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in publisher: "CrystaTech, Inc. United States"  
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Hybrid Sulfur Recovery Process for Natural Gas Upgrading Quarterly Report

Description: This first quarter report of 2001 describes progress on a project funded by the U.S. Department of Energy (DOE) to test a hybrid sulfur recovery process for natural gas upgrading. The process concept represents a low cost option for direct treatment of natural gas streams to remove H{sub 2}S in quantities equivalent to 0.2-25 metric tons (LT) of sulfur per day. This process is projected to have lower capital and operating costs than the competing technologies, amine/aqueous iron liquid redox an… more
Date: August 2001
Creator: Srinivas, Girish; Gebhard, Steven C. & DeBerry, David W.
Item Type: Refine your search to only Report
Partner: UNT Libraries Government Documents Department
open access

Hybrid Sulfur Recovery Process for Natural Gas Upgrading Quarterly Report

Description: This fourth quarter report of 2002 describes progress on a project funded by the U.S. Department of Energy (DOE) to test a hybrid sulfur recovery process for natural gas upgrading. The process concept represents a low cost option for direct treatment of natural gas streams to remove H{sub 2}S in quantities equivalent to 0.2-25 metric tons (LT) of sulfur per day. This process is projected to have lower capital and operating costs than the competing technologies, amine/aqueous iron liquid redox a… more
Date: January 2003
Creator: Lundeen, Joe; Srinivas, Girish & DeBerry, David W.
Item Type: Refine your search to only Report
Partner: UNT Libraries Government Documents Department
open access

Hybrid Sulfur Recovery Process for Natural Gas Upgrading Quarterly Report

Description: This first quarter report of 2004 describes progress on a project funded by the U.S. Department of Energy (DOE) to test a hybrid sulfur recovery process for natural gas upgrading. The process concept represents a low-cost option for direct treatment of natural gas streams to remove H{sub 2}S in quantities equivalent to 0.2-25 metric tons (LT) of sulfur per day. This process is projected to have lower capital and operating costs than the competing technologies, amine/aqueous iron liquid redox an… more
Date: April 2004
Creator: Dalrymple, Dennis
Item Type: Refine your search to only Report
Partner: UNT Libraries Government Documents Department
open access

Hybrid Sulfur Recovery Process for Natural Gas Upgrading Quarterly Report

Description: This second quarter report of 2002 describes progress on a project funded by the U.S. Department of Energy (DOE) to test a hybrid sulfur recovery process for natural gas upgrading. The process concept represents a low cost option for direct treatment of natural gas streams to remove H{sub 2}S in quantities equivalent to 0.2-25 metric tons (LT) of sulfur per day. This process is projected to have lower capital and operating costs than the competing technologies, amine/aqueous iron liquid redox a… more
Date: July 2002
Creator: Srinivas, Girish; Gebhard, Steven C. & DeBerry, David W.
Item Type: Refine your search to only Report
Partner: UNT Libraries Government Documents Department
open access

Hybrid Sulfur Recovery Process for Natural Gas Upgrading Quarterly Report

Description: This third quarter report of 2003 describes progress on a project funded by the U.S. Department of Energy (DOE) to test a hybrid sulfur recovery process for natural gas upgrading. The process concept represents a low-cost option for direct treatment of natural gas streams to remove H{sub 2}S in quantities equivalent to 0.2-25 metric tons (LT) of sulfur per day. This process is projected to have lower capital and operating costs than the competing technologies, amine/aqueous iron liquid redox an… more
Date: October 2003
Creator: Dalrymple, Dennis
Item Type: Refine your search to only Report
Partner: UNT Libraries Government Documents Department
open access

Hybrid Sulfur Recovery Process for Natural Gas Upgrading Quarterly Report

Description: This second quarter report of 2003 describes progress on a project funded by the U.S. Department of Energy (DOE) to test a hybrid sulfur recovery process for natural gas upgrading. The process concept represents a low cost option for direct treatment of natural gas streams to remove H{sub 2}S in quantities equivalent to 0.2-25 metric tons (LT) of sulfur per day. This process is projected to have lower capital and operating costs than the competing technologies, amine/aqueous iron liquid redox a… more
Date: July 2003
Creator: Dalrymple, Dennis
Item Type: Refine your search to only Report
Partner: UNT Libraries Government Documents Department
open access

Hybrid Sulfur Recovery Process for Natural Gas Upgrading Quarterly Report

Description: This final report describes the objectives, technical approach, results and conclusions for a project funded by the U.S. Department of Energy to test a hybrid sulfur recovery process for natural gas upgrading. The process concept is a configuration of CrystaTech, Inc.'s CrystaSulf{reg_sign} process which utilizes a direct oxidation catalyst upstream of the absorber tower to oxidize a portion of the inlet hydrogen sulfide (H{sub 2}S) to sulfur dioxide (SO{sub 2}) and elemental sulfur. This hybri… more
Date: June 2004
Creator: Dalrymple, Dennis
Item Type: Refine your search to only Report
Partner: UNT Libraries Government Documents Department
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