CN109954476A - A kind of bivalve layer calcium carbonate hollow microsphere CO of additive Mn2The preparation method of adsorbent - Google Patents

A kind of bivalve layer calcium carbonate hollow microsphere CO of additive Mn2The preparation method of adsorbent Download PDF

Info

Publication number
CN109954476A
CN109954476A CN201910240378.1A CN201910240378A CN109954476A CN 109954476 A CN109954476 A CN 109954476A CN 201910240378 A CN201910240378 A CN 201910240378A CN 109954476 A CN109954476 A CN 109954476A
Authority
CN
China
Prior art keywords
adsorbent
additive
calcium carbonate
water
calcium
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.)
Granted
Application number
CN201910240378.1A
Other languages
Chinese (zh)
Other versions
CN109954476B (en
Inventor
王胜平
李姗
江涛
徐志鸿
马新宾
赵玉军
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tianjin University
Original Assignee
Tianjin University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Tianjin University filed Critical Tianjin University
Priority to CN201910240378.1A priority Critical patent/CN109954476B/en
Publication of CN109954476A publication Critical patent/CN109954476A/en
Application granted granted Critical
Publication of CN109954476B publication Critical patent/CN109954476B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0222Compounds of Mn, Re
    • 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
    • B01J20/04Solid 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
    • B01J20/043Carbonates or bicarbonates, e.g. limestone, dolomite, aragonite
    • 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
    • B01J20/28014Solid 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 form
    • B01J20/28016Particle form
    • B01J20/28021Hollow particles, e.g. hollow spheres, microspheres or cenospheres
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Abstract

The present invention is a kind of bivalve layer calcium carbonate hollow microsphere CO of additive Mn2The preparation method of adsorbent.This method comprises the following steps: first with sucrose solution hydro-thermal reaction and etc. carbon ball is prepared, then using carbon ball as sacrifice template, it adds it in calcium salt and the mixed solution of manganese salt, then by water-bath, drying, roasting, the bivalve layer calcium carbonate hollow microsphere CO of additive Mn is obtained2Adsorbent.The present invention can accurately realize the regulation of the shell thickness, microballoon size, calcium manganese ratio to the hollow calcium carbonate microspheres of bivalve layer of additive Mn by modulation calcium manganese ratio, carbon ball template, solvent composition.Preparation-obtained adsorbent presents higher adsorption capacity and good stability in adsorption desorption circulation, wherein the initial adsorption capacity upto of the adsorbent of best performance to 0.62g CO2/ g adsorbent remains to maintain 0.53g CO after 25 circulations2/g adsorbent。

Description

A kind of bivalve layer calcium carbonate hollow microsphere CO of additive Mn2The preparation method of adsorbent
Technical field
The present invention relates to a kind of calcium oxide-based CO of the special appearance of inert component doping2The preparation method of adsorbent belongs to In CO2High temperature trapping and field of material preparation.
Background technique
In recent years, as usage amount of the mankind to fossil fuel increasingly increases, burning produces a large amount of CO2。CO2Make For one of main greenhouse gases, environmental problem brought by the greenhouse effects of generation is more serious.Currently by mankind's activity The CO of generation2Most of flue gas in coal-burning power plant, and Ca-base adsorbent can be straight due to its higher operation temperature It connects to the CO in flue gas2It is trapped, without carrying out cooling processing to flue gas, the energy can be saved, add its adsorption capacity Greatly, raw material sources are extensive, many merits such as low in cost, become current most application prospect collecting carbonic anhydride technology it One.
But the current main application difficult point of Ca-base adsorbent is easy sintering deactivation in use, be on the one hand because For CaCO3Tamman's temperature it is low, be on the other hand because of CaO and CaCO3Molal volume difference it is larger, adsorption desorption circulation in The mechanical stress generated by volume change generates constant impingement to the structure of adsorbent, and then the collapsing for aggravating sorbent structure is burnt Knot causes inactivation.For these problems, current technical method is that dystectic inertia group is doped in Ca-base adsorbent Point, and doping method is mainly more traditional technical method, for example sol-gal process, wet mixing are legal, infusion process etc., these Method can not achieve through the structure design to adsorbent the sintering for avoiding Ca-base adsorbent, thus can be from Ca-base adsorbent Structure design on cope with the Sintering Problem of Ca-base adsorbent.
Summary of the invention
It is an object of the present invention to be easy sintering current Ca-base adsorbent aiming at the problem that rapid deactivation, a kind of manganese is provided and is mixed Miscellaneous bivalve layer calcium carbonate hollow microsphere CO2The preparation method of adsorbent.This method is using more shell hollow microsphere structures On the basis of, uniqueness introduces manganese inert component, and its role is to by reducing calcium carbonate crystallite dimension, increase shell intensity and mentioning High adsorbent improves the adsorption capacity and stability of adsorbent at sphericity, the effective physical barrier of formation etc..
Technical scheme is as follows:
A kind of bivalve layer calcium carbonate hollow microsphere CO of additive Mn2The preparation method of adsorbent, includes the following steps:
1) sucrose solution is put in crystallizing kettle, hydrothermal crystallizing reaction 1.5~3 hours is carried out at 160~230 DEG C, so Products obtained therefrom is filtered afterwards, alternately washing is carried out with second alcohol and water to gained filter cake, then dry 8~16h at 60~120 DEG C, The carbon ball that diameter is 1~4 μm is obtained after grinding;
Wherein, the concentration of sucrose solution is 0.5M~2M;
2) metal salt is added in solvent, metal salt solution is obtained after stirring and dissolving, then add institute in step 1) Carbon ball processed, obtains suspension;After suspension ultrasonic disperse 5~30 minutes, then in 25~60 DEG C of water-bath 5~15h of magnetic agitation, Gained filter cake is after being filtered, washed, dry 8 at 60~120 DEG C~for 24 hours;
Wherein, metal salt is calcium nitrate or calcium nitrate and manganese acetate, molar ratio calcium nitrate: manganese acetate=1:0~ 0.01;Solvent is the mixed solution of water or second alcohol and water, volume ratio water: ethyl alcohol=1:0~5;In metal salt solution, nitre Sour calcium concentration is 1-4M;300~1200mg carbon ball is added in every 30 milliliters of metal salt solutions;
3) it is placed in Muffle furnace after being ground 2) middle gained dry products, in air atmosphere, with the first heating speed Rate is warming up to 380~420 DEG C, then with the second heating rate temperature to 490~510 DEG C, keeps 1~3h of temperature calcination, obtains manganese The bivalve layer calcium carbonate hollow microsphere CO of doping2Adsorbent;
The first heating rate in the step 3) is 1~10 DEG C/min, and the second heating rate is the first heating speed The 25%~75% of rate.
In the step 2), when solvent is the mixed solution of second alcohol and water, volume ratio is preferably water: ethyl alcohol=1: 1~5.
In the step 2), when metal salt is calcium nitrate and manganese acetate, molar ratio is preferably calcium nitrate: manganese acetate= 1:0.01~0.5.
The invention has the benefit that
1. the present invention is successfully prepared a kind of Ca-base adsorbent of novel additive Mn with double layer hollow micro-sphere structure, Fig. 4 is the scanning electron microscope image of the bivalve layer calcium carbonate tiny balloon of typical additive Mn, is produced as we can see from the figure It is product uniform particle diameter, good at sphericity.Fig. 1 is the transmission electron microscope image of four kinds of different calcium manganese ratio adsorbents, can from figure To see that the product of four kinds of different calcium manganese ratios has been respectively formed clearly double layer hollow micro-sphere structure.
2. compared with the absorption property of Most current Ca-base adsorbent reported in the literature, additive Mn prepared by the present invention Double layer hollow calcium carbonate microspheres adsorbent present higher adsorption capacity and stability, and wherein the incorporation of manganese significantly mentions The high absorption property of adsorbent, wherein when Microsphere Size is 500nm, calcium manganese molar ratio is 12-1, the initial suction of adsorbent Attached capacity is up to 0.62g-CO2/ g-adsorbent is higher by 30% than the adsorbent absorption property without additive Mn, at 25 0.53g-CO is still able to maintain after circulation2/ g-adsorbent is higher by 130% than the adsorbent absorption property without additive Mn, Present more excellent absorption property stability.
3. synthesis technology of the invention is not related to the use of any organic solvent, initiator and surfactant, have green The advantages that color is nontoxic, simple to operation, products therefrom uniform particle diameter.
4. the present invention can accurately realize the bivalve to additive Mn by modulation solvent composition, carbon ball size, calcium manganese ratio The regulation of the shell thickness, microballoon size, calcium manganese ratio of the hollow calcium carbonate microspheres of layer.
Detailed description of the invention
Fig. 1 is the transmission electron microscope image of the double layer hollow calcium carbonate microspheres adsorbent of four kinds of different calcium manganese molar ratios (TEM), wherein Fig. 1 a, Fig. 1 b, Fig. 1 c and Fig. 1 d be respectively pure calcium carbonate, practical calcium manganese molar ratio be 30/1,12/1 and 7/1 Double layer hollow calcium carbonate microspheres transmission electron microscope image (TEM);
Fig. 2 is the sorption cycle test result of four kinds of different adsorbents of calcium manganese molar ratio;
Fig. 3 is the double layer hollow calcium carbonate microspheres transmission electron microscope figure of the additive Mn of shell layer prepared by embodiment 2 Picture;
Fig. 4 is the double layer hollow calcium carbonate microspheres scanning electron microscope image for the additive Mn that embodiment 3 prepares 500nm (SEM);
Fig. 5 is the double layer hollow calcium carbonate microspheres transmission electron microscope image for the additive Mn that embodiment 3 prepares 500nm;
Fig. 6 is the sorption cycle test of the double layer hollow calcium carbonate microspheres adsorbent of 3 kinds of different size of additive Mns;
Specific embodiment
Technical solution of the present invention is further explained and described below by way of specific embodiment combination attached drawing.
Embodiment 1
(1) preparation of carbon ball template: the aqueous solution for the sucrose that concentration is 1M is fitted into crystallizing kettle, in 200 DEG C of progress water Products obtained therefrom is filtered after the completion, is carried out to gained filter cake with second alcohol and water by thermal crystallisation reaction, time 120min, crystallization It alternately washs, by products obtained therefrom, dry 12h, then grinding, gained carbon ball diameter are 2 μm at 80 DEG C.
(2) 20ml dehydrated alcohol and 10ml deionized water are taken, mixed solvent is obtained, by the Ca (NO of 14.169g3)2·4H2O and Mn (the CH of 0.588g3COO)2·4H2(i.e. the concentration of calcium ion is 2mol/L to O, and the calcium manganese ion molar ratio that feeds intake is 25/1, finally Obtaining actually measured calcium manganese ion molar ratio in adsorbent is 12/1) to be added in above-mentioned solvent to obtain metal salt solution A, in 1) Made carbon ball template 600mg is added in this metal salt solution A, obtains suspension B, after carrying out ultrasonic disperse 30 minutes to B, will be hanged Filter cake is dried 12h by water-bath magnetic agitation 8 hours at 40 DEG C turbid B, rear to filter, washing at 80 DEG C.
(3) gained dry products in (2) are ground, is roasted after grinding, roasting condition is air atmosphere, in horse 400 DEG C first not are warming up to 2 degree every point in furnace, switches heating rate immediately after, 500 DEG C is warming up to 1 degree every point, finally exists 500 DEG C of roastings obtain final products in 2 hours.The practical calcium manganese ratio that products obtained therefrom is measured by ICP is 12:1, therefore is named as Ca12Mn1。
Embodiment 2
(1) preparation of carbon ball template: the aqueous solution for the sucrose that concentration is 1M is fitted into crystallizing kettle, in 200 DEG C of progress water Thermal crystallisation reacts 110min, filters products obtained therefrom after the completion of crystallization, is repeatedly handed over second alcohol and water gained filter cake For washing, then the dry 12h at 80 DEG C, grinding, gained carbon ball diameter are 1 μm.
(2) 20ml dehydrated alcohol and 10ml deionized water are taken, mixed solvent is obtained, by the Ca (NO of 14.169g3)2·4H2O and Mn (the CH of 0.588g3COO)2·4H2(i.e. the concentration of calcium ion is 2mol/L to O, and the calcium manganese ion molar ratio that feeds intake is 25/1, finally Obtaining actually measured calcium manganese ion molar ratio in adsorbent is 12/1) to be added in above-mentioned solvent to obtain metal salt solution A, in 1) Made carbon ball template 600mg is added in this metal salt solution A, obtains suspension B, after carrying out ultrasonic disperse 30 minutes to B, will be hanged Filter cake is dried 12h by water-bath magnetic agitation 8 hours at 40 DEG C turbid B, rear to filter, washing at 80 DEG C.
3) 2) middle gained dry products are ground, is roasted after grinding, roasting condition is air atmosphere, in Muffle 400 DEG C first are warming up to 2 degree every point in furnace, then switches heating rate, then be warming up to 500 DEG C with 1 degree every point, finally 500 DEG C roasting obtains final products in 2 hours.The practical calcium manganese molar ratio measured according to ICP, products obtained therefrom are named as Ca12Mn1- 500。
Embodiment 3
(1) preparation of carbon ball template: the aqueous solution for the sucrose that concentration is 1M is fitted into crystallizing kettle, in 200 DEG C of progress water Thermal crystallisation reacts 120min, filters products obtained therefrom after the completion of crystallization, is repeatedly handed over second alcohol and water gained filter cake For washing, then the dry 12h at 80 DEG C, grinding, gained carbon ball diameter are 2 μm.
(2) 30ml deionized water is taken, mixed solvent is obtained, by the Ca (NO of 14.169g3)2·4H2The Mn of O and 0.588g (CH3COO)2·4H2(i.e. the concentration of calcium ion is 2mol/L to O, and the calcium manganese ion molar ratio that feeds intake is 25/1, finally obtains adsorbent In actually measured calcium manganese ion molar ratio be 12/1) to be added in above-mentioned solvent and obtain metal salt solution A, by made carbon ball mould in 1) Plate 600mg is added in this metal salt solution A, obtains suspension B, after carrying out ultrasonic disperse 30 minutes to B, by suspension B 40 Filter cake is dried 12h by water-bath magnetic agitation 8 hours at DEG C, rear to filter, washing at 80 DEG C.
3) 2) middle gained dry products are ground, is roasted after grinding, roasting condition is air atmosphere, in Muffle 400 DEG C first are warming up to 2 degree every point in furnace, then switches heating rate, 500 DEG C are warming up to 1 degree every point, finally at 500 DEG C Roasting obtains final products in 2 hours.The practical calcium manganese molar ratio measured according to ICP, products obtained therefrom are the relatively thin Ca12Mn1 of shell Adsorbent.
Embodiment 4
For other steps with embodiment 1, difference is Mn (CH3COO)2·4H2The additive amount of O is 0.196g, that is, feed intake calcium Manganese molar ratio is 75:1, and measuring practical calcium manganese molar ratio by ICP is 30:1, is named as Ca30Mn1.
Embodiment 5
For other steps with embodiment 1, difference is Mn (CH3COO)2·4H2The additive amount of O is 1.471g, that is, feed intake calcium Manganese molar ratio is 10:1, and measuring practical calcium manganese molar ratio by ICP is 7:1, is named as Ca7Mn1.
The calcium manganese ratio of involved adsorbent is the practical calcium manganese molar ratio measured by ICP in attached drawing.
From Fig. 1 it will be seen that the product of four kinds of different calcium manganese ratios has been respectively formed clearly double layer hollow micro-sphere structure.
Fig. 2 is the CO of the double layer hollow microsphere adsorbing agent of four kinds of different calcium manganese molar ratios2Absorption property evaluation result.Evaluation Process is that (STA449F3) is carried out on thermogravimetric analyzer.When evaluation, the product of about 5mg is placed on crucible, in N2Gas Under atmosphere, after being warming up to 600 DEG C with the heating rate of 10 DEG C/min, switching atmosphere to 50vol%CO2/ 50vol%N2, inhaled It is attached, adsorption time 45min.After the completion of absorption, 700 DEG C are warming up to the heating rate of 10 DEG C/min in a nitrogen atmosphere, in nitrogen 20min is desorbed under gas atmosphere.After the completion of desorption, 600 DEG C of progress are cooled to the rate of temperature fall of 10 DEG C/min in a nitrogen atmosphere Absorption.It loops back and forth like this and completes multiple adsorption desorption performance cycle test.It can be observed from fig. 2 that three kinds of adsorbents of doping manganese Got well than not carrying out the absorption property of adsorbent of additive Mn.The adsorbent initial adsorption capacity of manganese of wherein undoping is 0.45g-CO2/ g-ads, 25 circulation after drop to 0.23g-CO2/ g-ads, stability are poor.And for calcium manganese ratio be 30-1 when, Initial adsorption capacity boost is to 0.67g-CO2/ g-ads, however absorption property still less stable.When calcium manganese ratio be reduced to 12-1 and When 10-1, the initial adsorption capacity of adsorbent respectively reaches 0.56g-CO2/ g-ads and 0.47g-CO2/ g-ads, after 25 recycle Adsorption capacity slightly decreases, and shows excellent stability.Illustrate that the addition of manganese can not only improve the adsorption capacity of adsorbent, And the incorporation of enough manganese can significantly improve the absorption stability of adsorbent.
Fig. 3 corresponds to the TEM figure of the product in embodiment 3, it can be seen that after solvent is changed to pure water, can effectively adjust Shell thickness is saved, can get the hollow calcium carbonate microspheres of bivalve layer of the relatively thin additive Mn of shell.
Fig. 4 corresponds to the SEM figure of the product in embodiment 2, it can be seen that uses the sacrifice template using carbon ball as template The bivalve layer hollow microsphere adsorbent of the preparation-obtained additive Mn of method has the characteristics that uniform particle diameter, good at sphericity.
Fig. 5 corresponds to the TEM figure of the product in embodiment 2, which is 500nm, it can be seen that is passed through Using the carbon ball template with smaller diameter, the bivalve layer hollow microsphere absorption of the smaller additive Mn of diameter can be effectively obtained Agent is realized by using different size of carbon ball template and is adjusted to the size of the bivalve layer hollow microsphere of additive Mn.
Fig. 6 be calcium manganese ratio be 12-1, diameter be respectively 1500,1200,500nm three kinds of additive Mns bivalve layer it is hollow The CO of microsphere adsorbing agent2Absorption property evaluation result.Evaluation condition is identical as the condition in Fig. 1, it can be seen that microsphere diameter compared with Hour, that is, Ca12Mn1-500, adsorption capacity will be consistently higher than other the two kinds microballoons being relatively large in diameter and inhale in 25 circulations Attached dose.Its initial adsorption capacity is 0.62g-CO2/ g-ads, 25 circulation after adsorption capacity remain to maintain 0.53g-CO2/g- Ads presents more excellent CO2Absorption property.
Unaccomplished matter of the present invention is well-known technique.

Claims (3)

1. a kind of bivalve layer calcium carbonate hollow microsphere CO of additive Mn2The preparation method of adsorbent, it is characterized in that this method includes such as Lower step:
1) sucrose solution is put in crystallizing kettle, hydrothermal crystallizing is carried out at 160~230 DEG C and is reacted 1.5~3 hours, then will Products obtained therefrom filters, and carries out alternately washing with second alcohol and water to gained filter cake, then dry 8~16h at 60~120 DEG C, grinding The carbon ball that diameter is 1~4 μm is obtained afterwards;
Wherein, the concentration of sucrose solution is 0.5M~2M;
2) metal salt is added in solvent, metal salt solution is obtained after stirring and dissolving, then add made carbon in step 1) Ball obtains suspension;After suspension ultrasonic disperse 5~30 minutes, then in 25~60 DEG C of water-bath 5~15h of magnetic agitation, gained Filter cake is after being filtered, washed, dry 8 at 60~120 DEG C~for 24 hours;
Wherein, metal salt is calcium nitrate or calcium nitrate and manganese acetate, molar ratio calcium nitrate: manganese acetate=1:0~0.01; Solvent is the mixed solution of water or second alcohol and water, volume ratio water: ethyl alcohol=1:0~5;In metal salt solution, calcium nitrate is dense Degree is 1-4M;300~1200mg carbon ball is added in every 30 milliliters of metal salt solutions;
3) it is placed in Muffle furnace after being ground 2) middle gained dry products, in air atmosphere, with the first heating rate liter Then temperature is warming up to 490~510 DEG C to 380~420 DEG C with the second heating rate, keep 1~3h of temperature calcination, obtain manganese and mix Miscellaneous bivalve layer calcium carbonate hollow microsphere CO2Adsorbent;
The first heating rate in the step 3) is 1~10 DEG C/min, and the second heating rate is the first heating rate 25%~75%.
2. the bivalve layer calcium carbonate hollow microsphere CO of additive Mn as described in claim 12The preparation method of adsorbent, feature For in the step 2), when solvent is the mixed solution of second alcohol and water, volume ratio is preferably water: ethyl alcohol=1:1~5.
3. the bivalve layer calcium carbonate hollow microsphere CO of additive Mn as described in claim 12The preparation method of adsorbent, feature For in the step 2), when metal salt is calcium nitrate and manganese acetate, molar ratio is preferably calcium nitrate: manganese acetate=1:0.01 ~0.5.
CN201910240378.1A 2019-03-28 2019-03-28 Manganese-doped double-shell calcium carbonate hollow microsphere CO2Method for preparing adsorbent Active CN109954476B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910240378.1A CN109954476B (en) 2019-03-28 2019-03-28 Manganese-doped double-shell calcium carbonate hollow microsphere CO2Method for preparing adsorbent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910240378.1A CN109954476B (en) 2019-03-28 2019-03-28 Manganese-doped double-shell calcium carbonate hollow microsphere CO2Method for preparing adsorbent

Publications (2)

Publication Number Publication Date
CN109954476A true CN109954476A (en) 2019-07-02
CN109954476B CN109954476B (en) 2021-09-28

Family

ID=67025081

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910240378.1A Active CN109954476B (en) 2019-03-28 2019-03-28 Manganese-doped double-shell calcium carbonate hollow microsphere CO2Method for preparing adsorbent

Country Status (1)

Country Link
CN (1) CN109954476B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113912099A (en) * 2021-11-23 2022-01-11 新乡学院 Multilayer calcium carbonate hollow microsphere for drug loading and preparation method and application thereof

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103923650A (en) * 2013-01-11 2014-07-16 海洋王照明科技股份有限公司 Metal particle-doped hollow structure calcium stannate luminescence material and preparation method thereof
CN104961115A (en) * 2015-06-24 2015-10-07 浙江理工大学 Hollow hydroxyapatite microsphere and preparation method thereof

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103923650A (en) * 2013-01-11 2014-07-16 海洋王照明科技股份有限公司 Metal particle-doped hollow structure calcium stannate luminescence material and preparation method thereof
CN104961115A (en) * 2015-06-24 2015-10-07 浙江理工大学 Hollow hydroxyapatite microsphere and preparation method thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
冯嘉琪: ""多壳层碳酸钙空心微球吸附剂的制备及其 CO2吸附性能研究"", 《中国优秀硕士学位论文全文数据库 工程科技I辑》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113912099A (en) * 2021-11-23 2022-01-11 新乡学院 Multilayer calcium carbonate hollow microsphere for drug loading and preparation method and application thereof

Also Published As

Publication number Publication date
CN109954476B (en) 2021-09-28

Similar Documents

Publication Publication Date Title
CN111333124B (en) Spinel-type mesoporous high-entropy oxide nanosphere with hollow structure and preparation method and application thereof
CN111943227B (en) Preparation method of low-defect and low-water-content Prussian white analogue
CN111302781A (en) Preparation method of Fe-Ti-Ni-Co-Mn high-entropy oxide ceramic material
CN111268736A (en) Three-dimensional flower-ball-shaped β -manganese dioxide and preparation method and application thereof
CN105668647A (en) High-specific surface area perovskite nano-LaCoO3 porous hollow sphere material and preparation method thereof
CN109772465A (en) A kind of preparation method of water solubility carbon dots modified perovskite type catalysis material
CN108786786A (en) A kind of photocatalytic degradation nanometer MoO3The preparation method of powder
KR101189593B1 (en) Oxygen adsorbent having high sorption rate for oxygen and preparation method thereof
CN109954476A (en) A kind of bivalve layer calcium carbonate hollow microsphere CO of additive Mn2The preparation method of adsorbent
CN110180489B (en) Sulfur-doped lithium-rich manganese lithium adsorbent and preparation method and application thereof
CN113967482B (en) Method for preparing bimetallic hexahedral nanosheet Ti-Ni-MOF catalyst through mesoscale regulation and control and application
CN113145124B (en) 3D core-shell beta-bismuth oxide/cobalt aluminum hydrotalcite direct Z-type heterojunction catalyst and preparation method and application thereof
JP3753754B2 (en) Method for producing spinel type LiMn2O4
CN110508275B (en) Mesoporous material loaded manganese dioxide catalyst and preparation method thereof
CN112850764A (en) Method for preparing shape-controllable aluminum oxide hollow microspheres without template agent
CN110947396B (en) Spherical manganese oxide coated iron oxide core shell structural composite, preparation method and application
CN109529909A (en) The method of fly ash base denitrating catalyst and preparation method thereof and denitration
CN112076717A (en) Method for preparing lithium ion sieve through melt impregnation reaction
CN110371973A (en) A kind of poly- p-phenylenediamine/graphene-based nitrogen-doped porous carbon material preparation method
CN113041988B (en) Titanium lithium ion sieve and preparation method and application thereof
CN109482225A (en) The method of fly ash base denitrating catalyst and preparation method thereof and denitration
CN105152220B (en) The method that ball-milling method prepares spinel lithium manganate
CN113617327A (en) Synthesis method of nano single crystal manganese lithium adsorbent
CN109665557A (en) A kind of flower-shaped copper oxide and its preparation method and application
CN101829539B (en) Method for preparing NiAl composite oxide desulfurizing agent with flower-shaped appearance

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant