Thick oil demulsifier and its prepn
A demulsifier and viscous oil technology, applied in the direction of hydrocarbon oil dehydration/demulsification, petroleum industry, etc., to facilitate industrial production, speed up demulsification and dehydration, and reduce elasticity and viscosity.
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Embodiment 1
[0024] Example 1 Put 120kg of naphthol and 650kg of diethylenetriamine into the reaction kettle, raise the temperature to 80°C, stir evenly, slowly add 230kg of 37% formaldehyde solution dropwise, and the dropping time is 60min. The time is 60 minutes. Then dehydrate at a temperature of 180°C, a pressure of -0.09Mpa, and a reaction time of 180 minutes. After the reaction is completed, a reddish-brown viscous phenolamine resin is obtained. Add 50kg of this phenolic amine resin and 30kg of catalyst (compounded by calcium oxide and silicon dioxide with a weight ratio of 9.5:0.5) into the autoclave, seal it, replace it with nitrogen, raise the temperature and start stirring. When the temperature in the kettle reaches 130-140°C, add 670kg of propylene oxide and 250kg of ethylene oxide, and control the reaction temperature at 160-180°C and the pressure in the kettle at 0.3-0.6MPa. When the proportioning amount of propylene oxide and propylene oxide is added, the reaction is complet...
Embodiment 2
[0025] Example 2 Put 100kg of octylphenol and 650kg of tetraethylenepentamine into the reaction kettle, raise the temperature to 50°C, stir evenly, slowly add 250kg of 40% formaldehyde solution dropwise, the dropping time is 60min, and keep the temperature at 60°C after the addition. The reaction time is 60min. Then dehydrate at a temperature of 100°C and a pressure of -0.08Mpa, and the reaction time is 160 minutes. After the reaction is completed, a reddish-brown viscous phenolamine resin is obtained. Add 130kg of phenolamine resin and 20kg of catalyst (compounded by calcium hydroxide and oxalic acid with a weight ratio of 9:1) into the autoclave, seal and replace with nitrogen, heat up and start stirring, when the temperature in the still reaches 80 At ~90°C, add 590kg of propylene oxide and 260kg of ethylene oxide, control the reaction temperature at 80-100°C and the pressure in the kettle at 0.3-0.6Mpa, when the proportioning amount of propylene oxide and ethylene oxide is...
Embodiment 3
[0026]Example 3 150kg of bisphenol A and 550kg of tetraethylenepentamine were heated up to 70°C, stirred evenly, and 300kg of 35% formaldehyde solution was slowly added for 60 minutes. After the addition, the constant temperature was 80°C, and the reaction time was 60 minutes. Then dehydrate at a temperature of 120°C and a pressure of -0.09Mpa, and the reaction time is 160 minutes. After the reaction is completed, a reddish-brown viscous phenolamine resin is obtained. Add 70kg of phenolamine resin and 20kg of catalyst (compounded by calcium sulfate and tartaric acid with a weight ratio of 9.59:10.5) into the autoclave. After sealing and nitrogen replacement, heat up and start stirring. When the temperature in the autoclave reaches 130~ At 140°C, add 550kg of propylene oxide and 360kg of ethylene oxide, control the reaction temperature at 140-150°C and the pressure inside the kettle at 0.3-0.6Mpa. When the pressure is gradually lowered until it stops falling for 30 minutes, the...
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