Continuous production method for 4,6-dinitryl o-sec-butylphenol inhibitor
A technology of o-sec-butylphenol and polymerization inhibitor, applied in 4 fields, can solve problems such as increased production risk, and achieve the effect of reducing the number of operators, reducing the influence of human factors, and reducing the size of the reaction equipment
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[0023] Connect 5 small enamel kettles of 100-500L in series by utilizing the potential difference, and the reaction materials o-sec-butylphenol, sulfuric acid, and nitric acid are set at a molar ratio of sulfuric acid to o-sec-butylphenol of 1:1.2-1.4, nitric acid and o-sec The butylphenol molar ratio is 1:2.2-3.2, and the amount is continuously added to the reactor equipment in sequence through the metered flow rate, and the temperature is controlled by the ice-salt water vapor. 97%-98% o-sec-butylphenol passes through the flowmeter at 0.10-0.25m per hour 3 Enter the R-1 sulfonation tank, and at the same time, 70%-90% sulfuric acid flows at 0.05-0.125m per hour 3 Enter the R-1 sulfonation tank for sulfonation reaction, the temperature is controlled at 40-60°C. It flows into the R-2 sulfonation tank through the potential difference for further reaction, and the temperature is controlled at 70-90°C. Flow into the R-3 tank through the potential difference, and at the same time...
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