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Selective hydrogenation desulfurization transmutation method for gasoline

A hydrodesulfurization and selective technology, applied in refining to remove heteroatoms, etc., can solve the problems of hydrogen consumption, gasoline octane number decline, etc., and achieve the effect of reducing losses and good hydrodesulfurization selectivity

Inactive Publication Date: 2008-06-11
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, due to the low degree of branching olefins are easily hydrogenated and saturated into low-octane alkanes during this process
This will not only greatly reduce the octane number of gasoline, but also cause a large amount of unnecessary hydrogen consumption

Method used

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  • Selective hydrogenation desulfurization transmutation method for gasoline

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] Take by weighing 274.2 grams (dry basis) of aluminum oxide hydrate (trade name SB, German Condea company product, wherein gibbsite content 85% by weight) prepared by alkoxy aluminum hydrolysis method, and extrude into a circumscribed circle with a diameter of The 1.4 mm trefoil strip was dried at 120° C. for 4 hours and calcined at 1000° C. for 4 hours to obtain carrier Z1.

[0027] Molybdenum and cobalt are introduced into the carrier Z1 by step-by-step impregnation. First, weigh 5.33 grams of ammonium molybdate, dissolve it into 90 milliliters of solution with 16% by weight of NH3 solution, impregnate 100 grams of carrier Z with this solution for 14 hours, dry at 120°C for 4 hours, and roast at 420°C for 4 hours; after that, weigh 8.94 g of cobalt nitrate was dissolved in water to form 80 ml of solution, impregnated with this solution to impregnate Z1 loaded with molybdenum again, dried at 120° C. for 4 hours, and calcined at 420° C. for 4 hours to obtain catalyst C1....

Embodiment 2

[0030] Take by weighing 200 grams (dry basis) of alumina precursor (prepared by sodium metaaluminate-sodium sulfate method, trade name Changling Dry Rubber Powder, Changling Refinery Catalyst Factory product, wherein gibbsite content 68 weight %), Extruded into a three-lobed strip with a circumscribed circle diameter of 1.4mm on an extruder, dried at 120°C, and calcined at 1050°C for 4 hours to obtain the carrier Z2.

[0031] Molybdenum and cobalt are introduced into the carrier Z2 by step-by-step impregnation. First, weigh 11.1 grams of ammonium molybdate, dissolve it into 90 milliliters of solution with 16% by weight NH3 solution, impregnate 100 grams of carrier Z with this solution for 24 hours, dry at 120°C for 4 hours, and roast at 420°C for 4 hours; after that, weigh 5.0 g of cobalt nitrate was dissolved in water into 80 ml of solution, impregnated with this solution to impregnate Z2 loaded with molybdenum again, dried at 120° C. for 4 hours, and calcined at 420° C. for ...

Embodiment 3

[0033] Weigh 200 grams (dry basis) of the alumina precursor (the same as in Example 2), extrude it into a trilobal strip with a circumscribed circle diameter of 1.4 mm on an extrusion machine, dry it at 120 ° C, and roast it at 1100 ° C for 4 hours to obtain Carrier Z3.

[0034] Molybdenum and cobalt were introduced into the carrier Z3 by step-by-step impregnation. First, take 18.1 grams of ammonium molybdate, dissolve it into 90 milliliters of solution with 16% by weight NH3 aqueous solution, impregnate 100 grams of carrier Z with this solution for 34 hours, dry at 120°C for 4 hours, and roast at 420°C for 4 hours; after that, weigh 14.0 g of cobalt nitrate was dissolved in water to form 80 ml of solution, impregnated with this solution to impregnate Z3 loaded with molybdenum again, dried at 120° C. for 4 hours, and calcined at 420° C. for 4 hours to obtain catalyst C3. The content of cobalt and molybdenum oxides in C3 and the crystal phase of the carrier are listed in Table...

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Abstract

The invention relates to a method for the modification of selective hydrodesulfurization gasoline. The method comprises the steps that under the condition of hydrofining reaction, gasoline fraction oil is contacted with catalyst, the catalyst includes a carrier, and at least one kind of hydrogenation active metal component selected from Group VIB and at least one kind of hydrogenation active metal component selected from Group VIII which are loaded on the carrier, the components are metered through oxide and taken the catalyst as basic reference, the content of Group VIB metal components is 0.5 to 35 wt. percent, the content of Group VIII metal components is 0.1 to 10 wt. percent, the content of the carrier is 55 to 99.4 wt. percent, wherein the carrier includes aluminium oxide having an alpha structure, the specific value of the mole number of Group VIII metal and the mole number sum of the Group VIII metal and the Group VIB metal is 0.05 to 0.6. Compared with the prior method, the method provided through the invention has better hydrodesulfurization selectivity.

Description

technical field [0001] The invention relates to a gasoline upgrading method, in particular to a gasoline selective hydrodesulfurization upgrading method. Background technique [0002] As we all know, air pollution brings serious environmental problems. Excessive engine emissions are one of the main causes of air pollution. In recent years, in order to meet the requirements of protecting the environment, countries around the world have put forward stricter restrictions on the composition of engine fuel in order to reduce the emission of harmful substances. SOx, the combustion product of sulfide in gasoline, is one of the main harmful substances, and it is also one of the main substances that poison the catalyst of the catalytic converter of automobile exhaust gas. The United States requires that by 2006 the sulfur content in gasoline should be lower than 30ppm. In California, USA, as early as 1996, the sulfur content in gasoline was required to be lower than 40ppm. Japan’...

Claims

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Application Information

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IPC IPC(8): C10G45/04
Inventor 李明丰褚阳夏国富聂红石亚华李大东胡云剑习远兵
Owner CHINA PETROLEUM & CHEM CORP