A heavy oil visbreaking equipment and a heavy oil visbreaking method
A technology for heavy oil and equipment, which is only applied in multi-stage serial refining and cracking process treatment, treatment of hydrocarbon oil, petroleum industry, etc. It can solve the problems of prolonging the production cycle and achieve the effect of increasing liquid yield and reducing coking
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[0029] According to the present invention, the heavy oil visbreaking unit can achieve the purpose of the present invention as long as it can achieve the aforementioned purpose. According to a preferred embodiment of the present invention, the heavy oil visbreaking unit c is a spray visbreaking tower, and the spray visbreaking The viscous tower includes an upper straight cylinder reaction zone 21 and a lower cone collection zone 22 connected to each other, a raw material inlet, a product outlet, and an atomizing nozzle 18 arranged on the top of the upper straight cylinder reaction zone 21 and communicated with the raw material inlet;
[0030] Wherein, the upper straight cylinder reaction zone 21 is used for heat exchange between the heavy oil raw material and the gas from the gas deoxygenation unit b to the temperature required for cracking and visbreaking reaction;
[0031] Wherein, the lower cone collection area 22 is used to collect visbreaking residue;
[0032] Wherein, the...
Embodiment
[0102] Three groups of tests were carried out on the heavy oil visbreaking medium-scale test device, namely Example 1, Example 2, and Example 3. The test device flow chart of embodiment sees figure 1 .
[0103] Follow the steps below (eg figure 1 ):
[0104] 1. After the heavy oil is preheated to 150-350°C through the heat exchanger f (200°C in Example 1, 250°C in Example 2, and 280°C in Example 3), it enters from the top of the spray vis-reducing tower, and is sprayed by atomization The nozzle disperses into small droplets of 20-600μm.
[0105] 2. The small droplets are in contact with 400-900°C high-temperature deoxygenation hot air (450°C in embodiment 1, 500°C in embodiment 2, and 600°C in embodiment 3) in the spray vis-reducing tower for 0.01-60min (the embodiment 1 is 600°C). 10min, embodiment 2 is 8min, embodiment 3 is 5min), the liquid droplet takes place thermal cracking reaction rapidly in the hot blast, after the reaction, the remaining viscosity-reducing residu...
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