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Methyl Acraldehyde, Catalyst Used For Preparing Methyl Acraldehyde And Preparation Method Thereof

A technology of methacrylic acid and methacrolein, used in catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., to achieve high activity and less production

Inactive Publication Date: 2012-03-14
NIPPON KAYAKU CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, these methods are not sufficiently satisfactory as industrial methods, and the development of catalysts that generate less high-boiling by-products is desired.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0068] 3000 g of ammonium molybdate and 55.2 g of cesium nitrate were dissolved while heating and stirring 12000 ml of distilled water to obtain an aqueous solution (A). Separately, 2,782 g of cobalt nitrate, 1,144 g of iron nitrate, and 412 g of nickel nitrate were dissolved in 2,300 ml of distilled water to prepare an aqueous solution (B), and 1,167 g of bismuth nitrate was dissolved in 1,215 ml of distilled water adjusted to be acidic by adding 292 ml of concentrated nitric acid to prepare an aqueous solution (C). . Mix (B) and (C) sequentially in the above aqueous solution (A) while vigorously stirring, finally add 60 g of acetic acid, use a spray dryer to dry the resulting suspension, and calcinate at 460 ° C for 5 hours to obtain the pre- Calcined powder (D). The compositional ratios of the catalyst active component excluding oxygen at this time were Mo=12, Bi=1.7, Fe=2.0, Co=6.75, Ni=1.0, and Cs=0.20 in atomic ratio.

[0069] Thereafter, 5 parts by mass of crystalline...

Embodiment 2

[0072]450 g of ammonium molybdate and 3.8 g of cesium nitrate were dissolved while heating and stirring 2000 ml of distilled water to obtain an aqueous solution (A). Separately, 456 g of cobalt nitrate and 158 g of iron nitrate were dissolved in 500 ml of distilled water to prepare an aqueous solution (B), and 190 g of bismuth nitrate was dissolved in 200 ml of distilled water acidified by adding 48 ml of concentrated nitric acid to prepare an aqueous solution (C). Mix (B) and (C) sequentially in the above aqueous solution (A) while vigorously stirring, finally add 35g of propionic acid, dry the resulting suspension with a spray dryer, and calcinate at 460°C for 5 hours to obtain Pre-calcined powder (D). At this time, the composition ratios of the catalyst active component excluding oxygen were Mo=13, Bi=2.0, Fe=2.0, Co=8.0, and Cs=0.1 in atomic ratio.

[0073] Thereafter, 5 parts by mass of crystalline cellulose was mixed with 100 parts by mass of precalcined powder (D) to o...

Embodiment 3

[0075] 500 g of ammonium molybdate and 10.2 g of cesium nitrate were dissolved while heating and stirring 3000 ml of distilled water in which 40 g of propionic acid was dissolved to obtain an aqueous solution (A). Separately, 485 g of cobalt nitrate, 190 g of iron nitrate, and 72 g of nickel nitrate were dissolved in 395 ml of distilled water to prepare an aqueous solution (B), and 196 g of bismuth nitrate was dissolved in 206 ml of distilled water adjusted to be acidic by adding 50 ml of concentrated nitric acid to prepare an aqueous solution (C). . Mix (B) and (C) sequentially in the above aqueous solution (A) while vigorously stirring, dry the resulting suspension with a spray dryer, and calcinate at 460°C for 5 hours to obtain pre-calcined powder (D) . The compositional ratios of the catalyst active component excluding oxygen at this time were Mo=12, Bi=1.8, Fe=2.0, Co=7.75, Ni=1.5, and Cs=0.30 in atomic ratio.

[0076] Thereafter, 5 parts by mass of crystalline cellulos...

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PUM

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Abstract

The invention relates to a composite oxide catalyst containing molybdenum used in preparing methyl acraldehyde through gas phase catalytically oxidation of at least one gas containing molecular oxygen selected from a group formed by isobutene and tertiary butanol, and provides the catalyst having low generation of compound by products having high activity and high boiling point and capable of obtaining methyl acraldehyde stably at high yield, and a preparation method. The preparation method of composite oxide catalyst containing molybdenum and bismuth includes two stages of (1) preparing solution or sizing agent containing catalyst material by adding organic acid in integration precedures of an aqueous system of supply source compound including at least the component elements; and (2) drying and sintering the solution or the sizing agent. It is characterized in that the ratio of an acid volume of the catalyst on a low temperature side measured through a ammonia temperaturing rise removing method and an acid volume of the catalyst on a high temperature side measured through a ammonia temperaturing rise removing method is lower than 0.14.

Description

technical field [0001] The present invention relates to a molybdenum-containing composite oxide catalyst used for producing methacrolein by gas-phase catalytic oxidation of at least one selected from the group consisting of isobutene and tert-butanol using a gas containing molecular oxygen, and a production method thereof. Background technique [0002] In the case of producing methacrylic acid by gas-phase catalytic oxidation reaction of at least one selected from isobutene and tert-butanol, it is generally used to first convert at least one gas-phase catalytic oxidation selected from isobutene and tert-butanol into methacrolein (hereinafter, this reaction is referred to as "front-stage reaction", and the catalyst used therein is referred to as "front-stage catalyst"), and then the methacrolein gas-phase catalytic oxidation is converted into methacrylic acid (hereinafter, this reaction is referred to as " Back-stage reaction", in which the catalyst used is called "back-stage...

Claims

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Application Information

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IPC IPC(8): B01J23/887C07C27/14C07C47/22C07C45/35C07C45/37C07C57/05C07C51/25C07C51/23
CPCB01J23/31B01J37/08C07C45/32C07C47/22
Inventor 饭岛孝幸小岛利丈西村英二
Owner NIPPON KAYAKU CO LTD
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