A kind of preparation method of green high-purity thermoplastic phenolic resin
A phenolic resin and thermoplastic technology, applied in the field of green high-purity thermoplastic phenolic resin preparation, can solve the problems of high-concentration phenol-containing waste water, excessive free phenol, difficult to obtain thermoplastic phenolic resin, etc., achieving less free phenol content and reducing free phenol. , the effect of high yield
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Embodiment 1
[0053] A kind of preparation method of green high-purity thermoplastic phenolic resin of the present embodiment, its steps are as follows:
[0054] Take 0.5 moles of phenol as an example to prepare other raw materials used for high-purity thermoplastic phenolic resin and the preparation method comprises the following steps:
[0055] (1), ingredients
[0056] Take 47g of phenol, 9.76g of paraformaldehyde, 15.75g of water, and 0.12g of acetic acid, mix them in a reaction kettle, and stir evenly, that is, the molar ratio of phenol to aldehyde compounds, water, and organic acids is 1:0.65:1.75:0.004; Paraformaldehyde is a low molecular weight polyoxymethylene with a degree of polymerization of 8-100.
[0057] (2), chemical reaction
[0058] The reactant was heated to 90° C. under stirring, and reacted at constant temperature for 4 hours.
[0059] (3), dehydration and granulation of phenolic resin
[0060] Step (2) After the reaction is completed, the reaction product is dehydr...
Embodiment 2
[0074] Take 0.5 moles of phenol as an example to prepare other raw materials used for high-purity thermoplastic phenolic resin and the preparation method comprises the following steps:
[0075] In the batching process step (1) in Example 1, take 47g of phenol, 20.29g of formaldehyde with a mass concentration of 37%, 0g of water, and 0.18g of hydrochloric acid and mix them in the reactor, stir evenly, that is, phenol and aldehyde compounds , water, and inorganic acid in a molar ratio of 1:0.5:0:0.01. Other processing steps are identical with embodiment 1, the productive rate of the thermoplastic phenolic resin recorded, softening point, free phenol, molecular weight Mw and the waste water volatile phenol in the production process are: productive rate: 96.8%, softening point: 63 ℃, free Phenol: 0.1%, molecular weight Mw: 908, waste water volatile phenol: 0.5mg / L.
Embodiment 3
[0077] Take m-cresol 0.5 mole as an example to prepare other raw materials used for high-purity thermoplastic phenolic resin and the preparation method comprises the following steps:
[0078] In the batching process step (1) among the embodiment 1, get m-cresol 54g, paraformaldehyde 14.26g, water 2.7g, organic acid be any one in oxalic acid or maleic acid or citric acid to be catalyst, phenol and Aldehyde compounds, water, and organic acids are mixed in a molar ratio of 1:0.95:0.3:0.050, respectively placed in a reactor and stirred evenly, and reacted separately. The other processing steps were the same as in Example 1 to obtain 3 kinds of thermoplastic phenolic resins. The yield, softening point, free phenol, molecular weight Mw and waste water volatile phenol in the production process of the thermoplastic phenolic resin prepared with oxalic acid as a catalyst are: yield: 109.7%, softening point: 99 ° C, free phenol: 0.1%, Molecular weight Mw: 3108, waste water volatile phen...
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