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
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...
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...
Hi,
we have to replace an existing heat exchanger ( a condenser using cold water ) by an air cooler ( fin fan), the elevation is about 4000 mm and we look to lift it to about 12000 mm,is is it possible to determine how this will perform the process, otherwise , between 4 m elevation and 12 m...
Hi,
what value of velocity for sea water piping i should take for sizing a network to feed 8 heat exchangers all over a plant.
literatures give diffenet values
Hi, it is my first partcipation,
i have to design a seaw water network used for cooling in several heat exchangers, the old network was underground, and we want to make it outside, but i need to calculate the water temperature change due to air temperature which can reach 47 °C,
is the heat...
