CN106268708A - A kind of high-efficiency and continuous carbon dioxide recycle material for trapping and preparation method - Google Patents
A kind of high-efficiency and continuous carbon dioxide recycle material for trapping and preparation method Download PDFInfo
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- CN106268708A CN106268708A CN201610669812.4A CN201610669812A CN106268708A CN 106268708 A CN106268708 A CN 106268708A CN 201610669812 A CN201610669812 A CN 201610669812A CN 106268708 A CN106268708 A CN 106268708A
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/04—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
- B01J20/043—Carbonates or bicarbonates, e.g. limestone, dolomite, aragonite
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
- B01J20/28004—Sorbent size or size distribution, e.g. particle size
- B01J20/28007—Sorbent size or size distribution, e.g. particle size with size in the range 1-100 nanometers, e.g. nanosized particles, nanofibers, nanotubes, nanowires or the like
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3214—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the method for obtaining this coating or impregnating
- B01J20/3225—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the method for obtaining this coating or impregnating involving a post-treatment of the coated or impregnated product
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
- B01J20/3234—Inorganic material layers
- B01J20/3236—Inorganic material layers containing metal, other than zeolites, e.g. oxides, hydroxides, sulphides or salts
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
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- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/16—Alumino-silicates
- B01J20/18—Synthetic zeolitic molecular sieves
- B01J20/183—Physical conditioning without chemical treatment, e.g. drying, granulating, coating, irradiation
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3202—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
- B01J20/3204—Inorganic carriers, supports or substrates
Abstract
A kind of high-efficiency and continuous collecting carbonic anhydride material and preparation method, the effective ingredient of this material for trapping is the sodium carbonate of nano-porous materials and load thereof, the various membranaceous or block structure that its outward appearance is the outward appearance of nano-porous materials selected or nano-porous materials is made;Its preparation method is: first choose the aperture nano-porous materials less than 500nm;Then it is processed 2~3 hours by the soaking in sodium carbonate solution of 1mol/L, carry out normal temperature drying process afterwards, just can obtain being loaded with the nano-porous materials of sodium carbonate;The circulation absorption that the present invention only just can make this material carry out carbon dioxide by changing humidity traps;Nano-porous materials has the pore structure of prosperity, when occurring in chemical reaction is limited in nano aperture, can show some and diametrically opposite characteristic under macroscopic conditions, and the present invention makes full use of this characteristic, it is achieved the circularly trapping of carbon dioxide;The preparation cost of raw material of the present invention is cheap, and meanwhile, circulation absorption process is carried out at normal temperatures, it is only necessary to change humidity, relies on solar energy to realize.
Description
Technical field
The present invention relates to a kind of collecting carbonic anhydride material, be specifically related to a kind of high-efficiency and continuous carbon dioxide recycle trapping material
Material and preparation method.
Background technology
Carbon dioxide is the predominant gas causing greenhouse effect, and too high gas concentration lwevel can cause the one of ecosystem
The calamitous great change of series, it will serious threat human survival.It is a kind of control two by the collecting carbonic anhydride in air storage
The effective ways of carbonoxide concentration.Alkaline solution such as sodium hydroxide solution be at present carbon dioxide is rapidly and efficiently trapped the most square
Material the most efficiently, becomes sodium carbonate liquor after sodium hydroxide solution absorbing carbon dioxide.But sodium carbonate is converted into hydrogen-oxygen
Changing sodium to need to introduce calcium hydroxide and through a series of high temperature, dry, calcining and other processes, therefore the recovery of sodium hydroxide is one
The process of highly energy-consuming, and this removal process is along with a large amount of discharges of carbon dioxide, therefore uses sodium hydroxide to carry out air
The circularly trapping of middle carbon dioxide is uneconomic, and efficiency is the lowest.
Nano-porous materials such as zeolite molecular sieve is also used as solid titanium dioxide due to the pore structure with prosperity
Carbon adsorbent.But adsorbed the zeolite needs of carbon dioxide in high temperature environments could desorption carbon dioxide, therefore use
Zeolite carries out the process that the circularly trapping of carbon dioxide is a highly energy-consuming, is unpractiaca.
Summary of the invention
In order to solve the problem that above-mentioned prior art exists, it is an object of the invention to provide a kind of high-efficiency and continuous titanium dioxide
Carbon cycle material for trapping and preparation method, this material is the nano-porous materials being loaded with sodium carbonate, in actual use, it is only necessary to
The humidity changing material local environment can realize absorption or the desorption of carbon dioxide, i.e. realizes dioxy by the change of humidity
Change trapping and the regeneration of adsorbent of carbon.Can circulate down on this procedural theory always, thus can realize the efficient of carbon dioxide
Circularly trapping continuously.Comparing traditional carbon dioxide absorber, it is low that this invention has preparation cost, and cyclic process power consumption is low, can
The advantages such as regeneration.
In order to achieve the above object, the present invention adopts the following technical scheme that
A kind of high-efficiency and continuous carbon dioxide recycle material for trapping, the effective ingredient of described material for trapping is nano-porous materials
And the sodium carbonate of load, it is various membranaceous that its outward appearance is the outward appearance of nano-porous materials selected or nano-porous materials is made
Or block structure.
The preparation method of high-efficiency and continuous carbon dioxide recycle material for trapping described above, comprises the steps:
(1) a kind of aperture nano-porous materials less than 500nm is selected;
(2) above-mentioned nano-porous materials is immersed in the sodium carbonate liquor that concentration is 1mol/L 2~3 hours;
(3) nano-porous materials that above-mentioned soaking in sodium carbonate solution is crossed is carried out normal temperature drying process, i.e. available final
Carbon dioxide recycle material for trapping.
Preferably, described nano-porous materials is zeolite molecular sieve, activated carbon or both combinations.
Compared to the prior art, the invention have the advantages that
(1) the flourishing pore structure of nano-porous materials and huge specific surface area, little trapping material are made full use of
Material can realize the absorbability of superpower carbon dioxide.
(2) material for trapping can realize circular regeneration by changing humidity, and meanwhile, circulation absorption process is entered at normal temperatures
OK, it is only necessary to change humidity, renovation process is simple and energy consumption is low to rely on solar energy to realize.
(3) material for trapping preparation method is simple, and the cost of material is low in preparation, is suitable for extensive preparation and application.
(4) material for trapping has high selectivity to carbon dioxide.
Accompanying drawing explanation
Fig. 1 is that the chemical reaction free energy occurred in the present invention is with moisture subnumber variation diagram.
Fig. 2 is to select 5A molecular sieve as the carbon dioxide recycle material for trapping outward appearance of nano-porous materials in the present invention
Figure.
Fig. 3 be in the present invention carbon dioxide recycle material for trapping microstructure schematic diagram.
Fig. 4 is the carbon dioxide recycle absorption figure that in the present invention, material for trapping carries out that experimental test obtains.
Detailed description of the invention
Principle and detailed description of the invention to the present invention elaborate below in conjunction with the accompanying drawings:
The chemical reaction that the present invention utilizes is:
Above-mentioned reaction is a reversible reaction, and its free energy of reaction under the constraint of nano-pore changes as shown in Figure 1.Work as water
When molecule is less, free energy of reaction is less than zero, and reaction forward is spontaneous to be carried out, and the hydroxyl of generation can be combined with carbon dioxide,
Absorbing carbon dioxide.When hydrone is more, free energy of reaction is more than zero, reacts the most spontaneous carrying out, and hydroxyl reduces, dioxy
Change carbon desorption.
Below with 5A zeolite molecular sieve as specific embodiment.Weigh the 5A zeolite molecular sieve of 5g, be soaked in the carbon of 1mol/L
In acid sodium solution 2 hours, carbonate is made to enter in molecular sieve pores.Filter out solution afterwards and molecular sieve after soaking is carried out
Normal temperature drying obtains being loaded with the zeolite molecular sieve of sodium carbonate.Soak, be dried after molecular sieve as shown in Figure 2.Through above-mentioned
Molecular sieve after method processes i.e. can be used as carbon dioxide recycle material for trapping.Its microstructure schematic diagram is as it is shown on figure 3, carbon
Acid group and hydrone are limited in nanoaperture.
Fig. 4 is that the carbon dioxide recycle material for trapping preparing said method carries out carbon dioxide desorption/adsorb survey again
Test result figure.In figure, square data points is gas concentration lwevel, and triangular data points is relative humidity.By absorbing carbon dioxide
Saturated material for trapping is placed in sealed environment, and the atmosphere in this environment is identical with air, simultaneously by humidity measurement instrument and dioxy
Change concentration of carbon detector to be also positioned in this environment.Raising the humidity in environment, hydrone enters in the hole of material for trapping, with
Moisture to increase, from aforementioned principles, back reaction is spontaneous to be carried out, and hydroxide ion reduces, and carbon dioxide desorption, in environment
Gas concentration lwevel raises, until the complete desorption of carbon dioxide, i.e. material for trapping realize regeneration.Now reduce humidity, moisture
Son departs from material for trapping, and positive reaction is spontaneous to be carried out, and hydroxide ion increases, and carbon dioxide is adsorbed, dense carbon dioxide in environment
Degree reduces, and still can realize collecting carbonic anhydride, and amount of collected does not reduce after material for trapping regeneration is described.
Above-mentioned is only with 5A zeolite molecular sieve as specific embodiment, it should be pointed out that common for the art
For technical staff, under the premise without departing from the principles of the invention, it is also possible to make some improvements and modifications, these improve and profit
Decorations also should be protection scope of the present invention.
Claims (3)
1. a high-efficiency and continuous carbon dioxide recycle material for trapping, it is characterised in that: the effective ingredient of described material for trapping is for receiving
Rice porous material and the sodium carbonate of load thereof, its outward appearance is the outward appearance of the nano-porous materials selected or nano-porous materials is made
Various membranaceous or block structure.
2. the preparation method of high-efficiency and continuous carbon dioxide recycle material for trapping described in claim 1, it is characterised in that: include as follows
Step:
(1) a kind of aperture nano-porous materials less than 500nm is selected;
(2) above-mentioned nano-porous materials is immersed in the sodium carbonate liquor that concentration is 1mol/L 2~3 hours;
(3) nano-porous materials that above-mentioned soaking in sodium carbonate solution is crossed is carried out normal temperature drying process, i.e. can get final two
Carbonoxide circularly trapping material.
Preparation method the most according to claim 2, it is characterised in that: described nano-porous materials is zeolite molecular sieve, work
Property charcoal or both combination.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113713789A (en) * | 2021-08-31 | 2021-11-30 | 西安交通大学 | Carbon dioxide adsorbs membrane deformable structure based on humidity drive |
CN114452768A (en) * | 2022-03-03 | 2022-05-10 | 霖和气候科技(北京)有限公司 | CO based on wet-process regenerated adsorption material2Direct air capture system and method |
CN114558414A (en) * | 2022-03-09 | 2022-05-31 | 霖和气候科技(北京)有限公司 | Method for decarbonizing concentrated carbon dioxide emission source based on wet-process regeneration carbon dioxide capture material |
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CN101588856A (en) * | 2006-11-15 | 2009-11-25 | 环球研究技术有限公司 | Removal of carbon dioxide from air |
CN101804322A (en) * | 2010-04-29 | 2010-08-18 | 东华大学 | High-strength dry type CO2 adsorbent for regeneration using river sediment as carrier and preparation method thereof |
CN103301805A (en) * | 2012-03-07 | 2013-09-18 | 苏州绿奇创环保科技有限公司 | Carbon dioxide adsorbent and preparation method thereof |
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2016
- 2016-08-15 CN CN201610669812.4A patent/CN106268708A/en active Pending
Patent Citations (3)
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CN101588856A (en) * | 2006-11-15 | 2009-11-25 | 环球研究技术有限公司 | Removal of carbon dioxide from air |
CN101804322A (en) * | 2010-04-29 | 2010-08-18 | 东华大学 | High-strength dry type CO2 adsorbent for regeneration using river sediment as carrier and preparation method thereof |
CN103301805A (en) * | 2012-03-07 | 2013-09-18 | 苏州绿奇创环保科技有限公司 | Carbon dioxide adsorbent and preparation method thereof |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113713789A (en) * | 2021-08-31 | 2021-11-30 | 西安交通大学 | Carbon dioxide adsorbs membrane deformable structure based on humidity drive |
CN113713789B (en) * | 2021-08-31 | 2023-06-02 | 西安交通大学 | Carbon dioxide adsorption film deformable structure based on humidity driving |
CN114452768A (en) * | 2022-03-03 | 2022-05-10 | 霖和气候科技(北京)有限公司 | CO based on wet-process regenerated adsorption material2Direct air capture system and method |
CN114558414A (en) * | 2022-03-09 | 2022-05-31 | 霖和气候科技(北京)有限公司 | Method for decarbonizing concentrated carbon dioxide emission source based on wet-process regeneration carbon dioxide capture material |
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