helixd
Chemical
- Aug 3, 2013
- 3
thread1036-236204
Dear all,
I saw a previous post on calculating settle out pressures on compressor loops - The situation is such that we have a gas system consisting of a cooler, scrubber (remove free water after cooling) and a compressor unit. Now we assume that the ESDVs (located b4 cooler and after compressor) are activated. A recycle valve that fails open exists that connects the discharge of the compressor back to the suction (in fact the cooler first) thus resulting in a closed recycle loop. I need to determine the settle out pressure and temperature. We assume when the ESDV’s are activated, all the units stop working.
To simplify the whole question, I took in my calculations, 2 closed containers connected by a valve (to depressurise from 60 to 20barg). This can be used to generalize the above scenario. Container A is at 20 barg, 10m3, 45deg C while container B is at 60barg, 1m3, 120deg C. I also assumed z factor equal to 1.
I used the method given by the below link (similar to yours) but I’m not sure if this method is applicable to my situation. I’m not sure why some of the working done is based on standard temp and pressure (equation 4), i.e. 0 deg C and 1 atm. Also the energy balance (Q=n*cp*delta T) assumes constant specific heats, but how do the equations work out (equation 7)?
If I follow the procedure as per the simplified question given above, I obtain 60degC and 24barg as my settling Temp and Pressures. Kindly let me know if you think this method is applicable, or if there is any other method based on inputting P, V, T info in getting the results.
I have attached my excel working for your reference.
Appreciate your guidance to the question above. Thank you for your time.
Regards,
helix
Dear all,
I saw a previous post on calculating settle out pressures on compressor loops - The situation is such that we have a gas system consisting of a cooler, scrubber (remove free water after cooling) and a compressor unit. Now we assume that the ESDVs (located b4 cooler and after compressor) are activated. A recycle valve that fails open exists that connects the discharge of the compressor back to the suction (in fact the cooler first) thus resulting in a closed recycle loop. I need to determine the settle out pressure and temperature. We assume when the ESDV’s are activated, all the units stop working.
To simplify the whole question, I took in my calculations, 2 closed containers connected by a valve (to depressurise from 60 to 20barg). This can be used to generalize the above scenario. Container A is at 20 barg, 10m3, 45deg C while container B is at 60barg, 1m3, 120deg C. I also assumed z factor equal to 1.
I used the method given by the below link (similar to yours) but I’m not sure if this method is applicable to my situation. I’m not sure why some of the working done is based on standard temp and pressure (equation 4), i.e. 0 deg C and 1 atm. Also the energy balance (Q=n*cp*delta T) assumes constant specific heats, but how do the equations work out (equation 7)?
If I follow the procedure as per the simplified question given above, I obtain 60degC and 24barg as my settling Temp and Pressures. Kindly let me know if you think this method is applicable, or if there is any other method based on inputting P, V, T info in getting the results.
I have attached my excel working for your reference.
Appreciate your guidance to the question above. Thank you for your time.
Regards,
helix