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Catalyst for synthesizing methyl formate and preparation method of catalyst for synthesizing methyl formate

A technology of methyl formate and catalyst, which is applied in the field of methyl formate synthesis catalyst and its preparation method, can solve problems such as loss, and achieve the effects of easy operation, simple preparation and good methanol dehydrogenation performance

Active Publication Date: 2014-07-09
SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Patent EP 2329881 recently discloses a kind of methanol dehydrogenation with copper-zinc-aluminum as the main active component to prepare methyl formate, emphasizing the good stability of the catalyst, but the published data shows that the catalyst is prepared according to the method described and in the Tested at 280°C, the catalyst activity lost about 30% after about 1000 hours. Obviously, this is still far from the requirements of industrial applications.

Method used

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  • Catalyst for synthesizing methyl formate and preparation method of catalyst for synthesizing methyl formate

Examples

Experimental program
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Effect test

Embodiment 1

[0024] 12.39g ammonium heptamolybdate ((NH 4 ) 6 Mo 7 o 24 4H 2 O) broken into particles below 0.5 mm, and calcined at 400° C. for 2 hours to obtain a carbide precursor. Using the mixed gas of methane and hydrogen as the carbonization medium (the volume ratio of methane and hydrogen is 1:4), in a fixed bed reactor, 0.1MPa, 10000h -1 The temperature-programmed carbonization treatment was carried out on the precursor under the condition of space velocity. The temperature-rising program was as follows: increase from room temperature to 750 °C at a rate of 5 °C / min, stay for 3 hours, and then cool down to room temperature naturally. At room temperature, the carbonized sample was passivated by using air and argon to configure a passivation gas with an oxygen volume concentration of 5.0%. The passivation time was 6 hours, and 7.1 g of metal carbides were obtained.

[0025] According to the molar ratio of K and Mo of 0.15:1, an appropriate amount of potassium nitrate was weighed...

Embodiment 2

[0028] 13.93g ammonium dimolybdate ((NH 4 ) 2 Mo 2 o 7 ) into particles below 0.8mm, and calcined at 700°C for 3 hours to obtain a carbide precursor. Using the mixed gas of ethane and hydrogen as the carbonization medium (the volume ratio of ethane and hydrogen is 1:6), in a fixed bed reactor, 1.0MPa, 11000h -1 Under space velocity conditions, the precursor was subjected to temperature-programmed carbonization treatment. The temperature-rising program was as follows: increase from room temperature to 675 °C at a rate of 1 °C / min, stay for 4 hours, and then cool down to room temperature naturally. At room temperature, the carbonized sample was passivated by configuring a passivation gas with an oxygen volume concentration of 1.0% with oxygen and argon. The passivation time was 5 hours, and 7.1 g of metal carbides were obtained.

[0029] According to the molar ratio of Fe and Mo of 0.8:1, an appropriate amount of iron nitrate was weighed and mechanically mixed with the obtai...

Embodiment 3

[0031] 13.33 ammonium tungstate ((NH 4 ) 10 h 2 (W 2 o 7 ) 6 ) into particles below 1.0mm, and calcined at 800°C for 4 hours to obtain a carbide precursor. Using the mixed gas of ethane, ethylene and hydrogen as the carbonization medium (the volume ratio of (ethane+ethylene) and hydrogen is 1:5), in a fixed bed reactor, 0.6MPa, 13000h -1 The temperature-programmed carbonization treatment was carried out on the precursor under the space velocity condition. The temperature-rising program was as follows: increase from room temperature to 1000 °C at a rate of 4 °C / min, stay for 1 h, and then cool down to room temperature naturally. At room temperature, oxygen and helium were used to prepare a passivation gas with an oxygen volume concentration of 3.0% to passivate the carbonized sample. The passivation time was 5 hours, and 10.0 g of metal carbide was obtained.

[0032] Weigh an appropriate amount of sodium bicarbonate and mechanically mix it with the obtained metal carbide ...

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Abstract

The invention relates to a catalyst for synthesizing methyl formate. The catalyst is composed of a VIB-group metal carbide and an assistant metal compound. According to the molar ratio of metal elements in the metal carbide and the assistant metal compound, the catalyst has the molar composition of the amount of substance of the metal element in the assistant metal compound to the amount of substance of the metal element in the VIB-group metal carbide being (0.04-0.8):1.0. The catalyst for synthesizing methyl formate has the advantages of good temperature tolerance and stable performances.

Description

technical field [0001] The invention relates to a catalyst for synthesizing methyl formate and a preparation method thereof, in particular to a catalyst for catalyzing methanol dehydrogenation to produce methyl formate and a preparation method thereof. technical background [0002] Methyl formate is an important chemical intermediate. The process of methanol dehydrogenation to prepare methyl formate is simple, easy to operate, non-corrosive, less investment in equipment, hydrogen by-product, and is a production route with important industrial significance. But methanol dehydrogenation to methyl formate is an endothermic reaction controlled by thermodynamics. Under the rated liquid air, the single-pass yield (the product of methanol conversion and methyl formate selectivity) is limited, so it is necessary to increase the liquid air and reaction Temperature increases the space-time yield of methyl formate (the amount of methyl formate generated per unit time and unit amount o...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/22C07C69/06C07C67/40
Inventor 李德宝陈从标肖勇
Owner SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI