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Catalyst for preparing MEK (Methyl Ethyl Ketone) by carrying out dehydrogenation on 2-butanol and preparation method and application thereof

A catalyst and a technology for sec-butanol, which are applied in the field of catalysts for preparing methyl ethyl ketone by dehydrogenation of sec-butanol and the field of preparation thereof, can solve the problems that it is difficult to meet the long-term operation of oxidation regeneration, affect the service life of the catalyst, increase the cost of catalyst preparation, etc. Selectivity, reducing catalyst carbon deposition, and improving the effect of methyl ethyl ketone selectivity

Inactive Publication Date: 2016-08-31
BEIJING INSTITUTE OF PETROCHEMICAL TECHNOLOGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the specific surface area of ​​the catalyst is small, the mechanical strength is low, and it is prone to pulverization after long-term operation, which affects the service life of the catalyst
And the precipitating agent needs to be used in the preparation process, resulting in unenvironmentally friendly acid-base waste liquid
Chinese patent CN 103599786 A "Catalyst and its preparation method for the dehydrogenation of sec-butanol to methyl ethyl ketone" provides a Cu / SiO 2 Catalyst, using potassium sodium modified catalyst, although the conversion rate and selectivity of sec-butanol dehydrogenation to methyl ethyl ketone have been improved to a certain extent, but its active component content is relatively high, which increases the cost of catalyst preparation, and SiO 2 It is difficult to form as a carrier, and it is not easy for industrial application
In addition, the poor stability of copper-based catalysts due to high-temperature sintering has been difficult to meet the requirements of oxidation regeneration and long-term industrial operation.

Method used

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  • Catalyst for preparing MEK (Methyl Ethyl Ketone) by carrying out dehydrogenation on 2-butanol and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] I. Catalyst preparation

[0024] Mix 45g of aluminum oxide, 5g of calcium oxide, 1g of magnesium oxide, and 1g of nickel oxide with a nitric acid solution with a mass concentration of 10% to form a ball, then extrude it, and dry it at a temperature of 40-70°C for 4 hours , and then calcined at 540° C. for 4 hours to obtain a catalyst carrier, and the carrier is made into particles with a length of 3-10 mm.

[0025] Weigh 41.10g of copper nitrate trihydrate and 3.84g of boric acid and dissolve them in absolute ethanol, heat and stir in a water bath until completely dissolved, and control the temperature of the water bath to 65±5°C. Immerse the equal volume of the prepared carrier particles in the ethanol solution for about 20 hours, dry at 40-70°C, and calcinate at 540°C for 4 hours to obtain catalyst A.

[0026] II. Catalyst Performance Evaluation

[0027] 10 g of catalyst A prepared above is used for the dehydrogenation of sec-butanol to produce methyl ethyl ketone, ...

Embodiment 2

[0030] I. Catalyst preparation

[0031] Mix 42.5g of aluminum oxide, 7.5g of calcium oxide, 1g of magnesium oxide, and 1g of nickel oxide with a nitric acid solution with a mass concentration of 10% to form a ball, then extrude it, and dry it at a temperature of 40-70°C 2 hours, and then calcined at 540° C. for 4 hours to obtain a catalyst carrier, and the carrier is made into particles with a length of 3-10 mm.

[0032] Weigh 41.10g of copper nitrate trihydrate and 3.84g of boric acid and dissolve them in absolute ethanol, heat and stir in a water bath until completely dissolved, and control the temperature of the water bath to 65±5°C. The carrier particles prepared above were immersed in the ethanol solution in an equal volume for about 20 hours, dried at 40-70°C, and calcined at 540°C for 4 hours to obtain catalyst B.

[0033] II. Catalyst Performance Evaluation

[0034] The dehydrogenation reaction process is the same as in Example 1, and the reaction results are: the co...

Embodiment 3

[0036] I. Catalyst preparation

[0037] Mix 35g of aluminum oxide, 15g of calcium oxide, 1g of magnesium oxide, and 1g of nickel oxide with a nitric acid solution with a mass concentration of 10% to form a ball, then extrude it, and dry it at a temperature of 40-70°C for 2 hours , and then calcined at 540° C. for 4 hours to obtain a catalyst carrier, and the carrier is made into particles with a length of 3-10 mm.

[0038] Weigh 41.10g of copper nitrate trihydrate and 3.84g of boric acid and dissolve them in absolute ethanol, heat and stir in a water bath until completely dissolved, and control the temperature of the water bath to 65±5°C. Immerse the equal volume of the prepared carrier particles in the ethanol solution for about 20 hours, dry at 40-70°C, and calcinate at 540°C for 4 hours to obtain catalyst C.

[0039] II. Catalyst Performance Evaluation

[0040] The dehydrogenation reaction process is the same as in Example 1, and the reaction results are: the conversion r...

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Abstract

The invention relates to a catalyst for preparing MEK (Methyl Ethyl Ketone) by carrying out dehydrogenation on 2-butanol, and preparation method and application of the catalyst. The catalyst is prepared by taking copper as a main activator, aluminum oxide as a carrier, B2O3 as an assistant and MO as a modifier; the catalyst is prepared from the following components in parts by weight: 5 to 35 parts of CuO, 3 to 15 parts of B2O3, 15 to 92 parts of Al2O3 and 0 to 35 parts of MO, wherein MO is one or more of CaO, MgO and NiO. According to the catalyst, and the preparation method and the application of the catalyst, disclosed by the invention, a tubular fixed bed reactor is adopted, hydrogen reduction is firstly carried out on the catalyst under the condition that the temperature 300 to 350 DEG C, and then a dehydrogenation reaction is carried out by feeding the 2-butanol and enabling the 2-butanol to be in contact with the catalyst, so that not only are the conversion rate of the 2-butanol and the selectivity of the MEK increased, but also the catalyst has high stability; the problems of low activity, easiness in sintering and instability of a copper-based catalyst are solved.

Description

technical field [0001] The invention belongs to the technical field of catalysts for preparing methyl ethyl ketone by dehydrogenation of sec-butanol, and in particular relates to a catalyst for preparing methyl ethyl ketone by dehydrogenation of sec-butanol and its preparation method and application. Background technique [0002] The catalysts used in the dehydrogenation of sec-butanol to prepare methyl ethyl ketone are mainly copper-based catalysts, such as: Cu / ZnO, Cu / Al 2 o 3 , Cu / ZrO 2 、Cu-ZnO / Al 2 o 3 , Cu / SiO 2 and Cu / Cr 2 o 3 Wait. However, due to its carrier Al 2 o 3 and SiO 2 The acidic site of the alcohol easily leads to the dehydration of the alcohol to form an alkene and the condensation of a ketone to form a high-carbon ketone, which reduces the reaction selectivity, although ZrO 2 At the same time, it has acidity, alkalinity and redox, and has obvious advantages as a copper-based catalyst carrier, but its comparative area is small and its thermal sta...

Claims

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Application Information

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IPC IPC(8): B01J23/78C07C45/00C07C49/10
CPCB01J23/002B01J23/78B01J2523/00C07C45/002
Inventor 姚志龙张岳娇胡彬马松孙培永张胜红
Owner BEIJING INSTITUTE OF PETROCHEMICAL TECHNOLOGY
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