This is a lot of good work, Alan.  I am amazed at the number of high
quality posts on Vortex.  I am having trouble keeping up because each
post warrants a good deal of thought. 

I examined pictures of the manifold and created a diagram to capture the
important features.  [I made a small .png version of the diagram that I
am trying to include.]   I am not sure it is schematically correct yet.
A characteristic that I believe is very important in the analysis of the
possible temperature contamination is the issue of the fittings used in
the manifold.  These use pipe threads, and appear to be NPT because of
the use of pipe dope.  At each junction of pipe threads, there will be a
large thermal resistance compared to continuous brass.  Analysis of
these across-the-thread resistances are going to be hard, particularly
with pipe dope and or Teflon tape present as is required to seal NPT.
The resistance across the thread boundaries will be high and the net
effect will be to significantly decouple the Tout thermocouple from the
manifold. 

These thread boundary effects don't appear to be included in your model.

If the 35kB .png of the diagram I created doesn't make it through the
thread, email me and I will send it to you direct.

Regards,  Bob Higgins

-----Original Message-----
From: Alan J Fletcher [mailto:a...@well.com] 
Sent: Wednesday, October 26, 2011 6:49 PM

I have built a SPICE circuit simulation model of the manifold --- and 
the results are VERY BAD !!!!

An initial small-scale model  indicates that the ENTIRE top of the 
manifold is "contaminated" by the HOT side.

Even with a "stepped" manifold (representing the various pipe 
fittings) , and with the thermocouple at the END of the tube, I get a 
10 C ERROR !!!!!

My preliminary results are at : 
http://lenr.qumbu.com/rossi_ecat_oct11_spice.php

I can make a more accurate model with Spice, but a Finite Element 
Model is clearly needed.


<<attachment: ExchangerManifold_sm.png>>

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