CN104229806B - A kind of method for being catalyzed nucleation process synthesis magadiite - Google Patents
A kind of method for being catalyzed nucleation process synthesis magadiite Download PDFInfo
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- CN104229806B CN104229806B CN201410458274.5A CN201410458274A CN104229806B CN 104229806 B CN104229806 B CN 104229806B CN 201410458274 A CN201410458274 A CN 201410458274A CN 104229806 B CN104229806 B CN 104229806B
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- nucleator
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- 238000000034 method Methods 0.000 title claims abstract description 35
- 238000010899 nucleation Methods 0.000 title claims abstract description 24
- 230000006911 nucleation Effects 0.000 title claims abstract description 23
- 230000015572 biosynthetic process Effects 0.000 title claims abstract description 22
- 238000003786 synthesis reaction Methods 0.000 title claims abstract description 22
- 230000008569 process Effects 0.000 title claims abstract description 9
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 28
- 239000000203 mixture Substances 0.000 claims abstract description 19
- 239000003513 alkali Substances 0.000 claims abstract description 16
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 15
- 239000010703 silicon Substances 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 15
- 238000002425 crystallisation Methods 0.000 claims abstract description 9
- 230000008025 crystallization Effects 0.000 claims abstract description 9
- 239000000463 material Substances 0.000 claims abstract description 8
- 238000001035 drying Methods 0.000 claims abstract description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 24
- CDBYLPFSWZWCQE-UHFFFAOYSA-L sodium carbonate Substances [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 16
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 13
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 10
- 239000011324 bead Substances 0.000 claims description 9
- 238000006243 chemical reaction Methods 0.000 claims description 9
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 8
- 239000000919 ceramic Substances 0.000 claims description 7
- 229910000831 Steel Inorganic materials 0.000 claims description 4
- 239000000377 silicon dioxide Substances 0.000 claims description 4
- 239000010959 steel Substances 0.000 claims description 4
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims 2
- 239000004408 titanium dioxide Substances 0.000 claims 1
- 238000010189 synthetic method Methods 0.000 abstract description 3
- 239000003054 catalyst Substances 0.000 abstract description 2
- 239000002131 composite material Substances 0.000 abstract description 2
- 239000000945 filler Substances 0.000 abstract description 2
- 239000002114 nanocomposite Substances 0.000 abstract description 2
- 239000003463 adsorbent Substances 0.000 abstract 1
- 238000002360 preparation method Methods 0.000 abstract 1
- 239000000047 product Substances 0.000 description 16
- 238000002441 X-ray diffraction Methods 0.000 description 7
- 239000000243 solution Substances 0.000 description 7
- 238000003756 stirring Methods 0.000 description 7
- 239000012071 phase Substances 0.000 description 5
- 239000011259 mixed solution Substances 0.000 description 4
- 238000004451 qualitative analysis Methods 0.000 description 4
- 238000001228 spectrum Methods 0.000 description 4
- 239000013067 intermediate product Substances 0.000 description 3
- 230000004913 activation Effects 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000011229 interlayer Substances 0.000 description 2
- 239000002667 nucleating agent Substances 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 229910002012 Aerosil® Inorganic materials 0.000 description 1
- 206010013786 Dry skin Diseases 0.000 description 1
- 241000220317 Rosa Species 0.000 description 1
- FKNQFGJONOIPTF-UHFFFAOYSA-N Sodium cation Chemical compound [Na+] FKNQFGJONOIPTF-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 229910052681 coesite Inorganic materials 0.000 description 1
- 239000008119 colloidal silica Substances 0.000 description 1
- 229910052906 cristobalite Inorganic materials 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002389 environmental scanning electron microscopy Methods 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229910052909 inorganic silicate Inorganic materials 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 229910001415 sodium ion Inorganic materials 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229910052682 stishovite Inorganic materials 0.000 description 1
- 229910052905 tridymite Inorganic materials 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
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Abstract
The present invention discloses a kind of method for being catalyzed nucleation process synthesis magadiite, and the preparation method comprises the following steps:Silicon source, alkali source, catalysis nucleator and water are mixed, obtain mixture;Silicon source is met with the component in molar ratio computing mixture:Alkali source=3~7;Water:Alkali source=20~100;Mixture is put into closed container at autogenous pressures, 110~170 DEG C of crystallization 6~72 hours;The good product of crystallization is taken out, it is filtered, be washed to behind pH=7~8 in 60 DEG C~100 DEG C drying 4~12 hours, obtained two-dimensional layered-structure material magadiite.The synthesis cycle of the invention compared with the existing synthetic method for being not added with catalysis nucleator shortens 12~108 hours, synthesis temperature reduces 30~40 DEG C, and the magadiite can be used as catalyst, adsorbent, pillared composite, ion-exchanger, the filler etc. of nano composite material.
Description
Technical field
The present invention relates to magadiite synthetic method, and in particular to a kind of side for being catalyzed nucleation process synthesis magadiite
Method.
Background technology
Magadiite is a kind of two-dimensional layered-structure material, and its laminate is by electronegative SiO4Tetrahedron forms, and has
Preferably chemistry and heat endurance, interlayer have the hydration sodium ion that can be exchanged, have preferable dilatancy between laminate, can be with
Accommodate it is small arrive high-polymer molecular or group greatly to proton, these properties promote magadiite as cation-exchanger, absorption
The application of agent, pillared composite, catalyst, nano composite material filler etc..
The document on magadiite synthesis focuses mostly on different in the difference of silicon source, silicon source, alkali source, the proportioning of water at present
And itself and modenite, β zeolites, ZSM-35 one or more are compounded to form coexisting material, on catalysis nucleation process synthesis
Magadiite technique is not yet seen in word.
The content of the invention
The technical problems to be solved by the invention are that the synthesis cycle of magadiite in the prior art is longer, synthesis temperature
The problem of higher, there is provided a kind of method for being catalyzed nucleation process synthesis magadiite, the method is characterized in that improving nucleation speed
Also generation magadiite chemical reaction rate, the technique and the existing synthesis for being not added with being catalyzed nucleator are accelerated while rate
Method shortens 6~72 hours compared to synthesis cycle, and synthesis temperature reduces 6~20 DEG C.
To solve the above problems, the technical solution adopted by the present invention is as follows.
A kind of method for being catalyzed nucleation process synthesis magadiite, comprises the following steps:
(1) silicon source, alkali source, catalysis nucleator and water are mixed, obtains mixture;With the component in molar ratio computing mixture
Meet silicon source:Alkali source=3~7;Water:Alkali source=20~100;It is catalyzed two points that nucleator volume is no more than all volume of mixture
One of, and more than 1/6th of all volume of mixture;
(2) mixture that step (1) obtains is put into closed container at autogenous pressures, 110~170 DEG C of crystallization 6~144
Hour;
(3) the good product of crystallization is taken out, it is filtered, be washed to it is small in 60 DEG C~100 DEG C dryings 4~12 behind pH=7~8
When, two-dimensional layered-structure material magadiite is made.
In the above method, silicon source described in step (1) in aerosil or precipitated silica it is a kind of with
On.
In the above method, the alkali source described in step (1) is sodium hydroxide and the mixture of sodium carbonate;With molar ratio computing,
Wherein Na2CO3:NaOH=2~5.
In the above method, in step (1), described is catalyzed nucleator as one kind in bead, ceramic bead or steel ball, institute
State a diameter of 2mm~7mm of catalysis nucleator.
In the above method, in step (1), described catalysis nucleator is not involved in chemosynthesis reaction, reuses.
In the above method, concretely comprised the following steps described in step (1) by what silicon source, alkali source, catalysis nucleator and water mixed:First
Alkali source and water are mixed into solution, then mixed with silicon source, is finally mixed with catalysis nucleator.
Synthesis temperature reduces 6~20 DEG C degrees Celsius in the present invention, and its principle can be construed to:Its catalytic action is due to
The addition of catalysis nucleator makes some groups of reactant fix to form intermediate product with nucleating agent haptoreaction first, it
Carry out into nuclear reaction again afterwards, intermediate product is reduced to be nucleated catalytic machine and generates target product, and the generation of such intermediate product changes
Become response path, reduced the activation energy of reaction, and then reduced reaction temperature, improve reaction rate;Nucleation can
It is interpreted as in the case of no catalysis nucleator, as homogeneous nucleation, nucleation rate are:
N in formula --- the atomicity in unit volume liquid phase;
κ --- Boltzmann constant;
ΔGA--- atom crosses the activation energy through liquid-solid interface:
α --- nucleus form factor, to spherical nucleus, π/3 of α=16;
ΔGv--- volume free energy is poor.
The free Δ G of forming core of heterogeneous nucleationsAnd the forming core speed μ in the unit area of heterogeneous nucleussCalculating formula difference
For:
ΔGs=Δ G·f(θ)
In formula
The contact angle of θ --- nascent crystals and heterogeneous nucleus
Ns--- the atomicity in unit area
Remaining symbol is identical with the homogeneous nucleation formula without nucleator.
From three formula above, unless θ=180 °, otherwise f (θ) is always less than 1, so volume needed for Heterogeneous Nucleation
Forming core free energy is always less than the free energy of average forming core, and nucleation rate is always higher than the nucleation rate of homogeneous nucleation, and θ angles are got over
Small, difference is bigger, that is to say, that when reactant solution shows that wellability is better with nucleator, nucleation rate is higher.[Xing Jiandong,
Epitaxis [M], publishing house of Xi'an Communications University, 2008.5,5-7].So there is catalysis and the effect of nucleation simultaneously,
Tentatively it is referred to as " catalysis nucleation ".
Compared with prior art, the invention has the advantages that and technique effect:
The present invention adds catalysis nucleator, has synthesized the magadiite of simple phase under the process conditions limited,
This method synthesis cycle compared with the existing synthetic method for being not added with catalysis nucleator shortens 6~96 hours, and synthesis temperature reduces
6~20 DEG C degrees Celsius.Obtained material is with two-dimensional layered structure and interlayer is with tradable cation, is handed in ion
Change, be catalyzed, adsorbing etc. is widely used.
Brief description of the drawings
Fig. 1 is the X-ray diffracting spectrum of gained magadiite in embodiment 1.
Fig. 2 is the X-ray diffracting spectrum of gained magadiite in embodiment 2.
Fig. 3 is the X-ray diffracting spectrum of gained magadiite in embodiment 3.
Fig. 4 is the X-ray diffracting spectrum of gained magadiite in embodiment 4.
Fig. 5 a and Fig. 5 b are the ESEM collection of illustrative plates of gained magadiite in embodiment 4.
Embodiment
The present invention is described in detail below by embodiment, but protection scope of the present invention is not limited to these embodiments.
Fume colloidal silica (the SiO arrived used in following examples2Content wt.% >=99.8), buy in Jiang Xijia
Prompt new material Co., Ltd;Precipitated silica (93%SiO2, 7%H2O), buy in Shanghai Zhen Jiang Chemical Co., Ltd.s.
Embodiment 1
Take 0.40 gram of sodium hydroxide and 2.12 grams of sodium carbonate to be successively dissolved in 53.05 grams of water and mixed solution is made, will mix
Solution and 13.55 grams of precipitated silicas (aqueous 7wt%) add 15 points of 50 ceramic beads (diameter 5mm) and stirring after being sufficiently mixed
Clock, it is stirring evenly and then adding into autoclave and hydrothermal crystallizing is carried out at 110 DEG C 36 hours.Product is filtered, is washed to pH
Dried 6 hours at 80 DEG C after=7~8, produce magadiite.Qualitative analysis (its X-ray is carried out by X-ray diffraction method
Diffraction spectrogram is shown in accompanying drawing 1), it is known that the magadiite is simple phase, and with plus catalysis nucleator and method the same terms not
Same product is the same, and crystallization degree is suitable, it is known that the catalysis nucleation of ceramic bead makes reaction is approximate to shorten synthesis at 110 DEG C
Time 108h.
Embodiment 2
Take 0.40 gram of sodium hydroxide and 2.12 grams of sodium carbonate to be successively dissolved in 42.39 grams of water and mixed solution is made, will mix
Solution and 11.61 grams of precipitated silicas (aqueous 7wt%) add 15 points of 50 ceramic beads (diameter 5mm) and stirring after being sufficiently mixed
Clock, it is stirring evenly and then adding into autoclave and hydrothermal crystallizing is carried out at 110 DEG C 36 hours.Product is filtered, is washed to pH
Dried 6 hours at 80 DEG C after=7~8, produce magadiite, (electron-microscope scanning figure of the present embodiment products obtained therefrom can refer to figure
5b).Qualitative analysis (its X-ray diffraction spectrogram is shown in accompanying drawing 2) is carried out by X-ray diffraction method, it is known that the magadiite is single
Pure phase, crystallization degree are suitable, it is known that the product synthesized under the conditions of 150 DEG C, 36h ceramic bead catalysis nucleation under 110 DEG C,
36h cans are synthesized, and approximation reduces by 40 DEG C of synthesis temperature.
Embodiment 3
Take 0.40 gram of sodium hydroxide and 2.12 grams of sodium carbonate to be successively dissolved in 26.32 grams of water and mixed solution is made, will mix
Solution and 9.68 grams of precipitated silicas (aqueous 7wt%) add 15 points of 50 beades (diameter 5mm) and stirring after being sufficiently mixed
Clock, it is stirring evenly and then adding into autoclave and hydrothermal crystallizing is carried out at 130 DEG C 24 hours.Product is filtered, is washed to pH
Dried 6 hours at 80 DEG C after=7~8, produce magadiite, (electron-microscope scanning figure of the present embodiment products obtained therefrom can refer to figure
5b).Qualitative analysis (its X-ray diffraction spectrogram is shown in accompanying drawing 3) is carried out by X-ray diffraction method, it is known that the magadiite is single
Pure phase, and with without plus catalysis nucleator and the different product of method the same terms as, and with no plus catalysis nucleator and
The different product of method the same terms is the same, it is known that the product synthesized under the conditions of 160 DEG C, 24h is nucleated in the catalysis of ceramic bead
Lower 130 DEG C, 24h cans be synthesized, approximation reduce by 30 DEG C of synthesis temperature.
Embodiment 4
Take 0.40 gram of sodium hydroxide and 2.12 grams of sodium carbonate to be successively dissolved in 10.26 grams of water and mixed solution is made, will mix
Solution and 7.74 grams of precipitated silicas (aqueous 7wt%) add 50 steel balls (diameter 5mm) and stirred 15 minutes after being sufficiently mixed,
It is stirring evenly and then adding into autoclave and hydrothermal crystallizing is carried out at 170 DEG C 6 hours.Product is filtered, be washed to pH=7~
Dried 6 hours at 80 DEG C after 8, produce magadiite, (electron-microscope scanning figure of the present embodiment products obtained therefrom can refer to Fig. 5 b).
Such as the magadiite electron-microscope scannings soil in Fig. 5 a and Fig. 5 b (wherein Fig. 5 a are not add 170 DEG C of hydrothermal crystallizing 18h of catalysis nucleator)
In it can be seen that it has the rose valvular structure of stratiform, i.e., with two-dimensional layered structure, by contrast as can be seen that adding
The product of nucleating agent has more perfect crystallization structure and more orderly layer structure, is entered by X-ray diffraction method
Row qualitative analysis (its X-ray diffraction spectrogram is shown in accompanying drawing 4), it is known that the magadiite is simple phase, and is catalyzed into not adding
Core agent and method the same terms it is different product it is the same, it is known that the catalysis nucleation of steel ball makes the approximate contracting of reaction at 170 DEG C
Short generated time 12h.
The above embodiment of the present invention is only intended to clearly illustrate example of the present invention, and is not to the present invention
Embodiment restriction.For those of ordinary skill in the field, can also make on the basis of the above description
Other various forms of changes or variation.There is no necessity and possibility to exhaust all the enbodiments.It is all the present invention
All any modification, equivalent and improvement made within spirit and principle etc., should be included in the protection of the claims in the present invention
Within the scope of.
Claims (1)
- A kind of 1. method for being catalyzed nucleation process synthesis magadiite, it is characterised in that comprise the following steps:(1)Silicon source, alkali source, catalysis nucleator and water are mixed, obtain mixture;Met with the component in molar ratio computing mixture Silicon source:Alkali source=3~7;Water:Alkali source=20~100;The half that nucleator volume is no more than all volume of mixture is catalyzed, And more than 1/6th of all volume of mixture;Described catalysis nucleator is one in bead, ceramic bead or steel ball Kind, a diameter of 2mm~7mm of the catalysis nucleator;Described alkali source is the mixture of sodium hydroxide and sodium carbonate;With mole Than meter, wherein Na2CO3:NaOH=2~5;It is described to be concretely comprised the following steps what silicon source, alkali source, catalysis nucleator and water mixed:First will Alkali source and water are mixed into solution, are then mixed with silicon source, are finally mixed with catalysis nucleator;Described silicon source is gas phase titanium dioxide One or more of silicon or precipitated silica;Described catalysis nucleator is not involved in chemosynthesis reaction, reuses;(2)By step(1)Obtained mixture is put into closed container at autogenous pressures, and 110~170 DEG C of crystallization 6~144 are small When;(3)The good product of crystallization is taken out, it is filtered, be washed to behind pH=7~8 in 60 DEG C~100 DEG C drying 4~12 hours, make Obtain two-dimensional layered-structure material magadiite.
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CN102174209A (en) * | 2011-01-25 | 2011-09-07 | 中国科学院宁波材料技术与工程研究所 | Method for preparing controlled degradable polypropylene foamed particles |
CN103073004A (en) * | 2012-12-20 | 2013-05-01 | 华南理工大学 | Preparation method of two-dimensional layered-structure material magadiite |
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CN102174209A (en) * | 2011-01-25 | 2011-09-07 | 中国科学院宁波材料技术与工程研究所 | Method for preparing controlled degradable polypropylene foamed particles |
CN103073004A (en) * | 2012-12-20 | 2013-05-01 | 华南理工大学 | Preparation method of two-dimensional layered-structure material magadiite |
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