• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Catalysts containing the oxides of molybdenum and phosphorus promoted with rubidium and at least one element selected from the group consisting of As, Cd, In, Sn, Tl, K, Ca, V, U, Ce, W, Ni, Zr, Ba, Fe, Rh, Mn, Re, Ru, Co, and Cu have been found to be especially desirable in the vapor phase oxidation of acrolein and methacrolein with molecular oxygen to yield acrylic acid and methacrylic acid respectively. The reaction of methacrolein gives an especially pure product in high yields and selectivities of methacrylic acid.
    公开号:SU751311A3
    申请号:SU762388702
    申请日:1976-08-17
    公开日:1980-07-23
    发明作者:Фергюсон Вайт Джеймс；Роберт Ридж Джеймс
    申请人:Дзе Стандарт Ойл Компани (Фирма)；
    IPC主号:
    专利说明:

    (54) CATALYST FOR METHACROLEIN OXIDATION TO METACRYLIC ACID
    one
    The invention relates to the production of catalysts for the oxidation of unsaturated aldehydes to the corresponding acids, in particular methacrolein to methacrylic acid.
    A known catalyst for the oxidation of methacrolein to methacrylic acid, containing molybdenum, phosphorus, oxygen, as well as one of the elements tungsten, mouse, indium and cadmium l .10
    The immediate solution of the problem is a catalyst for the oxidation of methacrolein to methacrylic acid, containing vanadium, molybdenum, phosphorus and oxygen, as well as 15 promoters selected from the group consisting of bismuth, mouse, boron, cerium, chromium, silver, iron, tungsten, lead, manganese, thallium, tellurium, nickel, niobium, boron, tin, 20 copper 2.
    The composition of the catalyst corresponds to the empirical formula
    PO Vb, 25
    where a is a number greater than 6;
    L = 0.1–12;
    X is the number of oxygen atoms required to saturate the valence of all elements, 30
    The disadvantages of the known catalyst are the insufficiently high activity and selectivity of the catalyst; the yield of methacrylic acid is 44-57% with a selectivity of 50.4-72%.
    The aim of the invention is to increase -. reduction of catalyst activity and selectivity.
    The proposed catalyst containing molybdenum, phosphorus, oxygen and a promoter is characterized in that it contains an element selected from the group consisting of mouse, cadmium, indium, tin, thallium, potassium, calcium, vanadium, uranium, cerium, tungsten. , nickel, zirconium, barium, iron, rhodium, manganese, rhenium, ruthenium, cobalt, copper, and additionally rubidium, while the composition of the catalyst corresponds to the empirical formula
    RO.
    Rbb Ios
    where A is an element selected from the group consisting of mouse, keshmi, indium, tin, thallium, potassium, calcium, vanadium, uranium, cerium, tungsten, nickel, zirconium, barium, iron, rhodium, manganese, rhenium, ruthenium, cobalt copper; and 0.025-0.625; b 0,025 - 0,5; from 2-3; X is the number of oxygen atoms required to saturate the valence of all elements. The proposed catalyst has an increased activity and selectivity, the yield of methacrylic acid per cycle increases to 68% with a selectivity of 74%. The catalyst is prepared in an aqueous mixture or in a solution of molybdenum, phosphorus and other components, including the evaporation of this aqueous mixture and the calcination of the resulting catalysts. Suitable molybdenum compounds that can be used in the preparation of catalysts corresponding to the formula shown include molybdenum trioxide, phosphomolybdic acid Göptamolybdat-ammonia. Suitable phosphorus compounds that can be used in the preparation of catalysts include orthophosphoric acid, metaphosphoric acid, triphosphoric acid, phosphorus chloride. The remaining components of the catalysts can be added in the form of oxides, acetates, formates, sulfates, nitrates, carbonates. The catalysts can also be prepared by mixing the catalytic components in an aqueous slurry or solution, heating the aqueous mixture to dryness and burning the resulting catalysts. The best results are obtained by refluxing phosphoric acid and molybdenum trioxide in water for about 1.5-3 hours, adding rubidi salt followed by the introduction the remaining components to water slurry and boiling to a thick paste, drying at 110-120 ° C in air and burning the resulting catalysts. Excellent results are achieved when soluble salts of catalytic components other than molybdenum are used in the preparation of catalysts. Insoluble salts or oxides can be used, however, optimum results are achieved when soluble salts of components other than molybdenum and phosphorus are used in the preparation of the catalyst. Oxidation reagents are methacrolein and molecular oxygen. Molecular oxygen is usually supplied to the reaction in the form of air, but oxygen containing gas can also be used. Usually, 0.5-10 mol of oxygen is added to 1 mol of methacrolein. Steam or an inert diluent can be introduced into the reaction. Preferably, the reactions are carried out in the presence of significant amounts of steam, about 2 to 20 mol of steam per 1 mol of methacrolein. The reaction temperature may vary depending on the catalyst used. Temperatures of 200 ° C are typically used, with temperatures of about 250-400 ° C being preferred. The reaction is conveniently carried out using a reactor with either a fixed bed or a fluidized bed. The contact time may be from fractions of a second to 20 seconds or more, preferably 4-5 seconds. The reaction can be carried out at atmospheric, more atmospheric or less atmospheric pressure, preferably pressures of 0.5-4 atm. The catalyst may be deposited on a carrier or without a carrier. Suitable support materials (supports) are silica, aundum, alumina, boron, zirconia, titanium and the like, but zirconia is most preferred. PRI me R 1. The catalyst of the formula Jnj ogRbQg Mod RO, EZH ° ° as follows. A pasty mixture of 86.2 g (0.6 mol) of molybdenum trioxide and 7.7 g (0.67 mol) of phosphorus with 85% phosphoric acid in 1500 ml of distilled water is prepared, boiled with stirring for 2 h with the formation of phosphomolybdic acid, which has a greenish-yellow color. 2.3 g (0.01 mol) of indium acetate was added to the mixture, the color did not change, then 14.4 g (0.1 mol) of rubidium acetate was added. The aqueous mixture, which was yellow in color and boiled dry, was air dried overnight. The catalyst is crushed and sieved to 20/30 mesh fractions. Examples 2-20. Various catalysts are prepared as in Example 1 using 86.2 g of molybdenum trioxide, 7.7 g of 85% phosphoric acid and 14.4 g of rubidium acetate. These catalysts are common. formula AjQj-Rbg J Mo.j. The catalytic component A is added after two hours of heating with a molybdenum trioxide reflux condenser and 85% phosphoric acid. For the preparation of catalysts, the compounds listed in Table 1 are used. The catalysts are boiled and dried according to Example 1. The catalysts are ground and passed through a sieve to a size of 20/30 mesh. Examples 21-33. The preparation of catalysts of the formula, eOX in which A includes at least two elements. The catalysts are prepared as described in Example 1. The catalytic components A are introduced after a two-hour heating with a reverse
    cooler and add 85% phosphoric acid. For the preparation of catalysts, the compounds listed in Table 2 are used.
    Examples 34-103 Preparation of methacrylic acid using various catalysts.
    Catalysts are prepared similarly using the appropriate ratios of ingredients. Some of these particle catalysts are loaded into a 20 cm reactor with a fixed bed consisting of a 1.3 cm long stainless steel tube equipped with a 0.3 cm axial thermal wall with a full length thickness. The reactor is heated to the reaction temperature in an air stream and a charge of methacrolein, air, steam is supplied in a ratio of 1: 6, 2: 5.2 over the catalyst at a contact time of about 4.5–5 s. The reactor is operated under the reaction conditions for 1-5 hours and the product is collected by cleaning the reactor from waste gases in two series of water scrubbers. The contents of the scrubbers are combined and diluted to 1100 cm for analysis.
    and filtering acidic contents. Purified fixed gases are dried and analyzed in a conventional column system. The results are expressed as follows.
    Single Pass (Cycle)
    isolated methacrylate
     acid (mol)
    X 100.
    methacrolein in the load (mol)
    Total Conversion
    reacted meta crawler (mol)
    X 100.
    methacrolein in the load (mol)
    Selectivity
    output for a single cycle
    X 100
    total conversion The results are shown in Table. 3
    Table 1
    Continued table. 3
    权利要求:
    Claims (2)
    [1]
    Claim
    A catalyst for the oxidation of methacrolein to methacrylic acid, including molybdenum, phosphorus, a promoter and oxygen, characterized in that, in order to increase the activity, activity and selectivity of the catalyst, it additionally contains rubidium, · and as a promoter an element selected from the group containing arsenic, cadmium, indium, tin, thallium, potassium., calcium, vanadium, uranium, cerium, tungsten, nickel, zirconium, barium, iron, rhodium, manganese, rhenium, ruthenium, cobalt, copper, and the composition of the catalyst corresponds to the empirical formula
    Ag (RbMo with PojjOx, and b from X wherein A - a member selected from the group consisting of arsenic, cadmium, indium, tin, thallium, potassium, calcium, vanadium, uranium, cerium, tungsten, nickel, zirconium, barium, iron, rhodium, manganese, rhenium, ruthenium, cobalt, copper;
    0.025-0.625; 0.025-0.5;
    [2]
    2 - s;
    the number of oxygen atoms needed to saturate the valency of all elements.
    类似技术:
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    SU751311A3|1980-07-23|Catalyzer for oxidizing methacrolein into methacrylic acid
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    US3875220A|1975-04-01|Process for the preparation of methacrylic acid from methacrolein
    AU608615B2|1991-04-11|Acetic acid from ethane, ethylene and oxygen
    US4155938A|1979-05-22|Oxidation of olefins
    US4180678A|1979-12-25|Process for preparing methacrylic acid
    EP0027351B1|1983-06-01|Oxidation catalysts and process for the preparation of methacrolein by vapour phase oxidation
    US4051180A|1977-09-27|Preparation of acrylic acid and methacrylic acid
    US4354044A|1982-10-12|Method for preparing methacrolein
    US4190608A|1980-02-26|Process for the oxidation of olefins using catalysts containing various promoter elements
    US4306090A|1981-12-15|Catalyst compositions and their use for the preparation of methacrolein
    US4101448A|1978-07-18|Catalyst compositions especially useful for preparation of unsaturated acids
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    US4225466A|1980-09-30|Catalytic oxide composition for preparing methacrylic acid
    US4017547A|1977-04-12|Oxidation of p-xylene to terephthalaldehyde
    US4558029A|1985-12-10|Antimony-containing C4 oxidation catalysts
    EP0046333B1|1985-04-17|Bismuth-containing catalyst compositions of use in the oxidation of methacrolein, production thereof and oxidation of methacrolein utilizing them
    AU612368B2|1991-07-11|Organic acids from alkanols
    JP4269437B2|2009-05-27|Method for producing methacrylic acid
    US4446328A|1984-05-01|Process for producing methacrolein
    US4359407A|1982-11-16|Catalyst compositions especially useful for preparation of unsaturated acids
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    JPH10128112A|1998-05-19|Catalyst for vapor phase contact oxidation reaction of isobutane and its preparation
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    同族专利:
    公开号 | 公开日
    PT65453B|1978-02-10|
    ATA583076A|1979-12-15|
    ES450761A1|1977-12-16|
    RO69967A|1981-05-15|
    BR7605401A|1977-08-16|
    NO762835L|1977-02-21|
    AT357510B|1980-07-10|
    US4017423A|1977-04-12|
    DE2634790A1|1977-07-07|
    GB1556719A|1979-11-28|
    JPS5236619A|1977-03-22|
    ES461628A1|1978-06-16|
    DD127322A5|1977-09-14|
    PT65453A|1976-09-01|
    BE845248A|1976-12-16|
    CA1072072A|1980-02-19|
    NL7609180A|1977-02-22|
    FR2321327A1|1977-03-18|
    FR2321327B1|1980-03-21|
    CS196318B2|1980-03-31|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3086026A|1959-06-27|1963-04-16|Basf Ag|Production of maleic acid and maleic anhydride|
    DE1146844B|1960-12-14|1963-04-11|Thyssensche Gas Und Wasserwerk|Process for coking gas-rich coals for the production of ore coke|
    US3882047A|1971-11-30|1975-05-06|Nippon Zeon Co|Oxidation catalyst composition of unsaturated carboxylic acid|
    US3795703A|1971-11-30|1974-03-05|Nippon Zeon Co|Process for preparing unsaturated carboxylic acids|
    GB1417787A|1972-11-13|1975-12-17|Mitsubishi Rayon Co|Catalyst composition for oxidation of butenes|
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    US4118419A|1975-12-03|1978-10-03|Mitsubishi Rayon Company, Ltd.|Catalytic process for the preparation of an unsaturated carboxylic acid|
    US4358608A|1976-06-07|1982-11-09|The Standard Oil Company|Process for producing unsaturated aliphatic acids|
    US4085065A|1976-10-19|1978-04-18|The Standard Oil Company |Process for the preparation of unsaturated acids from unsaturated aldehydes|
    JPS6214535B2|1978-06-21|1987-04-02|Nippon Kayaku Kk|
    JPS575213B2|1978-08-25|1982-01-29|
    US4404397A|1980-03-24|1983-09-13|Air Products And Chemicals, Inc.|High conversion of C3 and C4 olefins to corresponding unsaturated aldehydes and acids with stable molybdenum catalysts|
    US4271040A|1978-12-26|1981-06-02|Halcon Research And Development Corp.|Catalyst and process for producing methacrylic acid|
    US4252682A|1978-12-26|1981-02-24|Halcon Research And Development Corp.|Catalyst for producing methacrylic acid|
    JPS6230177B2|1979-03-16|1987-07-01|Nippon Kayaku Kk|
    US4279777A|1979-12-10|1981-07-21|The Standard Oil Company|Molybdenum-copper-tin catalysts|
    US4301030A|1980-08-05|1981-11-17|The Standard Oil Company|Bi-containing methacrolein oxidation catalysts|
    US4301031A|1980-08-05|1981-11-17|The Standard Oil Company|Methacrolein oxidation catalysts|
    DE3030243A1|1980-08-09|1982-03-18|Basf Ag, 6700 Ludwigshafen|OXIDATION CATALYST, IN PARTICULAR FOR THE PRODUCTION OF METHACRYLIC ACID BY GAS PHASE OXIDATION OF METHACROLEIN|
    US4347163A|1980-10-03|1982-08-31|Standard Oil Company|Te-containing methacrolein oxidation catalysts and their use|
    US4410448A|1981-12-28|1983-10-18|The Standard Oil Company|Method for controlling the change in the crush strength of a catalyst particle during finishing calcination|
    US4596784A|1982-06-07|1986-06-24|Rohm And Haas Company|Catalyst compositions and their use for the preparation of unsaturated carboxylic acids|
    US4710484A|1982-06-25|1987-12-01|The Standard Oil Company|Method for preparing a supported mixed-metal oxide oxidation catalyst|
    JPH0233419B2|1982-12-22|1990-07-27|Nippon Shokubai Kagaku Kogyo Kk|
    US5028713A|1983-12-08|1991-07-02|The Standard Oil Company|Ammoxidation of methyl substituted heteroaromatics to make heteroaromatic nitriles|
    US5210293A|1989-07-05|1993-05-11|Bp Chemicals Limited|Process and catalyst for the production of ethylene and acetic acid|
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    KR100477894B1|2002-06-04|2005-03-18|한국과학기술연구원|A preparation method of heteropolyacid catalyst and preparation method of metacrylic acid using thereof|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US05/605,362|US4017423A|1975-08-18|1975-08-18|Process for the preparation of unsaturated acids from unsaturated aldehydes|
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