The United States of America As Represented by the Administrator of the U.S. Environmental Protection Agency

Amerol Enterprises, LLC

Valerii Kukhar

Subhas K Sikdar

Rajender S Varma

Viktor Burdeynyy

Yurii Besugly

Svitlana Melnykova

Nataliia Khimach

Vladislav Kyselov

Rayisa Korzh

Yurii Kyselov

Dmytro Kamens'kyh

Volodymir Kashkovski

Valeriy Bortyshevskyy

Method for deep desulphurization of hydrocarbon fuels includes following steps: (1) treatment of a hydrocarbon fuel under the condition of its mixing with gaseous oxidant selected from the group consisting nitrogen monoxide, dry air, ozone and a mixture of at least two of said reagents in order to oxidize sulfur-containing compounds presented in said fuel, and with a fine-dispersed adsorbent based on montmorillonite in order to adsorb oxidized sulfur-containing compounds, and (2) separation of spent adsorbent together with adsorbed oxidized sulfur-containing compounds from refined fuel.

Method for deep desulphurization of hydrocarbon fuels

A method and apparatus for the generation of synthetic motor fuels and additives to oil fuels, C-Calcohols, hydrogen, methane, synthesized gas (H+CO) by hydrothermal treatment of carbonaceous compounds by providing a two-stage carbon gasification process operated under the supercritical conditions of HO and CO, including a first stage gasification reactor having a reaction zone for the conversion of carbonaceous compounds and a second stage reactor for the conversion of the products of the first stage reactor; feeding a aqueous suspension of carbonaceous compound in an amount of at least 30% by weight and an alkali metal or alkaline-earth metal catalyst or reactive OH-species from an electrolyzer through said first stage gasification reactor as a supercritical fluid at a volume velocity of 0.01-0.05 g of carbon per 1 cmper hour, at a carbon/catalyst mole ratio of between about 70/1 and 90/1, at a temperature of 390-450&#xb0; C., and under a pressure of about 225 to 500 bars; feeding the reaction products from the first stage reactor to the second stage reactor over a copper-zinc catalyst at the temperature of 200-280&#xb0; C. and under a pressure of at least about 100 bars so that any gases generated in the first stage are converted into C-Calcohols with the weight ratio of C-Cto C-Cbetween about 0-35% to 100-65%.

Process for generation of synthetic fuel from carbonaceus substances

Growing community of inventors

Kyiv, Ukraine

Valerii Kukhar