favourablejnr
Industrial
- May 5, 2003
- 1
Hello,
Before I begin, I am a manufacturing engineer. I am providing some assistance to a friend to redesign his operations. I am not proficient in thermodynamics, fluid mechanics or heat transfer (but I can re-read my old texts, etc.). In its most basic sense, I am attempting to redesign a batch processing system to a continuous processing system.
Here is the issue: I am trying to design a system that applies hot water (90 degC) to an aluminium object (c.c. 2kg with dimensions 500mm x 400mm x 50mm - this object is not solid) initially at ambient temperature so that the aluminium object is heated to 90 degC.
A simple solution is to submerge the aluminium object in a bath of heated water, then remove (current batch process). I need the heating process to be continuous and envisage the aluminium objects traversing a conveying system. Above the traversing objects is a system that either sprays or deluges the passing objects with the hot water.
Imagine a 4m long conveyor, travelling at 2 m/min on which the objects are placed. The objective is to infeed the ambient temperature objects and outfeed the objects at 90 degC. The 4m length is a preliminary guess based on initial experimentation that requires the objects to be submerged in hot water (90 degC) for 120 secs. I am interpreting the required submersion time as time required for the object to be in contact with the hot water.
Though 120 secs exceeds the calculable time for heating an aluminium object of this mass from ambient to 90 degc, it is relevant for this task due to other considerations (i.e the objects are covered in contaminants.)
I do not know how to determine the heat loss for the proposed water application system. I expect that it will be far less efficient than submersion. There is information available for spray cooling (which I have yet to review in any detail), but I have not readily found information about spray heating or the temperature effects of a deluge system.
There may be some parallels with fire protection systems designs.
I am expecting that the conveyor length will need to be greater than the simple calculation used to determine the length suggested above, due to the (expected) inefficiency of heat transfer from the hot water manifolds (maybe we could call them taps) compared to submersion.
If a manifold could be efficiently designed that provided flowing hot water (90 degC) over an area of 4000mm x 500mm, then I would be confident that each object is getting hot water applied to it for 120 secs. My preference is to minimise the manifold size (i.e. vastly less than 4000mm x 500mm).
The idea is that the water will be recycled (i.e. collected after application, cleaned, re-heated and returned to the manifold arrangement).
The water flow rate is also an open question, and may be intimately connected with the heat transfer question here.
Any pointers, guidance or suggestions will be appreciated.
Thanks, Alex
Before I begin, I am a manufacturing engineer. I am providing some assistance to a friend to redesign his operations. I am not proficient in thermodynamics, fluid mechanics or heat transfer (but I can re-read my old texts, etc.). In its most basic sense, I am attempting to redesign a batch processing system to a continuous processing system.
Here is the issue: I am trying to design a system that applies hot water (90 degC) to an aluminium object (c.c. 2kg with dimensions 500mm x 400mm x 50mm - this object is not solid) initially at ambient temperature so that the aluminium object is heated to 90 degC.
A simple solution is to submerge the aluminium object in a bath of heated water, then remove (current batch process). I need the heating process to be continuous and envisage the aluminium objects traversing a conveying system. Above the traversing objects is a system that either sprays or deluges the passing objects with the hot water.
Imagine a 4m long conveyor, travelling at 2 m/min on which the objects are placed. The objective is to infeed the ambient temperature objects and outfeed the objects at 90 degC. The 4m length is a preliminary guess based on initial experimentation that requires the objects to be submerged in hot water (90 degC) for 120 secs. I am interpreting the required submersion time as time required for the object to be in contact with the hot water.
Though 120 secs exceeds the calculable time for heating an aluminium object of this mass from ambient to 90 degc, it is relevant for this task due to other considerations (i.e the objects are covered in contaminants.)
I do not know how to determine the heat loss for the proposed water application system. I expect that it will be far less efficient than submersion. There is information available for spray cooling (which I have yet to review in any detail), but I have not readily found information about spray heating or the temperature effects of a deluge system.
There may be some parallels with fire protection systems designs.
I am expecting that the conveyor length will need to be greater than the simple calculation used to determine the length suggested above, due to the (expected) inefficiency of heat transfer from the hot water manifolds (maybe we could call them taps) compared to submersion.
If a manifold could be efficiently designed that provided flowing hot water (90 degC) over an area of 4000mm x 500mm, then I would be confident that each object is getting hot water applied to it for 120 secs. My preference is to minimise the manifold size (i.e. vastly less than 4000mm x 500mm).
The idea is that the water will be recycled (i.e. collected after application, cleaned, re-heated and returned to the manifold arrangement).
The water flow rate is also an open question, and may be intimately connected with the heat transfer question here.
Any pointers, guidance or suggestions will be appreciated.
Thanks, Alex