Mild hydrogenation purifying method for coal direct liquefaction oil
A technology of direct coal liquefaction and hydrogenation upgrading, which is applied in the fields of hydrogenation treatment process, preparation of liquid hydrocarbon mixture, petroleum industry, etc., can solve the problems of high one-time investment and complicated process, and achieve the effect of improving economy
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Embodiment 1
[0040] In this example, coal direct liquefied oil T is used as the raw material, and the basic properties of the raw material are listed in Table 1. It can be seen from Table 1 that the nitrogen content and oxygen content of direct coal liquefaction oil T are relatively high, respectively 2620μg / g and 2.68% by weight, and the density is relatively high, reflecting its high aromatic content. The bromine value is 42.9gBr / 100g, reflecting It contains more olefins.
[0041] In the stable hydrogenation unit, the coal direct liquefied oil T is mixed with hydrogen, enters the stable hydrogenation reactor, and successively contacts the hydrogenation protection agent RGC-1 and the hydrogenation treatment catalyst RTC-32 to react, the hydrogenation protection agent and the hydrogenation treatment The loading volume ratio of the catalyst is 1:4, and the reaction products are separated and fractionated to obtain naphtha fraction and diesel fraction, and the obtained diesel fraction enters...
Embodiment 2
[0044] In this example, direct coal liquefied oil S is used as the raw material, and the basic properties of the raw material are listed in Table 1. In the stable hydrogenation unit, the direct coal liquefied oil S is mixed with hydrogen, enters the stable hydrogenation reactor, and successively contacts the hydrogenation protection agent RGC-1 and the hydrogenation catalyst RTC-32 to react, the hydrogenation protection agent and the hydrogenation treatment The loading volume ratio of the catalyst is 1:6, and the reaction products are separated and fractionated to obtain naphtha fraction and diesel fraction, and the obtained diesel fraction enters the hydroreforming unit, and then enters the hydroreforming reactor after being mixed with hydrogen , and react with the hydrogenation upgrading catalyst RCC-2, and the reaction product is separated and fractionated to obtain a diesel product. The main operating conditions of the stable hydrogenation reactor and the hydroupgrading re...
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