Process for producing 3,3',5,5'-tetraalkyl-4,4'-biphenol
A manufacturing method, tetraalkyl technology, applied in 3 fields, can solve problems such as prolonged reaction time, achieve the effect of suppressing the increase of reaction time, suppressing the decline of conversion rate, and reducing the amount of waste
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[0076] Hereinafter, although an Example demonstrates this invention, this invention is not limited to the following Example. In addition, the analysis methods of 2,6-xylenol and 3-methylsalicylaldehyde (MSA) in Examples and Comparative Examples are as follows.
[0077] For quantitative analysis of 2,6-xylenol and MSA, a capillary column ("CBP-5" manufactured by J&W Co., Ltd.) packed with phenylmethylpolysiloxane with a crosslinking degree of 5% was used as a column, and as a detector , performed by gas chromatography ("GC-14B" manufactured by Shimadzu Corporation) using a hydrogen flame ionization detector. 20 g of the test material was dissolved in 20 ml of dimethylformamide to prepare and measure the test material, and phenol was used as an internal standard substance. Quantification of 2,6-xylenol by the internal standard method, and for MSA, the purity of 2,6-xylenol quantified by the internal standard method and the areas of the gas chromatograms of 2,6-xylenol and MSA ...
reference example 1
[0079] In a 1L separable flask with a baffle, add 183g of 2,6-xylenol containing a specified amount of 3-methyl salicylaldehyde, 20g of borax, 0.6g of sodium lauryl sulfate, 600g of water, Copper acetate (monohydrate) 6mg (0.03mmol), stirring while heating. Oxygen introduction was started when the content reached 70°C. In the state of keeping the reaction temperature at 70°C and the oxygen partial pressure at 0.01MPaG, keep stirring, monitor the oxygen absorption, and adjust the reaction speed. The results are shown in Table 1 below.
[0080] experiment
Embodiment 1
[0082] 100 parts by weight of a distillation recovery liquid containing 11 weight % of 2,6-xylenol, 89 parts by weight of water, and a small amount of MSA are supplied from the recovery raw material tank to a stainless steel reactor. ), continue to add new raw material 2, 64 parts by weight of 6-xylenol and 42 parts by weight of new water, heat up while stirring. The concentration of MSA contained in 2,6-xylenol (75 parts by weight) in the added reaction liquid was 0.07 parts by weight. When the temperature of the contents reached 60° C., 3.3 parts by weight of borax, 0.13 parts by weight of sodium lauryl sulfate, and 0.004 parts by weight of copper acetate (monohydrate) were added, and the temperature was raised while stirring. When the temperature of the contents reached 70°C, the introduction of oxygen was started. Stirring was continued with the reaction temperature kept at 70°C, and when the oxygen consumption reached the amount of oxidative dimerization of about 85% by ...
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