CN201799208U - Novel energy storing device based on carbon dioxide - Google Patents
Novel energy storing device based on carbon dioxide Download PDFInfo
- Publication number
- CN201799208U CN201799208U CN201020144405XU CN201020144405U CN201799208U CN 201799208 U CN201799208 U CN 201799208U CN 201020144405X U CN201020144405X U CN 201020144405XU CN 201020144405 U CN201020144405 U CN 201020144405U CN 201799208 U CN201799208 U CN 201799208U
- Authority
- CN
- China
- Prior art keywords
- purification
- electrochemical
- carbon dioxide
- energy
- solidification
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Classifications
-
- 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
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
-
- 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
Landscapes
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model discloses a novel energy storing device based on carbon dioxide, which comprises an industrial waste gas discharging passage, a CO2 (carbon dioxide) purification absorbing device, a CO2 purification releasing device, a CO2 electrochemical curing device, a fuel cell and a CO2 electrochemical curing power supply deice, wherein the CO2 purification absorbing device is arranged inside the industrial waste gas discharging passage, and is connected with the CO2 purification releasing device through a circulation loop; the CO2 purification releasing device, the CO2 electrochemical curing device and the fuel cell are sequentially connected through a gas transmission pipeline; and the CO2 electrochemical curing power supply deice is electrically connected with the CO2 electrochemical curing device. The novel energy storing device integrates purification recovery of CO2, the electrochemical curing of CO2 and power generation into a whole, can effectively reduce CO2 discharge during the industrialization process, alleviates global warming, and is characterized by simplicity and actual effect.
Description
Technical field
The utility model relates to a kind of novel energy-storing device based on carbon dioxide.
Background technology
The solution route of current energy crisis comprises 1) saving of the energy; 2) exploitation of new forms of energy.The former relates to the rational use energy; The latter then comprises the utilization of tide energy, wind energy, solar energy etc.No matter be reasonably to use the energy or the exploitation of new forms of energy, all relate to the temporary transient storage problem of energy, this relates to the exploitation of novel energy-storing system again.At present, traditional energy storage system comprises electrochemical capacitor, various secondary cell, and the power station utilizes unnecessary electricity again water to be extracted into high water level, or the like.The natural energy storage mode of occurring in nature is to utilize solar energy with carbon dioxide biological curing process, the research emphasis that to imitate this biological thermal energy storage process also be present scientific circles; In addition, the first cause that terrestrial climate warms is the increase of carbon dioxide content on the earth, and therefore, the carbon dioxide that can utilize course of industrialization to produce again also just has important meaning for the greenhouse effects that slow down the earth.
At present, though the purification of the carbon dioxide that produces relevant for course of industrialization, the research of the curing of carbon dioxide and storage etc., the report or the patent that are based on the energy storage method/equipment of carbon dioxide material are not also seen.
Summary of the invention
The utility model purpose is: provide a kind of novel energy-storing device based on carbon dioxide, this device collection CO
2Purification recovery, electrochemical solidification, generate electricity in one, can effectively reduce the CO in the course of industrialization
2Discharge capacity is alleviated global greenhouse effect, has the characteristics of easy actual effect.
The technical solution of the utility model is: a kind of novel energy-storing device based on carbon dioxide, it comprises industrial gas emission passage, CO
2Purification absorption plant, CO
2Purification releasing device, CO
2Electrochemical solidification device, fuel cell and CO
2The electrochemical solidification power supply device, described CO
2The purification absorption plant is arranged in the industrial gas emission passage, and with described CO
2The purification releasing device links to each other by closed circuit, described CO
2Purification releasing device, CO
2Electrochemical solidification device and fuel cell are linked in sequence by the gas delivery tube road, and described CO
2Electrochemical solidification power supply device and CO
2The electrochemical solidification device is electrically connected.
Device described in the utility model also comprises the extractor fan that is arranged in the industrial gas emission passage, and described extractor fan is electrically connected with described fuel cell electric energy output.
Device described in the utility model also comprises fuel cell CO
2Purifying plant is used for reclaiming and CO that the fuel cell electric discharge course of reaction of purifying is produced
2, and described fuel cell CO
2Purifying plant inserts CO by transfer conduit
2The electrochemical solidification device.
CO described in the utility model
2Purification absorption plant and CO
2The purification medium that circulates in the closed circuit of purification releasing device is the aqueous solution of ammoniacal liquor or amine substance.
CO described in the utility model
2Purification absorption plant and CO
2The purification medium that circulates in the closed circuit of purification releasing device also can be to CO
2The solid absorbent that special efficacy absorption is arranged.
CO described in the utility model
2The negative electrode that the electrochemical solidification device adopts is the two or more alloy in Ni, Cu, Sn, Ag, Pt, Zr, Ti, Co, these metals of Pb, the anode that described electrolysis is adopted is the two or more alloy among metal Pt, Pd, Ag, the Ni, and the electrolyte that described electrolysis is adopted is Li
2SO
4, Li
2CO
3, LiNO
3, Na
2SO
4, Na
2CO
3, NaNO
3, K
2SO
4, K
2CO
3, KNO
3The mixed solution of one or more in these electrolyte, solvent are a kind of or several mixed solvents in the alcohols solvents such as water or methyl alcohol, ethanol, propyl alcohol, and it is saturated that the electrolyte concentration scope is that 0.01M arrives, and Faradaic current is 1-200mA/cm
2, the electrolysis temperature scope is-40~80 ℃.
CO described in the utility model
2The electrochemical solidification power supply device is the association of solar cell or solar cell and energy-storage battery, and described energy-storage battery is lithium ion battery or lead-acid battery.
CO described in the utility model
2The electrochemical solidification power supply device also can be the association of wind-driven generator or wind-driven generator and energy-storage battery, and described energy-storage battery is lithium ion battery or lead-acid battery.
The utility model has the advantages that:
The utility model is based on the novel energy-storing device of carbon dioxide, and its advantage is as follows:
1. the CO in can more efficiently minimizing course of industrialization
2Discharge capacity is alleviated global greenhouse effect.
2. compared with prior art (as with CO
2Bury at the deep-sea), the utility model can be thoroughly with CO
2Convert organic molecule to, do not exist the carbon dioxide that is cured to be released to the possibility of atmosphere again.
The utility model is based on the novel energy-storing device of carbon dioxide, and it collects CO
2Purification recovery, electrochemical solidification, generate electricity in one, the long-distance transport process in the middle of having avoided has the characteristics of easy actual effect; And the electric energy that this device produces can directly apply to himself, and electrochemical solidification process energy for example is provided, or as CO
2The power of purifying.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further described:
Fig. 1 is the structural representation of the utility model device.
Wherein: A, industrial gas emission passage; B, CO
2The purification absorption plant; C, CO
2The purification releasing device; D, CO
2The electrochemical solidification device; E, fuel cell; F, CO
2The electrochemical solidification power supply device; G, extractor fan; H, fuel cell CO
2Purifying plant.
The specific embodiment
Embodiment 1: below in conjunction with device shown in Figure 1 the utility model is explained in detail and illustrates:
Present embodiment provides this novel energy-storing device based on carbon dioxide is by industrial gas emission passage A, CO
2Purification absorption plant B, CO
2Purification releasing device C, CO
2Electrochemical solidification device D, fuel cell E, CO
2Electrochemical solidification power supply device F, extractor fan G, fuel cell CO
2Purifying plant H and respective transmissions pipeline are formed jointly.Described CO
2Purification absorption plant B is arranged in the industrial gas emission passage A, and with described CO
2Purification releasing device C links to each other by closed circuit; Described CO
2Purification releasing device C, CO
2Electrochemical solidification device D and fuel cell E are linked in sequence by the gas delivery tube road, and described CO
2Electrochemical solidification power supply device F and CO
2Electrochemical solidification device D is electrically connected.Described extractor fan G is arranged in the industrial gas emission passage A, and is electrically connected with described fuel cell E electric energy output end.Described fuel cell CO
2Purifying plant H inserts CO by transfer conduit
2Electrochemical solidification device D.
CO described in the present embodiment
2Purification absorption plant B and CO
2The purification medium of selecting for use in the closed circuit between the purification releasing device C is an ammoniacal liquor.Described CO
2The negative electrode that electrolysis is adopted among the electrochemical solidification device D is the alloy of metal Ni, Cu, and anode adopts the alloy of metal Pt, Pd, and electrolyte is Na
2SO
4Solution, solvent are water and ethanol mixed solvent, and the electrolyte concentration scope is 0.02M, and Faradaic current is 50mA/cm
2, electrolysis is carried out under 25 ℃ of conditions of normal temperature.Described CO
2Electrochemical solidification power supply device F adopts the association of solar cell and lithium ion battery, and extractor fan G is a blower fan.
The concrete course of work of the described device of present embodiment is as follows:
Under the swabbing action of extractor fan G, contain high concentration CO
2Industrial waste gas enters from the inlet of industrial gas emission passage A, at CO
2Purification absorption plant B is interior by WITH AMMONIA TREATMENT, CO wherein
2Absorbed by ammoniacal liquor, remaining gas is then emitted and from the outlet of the industrial gas emission passage A (CO from the gas that discharge in the exit that comes out
2Content is very low).Contain high concentration CO
2Ammoniacal liquor by closed circuit be transferred to CO
2Among the purification releasing device C, at CO
2Contain high concentration CO among the purification releasing device C
2Ammoniacal liquor discharge wherein CO
2, discharged CO
2Low CO
2Content ammoniacal liquor then returns CO by another of closed circuit
2Purification absorption plant B, and continue to absorb CO there
2By ammoniacal liquor to CO
2Absorption that moves in circles and release, reaching purifies concentrates CO
2Purpose.At CO
2The high-purity CO that obtains among the purification releasing device C
2Be transferred to CO
2Among the electrochemical solidification device D, CO there
2Be electrochemically reduced to organic molecule such as formaldehyde, formic acid, methyl alcohol etc.These organic molecules are transported to the exoelectrical reaction that participates in fuel cell E among the fuel cell E by transfer conduit, the electric energy that produces can be directly used in illumination, perhaps flow to extractor fan G and drive the blower fan running, perhaps part is used for illumination, and part flows to extractor fan G and drives the blower fan running.Simultaneously, the CO that in fuel cell E, produces
2By fuel cell CO
2After purifying plant H purifies, arrive CO through transfer conduit quilt transporting again
2Among the electrochemical solidification device D, and participate in CO there
2The electrochemical solidification process.CO
2Electrochemical solidification power supply device F is the integrated electric energy generation/stocking system of solar cell and lithium ion battery, is used to CO
2The electrochemical solidification device D provide energy source and power.This novel energy-storing device based on carbon dioxide that present embodiment provides is constantly purified and is reclaimed CO
2, the organic molecule amount that fuel cell E consumes is less than CO
2In the time of the quantum of output of electrochemical solidification device D, can be with unnecessary output from CO
2Separate among the electrochemical solidification device D and be used for other purpose.Present embodiment collection CO
2Purification recovery, electrochemical solidification, generate electricity in one, the long-distance transport process in the middle of having avoided has the characteristics of easy actual effect; And the electric energy that this device produces can directly apply to himself, and electrochemical solidification process energy for example is provided, or CO
2Purification power.
Embodiment 2: with reference to shown in Figure 1, the structure of present embodiment is with embodiment 1, and its difference is: CO described in the present embodiment
2Purification absorption plant B and CO
2The purification medium of selecting for use in the closed circuit between the purification releasing device C is to CO
2The solid absorbent that characteristic absorption is arranged.Described CO
2The negative electrode that electrolysis is adopted among the electrochemical solidification device D is the alloy of metal Cu, Sn, Ag, and anode adopts the alloy of metal A g, Ni, and electrolyte is LiNO
3And Na
2SO
4Mixed solution, solvent is the mixed solvent of water and methyl alcohol, the electrolyte concentration scope is 0.05M, Faradaic current is 20mA/cm
2, electrolysis temperature is-20 ℃.Described CO
2Electrochemical solidification power supply device F adopts the association of wind-driven generator and lead-acid battery.Extractor fan G is a blower fan.The operation principle of present embodiment is referring to embodiment 1.
Embodiment 3: with reference to shown in Figure 1, the structure of present embodiment is with embodiment 1, and its difference is: CO described in the present embodiment
2Purification absorption plant B and CO
2The purification medium of selecting for use in the closed circuit between the purification releasing device C is an ammoniacal liquor.Described CO
2The negative electrode that electrolysis is adopted among the electrochemical solidification device D is the alloy of metal A g, Ti, Pb, and anode adopts the alloy of metal Pt, Ag, and electrolyte is K
2SO
4, K
2CO
3And KNO
3Mixed solution, solvent is the mixed solvent of water, methyl alcohol and propyl alcohol, the electrolyte concentration scope is 1M, Faradaic current is 150mA/cm
2, electrolysis temperature is 60 ℃.Described CO
2Electrochemical solidification power supply device F adopts the association of wind-driven generator and lead-acid battery.Extractor fan G is a blower fan.The operation principle of present embodiment is referring to embodiment 1.
Certainly more than only is a kind of concrete exemplary applications of the utility model device, and the protection domain of the utility model device is not constituted any limitation.In addition to the implementation, the utility model device can also have other embodiment.All employings are equal to the technical scheme of replacement or equivalent transformation formation, all drop within the utility model device scope required for protection.
Claims (7)
1. the novel energy-storing device based on carbon dioxide is characterized in that it comprises industrial gas emission passage (A), CO
2Purification absorption plant (B), CO
2Purification releasing device (C), CO
2Electrochemical solidification device (D), fuel cell (E) and CO
2Electrochemical solidification power supply device (F), described CO
2Purification absorption plant (B) is arranged in the industrial gas emission passage (A), and with described CO
2Purification releasing device (C) links to each other by closed circuit, described CO
2Purification releasing device (C), CO
2Electrochemical solidification device (D) and fuel cell (E) are linked in sequence by the gas delivery tube road, and described CO
2Electrochemical solidification power supply device (F) and CO
2Electrochemical solidification device (D) is electrically connected.
2. the novel energy-storing device based on carbon dioxide according to claim 1, it is characterized in that also comprising the extractor fan (G) that is arranged in the industrial gas emission passage (A), and described extractor fan (G) is electrically connected with described fuel cell (E) electric energy output end.
3. the novel energy-storing device based on carbon dioxide according to claim 1 is characterized in that also comprising fuel cell CO
2Purifying plant (H) is used for the CO that recovery and purification fuel cell (E) exoelectrical reaction process are produced
2, and described fuel cell CO
2Purifying plant (H) inserts CO by transfer conduit
2Electrochemical solidification device (D).
4. according to claim 1 or 2 or 3 described novel energy-storing devices, it is characterized in that described CO based on carbon dioxide
2Purification absorption plant (B) and CO
2The purification medium that circulates in the closed circuit of purification releasing device (C) is an ammoniacal liquor.
5. according to claim 1 or 2 or 3 described novel energy-storing devices, it is characterized in that described CO based on carbon dioxide
2Purification absorption plant (B) and CO
2The purification medium that circulates in the closed circuit of purification releasing device (C) is to CO
2The solid absorbent that absorption characteristic is arranged.
6. according to claim 1 or 2 or 3 described novel energy-storing devices, it is characterized in that described CO based on carbon dioxide
2Electrochemical solidification power supply device (F) is the association of solar cell or solar cell and energy-storage battery, and described energy-storage battery is lithium ion battery or lead-acid battery.
7. according to claim 1 or 2 or 3 described novel energy-storing devices, it is characterized in that described CO based on carbon dioxide
2Electrochemical solidification power supply device (F) is the association of wind-driven generator or wind-driven generator and energy-storage battery, and described energy-storage battery is lithium ion battery or lead-acid battery.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201020144405XU CN201799208U (en) | 2010-03-24 | 2010-03-24 | Novel energy storing device based on carbon dioxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201020144405XU CN201799208U (en) | 2010-03-24 | 2010-03-24 | Novel energy storing device based on carbon dioxide |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201799208U true CN201799208U (en) | 2011-04-20 |
Family
ID=43868725
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201020144405XU Expired - Fee Related CN201799208U (en) | 2010-03-24 | 2010-03-24 | Novel energy storing device based on carbon dioxide |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN201799208U (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103097290A (en) * | 2011-04-21 | 2013-05-08 | 松下电器产业株式会社 | Device for adsorbing and emitting carbon dioxide |
CN107002259A (en) * | 2014-12-05 | 2017-08-01 | 西门子公司 | Power plant |
CN115011982A (en) * | 2021-03-05 | 2022-09-06 | 本田技研工业株式会社 | Apparatus for producing carbon compound and method for producing carbon compound |
CN115125545A (en) * | 2021-03-11 | 2022-09-30 | 本田技研工业株式会社 | Carbon dioxide treatment device and method for producing carbon compound |
-
2010
- 2010-03-24 CN CN201020144405XU patent/CN201799208U/en not_active Expired - Fee Related
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103097290A (en) * | 2011-04-21 | 2013-05-08 | 松下电器产业株式会社 | Device for adsorbing and emitting carbon dioxide |
CN103097290B (en) * | 2011-04-21 | 2015-07-15 | 松下电器产业株式会社 | Device for adsorbing and emitting carbon dioxide |
US9205369B2 (en) | 2011-04-21 | 2015-12-08 | Panasonic Intellectual Property Management Co., Ltd. | Adsorption and release device of carbon dioxide |
CN107002259A (en) * | 2014-12-05 | 2017-08-01 | 西门子公司 | Power plant |
US10385732B2 (en) | 2014-12-05 | 2019-08-20 | Siemens Aktiengesellschaft | Power plant |
CN107002259B (en) * | 2014-12-05 | 2019-10-29 | 西门子公司 | Power plant |
CN115011982A (en) * | 2021-03-05 | 2022-09-06 | 本田技研工业株式会社 | Apparatus for producing carbon compound and method for producing carbon compound |
CN115125545A (en) * | 2021-03-11 | 2022-09-30 | 本田技研工业株式会社 | Carbon dioxide treatment device and method for producing carbon compound |
US11840768B2 (en) | 2021-03-11 | 2023-12-12 | Honda Motor Co., Ltd. | Carbon dioxide treatment device and method of producing carbon compound |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104481617B (en) | Based on the energy storage device of redox reaction and energy storage method thereof and electricity-generating method | |
CN102797970A (en) | Energy storage and energy supply integrated system based on hydrogen energy | |
CN210916273U (en) | System for producing hydrogen through electrolytic cell by power of thermal power plant | |
CN201799208U (en) | Novel energy storing device based on carbon dioxide | |
CN201549546U (en) | Columnar flow battery device | |
CN101651219B (en) | Vanadium-chromium double flow battery | |
CN103123976B (en) | Based on Fe (II) the EDTA renovation process of microbiological fuel cell | |
CN105617842A (en) | Device for separation and purification of carbon dioxide | |
CN103422112A (en) | Method and system for preparing hydrogen and carrying out combined water supply and power supply | |
CN106532096A (en) | Low-cost flow battery negative electrode electrolyte and preparation method therefor | |
CN113037180A (en) | Novel mobile power supply system | |
Nadeem et al. | Review of smart and innovative energy storage systems | |
CN113278987B (en) | SOEC and AEL electrolysis coupling solid circulation hydrogen storage and release system | |
CN214914809U (en) | Carbon dioxide capture system utilizing waste gas temperature difference for power generation | |
CN101841051A (en) | New CO2-based energy storage method and device | |
CN107565151B (en) | Regeneration method of electrode activity of all-vanadium redox flow battery | |
CN201528013U (en) | Vanadium-chromium dual-liquid flow battery | |
CN104466208A (en) | Diesel type solid oxide fuel cell charging station | |
CN204349498U (en) | A kind of liquefied petroleum gas type Solid Oxide Fuel Cell charging station | |
CN209923401U (en) | Hydrogenation reduction furnace for reducing lithium ion battery anode material | |
CN203360587U (en) | System for preparing hydrogen and carrying out combined-type water supply and power supply | |
KR20110101891A (en) | Power plant integrating metal-air battery and solar/wind power generator | |
CN1216432C (en) | Method for producing electrode of sodium polysulfide/bromine novel energy storage cell | |
CN204348818U (en) | A kind of diesel-type Solid Oxide Fuel Cell charging station | |
CN204481084U (en) | A kind of gasoline-type Solid Oxide Fuel Cell charging station |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110420 Termination date: 20140324 |