Catalytic conversion process for petroleum hydrocarbons
A catalytic conversion method and technology for petroleum hydrocarbons are applied in the field of catalytic conversion of petroleum hydrocarbons to increase the production of propylene and BTX, which can solve the problems of unachieved and limited increase, and achieve fast recovery, increase octane number, and make up for octane number. effect of loss
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Embodiment 1
[0046] This example shows that the method provided by the invention can significantly increase the yield of propylene, and at the same time increase the content of BTX in gasoline products.
[0047] The test was carried out on a medium-sized catalytic conversion device modified according to the method of the present invention, and the structure diagram of the reaction and regeneration part is shown in Fig. 1 . The physicochemical properties of the petroleum hydrocarbon raw materials used in the test are shown in raw material a in Table 1. The catalyst used was industrially produced by the Catalyst Factory of Qilu Petrochemical Branch of China Petroleum and Chemical Corporation, and the trade name was RMP. The physical and chemical properties are shown in Table 2. See feedstock A in Table 3 for the weight composition of the C4 fraction used. The main operating conditions and product conditions are shown in Table 4.
[0048] The test procedure is as follows: the raw material a...
Embodiment 2
[0051] This example shows that the method provided by the invention can significantly increase the yield of propylene, and at the same time increase the content of BTX in gasoline products.
[0052] The test was carried out on a medium-sized catalytic conversion device modified according to the method of the present invention, and the structure diagram of the reaction and regeneration part is shown in Fig. 1 . The physicochemical properties of the petroleum hydrocarbon raw materials used in the test are shown in Table 1, raw material b. The catalyst used is the same as in Example 1. See feedstock B in Table 3 for the weight composition of the C5 fraction used. The main operating conditions and product conditions are shown in Table 5.
[0053]The test procedure is as follows: the raw material b in Table 1 is preheated and then injected into the reaction zone A of the riser to contact and react with the regenerant in it, and the resulting reaction oil gas and catalyst mixture ...
Embodiment 3
[0056] This example shows that the method provided by the invention can significantly increase the yield of propylene, and at the same time increase the content of BTX in gasoline products.
[0057] The test was carried out on a medium-sized catalytic conversion device modified according to the method of the present invention, and the structure diagram of the reaction and regeneration part is shown in Fig. 1 . The physicochemical properties of the petroleum hydrocarbon raw materials used in the test are shown in Table 1, raw material b. The catalyst used is the same as in Example 1. See feedstock C in Table 3 for the weight composition of the C4-C5 cuts used. The main operating conditions and product conditions are shown in Table 6.
[0058] The test procedure is as follows: the raw material b in Table 1 is preheated and then injected into the reaction zone A of the riser to contact and react with the regenerant in it, and the resulting reaction oil gas and catalyst mixture ...
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