CN110590539A - Method for producing acrylic acid - Google Patents
Method for producing acrylic acid Download PDFInfo
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- CN110590539A CN110590539A CN201810598810.XA CN201810598810A CN110590539A CN 110590539 A CN110590539 A CN 110590539A CN 201810598810 A CN201810598810 A CN 201810598810A CN 110590539 A CN110590539 A CN 110590539A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/31—Chromium, molybdenum or tungsten combined with bismuth
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/32—Manganese, technetium or rhenium
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/32—Manganese, technetium or rhenium
- B01J23/34—Manganese
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/32—Manganese, technetium or rhenium
- B01J23/36—Rhenium
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/25—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring
- C07C51/252—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring of propene, butenes, acrolein or methacrolein
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
Abstract
The invention relates to a method for producing acrylic acid, mainly solve the problem that the acrolein conversion rate is low and acrylic acid yield is low of the existing catalyst, through adopting the production method of acrylic acid, including under the existence of catalyst, acrolein reacts with oxidizing gas containing oxygen to get acrylic acid; the catalyst comprises a carrier and an active component loaded on the carrier, wherein the active component is represented by the general formula: VMoaBibWcXdYeZfOgWherein X is selected fromThe technical scheme is that the acrylic acid-base composite material comprises one or more of Sc, Ti, Y, Zr, Hf, Ta and Cr, wherein Y comprises at least one of Ga, Ge, In, Sn, TI, Pb, Cd, Mn, Tc, Re, Rh, Ir, Pd, Pt, Ag, Au and La, and Z is one or more of alkali metals or alkaline earth metals.
Description
Technical Field
The present invention relates to a process for producing acrylic acid.
Background
Acrolein is the simplest unsaturated aldehyde, is an important chemical synthesis intermediate, and is widely used for synthesis of important chemical products such as picoline, pyridine, glutaraldehyde, acrylic acid and the like. Acrylic acid is an important organic chemical raw material, is mainly used for manufacturing multifunctional high polymer materials such as acrylates, and is widely applied to the fields of papermaking, leather, coating, textile, plastics, rubber, oil additives, petroleum exploitation and the like. In recent years, the market demand for acrylic acid has increased worldwide, and the production of acrylic acid has been a focus of research.
The synthesis of acrylic acid by the acrolein oxidation process is currently used on a large industrial scale. The catalyst used for synthesizing acrylic acid by acrolein oxidation method is generally Mo-V series oxide, the basic elements of the catalyst are Mo and V, and other elements used for improving the performance of the catalyst, such as Nb, Sn, Cr, W, Fe, Co, Ni, Sb and the like, are added. US Pat7220698B2 describes the introduction of a trace amount of a catalyst poison into the catalyst preparation process to inhibit thermal degradation of the catalyst and provide stability to the catalyst. US Pat7456129B2 describes varying acid content, controlling acid strength, and improving catalyst performance during catalyst support preparation. CN 16997701 and CN1210511 propose a preparation method of a composite oxide catalyst, which is to Co-precipitate mixed liquor of various element components (containing Fe, Co, Mo, V, Bi, Ni, etc.), dry into powder, perform tabletting, extrusion molding, and finally bake to obtain the composite oxide catalyst. The acrylic acid catalyst can be successfully prepared by the methods and the performance of the catalyst is improved, but the catalyst has poor mechanical strength and low catalytic activity ratio, so that the practical application is limited.
The active components of the catalyst are loaded on the carrier with large specific surface area, so that the mechanical strength of the catalyst can be increased, the loading capacity of the active components is greatly increased, and the active components of the catalyst are exerted to a great extent through a synergistic effect. CN1130172 (preparation method of acrylic acid) describes a preparation method of a spherical catalyst, in which a carrier is added into an active component mixed solution, and is evaporated and dried, so that the active component is deposited on the surface of the carrier. However, the catalytic activity, selectivity and yield of the acrylic acid catalyst obtained in the prior art need to be further improved.
Disclosure of Invention
The invention aims to solve the technical problems of low acrolein conversion rate and low acrylic acid yield of the existing catalyst, and provides a novel acrylic acid production method.
In order to solve the technical problems, the technical scheme of the invention is as follows:
a process for producing acrylic acid, comprising reacting acrolein with an oxygen-containing oxidizing gas in the presence of a catalyst to obtain acrylic acid; the catalyst comprises a carrier and an active component loaded on the carrier, wherein the active component is represented by the general formula: VMoaBibWcXdYeZfOgWherein X is selected from one or more of Sc, Ti, Y, Zr, Hf, Ta and Cr, Y is selected from at least one of Ga, Ge, In, Sn, TI, Pb, Cd, Mn, Tc, Re, Rh, Ir, Pd, Pt, Ag, Au and La, and Z is selected from one or more of alkali metal or alkaline earth metal; a is the molar ratio of Mo to V, and the value of a is 2.0-8.0; b is the molar ratio of Bi to V, and the value of b is 0.2-0.8; c is the molar ratio of W to V, and the value of c is 0.2-1.0; d is the molar ratio of X to V, and the value of d is 0.2-1.0; e is the molar ratio of Y to V, and the value of e is 0.05-1.2; f is the molar ratio of Z to V, and the value of f is 0.05-1.2; g is the mole number of oxygen atoms needed to satisfy the valence of each element in the active component.
In the above-mentioned technical solutions, the reaction is preferably carried out in the presence of a dilute gas phase feed.
In the above technical solution, the oxidizing gas is preferably pure oxygen, oxygen-enriched oxygen, or air.
In the above technical solution, the dilute gas phase material is preferably water vapor.
In the technical scheme, the reaction temperature is preferably 100-500 ℃.
In the above technical scheme, the material comprising acrolein, air and water vapor is used as the raw material gas for reaction, and the ratio by volume of acrolein: air: the steam is 1 (1-6) and 0.5-5.
In the technical scheme, the preferred volume space velocity of the feed gas is 800-2000 hours-1。
In the above-mentioned embodiments, as one of preferable embodiments, Y preferably includes Tc and Re together, and Tc and Re have a synergistic effect in improving the yield of acrylic acid.
In the above-mentioned second preferred embodiment, Y preferably includes both Tc and Mn, and Tc and Mn have a synergistic effect in increasing the yield of acrylic acid.
In the above technical solution, as a third preferred technical solution, Y preferably includes Tc and La simultaneously, and Tc and La have a synergistic effect in improving the yield of acrylic acid.
In the above technical solutions, as one of the more preferable technical solutions, Y simultaneously includes Tc, Re and Mn, and the three have a synergistic effect of ternary combination in the aspect of improving the yield of acrylic acid.
In the above-mentioned second preferred embodiment, Y simultaneously includes Tc, Mn and La, and the three components have a synergistic effect of ternary combination in improving the yield of acrylic acid.
In the above-mentioned technical solutions, as a third preferred technical solution, Y simultaneously includes Tc, Re and La, and the three have a synergistic effect of ternary combination in the aspect of improving the yield of acrylic acid.
In the above technical scheme, the molar ratio of Mo to V may be, but not limited to, 2.5, 3.0, 3.5, 4.0, 4.5, 5.0, 5.5, 6.0, 7.0, and the like.
In the above technical scheme, the molar ratio of Bi to V may be, but not limited to, 0.25, 0.30, 0.35, 0.40, 0.45, 0.50, 0.55, 0.60, 0.70, and the like.
In the above technical scheme, the molar ratio of W to V may be, but not limited to, 0.25, 0.30, 0.35, 0.40, 0.45, 0.50, 0.55, 0.60, 0.70, and the like.
In the above technical solution, the molar ratio of Cr to V may be, but not limited to, 0.25, 0.30, 0.35, 0.40, 0.45, 0.50, 0.55, 0.60, 0.70, and the like.
In the above technical scheme, the molar ratio of Na to V may be, but not limited to, 0.25, 0.30, 0.35, 0.40, 0.45, 0.50, 0.55, 0.60, 0.70, and the like.
In the above technical scheme, the molar ratio of Tc to V may be, but not limited to, 0.05, 0.10, 0.15, 0.20, 0.25, 0.30, 0.35, 0.40, 0.45, 0.50, 0.55, 0.60, etc.
In the above technical scheme, the molar ratio of Re to V may be, but not limited to, 0.05, 0.10, 0.15, 0.20, 0.25, 0.30, 0.35, 0.40, 0.45, 0.50, 0.55, 0.60, etc.
In the above technical scheme, the molar ratio of Mn to V may be, but not limited to, 0.05, 0.10, 0.15, 0.20, 0.25, 0.30, 0.35, 0.40, 0.45, 0.50, 0.55, 0.60, and the like.
In the above technical scheme, the molar ratio of La to V may be, but not limited to, 0.05, 0.10, 0.15, 0.20, 0.25, 0.30, 0.35, 0.40, 0.45, 0.50, 0.55, 0.60, etc.
In the above technical scheme, more specific examples of the general formula of the active ingredient can be, but are not limited to:
VMo2.0～8.0Bi0.2～0.8W0.2～1.0Cr0.2～1.0Tc0.05～0.60Re0.05～0.60Na0.05～1.2Og；
VMo2.0～8.0Bi0.2～0.8W0.2～1.0Cr0.2～1.0Tc0.05～0.60Mn0.05～0.60Na0.05～1.2Og；
VMo2.0～8.0Bi0.2～0.8W0.2～1.0Cr0.2～1.0Tc0.05～0.60La0.05～0.60Na0.05～1.2Og；
VMo2.0～8.0Bi0.2～0.8W0.2～1.0Cr0.2～1.0Tc0.05～0.45Re0.05～0.3Mn0.05～0.45Na0.05～1.2Og；
VMo2.0～8.0Bi0.2～0.8W0.2～1.0Cr0.2～1.0Tc0.05～0.45Mn0.05～0.3La0.05～0.45Na0.05～1.2Og；
VMo2.0～8.0Bi0.2～0.8W0.2～1.0Cr0.2～1.0Tc0.05～0.45Re0.05～0.3La0.05～0.45Na0.05～1.2Og；
wherein g is the mole number of oxygen atoms required to satisfy the valence of each element in the active component.
In the technical scheme, the content of the active component in the catalyst is preferably 10-60 w% by weight.
In the technical scheme, the content of the carrier in the catalyst is preferably 40-90 w% by weight.
In the above technical solutions, the shape and size of the carrier are not particularly limited, and all the carriers can obtain comparable technical effects, for which the skilled person can reasonably select. For convenience of comparison, the carriers of the embodiments of the present invention are all spherical.
In the above technical solution, the support is preferably at least one of alumina, lithium oxide, magnesia, zirconia, silica and titania.
In the technical scheme, the catalyst is prepared by adopting a method comprising the following steps:
preparing mixed liquid of active component elements;
mixing the active component element mixed solution with a carrier;
and (4) roasting.
In the above technical solution, the mixed solution may be a solution, a suspension, or a mixture of a solution and a suspension.
In the above technical solution, the conditions for calcination are not particularly limited as long as the conditions are such that the specific compound forms of all the active elements present in the above mixed solution can be calcined into oxide forms, and those skilled in the art can select the conditions for calcination appropriately without creative efforts.
In the above technical scheme, the roasting temperature is 300-550 ℃ by way of example only.
In the above technical scheme, the roasting time is 1-12 hours, which is only an example.
In the above technical scheme, the roasting atmosphere is an inert atmosphere or an atmosphere containing O by way of example only2Of the atmosphere (c). However, the atmosphere for the calcination is preferably air from the economical viewpoint. The atmosphere for calcination in the present invention is air unless otherwise specified.
In the above technical scheme, the catalyst can be prepared in the following manner:
1. preparation of active element solution
Dissolving a compound of the required active component elements to obtain a mixed solution of the active elements; the dissolution step is not particularly limited, and the specific dissolution procedure and process conditions may be appropriately selected by those skilled in the art.
2. Active element loading
And (2) mixing the carrier particles with the mixed liquid of the active elements obtained in the step (1) (wherein the dosage of the mixed liquid of the active elements is 5-50 w% of the required amount of the catalyst), and drying to obtain a catalyst precursor I. The drying temperature can be, but is not limited to, 60-100 ℃, and the drying time can be, but is not limited to, 2-8 hours.
3. Roasting
Calcining the catalyst precursor I to obtain the catalyst. The catalyst precursor I may further comprise a drying step before calcination, wherein the drying temperature is, for example and without limitation, 60-100 ℃, and the drying time is, for example and without limitation, 2-12 hours. The roasting temperature is, for example, but not limited to, 300-550 ℃, and the roasting time is, for example, but not limited to, 1-12 hours.
The catalyst prepared in this way is surprisingly good in terms of acrolein conversion and acrylic acid yield.
The catalyst evaluation method of the present invention is as follows:
a reactor: a fixed bed reactor with an inner diameter of 25 mm and a reactor length of 750 mm;
catalyst loading: 200 g;
reaction temperature: 280 ℃;
reaction time: 4 hours;
the volume ratio of raw materials is as follows: acrolein: air: water vapor 1: 3.5: 2;
total volume space velocity of raw materials: 1400 hours-1。
Acrolein conversion and acrylic acid yield are defined as follows:
acrolein conversion ═ 100% (molar amount of acrolein reaction/molar amount of acrolein total added);
the yield of acrylic acid (molar amount of acrylic acid produced/total molar amount of acrolein added) × 100%.
The catalyst of the present invention has acrolein converting rate up to 99% and acrylic acid yield up to 96%, and may be used in industrial production of acrylic acid.
Detailed Description
[ example 1 ]
1. Preparation of active element solution
Ammonium metavanadate (molecular formula: NH) containing 0.1 mol of V4VO3) Dissolved in hot water (200 g) at 80 ℃. Ammonium molybdate (molecular formula is (NH)) containing 0.4 mol of Mo4)2MoO4) Adding the mixture, and respectively adding ammonium tungstate (molecular formula: (NH)4)10W12O41) Ammonium chromate containing 0.04 mol Cr (formula: (NH)4)2CrO4) Technetium heptaoxide containing 0.04 mol Tc (formula: tc2O7) Sodium nitrate (molecular formula of NaNO) containing 0.04 mol of Na3) And stirred to dissolve the whole solution to obtain a solution I. Bismuth nitrate (molecular formula: Bi (NO): containing 0.04 mol of Bi3)3) Adding the aqueous solution into the above solutions respectively, mixing, evaporating at 80 deg.C until the mixed solution is equivalent to VMo containing active component4Bi0.4W0.4Cr0.4Tc0.4Na0.4OgWas 0.4g/g, to obtain a solution II.
2. Active element loading
200g of a spherical alumina carrier having a diameter of 5mm was uniformly mixed with 200g of the solution II, and dried at 80 ℃ for 4 hours to obtain a catalyst precursor I.
3. Roasting
The catalyst precursor I was dried at 90 ℃ for 6 hours and calcined at 400 ℃ for 3 hours to give a catalyst having the following composition:
32w％VMo4Bi0.4W0.4Cr0.4Tc0.4Na0.4Og+68w％Al2O3。
4. catalyst evaluation
The acrolein conversion and acrylic acid yield were examined.
The evaluation results of the supporting step in the catalyst and the catalyst are shown in Table 1 for convenience of comparison.
[ example 2 ]
1. Preparation of active element solution
Ammonium metavanadate (molecular formula: NH) containing 0.1 mol of V4VO3) Dissolved in hot water (200 g) at 80 ℃. Ammonium molybdate (molecular formula is (NH)) containing 0.4 mol of Mo4)2MoO4) Adding the mixture, and respectively adding ammonium tungstate (molecular formula: (NH)4)10W12O41) Ammonium chromate containing 0.04 mol Cr (formula: (NH)4)2CrO4) Rhenium heptoxide (molecular formula: re2O7) Sodium nitrate (molecular formula of NaNO) containing 0.04 mol of Na3) And stirred to dissolve the whole solution to obtain a solution I. Bismuth nitrate (molecular formula: Bi (NO): containing 0.04 mol of Bi3)3) Adding the aqueous solution into the above solutions respectively, mixing, evaporating at 80 deg.C until the mixed solution is equivalent to VMo containing active component4Bi0.4W0.4Cr0.4Re0.4Na0.4OgWas 0.4g/g, to obtain a solution II.
2. Active element loading
200g of a spherical alumina carrier having a diameter of 5mm was uniformly mixed with 200g of the solution II, and dried at 80 ℃ for 4 hours to obtain a catalyst precursor I.
3. Roasting
The catalyst precursor I was dried at 90 ℃ for 6 hours and calcined at 400 ℃ for 3 hours to give a catalyst having the following composition:
32w％VMo4Bi0.4W0.4Cr0.4Re0.4Na0.4Og+68w％Al2O3
4. catalyst evaluation
The acrolein conversion and acrylic acid yield were examined.
The evaluation results of the supporting step in the catalyst and the catalyst are shown in Table 1 for convenience of comparison.
[ example 3 ]
1. Preparation of active element solution
Ammonium metavanadate (molecular formula: NH) containing 0.1 mol of V4VO3) Dissolved in hot water (200 g) at 80 ℃. Ammonium molybdate (molecular formula is (NH)) containing 0.4 mol of Mo4)2MoO4) Adding the mixture, and respectively adding ammonium tungstate (molecular formula: (NH)4)10W12O41) Ammonium chromate containing 0.04 mol Cr (formula: (NH)4)2CrO4) Manganese nitrate containing 0.04 mol of Mn (molecular formula: mn (NO)3)2) Sodium nitrate (molecular formula of NaNO) containing 0.04 mol of Na3) And stirred to dissolve the whole solution to obtain a solution I. Bismuth nitrate (molecular formula: Bi (NO): containing 0.04 mol of Bi3)3) Adding the aqueous solution into the above solutions respectively, mixing, evaporating at 80 deg.C until the mixed solution is equivalent to VMo containing active component4Bi0.4W0.4Cr0.4Mn0.4Na0.4OgWas 0.4g/g, to obtain a solution II.
2. Active element loading
200g of a spherical alumina carrier having a diameter of 5mm was uniformly mixed with 200g of the solution II, and dried at 80 ℃ for 4 hours to obtain a catalyst precursor I.
3. Roasting
The catalyst precursor I was dried at 90 ℃ for 6 hours and calcined at 400 ℃ for 3 hours to give a catalyst having the following composition:
32w％VMo4Bi0.4W0.4Cr0.4Mn0.4Na0.4Og+68w％Al2O3
4. catalyst evaluation
The acrolein conversion and acrylic acid yield were examined.
The evaluation results of the supporting step in the catalyst and the catalyst are shown in Table 1 for convenience of comparison.
[ example 4 ]
1. Preparation of active element solution
Ammonium metavanadate (molecular formula: NH) containing 0.1 mol of V4VO3) Dissolved in hot water (200 g) at 80 ℃. Ammonium molybdate (molecular formula is (NH)) containing 0.4 mol of Mo4)2MoO4) Adding the mixture, and respectively adding ammonium tungstate (molecular formula: (NH)4)10W12O41) Ammonium chromate containing 0.04 mol Cr (formula: (NH)4)2CrO4) Lanthanum oxide containing 0.04 mol of La (formula: la2O3) Sodium nitrate (molecular formula of NaNO) containing 0.04 mol of Na3) And stirred to dissolve the whole solution to obtain a solution I. Bismuth nitrate (molecular formula: Bi (NO): containing 0.04 mol of Bi3)3) Adding the aqueous solution into the above solutions respectively, mixing, evaporating at 80 deg.C until the mixed solution is equivalent to VMo containing active component4Bi0.4W0.4Cr0.4La0.4Na0.4OgWas 0.4g/g, to obtain a solution II.
2. Active element loading
200g of a spherical alumina carrier having a diameter of 5mm was uniformly mixed with 200g of the solution II, and dried at 80 ℃ for 4 hours to obtain a catalyst precursor I.
3. Roasting
The catalyst precursor I was dried at 90 ℃ for 6 hours and calcined at 400 ℃ for 3 hours to give a catalyst having the following composition:
32w％VMo4Bi0.4W0.4Cr0.4La0.4Na0.4Og+68w％Al2O3
4. catalyst evaluation
The acrolein conversion and acrylic acid yield were examined.
The evaluation results of the supporting step in the catalyst and the catalyst are shown in Table 1 for convenience of comparison.
[ example 5 ]
1. Preparation of active element solution
Ammonium metavanadate (molecular formula: NH) containing 0.1 mol of V4VO3) Dissolved in hot water (200 g) at 80 ℃. Ammonium molybdate (molecular formula is (NH)) containing 0.4 mol of Mo4)2MoO4) Adding the mixture, and respectively adding ammonium tungstate (molecular formula: (NH)4)10W12O41) Ammonium chromate containing 0.04 mol Cr (formula: (NH)4)2CrO4) Technetium heptaoxide containing 0.02 mol Tc (formula: tc2O7) Rhenium heptoxide (molecular formula: re2O7) Sodium nitrate (molecular formula of NaNO) containing 0.04 mol of Na3) And stirred to dissolve the whole solution to obtain a solution I. Bismuth nitrate (molecular formula: Bi (NO): containing 0.04 mol of Bi3)3) Adding the aqueous solution into the above solutions respectively, mixing, evaporating at 80 deg.C until the mixed solution is equivalent to VMo containing active component4Bi0.4W0.4Cr0.4Tc0.2Re0.2Na0.4OgWas 0.4g/g, to obtain a solution II.
2. Active element loading
200g of a spherical alumina carrier having a diameter of 5mm was uniformly mixed with 200g of the solution II, and dried at 80 ℃ for 4 hours to obtain a catalyst precursor I.
3. Roasting
The catalyst precursor I was dried at 90 ℃ for 6 hours and calcined at 400 ℃ for 3 hours to give a catalyst having the following composition:
32w％VMo4Bi0.4W0.4Cr0.4Tc0.2Re0.2Na0.4Og+68w％Al2O3。
4. catalyst evaluation
The acrolein conversion and acrylic acid yield were examined.
The evaluation results of the supporting step in the catalyst and the catalyst are shown in Table 1 for convenience of comparison.
[ example 6 ]
1. Preparation of active element solution
Ammonium metavanadate (molecular formula: NH) containing 0.1 mol of V4VO3) Dissolved in hot water (200 g) at 80 ℃. Ammonium molybdate (molecular formula is (NH)) containing 0.4 mol of Mo4)2MoO4) Adding the mixture, and respectively adding ammonium tungstate (molecular formula: (NH)4)10W12O41) Ammonium chromate containing 0.04 mol Cr (formula: (NH)4)2CrO4) Technetium heptaoxide containing 0.02 mol Tc (formula: tc2O7) Manganese nitrate containing 0.02 mol of Mn (molecular formula: mn (NO)3)2) Sodium nitrate (molecular formula of NaNO) containing 0.04 mol of Na3) And stirred to dissolve the whole solution to obtain a solution I. Bismuth nitrate (molecular formula: Bi (NO): containing 0.04 mol of Bi3)3) Adding the aqueous solution into the above solutions respectively, mixing, evaporating at 80 deg.C until the mixed solution is equivalent to VMo containing active component4Bi0.4W0.4Cr0.4Tc0.2Mn0.2Na0.4OgWas 0.4g/g, to obtain a solution II.
2. Active element loading
200g of a spherical alumina carrier having a diameter of 5mm was uniformly mixed with 200g of the solution II, and dried at 80 ℃ for 4 hours to obtain a catalyst precursor I.
3. Roasting
The catalyst precursor I was dried at 90 ℃ for 6 hours and calcined at 400 ℃ for 3 hours to give a catalyst having the following composition:
32w％VMo4Bi0.4W0.4Cr0.4Tc0.2Mn0.2Na0.4Og+68w％Al2O3。
4. catalyst evaluation
The acrolein conversion and acrylic acid yield were examined.
The evaluation results of the supporting step in the catalyst and the catalyst are shown in Table 1 for convenience of comparison.
[ example 7 ]
1. Preparation of active element solution
Ammonium metavanadate (molecular formula: NH) containing 0.1 mol of V4VO3) Dissolved in hot water (200 g) at 80 ℃. Ammonium molybdate (molecular formula is (NH)) containing 0.4 mol of Mo4)2MoO4) Adding the mixture, and respectively adding ammonium tungstate (molecular formula: (NH)4)10W12O41) Ammonium chromate containing 0.04 mol Cr (formula: (NH)4)2CrO4) Technetium heptaoxide containing 0.02 mol Tc (formula: tc2O7) Lanthanum oxide containing 0.02 mol of La (molecular formula: la2O3) Sodium nitrate (molecular formula of NaNO) containing 0.04 mol of Na3) And stirred to dissolve the whole solution to obtain a solution I. Bismuth nitrate (molecular formula: Bi (NO): containing 0.04 mol of Bi3)3) Adding the aqueous solution into the above solutions respectively, mixing, evaporating at 80 deg.C until the mixed solution is equivalent to VMo containing active component4Bi0.4W0.4Cr0.4Tc0.2La0.2Na0.4OgWas 0.4g/g, to obtain a solution II.
2. Active element loading
200g of a spherical alumina carrier having a diameter of 5mm was uniformly mixed with 200g of the solution II, and dried at 80 ℃ for 4 hours to obtain a catalyst precursor I.
3. Roasting
The catalyst precursor I was dried at 90 ℃ for 6 hours and calcined at 400 ℃ for 3 hours to give a catalyst having the following composition:
32w％VMo4Bi0.4W0.4Cr0.4Tc0.2La0.2Na0.4Og+68w％Al2O3。
4. catalyst evaluation
The acrolein conversion and acrylic acid yield were examined.
The evaluation results of the supporting step in the catalyst and the catalyst are shown in Table 1 for convenience of comparison.
[ example 8 ]
1. Preparation of active element solution
Ammonium metavanadate (molecular formula: NH) containing 0.1 mol of V4VO3) Dissolved in hot water (200 g) at 80 ℃. Ammonium molybdate (molecular formula is (NH)) containing 0.4 mol of Mo4)2MoO4) Adding the mixture, and respectively adding ammonium tungstate (molecular formula: (NH)4)10W12O41) Ammonium chromate containing 0.04 mol Cr (formula: (NH)4)2CrO4) Technetium heptaoxide containing 0.015 mol of Tc (molecular formula: tc2O7) Rhenium heptoxide (molecular formula: re2O7) Manganese nitrate containing 0.015 mol of Mn (molecular formula: mn (NO)3)2) Sodium nitrate (molecular formula of NaNO) containing 0.04 mol of Na3) And stirred to dissolve the whole solution to obtain a solution I. Bismuth nitrate (molecular formula: Bi (NO): containing 0.04 mol of Bi3)3) Adding the aqueous solution into the above solutions respectively, mixing, evaporating at 80 deg.C until the mixed solution is equivalent to VMo containing active component4Bi0.4W0.4Cr0.4Tc0.15Re0.1Mn0.15Na0.4OgWas 0.4g/g, to obtain a solution II.
2. Active element loading
200g of a spherical alumina carrier having a diameter of 5mm was uniformly mixed with 200g of the solution II, and dried at 80 ℃ for 4 hours to obtain a catalyst precursor I.
3. Roasting
The catalyst precursor I was dried at 90 ℃ for 6 hours and calcined at 400 ℃ for 3 hours to give a catalyst having the following composition:
32w％VMo4Bi0.4W0.4Cr0.4Tc0.15Re0.1Mn0.15Na0.4Og+68w％Al2O3
4. catalyst evaluation
The acrolein conversion and acrylic acid yield were examined.
The evaluation results of the supporting step in the catalyst and the catalyst are shown in Table 1 for convenience of comparison.
[ example 9 ]
1. Preparation of active element solution
Ammonium metavanadate (molecular formula: NH) containing 0.1 mol of V4VO3) Dissolved in hot water (200 g) at 80 ℃. Ammonium molybdate (molecular formula is (NH)) containing 0.4 mol of Mo4)2MoO4) Adding the mixture, and respectively adding ammonium tungstate (molecular formula: (NH)4)10W12O41) Ammonium chromate containing 0.04 mol Cr (formula: (NH)4)2CrO4) Technetium heptaoxide containing 0.015 mol of Tc (molecular formula: tc2O7) Manganese nitrate containing 0.01 mol of Mn (molecular formula: mn (NO)3)2) Lanthanum oxide containing 0.015 mol of La (molecular formula: la2O3) Sodium nitrate (molecular formula of NaNO) containing 0.04 mol of Na3) And stirred to dissolve the whole solution to obtain a solution I. Bismuth nitrate (molecular formula: Bi (NO): containing 0.04 mol of Bi3)3) Adding the aqueous solution into the above solutions respectively, mixing, evaporating at 80 deg.C until the mixed solution is equivalent to VMo containing active component4Bi0.4W0.4Cr0.4Tc0.15Mn0.1La0.15Na0.4OgWas 0.4g/g, to obtain a solution II.
2. Active element loading
200g of a spherical alumina carrier having a diameter of 5mm was uniformly mixed with 200g of the solution II, and dried at 80 ℃ for 4 hours to obtain a catalyst precursor I.
3. Roasting
The catalyst precursor I was dried at 90 ℃ for 6 hours and calcined at 400 ℃ for 3 hours to give a catalyst having the following composition:
32w％VMo4Bi0.4W0.4Cr0.4Tc0.15Mn0.1La0.15Na0.4Og+68w％Al2O3
4. catalyst evaluation
The acrolein conversion and acrylic acid yield were examined.
The evaluation results of the supporting step in the catalyst and the catalyst are shown in Table 1 for convenience of comparison.
[ example 10 ]
1. Preparation of active element solution
Ammonium metavanadate (molecular formula: NH) containing 0.1 mol of V4VO3) Dissolved in hot water (200 g) at 80 ℃. Ammonium molybdate (molecular formula is (NH)) containing 0.4 mol of Mo4)2MoO4) Adding the mixture, and respectively adding ammonium tungstate (molecular formula: (NH)4)10W12O41) Ammonium chromate containing 0.04 mol Cr (formula: (NH)4)2CrO4) Technetium heptaoxide containing 0.015 mol of Tc (molecular formula: tc2O7) Rhenium heptoxide (molecular formula: re2O7) Lanthanum oxide containing 0.015 mol of La (molecular formula: la2O3) Sodium nitrate (molecular formula of NaNO) containing 0.04 mol of Na3) And stirred to dissolve the whole solution to obtain a solution I. Bismuth nitrate (molecular formula: Bi (NO): containing 0.04 mol of Bi3)3) Adding the aqueous solution into the above solutions respectively, mixing, evaporating at 80 deg.C until the mixed solution is equivalent to VMo containing active component4Bi0.4W0.4Cr0.4Tc0.15Re0.1La0.15Na0.4OgWas 0.4g/g, to obtain a solution II.
2. Active element loading
200g of a spherical alumina carrier having a diameter of 5mm was uniformly mixed with 200g of the solution II, and dried at 80 ℃ for 4 hours to obtain a catalyst precursor I.
3. Roasting
The catalyst precursor I was dried at 90 ℃ for 6 hours and calcined at 400 ℃ for 3 hours to give a catalyst having the following composition:
32w％VMo4Bi0.4W0.4Cr0.4Tc0.15Re0.1La0.15Na0.4Og+68w％Al2O3
4. catalyst evaluation
The acrolein conversion and acrylic acid yield were examined.
The evaluation results of the supporting step in the catalyst and the catalyst are shown in Table 1 for convenience of comparison.
TABLE 1
Claims (10)
1. A process for producing acrylic acid, comprising reacting acrolein with an oxygen-containing oxidizing gas in the presence of a catalyst to obtain acrylic acid; the catalyst comprises a carrier and an active component loaded on the carrier, wherein the active component is represented by the general formula: VMoaBibWcXdYeZfOgWherein X is selected from one or more of Sc, Ti, Y, Zr, Hf, Ta and Cr, Y is selected from at least one of Ga, Ge, In, Sn, TI, Pb, Cd, Mn, Tc, Re, Rh, Ir, Pd, Pt, Ag, Au and La, and Z is selected from one or more of alkali metal or alkaline earth metal; a is the molar ratio of Mo to V, and the value of a is 2.0-8.0; b is the molar ratio of Bi to V, and the value of b is 0.2-0.8; c is the molar ratio of W to V, and the value of c is 0.2-1.0; d is the molar ratio of X to V, and the value of d is 0.2-1.0; e is the molar ratio of Y to V, and the value of e is 0.05-1.2; f is the molar ratio of Z to V,f takes a value of 0.05-1.2; g is the mole number of oxygen atoms needed to satisfy the valence of each element in the active component.
2. The process for producing acrylic acid as claimed in claim 1, wherein said reaction is carried out in the presence of a dilute gaseous material.
3. The method for producing acrylic acid according to claim 1, wherein said oxidizing gas is selected from the group consisting of pure oxygen, oxygen-rich gas and air.
4. The process for producing acrylic acid according to claim 2, wherein said diluting gas-phase material is steam.
5. The process for producing acrylic acid as claimed in claim 1, wherein the reaction temperature is 100 to 500 ℃.
6. The process for producing acrylic acid as claimed in claim 1, wherein the raw material gas for the reaction is a material consisting of acrolein, air and water vapor, and the ratio by volume of acrolein: air: the steam is 1 (1-6) and 0.5-5.
7. The process for producing acrylic acid as claimed in claim 6, wherein the volume space velocity of the raw material gas is 800 to 2000 hours-1。
8. The process for producing acrylic acid as claimed in claim 1, wherein the catalyst contains the active component in an amount of 10 to 60% by weight.
9. The process for producing acrylic acid according to claim 1, wherein the carrier is at least one member selected from the group consisting of alumina, lithium oxide, magnesium oxide, zirconia, silica and titania.
10. The method for producing acrylic acid as described in claim 1, wherein said catalyst is prepared by a method comprising the steps of:
preparing mixed liquid of active component elements;
mixing the active component element mixed solution with a carrier;
and (4) roasting.
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| CN112774673A (en) * | 2021-02-05 | 2021-05-11 | 西安凯立新材料股份有限公司 | Catalyst for preparing acrylic acid by acrolein air oxidation and preparation method and application thereof |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1343192A (en) * | 1999-03-10 | 2002-04-03 | 巴斯福股份公司 | Method for catalytic gas phase oxidation of acrolein into acrylic acid |
| CN1684936A (en) * | 2002-09-27 | 2005-10-19 | 巴斯福股份公司 | Heterogeneously catalyzed gas-phase partial oxidation of acrolein to acrylic acid |
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Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1343192A (en) * | 1999-03-10 | 2002-04-03 | 巴斯福股份公司 | Method for catalytic gas phase oxidation of acrolein into acrylic acid |
| CN1684936A (en) * | 2002-09-27 | 2005-10-19 | 巴斯福股份公司 | Heterogeneously catalyzed gas-phase partial oxidation of acrolein to acrylic acid |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112774673A (en) * | 2021-02-05 | 2021-05-11 | 西安凯立新材料股份有限公司 | Catalyst for preparing acrylic acid by acrolein air oxidation and preparation method and application thereof |
| CN112774673B (en) * | 2021-02-05 | 2022-10-18 | 西安凯立新材料股份有限公司 | Catalyst for preparing acrylic acid by acrolein air oxidation and preparation method and application thereof |
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