Surface Spray Cooling
From ThermalFluidsPedia
(Created page with 'When liquid drops are sprayed onto a hot surface, heat conduction causes the liquid to superheat and evaporate into a gas (see Figure 9.2). The cooling capacity of the process de…') 
Yuwen Zhang (Talk  contribs) 

(3 intermediate revisions not shown)  
Line 1:  Line 1:  
  +  [[Image:NewChapter9 (7).jpgthumb200 pxalt= Evaporation from a liquid droplet on a heated wall.  '''Evaporation from a liquid droplet on a heated wall.''' ]]  
  +  
  +  
  +  
  +  When liquid drops are sprayed onto a hot surface, heat conduction causes the liquid to superheat and evaporate into a gas (see figure). The cooling capacity of the process depends on the time required for an averagesized drop to cool. If the shape of the droplet can be assumed to be hemispherical during the evaporation process, the energy balance at the interface can be written as  
  +  
  +  
  +  
  Analytical solution of eq. (  +  { class="wikitable" border="0" 
+    
+   width="100%"   
+  <center><math>{{\rho }_{\ell }}{{h}_{\ell v}}2\pi r_{I}^{2}\frac{d{{r}_{I}}}{dt}={{k}_{\ell }}\int_{0}^{\pi /2}{\frac{\partial {{T}_{\ell }}({{r}_{I}},\theta )}{\partial r}}2\pi r_{I}^{2}\cos \theta d\theta h2\pi r_{I}^{2}\left( {{T}_{\infty }}{{T}_{sat}} \right)</math></center>  
+  {{EquationRef(1)}}  
+  }  
+  
+  where ''r<sub>I</sub>'' is the radius of the droplet. Equation (1) can be simplified as  
+  
+  { class="wikitable" border="0"  
+    
+   width="100%"   
+  <center><math>{{\rho }_{\ell }}{{h}_{\ell v}}\frac{d{{r}_{I}}}{dt}={{k}_{\ell }}\int_{0}^{\pi /2}{\frac{\partial {{T}_{\ell }}({{r}_{I}},\theta )}{\partial r}}\cos \theta d\theta h\left( {{T}_{\infty }}{{T}_{sat}} \right)</math></center>  
+  {{EquationRef(2)}}  
+  }  
+  
+  Analytical solution of eq. (2) is very difficult because the temperature distribution in the liquid droplet is twodimensional in nature. ''A'' scale analysis similar to that in [[#ReferencesLock (1994)]] is presented here to estimate the time required for droplet with an initial radius of ''R<sub>i</sub>'' to evaporate completely.  
The scale of the radius of the droplet, ''r<sub>I</sub>'', is ''R<sub>i</sub>''. Thus the scale of the temperature gradient at the interface is  The scale of the radius of the droplet, ''r<sub>I</sub>'', is ''R<sub>i</sub>''. Thus the scale of the temperature gradient at the interface is  
  
  
  
  The scale analysis of eq. (  +  { class="wikitable" border="0" 
  +    
  <center><math>{{\rho }_{\ell }}{{h}_{\ell v}}\frac{{{R}_{i}}}{{{t}_{f}}}\sim {{k}_{\ell }}\frac{{{T}_{w}}{{T}_{sat}}}{{{R}_{i}}}+h({{T}_{\infty }}{{T}_{sat}})</math>  +   width="100%"  
  +  <center><math>\frac{\partial T({{r}_{I}},\theta )}{\partial r}\sim \frac{{{T}_{w}}{{T}_{sat}}}{{{R}_{i}}}</math></center>  
+  {{EquationRef(3)}}  
+  }  
+  
+  The scale analysis of eq. (2) yields  
+  
+  { class="wikitable" border="0"  
+    
+   width="100%"   
+  <center><math>{{\rho }_{\ell }}{{h}_{\ell v}}\frac{{{R}_{i}}}{{{t}_{f}}}\sim {{k}_{\ell }}\frac{{{T}_{w}}{{T}_{sat}}}{{{R}_{i}}}+h({{T}_{\infty }}{{T}_{sat}})</math></center>  
+  {{EquationRef(4)}}  
+  }  
which can be rearranged as  which can be rearranged as  
  
  
  
  +  { class="wikitable" border="0"  
  +    
  <center><math>{{\rho }_{\ell }}{{h}_{\ell v}}\frac{R_{i}^{2}}{{{  +   width="100%"  
  +  <center><math>\frac{{{\rho }_{\ell }}{{h}_{\ell v}}}{{{k}_{\ell }}}\frac{R_{i}^{2}}{{{t}_{f}}}\sim ({{T}_{w}}{{T}_{sat}})+\frac{h{{R}_{i}}}{{{k}_{\ell }}}({{T}_{\infty }}{{T}_{sat}})</math></center>  
+  {{EquationRef(5)}}  
+  }  
  +  Since the liquid droplet is very small, <math>h{{R}_{i}}/{{k}_{\ell }}</math> is very small, so the second term on the righthand side of eq. (4) is much smaller than the first. Equation (4) can be simplified by neglecting the second term on the righthand side, i.e.,  
  +  { class="wikitable" border="0"  
  +    
  <center><math>  +   width="100%"  
  +  <center><math>{{\rho }_{\ell }}{{h}_{\ell v}}\frac{R_{i}^{2}}{{{k}_{\ell }}{{t}_{f}}}\sim ({{T}_{w}}{{T}_{sat}})</math></center>  
+  {{EquationRef(6)}}  
+  }  
  +  The physical significance of eq. (6) is that the latent heat of evaporation is balanced primarily by conduction in the liquid droplet, while the effect of convection on the surface of the droplet is negligible.  
  +  
  +  
  +  
  Combining eqs. (  +  The time that it takes to completely evaporate the droplet with an initial radius of ''R<sub>i</sub>'' is therefore estimated by 
  +  
  <center><math>{{t}_{f}}\sim \frac{{{\rho }_{\ell }}{{h}_{\ell v}}{{R}_{i}}}{{{{{q}''}}_{w}}}</math>  +  { class="wikitable" border="0" 
  +    
+   width="100%"   
+  <center><math>{{t}_{f}}\sim \frac{{{\rho }_{\ell }}{{h}_{\ell v}}R_{i}^{2}}{{{k}_{\ell }}\left( {{T}_{w}}{{T}_{sat}} \right)}</math></center>  
+  {{EquationRef(7)}}  
+  }  
+  
+  For the cases where the substrate heat flux beneath the droplet, <math>{{{q}''}_{w}}</math>, is known, eq. (6) should be rewritten in terms of heat flux. The scale of the heat flux at the heating surface is  
+  
+  { class="wikitable" border="0"  
+    
+   width="100%"   
+  <center><math>{{{q}''}_{w}}\sim \frac{{{k}_{\ell }}\left( {{T}_{w}}{{T}_{sat}} \right)}{{{R}_{i}}}</math></center>  
+  {{EquationRef(8)}}  
+  }  
+  
+  Combining eqs. (7) and (8) yields  
+  
+  { class="wikitable" border="0"  
+    
+   width="100%"   
+  <center><math>{{t}_{f}}\sim \frac{{{\rho }_{\ell }}{{h}_{\ell v}}{{R}_{i}}}{{{{{q}''}}_{w}}}</math></center>  
+  {{EquationRef(9)}}  
+  }  
which indicates that a smaller drop will provide a larger cooling effect.  which indicates that a smaller drop will provide a larger cooling effect.  
  While eqs. (  +  While eqs. (7) and (9) provide the order of magnitude of the time required to completely evaporate the droplet, quantitative estimation of the evaporation time is often also desirable. A simple approximate analysis will be done below by estimating the conduction in the liquid droplet by the following correlation: 
  +  
  <center><math>{{q}_{d}}={{k}_{\ell }}\bar{A}\frac{{{T}_{w}}{{T}_{sat}}}{{\bar{\delta }}}</math>  +  { class="wikitable" border="0" 
  +    
+   width="100%"   
+  <center><math>{{q}_{d}}={{k}_{\ell }}\bar{A}\frac{{{T}_{w}}{{T}_{sat}}}{{\bar{\delta }}}</math></center>  
+  {{EquationRef(10)}}  
+  }  
where <math>\bar{A}</math> and <math>\bar{\delta }</math> are the average crosssectional area of heat conduction and the average path length of the conduction, respectively. For a hemispherical droplet, the contact area between the droplet and the heated wall is <math>{{A}_{w}}=\pi r_{I}^{2}</math> and the interfacial area of the droplet is <math>{{A}_{I}}=2\pi r_{I}^{2}</math>. Thus, we can take the average conduction area as  where <math>\bar{A}</math> and <math>\bar{\delta }</math> are the average crosssectional area of heat conduction and the average path length of the conduction, respectively. For a hemispherical droplet, the contact area between the droplet and the heated wall is <math>{{A}_{w}}=\pi r_{I}^{2}</math> and the interfacial area of the droplet is <math>{{A}_{I}}=2\pi r_{I}^{2}</math>. Thus, we can take the average conduction area as  
  +  { class="wikitable" border="0"  
+    
+   width="100%"   
+  <center><math>\bar{A}=\frac{1}{2}({{A}_{w}}+{{A}_{I}})=\frac{3}{2}\pi r_{I}^{2}</math></center>  
+  {{EquationRef(11)}}  
+  }  
The average path length for conduction is  The average path length for conduction is  
  +  
  <center><math>\bar{\delta }=\frac{V}{{\bar{A}}}=\frac{(2/3)\pi r_{I}^{3}}{(3/2)\pi r_{I}^{2}}=\frac{4}{9}{{r}_{I}}</math>  +  { class="wikitable" border="0" 
  +    
+   width="100%"   
+  <center><math>\bar{\delta }=\frac{V}{{\bar{A}}}=\frac{(2/3)\pi r_{I}^{3}}{(3/2)\pi r_{I}^{2}}=\frac{4}{9}{{r}_{I}}</math></center>  
+  {{EquationRef(12)}}  
+  }  
Therefore, the conduction in the liquid droplet becomes  Therefore, the conduction in the liquid droplet becomes  
  
  
  
  Replacing the first term on the righthand side of eq. (  +  { class="wikitable" border="0" 
  +    
  <center><math>{{\rho }_{\ell }}{{h}_{\ell v}}2\pi r_{I}^{2}\frac{d{{r}_{I}}}{dt}=\frac{27}{8}\pi {{k}_{\ell }}{{r}_{I}}({{T}_{w}}{{T}_{sat}})</math>  +   width="100%"  
  +  <center><math>{{q}_{d}}=\frac{27}{8}\pi {{k}_{\ell }}{{r}_{I}}({{T}_{w}}{{T}_{sat}})</math></center>  
+  {{EquationRef(13)}}  
+  }  
+  
+  Replacing the first term on the righthand side of eq. (2) with eq. (13), and dropping the second term on the righthand side of eq. (2) (see the above scale analysis), the energy balance for the hemispherical droplet becomes  
+  
+  { class="wikitable" border="0"  
+    
+   width="100%"   
+  <center><math>{{\rho }_{\ell }}{{h}_{\ell v}}2\pi r_{I}^{2}\frac{d{{r}_{I}}}{dt}=\frac{27}{8}\pi {{k}_{\ell }}{{r}_{I}}({{T}_{w}}{{T}_{sat}})</math></center>  
+  {{EquationRef(14)}}  
+  }  
which can be rearranged as  which can be rearranged as  
  +  
  <center><math>{{r}_{I}}\frac{d{{r}_{I}}}{dt}=\frac{27}{16}\frac{{{k}_{\ell }}({{T}_{w}}{{T}_{sat}})}{{{\rho }_{\ell }}{{h}_{\ell v}}}</math>  +  { class="wikitable" border="0" 
  +    
+   width="100%"   
+  <center><math>{{r}_{I}}\frac{d{{r}_{I}}}{dt}=\frac{27}{16}\frac{{{k}_{\ell }}({{T}_{w}}{{T}_{sat}})}{{{\rho }_{\ell }}{{h}_{\ell v}}}</math></center>  
+  {{EquationRef(15)}}  
+  }  
which is subject to the following initial conditions:  which is subject to the following initial conditions:  
  +  
+  { class="wikitable" border="0"  
+    
+   width="100%"   
<center><math>{{r}_{I}}={{R}_{i}}\begin{matrix}  <center><math>{{r}_{I}}={{R}_{i}}\begin{matrix}  
, & t=0 \\  , & t=0 \\  
  \end{matrix}</math>  +  \end{matrix}</math></center> 
  +  {{EquationRef(16)}}  
+  }  
  Integrating eq. (  +  Integrating eq. (15) and considering its initial condition, eq. (16), one obtains the transient radius of the liquid droplet: 
  +  
  +  
  +  
  +  { class="wikitable" border="0"  
  +    
  <center><math>{{  +   width="100%"  
  +  <center><math>{{r}_{I}}=\sqrt{R_{i}^{2}\frac{27}{8}\frac{{{k}_{\ell }}({{T}_{w}}{{T}_{sat}})t}{{{\rho }_{\ell }}{{h}_{\ell v}}}}</math></center>  
+  {{EquationRef(17)}}  
+  }  
  which agrees with the results obtained by scale analysis, eq. (  +  The time required for the droplet to evaporate completely can be obtained by letting <math>{{r}_{I}}</math> in eq. (17) equal zero, i.e., 
+  
+  { class="wikitable" border="0"  
+    
+   width="100%"   
+  <center><math>{{t}_{f}}=\frac{8{{\rho }_{\ell }}{{h}_{\ell v}}R_{i}^{2}}{27{{k}_{\ell }}({{T}_{w}}{{T}_{sat}})}</math></center>  
+  {{EquationRef(18)}}  
+  }  
+  
+  which agrees with the results obtained by scale analysis, eq. (17).  
The above analysis is otherwise simplistic because it assumes that the shape of the droplet is hemispherical. In fact, the shape of the droplet depends on the velocity with which it impacts the wall as well as the wettability of the liquid droplet on the wall. If the contact area between the droplet and the wall is larger (due to higher impacting velocity or good wettability), the time for conduction through the liquid is shorter and the life of the drop will be shorter as well.  The above analysis is otherwise simplistic because it assumes that the shape of the droplet is hemispherical. In fact, the shape of the droplet depends on the velocity with which it impacts the wall as well as the wettability of the liquid droplet on the wall. If the contact area between the droplet and the wall is larger (due to higher impacting velocity or good wettability), the time for conduction through the liquid is shorter and the life of the drop will be shorter as well.  
+  
+  ==References==  
+  
+  Faghri, A., and Zhang, Y., 2006, ''Transport Phenomena in Multiphase Systems'', Elsevier, Burlington, MA  
+  
+  Faghri, A., Zhang, Y., and Howell, J. R., 2010, ''Advanced Heat and Mass Transfer'', Global Digital Press, Columbia, MO.  
+  
+  Lock, G.S.H., 1994, Latent Heat Transfer, Oxford Science Publications, Oxford University, Oxford, UK. 
Current revision as of 09:17, 7 July 2010
When liquid drops are sprayed onto a hot surface, heat conduction causes the liquid to superheat and evaporate into a gas (see figure). The cooling capacity of the process depends on the time required for an averagesized drop to cool. If the shape of the droplet can be assumed to be hemispherical during the evaporation process, the energy balance at the interface can be written as

where r_{I} is the radius of the droplet. Equation (1) can be simplified as

Analytical solution of eq. (2) is very difficult because the temperature distribution in the liquid droplet is twodimensional in nature. A scale analysis similar to that in Lock (1994) is presented here to estimate the time required for droplet with an initial radius of R_{i} to evaporate completely.
The scale of the radius of the droplet, r_{I}, is R_{i}. Thus the scale of the temperature gradient at the interface is

The scale analysis of eq. (2) yields

which can be rearranged as

Since the liquid droplet is very small, is very small, so the second term on the righthand side of eq. (4) is much smaller than the first. Equation (4) can be simplified by neglecting the second term on the righthand side, i.e.,

The physical significance of eq. (6) is that the latent heat of evaporation is balanced primarily by conduction in the liquid droplet, while the effect of convection on the surface of the droplet is negligible.
The time that it takes to completely evaporate the droplet with an initial radius of R_{i} is therefore estimated by

For the cases where the substrate heat flux beneath the droplet, q''_{w}, is known, eq. (6) should be rewritten in terms of heat flux. The scale of the heat flux at the heating surface is

Combining eqs. (7) and (8) yields

which indicates that a smaller drop will provide a larger cooling effect.
While eqs. (7) and (9) provide the order of magnitude of the time required to completely evaporate the droplet, quantitative estimation of the evaporation time is often also desirable. A simple approximate analysis will be done below by estimating the conduction in the liquid droplet by the following correlation:

where and are the average crosssectional area of heat conduction and the average path length of the conduction, respectively. For a hemispherical droplet, the contact area between the droplet and the heated wall is and the interfacial area of the droplet is . Thus, we can take the average conduction area as

The average path length for conduction is

Therefore, the conduction in the liquid droplet becomes

Replacing the first term on the righthand side of eq. (2) with eq. (13), and dropping the second term on the righthand side of eq. (2) (see the above scale analysis), the energy balance for the hemispherical droplet becomes

which can be rearranged as

which is subject to the following initial conditions:

Integrating eq. (15) and considering its initial condition, eq. (16), one obtains the transient radius of the liquid droplet:

The time required for the droplet to evaporate completely can be obtained by letting r_{I} in eq. (17) equal zero, i.e.,

which agrees with the results obtained by scale analysis, eq. (17).
The above analysis is otherwise simplistic because it assumes that the shape of the droplet is hemispherical. In fact, the shape of the droplet depends on the velocity with which it impacts the wall as well as the wettability of the liquid droplet on the wall. If the contact area between the droplet and the wall is larger (due to higher impacting velocity or good wettability), the time for conduction through the liquid is shorter and the life of the drop will be shorter as well.
References
Faghri, A., and Zhang, Y., 2006, Transport Phenomena in Multiphase Systems, Elsevier, Burlington, MA
Faghri, A., Zhang, Y., and Howell, J. R., 2010, Advanced Heat and Mass Transfer, Global Digital Press, Columbia, MO.
Lock, G.S.H., 1994, Latent Heat Transfer, Oxford Science Publications, Oxford University, Oxford, UK.