A process for sulfonating mixtures of long-chain olefins and alkanes with sulfur trioxide gas
A technology for sulfonating long-chain olefins and alkane mixtures, applied in chemical/physical processes, organic chemistry, sulfonic acid preparation, etc., can solve problems such as long time, poor safety, and high energy consumption, and achieve simple methods and short processes Effect
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Embodiment 1
[0032] Example 1: The C14-18 internal olefin / alkane mixture (olefin content 10% (w / w)) from the dehydrogenation of normal paraffins enters the sulfonation reactor from the upper part of the membrane sulfonator, and the feed temperature is 15 ° C. The amount of material is 40Kg / tube, and the sulfur trioxide / air mixed gas from the oleum stripping method also enters the sulfonation reactor from the upper part of the membrane sulfonator, and the SO 3 The gas concentration is 3% (V / V), olefin and SO 3 The molar ratio is 1:1.0, and the cooling water temperature of the sulfonator jacket is 15°C. The two flow down, and the sulfonation reaction occurs. The reaction product leaves from the lower part of the membrane sulfonator and enters the gas-liquid separator to be divided into a liquid phase and a gas phase. The gas phase is the sulfonated tail gas, and the liquid phase is the sulfonation of alkanes and olefins. mixture of products. The sulfonated tail gas is evacuated after cyclo...
Embodiment 2
[0034] The C18-28α-olefin / alkane mixture (olefin content 40% (w / w)) obtained from the rectification of Fischer-Tropsch synthetic oil enters the sulfonation reaction tube from the upper part of the membrane sulfonator, the feed temperature is 35°C, and the feed amount The sulfur trioxide / air mixture from the sulfur combustion method also enters the sulfonation reaction tube from the upper part of the membrane sulfonator, and the SO 3 The gas concentration is 7% (V / V), olefin and SO 3 The molar ratio is 1:1.2, and the cooling water temperature of the jacket of the sulfonator is 65°C. The two flow down, and the sulfonation reaction occurs. The reaction product leaves from the lower part of the membrane sulfonator and enters the gas-liquid separator to be divided into a liquid phase and a gas phase. The gas phase is the sulfonated tail gas, and the liquid phase is the sulfonation of alkanes and olefins. mixture of products. The sulfonated tail gas is evacuated after cyclone sepa...
Embodiment 3
[0036] The C15-C18α-olefin / alkane mixture (olefin content 60% (w / w)) obtained by the rectification of Fischer-Tropsch synthetic oil enters the sulfonation reactor from the upper part of the membrane sulfonator, the feed temperature is 25°C, and the feed amount The sulfur trioxide / air mixture from the sulfur combustion method also enters the sulfonation reactor from the upper part of the membrane sulfonator, and the SO 3 The gas concentration is 5.8% (V / V), olefin and SO 3The molar ratio is 1:1.15, and the cooling water temperature of the jacket of the sulfonator is 45°C. The two flow down, and the sulfonation reaction occurs. The reaction product leaves from the lower part of the membrane sulfonator and enters the gas-liquid separator to be divided into a liquid phase and a gas phase. The gas phase is the sulfonated tail gas, and the liquid phase is the sulfonation of alkanes and olefins. mixture of products. The sulfonated tail gas is evacuated after cyclone separation, con...
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