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1 LST Gas System R. Messner May 2004 Readiness Review

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LST Gas System. R. Messner May 2004 Readiness Review. Will cover a few of the items below. Gas Mix – the issue of what gas mixtures will be allowed in the LST system has been resolved FHA: O’Neill, Budnick HEEC review Gas Mixing System In leak test Want to test output flows ASAP - PowerPoint PPT Presentation

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Page 1: LST Gas System

1

LST Gas System

R. Messner

May 2004

Readiness Review

Page 2: LST Gas System

2

Will cover a few of the items below

• Gas Mix – the issue of what gas mixtures will be allowed in the LST system has been resolved

– FHA: O’Neill, Budnick– HEEC review

• Gas Mixing System– In leak test– Want to test output flows ASAP– Integrate with the GIB

• Gas Interrupt Box (GIB)– Finished with checkout– Had found problems with firmware; fixed

• IR-2 Distribution Panels– Flow restrictor in hand, checked out

• Gas Supply Manifolds– Next to be assembled

• Gas Shack Safety System Expansion underway

• Electrical

• External Monitor System

Page 3: LST Gas System

3

Gas Mix Instead of getting a specific mix approved,

we want approval for a region of mixes

0 20 40 60 80 100

0

20

40

60

80

100

Per Cent Argon

%CO2=100-%Ar-%Isobutane

Not 'Physical'

Representation of a three component gas

Possible Mixes

Bureau of Mines Tci

CERN Tci

Page 4: LST Gas System

4

Gas Mix The operating region takes into account the stability we have seen in the RPC system

0 2 4 6 8 10

7.5

8

8.5

9

9.5

10

Compare_errors_vs_flammable_region_II

Per Cent Argon (proposed limit, 9.7% isobutane at 0% argon)

Runnable Region (9.41 % isobutane at 0% argon)

Runnable Region +- 1.0% drift

Example Point (8.65% isobutane, 3% argon)

Per Cent Argon

All Operational Settings Are To Be Below the Blue Line

%CO2=100-%Ar-%Isobutane

Page 5: LST Gas System

5

G as In te rru p t B ox

M o n ito rs gas flow s;w ill sh u t o ff in pu ts ifflo w s or ra tio s areno t corre c t

(h o m e m a d e )

F low C o ntro l B o x

O n e m a ste r flo w ;s la ve s se t b y ara tio to ac tu a l f lo wo f m a ste r

M a ss F lo w C o ntro lle rs

C O 2 C O 2

A r A r

Iso Iso

M a ss F lo w M e ters

Pre

ssu

reS

ens

ors

M ass F lo w M ete r R e a d in gs

Ve n t

Sta tu s

S a m p leP o rt

A fourth mass flow meter can provide a tie-breaking vote in case of MFM/MFC disagreementCan also pick up small drifts in mixed gas flows

Shut-off solenoids will close if the gas mix drifts out of the allowed region

Mixing System Functionality

Page 6: LST Gas System

6

Gas Rack - in leak test

Page 7: LST Gas System

7

Gas Rack

Page 8: LST Gas System

8

Gas Interrupt Box Functionality

Reading InFrom Flowmeters

0-5 Volts

Reading Out

SolenoidPower

Trip?

Reading In Range?

To Monitor

To MonitorTo Monitor

ToSolenoids

ShutOffPower

S

S im p so n 2

%

S

S im pso n 2

%

Iso

CO2

S

S im p so n 2

%

Argon

Reading In Range?

Reading In Range?

S

S im p so n 2

%

Mix

Page 9: LST Gas System

9

GIB in checkout

Page 10: LST Gas System

10

Overview of the IR-2 Distribution

Layer Distribution Manifold with Resistors

Sextant Distribution Manifoldwith safety bubblers and rotameters

Left Side Modules

Right Side Modules

PSI “ H2O

Output Collection Manifold with Bubblers

Le ft H a lf

R igh t H a lf

Le ft H a lf

R igh t H a lf

Page 11: LST Gas System

11

Silica tubing flow resistor

Page 12: LST Gas System

12

Check of silica tubing flow resistance

0

1

2

3

4

5

0.005 0.01 0.015 0.02 0.025 0.03 0.035 0.04

Delta_P_thru_one_inch_of_tube

Delta P (inches H20) for 5.22 liters per hour thru one inch of tubeMeasurement y = 2.0575e-07 * x̂ (-3.9842) R= 1

Inner Diameter (inch)

Measured at 50 cc/min: Delta P = 1.8-2.0 inches H2O for a 1.875 inch long piece of 0.53 mm ID silicon tubing

Page 13: LST Gas System

13

Gas Shack Layout

22 feet

RPC

DCH

inertgas

DCHgas

DCHgas

elec

Cabinet

Term

inal

15.5Feet

12 Feet19 Feet

10 FeetCovered

North

CO2

Air

He

MH-6

ElectricalPanel

Fan

3.88 in

VMEcrate

Light

Light

DCH and RPC Manifold Panels

N2

Argon

Construct a new isobutane supply rack and manifold;Will have two isobutane shutoff valves, orifice

Two new inert gas supplies;Each will have a shutoff valve, orifice, overpressure releases

Page 14: LST Gas System

14

Summary

• The loose ends involved in determining a permissible gas mix have been resolved

• Very close to having a functional mixing system with its monitor system to ensure a non-flammable and a runnable mix– Use air or nitrogen, check the self consistency

and stability of system

• It is important to keep moving ahead; sufficient and timely technical support is critical– Want the gas rack in the gas shack before the end

of May– Delayed a bit because we want to get the manifolds

done first; then we can do more things in parallel

• Expansion of Gas Shack safety system in progress

• EPICs monitor system will be the next item to attack

Page 15: LST Gas System

15

Spare Slides

Page 16: LST Gas System

16

Looked at the recent performance of the RPC system

Snapshots taken a week apart, a half day at a time

This is a measure of the stability of the gas mixture

+- 0.0005 out of 0.045

Or ~ 1.0 % of the reading

0.044

0.0445

0.045

0.0455

0.046

0 2000 4000 6000 8000 10000 12000

gasreadings_output_oct_dec_2003_cleaned

Fraction of Isobutane

Index

11/20 11/27 12/04 12/11 12/18

Page 17: LST Gas System

17

Recent performance of the RPC system

0

500

1000

1500

2000

Percentage Isobutane

Range

-1 % of nominal+1 % of nominal

Isobutane Fraction in Gas Mixture