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Cracking method for hydrogenation of carbon nine and above hydrocarbons

A technology for cracking carbon and catalysts, which is applied in the hydrogenation field of cracking carbon nine and above hydrocarbons, and can solve problems such as high olefin content and poor catalyst stability

Active Publication Date: 2016-05-18
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The technical problem to be solved by the present invention is the technical problem of high olefin content and poor catalyst stability in the cracked carbon nine hydrogenation products existing in the prior art, and a new cracking carbon nine and above hydrocarbon hydrogenation method is provided

Method used

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  • Cracking method for hydrogenation of carbon nine and above hydrocarbons
  • Cracking method for hydrogenation of carbon nine and above hydrocarbons
  • Cracking method for hydrogenation of carbon nine and above hydrocarbons

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] Weigh 30 grams of pseudo-boehmite, 140 grams of θ-alumina, 30 grams of δ-alumina, and 9 grams of scallop powder, mix them, and then add 20 grams of polyvinyl alcohol-containing solution (mass concentration is 5%), the concentration 4.0 grams of 68% nitric acid, 300 ml of aqueous solution, extruded into a clover-shaped carrier with a diameter of 2.5 mm, and the wet strip was passed through 120 o C dried for 4 hours at 750 o C was calcined for 4 hours to obtain carrier Z1. Mix nickel carbonate: ammonium carbonate: ammonia water = 1.0: 1.0: 2.0 in proportion and stir evenly to prepare a solution with a metal nickel content of 10%. Put the carrier Z1 in the solution for equal impregnation, 60 o C drying for 8 hours, 450 o C was calcined for 4 hours to obtain Ni-based catalyst A1. The catalyst composition is shown in Table 1.

[0023] With nitric acid in [H + ] / [AlOOH] under the condition that the molar ratio was 0.25, the pseudo-boehmite powder was peptized for 24 hours...

Embodiment 2

[0028] Weigh 30 grams of pseudo-boehmite, 140 grams of θ-alumina, 60 grams of δ-alumina, 9 grams of scallop powder, 40 grams of silica sol, mix, and then add polyvinyl alcohol-containing solution (mass concentration is 5%) 25 grams, 4.0 grams of nitric acid with a concentration of 68%, 1.5 g of calcium nitrate, 310 ml of aqueous solution, extruded into a clover-shaped carrier with a diameter of 2.5 mm, and wet strips after 120 o C dried for 4 hours at 750 o C roasting for 4 hours. Vector Z2 was prepared. Mix ammonium molybdate: nickel carbonate: ammonium carbonate: ammonia water = 0.02: 1.0: 1.0: 2.0 in proportion and stir evenly to prepare a solution with a metal nickel content of 10% and a molybdenum content of 0.5%, and place the carrier Z2 in the solution Equal impregnation in 60 o C drying for 8 hours, 450 o C was calcined for 4 hours to obtain Ni-based catalyst A2. The catalyst composition is shown in Table 1.

[0029] With nitric acid in [H + ] / [AlOOH] under the c...

Embodiment 3

[0034] Weigh 30 grams of pseudo-boehmite, 140 grams of θ-alumina, 80 grams of δ-alumina, 9 grams of scallop powder, 20 grams of silica sol, mix, and then add polyvinyl alcohol-containing solution (mass concentration is 5%) 25 grams, 4.0 grams of nitric acid with a concentration of 68%, 0.5 g of magnesium nitrate, 310 ml of aqueous solution, extruded into a clover-shaped carrier with a diameter of 2.5 mm, and wet strips after 120 o C dried for 4 hours at 750 o C roasting for 4 hours. Vector Z3 was prepared. Mix nickel carbonate: ammonium carbonate: ammonia water = 1.25: 1.0: 2.0 in proportion and stir evenly to prepare a solution with a metal nickel content of 13%. Put the carrier Z3 in the solution for equal impregnation, 60 o C drying for 8 hours, 450 o C was calcined for 4 hours to obtain Ni-based catalyst A3. The catalyst composition is shown in Table 1.

[0035] With nitric acid in [H + ] / [AlOOH] under the condition that the molar ratio was 0.25, the pseudo-boehmite p...

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Abstract

The invention relates to a cracking C9 and C9+ hydrocarbon hydrogenation method which mainly solves the technical problem that the existing cracking C9 hydrogenation product in the prior art is high in olefin content and poor in catalyst stability. The invention adopts the following technical scheme: two fixed bed hydrogenation reactors are serially connected for treatment of materials, and cracking C9 fractions and hydrogen gas are fed into the reactors containing nickel-based catalyst beds, so that dicyclopentadiene, styrene and derivatives thereof, indene and other unsaturated components in the C9 fractions and the hydrogen gas are in contact with the beds to perform deep hydrogenation on the diolefine and mono olefin. Thus, the technical scheme well solves the problem. The invention can be used for industrial production of cracking C9 and C9+ hydrocarbon hydrotreatment.

Description

technical field [0001] The invention relates to a method for cracking and hydrogenating hydrocarbons with carbon nine and above. Background technique [0002] Cracked carbon nine and above hydrocarbon fractions have unstable composition, high colloid content and many impurities. The cracking of carbon nine and above hydrocarbons contains a large number of polymerizable active components, mainly including styrene and its derivatives, dicyclopentadiene and its derivatives, indene and its derivatives, etc., and As, S, O, N, etc. The high content of impurities and colloids deactivates the catalyst quickly, so the catalyst has to be activated and regenerated frequently. The catalyst system for cracking carbon nine and above hydrocarbons to increase the production of BTX aromatics by hydrodealkylation requires a working temperature of 350-500°C. Such a high reaction inlet temperature will inevitably lead to the rapid polymerization of the active components in the cracked carbon ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G65/06
CPCC10G65/06
Inventor 刘仲能赵多王建强任杰王燕波
Owner CHINA PETROLEUM & CHEM CORP