Formula for relation between pressure and volume for GAS

Click For Summary

Discussion Overview

The discussion revolves around calculating the relationship between pressure and volume in a closed tank containing fluids and pressurized gas, specifically in the context of a practical scenario involving a tanker. Participants explore various formulas and factors that influence the pressure changes as fluids are drained from the tank.

Discussion Character

  • Exploratory
  • Technical explanation
  • Debate/contested
  • Mathematical reasoning

Main Points Raised

  • One participant describes a scenario involving a closed tank with fluids and pressurized CO2, seeking to determine how much fluid can be drained before the pressure drops to zero.
  • Another participant suggests using atmospheric pressure as a reference and proposes a calculation involving a factor derived from the pressure in mmWG to determine the volume of fluid that can be drained.
  • A later reply clarifies that the goal is to understand the point at which fluid drainage ceases, rather than achieving zero pressure, and discusses the implications of gas cooling during fluid drainage.
  • Participants discuss the importance of initial pressure and the potential need for additional pressure to maintain fluid flow, considering factors such as adiabatic gas expansion and cooling effects.
  • There is a reiteration of the factor used in calculations, with some participants expressing uncertainty about its application in different scenarios involving varying tank capacities and pressures.

Areas of Agreement / Disagreement

Participants express differing views on the implications of pressure changes during fluid drainage, particularly regarding the effects of adiabatic cooling and the conditions necessary to maintain fluid flow. The discussion remains unresolved, with multiple competing perspectives on the calculations and assumptions involved.

Contextual Notes

Participants note that the analysis may overlook certain factors, such as the impact of adiabatic cooling on gas pressure and fluid flow, which could significantly affect the outcomes of the proposed calculations.

Wiecker
Messages
2
Reaction score
0
Hi all,

I am brand new here and need some help - i hope it is the right category i am posting in.

I am no expert in physics - i am working at sea as a mate on board producttankers. I would like some advice for calculating or formulas for the following scenario:

- A closed tank 10m3 is half full with fluids(5m3)
- On top of the fluids there is pressurized inertgas (CO2); the pressure is 500mmWG absolute
- In the bottom of the tank there is a draining valve.

How many fluids can i drain before the pressure drops to Zero?

Thanks in advance.

Brgds, Stefan
 
Physics news on Phys.org
Sounds like an exam question... The best way to calculate this is using atm (atmospheres) as a pressure unit. 1mWG is 0,09678 atm of overpressure with regard to free air. So the actual pressure of 0.5mWG=500mmWG is 1atm+0.048atm=1.048 atm. You can regard this as the compression factor. So if you expand the gas by 1.048 the pressure will be the same as on the outside. You then have drained 1.048\cdot 5m^3 - 5m^3=0.048 \cdot 5m^3 = 0.224m^3 and the pressure is 0mmWG But then there is pressure on the bottom from the weight of the fluid sou you could drain a bit more and produce negative pressures in the CO_2. If you have water in the container, then the draining should stop when the height of the water is the same as the negative mmWG in the CO_2 (I think the extra volume you can squeeze out depends on the shape of the container, but I am not sure and too lazy to calculate this now).
 
Thanks for your adivice.

So your solution is telling me that 0,048 i a factor or constant, which regards to a drop of 500mmWG pressure?

The question is not an examquestion - it is with regards to optimizing a fuelprocess on board a tanker.

A real case scenario would be a tanker of a total capacity of let's say 50.000 m3 with 30.000 cargo discharging via an enclosed system to a shoretank. Let's say i use your formula with 0,048 as a factor:

50.000 - 30.000 = 20.000 m3 of inertgas at a pressure of 500mmWG. Then i can discharge 20.000 * 0,048 = 960 m3? And after i have discharged 10.000m3 of cargo my inertgascapacity will be 30.000. Let's say i have pressurized the tanks again to 500mmWG - now i can discharge 30.000 * 0,048 = 1440 m3?

Is that correct understood?
 
OK, so you don't mean zero pressure, you just mean the point at which the fluid drain ceases. And the aim is to empty the tank, just.
Simplest is to run it backwards. At the end, you want a tankfull of gas at 1 atm. So when the tank is half full of fluid it must be at 2 atm. But there's a catch. As the fluid drains and the gas expands it will cool. This will lower the pressure and inhibit draining. If you have plenty of time there's no problem. Heat will slowly flow into bring the gas back to ambient and fluid flow continue. In practice, time matters, so you will need some extra initial pressure.
If you want no delay, you can use the adiabatic gas expansion formula to find how the pressure will change.
 
Wiecker said:
Thanks for your adivice.

So your solution is telling me that 0,048 i a factor or constant, which regards to a drop of 500mmWG pressure?

Correct.

A real case scenario would be a tanker of a total capacity of let's say 50.000 m3 with 30.000 cargo discharging via an enclosed system to a shoretank. Let's say i use your formula with 0,048 as a factor:

50.000 - 30.000 = 20.000 m3 of inertgas at a pressure of 500mmWG. Then i can discharge 20.000 * 0,048 = 960 m3?

This is basically what I said, but I do not know how these things work. So what I can say is that after draining this amount of liquid the pressure in the gas will be the same on the inside as in the air on the outside (0mmWG). And only if you measure overpressure with respect to the outside. If you want to know if this stops the flow of liquid there are more things to consider. Maybe you know from experience if 0mmWG pressure is enough to stop the flow or if the pressure needs to be negative to hold the liquid in or if there is counter pressure in the tank you discharge into.

And after i have discharged 10.000m3 of cargo
by pressurizing a number of times I suppose
my inertgascapacity will be 30.000. Let's say i have pressurized the tanks again to 500mmWG - now i can discharge 30.000 * 0,048 = 1440 m3?

Is that correct understood?

Yes, exactly.
 
This analysis is still ignoring the adiabatic cooling. This will significantly reduce the flow. see my earlier post.
 

Similar threads

  • · Replies 7 ·
Replies
7
Views
14K
  • · Replies 14 ·
Replies
14
Views
9K
  • · Replies 26 ·
Replies
26
Views
2K
  • · Replies 15 ·
Replies
15
Views
4K
  • · Replies 67 ·
3
Replies
67
Views
6K
  • · Replies 11 ·
Replies
11
Views
7K
  • · Replies 14 ·
Replies
14
Views
2K
  • · Replies 8 ·
Replies
8
Views
4K
  • · Replies 45 ·
2
Replies
45
Views
5K
  • · Replies 35 ·
2
Replies
35
Views
6K