|

Carbon Dioxide Supply
Started by Phenom, Dec 16 2011 11:45 PM
3 replies to this topic
Share this topic:
#1
Posted 16 December 2011 - 11:45 PM
Hello everyone. I need to design a system for supplying CO2 from a cylinder. The conditions of the cylinder are 60barg pressure and at 35°C. The purity of gas in the cylinder is 100%. The pressure at the delivery point should be 0.5barg.
Can anyone help me with this. The problem encountered is frosting of gas when the pressure is reduced.
Thanks in advance.
Can anyone help me with this. The problem encountered is frosting of gas when the pressure is reduced.
Thanks in advance.
#2
Posted 17 December 2011 - 12:43 PM
phenom.sam,
Refer the attachment provided. This should help you in geting at some conclusion.
Regards,
Ankur
Refer the attachment provided. This should help you in geting at some conclusion.
Regards,
Ankur
Attached Files
#3
Posted 19 December 2011 - 04:33 AM
Thank you sir
#4
Posted 09 January 2012 - 10:02 AM
I understand you mainly need data on the connecting piping to avoid frosting. Having no experience in CO2 handling, attached "FO.bmp" shows a high pressure nitrogen cylinder connected to a fuel oil accumulator (in a fuel oil supply system to a boiler). Based on this example, the attached "CO2.xls" has been prepared as a first scheme for further investigation and development.Hello everyone. I need to design a system for supplying CO2 from a cylinder. The conditions of the cylinder are 60barg pressure and at 35°C. The purity of gas in the cylinder is 100%. The pressure at the delivery point should be 0.5barg. Can anyone help me with this. The problem encountered is frosting of gas when the pressure is reduced.Thanks in advance.
CO2 in the bottle (cylinder) is gas under mentioned conditions, not far from its critical, as indicated in http://en.wikipedia....Carbon_dioxide . Rough values of CO2 enthalpy indicate increase with decreasing pressure at constant temperature (CO2.xls). To avoid effect of freezing, enthalpy loss has to be given as heat (e.g. through a heat exchanger), so that CO2 temperature remains at 35 oC after the pressure reduction. Rest is similar to "FO.bmp" and explained in the attached "CO2.xls", where a preliminary rough diagram is also presented.
Hopefully this incomplete diagram (e.g. what happens if heating medium fails, what is CO2 temperature downstream exchanger, etc) is useful. Comments could help in necessary improvements.
Attached Files
Similar Topics
Air Supply To Pneumatic HoistStarted by Guest_Im97_* , 25 Nov 2024 |
|
![]() |
||
![]() Activated Carbon SelectionStarted by Guest_Talhafarooq_* , 25 Nov 2024 |
|
![]() |
||
![]() Most Feasible And Economically Friendly Nitrogen Supply For Tank BlankStarted by Guest_Godwin Anyimah_* , 27 Sep 2024 |
|
![]() |
||
![]() ![]() Carbon Bed Filter CalculationsStarted by Guest_kyayura_* , 25 Jul 2023 |
|
![]() |
||
![]() Carbon Capture Absorber SimulationStarted by Guest_raisoturu_* , 21 May 2024 |
|
![]() |