Jump to content


Photo
- - - - -

carbonation equations


  • Please log in to reply
10 replies to this topic

#1 ThroatwobblerMangrove

ThroatwobblerMangrove

    Open Letter (and similar documents) Comptroller

  • Members
  • PipPipPipPip
  • 4491 posts

Posted 06 November 2009 - 11:40 AM

Does anyone have an equation that is something like:V(t,T,P) = <insert equation here>, where V(t,T,P) is the function for volumes of CO2, t = time, T = temperature, P = PSI.It would be interesting to know so that I could crank the pressure up and know at what time t that I should start turning it down. Anyone have this?

#2 ThroatwobblerMangrove

ThroatwobblerMangrove

    Open Letter (and similar documents) Comptroller

  • Members
  • PipPipPipPip
  • 4491 posts

Posted 06 November 2009 - 11:46 AM

Does anyone have an equation that is something like:V(t,T,P) = <insert equation here>, where V(t,T,P) is the function for volumes of CO2, t = time, T = temperature, P = PSI.It would be interesting to know so that I could crank the pressure up and know at what time t that I should start turning it down. Anyone have this?

Does surface area come into play here? How about the gravity of the beer?

#3 ThroatwobblerMangrove

ThroatwobblerMangrove

    Open Letter (and similar documents) Comptroller

  • Members
  • PipPipPipPip
  • 4491 posts

Posted 06 November 2009 - 12:04 PM

Does surface area come into play here? How about the gravity of the beer?

I suspect both of those things do. This would probably be very similar to a heat transfer problem so we'd have to bust out some partial differential equations. ;)

#4 ThroatwobblerMangrove

ThroatwobblerMangrove

    Open Letter (and similar documents) Comptroller

  • Members
  • PipPipPipPip
  • 4491 posts

Posted 06 November 2009 - 01:22 PM

And you guys call yourselves beer nerds, pppppfffttt.

#5 ANUSTART

ANUSTART

    The Drunk Dump Truck Euphanism.

  • Members
  • PipPipPipPip
  • 3268 posts
  • LocationDenver, CO

Posted 06 November 2009 - 01:30 PM

Chart. Look at numbers. No do math.

#6 ThroatwobblerMangrove

ThroatwobblerMangrove

    Open Letter (and similar documents) Comptroller

  • Members
  • PipPipPipPip
  • 4491 posts

Posted 06 November 2009 - 01:34 PM

Chart. Look at numbers. No do math.

the charts seemingly only deal with equilibrium.

#7 MtnBrewer

MtnBrewer

    Skynet Architect

  • Moderators
  • PipPipPipPip
  • 6695 posts
  • LocationThe Springs

Posted 06 November 2009 - 01:47 PM

Does surface area come into play here? How about the gravity of the beer?

I don't know about gravity but certainly surface area will matter. It won't matter in how much CO2 is dissolved but it will matter in the rate at which it's dissolved. I don't know what the exact equation would be but I'm pretty sure that it would take the general form of D = E - e-rt, where D is the amount of dissolved CO2, E is the amount at equilibrium and r is a factor governing the rate. In other words, the amount of dissolved CO2 would asymptotically approach the equilibrium value. E would be dependent on temperature and pressure and r may depend on these things as well.

#8 RommelMagic

RommelMagic

    Advanced Member

  • Members
  • PipPipPip
  • 454 posts
  • LocationHighland Falls, NY

Posted 06 November 2009 - 02:13 PM

My equation is (P+T)+ M= ?, whereas P=pressure, T=time, M=mouthfeel and the question mark is where it is determined if the beer is ready or not.

#9 ThroatwobblerMangrove

ThroatwobblerMangrove

    Open Letter (and similar documents) Comptroller

  • Members
  • PipPipPipPip
  • 4491 posts

Posted 06 November 2009 - 03:31 PM

I don't know about gravity but certainly surface area will matter. It won't matter in how much CO2 is dissolved but it will matter in the rate at which it's dissolved. I don't know what the exact equation would be but I'm pretty sure that it would take the general form of D = E - e-rt, where D is the amount of dissolved CO2, E is the amount at equilibrium and r is a factor governing the rate. In other words, the amount of dissolved CO2 would asymptotically approach the equilibrium value. E would be dependent on temperature and pressure and r may depend on these things as well.

that's not a bad thought, the rate of transfer will certainly be dependent on the CO2 deltas (similar to temperature deltas in heat transfer).

#10 3rd party JKor

3rd party JKor

    Puller of Meats

  • Patron
  • PipPipPipPipPipPip
  • 64096 posts
  • LocationNW of Boston

Posted 06 November 2009 - 06:40 PM

Unfortunately, it's even more complicated than that. The equation MB posted only works if you assume the keg is well mixed. In reality, there will be a concentration gradient of carbonic acid from the top to the bottom of the keg unless you are continuously agitating it. Not only do you need to calculate the amount of CO2 that passes the phase boundary, which is driven by co2 pressure, surface area and the concentration of carbonic acid at the liquid surface, you also need to know the diffusion rate of carbonic acid away from the phase boundary.The equations to solve for this are not overwhelmingly difficult, the problem is getting realistic values for the rate constants. It's one of those things that you either need to scour brewing science literature for, or do the experiments yourself.

#11 ThroatwobblerMangrove

ThroatwobblerMangrove

    Open Letter (and similar documents) Comptroller

  • Members
  • PipPipPipPip
  • 4491 posts

Posted 06 November 2009 - 06:43 PM

Unfortunately, it's even more complicated than that. The equation MB posted only works if you assume the keg is well mixed. In reality, there will be a concentration gradient of carbonic acid from the top to the bottom of the keg unless you are continuously agitating it. Not only do you need to calculate the amount of CO2 that passes the phase boundary, which is driven by co2 pressure, surface area and the concentration of carbonic acid at the liquid surface, you also need to know the diffusion rate of carbonic acid away from the phase boundary.The equations to solve for this are not overwhelmingly difficult, the problem is getting realistic values for the rate constants. It's one of those things that you either need to scour brewing science literature for, or do the experiments yourself.

yeah - I found some literature and the constants are hiding a lot of details I think.


0 user(s) are reading this topic

0 members, 0 guests, 0 anonymous users