I am hosting a dinner tonight for which I'll be serving white wine (Riesling to be more specific). Generally white wine is best served chilled (not COLD!) at around 50 F or 10 C.

Just for kicks, I thought I'd treat this as a problem of transient conduction. I assume that (forced)convection is negligible since I will leave my wine bottle in my kitchen which has still air.

The following assumptions are made:

  • The wine bottle is assumed to be cylindrical with an outside to inside radii, $r_o/r_i$ ratio of 1.10
  • The only mode of heat transfer for this bottle is conduction (perhaps a poor assumption?). The kitchen air is considered to be still and at 25 C
  • The un-open bottle of wine is a closed thermodynamic system. The glass material has a conductivity $k$ of 1.0 W/m-K and the wine itself has a specific heat at constant volume, $C_v$ of 2.75 kJ/kg-k as per this
  • The volume of the bottle of wine is 750 mL or $750 \times 10^{-6} m^3$
  • The wine is at a temperature of 5 C and hence needs to be warmed for a while. The entire wine is assumed to have a lumped capacitance (all the wine is at the same temperature with little variation with radius).
  • The temperature difference between the wine and the bottle wall is assumed to be $\sim 10 C$ and so is the temperature difference between the bottle wall and the room (just a rough order of magnitude).

The first law of thermodynamics (transient) is applied to this closed system bottle of wine:

$$\frac{\mathrm{d}{E}}{\mathrm{d}t} = \delta\dot{Q} - \delta\dot{W}$$

The $\delta\dot{W}$ term is zero for this closed system as only heat is exchanged with the kitchen atmosphere.

$$\frac{m C_v \Delta T_\text{wine-bottle}}{\Delta t} = \frac{2 \pi k \Delta T_\text{bottle-kitchen}}{ln(r_o/r_i)}$$

This gives me the time the bottle of wine needs to be placed in my kitchen outside the fridge as:

$$\Delta t \approx 0.025 \frac{\Delta T_\text{bottle-air}}{\Delta T_\text{wine-bottle}} C_v \approx 68 \text{ seconds}$$

This seems to be a rather small amount of time!!! Are my assumptions wrong? Should I improve this with convective heat transfer between the bottle and the kitchen air? Will my guests be disappointed? :P

EDIT::Including convective heat transport:

$$\underbrace{\frac{m C_v \Delta T_\text{wine-bottle}}{\Delta t}}_\text{Change in total/internal energy w.r.t time} = \underbrace{\frac{2 \pi k \Delta T_\text{bottle-kitchen}}{ln(r_o/r_i)}}_\text{conduction} + \underbrace{h A \Delta T_\text{bottle-kitchen}}_\text{convection}$$.

Here $h$ is the heat transfer coefficient $\sim 1 W/m-K$, $A$ is the surface area of the cylinder. Based on the volume of the cylinder being $70 mL = \pi r_i^2 h$. The height of the bottle is about $1 foot$ or $0.3048 m$ and the generally close assumption that $r_o \approx 1.1 r_i$, I have (all $\Delta T$'s are close and cancel out):

$$\Delta t = \frac{m C_v ln(r_o/r_i)}{\left[ 2 \pi k + 2\pi r_o(r_o + h) ln(r_o/r_i)\right]} \\ \Delta t \approx 260.76 \text{ seconds} \approx 4 \text{ minutes} $$

This seems more plausible..... But I start doubting myself again.

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    $\begingroup$ Did you invite Sheldon Cooper or something? $\endgroup$ – RedGrittyBrick Mar 1 '13 at 18:08
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    $\begingroup$ @RedGrittyBrick What is a SheldonCooper? :P $\endgroup$ – dearN Mar 1 '13 at 18:08
  • $\begingroup$ I think air is not a good approximation to a thermal reservoir; its heat capacity and conductivity are too low (so you end up with a cold boundary layer around the bottle). Also, you left out some important info: the producer and vintage! $\endgroup$ – Art Brown Mar 1 '13 at 18:31
  • $\begingroup$ @ArtBrown I just worked out the effect of convective heat transport and will add that as an edit. Cold Creek from WA, 2008. $\endgroup$ – dearN Mar 1 '13 at 18:36
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    $\begingroup$ Just some suggestions: (1) The units in the second equation don't match. (2) It's not clear that convection can be treated so simply. Perhaps mixing length theory should be applied. (3) There should be some quantitative estimate of conduction and radiation; at least I'm not convinced they don't matter. (4) In kJ/(kg K), the specific heat of water is 4.2; ethanol (at 2.4) is a minor contribution (this is only wine after all, not hard liquor). That quoted $C_V$ seems a bit low. $\endgroup$ – user10851 Mar 1 '13 at 23:25

I'm no expert, but here goes...

I assume the bottle diameter $d$ is 80 mm, and its glass thickness $l$ is 2 mm. (Height $h$ cancels out of the result). The surface area $A$ of the glass is then approximately $A = \pi d h $.

Start by estimating the thermal conductivities for the 3 heat transfer processes:


The thermal conductivity of glass is $k=1 W/m/K$.
$$q = (k A / l) \Delta T_{glass} = 500 A \Delta T = G_{cond} A \Delta T \quad, \quad G_{cond} = 500 W/m^2/K$$


The convective heat transfer coefficient of air is $h=5-25 W/m^2/K$, according to one reference (a lot of wiggle room here): http://www.engineeringtoolbox.com/convective-heat-transfer-d_430.html $$ q = h A \Delta T \quad, \quad G_{conv} = h W/m^2/K$$

Radiation (larger than I expected, hat tip to Chris White):

The Stefan-Boltzmann constant is $\sigma = 5.67x10^{-8} W/m^2/K^4$. $$ q = \epsilon \sigma A \left(T_1^4-T_2^4 \right) = \epsilon \sigma A (T_1^3 + T_1^2 T_2 + T_1 T_2^2 + T_2^3)\Delta T \approx 4 \sigma T_{avg}^3 A \Delta T \approx 5 \epsilon A \Delta T = G_{rad} A \Delta T$$ $$ G_{rad} = 5 \epsilon W/m^2/K$$

Here $\epsilon$ is the emissivity, which is $1$ for a black body and zero for a perfect reflector. Per Schaum's "Heat Transfer" $\epsilon = 0.94$ for smooth glass, which is $1$ at this level of accuracy.

Radiation occurs in parallel with convection, so their conductivities add, while conduction through the glass is in series with the other $2$, so its (relatively very large) conductivity adds in parallel. The total conductivity $G$ is then determined by: $$q = G A \Delta T$$ $$\frac{1}{G} = \frac{1}{G_{cond}} + \frac{1}{G_{conv}+G_{rad}} \approx \frac{1}{G_{conv}+G_{rad}}$$ $$G \approx 10 - 30 W/m^2/K$$

[Conduction through the glass is much easier than convection + radiation, so the latter two form the heat transfer "bottleneck" (hee hee); conduction is negligibly large.]

Now, for the wine, $q = m C_v dT/dt$ , where $m = \rho V$ , $\rho = 978 kg/m^3 \text{ and } C_v = 4.3 kJ/kg/K$ , according to a report I found on-line:


Equating the $2$ expressions for $q$, we get a nice first order diff eq: $$ \frac{dT}{dt} = (T-T_{amb})/\tau $$ where the time constant $\tau$ is: $$ \tau = \frac{m C_v}{G A} = \frac{\rho C_v }{G} \frac{V}{A} = \frac{\rho C_v }{G} \frac{d}{4} = \frac{84,100}{G} = 2800-8410 \text{ seconds, or } 47 \text{ to } 140 \text{ minutes}.$$

We're only warming the bottle by $5$ out of the initial temperature difference of $20$ degrees, so we don't need to compute logarithms and instead use a linear expression (equivalent to assuming constant heat flow $q$). The time $t_{warm-up}$ required to achieve optimum serving temperature is just: $$ t_{warm-up} = \tau \frac{5}{20} = 12 \text{ to } 35 \text{ minutes}.$$

Update: Here's some data for water in a wine bottle (hey, I'm not wasting good wine). I used one of those vacuum storage stoppers; the hole was just right to poke through a kitchen thermometer. Two diffferent ones, actually. The third curve is an exponential with a 30 minute time constant, which looks to be in the ballpark. It looks like I'm underestimating something, maybe convection? fluid warming data

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  • $\begingroup$ Nice set of calculation but why radiation?? I would think that conduction+convection are a better assumption. Must go find my Karlekar and Desmond $\endgroup$ – dearN Mar 2 '13 at 13:45
  • $\begingroup$ I thought radiation would be negligible and was only making an estimate to justify ignoring it, per Chris White's comment to your question. I was surprised to see it had an effect. $\endgroup$ – Art Brown Mar 2 '13 at 17:03
  • $\begingroup$ Yes, I am extremely surprised that radiation has an effect. I am not convinced however that radiation should be important for this case. I could just be wrong! $\endgroup$ – dearN Mar 2 '13 at 18:09
  • $\begingroup$ (1) You have used the Stefan Boltzmann law for radiation which is reserved only for blackbodies. (2) I think radiation heat transfer, in this case, should be calculated after considering radiation shape factors (3)*Based on *(1) and (2), I somehow feel it is ok to neglect radiation heat transfer and that your answer may be flawed. $\endgroup$ – dearN Mar 4 '13 at 13:52
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    $\begingroup$ 1) I address emissivity in my edit. 2) I think a bottle standing upright has a good view of its surroundings. $\endgroup$ – Art Brown Mar 6 '13 at 4:24

I'm an engineer, not a physicist. My solution:

I suggest you find a bottle of wine with thesame alcohol content. You chill it in the fridge to same temperature as teh one you want to drink. You take it out way before the dinner, put it in the same position you would you real bottle, and start to monitor the temperature. The moment the temperature is right, you note the time this took (and start drinking). Then, you should know the time it takes your wine to reach optimal drinking tempreature after the fridge. Also, you get drink more wine.

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  • $\begingroup$ Hi Fellow engineer! Although an engineer, I strayed across the border into applied math and fluid physics. So my house is sans thermometers! And I like messing around with the conservation equations... $\endgroup$ – dearN Mar 4 '13 at 12:36
  • $\begingroup$ You will have to take regular sips. this will slightly skew your results, but could be worth it. Depending on how much you enjoy the multiple samples approach. $\endgroup$ – mart Mar 4 '13 at 16:02

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