Title: TRD Gas System TIM Report
1TRD Gas System TIM Report
- Peter Fisher
- MIT
- May 8, 2002
2TRD 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.
3TRD 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)
4Outline
- Mechanical layout
- C. Gargiulo
- J. Burger (manifolds)
- Electrical layout and signals
- A. Bartoloni (this session)
- Components
- Operations
- R.Henning (slow control session)
5TDR 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
6TRD Gas Supply Mounted to USS-02
7Box S Component Layout
Vacuum case
Box C
8Figure 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
9TRD 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)
10Magnetic Field at Gas System
Xe
Vacuum case
CO2
C
Marotta Valves
11TRD 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.
12TRD 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
13TDR 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
14Box S Signals and Power
15Box S Electronic Simulator
16Box C Electrical Signals
Three GlenAir connectors 21-pin power 9-pin
high current 25-pin signal
24 V supply still unresolved!!
17Box S Pinout
18TRD Gas System Components
- Box S
- Composite overwrapped pressure vessels (COVP)
- High pressure valves
- GP-50 (gyppie fifty) pressure sensors
- Box C
- Pumps
19Box S Component List
20Arde Vessels
21TRD 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
-
22TRD 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
23TRD 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
-
24Xe Vessel During Assembly
25TRD 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
26TRD 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)
27CO2 Vessel Prior to Overwrap
28Marotta MV197
- At storage tanks - 3200 psi
- Inline valves - does not leak out
- Based on MV100 design - same drivers
- Space qualified??
29Box C Components List
30Pumps
- 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
31Pumps
- 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
32Gas system test setup
33Test 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)
34CO2 Concentration test
35Component 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
36MV100 Test 1 Doc
37GP50 testing
- Temperature compensated pressure readings
- Three kinds 0-25psi, 0-300psi and 0-3000psi
- 0.15 accuracy for pressure
38GP50 testing
- Susceptible to magnetic fields (under study)
- B sensitivity can be compensated by orientation
or mu-metal shielding - Working on acceptance testing
39MV100 Testing Status
40System 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
41TRD Gas System Operations
- Ground operations
- Flight operations
- Normal data taking
- Normal filling
- Emergency response
- Startup, shutdown
- Scheme
42TRD 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
43TRD 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
44Recovery 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)
46Recovery 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)
47Recovery 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
48Recovery system - recovering procedure
- Seal TRD straws
- Open Box S vessel to cold 25 l standard gas
bottles - Xe condenses
- Seal storage vessels
49Box C OperationsNormal on-orbit
50Gas 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!
51Box 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
52Box S Emergency Response
Under review!
53Box C Off-Nominal Responses
54Box 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.
55Box 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.
56Assembly 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
57Assembly 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
58TRD Gas System Weight Estimate (unchanged)
59TRD Gas System Issues
- Where is gt24 V?
- Need thermal environment designed around 20 C
- Dallas temperature sensors
- where?
- How many?