A method and system for preparing low-carbon olefins
A low-carbon olefin and cracking furnace technology, which is applied in the fields of hydrocarbon cracking to produce hydrocarbons, processing hydrocarbon oil, and hydrocarbon oil processing products, etc., can solve the problems of easy coking, low low-carbon olefin yield, insufficient crude oil vaporization, etc. Yield, the effect of extending the operating cycle
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Embodiment 1
[0097] use figure 1 The shown system is carried out, wherein the vaporization treatment unit adopts a cyclone separator, and the cracking furnace is a single furnace cracking furnace, which only contains the first radiant section 3 .
[0098] (1) The crude oil after dehydration and desalting is mixed with superheated steam in the first tube group of the convection section of the cracking furnace, and then preheated to obtain preheated crude oil. The weight ratio of superheated steam to crude oil is 0.70:1. The crude oil continues to be heated to 280°C to become the preheated crude oil.
[0099] (2) The temperature of the preheated crude oil is 280°C, and it is sent to a cyclone separator with internal components (the guide vane type cyclone separator is selected in this embodiment) for vaporization treatment to obtain the first vapor phase and the first liquid phase. Mutually. The separation efficiency of the cyclone is 98%, and the liquid phase in the first vapor phase afte...
Embodiment 2
[0109] use figure 1 The system shown is carried out, wherein the vaporization separation unit adopts a cyclone, and the cracking furnace is a single furnace cracking furnace, which only contains the first radiant section 3 .
[0110] (1) The dehydrated and desalted crude oil is mixed with superheated steam in the first tube group 1 of the convection section of the cracking furnace 4, and then preheated to obtain preheated crude oil. The crude oil continues to be heated to 315°C to become the preheated crude oil.
[0111] (2) The temperature of the preheated crude oil is 315°C, and it is sent to the first cyclone separator 5 with internal components (the guide vane type cyclone separator is selected in this embodiment) for vaporization and separation to obtain the first gas phase and the second cyclone separator. a liquid phase. The separation efficiency of the first cyclone separator 5 is 98%, and the liquid phase in the first gas phase after separation is 150 mg / m 3 .
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Embodiment 3
[0120] use figure 1 The system shown is carried out, wherein the vaporization separation unit adopts a cyclone, and the cracking furnace is a single furnace cracking furnace, which only contains the first radiant section 3 .
[0121] (1) The dehydrated and desalted crude oil is mixed with superheated steam in the first tube group 1 of the convection section of the cracking furnace 4, and then preheated to obtain preheated crude oil. The crude oil continues to be heated to 120°C to become the preheated crude oil.
[0122] (2) The temperature of the preheated crude oil is 220°C and the pressure is 0.15MPa, and it is sent to the first cyclone separator 5 with internal components (the guide vane type cyclone separator is selected in this embodiment) for vaporization and separation. a first gas phase and a first liquid phase. The separation efficiency of the first cyclone separator 5 is 98%, and the liquid phase in the first gas phase after separation is 100 mg / m 3 .
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