compounds from a primary fuel stream, the system comprising:

a first separation stage to separate a portion of a primary fuel stream into a first vapor permeate stream and a first retentate stream;

a first separation stage partial condenser connected to the first vapor permeate stream condensing a portion of the first vapor permeate stream into a first liquid stage stream and a first vapor stage stream;

a second separation stage partial condenser condensing a portion of the first vapor stage stream into a second liquid stage; and

a polishing filter, connected between the first separation stage and the first separation stage partial condenser receiving the first stage permeate vapor, that contains a catalyst to convert the undesirable compounds to sulfides or oxides to increase the selectivity and absorption capacity of the polishing filter.

6. A system for producing an auxiliary fuel stream containing a low concentration of undesirable compounds from a primary fuel stream, the system comprising:

a first separation stage to separate a portion of a primary fuel stream into a first vapor permeate stream and a first retentate stream;

a first separation stage partial condenser connected to the first vapor permeate stream condensing a portion of the first vapor permeate stream into a first liquid stage stream and a first vapor stage stream;

a reactive catalyst reactor receiving the first vapor stage stream; and

a second separation stage partial condenser condensing a portion of the first vapor stage stream from the catalyst reactor into a second liquid stage; and

a second separation stage for separating the second liquid stage stream into a second vapor permeate stream and a second retentate stream; and

a mixer to mix the first retentate stream and the second vapor permeate stream and returning the mixture to the primary fuel stream.

7. The system of claim 6 , further comprising a polishing filter connected to the second liquid stage stream, and wherein effluent liquid from the polishing filter becomes clean fuel.

8. The system of claim 6 wherein the first separation stage comprises a high flux, selective membrane maintained within a predetermined pervaporation temperature range and a predetermined pervaporation vacuum range operable to separate the primary fuel stream into the first vapor permeate stream and the first retentate stream.

9. The system of claim 6 , wherein the temperature of the first partial condenser is controlled to manage the condensing of the portion of the first vapor permeate stream.

10. The system of claim 8 , wherein the temperature of the first partial condenser is controlled to manage condensation of the portion of the first vapor permeate stream.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 22, 2025
From: INTELLIGENT ENERGY, INC.
To: INTELLIGENT ENERGY LIMITED
Reel/Frame 071351/0389 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 28, 2014
From: KANDASWAMY, DURAISWAMY; WOODS, RICHARD ROOT
To: INTELLIGENT ENERGY, INC.
Reel/Frame 032319/0857 →
Continuity (4)
Continuation In Part 11733718 · Apr 10, 2007
Continuation In Part 11345980 · Feb 1, 2006
Provisional Application 60649646 · Feb 2, 2005
Related Publication 20090166264A1 · Jul 2, 2009