CN103586058A - Supported phosphotungstic acid catalyst, preparation method and application thereof, and ethyl acetate preparation method - Google Patents
Supported phosphotungstic acid catalyst, preparation method and application thereof, and ethyl acetate preparation method Download PDFInfo
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- CN103586058A CN103586058A CN201210289209.5A CN201210289209A CN103586058A CN 103586058 A CN103586058 A CN 103586058A CN 201210289209 A CN201210289209 A CN 201210289209A CN 103586058 A CN103586058 A CN 103586058A
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Abstract
The invention discloses a supported phosphotungstic acid catalyst, a preparation method thereof, and an ethyl acetate preparation method. The catalyst is composed of 10-90wt% of a support and 10-90wt% of phosphotungstic acid supported on the support, the support is hexahedral meso-porous silica, and the bottom surface edge length, the height, the specific surface area, the pore volume, the most probable aperture and the pore wall thickness of the support are 2.5-5.0mum, 1-10mum, 500-700m<2>/g, 0.4-1.0ml/g, 3.0-7.0nm and 6-7 respectively, In the catalyst, phosphotungstic acid is supported on the specific hexahedral meso-porous silica support, so the esterifying catalysis activity of the catalyst is high, and is still high after repeated use, thereby the catalyst can be recovered and recycled.
Description
Technical field
The present invention relates to a kind of carried phospho-tungstic acid Catalysts and its preparation method, also relate to and use the application of this catalyst in esterification, and the preparation method of ethyl acetate.
Background technology
Within 1992, Mobile company synthesizes mesoporous material (Beck J S, Vartuli J C, Roth W J, et al.J.Am.Chem.Soc., 1992,114 (27): 10834-10843), this mesoporous material has high specific surface, regular pore passage structure and narrow pore-size distribution, make mesoporous material obtain very large concern in the application of catalysis, separation, medicine and other fields; Within 1998, Zhao east unit waits people to synthesize a kind of new material-mesoporous material SBA-15 (D.Y.Zhao, J.L.Feng, Q.S.Huo, et al Science 279 (1998) 548-550), this material has the block mesoporous material aperture (6-30nm) of hexahedron, the large (1.0cm of pore volume of high-sequential
3/ g), the high mechanical properties that thicker hole wall (4-6nm) keeps and good catalytic adsorption performance; Zhao Dongyuan, Yu Chengzhong, Yu Yonghao invent a kind of preparation method (CN1341553A) of mesonic pore molecular sieve carrier material, and this mesoporous material is as heterogeneous reaction catalyst carrier, easily realize separated (Wight, the A.P. of catalyst and product; Davis, M.E.Chem.Rev.2002,102,3589; De Vos, D.E.; Dams, M.; Sels, B.F.; Jacobs, P.A.Chem.Rev.2002,102,3615.).Yet conventional ordered mesoporous material SBA-15 has stronger water suction, moisture absorption ability at present, rod length approaches 5 μ m, and there is adhesion between rod and rod, in catalytic reaction process, be unfavorable for that material transmits in mesopore orbit, this will further aggravate the reunion of ordered mesoporous material, give ordered mesoporous material storage, transport, rear processing and application make troubles.
Esterification catalytic reaction common acid is as catalyst, except traditional inorganic acid, and solid super-strong acid (Van Rhijn, W.M. that the mesoporous material of take is in addition carrier; De Vos, D.E.; Sels, B.F.; Et al.Chem. Commun.1998, No.3,317.; Du, C.H.; Qin, Y.N.; He, Y.F.; Et al.Chin.J.Chem.Phys.2003,16,504.[，Qin Yongning, Changhai of shutting out, He Yan seam, Ma Zhi, Wu Shuxin, Chinese Journal of Chemical Physics, 2003,16,504.]) and ionic liquid (Chiappe, C.; Pieraccini, D.J.Phys.Org.Chem.2005,18,275.; Qiao, K.; Hagiwara, H.; Yokoyama, C.J.Mole.Catal.A:Chem.2006,246,65.; Chen Weiyi, ground force, Zhang Yong, organic chemistry, 2006,26,87.) etc.Inorganic acid catalyst is to instrument seriously corroded, and homogeneous catalysis product is not easily separated, easily produces the pollutants such as spent acid waste liquid; Solid acid has pair shortcoming of instrument seriously corroded equally, and catalytic activity reduction is fast, and cost is higher.As using mesoporous material as carrier loaded homogeneous catalyst, can avoid instrument corrosion, catalyst is easily realized the separated of catalyst and product, recycling repeatedly.Conventional carrying method is solvent method supported catalyst at present, processes in catalyst process and also must remove added solvent, and technique is more complicated, and cost is increased.
Therefore, develop a kind of novel catalyst for the synthesis of ethyl acetate and become problem in the urgent need to address.
Summary of the invention
The object of the invention is to overcome the existing shortcomings such as, complex process serious to equipment corrosion for catalyzing and synthesizing that the catalyst of ethyl acetate exists, a kind of preparation method of novel catalyst and ethyl acetate for the synthesis of ethyl acetate is provided.
The invention provides a kind of carried phospho-tungstic acid catalyst, wherein, this catalyst is comprised of the block meso-porous titanium dioxide silicon carrier of hexahedron and the phosphotungstic acid that loads on the block meso-porous titanium dioxide silicon carrier of described hexahedron, and the gross weight of described catalyst of take is benchmark, the content of described phosphotungstic acid is 10-90 % by weight, and the content of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 10-90 % by weight; The bottom surface length of side of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 2.5-5.0 micron, and height is 1-10 micron, and specific area is 500-700 meters squared per gram, and most probable aperture is 3.0-7.0 nanometer, and pore wall thickness is 6-7 nanometer.
The present invention also provides a kind of preparation method of carried phospho-tungstic acid catalyst, wherein, the method comprises: by the block meso-porous titanium dioxide silicon carrier of hexahedron ball milling together with phosphotungstic acid, phosphotungstic acid is loaded on the block meso-porous titanium dioxide silicon carrier of described hexahedron, the gross weight of the block meso-porous titanium dioxide silicon carrier of the described hexahedron of take and phosphotungstic acid is benchmark, the consumption of described phosphotungstic acid is 10-90 % by weight, and the consumption of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 10-90 % by weight; The bottom surface length of side of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 2.5-5.0 micron, and height is 1-10 micron, and specific area is 500-700 meters squared per gram, and most probable aperture is 3.0-7.0 nanometer, and pore wall thickness is 6-7 nanometer.
In addition, the present invention also provides the application of described catalyst in esterification.
Also have, the present invention also provides a kind of preparation method of ethyl acetate, wherein, the method comprises: under the existence of catalyst, under the condition of esterification, acetic acid is contacted with ethanol, to obtain ethyl acetate, wherein, described catalyst is carried phospho-tungstic acid catalyst provided by the invention.
In catalyst of the present invention, phosphotungstic acid loads on the block meso-porous titanium dioxide silicon carrier of specific hexahedron, on the one hand, not only the activity of this carried phospho-tungstic acid catalyst esterification is higher, and the activity of this carried phospho-tungstic acid catalyst esterification is still higher while reusing, and this carried phospho-tungstic acid catalyst is recovered and cycling and reutilization.Also owing to thering is corrosive phosphotungstic acid, load on the block meso-porous titanium dioxide silicon carrier of specific hexahedron on the other hand, prevented equipment corrosion, so this carried phospho-tungstic acid catalyst catalyst that is a kind of environmental protection.
In the present invention, by ball-milling method, phosphotungstic acid is carried on the block meso-porous titanium dioxide silicon carrier of specific hexahedron, in whole mechanical milling process, do not introduce solvent, process is simple and easy to do, after mechanical milling process, gained catalyst also keeps hexahedron block, and while carrying out the esterification of catalysis acetic acid and ethanol with this catalyst, catalyst can pass through and reclaim and Reusability, and carried phospho-tungstic acid catalyst provided by the invention can reduce side reaction, improve product purity, etching apparatus, is not conducive to environmental protection.
Accompanying drawing explanation
Fig. 1 is X-ray diffracting spectrum, wherein, a is that XRD spectra, the b of the block meso-porous titanium dioxide silicon carrier of hexahedron (FDU) is the XRD spectra of the block mesoporous silicon oxide of hexahedron (FDU-HPA) and the XRD spectra of the block mesoporous silicon oxide of hexahedron (FDU-HPA) that c is the reacted load phosphotungstic acid of quadric catalysis by ball-milling method load phosphotungstic acid, abscissa is 2 θ, and ordinate is intensity.
Fig. 2 is TEM transmission electron microscope picture, wherein, and a
1and a
2for the pore structure schematic diagram of the block meso-porous titanium dioxide silicon carrier of hexahedron (FDU), b for by ball-milling method load the pore structure schematic diagram of the block mesoporous silicon oxide of hexahedron (FDU-HPA) of phosphotungstic acid.
Fig. 3 is SEM scanning electron microscope (SEM) photograph, wherein, and a
1and a
2for the microscopic appearance figure of the block meso-porous titanium dioxide silicon carrier of hexahedron (FDU), b
1for by ball-milling method load the microscopic appearance figure of the block mesoporous silicon oxide of hexahedron (FDU-HPA) of phosphotungstic acid.
Fig. 4 is SEM scanning electron microscope (SEM) photograph, and wherein, a is the microscopic appearance figure of rod-like mesoporous material SBA-15, the microscopic appearance figure of the rod-like mesoporous material SBA-15 that b is the load phosphotungstic acid prepared by ball-milling method.
The specific embodiment
The invention provides a kind of carried phospho-tungstic acid catalyst, wherein, this catalyst comprises the block meso-porous titanium dioxide silicon carrier of hexahedron and loads on the phosphotungstic acid on the block meso-porous titanium dioxide silicon carrier of described hexahedron, and the gross weight of described catalyst of take is benchmark, the content of described phosphotungstic acid is 10-90 % by weight, the content of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 10-90 % by weight, more preferably in situation, the gross weight of described catalyst of take is benchmark, the content of described phosphotungstic acid is 30-60 % by weight, the content of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 40-70 % by weight.
The bottom surface length of side of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 2.5-5.0 micron, is preferably 2.5-4.5 micron, more preferably 4 microns; Height is 1-10 micron, is preferably 2-8 micron, more preferably 5 microns; Specific area is 500-700 meters squared per gram, is preferably 550-650 meters squared per gram, more preferably 598 meters squared per gram; Pore volume is 0.4-1.0 ml/g, is preferably 0.5-0.9 ml/g, more preferably 0.7 ml/g; Most probable aperture is 3.0-7.0 nanometer, is preferably 4-6 nanometer, more preferably 4.8 nanometers; Pore wall thickness is 6-7 nanometer, is preferably 6.4 nanometers.
The various hexahedron structures that hexahedron bulk described in the present invention can it has been generally acknowledged that for this area; In this case, not only can obtain gratifying catalytic effect, but also can reduce costs.
According to the present invention, the specific area of described carried phospho-tungstic acid catalyst can be 20-50 meters squared per gram, is preferably 25-40 meters squared per gram, more preferably 32 meters squared per gram; Pore volume can be 0.1-0.5 ml/g, is preferably 0.1-0.3 ml/g, more preferably 0.1 ml/g; Most probable aperture can be 1-7 nanometer, is preferably 3-5 nanometer, more preferably 3.8 nanometers; Pore wall thickness is 4-10.0 nanometer, is preferably 6-8 nanometer, more preferably 7.5 nanometers.
According to the present invention, described carrier is the block mesoporous silicon oxide of hexahedron, and the block mesoporous silicon oxide of described hexahedron can prepare by the method comprising the following steps:
(1) template, potassium sulfate and mixed in hydrochloric acid to solids is fully dissolved;
(2) the standing 1-20 hour after 25-60 ℃ of temperature, mechanical agitation speed are to stir 5-60 minute under 100-400r/min by step (1) gained solution and esters of silicon acis;
(3) by step (2) products therefrom crystallization under crystallization condition;
(4) step (3) gained crystallization product is filtered, and will filter deionized water washing for gained solid, dry;
(5) by the dry products therefrom heating of step (4), removed template method;
Described template is polyethylene glycol oxide-PPOX-polyethylene glycol oxide.
Under preferable case, described esters of silicon acis is ethyl orthosilicate.
Under preferable case, described crystallization condition comprises that temperature is 90-180 ℃, is preferably 95-110 ℃, and the time is 10-40 hour, is preferably 12-30 hour.
Under preferable case, the condition of described removed template method comprises that temperature is 300-600 ℃, is preferably 350-550 ℃, and the time is 8-20 hour, is preferably 10-19 hour.
Under preferable case, count in molar ratio, polyethylene glycol oxide-PPOX-polyethylene glycol oxide: potassium sulfate: water: hydrogen chloride: esters of silicon acis=1:100-800:10000-30000:10-9000:20-200, be preferably 1:50-700:12000-25000:500-8500:30-100, be particularly preferably 1:63:14320:1846:60.Wherein, the molal quantity of polyoxyethylene-poly-oxypropylene polyoxyethylene calculates according to the mean molecule quantity of polyoxyethylene-poly-oxypropylene polyoxyethylene.
Described template can be the conventional various triblock copolymer polyoxyethylene-poly-oxypropylene polyoxyethylene templates that use in this area, for example, can be that the commodity that Fuka company produces are called
the template of F108, molecular formula is EO
132pO
60eO
132.
The present invention also provides a kind of preparation method of catalyst, wherein, the method comprises: by the block meso-porous titanium dioxide silicon carrier of hexahedron together with phosphotungstic acid in ball sealer grinding jar ball milling, phosphotungstic acid is loaded on the block meso-porous titanium dioxide silicon carrier of described hexahedron, the gross weight of the block meso-porous titanium dioxide silicon carrier of the described hexahedron of take and phosphotungstic acid is benchmark, the consumption of described phosphotungstic acid is 10-90 % by weight, the consumption of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 10-90 % by weight, more preferably, the gross weight of the block meso-porous titanium dioxide silicon carrier of the described hexahedron of take and phosphotungstic acid is benchmark, the consumption of described phosphotungstic acid is 30-60 % by weight, the consumption of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 40-70 % by weight.
According to the present invention, the bottom surface length of side of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 2.5-5.0 micron, is preferably 2.5-4.5 micron, more preferably 4 microns; Height is 1-10 micron, is preferably 2-8 micron, more preferably 5 microns; Specific area is 500-700 meters squared per gram, is preferably 550-650 meters squared per gram, more preferably 598 meters squared per gram; Pore volume is 0.4-1.0 ml/g, is preferably 0.5-0.9 ml/g, more preferably 0.7 ml/g; Most probable aperture is 3.0-7.0 nanometer, is preferably 4-6 nanometer, more preferably 4.8 nanometers; Pore wall thickness is 6-7 nanometer, is preferably 6.4 nanometers.The various hexahedrons that hexahedron bulk described in the present invention can it has been generally acknowledged that for this area.
To the condition of grinding and concrete operation method, there is no particular limitation, not destroy or substantially not destroy carrier structure and phosphotungstic acid is entered in carrier duct, is as the criterion.Those skilled in the art can select various suitable conditions to implement the present invention according to mentioned above principle.
According to one embodiment of the present invention, the preparation method of described carried phospho-tungstic acid catalyst comprises: the block mesoporous silicon oxide of hexahedron and phosphotungstic acid are joined in the ball grinder of ball mill, ball grinder inwall is polytetrafluoroethyllining lining, the diameter of abrading-ball is 2-3mm, rotating speed is 300-500r/min, in ball grinder, temperature is continuously grinding 0.1-100 hour at 15-100 ℃, takes out afterwards pressed powder, obtains the block mesoporous silicon oxide of hexahedron of load phosphotungstic acid.The quantity of abrading-ball depends on the size of ball grinder, and the ball grinder that is 50-150ml for size can be used 1 abrading-ball.The material of described abrading-ball can be agate, polytetrafluoroethylene (PTFE), is preferably polytetrafluoroethylene (PTFE).
According to a kind of specific embodiment of the present invention, the preparation method of described carried phospho-tungstic acid catalyst comprises the following steps:
The 1st step, by triblock copolymer polyethylene glycol oxide-PPOX-polyethylene glycol oxide (EO
132pO
60eO
132, be abbreviated as F108) and potassium sulfate, join in hydrochloric acid, by molar feed ratio,
Count in molar ratio, polyethylene glycol oxide-PPOX-polyethylene glycol oxide: potassium sulfate: water: hydrogen chloride=1:100-800:10000-30000:10-9000,
Being mixed to solids fully dissolves;
The 2nd step adds ethyl orthosilicate in previous step gained solution, and at 25 ℃ of-60 ℃ of temperature, mechanical agitation speed is under 100-400r/min, to stir standing 1-20 hour after 5-60 minute; Press molar feed ratio,
Triblock copolymer polyoxyethylene-poly-oxypropylene polyoxyethylene: ethyl orthosilicate=1:20-200; Elect 1:30-100 as, more preferably 1:63;
The 3rd step, is placed in closed reaction vessel by upper step gained solution, crystallization 10-40 hour at 90-180 ℃ of temperature;
The 4th step, filters crystallization afterproduct (preferably with after deionized water dilution), will filter deionized water washing for gained solid, dry, obtains the block mesoporous material raw powder of hexahedron;
The 5th step, by the block mesoporous material raw powder of gained hexahedron in Muffle furnace at 250-800 ℃ of temperature lower calcination 10-40 hour, removed template method, obtains the block mesoporous material of hexahedron of removed template method;
The 6th step, the block mesoporous silicon oxide of the hexahedron of upper step gained removed template method and phosphotungstic acid are joined in the ball grinder of ball mill, rotating speed be under 300-500r/min in ball grinder temperature be continuously grinding 0.1-100 hour at 15-100 ℃, the gross weight of the block meso-porous titanium dioxide silicon carrier of the described hexahedron of take and phosphotungstic acid is benchmark, the consumption of described phosphotungstic acid is 10-90 % by weight, and the consumption of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 10-90 % by weight; The consumption that is preferably described phosphotungstic acid is 30-60 % by weight, and the consumption of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 40-70 % by weight, takes out afterwards pressed powder, obtains the block mesoporous silicon oxide of hexahedron of load phosphotungstic acid.
Described template can be the conventional various triblock copolymer polyoxyethylene-poly-oxypropylene polyoxyethylene templates that use in this area, for example, can be the template of the commodity F108 by name of Aldrich company production.
Method and the condition of described crystallization and removed template method are known to the skilled person, and for example, crystallization temperature is 90-180 ℃, is preferably 95-110 ℃, and the time is 10-40 hour, is preferably 12-30 hour; The condition of described removed template method comprises that temperature is 300-600 ℃, is preferably 350-550 ℃, and the time is 8-20 hour, is preferably 10-19 hour.
In addition, the present invention also provides the application of described catalyst in esterification.
Also have, the present invention also provides a kind of preparation method of ethyl acetate, wherein, the method comprises: under the existence of catalyst, under the condition of esterification, acetic acid is contacted with ethanol, to obtain ethyl acetate, wherein, described catalyst is carried phospho-tungstic acid catalyst provided by the invention.
According to the present invention, in esterification, the mol ratio of acetic acid and ethanol can in very large range change, for example, the mol ratio of acetic acid and ethanol can be 1:0.5-10, and the consumption of described carried phospho-tungstic acid catalyst has no particular limits, those skilled in the art can carry out suitable adjustment according to the needs of reaction, but under preferable case, with respect to the acetic acid of 100 weight portions, the consumption of described catalyst can be 0.5-50 weight portion.
In the present invention, the condition of described esterification is conventionally known to one of skill in the art, for example, the condition of described esterification can comprise: the temperature of reaction is 100-150 ℃, the time of reaction is 0.5-72 hour, preferably, the temperature of reaction can be 120-140 ℃, and the time of reaction can be 20-30 hour.
According to the present invention, after esterification finishes, can carry out centrifugation to final reactant mixture, by the centrifugal solid formation obtaining vacuum drying 1-24 hour at 25-200 ℃, preferred vacuum drying 6-10 hour at 50-120 ℃, the catalyst that can be recycled.
Below in conjunction with embodiment, the present invention is described in detail.
In following examples, polyethylene glycol oxide-PPOX-polyethylene glycol oxide, is abbreviated as F108, and molecular formula is EO
132pO
60eO
132, commodity are by name
the material of F108.
In following examples, phosphotungstic acid (CAS12501-2-4) is a kind of heteropoly acid, buys from ACROS, and mean molecule quantity is 2880.
In following examples, on the X-ray diffractometer that X-ray diffraction analysis is D8Advance in the model purchased from German Bruker AXS company, carry out; Transmission electron microscope analysis is to carry out on the transmission electron microscope of Tecnai 20 in the model purchased from Dutch FEI Co.; In the SEM that scanning electron microscope analysis is XL-30 in the model purchased from U.S. FEI Co., carry out; On the nitrogen adsorption desorption instrument that the experiment of nitrogen adsorption-desorption is Autosorb-1 in the model purchased from U.S. Kang Ta company, carry out.
Embodiment 1
The present embodiment is for illustrating according to carried phospho-tungstic acid Catalysts and its preparation method of the present invention.
By 2.0 grams of F108 and 5.24 grams of potassium sulfate K
2sO
4join in the hydrochloric acid of 60 gram of 2 mol/L, mix to F108 and dissolve completely; Again 4.2 grams of ethyl orthosilicates are joined in above-mentioned solution at 38 ℃ of temperature to after stir speed (S.S.) is to stir 1 hour under 200r/min standing 20 hours; Gained solution is transferred in teflon-lined reactor, 100 ℃ of crystallization, after 24 hours, after filtering, wash, being dried, obtained the block mesoporous material raw powder of hexahedron; By the 400 ℃ of calcinings 10 hours in Muffle furnace of the block mesoporous material raw powder of hexahedron, removed template method, obtains the block mesoporous silicon oxide (FDU) of hexahedron of removed template method.
The block mesoporous silicon oxide FDU of above-mentioned 1 gram of hexahedron is put into 100ml ball grinder at room temperature state together with 1 gram of phosphotungstic acid, and the material of ball grinder and abrading-ball is polytetrafluoroethylene (PTFE), and the diameter of abrading-ball is 3mm, and quantity is 1, and rotating speed is 400r/min.Closure ball grinding jar, in ball grinder, temperature is ball milling 1 hour at 60 ℃, obtain 2 grams of target product carried phospho-tungstic acid catalyst, called after FDU-HPA, wherein, according to weight * 100% of weight/carried phospho-tungstic acid catalyst of the carrier of the content of carrier=add, calculate, the total amount of carried phospho-tungstic acid catalyst of take is benchmark, the content of phosphotungstic acid is 50 % by weight, and the content of the block meso-porous titanium dioxide silicon carrier of hexahedron is 50 % by weight.
With XRD, ESEM, transmission electron microscope and nitrogen adsorption desorption instrument, this carried phospho-tungstic acid catalyst is characterized.
Fig. 1 is X-ray diffracting spectrum, wherein, a is the XRD spectra of the block meso-porous titanium dioxide silicon carrier of hexahedron (FDU), b is the XRD spectra of the block mesoporous silicon oxide of the hexahedron by ball-milling method load phosphotungstic acid (FDU-HPA), and c is the XRD spectra of the block mesoporous silicon oxide of hexahedron (FDU-HPA) of the reacted load phosphotungstic acid of quadric catalysis, abscissa is 2 θ, and ordinate is intensity.In XRD spectra, can find out significantly that sample F DU and FDU-HPA occur 1 diffraction maximum in little angular region.The block meso-porous titanium dioxide silicon carrier (FDU) of hexahedron is described and passes through the block mesoporous silicon oxide (FDU-HPA) of hexahedron of ball-milling method load phosphotungstic acid and the XRD spectra of the block mesoporous silicon oxide of hexahedron (FDU-HPA) of the reacted load phosphotungstic acid of quadric catalysis, there is good mesoporous phase structure, and there is two-dimentional hexagonal structure, consistent (the Sun Jinyu of mesoporous material XRD spectra of this and bibliographical information, Zhao Dongyuan, " six squares " shape high-sequential big-pore mesoporous molecular sieve SBA-15's is synthetic, SCI, 2000, 1 (21): 21 ~ 23).
Fig. 2 is TEM transmission electron microscope picture, wherein, and a
1and a
2be the pore structure schematic diagram of the block meso-porous titanium dioxide silicon carrier of hexahedron (FDU), b for by ball-milling method load the pore structure schematic diagram of the block mesoporous silicon oxide of hexahedron (FDU-HPA) of phosphotungstic acid.From TEM transmission electron microscope picture, the block meso-porous titanium dioxide silicon carrier of hexahedron (FDU) is in the forward and backward peculiar two-dimentional hexagonal hole of the mesoporous material road structure that all shows of load phosphotungstic acid, the pore passage structure that shows sample substantially remains unchanged after supported catalyst, and the conclusion that this conclusion and XRD spectra obtain is consistent.
Fig. 3 is SEM scanning electron microscope (SEM) photograph, wherein, and a
1and a
2for the microscopic appearance figure of the block meso-porous titanium dioxide silicon carrier of hexahedron (FDU), b
1for by ball-milling method load the microscopic appearance figure of the block mesoporous silicon oxide of hexahedron (FDU-HPA) of phosphotungstic acid.As seen from the figure, the block mesoporous silicon oxide FDU of hexahedron microscopic appearance is that the bottom surface length of side is 2.5-5 micron, and height is that the hexahedron of 1-10 micron is block, and FDU-HPA microscopic appearance prepared by the ball-milling method still basic hexahedron that keeps is block, the bottom surface length of side is 2.5-5 micron, and height is 1-10 micron.
Fig. 4 is SEM scanning electron microscope (SEM) photograph, and wherein, a is the microscopic appearance figure of rod-like mesoporous material SBA-15, the microscopic appearance figure of the rod-like mesoporous material SBA-15 that b is the load phosphotungstic acid prepared by ball-milling method.The bar-shaped mesoporous silicon oxide SBA-15 microscopic appearance of the load phosphotungstic acid of preparing by ball-milling method as shown in Figure 4, is completely destroyed.
Table 1 is the pore structure parameter of the block mesoporous silicon oxide of hexahedron (FDU-HPA) of the block meso-porous titanium dioxide silicon carrier FDU of hexahedron and load phosphotungstic acid of the present invention.
Table 1
Note: average pore wall thickness=(a
0* 3
1/2)/2-average pore size;
Cell parameter a
0=d
100* 2
1/2;
D
100be 100 interplanar distances.
Data by upper table 1 can find out, the block mesoporous silicon oxide of hexahedron is after load phosphotungstic acid, and pore volume and specific area all significantly reduce, and this explanation phosphotungstic acid in load-reaction process enters into the block mesoporous silicon oxide composite inner of hexahedron.
The present embodiment is for illustrating according to carried phospho-tungstic acid Catalysts and its preparation method of the present invention.
According to the method for embodiment 1, prepare the block mesoporous silicon oxide (FDU) of hexahedron.
The block mesoporous silicon oxide FDU of above-mentioned 1 gram of hexahedron is put into 100ml ball grinder at room temperature state together with 2 grams of phosphotungstic acids, and the material of ball grinder and abrading-ball is polytetrafluoroethylene (PTFE), and the diameter of abrading-ball is 3mm, and quantity is 1, and rotating speed is 400r/min.Closure ball grinding jar, in ball grinder, temperature is ball milling 1 hour at 60 ℃, obtain 3 grams of target product carried phospho-tungstic acid catalyst, called after FDU-HPA-2, wherein, according to weight * 100% of weight/carried phospho-tungstic acid catalyst of the carrier of the content of carrier=add, calculate, the total amount of carried phospho-tungstic acid catalyst of take is benchmark, the content of phosphotungstic acid is 67 % by weight, and the content of the block meso-porous titanium dioxide silicon carrier of hexahedron is 33 % by weight.
With nitrogen adsorption desorption instrument, this carried phospho-tungstic acid catalyst is characterized.
Table 2
The present embodiment is for illustrating according to carried phospho-tungstic acid Catalysts and its preparation method of the present invention.
According to the method for embodiment 1, prepare the block mesoporous silicon oxide (FDU) of hexahedron.
The block mesoporous silicon oxide FDU of above-mentioned 1 gram of hexahedron is put into 100ml ball grinder at room temperature state together with 0.5 gram of phosphotungstic acid, and the material of ball grinder and abrading-ball is polytetrafluoroethylene (PTFE), and the diameter of abrading-ball is 3mm, and quantity is 1, and rotating speed is 400r/min.Closure ball grinding jar, in ball grinder, temperature is ball milling 1 hour at 60 ℃, obtain 1.5 grams of target product carried phospho-tungstic acid catalyst, called after FDU-HPA-3, wherein, according to weight * 100% of weight/carried phospho-tungstic acid catalyst of the carrier of the content of carrier=add, calculate, the total amount of carried phospho-tungstic acid catalyst of take is benchmark, the content of phosphotungstic acid is 33 % by weight, and the content of the block meso-porous titanium dioxide silicon carrier of hexahedron is 67 % by weight.
With nitrogen adsorption desorption instrument, this carried phospho-tungstic acid catalyst is characterized.
Table 3
The present embodiment is for illustrating the preparation with the block silica of hexahedron of dipping method load phosphotungstic acid
By the block mesoporous silicon oxide FDU of 1 gram of hexahedron of embodiment 1 preparation 400 ℃ of calcinings 10 hours under nitrogen protection, to remove hydroxyl and remaining moisture, thereby obtain the block mesoporous silicon oxide of hexahedron through thermal activation.
By the block mesoporous silicon oxide FDU of above-mentioned 1 gram of hexahedron through thermal activation vacuum drying 6 hours at 150 ℃, be cooled to after room temperature, again 30ml methyl alcohol and 4g phosphotungstic acid are put into 100ml teflon-lined reactor together, capping still, under 35 ℃ of conditions, stir 24 hours, obtain 1.25 grams of target product carried phospho-tungstic acid catalyst, called after FDU-HPA-JZ, wherein, according to weight * 100% of weight/carried phospho-tungstic acid catalyst of the carrier of the content of carrier=add, calculate, the total amount of carried phospho-tungstic acid catalyst of take is benchmark, the content of phosphotungstic acid is 20 % by weight, the content of the block meso-porous titanium dioxide silicon carrier of hexahedron is 80 % by weight.
With nitrogen adsorption desorption instrument, this carried phospho-tungstic acid catalyst is characterized.
Table 4
Comparative example 1
The bar-shaped mesoporous silicon oxide of preparing carried phospho-tungstic acid
By 1 gram of bar-shaped mesoporous silicon oxide SBA-15(purchased from high-tech share Co., Ltd of Jilin University) under room temperature state, put into 100ml ball grinder together with 1 gram of phosphotungstic acid, wherein, the material of ball grinder and abrading-ball is polytetrafluoroethylene (PTFE), the diameter of abrading-ball is 3mm, quantity is 1, and rotating speed is 400r/min.Closure ball grinding jar, in ball grinder, temperature is ball milling 1 hour at 60 ℃, obtains the rod-like mesoporous material (called after SBA-15-HPA) of 2 grams of load phosphotungstic acids.Wherein, according to weight * 100% of weight/carried phospho-tungstic acid catalyst of the carrier of the content of carrier=add, calculate, the total amount of carried phospho-tungstic acid catalyst of take is benchmark, and the content of phosphotungstic acid is 50 % by weight, and the content of bar-shaped meso-porous titanium dioxide silicon carrier is 50 % by weight.
With nitrogen adsorption desorption instrument, this carried phospho-tungstic acid catalyst is characterized.
Table 5
EXPERIMENTAL EXAMPLE 1
This EXPERIMENTAL EXAMPLE is used for explanation according to the catalytic activity of carried phospho-tungstic acid catalyst of the present invention.
By the vacuum drying 6 hours at 150 ℃ of the carried phospho-tungstic acid catalyst (FDU-HPA) in embodiment 1, be cooled to after room temperature, take 4 grams, then take 46 grams of ethanol, 60 grams of acetic acid are put into 100ml there-necked flask together, add condenser pipe, under 100 ℃ of conditions that add hot reflux, stir 4 hours, be cooled to after room temperature, centrifugation, adopts gc analysis reaction product liquid composition, result is: ethyl acetate is selectively 99%, and acetic acid conversion ratio is 95%.
EXPERIMENTAL EXAMPLE 2
This EXPERIMENTAL EXAMPLE is used for explanation according to the catalytic activity after carried phospho-tungstic acid catalyst recovery of the present invention.
Carried phospho-tungstic acid catalyst (FDU-HPA) in EXPERIMENTAL EXAMPLE 1 is reclaimed, and vacuum drying 6 hours at 150 ℃, be cooled to after room temperature, take 3 grams, take again 34.5 grams of ethanol, 45 grams of acetic acid are put into 100ml there-necked flask together, add condenser pipe, under 100 ℃ of conditions that add hot reflux, stir 4 hours, be cooled to after room temperature, centrifugation, adopt gc analysis reaction product liquid composition, result is: ethyl acetate is selectively 99%, and acetic acid conversion ratio is 90%.
EXPERIMENTAL EXAMPLE 3
This EXPERIMENTAL EXAMPLE is used for explanation according to the catalytic activity of carried phospho-tungstic acid catalyst of the present invention.
By the vacuum drying 6 hours at 150 ℃ of the carried phospho-tungstic acid catalyst (FDU-HPA-2) in embodiment 2, be cooled to after room temperature, take 2 grams, then take 23 grams of ethanol, 30 grams of acetic acid are put into 100ml there-necked flask together, add condenser pipe, under 100 ℃ of conditions that add hot reflux, stir 4 hours, be cooled to after room temperature, centrifugation, adopts gc analysis reaction product liquid composition, result is: ethyl acetate is selectively 99%, and acetic acid conversion ratio is 84%.
EXPERIMENTAL EXAMPLE 4
This EXPERIMENTAL EXAMPLE is used for explanation according to the catalytic activity after carried phospho-tungstic acid catalyst recovery of the present invention.
Carried phospho-tungstic acid catalyst (FDU-HPA-2) in EXPERIMENTAL EXAMPLE 3 is reclaimed, and vacuum drying 6 hours at 150 ℃, be cooled to after room temperature, take 1 gram, take again 11.5 grams of ethanol, 15 grams of acetic acid are put into 100ml there-necked flask together, add condenser pipe, under 100 ℃ of conditions that add hot reflux, stir 4 hours, be cooled to after room temperature, centrifugation, adopt gc analysis reaction product liquid composition, result is: ethyl acetate is selectively 99%, and acetic acid conversion ratio is 85%.
EXPERIMENTAL EXAMPLE 5
This EXPERIMENTAL EXAMPLE is used for explanation according to the catalytic activity of carried phospho-tungstic acid catalyst of the present invention.
By the vacuum drying 6 hours at 150 ℃ of the carried phospho-tungstic acid catalyst (FDU-HPA-3) in embodiment 3, be cooled to after room temperature, take 2 grams, then take 23 grams of ethanol, 30 grams of acetic acid are put into 100ml there-necked flask together, add condenser pipe, under 100 ℃ of conditions that add hot reflux, stir 4 hours, be cooled to after room temperature, centrifugation, adopts gc analysis reaction product liquid composition, result is: ethyl acetate is selectively 99%, and acetic acid conversion ratio is 85%.
EXPERIMENTAL EXAMPLE 6
This EXPERIMENTAL EXAMPLE is used for explanation according to the catalytic activity after carried phospho-tungstic acid catalyst recovery of the present invention.
Carried phospho-tungstic acid catalyst (FDU-HPA-3) in EXPERIMENTAL EXAMPLE 5 is reclaimed, and vacuum drying 6 hours at 150 ℃, be cooled to after room temperature, take 1 gram, take again 11.5 grams of ethanol, 15 grams of acetic acid are put into 100ml there-necked flask together, add condenser pipe, under 100 ℃ of conditions that add hot reflux, stir 4 hours, be cooled to after room temperature, centrifugation, adopt gc analysis reaction product liquid composition, result is: ethyl acetate is selectively 99%, and acetic acid conversion ratio is 85%.
EXPERIMENTAL EXAMPLE 7
Method according to EXPERIMENTAL EXAMPLE 1 is prepared ethyl acetate, different is, the block mesoporous material FDU(of the hexahedron called after FDU-HPA-JZ of the carried phospho-tungstic acid that carried phospho-tungstic acid catalyst (FDU-HPA) is made by dipping method by the embodiment 4 of identical weight) replace, result is: acetic acid conversion ratio is 82%, ethyl acetate be selectively 99%.
EXPERIMENTAL EXAMPLE 8
Method according to EXPERIMENTAL EXAMPLE 2 is prepared ethyl acetate, different is, the carried phospho-tungstic acid catalyst (FDU-HPA) of the EXPERIMENTAL EXAMPLE 1 reclaiming is by the block mesoporous material FDU(of the hexahedron called after FDU-HPA-JZ of EXPERIMENTAL EXAMPLE 7 carried phospho-tungstic acids of the recovery of identical weight) replace, result is: the conversion ratio of acetic acid is 83%, ethyl acetate be selectively 99%.
Experiment comparative example 1
Method according to EXPERIMENTAL EXAMPLE 1 is prepared ethyl acetate, different is, the rod-like mesoporous material SBA-15(called after SBA-15-HPA of the load phosphotungstic acid that carried phospho-tungstic acid catalyst (FDU-HPA) is made by the comparative example 1 of identical weight) replace, result is: acetic acid conversion ratio is 76%, ethyl acetate be selectively 81%.
Experiment comparative example 2
Method according to EXPERIMENTAL EXAMPLE 2 is prepared ethyl acetate, different is, the carried phospho-tungstic acid catalyst (FDU-HPA) of the EXPERIMENTAL EXAMPLE 1 reclaiming is by the rod-like mesoporous material SBA-15(called after SBA-15-HPA of the load phosphotungstic acid of the experiment comparative example 1 of the recovery of identical weight) replace, result is: acetic acid conversion ratio is 70%, ethyl acetate be selectively 80%.
By above embodiment 1-4 and comparative example 1 and EXPERIMENTAL EXAMPLE 1-8, the data of experiment comparative example 1-2 can be found out, EXPERIMENTAL EXAMPLE 1-8 is obviously than testing the effective of comparative example 1-2, and preferred EXPERIMENTAL EXAMPLE 1, EXPERIMENTAL EXAMPLE 2 is than EXPERIMENTAL EXAMPLE 3, EXPERIMENTAL EXAMPLE 4, EXPERIMENTAL EXAMPLE 5, EXPERIMENTAL EXAMPLE 6 effective, illustrate and adopt ball-milling method that phosphotungstic acid is carried on the block meso-porous titanium dioxide silicon carrier of hexahedron, the catalytic performance of the carried phospho-tungstic acid catalyst obtaining is better, when making to apply this catalyst and carrying out the esterification of catalysis acetic acid and ethanol, side reaction does not produce corrosion to equipment less simultaneously yet, and loaded catalyst of the present invention can pass through and reclaim and Reusability, aftertreatment technology is simple.
Claims (16)
1. a carried phospho-tungstic acid catalyst, it is characterized in that, this catalyst is comprised of the block meso-porous titanium dioxide silicon carrier of hexahedron and the phosphotungstic acid that loads on the block meso-porous titanium dioxide silicon carrier of described hexahedron, and the gross weight of described catalyst of take is benchmark, the content of described phosphotungstic acid is 10-90 % by weight, and the content of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 10-90 % by weight; The bottom surface length of side of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 2.5-5 micron, and height is 1-10 micron, and specific area is 500-700 meters squared per gram, and most probable aperture is 3-7 nanometer, and pore wall thickness is 6-7 nanometer.
2. carried phospho-tungstic acid catalyst according to claim 1, wherein, the gross weight of described catalyst of take is benchmark, and the content of described phosphotungstic acid is 30-60 % by weight, and the content of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 40-70 % by weight.
3. carried phospho-tungstic acid catalyst according to claim 1 and 2, wherein, the specific area of described carried phospho-tungstic acid catalyst is 20-50 meters squared per gram, and most probable aperture is 1-7 nanometer, and pore wall thickness is 4-10 nanometer.
4. according to the carried phospho-tungstic acid catalyst described in claim 1 or 3, wherein, the block meso-porous titanium dioxide silicon carrier of described hexahedron is made by the method comprising the following steps:
(1) template, potassium sulfate and mixed in hydrochloric acid to solids is fully dissolved;
(2) the standing 1-20 hour after 25-60 ℃ of temperature, mechanical agitation speed are to stir 5-60 minute under 100-400r/min by step (1) gained solution and esters of silicon acis;
(3) by step (2) products therefrom crystallization under crystallization condition;
(4) step (3) gained crystallization product is filtered, and will filter deionized water washing for gained solid, dry;
(5) by the dry products therefrom heating of step (4), removed template method;
Described template is polyethylene glycol oxide-PPOX-polyethylene glycol oxide.
5. carried phospho-tungstic acid catalyst according to claim 4, wherein, described esters of silicon acis is ethyl orthosilicate, and described crystallization condition comprises: temperature is 90-180 ℃, and the time is 10-40 hour; The condition of described removed template method comprises that temperature is 300-600 ℃, and the time is 8-20 hour.
6. according to the carried phospho-tungstic acid catalyst described in claim 4 or 5, wherein, count in molar ratio polyethylene glycol oxide-PPOX-polyethylene glycol oxide: potassium sulfate: water: hydrogen chloride: esters of silicon acis=1:100-800:10000-30000:10-9000:20-200.
7. the preparation method of a carried phospho-tungstic acid catalyst, wherein, the method comprises: by the block meso-porous titanium dioxide silicon carrier of hexahedron ball milling together with phosphotungstic acid, phosphotungstic acid is loaded on the block meso-porous titanium dioxide silicon carrier of described hexahedron, the gross weight of the block meso-porous titanium dioxide silicon carrier of the described hexahedron of take and phosphotungstic acid is benchmark, the consumption of described phosphotungstic acid is 10-90 % by weight, and the consumption of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 10-90 % by weight; The bottom surface length of side of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 2.5-5 micron, and height is 1-10 micron, and specific area is 500-700 meters squared per gram, and most probable aperture is 3-7 nanometer, and pore wall thickness is 6-7 nanometer.
8. preparation method according to claim 7, wherein, the gross weight of the block meso-porous titanium dioxide silicon carrier of the described hexahedron of take and phosphotungstic acid is benchmark, and the consumption of described phosphotungstic acid is 30-60 % by weight, and the consumption of the block meso-porous titanium dioxide silicon carrier of described hexahedron is 40-70 % by weight.
9. preparation method according to claim 7, wherein, the condition of described ball milling comprises: ball radius is 2-3mm, and rotating speed is 300-500r/min, and in ball grinder, temperature is 15-100 ℃, and the time is 0.1-100 hour.
10. preparation method according to claim 7, wherein, the block meso-porous titanium dioxide silicon carrier of described hexahedron is made by the method comprising the following steps:
(1) template, potassium sulfate and mixed in hydrochloric acid to solids is fully dissolved;
(2) the standing 1-20 hour after 25-60 ℃ of temperature, mechanical agitation speed are to stir 5-60 minute under 100-400r/min by step (1) gained solution and esters of silicon acis;
(3) by step (2) products therefrom crystallization under crystallization condition;
(4) step (3) gained crystallization product is filtered, and will filter deionized water washing for gained solid, dry;
(5) by the dry gained crystallization product heating of step (4), removed template method;
Described template is polyethylene glycol oxide-PPOX-polyethylene glycol oxide.
11. according to the described preparation method of claim 10, and wherein, described esters of silicon acis is ethyl orthosilicate, and described crystallization condition comprises: temperature is 90-180 ℃, and the time is 10-40 hour; The condition of described removed template method comprises that temperature is 300-600 ℃, and the time is 8-20 hour.
12. according to the preparation method described in claim 10 or 11, wherein, counts in molar ratio polyethylene glycol oxide-PPOX-polyethylene glycol oxide: potassium sulfate: water: hydrogen chloride: esters of silicon acis=1:100-800:10000-30000:10-9000:20-200.
The catalyst that preparation method in 13. claim 7-12 described in any one makes.
The application of catalyst in 14. claim 1-6 and 13 described in any one in esterification.
The preparation method of 15. 1 kinds of ethyl acetate, wherein, the method comprises: under the existence of catalyst, under the condition of esterification, acetic acid is contacted, to obtain ethyl acetate with ethanol, it is characterized in that, described catalyst is the catalyst described in any one in claim 1-6 and 13.
16. preparation methods according to claim 15, wherein, the mol ratio of acetic acid and ethanol is 1:0.5-10, and in the phosphotungstic acid of load in described catalyst, with respect to the acetic acid of 100 weight portions, the consumption of described catalyst is 0.5-50 weight portion.
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| CN108786800A (en) * | 2017-05-05 | 2018-11-13 | 中国石油化工股份有限公司 | The method of loaded catalyst and its preparation method and application and preparing propylene by dehydrogenating propane |
| CN110496618A (en) * | 2018-05-17 | 2019-11-26 | 中国石油化工股份有限公司 | The method of dehydrogenation of isobutane catalyst and preparation method thereof and preparing isobutene through dehydrogenation of iso-butane |
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| CN106622377A (en) * | 2015-11-04 | 2017-05-10 | 中国石油化工股份有限公司 | Spherical aluminum-containing mesoporous composite, supported catalyst, and preparation method of spherical aluminum-containing mesoporous composite, preparation method of supported catalyst, application of supported catalyst, and preparation method of ethyl acetate |
| CN106622377B (en) * | 2015-11-04 | 2019-06-28 | 中国石油化工股份有限公司 | It is a kind of spherical shape mesoporous composite material containing aluminium and loaded catalyst and its preparation method and application and ethyl acetate preparation method |
| CN108786800A (en) * | 2017-05-05 | 2018-11-13 | 中国石油化工股份有限公司 | The method of loaded catalyst and its preparation method and application and preparing propylene by dehydrogenating propane |
| CN108786800B (en) * | 2017-05-05 | 2020-07-21 | 中国石油化工股份有限公司 | Supported catalyst, preparation method and application thereof, and method for preparing propylene by propane dehydrogenation |
| CN110496618A (en) * | 2018-05-17 | 2019-11-26 | 中国石油化工股份有限公司 | The method of dehydrogenation of isobutane catalyst and preparation method thereof and preparing isobutene through dehydrogenation of iso-butane |
| CN110496618B (en) * | 2018-05-17 | 2021-11-19 | 中国石油化工股份有限公司 | Isobutane dehydrogenation catalyst, preparation method thereof and method for preparing isobutene through isobutane dehydrogenation |
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