A method and system for preparing light olefins from crude oil
A technology for low-carbon olefins and crude oil, applied in the field of low-carbon olefins preparation, can solve the problems of low yield of low-carbon olefins, insufficient crude oil vaporization, easy coking, etc., achieve high yield, solve insufficient gasification, and prolong operation. effect of cycle
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Embodiment 1
[0077] Example 1 is a method for preparing low-carbon olefins using crude oil
[0078] adopt Figure 1 The system shown is carried out, wherein the vaporization treatment unit employs a cyclone separator.
[0079](1) The dehydrated and desalinated crude oil is mixed with the superheated steam in the first tube group of the convection section of the cracking furnace, and the preheated crude oil is preheated to obtain the preheated crude oil, and the weight ratio of the superheated steam to the crude oil is 0.75:1. Crude oil continues to heat up to 280°C to become preheated crude oil.
[0080] (2) The temperature of the preheated crude oil is 280 ° C, it is fed into a cyclone separator with internal components (the present embodiment selects a guide vane cyclone separator) for vaporization treatment to obtain the first vapor phase and the first liquid phase. The separation efficiency of the cyclone separator is 98%, and the liquid phase in the first steam phase after separation is 26...
Embodiment 2
[0087] adopt Figure 1The system shown is carried out, wherein the vaporization separation unit employs a cyclone separator.
[0088] (1) The dehydrated and desalinated crude oil is mixed with superheated steam in the first convection section of the cracking furnace 4 in group 1, and the preheated crude oil is obtained. Crude oil continues to be heated to 315°C to become preheated crude oil.
[0089] (2) The temperature of the preheated crude oil is 315 ° C, it is fed into the first cyclone separator with an internal member 5 (the present embodiment selects a guide vane cyclone separator) for vaporization separation to obtain the first vapor phase and the first liquid phase. The separation efficiency of the first cyclone separator 5 is 98%, and the liquid phase in the first vapor phase after separation is 150mg / m 3 。
[0090] (3) The first liquid phase is sent to the convection section of the cracking furnace for preheating, preheating to 350 °C, the first liquid phase after preh...
Embodiment 3
[0096]adopt Figure 1 The system shown is carried out, wherein the vaporization separation unit employs a cyclone separator.
[0097] (1) The dehydrated and desalinated crude oil is mixed with superheated steam in the first convection section of the cracking furnace 4 in group 1, and the preheated crude oil is obtained. Crude oil continues to heat to 220°C to become preheated crude oil.
[0098] (2) The temperature of the crude oil after preheating is 220 ° C, it is fed into the first cyclone separator with an internal member 5 (the present embodiment selects a guide vane cyclone separator) for vaporization separation to obtain the first gas phase and the 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 100mg / m 3 。
[0099] (3) The first liquid phase is sent to the convection section of the cracking furnace for preheating, preheating to 260 °C, the first liquid phase after prehea...
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