Catalyst for use in producing lower aliphatic carboxylic acid ester, process for producing catalyst and process for producing lower alphatic carboxylic acid ester using the catalyst
A technology of aliphatic carboxylic acid and carboxylic acid ester, applied in the production of lower aliphatic carboxylic acid esters, catalysts for the production of lower aliphatic carboxylic acid esters, and the field of production of the catalysts, which can solve the problems of no discovery
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Embodiment 1
[0236] To a pressure vessel made of SUS 316L, 50 ml of the catalyst obtained in the preparation method of catalyst 1 was added, and then contact was performed under the contact conditions shown in Table 3. After the contact, the container is cooled to room temperature and the contacted catalyst (hereinafter referred to as "contact catalyst") is drawn out from the container. Subsequently, 40ml of contact catalyst was added to the reaction tube, and then kept at a temperature of 165°C, 0.8MPaG (gauge pressure) for 1,500 hours -1 A mixed gas of ethylene:acetic acid:steam:nitrogen (=78.5:8.0:4.5:9.0, volume ratio) was introduced into the GHSV to perform the reaction. The gas passing through the catalyst layer is collected under ice cooling for a predetermined time, and then the entire amount of condensed components (hereinafter referred to as "condensed solution") is recovered and analyzed. The gas flow rate of the outlet gas that remains uncondensed (hereinafter referred to as "uncon...
Embodiment 2 and 3
[0239] In the same manner as in Example 1, 50 ml of the catalyst obtained in the preparation method of catalyst 1 was added to a pressure vessel made of SUS 316L, and contacted under the contact conditions shown in Table 3. After that, the catalyst was drawn out, added to the reaction tube, and then reacted in the same manner. The results are given in Table 3.
Embodiment 4
[0241] 40 ml of the catalyst obtained in the preparation method of catalyst 2 was added to the reaction tube, and contact was performed under the contact conditions shown in Table 3. Subsequently, at a temperature of 165°C, 0.8MPaG (gauge pressure) and 1,500 hours -1 A mixed gas of ethylene:acetic acid:steam:nitrogen (=78.5:8.0:4.5:9.0, volume ratio) was introduced into the GHSV to perform the reaction. The results of the reaction are given in Table 3.
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Abstract
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