Method for improving selectivity of catalyst
A catalyst and selective technology, applied in chemical instruments and methods, catalyst activation/preparation, catalyst regeneration/reactivation, etc., can solve problems such as economic uneconomical, achieve easy implementation, decrease olefin hydrogenation saturation activity, and improve selectivity sexual effect
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Embodiment 1
[0039] Using fresh A and B catalysts, the loading volume ratio of A and B catalysts in the reactor is A:B=85:15. The catalysts A and B in the reactor are vulcanized. After the vulcanization is over, the gas in the reaction system is adjusted to be a catalytic gas. In the catalytic gas, the volume fraction of hydrogen is 80%, H 2 The volume fraction of S is 1.5%, and the catalytic raw material is introduced into the reaction system, and the hydrogen partial pressure is 1.6MPa under the catalytic condition; the hydrogen-oil ratio is 100Nm 3 / m 3 ;Volume space velocity 4.0h -1 ; After contacting with the catalyst for 48h under the condition of reaction temperature 360°C. The distillation range of the catalytic raw material is 30-350°C, wherein the volume fraction of olefins is 30%.
[0040] Then adjust to normal reaction conditions, switch the catalytic raw material to gasoline raw material, and switch the gas in the reactor to hydrogen-rich gas. Based on the whole hydrogen-ri...
Embodiment 2
[0043] Adopt fresh A catalyst to sulfide the A catalyst in the reactor. After the sulfidation is over, adjust the gas in the reaction system to be the catalyzing gas. In the catalyzing gas, the volume fraction of hydrogen is 82%, H 2 The volume fraction of S is 1.0%, the catalytic raw material is introduced into the reaction system, and the hydrogen partial pressure is 1.6MPa under the catalytic condition; the hydrogen-oil ratio is 200Nm 3 / m 3 ;Volume space velocity 4.0h -1 ; Contact with the catalyst for 48 hours at a reaction temperature of 350°C, the distillation range of the catalytic raw material is 30-350°C, wherein the volume fraction of olefins is 25%, and the volume fraction of aromatics is 30%.
[0044] Adjust to normal reaction conditions, switch the catalyzing raw material to gasoline raw material, switch the gas in the reactor to hydrogen-rich gas, take the hydrogen-rich gas as a whole as a benchmark, the volume fraction of hydrogen is 85%, and the volume fracti...
Embodiment 3
[0047] Using fresh A and B catalysts, the loading volume ratio of A and B catalysts in the reactor is A:B=85:15. The A and B catalysts in the reactor are vulcanized. After the vulcanization is over, the gas in the reaction system is adjusted to be the activating gas. In the catalyzing gas, the volume fraction of hydrogen is 85%, H 2 The volume fraction of S is 2.0%, the catalytic raw material is introduced into the reaction system, and the hydrogen partial pressure is 1.6MPa under the catalytic condition; the hydrogen-oil ratio is 100Nm 3 / m 3 ;Volume space velocity 4.0h -1 ; Contact the catalyst for 72 hours at a reaction temperature of 350°C, and the distillation range of the catalytic raw material is 30-350°C, wherein the volume fraction of olefins is 45%, and the volume fraction of aromatics is 25%.
[0048] Adjust to normal reaction conditions, switch the catalyst raw material to gasoline raw material, switch the gas in the reactor to hydrogen-rich gas, take the hydroge...
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