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CN102712019A - Sustainable economic development through integrated production of renewable energy, materials resources, and nutrient regimes - Google Patents

Sustainable economic development through integrated production of renewable energy, materials resources, and nutrient regimes Download PDF

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Publication number
CN102712019A
CN102712019A CN2010800488706A CN201080048870A CN102712019A CN 102712019 A CN102712019 A CN 102712019A CN 2010800488706 A CN2010800488706 A CN 2010800488706A CN 201080048870 A CN201080048870 A CN 201080048870A CN 102712019 A CN102712019 A CN 102712019A
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energy
resource
parts
hydrogen
carbon
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CN102712019B (en
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罗伊·E·麦卡利斯特
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McAlister Technologies LLC
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McAlister Technologies LLC
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Priority claimed from US12/707,653 external-priority patent/US8172990B2/en
Priority claimed from PCT/US2010/024497 external-priority patent/WO2010096503A1/en
Priority claimed from PCT/US2010/024499 external-priority patent/WO2010096505A1/en
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
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    • C12M43/00Combinations of bioreactors or fermenters with other apparatus
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    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/342Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents with the aid of electrical means, electromagnetic or mechanical vibrations, or particle radiations
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    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
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    • C01B2203/06Integration with other chemical processes
    • C01B2203/068Ammonia synthesis
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    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/0612Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
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    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
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    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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Abstract

The present disclosure is directed to a system and method of sustainable economic development, such as development through an integrated production of renewable energy, material resources, and nutrient regimes. In some embodiments, the system utilizes resources extracted from renewable energy sources to assist in the capture of energy from other renewable energy sources. In some embodiments, the system utilizes energy from renewable energy sources to extract resources from other renewable energy sources.

Description

Integrated production through renewable energy, material resources and nutrient realizes sustainable economic development
The cross reference of related application
The title that the application requires to submit on May 14th, 2010 is the U.S. Provisional Patent Application of " SYSTEM AND METHOD FOR RENEWABLE RESOURCE PRODUCTION " number 61/345; 053, the title of submitting on February 13rd, 2010 is the U.S. Provisional Application number 61/304 of " FULL SPECTRUM ENERGY AND RESOURCE INDEPENDENCE "; 403, the title of submitting on February 17th, 2010 is the Patent Application No. 12/707 of " ELECTROLYTIC CELL AND METHOD OF USE THEREOF "; 651, the title of submitting on February 17th, 2010 is that the title of submitting in the PCT application number PCT/US10/24497 of " ELECTROLYTIC CELL AND METHOD OF USE THEREOF ", on February 17th, 2010 is the Patent Application No. 12/707 of " APPARATUS AND METHOD FOR CONTROLLING NUCLEATION DURING ELECTROLYSIS "; 653, the title of submitting on February 17th, 2010 is that the title of submitting in the PCT application number PCT/US10/24498 of " APPARATUS AND METHOD FOR CONTROLLING NUCLEATION DURING ELECTROLYSIS ", on February 17th, 2010 is the Patent Application No. 12/707 of " APPARATUS AND METHOD FOR GAS CAPTURE DURING ELECTROLYSIS "; 656, the title of submitting on February 17th, 2010 be that the PCT application number PCT/US10/24499 of " APPARATUS AND METHOD FOR CONTROLLING NUCLEATION DURING ELECTROLYSIS " and the title submitted on August 27th, 2009 are the priority and the rights and interests of the U.S. Provisional Patent Application number 61/237,476 of " ELECTROLYZER AND ENERGY INDEPENDENCE TECHNOLOGIES ".These applications are incorporated herein separately by reference in full.
Background technology
The regenerative resource such as the sun, wind, wave, fall into water and biomass castoff has the great potential as main energy sources, stops its extensively variety of issue of employing but meet with at present.For example, in the production of electricity, utilize regenerative resource to depend on the availability in said source, it possibly be desultory.Solar energy receives the restriction of sun availability (promptly only daytime), the variational restriction of wind energy wind-engaging, and the drowning restriction that can receive arid, living beings receive the restriction of seasonal variety, or the like.Because these and other factor, many energy from renewable origin (capture or do not capture) tend to be wasted.
For many areas in the world, capture and save these poor efficiency in the energy and limited regenerative resource and grow into feasible energy supplier, because inefficiently usually make with high costs with the production of renewable energy resources energy.Therefore as if, the world continues to depend on oil and other fossil fuels as main energy sources, because the subsidy that government surpasses a century to infrastructure and technological development makes consumes fossil resource by contemporary people to produce utilisable energy convenient and seem cheapness.The exploitation of limited fossil and fissionable fuel reserves provides wrong sense of worth because the replacement cost and environmental degradation cost and the health effect that is caused in expensive source be not included in the purchasing price of this type energy.
Superfluous; Particularly from the power of large-scale fire coal and nuclear fuel central electric power station; Constitute invisible cost, comprise heavy metal residue toxic discharge quick generation the relevant environment pollution problem and from the needs of the greenhouse gases of combustion of fossil fuel and expensive long-term storage radioactive waste.Current communal facility distribution system relates to high capital equipment, maintenance and fuel cost and satisfies client's needs so that enough capacity to be provided.
The Sustainable Production of renewable resource and utilization existence these and other problem.
Description of drawings
Figure 1A is a block diagram, shows the system of integrated energy, farming merchant and industrial sustainable economic development according to aspect of the present disclosure.
Figure 1B is a block diagram, shows the system according to the integrated production of the sustainable economic development of aspect of the present disclosure.
Fig. 1 C is a sketch map, shows the system based on land according to the integrated production of the sustainable economic development of aspect of the present disclosure.
Fig. 1 D is a sketch map, shows the system based on the ocean according to the integrated production of the sustainable economic development of aspect of the present disclosure.
Fig. 1 E is a block diagram, shows the system according to the sustainable economic development of aspect of the present disclosure.
Fig. 2 A is a block diagram, shows some parts from the system of feedstock capture resource of using according to aspect of the present disclosure.
Fig. 2 B is a block diagram, shows some parts that are used for generating from the product from the process of the feedstock capture resource supplied with or accessory substance the system of resource according to aspect of the present disclosure.
Fig. 3 A-3F is a block diagram, shows the operation that generates parts according to resource in the system of aspect of the present disclosure.
Fig. 4 is a block diagram, shows according to the energy utility system of aspect of the present disclosure or is used to the energy from renewable resource.
Fig. 5 is a flow chart, shows the program of using the utilization of resources energy that is generated according to aspect of the present disclosure.
Fig. 6 is a flow chart, shows according to aspect of the present disclosure to use from the Energy extraction of regenerative resource or the program of generation resource.
The specific embodiment
The cross reference of related application
The application incorporates in full the title submitted on November 9th, 2004 by reference into and is the U.S. Provisional Patent Application of " MULTIFUEL STORAGE; METERING AND IGNITION SYSTEM " number 60/626; The title that 021 (attorney docket 69545-8013US) and on February 17th, 2009 submit to is the theme of the U.S. Provisional Patent Application number 61/153,253 (attorney docket 69545-8001US) of " FULL SPECTRUM ENERGY ".It is the theme of " METHODS AND APPARATUSES FOR DETECTION OF PROPERTIES OF FLUID CONVEYANCE SYSTEMS " (attorney docket 69545-8003US), " COMPREHENSIVE COST MODELING OF AUTOGENOUS SYSTEMS AND PROCESSES FOR THE PRODUCTION OF ENERGY, MATERIAL RESOURCES AND NUTRIENT REGIMES " (attorney docket 69545-8025US), " ELECTROLYTIC CELL AND METHOD OF USE THEREOF " (attorney docket 69545-8026US), " SYSTEMS AND METHODS FOR SUSTAINABLE ECONOMIC DEVELOPMENT THROUGH INTEGRATED FULL SPECTRUM PRODUCTION OF RENEWABLE ENERGY " (attorney docket 69545-8041US), " SUSTAINABLE ECONOMIC DEVELOPMENT THROUGH INTEGRATED FULL SPECTRUM PRODUCTION OF RENEWABLE MATERIAL RESOURCES " (attorney docket 69545-8042US), " METHOD AND SYSTEM FOR INCREASING THE EFFICIENCY OF SUPPLEMENTED OCEAN THERMAL ENERGY CONVERSION (SOTEC) " (attorney docket 69545-8044US), " GAS HYDRATE CONVERSION SYSTEM FOR HARVESTING HYDROCARBON HYDRATE DEPOSITS " (attorney docket 69545-8045US), " APPARATUSES AND METHODS FOR STORING AND/OR FILTERING A SUBSTANCE " (attorney docket 69545-8046US), " ENERGY SYSTEM FOR DWELLING SUPPORT " (attorney docket 69545-8047US), " ENERGY CONVERSION ASSEMBLIES AND ASSOCIATED METHODS OF USE AND MANUFACTURE " (attorney docket 69545-8048US) and " INTERNALLY REINFORCED STRUCTURAL COMPOSITES AND ASSOCIATED METHODS OF MANUFACTURING " each U.S. Patent application (69545-8049US) that the application also incorporates the following title of meanwhile submitting on August 16th, 2010 into by reference in full.
General introduction
The invention describes a kind of being used for applies renewable energy with the renewable energy that obtains to make with extra care and the therefore system of the economic sustainability of acquisition from the raw material production resource with regard to just to raw material and other inputs.Superfluous electricity particularly from the power of large-scale fire coal and nuclear fuel central electric power station, is wasted to a great extent and constitutes another economic problems, but the present invention allows to utilize such surplus capacity to produce renewable energy, material and nutrient.This solution will improve the return rate of current investment and stimulate the transition to the sustainable economic development practice.Exemplarily; Electricity from the surplus in fossil fuel or nuclear fuel power plant can exchange ground in order to produce the carbon reinforcing material with renewable electricity; To be used for solar energy dish formula generator and the wind turbine and the hydraulic turbine; Therein, such enhancing carbon from comprise renewable origin and fossil origin be derived from hydrocarbon for example methane extract.Ongoing utilize output that wind and flowing water produces renewable electricity from this type solar energy dish formula generator and turbine usually than this type hydrocarbon primary combustion provided that much higher times and the ability that efficiently satisfies client's needs improve greatly.
In the production process of resource (for example hydrogen, oxygen, carbon), system adopts reproducible process, and it extracts from the resource of using renewable energy and captures some or all resource and/or accessory substance and again in the input coefficient.In certain embodiments, the feasible Sustainable Production that realizes hydrogen, carbon and other resources of system.In certain embodiments, system utilizes in the Sustainable Production process of resource and as the result's of the Sustainable Production of resource energy.In certain embodiments, system allows through the renewable energy input in the refining input coefficient and therefore in system, obtains the economic multiplier effect of raw material, resource and other materials is realized sustainable economic development.
Many details shown in the accompanying drawing, size, angle, shape and other characteristics are merely example specific embodiment of the present disclosure.Therefore, other embodiment can have other details, size, angle and characteristic and not depart from spirit of the present disclosure or scope.In addition, those of ordinary skills should be understood that can not having some following details ground implements other embodiment of the present disclosure.
" embodiment " who mentions in the whole specification refers to that the special characteristic, structure or the characteristics that combine this embodiment to describe are included among at least one embodiment of the present disclosure.Therefore, the statement " in one embodiment " that occurs everywhere in whole specification differs to establish a capital and refers to same embodiment.In addition, said special characteristic, structure or characteristics can make up in one or more embodiments in any suitable manner.In addition, the title that provides among this paper is merely convenient so should not be construed as scope of disclosure or the implication that requires protection.
Whole system
Figure 1A shows comprehensive integrated production system 100; It is made up of three inter-related systems, comprises comprehensive energy garden 200 of being used for renewable energy production and material resources and extracting, is used for comprehensive farming merchant's network 300 of renewable nutrient (people, animal and plant nutrition) and energy feedstuff production (living beings, bio-waste and bio-fuel) and is used for sustainable material resources production and comprehensive industry park 400 of zero-emission manufacturing.
Figure 1A shows system 100, and it is the synthesis of system 200,300 and 400, to realize energy, material and the exchange of information between these systems.Methods in system's 100 synthesises, the particularly system 200 are utilized the macroscopic property of a plurality of inter-related Thermal Motors that connect with the calorifics mode; These Thermal Motors are connected to form the thermodynamics total system to be used as very large Thermal Motor effectively with the calorifics mode, and said very large Thermal Motor can be obtained the production capacity and the efficient of favourable raising.In system 100, system 200 is exclusively used in and between solar heat, underground heat, ocean heat and engine thermal source, obtains collaborative the connection to improve total available rechargeable energy output of specific location and the material resources that energy is provided and is extracted to system 300 and 400.
Comprehensively energy garden 200 connects with effectively as single big Thermal Motor with the calorifics mode, uses with two stages or the working fluid of multistage heating more, and the system and the subsystem of said single big Thermal Motor are interrelated to set up the energy cascade.Thereby through making working fluid between solar source, geothermal source, engine thermal source and other thermals source, systematically move the macroscopic property (for example temperature, pressure, purity, phase shift and energy conversion efficiency) to obtain cascading optimization work fluid, system's 200 total available rechargeable energy outputs obtain increasing.The energy output in a stage is put in the critical process in another stage again, so that move with regeneration or spontaneous mode, makes operational efficiency and economy improve.
The effect in energy garden 200 comprises comprehensively: collection, conversion and the storage of kinetic energy, heat energy and radiant energy form between the regenerative resource such as the sun, wind, flowing water, underground heat, living beings and the internal combustion engine; Between system, to set up spontaneous or the regenerated energy cascade; Thereby produce accumulation and collaborative benefit, such benefit can not obtain through only gathering, transform and store any regenerative resource.Method spontaneous or regenerated energy is implemented in system 200,300 and 400.In addition, system 200 also is used for the material resources extraction of numerous chemicals of system 300 and 400.For example, heat chemistry regeneration is used as the measure of carbon as the raw material (extraction can be carried out) of the follow-up manufacturing production of system's 400 place's durable goods of extracting in system 200,300 and 400.Again for example, heat chemistry regeneration also can be used as nitrogen and the measure of trace mineral for the follow-up manufacturing production of the vegetable fertilizer that is used for system 300 of extracting.In addition; System 200 also is used for bio-waste, living beings and bio-fuel transforms, usually to obtain biological methane gas and/or hydrogen storage, conveying at system 200,300 and 400 places and to use to generate electricity and/or to transmit electricity as the fuel of internal combustion engine and/or fuel cell as required.
Being system 10 to the manipulation of solar heat, underground heat, ocean heat and engine thermal source provides the highly unified platform of adaptation at the facility at place, all places climatic province and based on land with based on the facility of ocean.Improve the adaptive engineering in position and therefore will significantly improve the overall utilization that renewable energy is gathered, and therefore economically feasible solution is provided for local, zone, country and global economy.
The food production at system 300 places not only can be placed in the place, land but also can be placed in the place, ocean.The industrial production facilities of crop farm, livestock farm, ranch, pork and chicken, fresh water fishery, sea fishery, cattle farm etc. can be coupled to the consumer of system 200 as the energy that produces in the system 200; But produce useless byproduct then, these useless byproducts are drawn towards system 200 to be converted into renewable energy and reproducible material resources.In addition, system 300 is intended to improve the energy feedstuff production of this type bio-fuel crop such as crops such as algae, switchgrass, to improve the feasibility based on photosynthetic energy acquisition.Being used for the method and apparatus that water produces, purifies and keep is used in each of production system 200,300 and 400.But these are important component parts of system 300, with satisfy in the food production to the needs of big water gaging and overcome the document record because of the water waste due to the conventional food production operation with water pollution do not have the problem of sustainability.
System integration will improve " sustainability " ability---be defined as the increase of the output of the energy, material resources and the nutrient that use renewable method; To avoid exhausting and reducing or eliminating destructive ambient influnence of natural resources, like pollution and toxic emission as the accessory substance of producing.Sustainability need be for future generations' long-term welfare (and being not only current consumer's short-term benefit at once) feasible energy, material and food production method.
System integration can realize the raising of production capacity; Thereby realize " economic extendible capacity property "---be defined as significantly improving of energy, material and food output, this raising is by duplicating numerous comprehensive installation sites and reaching through the ability that the adaptability to various climatic provinces (promptly gathering renewable energy adaptively through the different resource characteristic of adaptation temperate zone, the torrid zone and arctic climate) that improves greatly increases the quantity in available place.Need so economic extendible capacity property to increase the bearing capacity of the earth, thereby support the energy requirement that constantly quick population growth and developing country increase fast.For successfully using, such production method and place must be available immediately, and with using conventional fossil fuel and/or nuclear power source by comparison, must be the economically feasible substitutes of the existing production measure of energy, material and food.
System integration also can realize the zero-emission and the zero waste method of energy production 200, manufacture of materials 400 and food production 300; Wherein: the organic waste that produces in the system 300 will be by in the living beings, bio-waste and the bio-fuel conversion system that exist in the systematicness ground import system 200, rather than by burning, bury or be poured in landfill yard, aquifer, streams, the ocean or as pollutant emission in atmosphere; Energy in the system 200 and material resources extract and are transferred to system 400 to produce durable goods; Energy in the system 200 and material resources extraction also are transferred to system 300 and think that land and the deepwater mankind, animal and plant life produce nutrient.
System integration will be created single economical production unit, and such economical production unit links up energy production and food production and material resources production consciously with the mode of these functions as complementary overall operation.
Said comprehensive integrated production system therefore be suitable for being installed in wherein do not have at present corresponding renewable energy infrastructure or wherein manufacturing capacity lacks, unemployment is normality or wherein not enough, the poor and malnutrition of food production be in the place or population of normality.The target of introducing this incorporate economical production method is to realize improving GDP (GDP) and improve the quality of living, reach the also quality of making the life better in company with significant employment that creates jobs in company with GDP systemicly.
In addition; System integration will be created single economical production unit; Such economical production unit links up waste management and energy conversion operation consciously; So that it is as complementary overall operation, thereby interrupt to cause polluting the burning that descends with environmental quality, the discarded object operation of burying and topple over the routine of falling.
Said comprehensive integrated production system is introduced the use of continuable discarded object-energy conversion as the integrated operation that runs through whole system.The target of this integral system is the conservation of nature environment, preserves limited natural resources, reduces communicable disease and reduce soil, water and air pollution (comprise and reduce greenhouse gases such as methane and the C02 that promotes climate change).
Said comprehensive integrated production system 100 provides the measure that reaches " Ecological Industrial "; In " Ecological Industrial "; People-system's production environment natural imitation ecosystem: wherein energy between system and discarded object and material flow the input that becomes new process with closed-loop fashion, and whole system is open to the sun (solar heat), the earth (underground heat), ocean (ocean heat) and living beings conversions (engine thermal) renewable sustainable energy that system provided.
Figure 1B is a block diagram; Show the comprehensive integrated production system 100 of sustainable economic development; The production that it comprises energy (for example electricity and fuel) comprises the production of nutrient (product that for example is used for people, animal or plant nutrition) and the production of material resources (for example hydrogen and carbon) simultaneously.System 100 is made up of integrated and complementary subsystem, and said system 100 has the Adaptive Control that spontaneous cascade energy transforms, and it captures and drops into some of each sub-systems or all energy, material and/or accessory substance again.Therefore, the continuous operation of system 100 is able to continue, and only need introduce few external energy or material resources or need not to introduce external energy or material resources.System 100 is an instance of Ecological Industrial; It will promote sustainable economic development; For example utilize renewable energy, produce food and produce material resources, such energy, food and material resources output are higher than uses routine techniques obtainable, also has other benefits in addition.
Comprehensively energy garden 200 makes the method that captures energy from renewable origin 210 (the for example sun, wind, flowing water, underground heat, discharge heat) and cooperates mutually from the method for renewable raw materials 220 (for example bio-waste 320, living beings 310) energy-producing method and production material resources (for example hydrogen 230, carbon 240, other materials resource such as trace mineral 250, pure water 260).Energy stores, reclaims and carry with the Adaptive Control method that spontaneous cascade energy transforms, and said method produces multiplier effect in energy production.In energy acquisition and production process, extract in bio-waste that material resources (for example hydrogen and carbon) uses from the production of renewable energy and the biomass material.Energy garden 200 stores, reclaims, carries, monitors and controls said energy and the efficient of said resource in the production of energy, material resources and nutrient, to obtain to improve comprehensively.
In the energy 210,220 that produces or gather some are provided for comprehensive farming merchant network 300.In the energy 210,220 that is produced some are provided for comprehensive industry park 400.In the energy 210,220 that is produced some are devoted comprehensive energy garden 200 again.In the energy 201,220 that is produced some are provided for outside recipient and/or are added to national grid and/or national gas distributing system road.
The renewable energy that the comprehensive energy of agricultural comprehensively merchant's network 300 receptions garden 200 is produced thinks that the operation of agricultural, animal husbandry and fishery subsystem provides power.This comprises the recyclable fuel that is used for farm equipment, vehicle, canoe and steamer and is used for electricity of light, heat and plant equipment etc.
Comprehensively farming merchant network 300 receives material resources and byproduct such as other materials resource (for example the trace mineral 250) and the pure water 260 that comprehensive energy garden 200 is produced, the nutrient in, animal husbandry agriculture and the fishery subsystem with enrichment and improve plant crop 340 and the production of animal crop 350 in efficient.
Farming is discussed network 300 collecting energy raw materials and is supplied to comprehensive energy garden 200 with in the production that is used in renewable energy it comprehensively.Proper raw material comprises living beings 310 (for example crop waste wood), bio-waste 320 (for example sewage, agricultural effluent, meat packing discarded object, fishing ground effluent), bio-fuel raw material 330 (for example algae, switchgrass) etc.
The renewable energy that comprehensive industry park 400 uses comprehensive energy garden 200 to be produced thinks that the operation of sustainable material resources production and zero-emission manufacturing provides power.This comprises recyclable fuel that is used for internal combustion engine (for example stationary engine, vehicular) and the electricity that is used for light, heat, plant equipment etc.
Material resources 230,240 and the byproduct 250 from energy garden 200 receptions comprehensively dropped in industry park 400 comprehensively, to produce other materials resource (for example designing carbon 420 and carbonado 430).
Certainly the material resources of energy garden 200 receptions and byproduct comprise solar plant 410, wind turbine 410, the hydraulic turbine 410, electrolyzer 410, internal combustion engine and generator 410, automobile, steamer and truck parts 440, semiconductor 450, nanometer technology product 460, agricultural and fishery equipment 470 etc. to manufacture a product like the green energy machine 410 based on carbon comprehensively in industry park 400 uses comprehensively.
Comprehensively industry park 400 to comprehensive energy garden 200 with farming merchant network 300 comprehensively provide in these products and the byproduct some or whole.
400 solar plants of producing and providing 410 in comprehensive industry park, wind turbine 410, the hydraulic turbine 410, electrolyzer 410, internal combustion engine and generator 410 etc. are used in energy garden 200 comprehensively, to produce renewable energy.
Farming merchant network 300 uses 400 internal combustion engines of producing and providing in comprehensive industry park and generator 410, agricultural and fishery equipment 470 and other devices comprehensively, to produce nutrient.
The energy that comprehensive integrated production system 100 is produced provides power for all subsystems, comprises dropping into energy again to promote the further production of renewable energy.Simultaneously, product that is produced in the system 100 and some in the byproduct or all dropped into the in service of all subsystems.Simultaneously, the discarded object that produced of system 100 is captured and as the raw material of the operation of all subsystems.Integrated and complementary subsystem adopts Adaptive Control to manage the spontaneous regeneration of spontaneous cascade energy conversion and material resources.Therefore, said system constantly drops into renewable energy, sustainable material resources and other byproducts again in the different source of subsystem (energy garden, farming merchant's network, industry park) and process.Like this, system 100 is capable of using than the energy and the resource of supplying with the big various resource in system of the obtainable amount of conventional measure.This industrial symbiosis produces multiplier effect on the amount of various resources of gathering from intrasystem renewable raw materials and byproduct source and energy, be worth thereby increase, and reduces cost and improves environment, in addition other benefits in addition.
Fig. 1 C is the sketch map of comprehensive integrated production system 100, shows the various exemplary functional areas based on the system on land; Fig. 1 D is the sketch map of comprehensive integrated production system 100, shows the various exemplary functional areas based on the system of ocean.Shown in system comprise that having the cascade energy transforms integrated production system on the land or ocean of Adaptive Control and spontaneous regeneration of material resources and nutrient production.This system comprises that said functional areas store, reclaim, carry, monitor and control energy and the efficient of material resources in the production of energy, material resources and nutrient, to obtain to improve from reaching from the functional areas of the purpose of renewable raw materials capturing material resource from renewable origin collection and/or generation energy.Following table 1 further set forth follow shown in exemplary output, system and the measure of functional areas.
Table 1: comprehensive integrated production system functional areas
Figure BDA0000158199170000111
Figure BDA0000158199170000121
Figure BDA0000158199170000131
Figure BDA0000158199170000141
Fig. 1 E is a block diagram, shows according to the sustainable economic development of aspect of the present disclosure another system 102 of producing of resource (like hydrogen and carbon) for example.In the process of system's 102 capture use regenerative resources extraction resources some or total material and/or accessory substance also drop into more said or total material and/or accessory substance again.Therefore, system helps sustainable economic development, and the for example utilization of renewable energy, this utilization also have other benefits in addition greater than utilizing renewable energy with routine techniques.
Raw material source 104 is to system's 102 base feeds.Raw material can be any material or material that comprises hydrogen or carbon.Suitable carbon containing or hydrogeneous raw material comprise living beings, bio-waste, coal, oil, natural gas, tire, plastics, diaper, forest waste wood, hospital waste, ocean residue, seawater, industrial wastewater, agricultural effluent, sewage, landfill yard waste water etc.In some cases, system can receive nitrogen-containing material 118, for example air.
Extract parts 110 and receive raw material 118 from raw material source 104.Extracting parts is constructed to extract resource or other materials or raw material is separated into different materials from raw material.In some cases, extract parts 110 raw material of being supplied with is dissociated into carbonaceous material, hydrogenous material, various nutrient and/or ash content.Extract parts 110 can with variously dissociate, extraction or isolation technics extract resource from the raw material of being supplied with, these technology comprise:
Thermal dissociation, it can comprise to one or more material heating to produce reaction;
Electrolysis is left, and it can comprise that the electrolysis following or do not follow separating substances, electrodialysis, electricity separate etc.;
Photodissociation, it can comprise and uses wavelength selected dissociate compound or depolymerization polymer; With
Magnetic dissociates or separates, its can comprise ferromagneticly dissociate, paramagnetic dissociates, magnetohydrodynamics is quickened, the magnetic core logical circuit deflection of material etc.
About suitable extraction, dissociate and/or other details of separation process and technology are found in priority document: the title of submitting on February 17th, 2010 is the Patent Application No. 12/707 of " ELECTROLYTIC CELLAND METHOD OF USE THEREOF "; 651, the title of submitting on February 17th, 2010 is the Patent Application No. 12/707 of " APPARATUS AND METHOD FOR CONTROLLING NUCLEATION DURING ELECTROLYSIS "; 653, the title of submitting on February 17th, 2010 is the Patent Application No. 12/707,656 of " APPARATUS AND METHOD FOR GAS CAPTURE DURING ELECTROLYSIS "; It is incorporated herein by reference in full.
In some cases, extract parts 110 usefulness from the outside or the electricity that receives of internal electric source 106 raw material is dissociated into various materials.The instance of suitable external power source comprises renewable resource (sun/photovoltaic source, the sun/thermal source, wind regime, geothermal source etc.) or non-renewable source (diesel-driven generator, natural gas generator, fire coal or nuclear generator).The instance of suitable internal electric source comprises internal combustion engine, fuel cell, thermoelectric device, piezo-electric device etc.Some or whole power supply can be constructed to think generation supply fuel or the auxiliary generation that offers the electricity of extraction parts 110 that offers the electricity that extracts parts 110 from the various parts reception accessory substances of system or other materials.
In some cases, extract parts 110 usefulness and raw material is dissociated into various materials from the energy that regenerative resource 108 receives.The instance of suitable regenerative resource comprises solar concentrator (those that for example describe among this paper) and other solar energy sources, the flowing water energy and/or wind energy.
In some cases, extracting parts 110 utilizes the energy from power supply 106 and regenerative resource 108 the two reception to come auxiliary material dissociating to various desired substances.In dissociation process, extract parts and can also change heat and/or the pressure that is applied to raw material.
Extract parts 110 raw material of being supplied with is dissociated into various products or accessory substance 112, comprise carbon dioxide (CO 2) 151, carbon monoxide (CO) 152, hydrogen (H 2) 153, water (H 2O) 154, methane (CH 4) 155, ash content 156 and/or other material (not shown).Use various products 112, system generates required resource 116, for example carbon 171, ammonia 176, fertilizer 177, hydrogen 174, methyl alcohol 173, oxygen 172 etc.
System 102 generates parts 160 to various resources and supplies with various products or accessory substance 112, to generate required resource 116.These resources generate parts 160 and comprise:
Be constructed to generate the resource generation parts 161 of oxygen 172 and carbon 171 (for example designing carbon) from carbon dioxide 151;
Be constructed to generate parts 162 with the resource that hydrogen 153 generates methyl alcohol 173 from carbon dioxide 151 or carbon monoxide 152;
Be constructed to generate the resource generation parts 163 of hydrogen 174 and carbon 171 from methane 155;
Be constructed to generate parts 164 from hydrogen 153 and the resource that nitrogen 175 generates ammonia 176;
Be constructed to generate parts 165 from ammonia 176 and the resource that ash content 156 generates suitable fertilizer 177; And/or other resources generate the parts (not shown).
Other details that generate the operation of parts about resource will combine Fig. 3 A-3F to discuss.
Except that using product or accessory substance 112 to generate the resource, system 102 can also store or otherwise utilize product 112 or resource 116 that generated or required.In some cases, system transfers to underground heat storage source 180 via pipeline 181 with methane 155.The storage of methane and the recovery subsequently system that can make can obtain energy, for example through thermal enhancement 182, chemistry gain 183 and/or carrier gain 184, to produce some solvent 185 like methyl alcohol, ammonia and/or water.
Exemplarily, be converted into the carbon reinforcing material through the material 110 with carbon containing and with the parts that are used for various application sustainable economic development be provided, said application comprises the equipment that utilizes the reproducible sun, wind, flowing water and/or geothermal energy resources.The energy production that carbon provides as this application of part of appliance is than much higher times of the energy production that primary combustion provided of this type carbon.In other cases, this type carbon is converted into the transporting equipment parts, and it is lighter and stronger than steel than aluminium, thereby alleviates light weight and improve fuel economy and the unfavorable discharging of minimizing.In other were used, carbon can be by special one-tenth radiator and heat transfer component, and with regard to equal cross-sectional area, it will conduct more heat than copper, thus the scope of the operating temperature that weight reduction and increase suit.In numerous other are used, special carbon deposits and/or coating will for visually for black or the selective surface benefits such as diamond-like hardness and corrosion resistance are provided.
In fact extracting carbon to be incorporated into equal co-producing hydrogen under all situations in the durable goods.It is very cheaply potentially that hydrogen produces through dissociating of source compound such as methane.This is because extract the required energy of hydrogen far below producing the required energy of hydrogen through heat, electricity, radiation or magnetic separation technique dissociate water from most of hydrocarbon.
Through in existing about 1,000,000,000 engines in the world, using hydrogen; The potentiality of sustainable economic development will obtain bringing into play, because will much higher return rate be provided from gasoline or diesel fuel for the previous investment of doing for the such engine of purchase to the appropriate technology of this transformation of using the hydrogen operation.Through Patent Application No. 12/653; 085, Patent Application No. 12/841,170, Patent Application No. 12/804,510, Patent Application No. 12/841; 146, Patent Application No. 12/841; 149, Patent Application No. 12/841,135, Patent Application No. 12/841,509 and Patent Application No. 12/804; In 508 disclosed technical transform for the engine with hydrogen operation can produce more power when needed, continue the longer time and the maintenance that needs still less, and in fact purify the air of its combustion chamber of entering.
Therefore, can make fund can be used for purchasing the carbon enhancement apparatus through fuel cost, raising power-production capacity, the reduction maintenance cost that reduces every EHPH and the return rate that improves the available engine investment that in fact purifies air to utilize renewable resource.Along with the reproducible sun, wind, flowing water and geothermal energy resources are utilized, this provides the commodity and the labor service production capacity of continuous increase for the anti-inflation economic development.Similar with it, because of this conversion, with the renewable nutrient that is provided for living beings and food production from the dependence of fossil fuel and waste treatment being put into practice (comply with one's wishes at the necessary trace mineral of many decades ground restriction, supply the landfill of sulphur body and fixed nitrogen).
In some cases, system is transferred to holder 191 with hydrogen 174 or to one or more energy 190.For example, hydrogen 174 can be supplied with fuel for internal electric source 106 for example is used for engine or fuel cell that auxiliary material dissociates.
Therefore, system 102 uses that renewable resources and renewable energy produce than will produce with conventional process has renewable resource and the energy made with extra care that large economy more is worth, in addition other benefits in addition.System uses this refining renewable resource and energy to gather new renewable resource and energy with sustainable, the pollution-free and non-mode that exhausts.That is to say that the resource to feed system obtains economic multiplier effect through constantly in system, for example in regenerative resource and intrasystem various process, dropping into resource again in system.
For example, system 102 is from the living beings of supplying with dissociate methane and hydrogen, from said methane and hydrogen collection rechargeable energy and resource such as carbon, and uses said carbon to gather more living beings and methane gathering more carbon and hydrogen, or the like.Therefore, system also constantly drops into this resource, other resources and other accessory substances the different energy and process from resource such as the hydrogen that the energy of supplying with takes a morsel again, to capture more substantial institute funding source from intrasystem various resources.This causes the multiplier effect of the amount of various resources that in system regenerative resource gathers and energy, thereby causes from the resource of regenerative resource and the sustainable economic development of energy, in addition other benefits in addition.
Exemplarily, can make hydrogen with from the source such as the carbon dioxide reaction that discharges of bakery, brewery, cement plant or thermal power plant to produce various materials, comprise solvent such as methyl alcohol, ethanol, butanols or oxolane.Such material can be used to provide the compact storage and the transportation of hydrogen, comprises as dissolving the multifunctional usage of the solvent of polarity and non-polar material widely.The extraction that this kind solvent can be realized renewable heat energy and hydrocarbon is reclaimed in storage from the oil and natural gas well of exhaustion, these hydrocarbon otherwise can't be from the extraction of this type well.Therefore, through utilizing existing pipeline and exhausted basically hydrocarbon stratum, the huge storage capacity of renewable hydrogen is provided.
Be in operation, the energy conversion cycles can be extracted beneficial effect with mineral and combine.Liquid storage hydrogen solvent is delivered in the stratum of heating up with the ground hot mode.In one embodiment, liquid is returned the face of land with the value of extracting dissolving with transform the energy of being sent through with the expansion of the steam of ground hot mode heating.In some cases, need near the critical-temperature of solvent and the pressure or on the part in operation gained loop.In another embodiment, the pressure that produced because of thermal enhancement gasifies of high pressure that is provided of post and/or liquid can store degree of depth place or near be utilized.Extract that required mineral are worth and energy after, cooled vapor is with through providing liquid to air or water or intrasystem other material heat extractions.The process of extracting energy and mineral value from the underground heat stratum that the liquid condensate of fluid such as generation like this is used to continue to select.Therefore, this process provides renewable energy production and additional hydrogen, material and can be used as carbon donor is used for utilizing the equipment of renewable energy resource with manufacturing the multiplier effect of supply of raw material.
Use renewable energy to produce resource
The inventor has recognized that, in the resource leaching process, utilizes the regenerative resource system that makes can keep and generate resource, raw material and other entering economically or leaves the material of system.Fig. 2 A is a block diagram, shows some parts 201 of using from the system 102 of feedstock capture resource.System 102 utilizes the energy 108 (for example regenerative resource) and the power supply 106 auxiliary required resources of feedstock capture from being supplied with by raw material source 110.Acquisition component, the extraction parts 110 of Fig. 1 for example are from various materials of feedstock capture or the product of being supplied with by raw material source 110 112.
Use various parts and the process described among this paper; System 102 can gather material and be used for many different purposes, comprise collection with material 202 (for example thinking that fuel cell or solar concentrator provide fuel) from fuel to power supply 106 or regenerative resource 108 that supply with, gather with the material 204 that migrates out system (for example externally to use, to store or the like) and/or gather to supply with the material 206 of more raw materials to raw material source 110.
Fig. 2 B is a block diagram, shows to be used for generating from the product from the process of the feedstock capture resource supplied with or accessory substance some parts 210 of the system 102 of resource.Product 112 is supplied to resource and generates parts 114, and resource generates parts 114 and utilizes the energy from power supply 106 or regenerative resource 108 receptions to generate a kind of or more kinds of resource 116.
Use various parts and the process described among this paper; System 102 can generate resource and be used for many different purposes, comprise collection with resource 212 from fuel to power supply 106 or regenerative resource 108 that supply with (for example think that fuel cell provides fuel or in running provide at the night of solar concentrator system working fluid or fuel), gather with the resource 214 that migrates out system (for example externally to use, to store or the like) and/or gather to generate parts 160 to resource and supply with materials so that generate the material 216 of resource.
Discuss as top, system utilizes multiple resource to generate parts 160 so that the Sustainable Production of resource requirement to be provided.Fig. 3 A-3F is a block diagram, shows the operation of resource generation parts 160 in the system 110.
Fig. 3 A shows resource and generates parts 161, and it is constructed to generate oxygen 172 and carbon 171 (for example designing carbon) from carbon dioxide 151.Resource component 161 is used to carry out various processes 310 from the energy of power supply 106 and/or regenerative resource 108, and the carbon donor such as carbon dioxide or carbon monoxide of dissociating for example as shown in the figure is to provide carbon and oxygen.Be in operation; For example gas or liquid are supplied with hot input area to this type carbon donor with fluid; For example shown in have and supply with the energy of concentrating solar radiation in the conveying worm of counterflow exchange and add the district and dissociate so that heat and/or radiation-induced heat absorption to be provided, as equation 310 or 310 ' in conclude prevailingly:
CO 2+ energy → C+0.5O 2Equation 310
CO+ energy → C+0.5O 2Equation 310 '
Fig. 3 B shows resource and generates parts 162, and it is constructed to generate methyl alcohol 173 from carbon dioxide and/or carbon monoxide 152 with hydrogen 153.Resource component 162 is used to carry out various processes 320 from the energy of power supply 106 and/or regenerative resource 108, for example for equation 320 and 320 for example ' in those example process of being concluded carry out the pressurization of reactant:
CO+2H 2→ CH 3OH equation 320
CO 2+ 3H 2→ CH 3OH+H 2O equation 320 '
Be in operation; Such pressurization can for example water or dissociating of hydrocarbon or another selected compound provide through various hydrogen donors; The volumetric expansion of the hydrogen that wherein prevents to be produced, so as to produce required pressure promote equation 320 and 320 for example ' shown in reaction.
Fig. 3 C shows resource and generates parts 163, and it is constructed to generate hydrogen 174 and carbon 171 from methane 155.Resource component 163 is used to carry out various processes 330 from the energy of power supply 106 and/or regenerative resource 108, for example cause equation 330 and 330 for example ' in the heat of dissociating, electricity and/or the magnetic energy conversion process concluded:
CH 4+ energy → C+2H 2Equation 330
CxHy+ energy → xC+0.5y H 2Equation 330 '
Fig. 3 D shows resource and generates parts 164, and it is constructed to generate ammonia 176 from hydrogen 153 and nitrogen 175.Resource component 164 is used to carry out various processes 340, for example Haber-Bosch process from the energy of power supply 106 and/or regenerative resource 108.An embodiment provides from the mixture of material and has optionally admitted and transportation of hydrogen; So that such hydrogen as disclosed in the top application of submitting to when incorporating into by reference send interface or near with the nitrogen reaction, its through superfluous hydrogen of burning in engine provide nitrogen from the source section depositing of surrounding air for example.Equation 340 has been concluded aerial oxygen and has been closed to produce the process of separable water and nitrogen stream with superfluous hydrogenation.
Air+H 2→ H 2O+N 2+ H 2+ argon gas equation 340
H 2+ N 2+ argon gas → NH 3+ argon gas equation 340 '
Be in operation, air gets into the combustion chamber of engine, and said engine can drive load such as pump or generator.Superfluous hydrogen is used to exhaust the oxygen in the combustion chamber through forming water vapour, said water vapour condensation subsequently or from discharge air-flow, remove through pressure oscillating or temperature swing medium.The much lower residue nitrogen of other components such as argon concentration discharge air-flow pressurized and provide with H-H reaction producing ammonia, like equation 340 ' concluded.Ammonia through condensation separation or in temperature swing or pressure oscillating system with being worth collection like argon gas by medium collection.
Fig. 3 E shows resource and generates parts 165, and it is configured to generate fertilizer 177 from ammonia 176 and ash content 156.Resource component 165 is used to carry out various processes 350 from the energy of power supply 106 and/or regenerative resource 108; For example in an exemplary embodiment; Ammonia and sulfur dioxide and water react as concluding prevailingly in the equation 350 to produce ammonium sulfate, the not trim of this equation:
NH 3+ SO 2+ H 2O → NH 4SO 4Equation 350
Be in operation, suitable reactor provides sulphur source such as the suitable reaction of sulfur oxide (comprising sulfur dioxide) in the presence of water and oxygen.Through utilizing superfluous ammonia, will obtain attractive conversion rate.Carrying out soil or hydroponics fluid test confirms the needs that add mineral such as phosphorus, potassium, iron, manganese, magnesium, calcium, boron, selenium, molybdenum etc. and the suitable prescription with this type additive is provided.
Certainly, system can utilize other resources generation parts or other processes to come the used resource of generation system.
Use the energy of the utilization of resources of extraction from regenerative resource
As discussed herein, system 102 utilizes some described in this paper or whole parts to generate required resource, for example hydrogen or carbon.System uses these resources to realize various purposes, comprises that the resource that use generates is used to the energy from regenerative resource.Fig. 4 is a block diagram, shows to be used to be used to the energy utility system 400 from the energy of renewable resource.
Energy utility system 400 comprises regenerative resource 410, for example solar energy source, wind energy, geothermal energy resources, the flowing water energy etc.Regenerative resource 410 provides energy to energy members 420, the utilization that energy members 420 promotes from the energy of regenerative resource 410.Energy members 420 receives one or more resources from resource component 430.Resource component 430 can be the various parts of system 102, comprises extracting parts 110, one or more resources generation parts 114, pipeline 180, storage/transportation parts 191 and/or miscellaneous part.
In some cases, energy members 420 is to the resource that renewable energy parts 410 provide resource component 430 to be supplied with, and makes the more substantial energy that the renewable energy parts are utilized in the time of can utilizing than unprovided resource.Fig. 5 is a flow chart, shows the program 500 of the utilization of resources energy that use generates.
In step 510, energy utility system 400 receives resource in resource component 430.For example, energy utility system 400 can be the part of system 102 and extract parts 110 (promptly after raw material dissociates) certainly or receive resource from one or more resources generation parts 114.
In step 520, energy utility system 400 possibly supplied with the resource that is received to regenerative resource 410 via energy members 420.For example, system 400 supplies with one or more resources to regenerative resource, and said resource can or strengthen the reaction that takes place at regenerative resource 410 places as fuel.
In step 530, regenerative resource 410 is used the utilization of resources energy of being supplied with.In the energy capture process, the more substantial energy that regenerative resource can be adopted or otherwise utilize resource to be captured when utilizing than unprovided resource.
For example, energy utility system 400 can be through supplying with the utilization that oxygen, burns oxygen focus on the temperature of the hot-zone that wherein receives solar energy with the lifting solar collector and the capture energy promotes solar collector place solar energy from the hot-zone to solar collector.About through supply with to regenerative resource renewable resource utilize the further details of energy quote above being found in and the application common co-pending incorporated in.
In some cases, renewable energy parts 410 provide energy to promote the extraction or the generation of resource to resource component 430.Fig. 6 is a flow chart, shows use from the Energy extraction of regenerative resource or the program 600 of generation resource.
In step 610, energy utility system 400 is from the regenerative resource received energy.For example, system can be from received energies such as solar energy source, wind energy, the flowing water energy.The energy that is received can be the energy of collecting from said source, perhaps can be the energy since other resource acquisitions of regenerative resource received energy.
In step 620, energy utility system 400 generates the parts energize to extracting parts or resource.For example, system 400 can be to extracting the parts energize, and said extraction parts for example carry out electrolysis with from the extraction of raw material separation of hydrogen and oxygen or the parts 140 that dissociate.
In step 630, Energy extraction that energy utility system 400 usefulness are supplied with or generation resource.Extraction parts 110 or resource generation parts 114 can be adopted or otherwise utilize the energy of being supplied with, and control or otherwise influence extraction or generative process, the for example electrolysis of material or burning.
For example, energy utility system 400 can promote that hydrogen and oxygen are from the production of water in the electrolytic cell through supply with the electricity of collecting from solar energy source to the electrode of electrolytic cell, and said electricity applies voltage and makes water decomposition Cheng Qing and oxygen between electrode.Further details about using regenerative resource to extract or generate resource are found in the application of incorporating into through top quoting common co-pending.
As discussed herein, energy that utilize in the energy utility system 400 and/or resource can be by system 102 in order to carrying out some or all processes of system 102, thereby produce required resource.For example, system 102 can receive the hydrogen that extracts with energy utility system 400, makes some hydrogen and air burning with generation water and nitrogen, and some hydrogen and the nitrogen that is generated are reacted to produce ammonia or ammonia derivative.And for example, system 102 can receive the hydrogen that extracts with energy utility system 400 and hydrogen and the carbon that is generated are reacted to produce methane.And for example, system 102 can receive the hydrogen that extracts with energy utility system 400 and make hydrogen and the resource of the oxide of carbon reaction with generation carbon, hydrogen and oxygen.
Therefore, through to resource extraction/generation parts energy being provided, it is then to the regenerative resource provisioning resources, and system utilizes energy with continuable mode.Such circulation behavior makes renewable production and the reproducible utilization of energy or the sustainable economic development that captures that realizes higher resource output, more substantial energy acquisition and concentrate on resource to also have other benefits in addition.
The whole bag of tricks of describing among this paper, parts and system produce the renewable thing (for example energy, material resources and nutrient) of system simultaneously with interrelated and continuable mode.Compare with the productive rate from conventional system, so inter-related production helps to improve the productive rate of resource and energy, because such system has utilized resource more efficiently.Said efficient utilization makes more substantial energy trap and therefore bring bigger economic development from regenerative resource (the for example sun, wind, water).
Conclusion
Only if explicitly call in the context, otherwise in whole specification and claims, word " comprises " etc. and to be understood to include meaning rather than exclusive or detailed meaning; That is to say that meaning is " including but not limited to ".Use the word of odd number or plural number also to comprise plural number or odd number respectively.When the right claim used during in the tabulation of mentioning two or more projects word " or " time, all description belows of word contained in this word: all items in any project in the tabulation, the tabulation and the combination in any of the project in the tabulation.
Above-described various embodiment is capable of being combined so that other embodiment to be provided.Mention in this specification and/or the application MSDS in the open case of listed all United States Patent (USP) cases, U.S. Patent application, patent application, foreign patent case, foreign patent application case and non-patent publications all be incorporated herein in full by reference.If desired, can revise aspect of the present disclosure and other embodiment of the present disclosure are provided with the principle that employing has heteroid fuel injector and igniter and different patent case, application case and open case.
Can be according to top detailed description to the change of disclosure work these and other.Usually, in subsidiary claims, used term should not be construed as the disclosure is limited to disclosed specific embodiment in this specification and claims, and is interpreted as containing all system and methods by claims operation.Therefore, the present invention does not receive said disclosed restriction, but its scope is broadly confirmed by subsidiary claims.

Claims (68)

1. system that realizes sustainable economic development, said system comprises:
Extract parts, wherein said extraction parts are constructed to authigenic material and extract carbon; With
Energy members, wherein said energy members are constructed to use the carbon that is extracted to be used to the energy from regenerative resource.
2. system according to claim 1, wherein said energy members are constructed to from the energy of said renewable energy utilization amount greater than the amount of the energy that utilizes from the carbon that uses combustion engine, fuel cell or thermoelectric element oxidation to extract.
3. system according to claim 1, said system also comprises:
The accessory substance parts, wherein said accessory substance parts are constructed to:
Use said regenerative resource and by said extraction parts from said living beings extract a kind of
Or multiplely do not generate accessory substance based on the material of carbon; With
To said regenerative resource the accessory substance that is generated is provided.
4. system according to claim 1, said system also comprises:
Accessory substance parts, wherein said accessory substance parts be constructed to use said regenerative resource and extract from said living beings by said extraction parts one or more do not generate accessory substance based on the material of carbon.
5. system according to claim 1, wherein said extraction parts comprise the parts that dissociate that are constructed to make with the mode of heat said living beings dehydrogenation.
6. system according to claim 1, wherein said extraction parts comprise the parts that dissociate that are constructed to make with the mode of electricity said living beings dehydrogenation.
7. system according to claim 1, wherein said extraction parts comprise the parts that dissociate that are constructed to make with the mode of light said living beings dehydrogenation.
8. system according to claim 1, wherein said extraction parts are constructed in the process of extracting carbon from said living beings from said energy members received energy.
9. system according to claim 1, wherein said regenerative resource are solar concentrator.
10. system according to claim 1, wherein said regenerative resource are the flowing water energy.
11. system according to claim 1, wherein said regenerative resource are wind energy.
12. a system that realizes sustainable economic development, said system comprises:
Extract parts, wherein said extraction parts are constructed to the extraction hydrogen from the water source; With
Energy members, wherein said energy members are constructed to use the hydrogen that is extracted to be used to the energy from regenerative resource.
13. system according to claim 12, wherein said extraction parts from said regenerative resource received energy to extract said hydrogen from said water source.
14. system according to claim 12, wherein said water source comprises source of seawater.
15. system according to claim 12, wherein said water source comprises the industrial wastewater source.
16. system according to claim 12, wherein said water source comprises the agricultural effluent source.
17. system according to claim 12, wherein said water source comprises source of sewage.
18. system according to claim 12, wherein said water source comprises the landfill yard waste water source.
19. system according to claim 12, wherein said extraction parts comprise the parts that dissociate that are constructed to other the material dissociates hydrogen of mode in said water source of heat.
20. system according to claim 12, wherein said extraction parts comprise the parts that dissociate that are constructed to other the material dissociates hydrogen of mode in said water source of electricity.
21. system according to claim 12, wherein said extraction parts comprise the parts that dissociate that are constructed to other the material dissociates hydrogen of mode in said water source of light.
22. system according to claim 12, wherein said extraction parts comprise the parts that dissociate that are constructed to other the material dissociates hydrogen of mode in said water source of magnetic.
23. system according to claim 12, wherein said extraction parts comprise the parts that dissociate that are constructed to other the material dissociates hydrogen of mode in said water source of heat.
24. system according to claim 12, wherein said regenerative resource are solar concentrator.
25. system according to claim 12, wherein said regenerative resource are wind energy.
26. system according to claim 12, wherein said regenerative resource are the flowing water energy.
27. system according to claim 12, wherein said regenerative resource are geothermal energy resources.
28. a method that realizes sustainable economic development, said method comprises:
From raw material dissociate two kinds or more kinds of material, wherein saidly comprise from regenerative resource and provide energy to carry out said dissociating with auxiliary from dissociate two kinds or more kinds of material of raw material; With
Use said renewable energy to be derived from said two kinds or more kinds of material extraction hydrogen that dissociates.
29. method according to claim 28, said method also comprises:
First's further dissociating with auxiliary material of the hydrogen that is extracted is provided to said regenerative resource; With
Parts to producing electricity provide the generation of the second portion of the hydrogen that is extracted with auxiliary electrical.
30. method according to claim 28, said method also comprises:
The first of the hydrogen that burning is extracted and air are to produce water and nitrogen; With
The second portion that makes the hydrogen that is extracted and the nitrogen that is produced reaction are to produce ammonia or derived from the resource of ammonia.
31. method according to claim 28, said method also comprises:
Make the hydrogen and the carbon donor that are extracted react the resource that comprises carbon and hydrogen with generation.
32. method according to claim 28, said method also comprises:
Make the oxide reaction of the hydrogen that extracted and carbon comprise the resource of carbon, hydrogen and oxygen with generation.
33. a system that realizes sustainable economic development, said system comprises:
The raw material parts, wherein said raw material parts are constructed in said system, supply raw materials;
Be used for extracting from the raw material that is provided the resource extraction subsystem of resource requirement, wherein said resource is extracted subsystem and is comprised:
Separating component, wherein said separating component are constructed to separate required resource from the raw material that is provided; With
Energy members, wherein said energy members are constructed to said separating component the separation from said raw material of resource that energy needs with auxiliary block post is provided;
Additional resource generates subsystem, and said additional resource generates subsystem and is used for the accessory substance generation additional resource in said separating component after separating required resource from said raw material, and wherein said additional resource generates subsystem and comprises:
Accessory substance receiving-member, wherein said accessory substance receiving-member are constructed to be received from one or more accessory substances that said raw material separates resource requirement; With
Energy members, wherein said energy members are constructed to provide energy so that said one or more accessory substances in the said accessory substance receiving-member are converted into additional resource.
34. system according to claim 33, wherein said raw material parts provide carbonaceous material in said system; With
Wherein said separating component is from the carbonaceous material that the provided carbon that dissociates.
35. system according to claim 33, wherein said separating component is to carry out thermal dissociation to separate the parts that dissociate of resource requirement from the raw material that is provided.
36. system according to claim 33, wherein said separating component is to carry out electrolysis from the parts that dissociate that separate resource requirement with the raw material that is provided certainly.
37. system according to claim 33, wherein said separating component is to carry out photodissociation to separate the parts that dissociate of resource requirement from the raw material that is provided.
38. system according to claim 33, wherein said separating component is to carry out magnetic to dissociate to separate the parts that dissociate of resource requirement from the raw material that is provided.
39. system according to claim 33, the said energy members that wherein said resource is extracted subsystem is the rechargeable energy parts.
40. system according to claim 33, the said energy members that wherein said resource is extracted subsystem is a solar concentrator.
41. system according to claim 33, the said energy members that wherein said resource is extracted subsystem is the flowing water energy.
42. system according to claim 33, the said energy members that wherein said resource is extracted subsystem is a wind energy.
43. system according to claim 33, wherein said accessory substance comprises carbon dioxide, and said additional resource comprises oxygen and carbon.
44. system according to claim 33, wherein said accessory substance comprises carbon monoxide and hydrogen, and said additional resource comprises methyl alcohol.
45. system according to claim 33, wherein said accessory substance comprises methane, and said additional resource comprises hydrogen and carbon.
46. system according to claim 33, wherein said accessory substance comprises hydrogen, and said additional resource comprises ammonia.
47. system according to claim 33, wherein said accessory substance comprises ash content, and said additional resource comprises fertilizer.
48. a method that realizes sustainable economic development, said method comprises:
From raw material dissociate two kinds or more kinds of material, wherein saidly comprise from regenerative resource and provide energy to carry out said dissociating with auxiliary from dissociate two kinds or more kinds of material of raw material; With
Use said renewable energy to be derived from least a extraction carbon in said two kinds or the more kinds of material that dissociates.
49. according to the described method of claim 48, the wherein said at least a material that dissociates comprises carbon dioxide.
50. according to the described method of claim 48, the wherein said at least a material that dissociates comprises carbon monoxide.
51. according to the described method of claim 48, the wherein said at least a material that dissociates comprises methane.
52. according to the described method of claim 48, said method also comprises:
Provide carbon-free a kind of in said two kinds or the more kinds of material that dissociates to said regenerative resource.
53. according to the described method of claim 48, said method also comprises:
As a kind of in said two kinds or the more kinds of material that dissociates during, said hydrogen is provided to said regenerative resource for hydrogen.
54. according to the described method of claim 48, a kind of not carbon containing in the wherein said material that dissociates, said method also comprises:
Provide said a kind of carbon-free dissociation substance to generate methyl alcohol to said regenerative resource.
55. according to the described method of claim 48, a kind of not carbon containing in the wherein said material that dissociates, said method also comprises:
Provide said a kind of carbon-free dissociation substance to generate ammonia to said regenerative resource.
56. according to the described method of claim 48, a kind of not carbon containing in the wherein said material that dissociates, said method also comprises:
Provide said a kind of carbon-free dissociation substance to generate fertilizer to said regenerative resource.
57. one kind is used for the process that energy transforms; Said process comprises the step that one or more flowing materials is filled to geo-logical terrain; Purpose is selected from the gain of heat, store chemistry and/or pressure off and on can and extract valuable material from said stratum; Wherein in one or more energy conversion devices, accomplish acting by at least a in said one or more flowing materials, at least a in wherein said one or more flowing materials is adjusted to the state that the liquid that is selected from liquid, mixing and steam, steam or gas are provided and sent to drive said one or more energy conversion device.
58. according to the described process of claim 57, wherein said geo-logical terrain hydrocarbonaceous.
59. according to the described process of claim 57, wherein after one or more flowing materials were filled to geo-logical terrain, said one or more flowing materials received supplemental heat from the source that is selected from the sun, industry, commerce and Thermal Motor source.
60. according to the described process of claim 57; Wherein said fluid is delivered to geo-logical terrain, purpose is selected from and stores chemical potential energy, pressure store potential energy, stores chemistry and pressure potential, from said stratum to said fluid heat transferring, the existence because of said fluid produces material to the transfer of said fluid with from said stratum from the material on said stratum.
61. one kind is used to the process that produces and utilize underground heat to produce and send the fluid that is selected from carbon dioxide, methane and hydrogen, purpose is selected from water plant planting, hothouse plants plantation, the plantation of hydroponics plant and as the working fluid of the one or more energy conversion devices of operation.
62. according to the described process of claim 61, wherein said water plant is selected from algae.
63. an extraction system, said extraction system comprises:
Extract carbon or hydrogen from carbon donor or hydrogen donor compound, wherein said hydrogen is used in after one or many is stored in one or more geo-logical terrains off and in the subsystem application one or more localities or a distance.
64. according to the described system of claim 63, said system also comprises:
Said device is supported different micro climate districts;
Said district also comprises the subarea; With
Said subarea contains unique heat, humidity, natural resources maybe can handle the energy transfer characteristics with acting.
65. a sustainable economic development automotive engine system, said system comprises:
The Economic Stimulus method that is used to boost productivity;
Be used to remove the method for the unfavorable factor that reduces productivity ratio;
Be used for the method that creates jobs in kind of a breed, manufacturing, production of energy, information and field of energy management; With
Be used to implement the method for the macroeconomy algorithm of sustainability;
Agro-farming in micro climate (artificial) population (continuable city);
Farm equipment from the carbon that extracts; With
Health benefit.
66. an agro-farming process, said process comprises:
One-tenth through reducing the used energy of kind of plant improved the method for crop yield originally;
Through being turned back to soil, the trace mineral reduce method to the needs of fertilizer;
With the method for algae to crop fertilization;
Water management system;
Energy production and management system;
CO2 is to improve crop productivity potential;
Be used for planting the system of plant at micro climate, said system can seal as required or monitoring of environmental to increase air (rising/down current) or precipitation; With
Macroscopic view food production system is to gather carbon or hydrogen from crop discarded object (stem, bar, hay).
A the system 67. fish lays eggs, said system comprises:
Nutrient, oxygen and the clear water method to support that fish lays eggs is provided;
Be used to monitor and control the system of temperature to provide environment to support; With
From living beings/liquid extraction protein, carbohydrate, fat, vitamin, mineral nutraceutical system as fish.
68. a poultry, pig, ox (animal-breeding) system, said system comprises:
The system of cultivated animals in controlled environment;
Be used to not have the system of agricultural chemicals or fertilizer ground kind plant;
Through extracting hydrogen and the water management system of purified water from acid rain and other acidifying water sources (comprising the water that is adjusted to the acidifying state with reducing agent);
Be used to adopt the system of crop drip irrigation.
CN201080048870.6A 2009-08-27 2010-08-16 Sustainable economic development through integrated production of renewable energy, materials resources, and nutrient regimes Expired - Fee Related CN102712019B (en)

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US23747609P 2009-08-27 2009-08-27
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US61/304,403 2010-02-13
US12/707,651 2010-02-17
US12/707,653 US8172990B2 (en) 2009-02-17 2010-02-17 Apparatus and method for controlling nucleation during electrolysis
PCT/US2010/024498 WO2010096504A1 (en) 2009-02-17 2010-02-17 Apparatus and method for controlling nucleation during electrolysis
PCT/US2010/024497 WO2010096503A1 (en) 2009-02-17 2010-02-17 Electrolytic cell and method of use thereof
PCT/US2010/024499 WO2010096505A1 (en) 2009-02-17 2010-02-17 Apparatus and method for gas capture during electrolysis
USPCT/US10/24498 2010-02-17
USPCT/US10/24497 2010-02-17
USPCT/US10/24499 2010-02-17
US12/707,656 2010-02-17
US12/707,656 US8075749B2 (en) 2009-02-17 2010-02-17 Apparatus and method for gas capture during electrolysis
US12/707,653 2010-02-17
US12/707,651 US8075748B2 (en) 2009-02-17 2010-02-17 Electrolytic cell and method of use thereof
US34505310P 2010-05-14 2010-05-14
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