CN102512922A - Method for cracking and separating carbon dioxide by using ultra-high temperature - Google Patents
Method for cracking and separating carbon dioxide by using ultra-high temperature Download PDFInfo
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- CN102512922A CN102512922A CN2011103241082A CN201110324108A CN102512922A CN 102512922 A CN102512922 A CN 102512922A CN 2011103241082 A CN2011103241082 A CN 2011103241082A CN 201110324108 A CN201110324108 A CN 201110324108A CN 102512922 A CN102512922 A CN 102512922A
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- carbon dioxide
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- reaction kettle
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- Y—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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
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- Y—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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
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- Y—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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Y—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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/133—Renewable energy sources, e.g. sunlight
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- Y—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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/151—Reduction of greenhouse gas [GHG] emissions, e.g. CO2
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Abstract
The invention relates to a method for cracking and separating carbon dioxide by using ultra-high temperature. The method is characterized in that the method comprises steps that: a, carbon dioxide discharged from coal chemical plants, carbon dioxide ore in the stratum, and carbon dioxide produced in thermoelectric power plants and fuel gas power plants are filled into a reaction kettle through pipelines; b, a combined heat polymerization energy of solar energy, wind energy, and pyroelectricity is adopted, and a temperature inside the reaction kettle is increased to 4000-6000 DEG C in a phased manner by using a two-stage heat polymerization energy boiler; through a thermal cracking and separating effect in the reaction kettle, carbon dioxide is converted into carbon monoxide, oxygen, carbon synthetic compounds, synthesized diamond, and the like through ultra-high temperature cracking and separating. According to the invention, the heat polymerization energy boiler and the ultra-high temperature reaction kettle are adopted; heat polymerization is carried out by using a combined energy of solar energy, wind energy, and fuel gas electricity; carbon dioxide is heated to a temperature above 2450 DEG C in the reaction kettle, and can automatically crack into carbon monoxide and oxygen or artificial diamond. The method brings a high economic value, and has energy-saving and environment-friendly characteristics.
Description
Technical field
The present invention relates to a kind of carbon dioxide cracking technique, concrete is a kind of energy-saving and environmental protection technology of utilizing the strong Pintsch process separating carbon dioxide of associating cumulative agitated reactor.
Background technology
Human coal combustion, oil, natural gas and trees; Produce and make earth intensification after great amount of carbon dioxide and methane get into atmosphere, make carbon cycle unbalance, changed the power conversion form of global biosphere; Since the industrial revolution; Carbon dioxide content has increased by 25% in the atmosphere, considerably beyond whole historical records in the past 160,000 years that scientist possibly survey out, and does not still have the sign that slows down at present.
The CO2 emissions increase is the root that causes terrestrial climate to warm in the atmosphere; The survey showed that for of International Energy Agency; The U.S., China, Russia and Japanese CO2 emissions almost account for the half the of global total amount, and investigation shows that U.S.'s CO2 emissions occupy first place in the world; Year is about 20 tons of CO2 emissions per capita, and the carbon dioxide of discharging accounts for 23.7% of global total amount.China year per capita CO2 emissions be about 2.51 tons, account for 13.9% of global total amount.
A series of problems such as global warming, the unusual weather conditions that a large amount of discharging carbon dioxide cause, sea level rise have become each national major issue of the present whole world.
Summary of the invention
To the problems referred to above, the objective of the invention is to propose a kind of method of strong Pintsch process separating carbon dioxide.This method is utilized hot polymerization ability pot, strong pyroreaction still; Adopting solar energy, wind energy and the fuel gas generation associating energy to carry out hot polymerization can; In agitated reactor, carbon dioxide is heated to more than 2450 ℃; Carbon dioxide can automatically be cracked into carbon monoxide and oxygen or produce diamond, has the characteristics of higher economic value and energy-saving and environmental protection preferably.
The objective of the invention is to realize through following technical scheme: the method for strong Pintsch process separating carbon dioxide is characterized in that may further comprise the steps:
A, the carbon dioxide that the carbon dioxide of coalification factory discharging, the carbon dioxide ore deposit in the stratum, steam power plant, plant gas are produced fill in the agitated reactor through pipeline;
B, can with solar energy, wind energy, combined heat and power hot polymerization; Through secondary hot polymerization ability pot; Stage by stage the agitated reactor internal temperature is promoted to 4000-6000 ℃, separates converting carbon dioxide to carbon monoxide, oxygen, carbon synthetic and diamond synthesis etc. through strong Pintsch process separation through the agitated reactor thermal cracking;
C, semi liquid state carbon dioxide per ton are convertible into oxygen 40%, carbon monoxide 50%, other carbonizable substance 10% after separating through strong Pintsch process;
D, oxygen recovery are supplied with factory's gasification and system wet goods; The synthetic oil that converts to of carbon monoxide and hydrogen; Carbonizable substance is used for industry.
The present invention is with hot polymerization ability pot, strong pyroreaction still; Adopting solar energy, wind energy and the fuel gas generation associating energy to carry out hot polymerization can; In agitated reactor, carbon dioxide is heated to more than 2450 ℃; Carbon dioxide can automatically be cracked into carbon monoxide and oxygen or produce diamond, has the effect of higher economic value and energy-saving and environmental protection preferably, and the UIT that belong to energy-saving and emission-reduction, environmental protection, makes harmful substance become clean energy resource learns a skill; This technology will be got huge effect on minimizing world carbon emission problem, let carbon dioxide become the environmental protection clean energy resource from nuisance.
Basic principle:
Through a kind of brand-new mode, adopt solar energy, wind energy and the fuel gas generation associating energy to carry out the hot polymerization ability, in agitated reactor, carbon dioxide is heated to more than 2450 ℃, carbon dioxide can automatically be cracked into carbon monoxide and oxygen or produce diamond.Chemical equation: 2CO
2(high temperature)=＞2CO+O
2CO
2(high temperature)=＞C+O
2
Description of drawings
Fig. 1 is a principle schematic of the present invention;
The specific embodiment
Below in conjunction with accompanying drawing and embodiment the present invention is done further explanation:
Embodiment: referring to accompanying drawing 1, the method for strong Pintsch process separating carbon dioxide is characterized in that may further comprise the steps:
A, the carbon dioxide that the carbon dioxide of coalification factory discharging, the carbon dioxide ore deposit in the stratum, steam power plant, plant gas are produced fill in the agitated reactor through pipeline;
B, can with solar energy, wind energy, combined heat and power hot polymerization; Through secondary hot polymerization ability pot; Stage by stage the agitated reactor internal temperature is promoted to 4000-6000 ℃, separates converting carbon dioxide to carbon monoxide, oxygen, carbon synthetic and diamond synthesis etc. through strong Pintsch process separation through the agitated reactor thermal cracking;
C, semi liquid state carbon dioxide per ton are convertible into oxygen 40%, carbon monoxide 50%, other carbonizable substance 10% after separating through strong Pintsch process;
D, oxygen recovery are supplied with factory's gasification and system wet goods; The synthetic oil that converts to of carbon monoxide and hydrogen; Carbonizable substance is used for industry.
Claims (1)
1. the method for a strong Pintsch process separating carbon dioxide is characterized in that may further comprise the steps:
A, the carbon dioxide that the carbon dioxide of coalification factory discharging, the carbon dioxide ore deposit in the stratum, steam power plant, plant gas are produced fill in the agitated reactor through pipeline;
B, can with solar energy, wind energy, combined heat and power hot polymerization; Through secondary hot polymerization ability pot; Stage by stage the agitated reactor internal temperature is promoted to 4000-6000 ℃, separates converting carbon dioxide to carbon monoxide, oxygen, carbon synthetic and diamond synthesis etc. through strong Pintsch process separation through the agitated reactor thermal cracking;
C, semi liquid state carbon dioxide per ton are convertible into oxygen 40%, carbon monoxide 50%, other carbonizable substance 10% after separating through strong Pintsch process;
D, oxygen recovery are supplied with factory's gasification and system wet goods; The synthetic oil that converts to of carbon monoxide and hydrogen; Carbonizable substance is used for industry.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011103241082A CN102512922A (en) | 2011-10-24 | 2011-10-24 | Method for cracking and separating carbon dioxide by using ultra-high temperature |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011103241082A CN102512922A (en) | 2011-10-24 | 2011-10-24 | Method for cracking and separating carbon dioxide by using ultra-high temperature |
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| Publication Number | Publication Date |
|---|---|
| CN102512922A true CN102512922A (en) | 2012-06-27 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2011103241082A Pending CN102512922A (en) | 2011-10-24 | 2011-10-24 | Method for cracking and separating carbon dioxide by using ultra-high temperature |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103357257A (en) * | 2013-08-05 | 2013-10-23 | 唐立刚 | Pyrolysis separation method for carbon dioxide through |
| CN114687820A (en) * | 2022-03-30 | 2022-07-01 | 刘小江 | Cogeneration device and method based on carbon dioxide conversion and utilization |
-
2011
- 2011-10-24 CN CN2011103241082A patent/CN102512922A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103357257A (en) * | 2013-08-05 | 2013-10-23 | 唐立刚 | Pyrolysis separation method for carbon dioxide through |
| CN114687820A (en) * | 2022-03-30 | 2022-07-01 | 刘小江 | Cogeneration device and method based on carbon dioxide conversion and utilization |
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Application publication date: 20120627 |