Method for reducing coking of cracking device
A cracking device and cracking furnace technology, applied in cracking, non-catalytic thermal cracking, petroleum industry, etc., can solve the problems of complex operation, toxic raw materials, etc., achieve the effects of inhibiting coking, convenient operation, and prolonging the operation cycle
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Embodiment 1
[0035]The cracking furnace tube was heat treated on the 200g / h laboratory ethylene cracking evaluation device. The furnace tube is made of 0Cr25Ni20 stainless steel. In the heat preparation stage, under normal pressure, 100g / h of 600°C water vapor carries 100ppm of silicon-containing organic compounds (tetraethoxysilane) and polysulfide organic compounds (di-tert-butyl polysulfide) into the cracking furnace , where the molar ratio of Si to S is 3:1, heat treatment at 750°C for 2h. After the experiment, the cracking furnace tube was evacuated by introducing nitrogen gas, and then the cracking furnace tube was rapidly heated to 860°C for the cracking experiment. Ethane feed 100g / h, water feed 30g / h, residence time 0.4s, cracking time 2h. After the end of the cracking experiment, evacuate with nitrogen, and use N 2 and O 2 The mixed gas is burned, and the CO and CO in the burnt gas are measured online with an infrared analyzer 2 Concentration, record the volume of charred ga...
reference example 1
[0037] In this reference example, no treatment was done to the furnace tube, and the pyrolysis was carried out according to the method in Example 1, and the amount of coking during the pyrolysis operation was tested. The amount of coke obtained is shown in Table 1.
Embodiment 2
[0041] The furnace tube is treated with reference to the method of Example 1, the difference is that 100 g / h of 600 ° C steam carries 300 ppm of silicon-containing organic compounds (tetraethoxysilane) and polysulfur organic compounds (di-tert-butyl polysulfide) thing), the rest are the same as in Example 1. The amount of coke obtained is shown in Table 1.
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