CN109647395B - Catalyst for dehydrogenation of isobutane - Google Patents

Catalyst for dehydrogenation of isobutane Download PDF

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CN109647395B
CN109647395B CN201710946328.6A CN201710946328A CN109647395B CN 109647395 B CN109647395 B CN 109647395B CN 201710946328 A CN201710946328 A CN 201710946328A CN 109647395 B CN109647395 B CN 109647395B
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catalyst
carrier
isobutane
drying
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CN109647395A (en
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姜冬宇
缪长喜
吴文海
樊志贵
曾铁强
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China Petroleum and Chemical Corp
Sinopec Shanghai Research Institute of Petrochemical Technology
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Sinopec Shanghai Research Institute of Petrochemical Technology
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Abstract

The invention relates to a catalyst for isobutane dehydrogenation, which mainly solves the problem of low activity of dehydrogenation catalysts prepared in the prior art. The invention adopts a composite catalyst, which comprises the following components in parts by weight: a) 0.1-5 parts of Pt or its oxide; b)0.1 to 5 parts of Sn or an oxide thereof; c) 90-99 parts of a composite oxide M1-M2-Al-O carrier, wherein M1 is selected from a mixture of elements IIA and VB, and M2 is selected from at least one of lanthanide elements, so that the problem can be well solved, and the method can be used for industrial production of isobutene prepared by isobutane dehydrogenation.

Description

Catalyst for dehydrogenation of isobutane
Technical Field
The invention relates to a catalyst for isobutane dehydrogenation.
Background
Isobutene is generally used as a by-product in refineries and chemical plants. Although MGG and catalytic cracking processes for producing isobutene in a high yield are developed and popularized, the amount of byproducts propylene and isobutene generated from oil refineries and chemical plants cannot meet the market demand, especially MTBE (methyl tert-butyl ether) produced by isobutene etherification as a low-pollution and high-octane gasoline additive becomes a large chemical product which is developed fastest in the world, and the demand for isobutene is increased day by day. Therefore, the process for producing isobutene by utilizing isobutane dehydrogenation is favored in areas with abundant propane and isobutane resources. Commercial dehydrogenation processes in the world are the STAR process from Philips oil, the Catofin process from combined catalysis and rum, the Oleflex process from UOP, and the Snamprogetti fluid bed dehydrogenation process developed by Russian-Laval research institute in conjunction with the engineering of Snamprogetti, Italy. The STAR and Catofin processes employ fixed bed batch regeneration reaction systems; the Oleflex process adopts a moving bed continuous regeneration type reaction system; and the Snamprogetti process adopts a fluidized bed reaction regeneration system. In addition, there are alkane dehydrogenation technologies developed in conjunction with Linde and BASF.
Because of the limitation of thermodynamic factors, isobutane dehydrogenation catalytic reaction is carried out at high temperature, the carbon deposition and inactivation of the catalyst are serious, and the development of a catalyst with high activity, high selectivity and high stability becomes the key of the technology. Catalysts which take platinum as a main active component and are reported by Chinese patent (CN96117222.3) and U.S. patent (US4438288) and catalysts which take chromium as a main active component and are disclosed by Chinese patent (CN200910012450.1, CN200610126812.6) are two important catalysts for direct dehydrogenation catalytic reaction of low-carbon alkane. The direct dehydrogenation process of the low-carbon alkane has already realized industrial application, wherein the Pt catalyst becomes a research hotspot due to the characteristics of high activity, low pollution, low wear rate and the like. The catalyst K-Ce-Pt-Sn/gamma-Al disclosed in the Chinese patent (CN200910209534.4)2O3After 6h of reaction, the conversion of propane was 38%, the selectivity of propylene was 98% and the amount of coke formation was small, and this study did not provide stability data. "Effect of variable loading in general oxidative dehydrogenation on V, published by Puglisi et al in Catalysis Letters 1996,41:41-432O5/SiO2catalyts' V load pair V2O5/SiO2Influence of the catalyst on the dehydrogenation performance of propane by oxidative dehydrogenation) the influence of the addition amount of V on V was investigated2O5/SiO2Influence of oxidative dehydrogenation Properties of propane, the results show that V2O5In an amount of 5% to 10%, propylene selectivity is highest and the catalyst exhibits good dehydrogenation performance.
Isobutane dehydrogenation catalysts have made great progress so far, but there is room for improvement in catalyst activity. The invention adopts M1-M2-Al-O as the carrier to load the Pt-Sn catalyst, improves the performance of the catalyst, has better application prospect, and has no related report at present.
Disclosure of Invention
One of the technical problems to be solved by the invention is that the activity of the isobutane dehydrogenation catalyst in the prior art is low, and the catalyst for preparing isobutene by isobutane dehydrogenation is high in activity. The second technical problem to be solved by the present invention is to provide a method for preparing a catalyst corresponding to the first technical problem.
In order to solve one of the above technical problems, the technical scheme adopted by the invention is as follows: a catalyst for preparing isobutene by isobutane dehydrogenation comprises the following components in parts by weight:
a) 0.1-5 parts of Pt or its oxide;
b)0.1 to 5 parts of Sn or an oxide thereof;
c) 90-99 parts of a composite oxide M1-M2-Al-O carrier, wherein M1 is selected from a mixture of elements IIA and VB, and M2 is selected from at least one of lanthanide.
In the technical scheme, the catalyst for isobutane dehydrogenation is characterized in that the catalyst is prepared from 0.1-2.0 parts of Pt or oxides thereof and 0.1-2.0 parts of Sn or oxides thereof by weight of a low-carbon alkane catalyst;
in the above technical solution, the preferable technical solution is that the element VB in M1 in the composite oxide M1-M2-Al-O carrier is selected from V or Nb, and the preferable technical solution is V.
In the technical scheme, the IIA element in M1 in the composite oxide M1-M2-Al-O carrier is selected from at least one of Be, Mg, Ca, Sr and Ba.
Preferably, the IIA element in M1 in the carrier is selected from at least one of Mg, Ca and Sr.
More preferably, the IIA element in M1 in the carrier is selected from Mg and Ca.
In the technical scheme, the preferable technical scheme is that the composite oxide M1-M2-Al-O carrier, M1 is selected from V, Mg and Ca in IIA and VB elements.
M2 in the composite oxide M1-M2-Al-O carrier is selected from at least one of La or Ce.
The preferable technical scheme is that M2 in the composite oxide M1-M2-Al-O carrier is selected from La and Ce.
In the technical scheme, IIA and VB elements selected by M1 in the composite oxide M1-M2-Al-O carrier and lanthanide elements of M2 are used together, so that a synergistic effect is achieved on isobutene selectivity.
In the technical scheme, in the composite oxide M1-M2-Al-O carrier, the molar ratio of Al to M1 is (1-1.99): 1, preferably (1.5-1.8): 1, the molar ratio of IIA to VB in M1 is (0.25-4); m2 is (1-199): 1, preferably (3-19): 1.
to solve the second technical problem, the invention adopts the following technical scheme: a catalyst for isobutane dehydrogenation and a preparation method thereof comprise the following steps:
a) weighing soluble salts of M1, M2 and Al with required contents, dissolving the soluble salts in a proper amount of deionized water, uniformly mixing, slowly dripping ammonia water under continuous stirring, and adjusting the pH value to 7-10; aging, filtering, drying and roasting the product to obtain an M1-M2-Al-O carrier;
b) dissolving a required amount of soluble salt of Sn in a proper amount of hydrochloric acid solution, adding the soluble salt into the carrier obtained in the step a under stirring, uniformly mixing, carrying out ultrasonic-assisted impregnation, drying and roasting to obtain a catalyst precursor I;
c) dissolving a required amount of soluble Pt salt in a proper amount of water, adding the catalyst precursor I obtained in the step b under stirring, uniformly mixing, ultrasonically assisting for impregnation, drying, and roasting to obtain the isobutane dehydrogenation catalyst.
In the technical scheme, the dipping temperature in the dipping process is 10-80 ℃, the dipping time is 1-24 hours, the drying temperature is 80-150 ℃, the drying time is 6-24 hours, the roasting temperature is 450-650 ℃, and the roasting time is 6-24 hours. The soluble salt of M1, M2 or the oxide thereof can be one of chloride, nitrate or acetate; the soluble salt of Pt is preferably chloroplatinic acid; the soluble salt of tin is selected from stannous chloride or stannic chloride.
The catalyst prepared by the method is subjected to activity evaluation in an isothermal fixed bed reactor, and for the evaluation of a system for preparing low-carbon olefin by dehydrogenating isobutane, the process is briefly described as follows:
adjusting the flow rate of isobutane through a mass flowmeter, mixing in a preheating zone, then entering a reaction zone,the preheating zone and the reaction zone of the reactor are heated by electric heating wires to reach a preset temperature, and the inside diameter of the reactor is a stainless steel sleeve with phi 9 mm-phi 6mm and the length is about 400 mm. The reacted gas was passed through a condensing pot and then analyzed for composition by gas chromatography. The catalyst evaluation conditions in the isothermal fixed bed reactor were as follows: filling about 0.5 g of catalyst into an isothermal reactor with the inner diameter of phi 9mm to phi 6mm (the height of a catalyst bed layer is about 17mm), wherein the volume ratio of water vapor to isobutane is (10-1): 1, the reaction temperature is 400-600 ℃, the reaction pressure is 0-1 MPa, and the mass space velocity of alkane is 3.0-8.0 h-1And the reaction raw material is in contact reaction with the catalyst to obtain isobutene.
In the case of isobutane dehydrogenation catalysts, many side reactions also occur at the acid centers on the surface of the carrier, such as cracking and isomerization of alkanes, cracking, isomerization and polymerization of olefins, and the like, and a single Al2O3Is not favorable for the selectivity and stability of the catalytic reaction.
The method provided by the invention selects a composite oxide M1-M2-Al-O as a carrier, M1 is selected from a mixture of IIA and VB elements, and M2 is selected from at least one of lanthanide series elements. The prepared catalyst is used for isobutane dehydrogenation reaction, the initial conversion rate of isobutane reaches more than 54%, and the selectivity of isobutane is higher than 96%; and a better technical effect is achieved.
The invention is further illustrated by the following examples.
Detailed Description
[ example 1 ]
Weighing 39.97g of beryllium chloride, 78.65g of vanadium chloride, 98.10g of lanthanum chloride and 213.33g of aluminum chloride soluble salt, dissolving in 1L of deionized water, uniformly mixing, slowly dripping ammonia water under continuous stirring, adjusting the pH value to 8.0, aging the product for 2 hours, carrying out suction filtration and washing with 4L of water to obtain a filter cake, drying the filter cake at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the Be0.5V0.5La0.4Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, placing in a beaker, then weighing 0.295g of stannic chloride, dissolving in 10mL of hydrochloric acid solution, adding the carrier under stirring, mixing well, 30 DEG CThe catalyst precursor was obtained by immersion for 12 hours and then dried at 90 ℃ for 16 hours, and is noted as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were as follows: 0.5 g of catalyst is loaded into the isothermal fixed bed reactor (the height of a catalyst bed layer is 17mm), the reaction is carried out under normal pressure and at the temperature of 550 ℃; the volume ratio of water vapor to isobutane was 2: 1; the mass space velocity of isobutane is 4.0h-1. The results are shown in Table 1.
[ example 2 ]
Weighing 128.2g of magnesium nitrate, 78.65g of vanadium chloride, 129.96g of lanthanum nitrate and 600.20g of aluminum nitrate soluble salt, dissolving in 1L of deionized water, uniformly mixing, slowly dripping ammonia water under continuous stirring, adjusting the pH value to 8.0, aging the product for 2 hours, carrying out suction filtration and washing with 4L of water to obtain a filter cake, drying the filter cake at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain Mg0.5V0.5La0.4Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 3 ]
88.09g of calcium acetate, 78.65g of vanadium chloride, 126.42g of lanthanum acetate and 276.39g of basic aluminum acetate soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped under continuous stirring, the pH value is adjusted to 8.0, the product is aged for 2 hours, 4L of water is used for filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃, and then is roasted for 20 hours in a 600 ℃ muffle furnace to obtain Ca0.5V0.5La0.4Al1.6OxAnd (3) a carrier. Weighing machinePutting 9.85g of carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, dipping for 12 hours at 30 ℃, and then drying for 16 hours at 90 ℃ to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 4 ]
107.36g of strontium acetate, 78.65g of vanadium chloride, 126.42g of lanthanum acetate and 276.39g of basic aluminum acetate soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped under continuous stirring, the pH value is adjusted to 8.0, the product is aged for 2 hours, 4L of water is used for filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃, and then is roasted for 20 hours in a 600 ℃ muffle furnace to obtain Sr0.5V0.5La0.4Al1.6An Ox carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 5 ]
122.13g of barium chloride, 78.65g of vanadium chloride, 98.10g of lanthanum chloride and 213.33g of aluminum chloride soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped under continuous stirring, the pH value is adjusted to 8.0, the product is aged for 2 hours, 4L of water is used for filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃, and then is roasted for 20 hours in a 600 ℃ muffle furnace to obtain Ba0.5V0.5La0.4Al1.6OXAnd (3) a carrier. 9.85g of the carrier was weighed into a beaker, and then 0.190g of stannous chloride was weighed to dissolve inAdding the carrier into 10mL hydrochloric acid solution while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 6 ]
51.28g of magnesium nitrate, 125.84g of vanadium chloride, 129.96g of lanthanum nitrate and 600.20g of aluminum nitrate soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped under continuous stirring, the pH value is adjusted to 8.0, a product is aged for 2 hours, 4L of water is used for suction filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃, and then is roasted for 20 hours in a 600 ℃ muffle furnace to obtain Mg0.2V0.8La0.4Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 7 ]
205.13g of magnesium nitrate, 31.46g of vanadium chloride, 129.96g of lanthanum nitrate and 600.20g of aluminum nitrate soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped under continuous stirring, the pH value is adjusted to 8.0, the product is aged for 2 hours, 4L of water is used for filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃, and then is roasted for 20 hours in a 600 ℃ muffle furnace to obtain Mg0.8V0.2La0.4Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, placing the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride into 10mL of hydrochloric acid solution, adding the carrier under stirring, and mixingMixing evenly, dipping for 12 hours at 30 ℃, and then drying for 16 hours at 90 ℃ to obtain the catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 8 ]
Weighing 66.6g of beryllium nitrate, 135.09g of niobium chloride, 129.96g of lanthanum nitrate and 600.20g of aluminum nitrate soluble salt, dissolving in 1L of deionized water, uniformly mixing, slowly dripping ammonia water under continuous stirring, adjusting the pH value to 8.0, aging the product for 2 hours, carrying out suction filtration and washing with 4L of water to obtain a filter cake, drying the filter cake at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the Be0.5Nb0.5La0.4Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 9 ]
128.21g of magnesium nitrate, 135.09g of niobium chloride, 129.96g of lanthanum nitrate and 600.20g of aluminum nitrate soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped under continuous stirring, the pH value is adjusted to 8.0, the product is aged for 2 hours, 4L of water is used for filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃, and then is roasted for 20 hours in a 600 ℃ muffle furnace to obtain Mg0.5Nb0.5La0.4Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hoursThe catalyst precursor is obtained in hours and is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 10 ]
118.08g of calcium nitrate, 135.09g of niobium chloride, 129.96g of lanthanum nitrate and 600.20g of aluminum nitrate soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped under continuous stirring, the pH value is adjusted to 8.0, the product is aged for 2 hours, 4L of water is used for filtration and washing to obtain a filter cake, the filter cake is dried at 90 ℃ for 16 hours and then roasted in a 600 ℃ muffle furnace for 20 hours to obtain Ca0.5Nb0.5La0.4Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 11 ]
105.82g of strontium nitrate, 135.09g of niobium chloride, 129.96g of lanthanum nitrate and 600.20g of aluminum nitrate soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped under continuous stirring, the pH value is adjusted to 8.0, the product is aged for 2 hours, 4L of water is used for filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃, and then is roasted for 20 hours in a 600 ℃ muffle furnace to obtain Sr0.5Nb0.5La0.4Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weigh 0.133gDissolving chloroplatinic acid in 10mL of water, adding the chloroplatinic acid into the catalyst I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 12 ]
130.67g of barium nitrate, 135.09g of niobium chloride, 129.96g of lanthanum nitrate and 600.20g of aluminum nitrate soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped under continuous stirring, the pH value is adjusted to 8.0, the product is aged for 2 hours, 4L of water is used for filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃, and then is roasted for 20 hours in a 600 ℃ muffle furnace to obtain Ba0.5Nb0.5La0.4Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 13 ]
Weighing 128.2g of magnesium nitrate, 78.65g of vanadium chloride, 219.30g of ceric ammonium nitrate and 600.20g of aluminum nitrate soluble salt, dissolving in 1L of deionized water, uniformly mixing, slowly dripping ammonia water under continuous stirring, adjusting the pH value to 8.0, aging the product for 2 hours, carrying out suction filtration and washing with 4L of water to obtain a filter cake, drying the filter cake at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain Mg0.5V0.5Ce0.4Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. 0.133g of chloroplatinic acid was weighed into 10mL of water, added to I with stirring,uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 14 ]
Weighing 128.2g of magnesium nitrate, 78.65g of vanadium chloride, 64.98g of lanthanum nitrate, 109.64g of ceric ammonium nitrate and 600.20g of aluminum nitrate soluble salt, dissolving in 1L of deionized water, uniformly mixing, slowly dripping ammonia water under continuous stirring, adjusting the pH value to 8.0, aging the product for 2 hours, carrying out suction filtration and washing by using 4L of water to obtain a filter cake, drying the filter cake for 16 hours at 90 ℃, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain Mg0.5V0.5La0.1Ce0.4Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 15 ]
Weighing 128.2g of magnesium nitrate, 78.65g of vanadium chloride, 162.46g of lanthanum nitrate and 562.70g of aluminum nitrate soluble salt, dissolving in 1L of deionized water, uniformly mixing, slowly dripping ammonia water under continuous stirring, adjusting the pH value to 8.0, aging the product for 2 hours, carrying out suction filtration and washing with 4L of water to obtain a filter cake, drying the filter cake at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain Mg0.5V0.5La0.5Al1.5OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid in 10mL of water, adding to I with stirring, mixing well at 30 deg.CDipping for 12 hours, drying for 16 hours at 90 ℃, and roasting for 20 hours in a muffle furnace at 600 ℃ to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 16 ]
Weighing 128.2g of magnesium nitrate, 78.65g of vanadium chloride, 32.49g of lanthanum nitrate and 675.23g of aluminum nitrate soluble salt, dissolving in 1L of deionized water, uniformly mixing, slowly dripping ammonia water under continuous stirring, adjusting the pH value to 8.0, aging the product for 2 hours, carrying out suction filtration and washing with 4L of water to obtain a filter cake, drying the filter cake at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain Mg0.5V0.5La0.2Al1.8OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1. [ example 17 ]
64.10g of magnesium nitrate, 59.04g of calcium nitrate, 78.65g of vanadium chloride, 129.96g of lanthanum nitrate and 600.20g of aluminum nitrate soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped under continuous stirring, the pH value is adjusted to 8.0, a product is aged for 2 hours, 4L of water is used for suction filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃, and then is roasted for 20 hours in a 600 ℃ muffle furnace to obtain Mg0.25Ca0.25V0.5La0.4Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding to I under stirring, mixing well, immersing at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and heating at 600 ℃ in a muffle furnaceAnd roasting for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 18 ]
64.10g of magnesium nitrate, 59.04g of calcium nitrate, 135.09g of niobium chloride, 129.96g of lanthanum nitrate and 600.20g of aluminum nitrate soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped under continuous stirring, the pH value is adjusted to 8.0, a product is aged for 2 hours, 4L of water is used for suction filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃, and then is roasted for 20 hours in a 600 ℃ muffle furnace to obtain Mg0.25Ca0.25Nb0.5La0.4Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 19 ]
64.10g of magnesium nitrate, 59.04g of calcium nitrate, 78.65g of vanadium chloride, 64.98g of lanthanum nitrate, 109.64g of ceric ammonium nitrate and 600.20g of aluminum nitrate soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped in under continuous stirring, the pH value is adjusted to 8.0, the product is aged for 2 hours, 4L of water is used for suction filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃ and then is roasted for 20 hours in a 600 ℃ muffle furnace, and Mg is obtained0.25Ca0.25V0.5Ce0.2La0.2Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into I under stirring, mixing uniformly,dipping for 12 hours at 30 ℃, drying for 16 hours at 90 ℃, and roasting for 20 hours in a muffle furnace at 600 ℃ to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 20 ]
Weighing 25.64g of magnesium nitrate, 23.61g of calcium nitrate, 125.84g of vanadium chloride, 64.98g of lanthanum nitrate, 109.64g of ceric ammonium nitrate and 600.20g of aluminum nitrate soluble salt, dissolving in 1L of deionized water, uniformly mixing, slowly dripping ammonia water under continuous stirring, adjusting the pH value to 8.0, aging the product for 2 hours, carrying out suction filtration and washing by using 4L of water to obtain a filter cake, drying the filter cake at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain Mg0.1Ca0.1V0.8Ce0.2La0.2Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
[ example 21 ]
102.56g of magnesium nitrate, 94.46g of calcium nitrate, 31.46g of vanadium chloride, 64.98g of lanthanum nitrate, 109.64g of ceric ammonium nitrate and 600.20g of aluminum nitrate soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped under continuous stirring, the pH value is adjusted to 8.0, the product is aged for 2 hours, 4L of water is used for suction filtration and washing to obtain a filter cake, the filter cake is dried at 90 ℃ for 16 hours and then is roasted in a 600 ℃ muffle furnace for 20 hours, and Mg is obtained0.4Ca0.4V0.2Ce0.2La0.2Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain the catalystAgent precursor, noted as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
Comparative example 1
129.96g of lanthanum nitrate and 600.20g of aluminum nitrate soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped in the mixture under continuous stirring, the pH value is adjusted to be 8.0, the product is aged for 2 hours, 4L of water is used for suction filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃, and then is roasted for 20 hours in a 600 ℃ muffle furnace to obtain La0.4Al1.6O3And (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
Comparative example 2
Weighing 128.2g of magnesium nitrate, 78.65g of vanadium chloride and 750.26g of aluminum nitrate soluble salt, dissolving in 1L of deionized water, uniformly mixing, slowly dripping ammonia water under continuous stirring, adjusting the pH value to 8.0, aging the product for 2 hours, leaching and washing with 4L of water to obtain a filter cake, drying the filter cake at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain Mg0.5V0.5Al2OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding to I while stirring, mixing well, immersing at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, baking in a 600 ℃ muffle furnaceBurning for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
Comparative example 3
256.41g of magnesium nitrate, 32.49g of lanthanum nitrate, 54.82g of ceric ammonium nitrate and 600.20g of aluminum nitrate soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped under continuous stirring, the pH value is adjusted to 8.0, the product is aged for 2 hours, 4L of water is used for suction filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃, and then is roasted for 20 hours in a 600 ℃ muffle furnace to obtain MgLa0.1Ce0.1Al1.8OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
Comparative example 4
157.3g of vanadium chloride, 64.98g of lanthanum nitrate, 109.64g of ceric ammonium nitrate and 600.20g of aluminum nitrate soluble salt are weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped under continuous stirring, the pH value is adjusted to 8.0, the product is aged for 2 hours, 4L of water is used for filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃, and then is roasted for 20 hours in a 600 ℃ muffle furnace to obtain VLa0.2Ce0.2Al1.6OxAnd (3) a carrier. Weighing 9.85g of carrier, putting the carrier into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier under stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, and then drying at 90 ℃ for 16 hours to obtain a catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. Catalyst evaluation conditions were carried out in the same manner asExample 1. The results are shown in Table 1. Comparative example 5
600.20g of aluminum nitrate soluble salt is weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped in under the condition of continuous stirring, the pH value is adjusted to 8.0, the product is aged for 2 hours, 4L of water is used for suction filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃, and then is roasted for 20 hours in a 600 ℃ muffle furnace to obtain a carrier Al2O3. Soaking in 500ml mixed solution containing 256.41 magnesium nitrate and 129.96g lanthanum nitrate at 30 deg.C for 12 hr, drying at 90 deg.C for 16 hr, and calcining at 600 deg.C in muffle furnace for 20 hr to obtain MgLa0.4Ox/Al1.6OxWeighing 9.85g of the catalyst precursor, putting the weighed mass into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier into the solution under stirring, uniformly mixing the mixture, soaking the mixture for 12 hours at 30 ℃, and then drying the mixture for 16 hours at 90 ℃ to obtain the catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
Comparative example 6
600.20g of aluminum nitrate soluble salt is weighed and dissolved in 1L of deionized water, the mixture is uniformly mixed, ammonia water is slowly dripped in under the condition of continuous stirring, the pH value is adjusted to 8.0, the product is aged for 2 hours, 4L of water is used for suction filtration and washing to obtain a filter cake, the filter cake is dried for 16 hours at 90 ℃, and then is roasted for 20 hours in a 600 ℃ muffle furnace to obtain a carrier Al2O3. Pouring the mixture into 500ml mixed solution containing 128.2g of magnesium nitrate, 78.65g of vanadium chloride, 64.98g of lanthanum nitrate and 109.64g of ceric ammonium nitrate, soaking the mixture for 12 hours at 30 ℃, then drying the mixture for 16 hours at 90 ℃, and roasting the dried mixture for 20 hours in a 600 ℃ muffle furnace to obtain Mg0.5V0.5La0.2Ce0.2Ox/Al1.6OxWeighing 9.85g of the carrier, putting the carrier into a beaker, weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier into the hydrochloric acid solution under stirring, uniformly mixing, soaking the carrier at 30 ℃ for 12 hours, and drying the carrier at 90 ℃ for 16 hoursThe catalyst precursor is obtained, and is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
Comparative example 7
Weighing 600.20g of aluminum nitrate soluble salt, dissolving in 1L of deionized water, uniformly mixing, slowly dripping ammonia water under continuous stirring, adjusting the pH value to 8.0, aging the product for 2 hours, carrying out suction filtration washing by using 4L of water to obtain a filter cake, drying the filter cake at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain a carrier Al2O3. Soaking in 500ml mixed solution containing 157.3g vanadium chloride and 129.96g lanthanum nitrate at 30 deg.C for 12 hr, drying at 90 deg.C for 16 hr, and calcining at 600 deg.C in muffle furnace for 20 hr to obtain VLa0.4Ox/Al1.6OxWeighing 9.85g of the catalyst precursor, putting the weighed mass into a beaker, then weighing 0.190g of stannous chloride, dissolving the stannous chloride in 10mL of hydrochloric acid solution, adding the carrier into the solution under stirring, uniformly mixing the mixture, soaking the mixture for 12 hours at 30 ℃, and then drying the mixture for 16 hours at 90 ℃ to obtain the catalyst precursor, which is marked as I. Weighing 0.133g of chloroplatinic acid, dissolving in 10mL of water, adding into the I while stirring, uniformly mixing, soaking at 30 ℃ for 12 hours, drying at 90 ℃ for 16 hours, and roasting in a 600 ℃ muffle furnace for 20 hours to obtain the isobutane dehydrogenation catalyst. The catalyst evaluation conditions were the same as in example 1. The results are shown in Table 1.
The catalyst composition for preparing isobutene by isobutane dehydrogenation is fixed as Pt: 0.5 part, Sn: 1.0 part, and the balance of carrier 98.5 parts. The above example and comparative supports were prepared in 1mol numbers and the composition and mole fraction of the support and the corresponding catalyst performance are listed in table 1.
TABLE 1
Figure BDA0001431783120000151
Figure BDA0001431783120000161
Figure BDA0001431783120000171

Claims (7)

1. The catalyst for isobutane dehydrogenation comprises the following components in parts by weight:
a) 0.1-5 parts of Pt or its oxide;
b)0.1 to 5 parts of Sn or an oxide thereof;
c) 90-99 parts of a composite oxide M1-M2-Al-O carrier, wherein M1 is selected from a mixture of at least one of IIA group elements and at least one of VB group elements, and M2 is selected from at least one of lanthanide;
wherein VB elements in M1 in the composite oxide M1-M2-Al-O carrier are selected from V or Nb;
m1 is (1-1.99): 1, the molar ratio of IIA to VB in M1 is (0.25-4); m2 is (1-199): 1.
2. the catalyst for dehydrogenating isobutane according to claim 1, wherein the part of Pt or an oxide thereof is 0.1-2.0 parts, and the part of Sn or an oxide thereof is 0.1-2.0 parts, based on the weight of the catalyst for dehydrogenating isobutane to prepare isobutene.
3. Catalyst for the dehydrogenation of isobutane according to claim 1, characterized in that the IIA element in M1 of the complex oxide M1-M2-Al-O support is selected from at least one of Be, Mg, Ca, Sr, Ba.
4. Catalyst for the dehydrogenation of isobutane according to claim 1, characterized in that M2 is selected from at least one of La or Ce in the complex oxide M1-M2-Al-O support.
5. A method for preparing the catalyst for isobutane dehydrogenation according to any one of claims 1 to 4, comprising the following steps:
a) weighing soluble salts of M1, M2 and Al with required contents, dissolving the soluble salts in a proper amount of deionized water, uniformly mixing, slowly dripping ammonia water under continuous stirring, and adjusting the pH value to 7-10; aging, filtering, drying and roasting the product to obtain an M1-M2-Al-O carrier;
b) dissolving a required amount of soluble salt of Sn in a proper amount of hydrochloric acid solution, adding the soluble salt into the carrier obtained in the step a under stirring, uniformly mixing, carrying out ultrasonic-assisted impregnation, drying and roasting to obtain a catalyst precursor I;
c) dissolving a required amount of soluble Pt salt in a proper amount of water, adding the catalyst precursor I obtained in the step b under stirring, uniformly mixing, ultrasonically assisting for impregnation, drying, and roasting to obtain the isobutane dehydrogenation catalyst.
6. The method for preparing a catalyst for dehydrogenation of isobutane according to claim 5, wherein the impregnation temperature in step b) and step c) is 10 to 80 ℃, the impregnation time is 1 to 24 hours, the drying temperature is 80 ℃ to 150 ℃, the drying time is 6 to 24 hours, the calcination temperature is 450 ℃ to 650 ℃, and the calcination time is 6 to 24 hours.
7. The catalyst of any one of claims 1 to 4 or the catalyst prepared by the method of claim 5 or 6 is used for dehydrogenation of isobutane, the reaction raw material is isobutane, and the reaction conditions are as follows: the volume ratio of the water vapor to the isobutane is (10-1): 1, the reaction temperature is 400-600 ℃, the reaction pressure is 0-1 MPa, and the mass space velocity of the alkane is 3.0-8.0 h-1And the reaction raw material is in contact reaction with the catalyst to obtain isobutene.
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