in P&IDs drawing we don't need symbols to define splitter/joiner.
intersections means that the tow stream are joined or on stream is splitted into two streams by means of directional arrows.
HI
WE ARE DESIGNING A GAS RECOVERY SYSTEM FROM A PROPANE REFRIGERATION LOOP.
PROPANE VAPORS RECOVERED WILL BE REINJECTED IN A BOIL-OFF SYSTEM TO BE COMPRESSED AND LIQUEFIED AGAIN WITH VAPORS COMING FROM STORAGE TANKS.
THE TIE-IN POINT IS LOCATED AT ABOUT 100 M FROM THE RECOVERY POINT IN THE...
HI
I AM A BEGINNER PROCESS ENGINEER, AND I HAVE TO DESIGN A SIMPLE SYSTEM TO POOR AND DRAIN OIL FROM THE HOT OIL LOOP.
THIS SYSTEM WILL BE USED IN CASE OF SIMPLE SHUTDONWN OF THE UNIT FOR MAINTENANCE IN THIS CASE OIL WILL BE AT AMBIANT TEPERATURE.
THE SYSTEM CAN BE USED ALSO IN EMERGENCY...
HI
WE ARE DESIGNING A GAS RECOVERY SYSTEM FROM A PROPANE REFRIGERATION LOOP.
PROPANE VAPORS RECOVERED WILL BE REINJECTED IN A BOIL-OFF SYSTEM TO BE COMPRESSED AND LIQUEFIED AGAIN WITH VAPORS COMING FROM STORAGE TANKS.
THE TIE-IN POINT IS LOCATED AT ABOUT 100 M FROM THE RECOVERY POINT IN THE...
hi,
I 'm a process engineer, i m not a specialiste in materials,
my question is:
for above ground installations ( filtraion lines 14", metering lines, headers...)for a natural gas pipeline what's the difference between the use of API 5L X70 and API 5L Gr B, which is the most useful and...
HI,
my question is about LPG storage facilities(high capcity)
what is the greatest capcity for lpg storage and handling facilities that can be constructed and what type of tanks is the most appropriate,
if possible examles over the world
I need informations about this topic please
thank...
HI,
my question is about LPG storage facilities(high capcity)
what is the greatest capcity for lpg storage and handling facilities that can be constructed and what type of tanks is the most appropriate,
if possible examles over the world
thank you very much.
hi,
we are a small company of engineering involved in hydrocarbons domaine, and we want to buy a software for instrumentation, other than inttols, is there any powerful software that help instrumentation engineers? thanks
thank you very much
what about the reduction poition;
1) B vlve - reduction 16x10 - control valv - reduction 10x16 - Blc valv
or
2) reduction 16x10 - blc vlv - control valv - blc valv - reduction 10x16
if someone can give me the reference of codes or standards that treat such problems ?
hi,
we have to install a pressure control valve of 10" with its tow block valves and its bypass on a natural gas line of 16",
the control valve will reduce preure from 55 bar to 43 bar, the flow rate i about 200 000 Nm3/hr.
so how to determine the bypass diametter ?
the block valves (to...
thank you matt
but I think if all the flowrate will be vented to atm the plant upstream (our costumer)will shuttdown every time the pressure increase in the station, the reliefing capacity is to evacuate just a defined quantity on NG to reach the normal operating pressure.
what do you say?
hi,
Please I have to design a pressure reliefing system for a natural gas metering station, and a segment pf pipeline, API standard(521,520)give a formula in which the reliefing capacity is given as a known data but I don't now how i can estimate this value (the quantity of NG to be vented in...
