pc43_ivaniouchenkov_hazop
TRANSCRIPT
Preliminary HAZOP Analysis of the MICE Hydrogen System
Node 5
Node 3
Node2
Node 1 Chiller/ heater
unit
Vent outside flame arrester Ventilation
system
H2 Detector
Hydrogen module enclosure
VP
X 2 X 2
VP
P
VP
Evacuated vent buffer tank
Node 4
P P
P
P
H2 Detector
H2 Detector
2.1 bar
1.7 bar
Vent valve
Vent valveVent outside flame arrester
Non-return valve
He / N2 Purge system
Vent outside flame arrester
Metal hydride hydrogen storage unit
(20 m3 capacity)
Fill valve P P
H2 Gas bottle
70 K Safety window
Internal Window
Hydrogen flow and safety system (option with a metal hydride storage unit)
LHe Heat exchanger
Vacuum vessel
Vacuum
LH2 Absorber
Liquid level gauge
14 K He from Cold box
18 K He to Compressor via Radiation
Pressuregauge
Pressureregulator
ValvePressure relief valve Bursting disk Vacuum VPP P
Version: 06/08/2003
Node 5
Node 3
Node 2
Vent outside flame arrester Ventilation
system
H2 Detector
Hydrogen module enclosure
VP
X 2 X 2
VP
P
VP
Evacuated vent buffer tank
Node 4
P P
P
P
H2 Detector
H2 Detector
2.1 bar
1.7 bar
Vent valve
Vent valveVent outside flame arrester
Non-return valve
He / N2 Purge system
Vent outside flame arrester Hydrogen tank
Volume: about 30 m3
1.6 bar abs > Pressure > 1.1 bar abs
Node 1
Fill valve PP
H2 Gas bottle
70 K Safety window
Internal Window
Hydrogen flow and safety system(option with a hydrogen tank)
LHe Heat exchanger
Vacuum vessel
Vacuum
LH2 Absorber
Liquid level gauge
14 K He from Cold box
18 K He to Compressor via Radiation shield
Pressuregauge
Pressureregulator
ValvePressure relief valve Bursting disk Vacuum VPP P
Version: 09/06/2003
Node 1: Option: Hydrogen storage unit.
Intent: To keep hydrogen gas in the storage unit-absorber vessel closed system.
Working conditions: P = … bar abs , T = 300 K, V = … m3 .
No Parameter Guide word Cause Consequence Safeguards Recommendations
1 Pressure Lower 1. Storage unit is leaking.
2. Pipe is leaking.
3. Absorber vessel is leaking.
1-2. Hydrogen is leaking out in the experimental hall.
3. Hydrogen is leaking into vacuum jacket.
Pressure gauge to trigger an alarm.
Hydrogen ventilation system collects and vents hydrogen out.
Hydrogen detector to trigger an alarm.
Implement an active pressure gauge.
Implement ventilation system.
Implement an active hydrogen detector.
2 Pressure Higher 1. Fill valve is accidentally open
2. Storage unit is overheated
3. Venting path is blocked ?
1-3. Absorber windows can break.
Pressure relief valve to vent outside.
Implement a pressure relief valve.
Node 1: Option: Hydrogen tank
Intent: To keep hydrogen gas in the tank - absorber vessel closed system.
Working conditions: P = … bar abs , T = 300 K, V = … m3 .
No Parameter Guide word Cause Consequence Safeguards Recommendations
1 Pressure Lower 1. Tank is leaking.
2. Pipe is leaking.
3. Absorber vessel is leaking.
1. Air can leak in the tank and in the hydrogen vessel and an explosive mixture can be formed.
1-2. Hydrogen is leaking out in the experimental hall.
3. Hydrogen is leaking into vacuum jacket.
Pressure gauge to trigger an alarm.
Hydrogen ventilation system collects and vents hydrogen out.
Hydrogen detector to trigger an alarm.
Implement an active pressure gauge.
Implement ventilation system.
Implement an active hydrogen detector.
2 Pressure Higher 1. Fill valve is accidentally open.
2. Tank is overheated.
3. Venting path is blocked ?
1-2. Absorber windows can brake
Pressure relief valve to vent outside.
Implement a pressure relief valve.
Node 2: Hydrogen absorber internal vessel with hydrogen windows.
Intent: To keep hydrogen liquid inside hydrogen absorber module.
Working conditions: P = … bar abs, T = 19 – 300 K, V = 25 l.
No Parameter Guide word Cause Consequence Safeguards Recommendations
1 Temperature Lower Too much cooling power from the He cooling system.
1. Pressure in the hydrogen system drops.
2. LH2 level in hydrogen vessel rises.
Pressure gauge to trigger an alarm.
Liquid hydrogen level meter to trigger an alarm.
Implement an active pressure gauge.
Implement an active liquid level meter.
2 Temperature Higher 1. Not enough cooling power from the He cooling system.
2. Power cut.
1-2. Liquid hydrogen evaporates and LH2 level goes down.
1-2. Hydrogen pressure rises.
Liquid hydrogen level meter to trigger an alarm.
Pressure gauge to trigger an alarm.
Implement an active liquid level meter.
Implement an active pressure gauge.
3 Pressure Lower 1. Window is leaking or broken.
2. Pipe is leaking.
3. Hydrogen tanks is leaking.
4. Absorber is over
1. Hydrogen leaks into vacuum vessel.
2-3. Hydrogen is leaking out.
4. Pressure in the system drops and air can leak in the system in case if the
Hydrogen detector to trigger an alarm.
Hydrogen ventilation system collects and vents hydrogen out.
Absorber temperature control system
Implement an active hydrogen detector.
Implement absorber temperature control
cooled. system seal is broken. maintains temperature. system.
4 Pressure Higher Temperature isincreased.
Windows can break. Pressure relief valve to dump hydrogen into a buffer tank
Implement a pressure relief valve and a buffer tank.
Node 3: Hydrogen absorber vacuum jacket with safety windows.
Intent: - To insulate thermally the internal hydrogen vessel .
- To provide additional barrier for air .
Working conditions: P = … bar abs, T = 19-300 K, V = ? l.
No Parameter Guide word Cause Consequence Safeguards Recommendations
1 Pressure Higher 1. Hydrogen window broken
2. Vacuum pump failure
Hydrogen bursts into vacuum jacket
Vacuum drops.
Pressure relief valve to dump hydrogen into a buffer tank and then to vent it outside.
Implement a buffer tank.
2 Hydrogenconcentration
Higher Hydrogen leaks due to window is broken .
An explosive mixture can be formed if there is an air leak in as well.
Active hydrogen sensor detects hydrogen and trigger s an alarm.
Implement an active hydrogen sensor.
Node 4: Buffer tank.
Intent: - To quickly relief pressure in the absorber module in case of window burst .
Working conditions: P = … bar abs, T= 300 K, V = … l.
No Parameter Guide word Cause Consequence Safeguards Recommendations
1 Pressure Higher 1. Venting path is blocked.
2. Vacuum pump failure
1. Absorber vacuum jacket windows can break.
2. Buffer tank can’t be used for dumping hydrogen in case of accident with absorber.
1-2. Active pressure gauge triggers an alarm.
Implement an active pressure gauge.
Keep a spare pump.
Node 5: Hydrogen module enclosure.
Intent: - To localize and vent hydrogen in case of hydrogen leak .
Working conditions: P = … bar abs, T= 300 K, V = … l.
No Parameter Guide word Cause Consequence Safeguards Recommendations
1 Hydrogenconcentration
Higher 1. Hydrogen leaks out absorber module
2. Hydrogen leaks out hydrogen pipes
3. Hydrogen leaks out storage unit.
1-3. Explosive oxygen-hydrogen mixture can be formed
Ventilation system to quickly vent hydrogen out.
Hydrogen detector to trigger an alarm and to start a high rate mode for the ventilation system.
Implement ventilation system equipped with hydrogen detector.