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HYDRODRIVE

SYNTHESIZER FOR MOLECULAR ENGINEERING

HELPING

ECONOMICAL HYDROGEN PRODUCTION ENABLING  ENERGY SAVINGS.

By

Dr. Paul De Vadder, Belgium.

ENTRANCE PRESSURE OF H₂O:

35 bar. iso-choric process, followed by iso-thermal before  molecular dissociation.

THERMAL CONSUMPTION:

800W/Kg for heat exchanger one,

160W/Kg for the second heating.

90W for the thirst heating.

But, with the loses of the quenching = 15%, we have: 920 W/Kg, 192 W/Kg; 108 W/Kg.

Or,

the real thermal total is: 1.220 W/Kg.

By this, the UV lighting keeps: 327W/Kg  for a speedy dissociation & the plasma forming keeps 420 W/Kg .

Thus general total:1980 W/Kg are for the production of 1 Kg H+…and   O--, or a  positive COP… for hydrogen thermal uses (maximum efficiency) if we use the most modern techniques to generate a cold plasma with the Hydrodrive Synthesizer for Molecular Engineering !.

Water has 4,412 KW/Kg in equilibrium formation energy.

If decomposed in ortho hydrogen form, this will give even a little more= 5.650W/Kg.,

But, in this case and because of the risk of potential formation of H₃O, IT IS ABSOLUTE NECESSITY to use an appropriate opto- catalyst

and to accelerate the decomposition by combined action of light and plasma to prevent the recombination.

Thus in the best case, we have: 5.650 W/Kg.,

Note1:

With classic electrolyte, we would use an average of 3.800 KW/Kg for 4,415 KW/Kg water  because of thermal loses

Note 2.

The proposed hybrid technique of plasma & catalyst has been tested daily 12 hours/day from 11 06 08 to 02 07.09 by Dr.Paul De Vadder in Europe Laboratories.

WHAT IS TODAY THE REVOLUTIONARY INPUT IN THE PROCESS?. 

In our case, we will use our “False Super Heating Pump”.

We will generate more energy kept from the ambient, converted into electricity and will improve more this process.

Thus, in really, we will consume 8 times lower primary basic energy for this process (COP 1 to 9).

Thus in finality, we need from the production line of the electricity 247 W/ Kg basic electricity which many times lower than 3,5 W/L hybrid gas or 1W for 0,6L hybrid gas in our developed process (1.65W/L).

Today, this will be canceled in:1W=> 14,85 L of hybrid gas)… in all circumstances (Doesn’t depend of the type of engine).

CONCLUSION:

For the “100MW”, we will need with the molecular association of the gases of oil seeds, 1.8 T/H oleaginous seeds (Prudently 2T) and 4.8 T/H water consumption and we would have to use 233 KW/H primary energy for the hydrogen generation…. Could anyone do better & Cheaper?.

CONSUMPTIONS FOR A UNIT OF 5 MW GAS TURBINE:

for a consumption of: 480 L/H water & 180 Kg /H seeds + 39KW to extract temperature out of the ambient for the primary energy that will generate the hydrogen as against in 5MW: 676 Kg/H seeds, without the H+ auxiliaries.