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TRD Gas System TIM Report

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Minimum burst factor = 3.1 x MDP. Peter Fisher. May 8,2002. 22 ... Minimum burst factor = 4.0 x MDP - 1 Liter Volume - Manufactured by ARDE (ARDE SKC 13181) ... – PowerPoint PPT presentation

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Title: TRD Gas System TIM Report


1
TRD Gas System TIM Report
  • Peter Fisher
  • MIT
  • May 8, 2002

2
TRD Gas System
Box S
Manifolds
TRD 300 Liters
Box C
Xe 1550psia
Mixing Vessel 200 psia
17.6-20.4psia
CO2 940 psia
Schematic Arrangement of the AMS-TRD gas
system. All pressures are given at 25 C.
3
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
    8020 mix
  • Structural Materials
  • - Tanks Composite over-wrapped stainless steel
  • - Lines and fittings stainless steel (welded
    connections)

4
Outline
  • Mechanical layout
  • C. Gargiulo
  • J. Burger (manifolds)
  • Electrical layout and signals
  • A. Bartoloni (this session)
  • Components
  • Operations
  • R.Henning (slow control session)

5
TDR Gas System-Mechanical
  • Box S/C are a single unit
  • Mount on wake port side
  • Design stabilized
  • Layout from Robert Becker
  • Finite element calculation from Corrado
  • Magnetic field tolerable

6
TRD Gas Supply Mounted to USS-02
7
Box S Component Layout
Vacuum case
Box C
8
Figure 2 Box S Diagram  
Xe
 
 
VG1a
RVG1a-2800psi
Ground Equipment
V17a
 
F3a
V1a
 
V3a
V2a
F2a
O1a
Xe Bottle 1550psia
P2a
F1a
60cc
30cc
V10a
V4a
O2a
V5
P1a
7 liters per day to Box C
V20a
 
RV3-300psi
O2b
V4b
V20b
V10b
D Vessel (Mix)

F1b
CO2 Bottle 940psia
 
O1b
V3b
V2b
30cc
F2b
15cc
V1b
F3b
P2b
V17b
P1b
Ground Equipment
RVG1b-1200psi
VG1b
CO2
9
TRD Gas System (Cont)
RV4 29psig
P5
P3
To Manifold
CO2 Analyzer
Ground Equipment
CP2
CP1
V9a
Purifier
V8B
V8A
From Manifold
V6b
V6a
V9b
V18a
V18b
P4
RV5-200psig
From Box S (From V4a)
From Box S (From V4b)
10
Magnetic Field at Gas System
Xe
Vacuum case
CO2
C
Marotta Valves
11
TRD Gas System (Cont)
VMnA
VMnB
VMnC
VMnD
TRD Segment n
From Gas System
To Gas System
430 cu. in (7 liters)
PMnB
PMnA
TRD segment There are a total of 41 segments fed
in parallel from the manifold.
12
TRD Gas System - Mechanical
  • Fittings and Connections
  • - All tubes in the TRD gas system are 1/8, 1/4
    or 1/2 outer diameter stainless steel tubes
  • - Connections are made with welded joints (as
    an alternate 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

13
TDR Gas System - Electrical
  • Controls to Box S, C and manifolds via USCM
  • All inputs, outputs and readouts have been
    specified
  • Electrical simulator for Box S constructed
  • Design by Rome (Borgia, Gentile and Bartolini) -
    separate talk

14
Box S Signals and Power
15
Box S Electronic Simulator
16
Box C Electrical Signals
Three GlenAir connectors 21-pin power 9-pin
high current 25-pin signal
24 V supply still unresolved!!
17
Box S Pinout
18
TRD Gas System Components
  • Box S
  • Composite overwrapped pressure vessels (COVP)
  • High pressure valves
  • GP-50 (gyppie fifty) pressure sensors
  • Box C
  • Pumps

19
Box S Component List
20
Arde Vessels
21
TRD Gas System - Components
  • 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

22
TRD Gas System Components
  • 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

23
TRD Gas System Components
  • 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

24
Xe Vessel During Assembly
25
TRD Gas System Components
  • Design and Operating Pressures (Cont)
  • - CO2 Tank (cont)
  • - Outside diameter 12.42 in.
  • - Volume 813 in3
  • - Tank weight 9.5 lbs
  • - Weight of CO2 11 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
    steel

26
TRD Gas System Components
  • 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)

27
CO2 Vessel Prior to Overwrap
28
Marotta MV197
  • At storage tanks - 3200 psi
  • Inline valves - does not leak out
  • Based on MV100 design - same drivers
  • Space qualified??

29
Box C Components List
30
Pumps
  • KNF NMP30 Brushless DC 24 V pump
  • Positive displacement - works in microgravity
  • Rated for 15,000 hours at full power
  • 30,000 hours (3.4 y) at half power
  • Weak point- bearings - failure does not break gas
    integrity
  • Two years under test at CERN

31
Pumps
  • 1.4 l/h across 3 psi gives 3 TRD volumes/day
  • Tested in magnetic field, OK up to 500 G
  • Enclosed in vessel to maintain integrity, reduce
    wear

32
Gas system test setup
33
Test system Results
1
0.8 psi
  • 11 automated filling cycles
  • Mix in Box S, transfer to C, monitor for 45
    minutes
  • 1 pressure stability

Pressure (psia)
Time (h)
34
CO2 Concentration test
35
Component testing
  • Marotta valves, GP-50 sensors under acceptance
    test
  • Pumps
  • on going long duration test
  • vibration test next month at Aachen or MIT
  • Magnetic field

36
MV100 Test 1 Doc
37
GP50 testing
  • Temperature compensated pressure readings
  • Three kinds 0-25psi, 0-300psi and 0-3000psi
  • 0.15 accuracy for pressure

38
GP50 testing
  • Susceptible to magnetic fields (under study)
  • B sensitivity can be compensated by orientation
    or mu-metal shielding
  • Working on acceptance testing

39
MV100 Testing Status
40
System Test
  • Assembled flight system (Box SC) will be
    vibration tested according to Structural
    Verification Plan (JSC-28792, Rev. B)
  • Functional test of commercial system with TRD
    test beam

41
TRD Gas System Operations
  • Ground operations
  • Flight operations
  • Normal data taking
  • Normal filling
  • Emergency response
  • Startup, shutdown
  • Scheme

42
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
    bottles

43
TRD testing at KSC
  • 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 construction

44
Recovery System
To box S
Regulator
VH8
PH4
RVH0
VH0
2800 psid
VH5
VH2
VH3
VH4
VH1
VH7
PH3
PH1
PH0
PH2
RGA
VH6
30cc Bottle
1 liter Bottle
Rotary Vacuum Pump
10 liter Bottle
25 liter Bottle
Sorption pump
45
(No Transcript)
46
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)

47
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 bottle

48
Recovery system - recovering procedure
  • Seal TRD straws
  • Open Box S vessel to cold 25 l standard gas
    bottles
  • Xe condenses
  • Seal storage vessels

49
Box C OperationsNormal on-orbit
50
Gas Mixing Procedure
  • - Mixing Program On Ground and JMDC
  • - Following Sequence
  • Start with Known Mixture in D Vessel. Vent D if
    mixture unknown.
  • Fill required partial pressure of CO2
  • Fill required partial pressure of Xe.
  • Vent to Box C when required.
  • - Minimize ground communication
  • Prototype system completed 500 mixing cycles
    under computer control.
  • Timing of Valve operations performed by UGBS, not
    USCM!

51
Box C daily filling procedure
  • Shut down CP1.
  • Close V8a and V8b.
  • (Confirm TRD manifolds are open)
  • (Box S opens V4a)
  • Open V6a.
  • Read all pressures every 1 sec
  • (Box S closes V4a)
  • Close V6a.
  • Wait 5 seconds
  • Open V8a.
  • Start CP1.

Black UGBC control Blue UGM, UGBS
52
Box S Emergency Response
Under review!
53
Box C Off-Nominal Responses
54
Box C Startup Sequence
  • Confirm V18a, V18b, V6a, V6b, are closed.
  • Open V8a, close V8b.
  • Power up CO2 analyzer, send initialization
    commands
  • Read all P, T, and query CO2 analyzer.
  • Turn on CP1.
  • Turn on high voltage to Tube 3 and Tube 4.
  • Read all P, T, pump current, and query CO2
    analyzer.
  • Begin normal operations.

55
Box C Shutdown Sequence
  • Shut down CO2 analyzer.
  • If on, shut down MCA.
  • Stop HV to Tube 3 and Tube 4.
  • If on, stop HV to Tube 1 and Tube 2.
  • Stop CP1.
  • If on, stop CP2.
  • Shut V8a and V8b.
  • Confirm V18a, V18b, V6a, V6b all closed.

56
Assembly schedule
  • Box S
  • Schematic prototype built, 500 cycles
  • Electrical dummy built, shipped
  • Commercial version complete at CERN Sept.02
  • Flight version from Arde Feb. 03
  • Testing Rome or Munich Fall 02

57
Assembly Schedule
  • Box C
  • Prototype C1B at Aachen
  • Prototype C1C at MIT, operations studies
  • Design for C2A nearly complete, assembly Sept.
    02
  • Flight C2B March 03
  • Testing MIT or Aachen - Fall 02, integrated test
    Fall 03

58
TRD Gas System Weight Estimate (unchanged)
59
TRD Gas System Issues
  • Where is gt24 V?
  • Need thermal environment designed around 20 C
  • Dallas temperature sensors
  • where?
  • How many?
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