CN106552609A - Carbon dioxide absorber and its preparation method based on layer stephanoporate silicon dioxide block - Google Patents

Carbon dioxide absorber and its preparation method based on layer stephanoporate silicon dioxide block Download PDF

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CN106552609A
CN106552609A CN201611107188.5A CN201611107188A CN106552609A CN 106552609 A CN106552609 A CN 106552609A CN 201611107188 A CN201611107188 A CN 201611107188A CN 106552609 A CN106552609 A CN 106552609A
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block
silicon dioxide
layer stephanoporate
carbon dioxide
stephanoporate silicon
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郭兴忠
丁力
单加琪
杨辉
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Zhejiang University ZJU
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Zhejiang University ZJU
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/10Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/103Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054Solid 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/50Carbon oxides
    • B01D2257/504Carbon dioxide
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02CCAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00Capture or disposal of greenhouse gases
    • Y02C20/40Capture or disposal of greenhouse gases of CO2

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  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
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  • Inorganic Chemistry (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Silicon Compounds (AREA)

Abstract

The invention discloses a kind of preparation method of the carbon dioxide absorber based on layer stephanoporate silicon dioxide block, comprises the following steps:Triblock copolymer P123 is dissolved in hydrochloric acid solution, then sequentially adds 1,3,5 trimethylbenzenes, methyl silicate, expoxy propane;Gained colloidal sol Jing gels, drying, be warming up to 400~800 DEG C and be incubated 5 ± 0.5h, obtain layer stephanoporate silicon dioxide block;Layer stephanoporate silicon dioxide block is put into into organic amine methanol solution, so that organic amine uniform load is in layer stephanoporate block;Gains are placed in baking oven and are dried, and obtain the carbon dioxide absorber based on layer stephanoporate silicon dioxide block.The present invention further simultaneously discloses the carbon dioxide absorber based on layer stephanoporate silicon dioxide block being prepared using said method.

Description

Carbon dioxide absorber and its preparation method based on layer stephanoporate silicon dioxide block
Technical field
The present invention relates to field of material technology, and in particular to a kind of carbon dioxide based on layer stephanoporate silicon dioxide block Adsorbent and preparation method.
Background technology
In recent years, the increasingly increase of greenhouse gases exacerbates global warming, and brings arid, flood, sea level A series of Climatic issues such as rising, so as to have a strong impact on the living environment of the ecological balance and human future of the earth.Dioxy It is the predominant gas for causing greenhouse effect to change carbon, while being also a kind of potential carbon resource, therefore reduces greenhouse gases titanium dioxide The discharge of carbon, environmental protection become one of current whole world key problem to be solved.In the capture technique of carbon dioxide, catch Obtain the height that material directly affects capture cost.
Conventional carbon dioxide capture material mainly has lyosoption, seperation film and solid absorbent etc. at present.Using Most capture materials is amine solvent, and the advantage of this capture material is that adsorption capacity is high, selectivity is good, but amine solvent has Renewable high energy consumption, have the shortcomings that to equipment that corrosivity are strong and also in being only applicable to or low concentration carbon dioxide absorption.Cause This in recent years solid absorbent receive extensive concern.
Conventional solid absorbent mainly includes that activated carbon, molecular sieve, metal-oxide, salt and amino modified are more Porous materials etc..As disclosed in CN105797678A " compound middle temperature carbon dioxide absorber and preparation method thereof ", there is provided one The method that magnalium type hydrotalcite composite material carrys out absorbing carbon dioxide is planted, existing middle temperature carbon dioxide absorber absorption effect is solved The low problem of rate;" a kind of carbon dioxide absorber and preparation method based on ordered mesopore carbon " disclosed in CN105289530A, Carbon dioxide absorber is prepared by material modification of ordered mesopore carbon, preferable adsorption effect is obtained.
But existing adsorbent be used mostly be single aperture micropore or mesoporous material, and material shape mostly is powder End or thin film, relatively difficult using rear recycling, the stratum that the foramen magnum-mesoporous-micropore of rising in recent years is distributed simultaneously is more Porous materials not only improve mass transfer and are conducive to absorption again, but rarely have based on layer stephanoporate block materials absorbing carbon dioxide at present Relevant report, therefore, develop it is significant based on this Novel carbon dioxide adsorbent.
The content of the invention
The technical problem to be solved in the present invention is to provide a kind of carbon dioxide based on layer stephanoporate silicon dioxide block and inhales Attached dose and preparation method, the method synthesize layer stephanoporate silicon dioxide block by sol-gel process, and by infusion process to which Carry out organic amine to support.
In order to solve above-mentioned technical problem, the present invention provides a kind of carbon dioxide based on layer stephanoporate silicon dioxide block The preparation method of adsorbent, comprises the following steps:
1), weigh the hydrochloric acid solution that 5.0~9.8g triblock copolymer P123s are placed in 25~30ml (preferably 28.8ml) In, stir under condition of ice bath to triblock copolymer P123 and be completely dissolved (mixing time about 3~6 hours);
2), the 1,3,5-trimethyl-benzene of 2~6ml is added (be slowly added dropwise, time for adding is 30 ± 5 minutes) to step 1) In solution, 1~3 hour under condition of ice bath, is sufficiently stirred for;
3), 10~14ml (preferably 12ml) methyl silicate is added to step 2) in solution, under condition of ice bath fully Stirring 1~3 hour, obtains solution (clear solution);
4), 3.2~6.4ml expoxy propane is added (be slowly added dropwise, time for adding is 30 ± 5 minutes) to step 3) obtained by In solution, under condition of ice bath, 2~5min is sufficiently stirred for, obtains colloidal sol (vitreosol);
5), by step 4) obtained by colloidal sol be placed in 12~48 hours in 40 ± 5 DEG C of baking ovens, obtain gel (translucent gels);
6), by step 5) obtained by gel be placed in 60 ± 5 DEG C of baking ovens be dried 2~5 days (purpose is to make moisture evaporating completely), Obtain block (white block);
7), by step 6) obtained by block be warming up to 400~800 DEG C and be incubated 5 ± 0.5h, after being cooled to room temperature, obtain rank Layer porous silica silicon bulk;
8), organic amine is added in methanol (absolute methanol), is stirred to organic amine and is completely dissolved, obtain organic amine methanol molten Liquid;
9), by step 7) obtained by layer stephanoporate silicon dioxide block be put into step 8) obtained by organic amine methanol it is molten Liquid, stirs 2~4h (preferably 3h) in 40 ± 5 DEG C (water-bath);So that organic amine uniform load is in layer stephanoporate block;
Organic amine in organic amine methanol solution is 0.43~4 with the mass ratio of layer stephanoporate silicon dioxide block:1 (compared with Good is 0.67~1.5:1);
10), by step 9) gains be placed in 80 ± 10 DEG C of baking ovens be dried 1~2 day, obtain based on layer stephanoporate dioxy The carbon dioxide absorber (that is, the modified layer stephanoporate silicon dioxide block of organic amine) of SiClx block.
As the improvement of the preparation method of the carbon dioxide absorber based on layer stephanoporate silicon dioxide block of the present invention: The step 8) in organic amine be polyethyleneimine, TEPA, at least one in pentaethylene hexamine it is (that is, a kind of or several Kind).
Enter one as the preparation method of the carbon dioxide absorber based on layer stephanoporate silicon dioxide block of the present invention Step is improved:The step 1) in hydrochloric acid solution concentration be 0.001molL-1~0.1molL-1.Above-mentioned concentration is, for example, 0.001mol·L-1、0.01mol·L-1、0.1mol·L-1
Enter one as the preparation method of the carbon dioxide absorber based on layer stephanoporate silicon dioxide block of the present invention Step is improved:The step 7) in, by step 6) block be put into Muffle furnace in atmosphere with 2 DEG C of min-1Speed be warming up to 400~800 DEG C, and 5 ± 0.5h is incubated, furnace cooling, obtains layer stephanoporate silicon dioxide block afterwards.
The present invention further simultaneously discloses based on layer stephanoporate silicon dioxide block two be prepared using said method Oxidation carbon adsorbent.
The preparation method of the present invention is as shown in Figure 1.
In the present invention, triblock copolymer P123, full name are poly(ethylene oxide)-poly(propylene oxide)-poly(ethylene oxide) three Block copolymer, its molecular formula are PEO-PPO-PEO.
The carbon dioxide absorber based on layer stephanoporate silicon dioxide block being prepared using the inventive method is (i.e., The carbon dioxide absorber of organic amine is supported based on layer stephanoporate silicon dioxide block), structure be foramen magnum-mesoporous-micropore simultaneously The layer stephanoporate silicon dioxide of distribution, is shaped as blocks of solid, and which is good to carbon dioxide adsorption and circular regeneration performance, reclaims again Raw convenient, which can be used for the carbon dioxide adsorption higher than room temperature.That is, which is good to carbon dioxide adsorption and circular regeneration performance.
The present invention has following technical advantage:Compared with same type adsorbent, it is proposed that a kind of to be based on layer stephanoporate dioxy The preparation method of the carbon dioxide absorber of SiClx block, the development for adsorbent provide new approaches;Product has good Heat stability, can be used for the carbon dioxide adsorption higher than room temperature;The carbon dioxide adsorption and circular regeneration performance of new adsorbent Well, required experiment condition and experimental cost are low, preparation technology environmental protection.
Description of the drawings
Below in conjunction with the accompanying drawings the specific embodiment of the present invention is described in further detail.
Fig. 1 is a kind of preparation flow figure of the carbon dioxide absorber based on layer stephanoporate silicon dioxide block.
Fig. 2 is 5000 times of stereoscan photograph of layer stephanoporate silicon dioxide of the synthesis of embodiment 1.
Fig. 3 is 50000 times of stereoscan photograph of layer stephanoporate silicon dioxide of the synthesis of embodiment 1.
Fig. 4 is the adsorption capacity change of 8 adsorption/desorption cyclic processes of adsorbent prepared by embodiment 4.
Fig. 5 is thermogravimetric analysiss (TG) result figure;
In Fig. 5, a:Embodiment 2;b:Embodiment 3;c:Embodiment 4.
Fig. 6 is the CO of embodiment 2, comparative example 1-1, comparative example 1-22Adsorption curve comparison diagram;
In Fig. 6, a:Embodiment 2;b:Comparative example 1-1;c:Comparative example 1-2.
Fig. 7 is the CO of embodiment 2, comparative example 2-1, comparative example 2-22Adsorption curve comparison diagram;
In Fig. 7, a:Embodiment 2;b:Comparative example 2-1;c:Comparative example 2-2.
Specific embodiment
With reference to specific embodiment, the present invention is described further, but protection scope of the present invention is not limited in This.
Embodiment 1, a kind of preparation method of layer stephanoporate silicon dioxide block:
Weigh 7g P123 and be added to 0.01molL-1Hydrochloric acid solution 28.8ml in, under condition of ice bath, magnetic agitation 5 is little When so that P123 is completely dissolved;The 1,3,5-trimethyl-benzene of (time for adding is 30 minutes) 4ml, ice bath bar are slowly added dropwise afterwards 3 hours are sufficiently stirred under part;Add and under 12ml methyl silicates, condition of ice bath, be sufficiently stirred for 3 hours;Then it is slowly added dropwise again (time for adding is 30 minutes) 5.5ml expoxy propane, is sufficiently stirred for 5min under condition of ice bath, obtains colloidal sol (vitreosol);Will Colloidal sol is placed in 36 hours in 40 ± 5 DEG C of baking ovens, and resulting gel (translucent gels) is placed in 60 ± 5 DEG C of baking ovens and is dried 4 days Resulting block (white block) is put into Muffle furnace in atmosphere with 2 DEG C of min by (purpose is to make moisture evaporating completely)-1 Speed be warming up to 550 DEG C, and be incubated 5h, after cooling to room temperature with the furnace afterwards, obtain layer stephanoporate silicon dioxide block.
Embodiment 2, a kind of preparation method of the carbon dioxide absorber based on layer stephanoporate silicon dioxide block:
Weigh 5.72g PEI (polyethyleneimine) be dissolved in methanol 15ml in be configured to PEI solution, add 8.58g to implement Layer stephanoporate silicon dioxide block obtained by example 1, stirs 3h under 40 ± 5 DEG C of water bath conditions, be placed in afterwards in baking oven be dried (80 ± In 10 DEG C of baking ovens be dried 2 days), obtain the layer stephanoporate silicon dioxide block that PEI load capacity is 40%, i.e., as product based on The carbon dioxide absorber of layer stephanoporate silicon dioxide block.After testing, the product has good carbon dioxide adsorption and follows Ring performance.
Embodiment 3, a kind of preparation method of the carbon dioxide absorber based on layer stephanoporate silicon dioxide block:
Weigh 6.54g PEI be dissolved in methanol 15ml in be configured to PEI solution, add the rank obtained by 6.54g embodiments 1 Layer porous silica silicon bulk, stirs 3h under 40 ± 5 DEG C of water bath conditions, is placed in baking oven afterwards and is dried (in 80 ± 10 DEG C of baking ovens It is dried 2 days), the layer stephanoporate silicon dioxide block that PEI load capacity is 50% is obtained, i.e., as product based on layer stephanoporate two The carbon dioxide absorber of silicon oxide block.After testing, product has good carbon dioxide adsorption and cycle performance.
Embodiment 4, a kind of preparation method of the carbon dioxide absorber based on layer stephanoporate silicon dioxide block
Weigh 8.52g PEI be dissolved in methanol 15ml in be configured to PEI solution, add the stratum in 5.68g embodiments 1 Porous silica silicon bulk, stirs 3h under 40 ± 5 DEG C of water bath conditions, is placed in baking oven afterwards to be dried and (is done in 80 ± 10 DEG C of baking ovens Dry 2 days), the layer stephanoporate silicon dioxide block that PEI load capacity is 60% is obtained, i.e., as product based on layer stephanoporate dioxy The carbon dioxide absorber of SiClx block.After testing, product has good carbon dioxide adsorption and cycle performance.
Test one, thermogravimetric analysiss (TG) are carried out to the product obtained by 2~embodiment of embodiment 4, as a result as shown in Figure 5.
Product be can be seen that from TG curves a little mass loss near 100 DEG C, and this adsorbs in being mainly product Caused by water volatilization, to 200 DEG C of almost no mass losses after this, the big mass loss near 200 DEG C is mainly by PEI point Caused by solution, therefore, understand that product has good heat stability within 200 DEG C from curve.
Experiment two, carbon dioxide adsorption:
CO2Absorption property is measured by DTG (TG), is comprised the following steps that:
1st, preprocessing process:Take 10mg or so samples, all the time 50ml/min high pure nitrogen purging atmosphere in, with 5 DEG C/ The programming rate of min is increased to 110 DEG C from room temperature, then keeps constant temperature 60min, with deviate from adsorbent duct remaining water and Air plankton;
2nd, 75 DEG C of the adsorption temp specified is cooled to the speed of 5 DEG C/min, and constant temperature 30min makes it stable;
3rd, adsorption process:High pure nitrogen is converted into into high-purity CO2, with high-purity CO of 70ml/min2Air-flow is adsorbed, and is inhaled The attached time is 200min;
4th, desorption process:Switch to high-purity N2, flow is still 50ml/min, is warming up to 110 DEG C with the speed of 5 DEG C/min, Constant temperature 50min is desorbed;
5th, repeat experiment 8 times, test its cycle performance;
6th, the CO in sample2Adsorption capacity is calculated according to the measurement result of TG.
The adsorption capacity of 8 adsorption/desorption cyclic processes of adsorbent prepared by embodiment 4 changes as described in Figure 4.
Comparative example 1-1, the weight of the PEI in embodiment 2 is made into 1.43g by 5.72g, i.e. organic amine and layer stephanoporate The mass ratio of silicon dioxide block is 0.16:1;Remaining is equal to embodiment 2.
Comparative example 1-2, the weight of the PEI in embodiment 2 is made into 34.3g by 5.72g, i.e. organic amine and layer stephanoporate The mass ratio of silicon dioxide block is 5:1;Remaining is equal to embodiment 2.
The CO of above-described embodiment 2, comparative example 1-1, comparative example 1-22Adsorption curve is contrasted as shown in fig. 6, from the curve of Fig. 6 In can look, the absorption property of embodiment 2 is best.
Comparative example 2-1, by the concentration of hydrochloric acid in embodiment 1 by " 0.01molL-1" make " 0.001molL into-1", its Remaining same embodiment 1.With the layer stephanoporate silicon dioxide block obtained by this scheme as 2 methods described of embodiment carries out carbon dioxide The preparation of adsorbent.
Comparative example 2-2, by the 0.01molL in embodiment 1-1Hydrochloric acid make water into, remaining is with embodiment 1.With this scheme The layer stephanoporate silicon dioxide block of gained carries out the preparation of carbon dioxide absorber such as 2 methods described of embodiment.
The CO of above-described embodiment 2, comparative example 2-1, comparative example 2-22Adsorption curve is contrasted as shown in fig. 7, from the curve of Fig. 7 In can look, the absorption property of embodiment 2 is best.
Comparative example 3-1, make the PEI in embodiment 2 into TEPAs, weight is constant;Remaining is equal to embodiment 2.
Comparative example 3-2, make the PEI in embodiment 2 into pentaethylene hexamines, weight is constant;Remaining is equal to embodiment 2.
On the premise of adsorption time is 200min;The adsorbance of 2 products obtained therefrom of embodiment is 1.84mmol/g, is contrasted The adsorbance of example 3-1 products obtained therefroms is 1.65mmol/g, and the adsorbance of comparative example 3-1 products obtained therefrom is 1.60mmol/g.
Finally, in addition it is also necessary to it is noted that listed above is only several specific embodiments of the invention.Obviously, this It is bright to be not limited to above example, there can also be many deformations.One of ordinary skill in the art can be from present disclosure The all deformations directly derived or associate, are considered as protection scope of the present invention.

Claims (5)

1. based on layer stephanoporate silicon dioxide block carbon dioxide absorber preparation method, it is characterised in that:Including following Step:
1) 5.0~9.8g triblock copolymer P123s, are weighed to be placed in the hydrochloric acid solution of 25~30ml, is stirred under condition of ice bath It is completely dissolved to triblock copolymer P123;
2), the 1,3,5-trimethyl-benzene of 2~6ml is added to step 1) in solution, under condition of ice bath, it is sufficiently stirred for 1~3 hour;
3), 10~14ml methyl silicates are added to step 2) in solution, it is sufficiently stirred under condition of ice bath 1~3 hour, obtains Solution;
4), 3.2~6.4ml expoxy propane is added to step 3) in resulting solution, under condition of ice bath, 2~5min is sufficiently stirred for, Obtain colloidal sol;
5), by step 4) obtained by colloidal sol be placed in 12~48 hours in 40 ± 5 DEG C of baking ovens, obtain gel;
6), by step 5) obtained by gel be placed in 60 ± 5 DEG C of baking ovens be dried 2~5 days, obtain block;
7), by step 6) obtained by block be warming up to 400~800 DEG C and be incubated 5 ± 0.5h, after being cooled to room temperature, obtain stratum many Hole silicon dioxide block;
8), organic amine is added in methanol, is stirred to organic amine and is completely dissolved, obtain organic amine methanol solution;
9), by step 7) obtained by layer stephanoporate silicon dioxide block be put into step 8) obtained by organic amine methanol solution, in 40 ± 5 DEG C of 2~4h of stirring;So that organic amine uniform load is in layer stephanoporate block;
Organic amine in organic amine methanol solution is 0.43~4 with the mass ratio of layer stephanoporate silicon dioxide block:1;
10), by step 9) gains be placed in 80 ± 10 DEG C of baking ovens be dried 1~2 day, obtain based on layer stephanoporate silicon dioxide The carbon dioxide absorber of block.
2. the preparation method of the carbon dioxide absorber based on layer stephanoporate silicon dioxide block according to claim 1, It is characterized in that:The step 8) in organic amine be polyethyleneimine, TEPA, at least one in pentaethylene hexamine.
3. according to claim 2 based on layer stephanoporate silicon dioxide block carbon dioxide absorber preparation method, its It is characterised by:The step 1) in hydrochloric acid solution concentration be 0.001molL-1~0.1molL-1
4. according to Claims 2 or 3 based on layer stephanoporate silicon dioxide block carbon dioxide absorber preparation method, It is characterized in that:
The step 7) in, by step 6) block be put into Muffle furnace in atmosphere with 2 DEG C of min-1Speed be warming up to 400~ 800 DEG C, and 5 ± 0.5h is incubated, furnace cooling, obtains layer stephanoporate silicon dioxide block afterwards.
5. the dioxy based on layer stephanoporate silicon dioxide block being prepared using such as the arbitrary methods described of Claims 1 to 4 Change carbon adsorbent.
CN201611107188.5A 2016-12-06 2016-12-06 Carbon dioxide absorber and its preparation method based on layer stephanoporate silicon dioxide block Pending CN106552609A (en)

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CN110075812A (en) * 2019-05-17 2019-08-02 上海大学 A kind of preparation method and application of amination silica dioxide granule adsorbent
CN110075812B (en) * 2019-05-17 2022-02-25 上海大学 Preparation method and application of silicon dioxide particle adsorbent
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Application publication date: 20170405