Method and apparatus for hydrogen production in an absorber liquid by electrochemical of coal and water

I claim a combination of processes as a single process for use with coal or carbon dust and their particulates and their electro-chemical reaction with water for the express purpose of producing hydrogen;

• consisting of:
• reducing coal or carbon to particles smaller than 500 micron or as small as practical,
• blending the coal or carbon dust with water to produce a ten percent to eighty percent coal slurry (by weight),
• introducing the coal (carbon) slurry to a slurry supply reservoir under superatmospheric pressure,
• transferring the coal (carbon)/slurry through a heater or heat exchanger, increasing its temperature, then
• passing the coal (carbon) slurry through electrolyte cell conductor tubes or retaining devices which both mixes the slurry and intermitantly passes a gaseous absorber liquid therein controlling the velocity of both liquids across the anode and across the cathode electrode, thus depolarizing the electrodes
• in an electro-chemical cell which by nonmiscible physical and gravity separation keeps separated the coal (carbon) slurry from the absorber liquid, as well as free gases of CO.sub.2 and H.sub.2,
• the carbon dioxide (CO.sub.2) pregnant absorber liquid and frees CO.sub.2 at the anode,
• the hydrogen (H.sub.2) pregnant absorber liquid, and frees H.sub.2 at the cathode,
• recycling the spent coal (carbon)/slurry from both the anode and cathode back to the coal (carbon)/water slurry reservoir,
• at the same time removing the absorber liquid pregnant with CO.sub.2 absorbed at the anode from the electrolysis system to the CO.sub.2 stripper, and the absorber liquid pregnant with H.sub.2 stripper, then
• reducing the operating pressure within both the CO.sub.2 and H.sub.2 stripper causing effervescence and thus release of both CO.sub.2 and H.sub.2 respectively, and their individual recovery,
• recycling the gases freed absorber liquid from both strippers back to the electrolytic cell "conductor" tubes,
• recovering the CO.sub.2 for use or disposal to atmosphere from both electrolytic cell at anode and CO.sub.2 stripper,
• recovering the H.sub.2 for use from both electrolytic cell at cathode, and stripper.