Production of ultrafine suspensions of bisphenol, sodium hydroxide and water
First Claim
1. A process for the production of ultrafine suspensions based on 2,2-bis- )-propane (=bisphenol A, "BPA"), sodium hydyroxide and water, characterized in thata) a melt of bisphenol A is combined with sodium hydroxide and water with intensive mixing (mixing energy 0.5 watt/liter),b) a temperature of at least 60°
- C. and at most 90°
C. being established in at most 1 minute after mixing, optionally by cooling, andc) the ratios of bisphenol A to NaOH are selected so that between 1.5 and 2.2 mol NaOH are used per mol bisphenol A and 15 parts by weight to 40 parts by weight of the sum of BPA and NaOH are present per 100 parts by weight water andd) at most 50% of the BPA used, optionally in the form of its alkali metal salt, are precipitated at those temperatures ande) the aqueous solution is subsequently cooled with further vigorous mixing (mixing energy>
0.5 watt/liter) to temperatures of 10 to 35°
C. in times of 1 second to 30 minutes, an opaque ultrafine suspension being formed.
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Abstract
The invention relates to ultrafine suspensions of bisphenol, sodium hydroxide and water for the production of polycarbonates by the two-phase interfacial process. According to the invention, these suspensions are prepared by cooling bisphenolate concentrations near the solubility limit in aqueous sodium hydroxide with intensive mixing at relatively high temperatures and precipitating bisphenolate or more bisphenolate in the form of fine droplets during the cooling process. The ultrafine suspensions provide for a high volume/time yield in the interfacial reaction.
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Citations
1 Claim
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1. A process for the production of ultrafine suspensions based on 2,2-bis- )-propane (=bisphenol A, "BPA"), sodium hydyroxide and water, characterized in that
a) a melt of bisphenol A is combined with sodium hydroxide and water with intensive mixing (mixing energy 0.5 watt/liter), b) a temperature of at least 60° - C. and at most 90°
C. being established in at most 1 minute after mixing, optionally by cooling, andc) the ratios of bisphenol A to NaOH are selected so that between 1.5 and 2.2 mol NaOH are used per mol bisphenol A and 15 parts by weight to 40 parts by weight of the sum of BPA and NaOH are present per 100 parts by weight water and d) at most 50% of the BPA used, optionally in the form of its alkali metal salt, are precipitated at those temperatures and e) the aqueous solution is subsequently cooled with further vigorous mixing (mixing energy>
0.5 watt/liter) to temperatures of 10 to 35°
C. in times of 1 second to 30 minutes, an opaque ultrafine suspension being formed.
- C. and at most 90°
Specification