Sawsan311
Chemical
- Jun 21, 2019
- 303
Dear All,
for high pressure drop liquid throttling applications , we tend to select angle type globe choke valve for fulfilling the same. Alternatively, a normal globe valve of straight pattern can be installed along with an RO.
I evaluated both scenarios and found the below:
1- angle valve installation is limited in size, some vendors stage up to 8'' body size only. can you confirm from your experience.
2- when I looked into sizing the RO , it is very tricky to distribute the pressure drop across the RO and the globe valve. Accordingly, if one takes 20% pressure drop across the upstream RO remaining pressure drop will be compensated by RO.
3- for the case where inlet pressure upstream the globe and RO is varying, I could see that if we size the liquid RO for the low delta P case, will end up with large RO for that constant Q. but in reality if the actual pressure is higher, the RO will give much higher flow which can in fact exceed the hydraulic velocity limit of the downstream piping in case the globe valve was not throttled sufficiently to limit that increased flow.
4- while I did the Cv calcs for the angle valve, in some cases, I saw that I would need a 6'' body size valve however, my main line size is 20'' so would that be fine? I have always came across a typical rule of thumb that globe valve size is typically 2 sizes smaller than the main line, but is 6 sizes less would be practical?
Appreciate your views.
Regards,
for high pressure drop liquid throttling applications , we tend to select angle type globe choke valve for fulfilling the same. Alternatively, a normal globe valve of straight pattern can be installed along with an RO.
I evaluated both scenarios and found the below:
1- angle valve installation is limited in size, some vendors stage up to 8'' body size only. can you confirm from your experience.
2- when I looked into sizing the RO , it is very tricky to distribute the pressure drop across the RO and the globe valve. Accordingly, if one takes 20% pressure drop across the upstream RO remaining pressure drop will be compensated by RO.
3- for the case where inlet pressure upstream the globe and RO is varying, I could see that if we size the liquid RO for the low delta P case, will end up with large RO for that constant Q. but in reality if the actual pressure is higher, the RO will give much higher flow which can in fact exceed the hydraulic velocity limit of the downstream piping in case the globe valve was not throttled sufficiently to limit that increased flow.
4- while I did the Cv calcs for the angle valve, in some cases, I saw that I would need a 6'' body size valve however, my main line size is 20'' so would that be fine? I have always came across a typical rule of thumb that globe valve size is typically 2 sizes smaller than the main line, but is 6 sizes less would be practical?
Appreciate your views.
Regards,