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Method for prolonging running period of acrylic acid device

A technology of operation cycle and acrylic acid, applied in chemical instruments and methods, preparation of carboxylate, preparation of organic compounds, etc., can solve the problems of decreasing catalyst activity, affecting economic benefits, reducing hot spot temperature of catalyst bed, etc. temperature, the effect of prolonging the operating cycle

Inactive Publication Date: 2014-12-10
CHINA NAT OFFSHORE OIL CORP +3
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method reduces the difficulty of catalyst loading because it does not use diluted packing, but because it also reduces the catalyst bed hot spot temperature by reducing the catalyst activity, the use efficiency of the catalyst is reduced
In addition, the coated catalyst is affected by the preparation process, and the specific surface loss of the catalyst is large. After the propylene concentration at the reactor inlet is increased or the space velocity is increased in the industrial device, the catalyst activity decreases and the acrolein yield decreases. economic benefits
Patent CN1255366C reports a method for preparing acrolein and acrylic acid. First, catalysts with different activities are prepared by different occupied volumes, calcination temperatures, or alkali metals, and then the catalyst activity is gradually increased from the inlet to the outlet of the raw material gas. Catalysts are filled into the reaction zone in sequence. Although this method reduces the hot spot temperature of the catalyst bed, the catalyst activity gradually weakens from the raw material inlet to the outlet, which reduces the reaction efficiency of the catalyst.

Method used

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  • Method for prolonging running period of acrylic acid device

Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0019] Preparation of coated catalyst 1

[0020] Dissolve 339g of ammonium paramolybdate in 2400ml of pure water, add 520ml of 25% ammonia solution; dissolve 242g of cobalt nitrate and 130g of nickel nitrate in 300ml of pure water; water, in addition, 116g of ferric nitrate was dissolved in 300ml of water. At 50°C, add the mixed solution of cobalt nitrate and nickel nitrate to the vigorously stirred ammonium molybdate solution added with 5% citric acid-polyvinylpyrrolidone in advance, and react to form a sol. After half an hour, add the mixed solution of bismuth nitrate and iron nitrate, and add ammonia water or nitric acid during the addition to keep the pH value of the system between 1-6, so that the above-mentioned aqueous slurry can be obtained. After cooling the slurry to below 40° C., 720 ml of ethanol was added and stirred at high speed to form a water-organic phase slurry.

[0021] On the basis of continuously replenishing ethanol, the water in the slurry is separate...

Embodiment 1

[0035] (Propylene Oxidation Reaction)

[0036] In a reaction tube with an inner diameter of 25 mm and a length of 4800 mm, the catalyst prepared in the above reference example is used to fill it to form a catalyst bed with a packing height of 3500 mm, and the remaining space in the reaction tube is filled with inert fillers. The specific loading method of the catalyst bed is: the catalyst bed near the reaction tube outlet is filled with the coating catalyst 2 carrying 33% active components, and the filling height is 2500mm; the catalyst bed near the reaction tube inlet is filled with the described The coated catalyst 1 loaded with 20% active components has a packing height of 1000mm. Feed into the feed gas consisting of 10% concentration of propylene, 17% concentration of steam and 73% concentration of air, at a pressure of 0.1MPa, the gas volume space velocity is 1800hr -1 propylene oxidation reaction. The resulting reaction structures are shown in Table 1.

Embodiment 2

[0038] (Propylene Oxidation Reaction)

[0039] In a reaction tube with an inner diameter of 25 mm and a length of 4800 mm, the catalyst prepared in the above reference example is used to fill it to form a catalyst bed with a packing height of 3500 mm, and the remaining space in the reaction tube is filled with inert fillers. The specific loading method of the catalyst bed is: the catalyst bed near the reaction tube outlet is filled with the coating catalyst 3 carrying 50% active components, and the filling height is 2500mm; the catalyst bed near the reaction tube inlet is filled with the described The coated catalyst 1 loaded with 20% active components has a packing height of 1000 mm. Feed into the feed gas consisting of 10% concentration of propylene, 17% concentration of steam and 73% concentration of air, at a pressure of 0.1MPa, the gas volume space velocity is 1800hr -1 propylene oxidation reaction. The resulting reaction structures are shown in Table 1.

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Abstract

The invention provides a method for prolonging the running period of an acrylic acid device. The method comprises the following steps: loading a catalyst without diluting by use of an inert filler, arranging coated catalyst bed layers having different heat resistances in a tube fixed-bed reactor according to the heat resistance in the axial direction of the reactor; and loading a coated catalyst relatively low in heat resistance in a position near the outlet of a reaction tube, and then orderly loading coated catalysts relatively high in heat resistance in such a manner that the coated catalyst close to the inlet of the reaction tube has the highest heat resistance, wherein the coated catalysts having different heat resistances are catalysts the inner cores of which are high-activity composite oxides with heat-resistant ceramic balls, and are obtained by controlling the sizes of the heat-resistant ceramic balls and the coating ratio of an active ingredient. Due to the adopted method, not only is the running period of the acrylic acid device prolonged, but also the production device has relatively high reaction efficiency.

Description

Technical field: [0001] The invention relates to the gas-phase catalytic oxidation of propylene to produce acrolein and acrylic acid, and provides a method for prolonging the operation period of an acrylic acid device. Background of the invention: [0002] The technology of producing acrolein and acrylic acid by the gas phase contact method has been developed into a relatively complete two-step process through continuous innovation by the majority of engineers, that is, propylene and gas containing molecular oxygen generate acrolein and propylene in the first oxidation reactor The aldehyde is further oxidized to acrylic acid in the second reactor in series. The two reactors are filled with different catalysts, the first reactor is mainly Mo-Bi-Fe-O composite oxide catalyst, and the second reactor is filled with Mo-V-W-O catalyst. [0003] However, there are various problems in the process of using this catalyst to produce acrolein and acrylic acid in industry, one of which ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C27/14C07C51/25C07C45/35C07C57/05C07C47/22B01J23/887B01J33/00
CPCC07C45/35C07C51/252B01J23/002B01J23/8876B01J33/00B01J37/0215B01J2523/842B01J2523/845B01J2523/847B01J2523/54B01J2523/68B01J35/51C07C57/04C07C47/22
Inventor 孙彦民曾贤君于海斌李晓云张学斌周鹏隋云乐李世鹏杨文建谢献娜
Owner CHINA NAT OFFSHORE OIL CORP
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