Sawsan311
Chemical
- Jun 21, 2019
- 303
Dear All,
With regards to the hazards associated with high pressure CO2 used in liquid/dense phase process applications, I would like to get your views on the requirement for double isolation or what is conventionally known as DBB for such application, I support that for all CO2 applications double isolation is required due to the following:
1- High CO2 expansion ratio in case of a release or a leak / passing valve i.e. liquid CO2 increases by 700-800 times in volume when expanded to atmospheric conditions.
2- CO2 cryogenic challenges associated with high J-T coefficient in conjunction with isentropic expansion associated with CO2 liquid evaporative cooling hence when released , very low temperature in magnitude as low as -80 to -90 C is envisaged. density exceeds density of air ( at atmospheric conditions) creating additional challenges of dispersion and risks of acute asphyxiation.
3- The risk of CO2 solid formation upon expansion which have an erosive characteristic over any nearby personnel/equipment.
If we need to rationalize the DBB requirement for CO2, what would be the pressure class rating recommended as a minimum criteria for double isolation. Based on the simulations I have done, even a 45 barg gas CO2 -300# (below critical point) is sufficient to have an expansion ratio of 80-90 times which is still very high inducing a secondary layer of isolation irrespective to the pipe size.
Appreciate your views.
Regards,
With regards to the hazards associated with high pressure CO2 used in liquid/dense phase process applications, I would like to get your views on the requirement for double isolation or what is conventionally known as DBB for such application, I support that for all CO2 applications double isolation is required due to the following:
1- High CO2 expansion ratio in case of a release or a leak / passing valve i.e. liquid CO2 increases by 700-800 times in volume when expanded to atmospheric conditions.
2- CO2 cryogenic challenges associated with high J-T coefficient in conjunction with isentropic expansion associated with CO2 liquid evaporative cooling hence when released , very low temperature in magnitude as low as -80 to -90 C is envisaged. density exceeds density of air ( at atmospheric conditions) creating additional challenges of dispersion and risks of acute asphyxiation.
3- The risk of CO2 solid formation upon expansion which have an erosive characteristic over any nearby personnel/equipment.
If we need to rationalize the DBB requirement for CO2, what would be the pressure class rating recommended as a minimum criteria for double isolation. Based on the simulations I have done, even a 45 barg gas CO2 -300# (below critical point) is sufficient to have an expansion ratio of 80-90 times which is still very high inducing a secondary layer of isolation irrespective to the pipe size.
Appreciate your views.
Regards,