logging in or signing up GSE25march2002 Gabrielle Download Post to : URL : Related Presentations : Share Add to Flag Embed Email Send to Blogs and Networks Add to Channel Uploaded from authorPOINTLite Insert YouTube videos in PowerPont slides with aS Desktop Copy embed code: (To copy code, click on the text box) Embed: URL: Thumbnail: WordPress Embed Customize Embed The presentation is successfully added In Your Favorites. Views: 74 Category: Entertainment License: All Rights Reserved Like it (0) Dislike it (0) Added: November 07, 2007 This Presentation is Public Favorites: 0 Presentation Description No description available. Comments Posting comment... Premium member Presentation Transcript TRD Gas System Ground Operations: TRD Gas System Ground Operations Peter Fisher MIT March 25, 2002TRD Gas System: TRD Gas System Plumbing Design - A simplified circuit diagram of the TRD gas system is shown in the following figures - The gas supply system consists of Xe/CO2 in an 80:20 mix Structural Materials - Tanks: Composite over-wrapped stainless steel - Lines and fittings: stainless steel (welded connections)TRD Gas System (Cont): TRD Gas System (Cont) Schematic Arrangement of the AMS-TRD gas system. All pressures are given at 25 C. TRD 300 Liters Manifolds Box C Box S CO2 940 psia 17.6-20.4psia Mixing Vessel 200 psia Xe 1550psiaSlide4: TRD Gas Supply Mounted to USS-02Slide6: Xe Bottle: 1550psia CO2 Bottle 940psia V10a V1a V20a V3a V4b V4a V5 V3b V2a V20b F3a P1a V2b V1b P2b RV3-300psi V10b D Vessel (Mix) F1a O1a 60cc 30cc P1b P2a 7 liters per day to Box C O1b F2a F3b F2b 15cc 30cc VG1a VG1b F1b Figure 2: Box S Diagram RVG1b-1200psi RVG1a-2800psi CO2 Xe Ground Equipment Ground Equipment V17a V17bTRD Gas System (Cont): TRD Gas System (Cont) Ground Equipment Purifier CO2 Analyzer P5 RV4 – 29psig P3 CP2 CP1 V8B V8A RV5-200psig P4 To Manifold From Manifold From Box S (From V4a) From Box S (From V4b) V18a V18b V6b V6a V9a V9bSlide8: TRD Gas System (Cont) TRD segment There are a total of 41 segments fed in parallel from the manifold. TRD Segment n From Gas System To Gas System PMnB PMnA VMnA VMnB VMnC VMnD 430 cu. in (7 liters)TRD Gas System (Cont): TRD Gas System (Cont) Fittings and Connections - All tubes in the TRD gas system are 3 mm or 6 mm outer diameter stainless steel tubes - Connections are made with welded joints (as an alternate metal sealed fittings will be used) - Connections between the gas manifolds and the TRD segments are made with 1 mm inner diameter PEEK tubing and metal connectors TRD Gas System (Cont): TRD Gas System (Cont) Design and Operating Pressures - Xe Tank - Maximum Design Pressure/Maximum Expected Operating Pressure (MDP)/(MEOP) = 3000 psid - Min./Max. design temperature = -60 F to +150 F (-51C to +65C) - Relief valves setting = 2800 psid - Normal Operating Pressure = 1550 psid - Normal Operating Temperature = 77 F (25 C) - Proof test factor = 1.5 x MDP - Minimum burst factor = 3.1 x MDP TRD Gas System (Cont): TRD Gas System (Cont) Design and Operating Pressures (Cont) - Xe Tank (cont) - Outside diameter = 15.37 in. - Volume = 1680 in3 - Tank weight = 17 lbs - Weight of Xenon = 109 lbs (max.) - External load test performed to 8.9 Grms at 0.08 g2/Hz all axes - Material is composite over wrapped stainless steel TRD Gas System (Cont): TRD Gas System (Cont) Design and Operating Pressures (Cont) - CO2 tank - Maximum Design Pressure/Maximum Expected Operating Pressure (MDP)/(MEOP) = 3200 psig - Min./Max. design temperature = -100 F to +300 F (-73 C to +149 C) - Relief valves setting = 1200 psig - Normal Operating Pressure = 940 psid - Normal Operating Temperature = 77 F (25 C) - Proof test factor = 1.5 x MDP - Minimum burst factor = 2.125 x MDP TRD Gas System (Cont): TRD Gas System (Cont) Design and Operating Pressures (Cont) - CO2 Tank (cont) - Outside diameter = 12.42 in. - Volume = 813 in3 - Tank weight = 9.5 lbs - Weight of CO2= 8.5 lbs (max.) - External load test performed to: - 8.9 Grms at 0.07 g2/Hz (axial) - 4.5 Grms at 0.02 g2/Hz (lateral) - Material is composite over wrapped stainless steelTRD Gas System (Cont): TRD Gas System (Cont) Design and Operating Pressures (Cont) - Mixing Tank - Cylindrical Pressure Volume - Maximum Design Pressure/Maximum Expected Operating Pressure (MDP)/(MEOP) = 300 psig - Min./Max. design temperature = -100 F to +300 F (-73 C to +149 C) - Normal Operating Pressure = 200 psia - Normal Operating Temperature = 77 F (25 C) - Proof test factor = 1.5 x MDP - Minimum burst factor = 4.0 x MDP - 1 Liter Volume - Manufactured by ARDE (ARDE SKC 13181)TRD Gas System (Cont): TRD Gas System (Cont) Design and Operating Pressures (Cont) - TRD Straws - Maximum Design Pressure/Maximum Expected Operating Pressure (MDP)/(MEOP) = 29.4 psid - Min./Max. design temperature = TBD - Relief valves setting = 29.4 psid - Normal Operating Pressure = 14.7 to 17.5 psia on orbit; 17.6 to 20.4 psia on ground - Normal Operating Temperature = 77 F (25 C) within +/- 1 C delta temperature throughout entire TRD - Proof test factor = 1.5 x MDP - Minimum burst factor >/= 2.0 x MDP TRD Gas System (Cont): TRD Gas System (Cont) - TRD Straws (cont.) The Xe/CO2 mixture is circulated through these tubes in a continuous loop Each manifold is connected by pressure controlled isolation valves at the inlet and outlet to box C The density and purity of the gas mixture is monitored and corrected to ensure efficient photon detection TRD Gas System (Cont): TRD Gas System (Cont) Pressure System Operations - Box S will be mounted to the USS-02 on the ISS wake side - Box C will be mounted near/on box S as a separate assembly - Tank Design - The Xe tank is already in use on the ISS as the Plasma Contactor Unit (PCU) - The CO2 tank is used on X-33 nitrogen tanks - Stress and fracture analysis on the Xe tank was done by Boeing, Canoga ParkTRD Ground Operations: TRD Ground Operations TRD testing Verify system operation Filling Transfer Xe, CO2 from standard 25 l gas bottles to Box S storage vessels Recovery Trasnfer Xe from Box S to standard 25 l gas bottlesTRD testing: TRD testing Need to fill 350 l TRD straws from standard 25 l bottles for testing Circulate through external filter, remove O2 Recover gas after use Standard procedure, will be carried out many times during constructionSlide20: Recovery System RGA VH2 VH3 PH3 VH4 VH5 VH8 VH6 10 liter Bottle PH4 VH1 VH0 30cc Bottle RVH0 1 liter Bottle 25 liter Bottle PH1 PH0 PH2 Regulator Rotary Vacuum Pump VH7 To box S Sorption pump 2800 psidSlide22: Recovery System Xe in TRD stored in Box S at high pressure - 1550 psia Expensive $10/l Need to be able to Transfer into Box S vessel from standard bottles Recover from Box S vessel to standard bottles Monitor gas composition in detail (Residual Gas Analyzer, RGA) Recovery system operations - filling Box S vessel: Recovery system operations - filling Box S vessel Open standard 25 l bottles to Box S vessel, pressure equilibrates ~1000 psia Seal Box S vessel Condense Xe from 25 l bottle to 10 l bottle, seal 25 l bottle, open to Box S vessel Repeat with 1 liter, 30 cc bottleRecovery system - recovering procedure: Recovery system - recovering procedure Seal TRD straws Open Box S vessel to cold 25 l standard gas bottles Xe condenses Seal storage vesselsTRD Ground Operations Equipment: TRD Ground Operations Equipment Recovery system (as shown) Supply of LN2 Vent/take-away for N2, Xe, CO2 Electrical power Connecting plumbing Standard gas bottles You do not have the permission to view this presentation. In order to view it, please contact the author of the presentation.
GSE25march2002 Gabrielle Download Post to : URL : Related Presentations : Share Add to Flag Embed Email Send to Blogs and Networks Add to Channel Uploaded from authorPOINTLite Insert YouTube videos in PowerPont slides with aS Desktop Copy embed code: (To copy code, click on the text box) Embed: URL: Thumbnail: WordPress Embed Customize Embed The presentation is successfully added In Your Favorites. Views: 74 Category: Entertainment License: All Rights Reserved Like it (0) Dislike it (0) Added: November 07, 2007 This Presentation is Public Favorites: 0 Presentation Description No description available. Comments Posting comment... Premium member Presentation Transcript TRD Gas System Ground Operations: TRD Gas System Ground Operations Peter Fisher MIT March 25, 2002TRD Gas System: TRD Gas System Plumbing Design - A simplified circuit diagram of the TRD gas system is shown in the following figures - The gas supply system consists of Xe/CO2 in an 80:20 mix Structural Materials - Tanks: Composite over-wrapped stainless steel - Lines and fittings: stainless steel (welded connections)TRD Gas System (Cont): TRD Gas System (Cont) Schematic Arrangement of the AMS-TRD gas system. All pressures are given at 25 C. TRD 300 Liters Manifolds Box C Box S CO2 940 psia 17.6-20.4psia Mixing Vessel 200 psia Xe 1550psiaSlide4: TRD Gas Supply Mounted to USS-02Slide6: Xe Bottle: 1550psia CO2 Bottle 940psia V10a V1a V20a V3a V4b V4a V5 V3b V2a V20b F3a P1a V2b V1b P2b RV3-300psi V10b D Vessel (Mix) F1a O1a 60cc 30cc P1b P2a 7 liters per day to Box C O1b F2a F3b F2b 15cc 30cc VG1a VG1b F1b Figure 2: Box S Diagram RVG1b-1200psi RVG1a-2800psi CO2 Xe Ground Equipment Ground Equipment V17a V17bTRD Gas System (Cont): TRD Gas System (Cont) Ground Equipment Purifier CO2 Analyzer P5 RV4 – 29psig P3 CP2 CP1 V8B V8A RV5-200psig P4 To Manifold From Manifold From Box S (From V4a) From Box S (From V4b) V18a V18b V6b V6a V9a V9bSlide8: TRD Gas System (Cont) TRD segment There are a total of 41 segments fed in parallel from the manifold. TRD Segment n From Gas System To Gas System PMnB PMnA VMnA VMnB VMnC VMnD 430 cu. in (7 liters)TRD Gas System (Cont): TRD Gas System (Cont) Fittings and Connections - All tubes in the TRD gas system are 3 mm or 6 mm outer diameter stainless steel tubes - Connections are made with welded joints (as an alternate metal sealed fittings will be used) - Connections between the gas manifolds and the TRD segments are made with 1 mm inner diameter PEEK tubing and metal connectors TRD Gas System (Cont): TRD Gas System (Cont) Design and Operating Pressures - Xe Tank - Maximum Design Pressure/Maximum Expected Operating Pressure (MDP)/(MEOP) = 3000 psid - Min./Max. design temperature = -60 F to +150 F (-51C to +65C) - Relief valves setting = 2800 psid - Normal Operating Pressure = 1550 psid - Normal Operating Temperature = 77 F (25 C) - Proof test factor = 1.5 x MDP - Minimum burst factor = 3.1 x MDP TRD Gas System (Cont): TRD Gas System (Cont) Design and Operating Pressures (Cont) - Xe Tank (cont) - Outside diameter = 15.37 in. - Volume = 1680 in3 - Tank weight = 17 lbs - Weight of Xenon = 109 lbs (max.) - External load test performed to 8.9 Grms at 0.08 g2/Hz all axes - Material is composite over wrapped stainless steel TRD Gas System (Cont): TRD Gas System (Cont) Design and Operating Pressures (Cont) - CO2 tank - Maximum Design Pressure/Maximum Expected Operating Pressure (MDP)/(MEOP) = 3200 psig - Min./Max. design temperature = -100 F to +300 F (-73 C to +149 C) - Relief valves setting = 1200 psig - Normal Operating Pressure = 940 psid - Normal Operating Temperature = 77 F (25 C) - Proof test factor = 1.5 x MDP - Minimum burst factor = 2.125 x MDP TRD Gas System (Cont): TRD Gas System (Cont) Design and Operating Pressures (Cont) - CO2 Tank (cont) - Outside diameter = 12.42 in. - Volume = 813 in3 - Tank weight = 9.5 lbs - Weight of CO2= 8.5 lbs (max.) - External load test performed to: - 8.9 Grms at 0.07 g2/Hz (axial) - 4.5 Grms at 0.02 g2/Hz (lateral) - Material is composite over wrapped stainless steelTRD Gas System (Cont): TRD Gas System (Cont) Design and Operating Pressures (Cont) - Mixing Tank - Cylindrical Pressure Volume - Maximum Design Pressure/Maximum Expected Operating Pressure (MDP)/(MEOP) = 300 psig - Min./Max. design temperature = -100 F to +300 F (-73 C to +149 C) - Normal Operating Pressure = 200 psia - Normal Operating Temperature = 77 F (25 C) - Proof test factor = 1.5 x MDP - Minimum burst factor = 4.0 x MDP - 1 Liter Volume - Manufactured by ARDE (ARDE SKC 13181)TRD Gas System (Cont): TRD Gas System (Cont) Design and Operating Pressures (Cont) - TRD Straws - Maximum Design Pressure/Maximum Expected Operating Pressure (MDP)/(MEOP) = 29.4 psid - Min./Max. design temperature = TBD - Relief valves setting = 29.4 psid - Normal Operating Pressure = 14.7 to 17.5 psia on orbit; 17.6 to 20.4 psia on ground - Normal Operating Temperature = 77 F (25 C) within +/- 1 C delta temperature throughout entire TRD - Proof test factor = 1.5 x MDP - Minimum burst factor >/= 2.0 x MDP TRD Gas System (Cont): TRD Gas System (Cont) - TRD Straws (cont.) The Xe/CO2 mixture is circulated through these tubes in a continuous loop Each manifold is connected by pressure controlled isolation valves at the inlet and outlet to box C The density and purity of the gas mixture is monitored and corrected to ensure efficient photon detection TRD Gas System (Cont): TRD Gas System (Cont) Pressure System Operations - Box S will be mounted to the USS-02 on the ISS wake side - Box C will be mounted near/on box S as a separate assembly - Tank Design - The Xe tank is already in use on the ISS as the Plasma Contactor Unit (PCU) - The CO2 tank is used on X-33 nitrogen tanks - Stress and fracture analysis on the Xe tank was done by Boeing, Canoga ParkTRD Ground Operations: TRD Ground Operations TRD testing Verify system operation Filling Transfer Xe, CO2 from standard 25 l gas bottles to Box S storage vessels Recovery Trasnfer Xe from Box S to standard 25 l gas bottlesTRD testing: TRD testing Need to fill 350 l TRD straws from standard 25 l bottles for testing Circulate through external filter, remove O2 Recover gas after use Standard procedure, will be carried out many times during constructionSlide20: Recovery System RGA VH2 VH3 PH3 VH4 VH5 VH8 VH6 10 liter Bottle PH4 VH1 VH0 30cc Bottle RVH0 1 liter Bottle 25 liter Bottle PH1 PH0 PH2 Regulator Rotary Vacuum Pump VH7 To box S Sorption pump 2800 psidSlide22: Recovery System Xe in TRD stored in Box S at high pressure - 1550 psia Expensive $10/l Need to be able to Transfer into Box S vessel from standard bottles Recover from Box S vessel to standard bottles Monitor gas composition in detail (Residual Gas Analyzer, RGA) Recovery system operations - filling Box S vessel: Recovery system operations - filling Box S vessel Open standard 25 l bottles to Box S vessel, pressure equilibrates ~1000 psia Seal Box S vessel Condense Xe from 25 l bottle to 10 l bottle, seal 25 l bottle, open to Box S vessel Repeat with 1 liter, 30 cc bottleRecovery system - recovering procedure: Recovery system - recovering procedure Seal TRD straws Open Box S vessel to cold 25 l standard gas bottles Xe condenses Seal storage vesselsTRD Ground Operations Equipment: TRD Ground Operations Equipment Recovery system (as shown) Supply of LN2 Vent/take-away for N2, Xe, CO2 Electrical power Connecting plumbing Standard gas bottles