IPC분류정보
국가/구분 |
United States(US) Patent
등록
|
국제특허분류(IPC7판) |
|
출원번호 |
US-0290069
(2011-11-05)
|
등록번호 |
US-8512215
(2013-08-20)
|
발명자
/ 주소 |
|
출원인 / 주소 |
|
대리인 / 주소 |
|
인용정보 |
피인용 횟수 :
0 인용 특허 :
29 |
초록
▼
A waste transformation and destruction apparatus includes a natural gas ignition system, a silica material bed, a heat transfer device, and a system for collecting plasma produced energy. A reaction formed by heat from ignition, carbon from the waste material, supercritical water, —OH radicals, and
A waste transformation and destruction apparatus includes a natural gas ignition system, a silica material bed, a heat transfer device, and a system for collecting plasma produced energy. A reaction formed by heat from ignition, carbon from the waste material, supercritical water, —OH radicals, and muons released from the silica bed transform the waste into a fuel. This fuel is more efficiently consumed by the complete combustion process resulting in near total elimination of the waste, increased energy production, and virtually no emissions.
대표청구항
▼
1. A method for destroying medical waste and/or converting organic materials into thermal energy and/or electrical energy, the method comprising: providing a reactor comprising: a reaction chamber;a heat source in communication with the reaction chamber;an air source fluidly coupled with the reactio
1. A method for destroying medical waste and/or converting organic materials into thermal energy and/or electrical energy, the method comprising: providing a reactor comprising: a reaction chamber;a heat source in communication with the reaction chamber;an air source fluidly coupled with the reaction chamber;a catalytic media located within the reaction chamber so as to receive heat from the heat source and airflow from the air source; andan opening through the reaction chamber through which medical waste and/or organic material can be introduced into the reaction chamber;introducing heat and airflow into the reaction chamber so as to heat the reaction chamber to a first desired temperature;introducing medical waste and/or organic material into the reaction chamber and converting the medical waste and/or organic material into a fuel within the reaction chamber in the presence of the catalytic media, the fuel producing its own heat within the reaction chamber; andshutting off heat from the heat source while maintaining airflow to the reaction chamber, the heat from the fuel continuing to heat the reaction chamber so as to reach or maintain a second desired temperature that is the same or greater than the first temperature. 2. The method of claim 1, wherein the reaction chamber has a cross-sectional dimension of from about 1 feet to about 100 feet. 3. The method of claim 1, wherein the catalytic media within the reaction chamber includes a bed of particles that produce reactive species within the reaction chamber. 4. The method of claim 3, wherein the particles are selected from silica sand, silica gel, hydroxylbastnasite, alumina, and combinations thereof. 5. The method of claim 3, further comprising forming a monomolecular film on an interior surface of the reaction chamber. 6. The method of claim 5, the monomolecular film on the interior surface of the reaction chamber enhancing formation of hydroxyl radicals, supercritical water, muons and/or other reactive species within the reaction chamber. 7. The method of claim 1, wherein the medical waste and/or organic material comprises at least one member selected from the group consisting of organic waste, coal, fossil fuels, biomass, municipal waste, biological waste, cells, viruses, bacteria, severed tissue, blood, corpses, and combinations thereof. 8. The method of claim 1, further comprising introducing additional heat to the reaction chamber from the heat source if the temperature within the reaction chamber drops below a predetermined minimum temperature. 9. The method of claim 1, wherein the airflow includes unheated air. 10. The method of claim 1, further comprising: providing a heat exchanger element thermally coupled with the reaction chamber;passing a heat exchanger fluid through the heat exchanger element so that heat produced within the reaction chamber heats the heat exchanger fluid; andgenerating electricity from the heated heat exchanger fluid. 11. The method of claim 10, wherein electricity is generated from a steam generator thermally coupled with the heat exchanger element. 12. The method of claim 1, further comprising: causing or allowing a plasma reaction to occur in the reaction chamber; andproducing electrical energy from the plasma reaction. 13. The method of claim 1, further comprising generating inert inorganic sterile materials from the medical waste and/or organic material. 14. The method of claim 1, wherein converting medical waste and/or organic material comprises reducing and eliminating pollutants from diesel exhaust and increasing efficiency and output of a diesel engine. 15. The method of claim 1, wherein converting medical waste and/or organic material comprises reducing and eliminating pollutants and emissions from and increasing efficiency of a coal fired electrical generation system. 16. The method of claim 1, wherein converting medical waste and/or organic material comprises reducing and eliminating pollutants and emissions from a commercial waste incineration system. 17. The method of claim 1, further comprising forming a monomolecular film on at least one substrate in communication with the reaction chamber. 18. The method of claim 17, wherein the at least one substrate is selected from the group consisting of tools, electrical transmission wires, aircraft wing surface, and munitions. 19. The method of claim 17, the monomolecular film comprising a semiconductor material. 20. The method of claim 19, wherein the semiconductor material is suitable for use in making microprocessors, computer chips, transistors, or photovoltaic solar cells. 21. The method of claim 20, the method forming a semiconductor chip comprising: the substrate; anda single layer of the monomolecular nano film comprised of aligned carbon molecules having dimensions of 30 angstroms by 50 angstroms and that elongate to 70 angstroms at high pressure resulting in substantial increase in temperature resistance and operating capabilities. 22. A method for converting organic materials into thermal and electrical energy, the method comprising: providing a reactor comprising: a reaction chamber;a heat source in communication with the reaction chamber;an air source fluidly coupled with the reaction chamber;a catalytic media located within the reaction chamber so as to receive heat from the heat source and airflow from the air source; andan opening through the reaction chamber through which medical waste and/or organic material can be introduced into the reaction chamber;introducing heat and airflow into the reaction chamber so as to heat the reaction chamber to a first desired temperature;introducing organic material into the reaction chamber and converting the organic material into a fuel within the reaction chamber in the presence of the catalytic media, the fuel producing its own heat within the reaction chamber;shutting off heat from the heat source while maintaining airflow to the reaction chamber, the heat from the fuel continuing to heat the reaction chamber so as to reach or maintain a second desired temperature that is the same or greater than the first temperature; andproducing or collecting electrical energy. 23. The method of claim 22, wherein producing or collecting electrical energy comprises: providing a heat exchanger element thermally coupled with the reaction chamber;passing a heat exchanger fluid through the heat exchanger element so that heat produced within the reaction chamber heats the heat exchanger fluid; andgenerating electricity from the heated heat exchanger fluid. 24. The method of claim 22, wherein producing or collecting electrical energy comprises: causing or allowing a plasma reaction to occur in the reaction chamber; andcollecting electrical energy from the plasma reaction. 25. A method for converting organic materials into thermal energy and, the method comprising: providing a reactor comprising: a reaction chamber;a heat source in communication with the reaction chamber;an air source fluidly coupled with the reaction chamber;a catalytic media located within the reaction chamber so as to receive heat from the heat source and airflow from the air source; andan opening through the reaction chamber through which medical waste and/or organic material can be introduced into the reaction chamber;introducing heat and airflow into the reaction chamber so as to heat the reaction chamber to a first desired temperature;introducing organic material into the reaction chamber and converting the organic material into a fuel within the reaction chamber in the presence of the catalytic media, the fuel producing its own heat within the reaction chamber;shutting off heat from the heat source while maintaining airflow to the reaction chamber, the heat from the fuel continuing to heat the reaction chamber so as to reach or maintain a second desired temperature that is the same or greater than the first temperature; andproviding a monomolecular film on at least one substrate in communication with the reaction chamber, the monomolecular film comprising a semiconductor material. 26. The method of claim 25, wherein the semiconductor material comprises comprising: the substrate; anda single layer of the monomolecular nano film comprised of aligned carbon molecules having dimensions of 30 angstroms by 50 angstroms and that elongate to 70 angstroms at high pressure resulting in substantial increase in temperature resistance and operating capabilities.
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