Roger wrote:

> In a message dated 9/23/2001 12:15:37 AM Eastern Daylight Time, 

> Frank: My process is quite similar to Ole Bobs. So what I've observed during 
> the production of HVAC CS should be relevant to your earlier suggestions. I 
> run my process until the conductivity of the water gets so high that the 
> combined ionized air resistance plus that of the water is too low for my 
> power supply to continue operating at its 30 ma internal set point. So 
> basically the product I get **already represents** the maximum total silver 
> obtainable. However, the silver concentration is limited by conductivity 
> constraints, not ionic silver precipitation. In fact, if I were to change the 
> physical configuration of my setup, I don't see any reason why I couldn't 
> continue producing CS. However, I'd need a longer tank which I don't have. 
> Roger 
> 
I am not convinced that the power limit of your power supply is related to the 
ionic silver saturation of your solution. That is why I suggested running 
until the solution can hold no more ionic silver and it is forced out in the 
form of the large flat particles. I have done this type of saturation test 
here (long ago) using pure water, not with any CO2 added.

I do not beleive you need a longer tank.

Perhaps you might consider altering your setup so that it can continue to 
ionize the silver electrodes. If you are using a standard NST for HV, the 
secondary is current is limited by a magnet shunt in the core, so as the 
conductivity of the solution increases, the secondary voltage starts to drop. 
You can let the voltage go as low as it wants without harming the transformer.
Many times we have run a 15KV unit down until the secondary voltage was below 
1KV.

Is this the sort of technical discussion that is no longer desired on this list?


frank key


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