Articles for Hife-Pipe Jacket Heat Transfer
Does anyone have any good articles they could send me on vessel jacket heat transfer (dimple, half-jacket, conventional, etc).
RJB, I do not have any articles about what you are asking about, but the
 major differences between the three types of jackets are 1) Surface 
Area and 2) Turbulence within the jacket and 3) the amount of "dead 
flow" within each of the three types of systems.
While Dimple and
 conventional (which I believe you mean tank inside of tank 
construction/ball valve), you have maximized your heating surface area.  You have 
better turbulence with dimple obviously and less of a chance of dead 
flow.  
With Half-Pipe jackets, you have no chance of dead flow 
areas, but you limit your heating surface area because you need space 
between the welds.  This is a very crude way to jacket a tank and I 
would not recommend it to anyone.
So, of the three, Dimple jacketing is the best method in my opinion.
If
 you are looking for another type of jacket for a tank, I would suggest 
looking into ControTrace.  It is an external heating jacket that has a 
lot of engineering behind it. 
The thread referenced by EGT01 will give you all you need to know about 
the heat transfer coefficients, but I would like to comment on a 
practical point.
A very important difference between the 
different types of jacketing methods (but which was not listed by 
perdog) is that they have very different abilities to withstand pressure
 external to the shell. A half pipe jacket will take a relatively high 
pressure, whereas an anular jacket will require a very thick shell to 
withstand the external pressure because of the larger unsupported areas.
 
I recently saw a tank destroyed because the operator left the 
jacket's cooling water return valve closed and just the pressure of the 
cooling water buckled the shell beyond repair. You can also have 
problems if the jacket is isolated and then a hot liquid is added to the
 tank. This can cause expansion or phase change in the jacket, leading 
to massive pressures. Always install relief valves if this is a risk.
I
 have used half pipe (and even angle irons) as external coils quite 
successfully, but with low heat transfer coefficients and high pressure 
drops.  But they can be broken down into several parallel circuits.
I
 have also used dimpled jackets on low pressure refigerated water duties
 where we were simply maintaining the temperature (no actual cooling). 
The dimples aid turbulence, and the welds in each dimple give extra 
stability to the shell for the external pressure.
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