APPARATUSES AND METHODS FOR CARBON DIOXIDE CAPTURING AND ELECTRICAL ENERGY PRODUCING SYSTEM
20210376413 · 2021-12-02
Inventors
Cpc classification
Y02P20/133
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
H10N10/13
ELECTRICITY
Y02B90/10
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
Y02E60/36
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
H01M2250/402
ELECTRICITY
F02C6/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Y02P20/10
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
H01M16/003
ELECTRICITY
C25B1/34
CHEMISTRY; METALLURGY
F05D2220/76
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02C7/12
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F05D2260/61
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
H10N10/00
ELECTRICITY
Y02E60/50
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
C25B15/081
CHEMISTRY; METALLURGY
Y02P20/129
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
International classification
H01M16/00
ELECTRICITY
F01D15/10
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
The present invention is an integrated system of a carbon dioxide capturing processes from the atmosphere and producing electrical energy from the integrated system.
The objective of the current invention is; capturing carbon dioxide from the air through the tree fashioned carbon dioxide capturing system and generating electric power through the integrated systems. To generate electric power at maximum efficiency, and capture carbon dioxide, the present invention comprises different integrated processes, integrated systems, and techniques. The present system comprises; an ionized and non-ionized hydrogen gas turbine system unit, carbon dioxide capturing tree system unit, a hybrid thermoelectric-generator and solid oxide fuel cell system unit, a hybrid hydrogen-chlorine fuel cell and carbon dioxide reactor core system unit.
Furthermore to capture carbon dioxide and generate electric power, the present invention comprises various other alternative embodiments.
Claims
1. A method and apparatus of carbon dioxide capturing and electrical energy producing system and comprising; (a) a non-ionized hydrogen gas turbine unit; to generating electric power from hydrogen and oxygen gases, (b) an ionized hydrogen gas turbine unit; to generating electric power from ionized hydrogen and oxygen gases, (c) a hybrid thermoelectric-generator and solid oxide fuel cell unit; for cogenerating electrical power from hydrogen-oxygen solid oxide fuel cell and from waste heat which released from a solid oxide fuel cell (d) a tree fashioned carbon dioxide capturing unit (e) a hybrid solar hydrogen-Oxygen gas generator system unit is; to produce uninterrupted hydrogen gas and oxygen gas and to feeding hydrogen gas to the other parts of the present system (f) an electrolysis of brine unit: for producing sodium hydroxide to carbon dioxide reactor core, and for producing hydrogen and chlorine gases for hybrid hydrogen-chlorine fuel cell and carbon dioxide reactor core system unit (g) a hybrid hydrogen-chlorine fuel cell and carbon dioxide reactor core system unit; for generating electrical power from output chlorine gas, and to powered carbon dioxide reactor core by hydrogen chlorine fuel cell, and to converting carbon dioxide gas into carbonate outputs, and to reduce the consumption of electrical power by carbon dioxide reactor core, and (h) a waste recovery system unit; to utilize the energy of exhaust heat from hydrogen gas turbine, solid oxide fuel cell, hydrogen-chlorine fuel cell, and carbon dioxide reactor core, and the waste heat recovery system unit is used to recover waste heat, and utilized to drive an additional steam turbine and generate additional electric power.
2. The apparatus carbon dioxide capturing and electrical energy producing system of claim 1, wherein the ionized hydrogen gas turbine system unit comprising; (a) a resonant cavity; to ionize and to increase energy the level of oxygen and hydrogen gases through high voltage and laser energy stimulation, and to create high thermal explosive energy in the combustion; and wherein the hydrogen and oxygen gases resonant cavities are installed with the combustion of the hydrogen gas turbine, and the gas resonant cavity means the hydrogen and oxygen gases ionized and stimulated in two different resonant cavities, and the ionized hydrogen and oxygen gases flow into combustion and become to contact and ignited in the combustion, (b) a gas mixing regulator; to mixes the oxygen gas with non-combustion ambient gases and to control the temperature in the combustion of ionized hydrogen gas turbine, and wherein the gas mixing regulator adapted with oxygen and ambient air gas pipes and mixing such gases at the desired ratio and the mixed gases flow to combustion, (c) a temperature sensor; for continual feedback signals and control of the temperature in the combustion of ionized hydrogen gas turbine, and wherein the temperature sensor is adapted in the combustion and sends a continuous signal to automatic hydrogen gas controller, to create stable temperature in combustion, (d) a pressure sensor; for continual feedback signals and control pressure in the ionized gas turbine, (e) an automatic hydrogen gas flow controller; for receiving feedback signals from the temperature sensor and for controlling hydrogen gas flow rate and for adjusting combustion temperature, and wherein an automatic hydrogen gas flow controller connected with hydrogen gas pipe and controlling the flow rate of hydrogen gas to combustion; and (f) a compressor
3. The hydrogen gas turbine system of claim 2, wherein the gas resonant cavity ionizes and stimulates the hydrogen and oxygen gases, and the apparatus at least comprising; (a) a light or lather sources; the light emitting diodes are installed in the resonant cavity tube and are arranged in a cluster-array provides and emits a narrow band of ultraviolet ray light energy into the voltage stimulated hydrogen gas, and oxygen gas, the absorbed laser energy or electromagnetic energy by hydrogen and oxygen gases causes many atoms to lose electrons while highly energizing the liberated combustible gas ions before and during thermal gas-ignition, and (b) a high voltage plates: adapted in the resonant cavity tube and are arranged in negative and positive polarities; and the hydrogen and oxygen gases exposing to the high voltage plates and the gases passing through the gas resonant cavity, at higher voltage of positive and negative plates, and causes more electrons to be pulled away or dislodged from the gas atoms, and the absorbed laser energy deflects the electrons away from the gas atom nucleus during voltage-pulse off-time; and wherein the resonant cavity further comprising the high voltage circuit and connected to the negative and positive plates, and wherein the high voltage circuit produces more than 15 kilovolts and the produced high voltage is supplied to the resonant cavity to ionize the gases, and the recurring positive voltage zone attracts the liberated negative electrically charged electrons to positive voltage plate, and while, at the same time, the negative electrical voltage potential plate attracts the positive electrical charged nucleus, and finally the ionized hydrogen and oxygen gases ignited in the combustion through thermal sparks and causes to releasing thermal explosive energy, and the thermal explosive energy drives the turbine.
4. The apparatus of electrical energy generating system from ionized hydrogen gas turbine system of claim 2, comprising at least the processes and steps of: i. producing sodium hydroxide from brine electrolysis, ii. utilizing sodium hydroxide and producing hydrogen and oxygen gases from a hydrogen-oxygen generator, iii. regulating hydrogen, regulating oxygen and non-combustion ambient gases, iv. ionizing oxygen and hydrogen gases in the resonant cavities, and flows the ionized gases into the combustor, v. burning ionized hydrogen atom with an ionized oxygen atom and ambient gases in combustion, and vi. thereby generating a source of super high temperature gas, and driving one or more gas turbines with the super high temperature gas to generate electrical power or to drive a shaft for some useful.
5. The carbon dioxide capturing and electrical energy producing system of claim 1, wherein the non-ionized hydrogen gas turbine system unit is the other alternative embodiment to generate electric power from hydrogen and oxygen gases, and the system at least comprising; (a) a gas mixing regulator; to mixes the oxygen gas with non-combustion ambient gases and to control the temperature in the combustion, (b) a temperature sensor; for continual feedback signals and control of the temperature in the combustion, (c) a pressure sensor; for continual feedback signals and control pressure in the gas turbine, and (d) an automatic hydrogen gas flow controller; for receiving feedback signals from the temperature sensor and for controlling hydrogen gas flow rate and for adjusting combustion temperature, and wherein the automatic hydrogen gas flow controller adapted with hydrogen gas pipe and controlling the flow rate of hydrogen gas to combustion.
6. The apparatus of generating electric energy from ionized and non-ionized hydrogen gas turbine system of claim 2, and claim 5 works with integration of other units of the capturing carbon dioxide and producing electrical energy system, and the ionized and non-ionized hydrogen gas turbine system units at least integrated with the; (a) hybrid solar hydrogen-oxygen fuel cell unit; to produce hydrogen and oxygen gases for ionized and non-ionized hydrogen gas turbine system units, (b) waste heat recovery system unit: to convert exhaust waste heat from ionized and non-ionized hydrogen gas turbine system units, and to generate additional electric power, and (c) carbon dioxide reactor core unit; to utilize exhaust waste heat from ionized and non-ionized hydrogen gas turbine system units and to increase carbon dioxide absorbing rate.
7. The method and apparatuses of generating power from non-ionized hydrogen gas turbine system claim 11 at comprising the steps and process of: i. producing sodium hydroxide from brine electrolysis, ii. by using sodium hydroxide, producing hydrogen and oxygen from hydrogen-oxygen generator, iii. regulating hydrogen, regulating oxygen and non-combustion ambient gases, and iv. directly flowing hydrogen gases into the combustor and burning hydrogen gas with oxygen and ambient air, and v. thereby generating a source of high temperature gas, driving one or more gas turbines with the high temperature gas to generate electrical power or to drive a shaft for some useful.
8. The carbon dioxide capturing and electrical energy producing system of claim 1, wherein the hybrid thermoelectric-generator and solid oxide fuel cell unit comprising; (a) a solid oxide fuel cell: to generate electric power based on a chemical reaction between hydrogen fuel and oxidizer oxygen or ambient air, and the solid oxide fuel cell also generates a high temperature of heat energy as a byproduct of the chemical reaction and the average waste heat temperature from solid oxide fuel cell is at least from 500 C.° to 1200 C.°, and the high-temperature waste heat utilizes to generate electrical energy from thermoelectric generator system, and wherein the solid oxide fuel cell produces waste heat energy byproducts and the waste heat energy further utilizes for; i. a carbon dioxide capturing system unit; to increase the carbon dioxide absorbing rate on the system, and ii. a waste heat recovery unit; to generate electric power; and further, the solid oxide fuel cell connected and coupled with the carbon dioxide capturing system unit and waste heat recovery unit, and (b) a thermoelectric generator: generates electric power by routing exhaust waste heat from the solid oxide fuel cell, and the exhaust waste heat inter into a hot side of the thermoelectric generator and routing cold intake gases from the ambient air into a cold side of the thermoelectric generator and the thermoelectric generator produces electric energy based on a heat flux differences across the thermoelectric electrodes; and wherein the thermoelectric generator and solid oxide fuel cell are geometrically, electrically and mechanically coupled to generate electric power at maximum thermodynamics efficiencies.
9. The carbon dioxide capturing and electrical energy producing system of claim 1, wherein the hybrid thermoelectric-generator and solid oxide fuel cell unit comprising the process and steps of: i. producing sodium hydroxide from brine electrolysis, ii. by using sodium hydroxide producing hydrogen and oxygen gases from the hydrogen-oxygen generator, iii. routing hydrogen and oxygen gases to solid oxide fuel cell and generate electric power and heat energy, and iv. routing the waste heat released from solid oxide fuel cell into the hot side of the thermoelectric generator and routing cold intake gases from the ambient air into a cold side and generate additional electrical energy from waste heat.
10. The carbon dioxide capturing and electrical energy producing system of claim 1 comprises a carbon dioxide capturing unit for extracting and capturing carbon dioxide from the atmosphere or flue gas, and the physical structure and shape of a carbon dioxide capturing system unit is fashioned as a tree structure, and the tree fashioned carbon dioxide capturing system unit at least comprises; (a) a fans; in the ergonomics of the tree fans are adapted in the leaves, to absorb carbon dioxide and ambient gases from the atmosphere, (b) an exhaust waste heat-based heater; the carbon dioxide absorbing part, and regeneration part utilizes exhausted waste heat which relisted from hybrid thermoelectric generator solid oxide fuel cell unit and waste heat released from hydrogen gas turbine unit, and wherein the heat-absorbing system fitted on the external surface of the absorbing part and regeneration part, and wherein the tree fashioned carbon dioxide capturing system unit is mechanically coupled and integrated with hydrogen gas turbine and hybrid thermoelectric solid oxide fuel cell system units, and wherein the used output waste heat from carbon dioxide absorbing part and regeneration part returned into the waste heat recovery system unit, (c) an absorbing part: absorb carbon dioxide through the solvents, sorbents, or adsorbents system; and wherein the carbon dioxide absorber part adapted in the branches and trunk of the tree fashioned system, and the absorber part comprises sorbents, adsorbents or solvents, (d) a carbon dioxide solvents, sorbents, adsorbents chemicals: the absorbing part utilizes liquid solvents, solid sorbents, or adsorbents to absorb and separate carbon dioxide from the atmosphere or flue gas, and the chemicals are mounted on the absorbing part of the system, and wherein the carbon dioxide separator part further utilizes a membrane method to capture carbon dioxide from the air or flue gas, (e) a regeneration part; the reached carbon dioxide solvents, sorbents, or adsorbents from absorbing part flows into the regenerator part and heat up, and carbon dioxide gas is produced, and solvents, sorbents, or adsorbents also produced for reuse, and wherein the regeneration part is mounted in the trunk of the tree fashioned system, and (f) a base of the tree; in the ergonomics of the tree at least carbon dioxide tankers, pumps, and controllers are mounted in the base of the tree; and wherein the base of the tree is coupled and connected with the upper level of the tree fashioned system, and wherein the tree fashioned carbon dioxide capturing system unit further comprising; a circulation pumps, stripper, carbon dioxide pumps, and carbon dioxide tankers.
11. The tree fashioned carbon dioxide capturing system unit claim 10 wherein the carbon dioxide absorbing part and regenerating part utilizes exhausted waste heat, and increase the temperature of the gases, sorbents, adsorbents, and solvents, and increase the carbon dioxide absorption rate in the system; and wherein the tree fashioned carbon dioxide capturing system unit is powered by the internally generated electric power from; the hydrogen gas turbine unit, and hybrid thermoelectric generator solid oxide fuel cell and waste heat recovery generator, and wherein the tree fashioned carbon dioxide capturing system is at least electrically and mechanically coupled and integrated with the hydrogen gas turbine unit, hybrid thermoelectric solid oxide fuel cell unit, and waste heat recovery generator unit.
12. The tree fashioned carbon dioxide capturing system unit claim 10 comprises at least the process and steps of; i. by using the fans which adapted on the leaves of the fashioned carbon dioxide capturing tree, sucking atmospheric gases from the atmosphere, the carbon dioxide capturing is from flue gas, the flue gases directly flow into the carbon dioxide absorber part ii. heating-up the atmospheric gases in the fashioned carbon dioxide capturing tree iii. flowing the hot atmospheric gases into carbon dioxide absorber part, and absorb carbon dioxide in the fashioned carbon dioxide capturing tree iv. flowing the carbon dioxide reached solvents, sorbents or adsorbents into regeneration part in the fashioned carbon dioxide capturing tree, and v. heating the carbon dioxide reached solvents, sorbents or adsorbents and produces carbon dioxide and regenerate solvents, sorbents or adsorbents for re-use, in the fashioned carbon dioxide capturing tree.
13. The carbon dioxide capturing and electrical energy producing system of claim 1, wherein the hybrid solar hydrogen-oxygen gas generator system unit produces hydrogen and oxygen gases, and the system comprising; (a) a solar powered hydrogen-oxygen gas generator; functioning with the integration of solar cells, and utilizes solar energy, and based on the electrolysis method it produces hydrogen and oxygen gases from the hydrogen-oxygen generator, and feeding hydrogen and oxygen gases to the hydrogen gas turbine unit and utilizes to startup the carbon dioxide capturing and electrical energy producing system, and wherein the solar powered hydrogen-oxygen gas generator further produces hydrogen and oxygen gases and stores in the tankers and utilizes as backup and startup for the hydrogen gas turbine, wherein a solar powered hydrogen-oxygen gas generator and the solar systems are physically and electrically integrated, to generate hydrogen and oxygen gases from solar energy, and (b) an internally powered hydrogen-oxygen gas generator; functioning with the integration of solid oxide fuel cell, thermoelectric generator, and hydrogen gas turbine, and utilizes electrical energy generated from solid oxide fuel cell, thermoelectric generator or hydrogen gas turbine, and powering the other hydrogen-oxygen gas generator cells and produce hydrogen and oxygen gases based on the electrolysis method, and feeding uninterrupted hydrogen and oxygen gases to hydrogen gas turbine and solid oxide fuel cell, and further the hydrogen gas feeding to the hydrogen-chlorine fuel cell; and wherein said hydrogen-oxygen gas generator system produces hydrogen and oxygen gases to the whole system, and the hydrogen-oxygen gas generator system at least comprises: an alkali chemical: the electrolysis utilizes alkali chemicals such as sodium hydroxide, potassium hydroxide, and other alkali bases, and an integrated sources of power, and wherein said hydrogen-oxygen gas generator system powered from two sources of energy; some of the hydrogen-oxygen gas generator cells are powered from solar energy and utilizes to produce for backup and reserving hydrogen gas, and and the rest of the hydrogen-oxygen gas generator cells are powered from internal generated electric power from thermoelectric generator solid oxide fuel cell unit, and hydrogen gas turbine unit, and produces enough amount of hydrogen and oxygen gases for the carbon dioxide capturing and electrical energy producing system,
14. The hybrid solar hydrogen-oxygen gas generator system unit claim 13 the system works with integrating of other units of the carbon dioxide capturing and electrical energy producing system units, and at least integrated with the; (a) hydrogen gas turbine unit: utilize hydrogen and oxygen gases which produced in the hybrid solar hydrogen-oxygen gas generator system unit, and generate electrical power from hydrogen gas turbine unit, (b) hybrid thermoelectric generator solid oxide fuel cell unit; utilizes hydrogen and oxygen gases from the hybrid solar hydrogen-oxygen gas generator system unit, and generate electric power and heat energy through the solid oxide fuel cell, and (c) electrolysis of brine unit: to generate hydrogen and oxygen gases, the hybrid solar hydrogen-oxygen gas generator system unit utilizes sodium hydroxide from the electrolysis of the brine unit.
15. The hybrid solar hydrogen-oxygen gas generator system unit claim 13 the system works with integrating of other units of the carbon dioxide capturing and electrical energy producing system units, and at least integrated with the; (a) hydrogen gas turbine unit: utilize hydrogen and oxygen gases which produced in the hybrid solar hydrogen-oxygen gas generator system unit, and generate electrical power from hydrogen gas turbine unit, (b) hybrid thermoelectric generator solid oxide fuel cell unit; utilizes hydrogen and oxygen gases from the hybrid solar hydrogen-oxygen gas generator system unit, and generate electric power and heat energy through the solid oxide fuel cell, and (c) electrolysis of brine unit: to generate hydrogen and oxygen gases, the hybrid solar hydrogen-oxygen gas generator system unit utilizes sodium hydroxide from the electrolysis of the brine unit, and wherein the hybrid solar hydrogen-oxygen gas generator system unit at least comprises the processes and steps of: i. producing electrical energy from solar and powering hydrogen-oxygen gas generator, ii. producing hydrogen and oxygen gases from hydrogen-oxygen generator, by using electrolysis of sodium hydroxide or other alkali bases, iii. storing energy in the form of hydrogen, iv. routing hydrogen and oxygen gases to hydrogen gas turbine and start the operation and produce electric power from the system, v. storing and distributing electric power, and vi. powering the rest of hydrogen-oxygen gas generator cells and produce enough amount of hydrogen and oxygen gases and continuing the operation of the system.
16. The carbon dioxide capturing and electrical energy producing system of claim 1 wherein said hybrid hydrogen-chlorine fuel cell and carbon dioxide reactor core system unit comprising; (a) a hydrogen chlorine fuel cell; mounted and integrated with reactor core, and generating electrical power from hydrogen and chlorine gas, and utilized to powering carbon dioxide reactor core by hydrogen chlorine fuel cell, and it reduces the consumption of electrical energy by carbon dioxide reactor core, and wherein the hydrogen chlorine fuel cell system that utilizes hydrogen as a fuel and chlorine gas as an oxidant, and the chlorine and hydrogen supplied respectively through the anode and cathode gas diffusion, and the system converts chemical energy into electrical energy, and the generated power utilized to power and operate the carbon dioxide reactor core, and wherein the hydrogen chlorine fuel cell system releases hydrogen chloride gas byproduct, and further, the hydrogen chloride gas reacts with water and is converted into hydrochloric acid, and the system cogenerates electrical energy and hydrochloric acid, and (b) a carbon dioxide reactor core system; converts carbon dioxide into carbonate and bicarbonate byproducts, and the system at least comprising; i. a high-pressure compressing system; to increase the pressure in the reactor core and to increase the reaction between carbon dioxide with an alkali base, ii. a concentrated lather or ray emitters system; to emit radiation to the carbon dioxide and alkali base, and carbon dioxide molecules are exposed to concentrated radiations, the carbon dioxide molecule bonds become vibrate and the kinetic energy of carbon dioxide molecule bonds increase and the system creates to increase the reaction rate of carbon dioxide with alkali base increase, and wherein concentrated radiation emitters adapted in the head of compressing piston, and comprises radiation controlling system and diode housing, and the automatic controlling system receive signal and operate the opening and clothing, and wherein concentrated radiation emitters are light emitting diodes, and the light emitting diode emits light, and to concentrate the light, the concave lenses are fitted on it, and iii. a heat absorbing system; some amount of waste heat exhausted from hydrogen gas turbine is directed into heat absorbing system, wherein the external part of the carbon dioxide reactor core, and the waste heat is circulated into the body of the reactor core and heat is absorbed by heat absorbing system, creates to increase the temperature inside of the reactor core, finally the system utilized to increase the reaction rate of carbon dioxide with sodium hydroxide or alkali base, and wherein said heat absorber system fashioned to circulate hot gas and the hot waste gas circulating in the prepared lines of the body of reactor core, and heat absorbs by the reactor core, and wherein the heat-absorbing system fitted on the external surface of the reactor core.
17. The carbon dioxide reactor core system claim 16 wherein the high-pressure compressing system installed in the top of the reactor and the system at least comprises; (a) an integrated automatic controlling system; utilizes at least to control compressing piston systems and pressure sensors, (b) a compressing piston; is adapted in the head of the reactor core, and (c) an automatic controlling system; receives a signal from pressure sensors and control the operation of the compressing system; and wherein the carbon dioxide reactor core system comprises a method to increase mass transfer and to increase kinetic collisions of carbon dioxide with sodium hydroxide, and the system further comprises different methods; such as spraying sodium hydroxide solution over carbon dioxide, in the reactor core, or bubbling carbon dioxide method; and wherein the hybrid hydrogen chlorine fuel cell and carbon dioxide reactor core system unit converts carbon dioxide into carbonate and bicarbonate byproducts, and at least comprising the processes and steps of; i. collecting chlorine and hydrogen gas from the electrolysis of sodium chloride, ii. producing electric power from hydrogen-chlorine fuel cell, powering the carbon dioxide reactor core, iii. capturing carbon dioxide from the atmosphere or flue gas and storing in the tankers iv. pumping carbon dioxide gas into carbon dioxide reactor core, v. pumping sodium hydroxide solution or alkali base into the reactor core, and spraying over the carbon dioxide, and vi. converting carbon dioxide to carbonate and bicarbonate products.
18. The hybrid hydrogen-chlorine fuel cell and carbon dioxide reactor core system unit claim 16 comprises the other alternative embodiment of carbon dioxide reactor core and the other alternative embodiment system comprises; (a) the heat-absorbing system; some amount of waste heat exhausted from the steam turbine is directed into the heat-absorbing system, wherein the external part of the carbon dioxide reactor core, and the waste heat is circulated into the body of the reactor core, and heat is absorbed by the heat-absorbing system, creates to increase the temperature inside of the reactor core, finally the system utilized to increase the reaction rate of carbon dioxide with sodium hydroxide, wherein the heat-absorbing system fitted on the external surface of the carbon dioxide reactor core, (b) the hydrogen chlorine fuel cell; system that utilizes hydrogen as a fuel and chlorine gas as an oxidant, and generates electric power wherein the hydrogen chlorine fuel cell integrated and coupled with the carbon dioxide reactor core (c) the carbon dioxide reactor core: comprises a sprayer, and spraying sodium hydroxide solution over carbon dioxide gas, in the reactor core, and the system converts into carbonates and bicarbonate byproducts; and wherein the other alternative embodiment of carbon dioxide reactor core comprising a sodium hydroxide or alkali base sprayer: and the sprayer is mounted on the top of the reactor core and spray sodium hydroxide or alkali base solution over the carbon dioxide zone.
19. The carbon dioxide capturing and electrical energy producing system of claim 1 wherein said waste heat recovery unit utilizes exhaust waste heat which released from hydrogen gas turbine, solid oxide fuel cell, hydrogen-chlorine fuel cell, carbon dioxide capturing unit and from carbon dioxide reactor core, and the waste heat recovery system unit used to recovered waste heat and utilized to drive an additional steam turbine and generate additional electric power, and the waste heat recovery system at least comprising; (a) a waste heat recovery generator; to recover waste heat exhausted from hydrogen gas turbine, solid oxide fuel cell, hydrogen-chlorine fuel cell, carbon dioxide capturing unit and from carbon dioxide reactor core, and wherein said waste heat recovery generator produce steams from exhausted waste heat and the produced steam flows into hydrogen-oxygen superheater, and wherein said waste heat recovery generator has a duct for receiving hot exhaust gas from hydrogen gas turbine, solid oxide fuel cell, hydrogen-chlorine fuel cell, carbon dioxide capturing unit, and from carbon dioxide reactor core, and the waste heat recovery steam generator is also associated with a heating system for receiving feed water for heating to steam and producing steam, (b) a hydrogen oxygen superheater; to re-heat the recovered steam and to produce high pressurized steam, and wherein the hydrogen-oxygen superheater system at least comprises; (a) an ignition system; for burning hydrogen and oxygen directly into the steam and creating superheat steam, and wherein the ignition system is mounted in a steam line for burning hydrogen and oxygen directly in the steam flowing through the superheater zone, thus increasing the temperature of such steam, (b) a hydrogen and oxygen gas supply lines; to supply hydrogen and oxygen to superheater zone (c) a hydrogen and oxygen flow rate regulator; to control the flow rate of hydrogen and oxygen gases, and to control the burning temperature in the superheater zone, and wherein the hydrogen and oxygen flow rate regulator receives a continuous signal from the temperature sensor to control the burning temperature in the superheater zone and to control the temperature of the steam (d) a temperature sensing device; is mounted in the superheater zone and utilized to feed continuous signals to the hydrogen and oxygen gas regulators and controllers and to position the hydrogen and oxygen gas valves to maintain the desired value; and wherein the hydrogen-oxygen superheater increases the temperature of the incoming steam to the desired value and the high temperature pressurized steam turned into the steam turbine and the steam turbine drives the electric generator and produce electric power, and (c) a steam turbine; to utilize the recovered waste steam and to drives the electric generator and it produces additional electric power; and wherein the waste heat recovery system unit comprises the other alternative hydrogen-oxygen superheater system, and the system comprising; burner, steam flowing pipe, ignition system, hydrogen and oxygen gas lines, hydrogen gas flow regulator, oxygen flow rate regulator, and temperature sensor; and wherein the other alternative embodiment of the hydrogen-oxygen superheater the hydrogen and oxygen gases burned over the steam containing pipes and the volume and pressure of the steam inside the pipe increased,
20. The waste heat recovery system unit claim 21 collects waste heat from carbon dioxide capturing and electrical energy system and converts into electrical energy, and the system comprising at least the process and steps of; (a) collecting waste heat exhausted from hydrogen gas turbine, solid oxide fuel cell, hydrogen-chlorine fuel cell, and carbon dioxide reactor core, (b) turning the collected waste heat into waste heat recovery steam generator, and the waste heat steam generator produce steams from exhausted waste heat, and the produced steam flows to hydrogen-oxygen superheater system, and (c) through the hydrogen-oxygen superheater, burning hydrogen and oxygen gases directly in the steam line and reheat the steam and produce high pressurized steam, the high pressure, and temperature steam flow into the steam turbine and the steam turbine drives the electric generator and produces additional electric power.
21. The carbon dioxide and electrical energy producing system claim 1 comprises the other alternative embodiments one, for alternative producing electric power and capturing carbon dioxide from the system, and the arrangements and integrations of the system at least comprising; (a) the non-ionized hydrogen gas turbine unit; to generate electric power (b) the hybrid solar hydrogen-oxygen gas generator unit; to produce hydrogen and oxygen gases for hydrogen gas turbine, (c) the tree fashioned carbon dioxide capturing unit: to capture carbon dioxide from the atmosphere (d) the waste heat recovery system unit; to recover waste heat released from non-ionized hydrogen gas turbine unit (e) the brine electrolysis unit; to produce sodium hydroxide for tree fashioned carbon dioxide capturing unite and for hybrid solar hydrogen-oxygen gas generator unit, and (f) the hydrogen chlorine fuel cell: to convert exhausted chlorine gas and hydrogen into electric power and hydrochloric acid.
22. The other alternative embodiment one, claim 21 wherein the tree fashioned carbon dioxide capturing system sucking atmospheric gases and directly converted carbon dioxide into carbonate and bicarbonate products, and the system at least comprising; (a) the fans; to absorb carbon dioxide and ambient gases from the atmosphere in the ergonomics of the tree fashioned carbon dioxide capturing system unit wherein the fans are adapted in the leaves of the tree fashioned, (b) the absorber part; in the tree fashioned system, carbon dioxide absorber parts are adapted in the branches and trunk, and the branches and trunk of the tree fashioned are hollow tubes, and the sprayers are adapted on the top of the tubes to spry sodium hydroxide or potassium hydroxide over the hot atmospheric gases, and inside of the tubes, carbon dioxide gases and sodium hydroxide or potassium hydroxide are intermixing together, (c) a vertical circular helical tube: in the ergonomics of the tree, the carbon dioxide absorbing performs in the vertical circular helical tube and mounted in the trunk tree fashioned system, and the carbon dioxide gas and sodium hydroxide or potassium hydroxide flows together inside of the vertical helical tube, and converted into carbonates; and due to the temperature and the structure of the vertical helical tube the absorption rate of carbon dioxide increase, and the carbonates and bicarbonates product accumulated in the base of the trunk, and (d) the base of the tree fashioned; at least the base of the tree fashioned comprises; carbonate and bicarbonate tankers and circulation pumps, and controllers; and wherein the tree fashioned carbon dioxide capturing system utilizes waste heat to increase the absorption of carbon dioxide, and the waste heat is pumped from hydrogen gas turbine, and the waste heat flows through the tubes in the branches and vertical helical tube wherein the trunk fashioned tree; and wherein the heat-absorbing system fitted on the external surface of the absorbing part of the branches and vertical helical tube, and wherein the another alternative embodiment one of carbon dioxide capturing and energy producing system, at least comprises the steps of; (a) producing hydrogen and oxygen gases from hybrid solar hydrogen-oxygen gas generator (b) by utilizing hydrogen and oxygen gases, producing electric power from non-ionized hydrogen gas turbine (c) producing sodium hydroxide, hydrogen, and chlorine through brine electrolysis (d) providing hydrogen and chlorine gases, and producing electric power from hydrogen-chlorine fuel cell, and (e) sucking atmospheric gases through the tree fashioned carbon dioxide capturing system unit; and to absorb carbon dioxide the system utilizes sodium hydroxide or potassium hydroxide, and directly converting into carbonate and bicarbonate products through the tree fashioned carbon dioxide capturing system unit.
23. The carbon dioxide and electrical energy producing system claim 1 comprises the other alternative embodiment two, for alternative producing electric power and capturing carbon dioxide from the system, and at least comprising; (a) the hybrid solar hydrogen and oxygen gas generator unit (b) the non-ionized hydrogen gas turbine unit, and (c) the tree fashioned carbon dioxide capturing unite; and the fans, the absorber part, the vertical circular tube, the base of the tree fashioned system, the waste heat, pumps, controllers, carbonate and bicarbonate tankers, and alkali base sprayer are further utilized in the other alternative embodiment two of the carbon dioxide capturing and energy producing system arrangements; and wherein the other alternative embodiment two of the carbon dioxide capturing and electrical energy producing system at least comprising the processes and steps of; (a) producing hydrogen and oxygen gases from hybrid solar hydrogen-oxygen gas generator (b) by utilizing hydrogen and oxygen gases, and producing electric power from non-ionized hydrogen gas turbine, and (c) sucking atmospheric gases through the tree fashioned carbon dioxide capturing system unit and directly converts carbon dioxide into carbonate and bicarbonate products.
24. The carbon dioxide and electrical energy producing system claim 1 comprises the other alternative embodiment three, for alternative producing electric power and capturing carbon dioxide from the system, and the system at least comprising; hybrid solar hydrogen and oxygen gas generator unit, fuel cell unit, and tree fashioned carbon dioxide capturing unit; and the fans, the absorber part, the vertical circular tube, the base of the tree fashioned system, carbonate and bicarbonate tankers, pumps, controllers, and alkali base sprayer, further utilized in the other alternative embodiment three of the carbon dioxide capturing and energy producing system arrangements; and wherein the other alternative embodiment three of the carbon dioxide capturing and energy producing system, the hydrogen-oxygen generator unit and the fuel cells unit are adapted on the base of the carbon dioxide capturing tree, and the solar cells are adapted in the top of the tree fashioned carbon dioxide capturing, beside the fans; and wherein the other alternative embodiment three of the carbon dioxide capturing and energy producing system at least comprising the processes and steps of; (a) utilizing solar power and producing hydrogen and oxygen gases from the hydrogen-oxygen gas generator (b) by utilizing hydrogen and oxygen gases, producing electric power from fuel cells, and powering tree fashioned carbon dioxide capturing system unit (c) sucking atmospheric gases through the tree fashioned carbon dioxide capturing system unit, and absorbing carbon dioxide through sodium hydroxide or potassium hydroxide, and directly converting into carbonate and bicarbonate products.
25. The carbon dioxide capturing and electrical energy producing system of claim 1 wherein the hydrogen gas turbine unit, hybrid thermoelectric-generator solid oxide fuel cell unit, solar hybrid hydrogen-oxygen gas generator system unit, hybrid hydrogen chlorine fuel cell and carbon dioxide reactor core unit, and waste recovery system units are physically, electrically, and mechanically coupled and integrated to perform the carbon dioxide capturing and electrical energy producing process from the system.
Description
BRIEF DESCRIPTION OF THE DRAWING
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DETAILED DESCRIPTIONS OF THE INVENTION
[0070] The current invention relates to the apparatuses and methods for capturing carbon dioxide and generating electrical power and the integrated system comprises the unit systems of; [0071] (a) non-ionized hydrogen gas turbine unit; to generating electric power from hydrogen and oxygen gases, [0072] (b) Ionized hydrogen gas turbine unit; to generating electric power from ionized hydrogen and oxygen gases, [0073] (c) hybrid thermoelectric-generator and solid oxide fuel cell unit; for cogenerating electrical power from hydrogen-oxygen solid oxide fuel cell and from waste heat which released from the solid oxide fuel cell [0074] (d) tree fashioned carbon dioxide capturing unit; to extracting and capturing carbon dioxide from the atmosphere, and the physical structure of the carbon dioxide capturing system unit is fashioned as a tree structure. [0075] (e) hybrid solar hydrogen-Oxygen gas generator system unit is; to produce uninterrupted hydrogen gas and oxygen gas, and to feeding hydrogen gas to the other parts of the present invention. [0076] (f) Electrolysis of brine unit: for producing sodium hydroxide to carbon dioxide reactor core, and for producing hydrogen and chlorine gases for hybrid hydrogen-chlorine fuel cell and carbon dioxide reactor core system unit [0077] (g) hybrid hydrogen-chlorine fuel cell and carbon dioxide reactor core system unit; for generating electrical power from output chlorine gas, and to powered carbon dioxide reactor core by hydrogen chlorine fuel cell, and to converting Co2 gas into carbonate outputs, and to reduce the consumption of electrical power by carbon dioxide reactor core. [0078] (h) a waste recovery system unit; to utilize the energy of exhaust heat from hydrogen gas turbine, solid oxide fuel cell, hydrogen-chlorine fuel cell, and from carbon dioxide reactor core. The waste heat recovery system unit uses to recover waste heat, and utilized to drive an additional steam turbine, and generate additional electric power.
Hydrogen Gas Turbine Unit;
A. Ionized Hydrogen Gas Turbine Unit;
[0079] In the one embodiment of the present invention, the carbon dioxide capturing and electric power generating system comprises the ionized gas turbine unit system for generating electric power from ionized hydrogen and oxygen. And the ionized gas turbine unit system at least comprises; hydrogen gas and oxygen gas sources, automatic hydrogen gas regulator, oxygen and ambient gases mixing regulator, hydrogen and oxygen resonant cavity, temperature sensor, pressure sensor, compressor, turbine, combustor, and electric generator. In the embodiment of the present invention, a gas turbine utilizes as hydrogen gas turbine, and to control the combustion rate and to increase the efficiency of hydrogen gas turbine the above certain parts are connected and integrated with it.
[0080] The ionized gas turbine system unit the oxygen and hydrogen gases are ionized before the gases flow to the combustor. The oxygen and hydrogen gases ionized in the resonant cavity 15 as illustrated in
[0081] As illustrated in
[0082] In the embodiment of
[0083] The absorbed Laser Energy (Electromagnetic Energy) by hydrogen gas
[0084] The exposing the displaced and moving combustible gas atoms passing through Gas Resonant Cavity 15 at higher voltage levels plates 41 & 48 causes more electrons to be “pulled away” or “dislodged” from the gas atoms, as illustrated in
[0085] Electron Extraction system
[0086] The absorbed Laser energy 40 weakens the “Electrical Bond” between the orbital electrons and the nucleus of the atoms; while, at the same time, electrical attraction-force, being stronger than “Normal” due to the lack of covalent electrons. “Locks Onto” and “Keeps” the hydrogen electrons. These “abnormal” or “unstable” conditions cause the combustible gas ions to overcompensate and breakdown into thermal explosive energy. By simply attenuating or varying voltage amplitude in direct relationship to voltage pulse-rate determines Atomic Power-Yield under the controlled state.
[0087] In combustion 16 high thermal explosive energy is released. As maintained above, exposing hydrogen and oxygen gases separately into two different resonant cavities to laser energy and high voltage potential causes to increase the output energy level in the combustion. Finally, combustible gas ions ignited in the combustion through thermal sparks and causes releasing thermal explosive energy beyond the gas-flame Stage, and the thermal explosive energy 46 flows to the turbine, as illustrated in
The Hydrogen, Oxygen, and Non-Combustible Gas Injection Process
[0088] As illustrated
[0089] In terms of operational performance, the non-burnable gas “restricts” the speed of the burning-rate hydrogen atoms and the oxygen atom in the combustion. The “gas restricting process” is, of course applicable to any type or combination of burnable gases or burnable gas mixture.
The Gas Mixing Regulator and Flame Temperature Adjuster
[0090] In both embodiments of non-ionized hydrogen gas turbine system unit
[0091] Fundamentally, the hydrogen gas turbine allows the “Burn-Rate” of hydrogen to be “Changed” or “adjusted” from 325 cm/sec to 42 cm/sec, and the combustion temperature adjusted from 1000 to 5000 degree f, but not limited. The combustion temperature adjusted and fixed at a suitable temperature of the combustion turbine 16. The gas flame-temperature remains constant with the constant gas flow-rate of the combustion gases. Temperature sensor 7 is mounted in the combustion, and pressure sensor 6 also mounted in the gas turbine to give feedback for “automatic hydrogen gas flow controller 14, and finally to control the burning rate of the hydrogen. Continual the feedback and control of the temperature in the combustion and the pressure in the gas turbine is, hereinafter, called “The Gas Combustion Stabilization Process” creates uniform combustion temperature. As illustrated
[0092] Thereafter the automatic hydrogen gas flow controller 14, controls the flow rate of hydrogen gas and controls the burring rate and regulates the out power of the hydrogen gas tribune. Automatically, the gas “Combustion Stabilization Process” changes the “Burn-Rate” of the hydrogen gases and obtaining the favourite gas-flame temperature. When the amount of hydrogen flow to the combustion increase, the burning-rate increase, and the amount of temperature in the combustion increase, and the pressure in gas turbine also increase. The amount of hydrogen gas flow is directly proportional to the burning-rate.
[0093] In other embodiment, to control the burning-rate of hydrogen in the combustion the Gas-Mixing regulator 9 system mixes the oxygen gas 10, with non-combustion ambient gases. The “gas-Mixing Regulator 9 fitted in the outer top of oxygen gas and ambient gas cylinders. The “Gas-Mixing Regulator” 9 mixes non-combustion ambient gases with the desired amount of oxygen gases, and the mixed gases finally supplied to combustion. And the mixed gases burn with hydrogen gas in the combustion. The “gas-mixing regulator works with integration of temperature sensor, pressure sensor, and automatic hydrogen gas regulator. Based on the continuous feedback from the temperature sensor, pressure sensor, and automatic hydrogen gas regulator, the gas mixing regulator 9 mixes the desired amount of oxygen 10 with non-combustible ambient gases. When the amount of oxygen in the mixed gas is higher, the burning-rate also increases. The amount of oxygen in the mixed gas is directly proportional to the burning-rate. This system supplies a uniform gas-mixture to combustion 9, and it plays a vital role in hydrogen burning-rate regulation.
[0094] The ionized hydrogen gas turbine
[0099] The generated electric power from this system utilizes for external output electric energy supplies and for running the internal systems of the carbon dioxide capturing process.
[0100] As illustrated in
B. Non-Ionized Hydrogen Gas Turbine Unit
[0105] The carbon dioxide capturing and electrical energy producing system invention comprising non-ionized hydrogen gas turbine system unit
[0106] Hydrogen is combusted into oxygen to generate extremely high temperature gas. The hydrogen is produced from both brine electrolysis 30 and from hydrogen-oxygen generator
[0107] By feeding the combustion generated gas 46 directly into gas turbine 19, unprecedented high conversional efficiency of electricity is achieved, and the generated electric power utilized for carbon dioxide capturing process and for output power commercialization.
[0108] As illustrated in
[0109] Instead of ionized hydrogen gas turbine the other alternative embodiment utilizes a non-ionized hydrogen gas turbine as illustrated in
[0110] In the other alternative embodiment of non-ionized hydrogen gas turbine uses directly hydrogen and oxygen gases as illustrated in
Hybrid Thermoelectric-Generator Solid Oxide Fuel Cell Unit
[0114] A carbon dioxide capturing and electrical energy producing system comprises a “hybrid thermoelectric generator and solid oxide fuel cell system” as illustrated in
[0115] In the current embodiment
[0116] The thermoelectric generator 27 generates electric power by routing exhaust waste heat 57 from the solid oxide fuel cell 26. The exhaust waste heat inters into a hot side of the thermoelectric generator and routing cold intake gases from the ambient air into a cold side of the thermoelectric generator as illustrated in
[0117] In summery the hybrid of solid oxide fuel cell and thermoelectric generator system
[0118] furthermore, routing the reset waste heat 65 which released from solid oxide fuel cell 26 directed into waste heat recovery system in 39, and waste heat recovery system creates hot steam, and utilized to drive an additional steam turbine, and produce additional electrical energy waste heat.
Hybrid Solar Hydrogen-Oxygen Gas Generator System Unit
[0119] As illustrated in
[0120] The main objective of the Hybrid Solar hydrogen-Oxygen gas generator system unit is; to produce uninterrupted hydrogen gas and oxygen gas, and to feeding hydrogen gas to the other parts of the system.
[0121] To start-up, the system, some cells of hydrogen-Oxygen gas generators 24 are powered by solar energy 21 to produce initial hydrogen and oxygen gases. And the rest cells of hydrogen-Oxygen gas generators 5 are powered from internal sources of electrical energy 28 as shown in
[0122] The importance of the “Hybrid Solar hydrogen-Oxygen gas generator system” is to reserve energy to start-up the system, or for start-up “Co2 capturing and electrical energy producing system”. The operation of the invention utilizes start-up energy from solar 21; the solar energy powers to hydrogen-oxygen gases generator 24 to produces hydrogen and oxygen gases. Some “hydrogen-Oxygen gas generator cells” 24 are powered by solar energy and the hydrogen-Oxygen gas generators produce hydrogen 22 and oxygen 23 gases. The produced hydrogen and oxygen gases are stored in the hydrogen tanks 11 and oxygen gas tanks 10 respectively. When the “Co2 capturing and electrical energy producing system” needs to start-up the system; it utilizes the stored hydrogen and oxygen gases from the tankers 10 & 11. And the hydrogen gas turbine 19 utilizes the stored hydrogen and oxygen gases to start the production of electric power. And the produced electrical energy utilizes; a) to operate the rest of hydrogen-oxygen gas generator cells 5 and produce more hydrogen and oxygen gases, b) to operate the other systems of “Co2 capturing and electrical energy producing system”. Furthermore, electric power is produced from one or more hydrogen gas turbines. The power utilizes for output commercial purposes. Likewise, the present invention produces megawatts of electric power and the present system uses as a power plant.
[0123] To produce hydrogen and oxygen gases through the “Hybrid Solar hydrogen-Oxygen gas generator system”
[0124] The solar hybrid hydrogen-oxygen gas generator system, produces hydrogen and oxygen gases from water. By the method of electrolysis, the water molecules split into hydrogen and oxygen gases. As illustrated in
[0125] In this embodiment, the sodium hydroxide base 31 which produced in the electrolysis of brine unit 31 utilizes for a dual purpose; one is utilized for carbon dioxide reactor core unit 33 or for tree fashioned Co2 capturing system unit 38 to converting carbon dioxide into useful carbonate products, and the second is utilizes for electrolysis to produce hydrogen and oxygen gases from water 6 & 24. Therefore, the sodium hydroxide base utilizes for hydrogen-oxygen gas generator 6& 24 to generate hydrogen and oxygen gases. Lastly, Hydrogen and oxygen gases stored in hydrogen tanks 11 and oxygen tanks 10 and utilizes to produce electrical energy through the gas turbine system 19. The hydrogen and oxygen gases utilize to operate solid oxide fuel cells and uses to run other parts of the system.
[0126] In the present system, the hydrogen gas is produced from two sources; one is from the hybrid Solar hydrogen-Oxygen gas generator system
[0127] In some embodiments of the invention, the hybrid solar hydrogen-oxygen gas generator system works with integrating other systems of the Cot capturing and electrical energy producing system, such as; [0128] i. Hydrogen gas turbine unit: the hydrogen and oxygen gases are produced from hybrid solar hydrogen-oxygen gas generator system unit
[0131] In other embodiment of the hybrid solar hydrogen-oxygen gas generator system unit utilizes potassium hydroxide and other alkali bases.
[0132] As described in other units of the co2 capturing and electrical energy producing system, enough electric power is generated from hydrogen gas turbine, hybrid thermoelectric generator unit, and waste recovery system unit. Therefore, the electrolysis of brine unit 30, and the other hydrogen-oxygen gas generator 24 wherein the hybrid solar hydrogen-oxygen gas generator system unit is powered from internally generated electric power.
[0133] The hybrid solar hydrogen-oxygen gas generator system unit comprises the processes and steps of: [0134] i. Producing electrical energy from solar 21 and powering some parts of hydrogen-oxygen gas generator cells 5 [0135] ii. Producing hydrogen 22 and oxygen 23 gases from the hydrogen-oxygen generator, by using electrolysis of sodium hydroxide 31 or other alkali bases. [0136] iii. Storing energy in the form hydrogen 11, [0137] iv. Routing Hydrogen and oxygen gases to hydrogen gas turbine 19 and start the operation and produce electric power 20 from the system, [0138] v. Storing and distributing electric power, [0139] vi. Powering the rest of hydrogen-oxygen gas generator cells 24 and produce enough amount of hydrogen 22 and oxygen gases 23 and continuing the operation of the system.
The Tree Fashioned Carbon Dioxide Capturing System Unit
[0140] In the other embodiment of carbon dioxide capturing and electrical energy producing system invention comprises a tree fashioned carbon dioxide capturing unit
[0141] In the present invention, the objectives of the tree fashioned carbon dioxide capturing system unit are; [0142] i. To utilize waste heat: the carbon dioxide absorbing/separating step, and regeneration step, utilizes waste exhausting heat which relisted from solid oxide fuel cell unit or hydrogen gas turbine unit, [0143] ii. To design a unique, less cost-effective, easily implemented, attractive, and high-efficiency carbon dioxide capturing system unit. The physical structure of the present system of a carbon dioxide capturing system unit is fashioned like a tree. Which means the carbon dioxide capturing system machine is having a tree physical structure. [0144] iii. To reduce high external electric power consumption: the carbon dioxide capturing system unit works with the integration of other units of the system. As described in the other units of the present invention, enough amount of electric power is generated from hydrogen gas turbine unit 19, hybrid thermoelectric solid oxide fuel cell system unit 26 & 27 and waste heat recovery system unit 39 & 25. Therefore, the tree fashioned carbon dioxide capturing system unit 38 is powered from internal generated electric powers, and this solves the high external energy consumption problem by carbon dioxide capturing system technologies.
[0145] The tree fashioned carbon dioxide capturing system unit comprises; [0146] i. Exhausted waste heat-based heater 77; as shown in
[0151] There are different kinds of carbon dioxide capture techniques such as solvents, sorbents, membranes and cryogenics. The solvents separation techniques use liquid adsorbents such as amines, mono-ethanolamine, or aqueous ammonia. The membrane separation technique uses separation membranes to concentrate carbon dioxide, cryogenics technique utilizes a cooling and condensation system. The solid separation techniques use solid adsorbents such as alkali or alkaline earth metals, alkali carbonates like sodium carbonate, potassium carbonate and others.
[0152] In the present invention, the tree fashioned carbon dioxide capturing system unit utilizes some of the following solvents or sorbents or adsorbents are listed as follows; [0153] i. Amines, mono-ethanolamine solvents, alkali metal base solvents like potassium hydroxide, sodium hydro oxide or calcium hydroxide, and other metal base solvents, or [0154] ii. Solid sorbents/adsorbents such as; alkali metal carbonates; sodium carbonate, potassium carbonate or alkaline earth metals, solid amines and mono-ethanolamine, and zeolites based sorbents. But the system is not only limited to these solvents/sorbents/adsorbents. Furthermore, the tree fashioned carbon dioxide capturing system unit also integrated, designed and working with a membrane-based carbon dioxide capture system.
[0155] In the present invention, to precede the carbon dioxide absorbing/separating step 76, and the regeneration step 78, it utilizes waste heat.
[0156] As illustrated in
[0157] In the other embodiment of the tree fashioned carbon dioxide capturing system unit, the system also absorbs carbon dioxide from flue gas. The released flue gas from the factory becomes to cool down through the heat exchangers adapted on it. The flue gases cooler part uses to cool down the flue gas to the right temperature for the absorber or separator part. The processes and systems of the carbon dioxide capturing from flue gas are almost the same as the carbon dioxide capturing from the atmosphere, and in the present invention the processes and systems of the carbon dioxide capturing from the atmosphere are also utilized in the processes and systems of a carbon dioxide capturing from flue system.
[0158] As illustrated above, the present system, the carbon dioxide absorbing step 76 and regeneration step 78 utilizes exhausted waste heat 79 which released from hydrogen gas turbine unit or hybrid thermoelectric generator solid oxide fuel cell unit, waste heat recovery system unit, as illustrated in
[0159] The purpose of heating ambient gases is; to increase the absorbing rate of carbon dioxide gas in solvents/absorbents or adsorbents.
[0160] As illustrated in
[0161] Alternatively, the output waste heat from carbon dioxide absorber part 76 and regeneration part 78 is returned into the waste heat recovery system unit to generate additional electric power
[0162] The tree fashioned carbon dioxide capturing unit
[0163] such as; [0164] i. hydrogen gas turbine unit, hybrid thermoelectric solid oxide unit, and waste heat recovery generator system unit; to use exhausted waste heat for carbon dioxide absorber part 76 and regeneration part 78 [0165] ii. Carbon dioxide reactor core unit; to capture and convert carbon dioxide into useful byproducts. [0166] iii. Waste heat recovery system unit; the output waste heat from tree fashioned carbon dioxide capturing system unit is returned to the waste heat recovery system. The out-put waste heat is returned to recover waste heat released from the carbon dioxide absorber part and regeneration part and utilizes to generate additional electric power. The waste heat recovery system 39 collects waste heat released from different parts, and units of the system. And the waste heat recovery system changes the waste heat into electric power.
[0167] As illustrated in
[0168] In the tree fashioned carbon dioxide tree
[0169] In the tree fashioned carbon dioxide capturing system unit
[0170] As described above, the carbon dioxide capturing and electrical energy generating system invention comprises the tree fashioned carbon dioxide capturing system unit
[0177] In the present system, the carbon dioxide absorbing step 76 and regeneration step 78 is designed to operate with the exhausted waste heat. To process the carbon dioxide capturing wherein the carbon dioxide absorber part 76 and regeneration part 78 are utilizes waste heat. As illustrated in
[0178] To capture carbon dioxide from the atmosphere or flue gas, most technology utilizes a large amount of external energy. The high energy consumption is a serious problem in most carbon dioxide capturing industries, and it raises the cost of carbon dioxide capturing and some of them are not economically viable. The current invention solves this problem. The present invention is designed to generate electric power by itself. The parts of carbon dioxide capturing unit are powered by internally generated electric power. This reduces the external electric power consumption highly, and the present invention is easily applicable and economically viable.
The Hybrid Hydrogen Chlorine Fuel Cell and Carbon Dioxide Reactor Core Unit
[0179] The other embodiment of carbon dioxide capturing and electrical energy producing system comprises a “hybrid hydrogen-chlorine fuel cell and carbon dioxide reactor core system” unit
[0180] The objective of the “hybrid hydrogen chlorine fuel cell and carbon dioxide reactor core” is; [0181] i. For producing electrical energy from brine electrolysis byproduct gases. This means; the hydrogen and chlorine gases are utilized to produce electrical energy through hydrogen-chlorine fuel cell 32. [0182] ii. To power carbon dioxide reactor core by hydrogen chlorine fuel cell, and to reduce the consumption of electrical energy by carbon dioxide reactor core. [0183] iii. To convert carbon dioxide into sodium carbonate and sodium bicarbonate or alkali carbonates 35. [0184] iv. To create a cost-efficient and energy-efficient carbon dioxide reactor core. And, finally to increase the value and efficiency of the “Co2 capturing and electrical energy producing system” invention.
[0185] In other embodiment of “Carbon dioxide capturing and Electrical energy producing system”
[0186] As illustrated in
[0187] As illustrated in
[0190] and carbon dioxide molecules are exposed to concentrated radiations, the carbon dioxide molecule bonds become vibrate and the kinetic energy of carbon dioxide molecule bonds increases and the system creates to increase the reaction rate of carbon dioxide with alkali base increase. [0191] 1. a heat-absorbing system /heat jacket/ 99 & 98; some amount of waste heat exhausted from hydrogen gas turbine is directed into the heat-absorbing system, wherein the external part of the carbon dioxide reactor core, and the waste heat is circulated into the body 101 of the reactor core and heat is absorbed by the heat-absorbing system, creates to increase the temperature inside of the reactor core, finally the system utilized to increase the reaction rate of carbon dioxide with sodium hydroxide.
[0192] As illustrated in
[0193] After the carbon dioxide molecules are exposed to concentrated radiations, the carbon dioxide molecule bonds become vibrate and the kinetic energy of carbon dioxide molecule bonds increases and at the end the reaction rate of carbon dioxide with alkali base increase. The emitting of concentrated radiations/laser to carbon dioxide creates to increase the reaction rate of carbon dioxide with an alkali base and this system plays its own role to increase the efficiency of carbon dioxide reactor core. The purpose of the emitting of concentrated radiations/laser to carbon dioxide is; to increase the reaction rate of carbon dioxide with an alkali base and converted into carbonates and sodium bicarbonate byproducts.
[0194] As illustrated in
[0195] The high pressure compressing system 91 installed at the top of the reactor and the system comprises; integrated automatic controlling system, compressing system 91, and sensors installed on it. The integrated automatic controlling system 91 systems and sensors used to control and to operate the reaction procedure on the system.
[0196] As shown in
[0197] In the current embodiment, the high carbon dioxide reactor system operation is partially powered by the hydrogen chlorine fuel cell. The objective of the hybrid of hydrogen chlorine fuel cell and carbon dioxide reactor core is to reduce external electric power consumption in the reactor and to powered by hydrogen chlorine fuel cell. Therefore, the integration of the “carbon dioxide reactor core system with a hydrogen-chlorine fuel cell” creates a self-powered carbon dioxide reactor core. And this integrated system reduces external power consumption and this system greatly helps to increases the efficiency of carbon dioxide reactor core, and finally increases the efficiency of the “Carbon dioxide capturing and electrical energy producing system” invention.
[0198] The carbon dioxide reactor core 33 comprises heat-absorbing system 99 & 98; and the system designed on the outer side of the reactor core. In this system, the heat absorber part is another system which utilized to boost the reaction rate of carbon dioxide with sodium hydroxide.
[0199] The waste heat from steam turbine 8 is directed into the outer side of the carbon dioxide reactor core 101. And the waste heat is circulated in the body of the reactor core 101, and heat is absorbed by heat absorbers 99 & 98 from the waste hot gases. Then the temperature inside of the reactor core becomes increased, finally, the reaction rate of carbon dioxide with sodium hydroxide is boosted. The magnitude of temperature in the reactor core is directly proportional to the dissolving rate of carbon dioxide in sodium hydroxide solution or alkali base.
[0200] In one embodiment of the carbon dioxide reactor core, to increase mass transfer and to increase kinetic collisions of carbon dioxide with sodium hydroxide, the carbon dioxide reactor core utilizes different methods; such as scattering sodium hydroxide solution at the top of the reactor core over carbon dioxide containing reactor core, bubbling method or film method.
[0201] The heat-absorbing system reduces electric energy utilization by electric heaters inside of the reactor and at the same time, it increases the efficiency of conversion of carbonate products. To increase the reaction rate and conversion rate of carbon dioxide into carbonate products, It's not important to installed electrical heaters in the reactor core, instead of that, the current system uses hot output waste gas from hydrogen turbine and the waste hot gas directly directed into the body of the reactor core 105, and the hot waste gas circulating in the prepared lines of the body of reactor core, and the heat absorber system absorbs heat and the reactor core becomes hot. Due to increasing the temperature in the reactor core, the dissolving rate of carbon dioxide with alkali base is increased.
[0202] In the present embodiment the heat absorber part system uses to increase the efficiency of carbon dioxide conversion rate by reducing electrical energy consumption in the reaction process. Instead of electric heaters, it uses waste heat from hydrogen gas turbine output hot gas.
[0203] In one embodiment, the carbon dioxide reactor core comprising an aqueous sodium hydroxide solution contains 35 to 60% (preferably 40% to 50%) by weight of sodium hydroxide. In this embodiment, the aqueous sodium hydroxide solution starts carbonating at a temperature, above 30° C. and lower than 120° C., at a different range of pressure.
[0204] The laboratory test result on the efficiency of carbon dioxide capture in sodium hydroxide solution depends on the concentration of sodium hydroxide and temperature of the inner reactor core. The concentration of sodium hydroxide in the solution at 50% by weight and the temperature of the inner reactor core at 80° C., the efficiency of absorption is from 85% to 90%.
[0205] In other embodiment of the invention, the laboratory test result on the efficiency of carbon dioxide reaction with sodium hydroxide solution depends on the concentration of sodium hydroxide, temperature of the inner reactor core, applied pressure over the reactants, and light/lather emitting intensity 94 over the reactants. When the magnitude of the temperature, pressure, and light/lather emitting intensity over the reactants increase; the efficiency of the conversion rate to sodium carbonate and sodium bicarbonate increases. The conversion efficiency of carbon dioxide is directly proportional to the magnitude of temperature, pressure, and light/lather intensity inside of the reactor core.
[0206] In one embodiment, the carbon dioxide reactor core unit comprises; the high pressure compressing system 91, the concentrated lather ray emitters system 104, and the heat-absorbing system, and these systems create to increase and boost the absorbing rate of carbon dioxide with alkali base at high efficiency. In the carbon dioxide reactor core unit, the sodium hydroxide/alkali base is sprayed over the carbon dioxide through sprayer 106.
[0207] The hydrogen-chlorine fuel cell generates electric power for the carbon dioxide reactor operation. Carbonates and hydrogen carbonates are by-products and released from the reaction core. The sodium carbonates and sodium hydrogen carbonates byproduct use for the different chemical industries, and the byproducts create additional income.
[0208] Overall, the integration of the art skill, and embodiment of the hybrid hydrogen chlorine fuel cell with the carbon dioxide reactor core unit system plays a big role to increases the efficiency of the “carbon dioxide capturing and energy producing systems” invention.
[0209] The hybrid hydrogen chlorine fuel cell and carbon dioxide reactor core system unit at least comprising the steps of; [0210] i. collecting chlorine and hydrogen gas from the electrolysis of sodium chloride, [0211] ii. producing electric power from the hydrogen-chlorine fuel cell, [0212] iii. powering the carbon dioxide reactor core, [0213] iv. sequestration carbon dioxide from the atmosphere and storing in the tankers [0214] v. pumping carbon dioxide gas into carbon dioxide reactor core, [0215] vi. Pumping and spraying sodium hydroxide solution or alkali base into the reactor core [0216] vii. pressing with high-pressure compressing system the carbon dioxide gas and sodium hydroxide solution together, [0217] viii. by using waste heat from hydrogen gas turbine, heating the carbon dioxide reactor core [0218] ix. Releasing concentrated light/laser over carbon dioxide gas and sodium hydroxide solution, and mixing. [0219] x. By using mixer blades mixing the carbon dioxide gas and sodium hydroxide solution and creating more collusion
[0220] The final output byproducts from the hybrid hydrogen chlorine fuel cell and carbon dioxide reactor core system unit are; sodium carbonate/sodium bicarbonate/alkali carbonates 35, and hydrochloric acid 36, and the byproduct uses for the different chemical industry, and the byproducts create additional income.
The Another Alternative Embodiment of Carbon Dioxide Reactor Core System /FIG. 15/
[0221] The “another alternative design of carbon dioxide reactor core” unit objectives are;
[0222] (a) to design a less cost-effective reactor core, and;
[0223] (b) to create different alternatives of carbon dioxide reactor core for different plants,
[0224] In other alternative embodiment of the hybrid hydrogen-chlorine fuel cell and carbon dioxide reactor core system wherein said the carbon dioxide reactor core system the other alternative embodiment system comprises;
[0225] a heat-absorbing jacket system 98 and 99; the heat-absorbing system fashioned and adapted in the external part of the carbon dioxide reactor core system.
[0226] Some amount of waste heat exhausted from hydrogen gas turbine is directed into heat-absorbing jacket system, wherein the external part of the carbon dioxide reactor core, and the waste heat is circulated into the external body of the reactor core and heat is absorbed by heat-absorbing jacket system, and the system creates to increase the temperature inside of the reactor core, finally the system utilized to increase the reaction rate of carbon dioxide with sodium hydroxide.
[0227] As illustrated in
[0228] The working system and methods of the another alternative embodiment of carbon dioxide reactor core system
[0229] The other alternative of carbon dioxide reactor core system integrated and hybrid with a hydrogen-chlorine fuel cell, and the other alternative method working together with all systems, process, and methods of hydrogen-chlorine fuel cell which described in previous pages /from page 27-32/.
[0230] The final output byproducts from the other alternative carbon dioxide reactor core system
Waste Heat Recovery System Unit
[0231] A carbon dioxide capturing and electrical energy producing system invention comprises a waste recovery system
[0232] The waste heat recovery system at least comprises; waste heat exhausted sources from hydrogen gas turbine and waste heat exhausted from different parts of the system, waste heat recovery generator 39, steam turbine 8, hydrogen-oxygen super heater 111 and electric generator 25.
[0233] According to the various embodiment of the current invention, the waste heat exhausted from different systems utilized for different applications. As described in previous pages, the waste heat exhausted from hydrogen gas turbine 19 flows into waste heat recovery generator 39, to drive the steam turbine. The output waste heat from waste heat recovery generator 39 flows to carbon dioxide capturing unit 38 and carbon dioxide reactor core 33 to heating the systems. In addition, the waste heat exhausted from solid oxide fuel cell 26 utilized for the thermoelectric generator to generate electric power
[0234] In the present embodiment of the invention, the waste heat exhausted from hydrogen gas turbine 19, solid oxide fuel cell 26, and hydrogen-chlorine fuel cell 32 is collected, recycled, and turned to drive steam turbine 8 and generates additional electrical power 25.
[0235] The waste heat exhausted from hydrogen gas turbine, solid oxide fuel cell 26, and hydrogen-chlorine fuel cell 32 flows to waste heat recovery steam generator 39. The waste heat recovery steam generator 39 has a duct 112 for receiving hot exhaust gas from hydrogen gas turbine, solid oxide fuel cell and hydrogen-chlorine fuel cell. The waste heat recovery steam generator is also associated with a heating system for receiving feed water for heating to steam. A heat pipe having a first end disposed within the duct operates to remove heat therefrom. A second end of the heat pipe disposed within the heating system operates to transfer heat to the feed water. The waste heat recovery steam generator 39 is essentially a large duct 112 with water-filled tube bundles disposed of therein. To recover waste heat from hydrogen gas turbine, solid oxide fuel cell, and hydrogen-chlorine fuel cell, feed water is circulated through the tube bundles such that the water is heated to steam as the exhaust waste gas passes through the duct and over the tube bundles. The waste heat steam generator 39 produces steams from waste exhausted heat and the produced steam flows to hydrogen-oxygen superheater 111, to re-heat the steam and to produce high pressurized steam. The high-pressure steam 119 drives steam turbine 8 and the steam turbine drives electric generator 25 and it produces additional electric power.
[0236] As described in
[0237] The hydrogen and oxygen are introduced into the burner and an ignition system in a manner to get intimate mixing of the two, and thus stable burning. By firing hydrogen and oxygen directly into the steam line in super heater 111 the steam temperature can be raised to a temperature where no thermal problems are created in the turbine.
[0238] As illustrated in
[0239] The hydrogen and oxygen flow regulator 113 and 114, feed the proper amount of hydrogen and oxygen to the burner 118 in super heater 111 in order to maintain the temperature leaving super heater at the desired value. The valves are controlled by a regulator that receives a temperature signal from a temperature sensing device which adapted in the super heater. Flow meters are used to measure the amount of hydrogen and oxygen flowing to the burners in super heater 118, and these signals are fed to the regulators and controllers to position the valves as to maintain a stoichiometric ratio. The hydrogen and oxygen are burned directly in the steam flowing through super heater 111, thus increasing the temperature of such steam.
[0240] As illustrated in
[0241] The waste heat recovery system unit utilizes to generate additional electric power from exhaust waste heat and, this system increases the values and efficiencies of carbon dioxide capturing and electrical energy producing system invention.
[0242] The waste heat recovery system unit comprising the steps of; [0243] i. Collecting waste heat exhausted from hydrogen gas turbine 9, solid oxide fuel cell 26, and hydrogen-chlorine fuel cell 32, [0244] ii. Turning the waste heat into waste heat recovery steam generator 39, and the waste heat steam generator 39, produce steams from waste exhausted heat and the produced steam flows to hydrogen-oxygen super heater 111 & 116, [0245] iii. In the hydrogen-oxygen super heater 111, burning hydrogen and oxygen gases and re-heat the steam and produce high pressurized steam 119. The high pressure and temperature steam drive steam turbine 8 and the steam turbine drives electric generator 25 and it produces additional electric power.
The Other Alternative Embodiment of Super Heater /FIG. 18/
[0246] The other alternative embodiment of super heater /
The Other Alternative Embodiments of “the Carbon Dioxide Capturing and Electrical Energy Producing System” Invention
[0247] The present invention of the carbon dioxide and electrical energy producing system comprises different other alternative embodiments. To create different choices for customers, the present invention includes different alternative embodiments, and each embodiment has different arrangements, integrations, efficiencies and costs. In the present invention, three different other alternative embodiments are included. The goals of the other alternative embodiments one, two and three are described as follows but not limited: [0248] i. To generate electric power [0249] ii. To capture carbon dioxide from the atmosphere or flue gas [0250] iii. To create innovative alternative designs for customers, to create different choices at different costs, and this helps to implement the technology easily. [0251] iv. To create an alternative embodiment for easy production
[0252] The three other Alternative embodiments of “the carbon dioxide capturing and electrical energy producing system” invention are described as follows;
A. The Other Alternative Embodiment-One of the “Carbon Dioxide and Electrical Energy Producing System” Invention
[0253] The other alternative embodiment one as shown in
[0260] As illustrated in other alternative embodiment one, in
[0261] As illustrated in other alternative embodiment one in
[0262] In the other alternative embodiment-one of carbon dioxide capturing and electrical energy producing system invention, and the physical structure of carbon dioxide capturing system unit is fashioned as a tree structure. In this alternative system, the carbon dioxide capturing system unit /
[0263] In the other alternative embodiment one
[0267] As illustrated in another alternative embodiment one,
[0268] And to increase the absorption rate of carbon dioxide it needs to heating-up the sucked gases to the right temperature for the absorber, and the absorber system 134 utilizes waste heat-based heater 135. To heat-up the incoming gases, the present other alternative embodiment one utilizes waste heat exhausted 79 which relisted from steam turbine unit 8. The exhaust waste heat from the steam turbine 8 is pumped into the absorber part
[0269] In another alternative embodiment one, the tree fashioned carbon dioxide capturing system unit at least comprises the parts of; intercoolers, sodium hydroxide or potassium hydroxide circulation pumps, heat exchangers, controlling part, carbon dioxide absorption part, stripper, and carbonates and bicarbonates tanker.
[0270] Furthermore, the other alternative embodiment one, wherein the tree fashioned carbon dioxide capturing system unit
[0274] Due to the temperature and the structure of the vertical helical tube 134 the absorption rate of carbon dioxide increase. The carbonates and bicarbonates product accumulated in the base of the trunk and finally the filtered atmospheric gases released into the atmosphere. [0275] iv. the base of the tree 136; in the ergonomics of the tree, at least carbonate and bicarbonate tankers and circulation pumps, controllers are installed in the base of the tree,
[0276] In other alternative embodiment one, the color of the tree fashioned carbon dioxide capturing system unit is green or other colors.
[0277] In other alternative embodiment one, tree fashioned carbon dioxide capturing system unit
[0281] The tree fashioned carbon dioxide capturing system unit
[0282] In other alternative embodiment one, tree fashioned carbon dioxide capturing system units
[0283] As illustrated in other alternative embodiment one of “carbon dioxide capturing and electrical energy producing system”
[0284] In other alternative embodiment one
B. The Other Alternative Embodiment-Two of the “Carbon Dioxide and Electrical Energy Producing System” Invention
[0292] The other alternative embodiment two of the carbon dioxide capturing and energy producing system; the arrangements and integrations at least comprising; [0293] i. Hybrid solar hydrogen and oxygen gas generator unit [0294] ii. Non-ionized hydrogen gas turbine unit [0295] iii. Tree fashioned carbon dioxide capturing unite
[0296] As illustrated in other alternative embodiment two, in
[0297] As illustrated in other alternative embodiment two, in
[0298] In other alternative embodiment two, the brine electrolysis unit is not utilized. The input chemicals for hybrid solar hydrogen-oxygen gas generator 24 and for tree fashioned carbon dioxide capturing system 125 utilizes from external sources. The other alternative embodiment-two of the carbon dioxide capturing and energy producing system helps to reduce the cost of the plant and creates an alternative opportunity for customers.
[0299] The other alternative embodiment two of the carbon dioxide capturing and energy producing system at least comprising the processes and steps of; [0300] i. Producing hydrogen and oxygen gases from hybrid solar hydrogen-oxygen gas generator [0301] ii. By utilizing hydrogen and oxygen gases, and producing electric power from non-ionized hydrogen gas turbine [0302] vii. Sucking atmospheric gases through the tree fashioned carbon dioxide capturing system unit, Sucking atmospheric gases through the tree fashioned carbon dioxide capturing system unit 135,
C. The Other Alternative Embodiment-Three of the “Carbon Dioxide and Electrical Energy Producing System” Invention
[0304] The other alternative embodiment three of the carbon dioxide capturing and energy producing system; the arrangements and integrations at least comprising; [0305] i. Solar cells and hydrogen-oxygen gas generator unit [0306] ii. Fuel cell/solid oxide fuel cell or proton exchange membrane full cell/iii. [0307] Tree fashioned carbon dioxide capturing unit
[0308] As illustrated in other alternative embodiment three, in
[0309] As illustrated in other alternative embodiment three, in
[0310] In other alternative embodiment three, the brine electrolysis unit is not utilized. The input chemicals for hydrogen-oxygen gas generator 24 and for tree fashioned carbon dioxide capturing system
[0311] The other alternative embodiment-three of the carbon dioxide capturing and energy producing system
[0312] The other alternative embodiment three of the carbon dioxide capturing and energy producing system
[0316] The Other Alternative embodiments of “the carbon dioxide capturing and electrical energy producing system” invention are exemplary and non-limiting.
[0317] As described in the above detailed description section of the carbon dioxide capturing and electrical energy producing system wherein a hydrogen gas turbine unit, hybrid thermoelectric-generator solid oxide fuel cell unit, solar hybrid hydrogen-oxygen gas generator system unit, hybrid hydrogen chlorine fuel cell with carbon dioxide reactor core unit and waste heat recovery system units are physically or electrically or mechanically coupled and integrated each other. The hybrid and integration of variety units of systems create to achieve the objective of capturing carbon dioxide and generating electrical power from the system.
[0318] The present invention comprising various alternative embodiments, such as; the carbon dioxide capturing and energy production system invention at least having four alternative embodiments /
[0319] The descriptions of the current processes, integrations, physical structures, hybrids, methods, arrangements and devices, including those in the appendices, are exemplary and non-limiting. Certain Substitutions, modifications, additions and/or rearrangements over the present invention is disclosed by the owner of the invention.
[0320] The present invention captures carbon dioxide and generating electric energy by itself, with zero Carbone emission and zero air pollutions. The economical and environmental benefits of the present invention are; reducing carbon emission and air pollutions, improving climate change and global warming problems and promoting a clean technology of the future. Therefore, the present invention creates a difference in solving of the present challenges and problems of climate change, and it's a helpful invention for the benefit of mankind.