Catalytic cracking processing method of shale oil
A catalytic cracking and shale oil technology, applied in the field of efficient utilization of shale oil resources, can solve the problems of high content and low conversion efficiency, and achieve the effect of simple operation, high conversion rate and short process
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Embodiment 1
[0064] This example follows figure 1 The process of the test was carried out, and the shale oil A shown in Table 1 was used as the raw material for catalytic cracking, and the test was carried out on a fixed-bed reactor. The two reactors were placed in parallel, and the diameter of the bottom of the reactor was expanded. Molten salt is used as a cooling medium to cool the catalyst (adsorbent, using CAT-1 catalyst). After being preheated at 200°C, the shale oil enters the bottom of the adsorption zone where the diameter of the fixed bed reactor expands (the inner diameter of the reactor in the adsorption zone is twice the inner diameter of the reactor in the cracking zone, and the length of the reactor in the adsorption zone is 2 times that of the reactor in the cracking zone. 30% of the length of the reactor in the above-mentioned cracking zone), along with the water vapor flow medium flowing from bottom to top, the adsorption reaction is carried out under the conditions of 28...
Embodiment 2
[0078] In this embodiment, shale oil B is used as a raw material for catalytic cracking, and the test is carried out on a fixed-bed reactor. Two reactors are placed in parallel in parallel, and the diameter of the upper part of the reactor is expanded (the inner diameter of the reactor in the adsorption zone is the diameter of the cracking zone. 5 times of the inner diameter of the reactor, the length of the reactor in the adsorption zone is 30% of the length of the reactor in the cracking zone), and the heat-taking coil is set and adopts molten salt as the cooling medium to cool the catalyst (adsorbent, adopts CAT -1 catalyst). After being preheated at 300°C, shale oil B enters the top of the adsorption zone where the diameter of the fixed bed reactor expands, and flows from bottom to top along with the water vapor flow medium. The adsorption reaction is carried out under the condition that the adsorption time is 6 minutes, and impurities such as basic nitrogen compounds, sul...
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