Means for temperature control of heated surfaces

Claim 2

A heat sink structure including a heated surface and further including a heat exchange surface on the interior surface thereof, said structure providing means for enclosing said heat exchange surface in a fluid tight manner and including means for providing a flow of fluid to remove heat from said heat exchange surface, said heat sink structure having at least one of a variable wall thickness separating said heated surface from said fluid cooled surface and a variable distribution of heat flux on said heated surface, the improvement wherein said fluid cooled heat exchange surface includes: means, disposed on said fluid cooled heat exchange surface in a variable manner commensurate with said variable wall thickness and said variable distribution of heat flux such that an approximately uniform temperature is achieved over said heated surface

Claim 3

In the apparatus of claim 1 the further improvement wherein said means comprises material of lower thermal conductivity than that of said heat sink structure.

Claim 4

In the apparatus of claim 2 the further improvement wherein said material of lower thermal conductivity is deposited in variable thickness on said fluid cooled heat exchange surface in such manner as to be responsive to said variations in said wall thickness and heat flux such that an approximately uniform surface temperature is achieved on said heated surface

Claim 5

A heat sink structure including a heated surface and including a heat exchange surface on the interior surface thereof, said structure providing means for enclosing said heat exchange surface in a liquid tight manner and including means for providing a flow of coolant liquid to remove heat from said heat exchange surface by nucleate boiling, said heat sink structure having at least one of a variable wall thickness separating said heated surface from said liquid cooled surface and a variable distribution of heat flux on said heated surface, said liquid cooled heated surface further includes: means, disposed on said heat exchange surface for forming pressure gradients in said liquid having a component perpendicular to said heat exchange surface without substantially impeding the relative velocity between said heat exchange surface and said Liquid, said component having a magnitude directly proportional to the square of the relative velocity between said heat exchange surface and said liquid, to facilitate removal of nucleate bubbles, the improvement wherein said liquid cooled heat exchange surface includes: means, disposed on said liquid cooled heat exchange surface in a variable manner commensurate with said variable wall thickness and said variable distribution of heat flux such that an approximately uniform temperature is achieved over said heated surface.

Claim 6

A heat sink structure including a heated surface and including a heat exchange surface on the interior surface thereof, said structure providing means for enclosing said heat exchange surface in a liquid tight manner and including means for providing a flow of coolant liquid to remove heat from said heat exchange surface by nucleate boiling, said heat sink structure having at least one of a variable wall thickness separating said heated surface from said liquid cooled surface and a variable distribution of heat flux on said heated surface, said liquid cooled heated surface further includes: means, disposed on said heat exchange surface for forming pressure gradients in said liquid having a component perpendicular to said heat exchange surface without substantially impeding the relative velocity between said heat exchange surface and said Liquid, said component having a magnitude directly proportional to the square of the relative velocity between said heat exchange surface and said liquid, to facilitate removal of nucleate bubbles, the improvement wherein said liquid cooled heat exchange surface includes: means, disposed on said liquid cooled heat exchange surface in a variable manner commensurate with said variable wall thickness and said variable distribution of heat flux such that an approximately uniform temperature is achieved over said heated surface.

Claim 7

In the apparatus of claim 4 the further improvement wherein said means comprises material of lower thermal conductivity than that of said heat sink structure.

Claim 8

In the apparatus of claim 5 the further improvement wherein said material of lower thermal conductivity is deposited in variable thickness on said liquid cooled heat exchange surface in such manner as to be responsive to said variations in said wall thickness and heat flux such that an approximately uniform surface temperature is achieved on said heated surface.

Claim 9

In the apparatus of claim 6 the further improvement wherein the interior surface of said heat sink structure contains one or more adjacent periodic curves across substantially the width of said structure and extending substantially the length of said structure and wherein a liquid coolant diverter is structured in close proximity to said heat exchange surface to provide predetermined liquid flow conditions at said anode heat exchange surface.

Claim 10

In the apparatus of claim 7 the further improvement wherein each said period or curve is provided with ducting for the alternate injection and removal of said liquid coolant.

Claim 11

In the apparatus of claim 8 the further improvement wherein said heat exchange surface is prepared with means disposed on said heat exchange surface for forming nucleate bubbles of predetermined size and distribution to thereby increase heat flux.

Claim 12

In the apparatus of claim 9 the further improvement wherein said means comprises cavities and said cavities have dimensions in the range of 0.002 mm to 0.2 mm, and said cavities being spaced apart on said heat exchange surface a distance ranging from 0.03 mm to 3 mm whereby more efficient heat transfer is obtained.

Claim 13

In the apparatus of claim 10 the further improvement wherein said heat exchange surface is further prepared with roughness said roughness having heights ranging from 0.0001" to 0.008" above said heat exchange surface whereby the viscous sublayer may be broken up.

Claim 14

In the apparatus of claim 10 the further improvement whereby the inside surface of said cavities are prepared with micro cavities the dimensions of said micro cavities being in the range of 1×10 -2 mm to 1×10 -4 mm.

Claim 15

In the apparatus of claim 4 the further improvement wherein said liquid coolant is introduced at approximately its boiling point.