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Saturated hydrogenation method for C5 fraction

A distillate and hydrogenation catalyst technology, which is applied in the field of hydrogenation of C5 distillate saturated hydrocarbons, can solve the problem of diolefins not having hydrogenation selectivity, etc., and achieve the goals of improving anti-colloid ability, high hydrogenation selectivity, and reducing coking process Effect

Active Publication Date: 2019-04-26
兰州金润宏成新材料科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The catalyst can be used for hydrofining of middle and low distillate oils. It can hydrogenate saturated monoolefins to the greatest extent while hydrodesulfurizing. It can meet the requirements of oil products with variable sulfur content and high space velocity, but it has no effect on diolefins. Hydrogenation selectivity

Method used

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  • Saturated hydrogenation method for C5 fraction

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] (1) Preparation of silica-alumina composition 1

[0031] 1. Preparation of nickel-containing magnesium aluminate LaMgAl 11 o 19 The process is as follows:

[0032] Take 7.8 grams of basic magnesium carbonate, 25 grams of lanthanum carbonate and 70.5 grams of aluminum hydroxide, mix well, add deionized water to form a highly dispersed suspension, then add 8 grams of nickel nitrate, spray dry, and dry at 140 ° C for 5 hours. and placed in an air atmosphere at 1300° C. for 4 hours and then ball milled for 18 hours to obtain nickel-containing magnesium lanthanum aluminate powder. The nickel-containing magnesium-lanthanum aluminate powder is added with water, and the highly dispersed nickel-containing magnesium-lanthanum aluminate slurry is obtained after ultrasonic vibration.

[0033] 2. Preparation of silica-alumina composition

[0034] Take 140g of pseudo-boehmite and 22g of scallop powder, mix evenly, add dilute nitric acid, then add 20g of sodium polyacrylate nitric...

Embodiment 2

[0038] (1) Preparation of silica-alumina composition 2

[0039] The preparation of nickel-containing magnesium lanthanum aluminate is the same as in Example 1, the preparation of the silica-alumina composition is the same as in Example 1, and 70% of pseudo-boehmite is mixed evenly with celadon powder, and the pore-enlarging agent 1 is polyvinyl alcohol. The added amount accounts for 22% of the mass of the added alumina, and the added amount of the pore expander 2 chitosan accounts for 5% of the added mass of the alumina and silicon oxide. The silica-alumina composition contains 4.9wt% silica and 6.5wt% nickel-containing magnesium lanthanum aluminate.

[0040] (2) Preparation of catalyst

[0041] The preparation method of the catalyst was the same as that in Example 1. The polyacrylic acid and the silica-alumina composition powder were mixed uniformly in a ratio of 1.8:1 by volume. The composition of the catalyst was shown in Table 1.

Embodiment 3

[0043] (1) Preparation of silica-alumina composition 3

[0044] The preparation of nickel-containing magnesium lanthanum aluminate is the same as in Example 1, the preparation of the silica-alumina composition is the same as in Example 1, and 65% of pseudo-boehmite is mixed evenly with squat powder, and the pore-enlarging agent 1 is polyacrylate The added amount accounts for 17% of the mass of the added alumina, and the added amount of the pore-enlarging agent 2 methylcellulose accounts for 3.7% of the added mass of the alumina and silicon oxide. The silica-alumina composition contained 6.2 wt% of silica and 7.8 wt% of nickel-containing magnesium lanthanum aluminate.

[0045] (2) Preparation of catalyst

[0046] The preparation method of catalyst 3 was the same as that in Example 1. Sodium polyacrylate was added to dilute nitric acid and mixed evenly with the silica-alumina composition powder at a volume ratio of 1.5:1. The composition of the catalyst was shown in Table 1.

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Abstract

The invention relates to a saturated hydrogenation method for a C5 fraction. Alkyne and diene in C5 fraction saturated hydrocarbon are hydrogenated to corresponding alkane by using a nickel-based saturated hydrogenation catalyst, and the catalyst is prepared from active components of molybdenum, nickel, cobalt, and magnesium and a silicon oxide-aluminum oxide composition. According to the reactionprocess conditions, the reactor inlet temperature is 30-55 DEG C, the reaction pressure is 1.0-4.5 MPa, the liquid volume space velocity is 1.5-4.5 h<-1>, and the volume ratio of hydrogen to oil is (120 to 450): 1. According to the saturated hydrogenation method for the C5 fraction, the used catalyst has high hydrogenation activity and good stability.

Description

technical field [0001] The present invention relates to a C 5 Distillate saturated hydrocarbon hydrogenation method, industrial C 5 Alkynes and diolefins in the distillate are hydrogenated to corresponding alkanes. Background technique [0002] C 4 、C 5 The distillate contains more diolefins. At a certain reaction temperature, the diolefins will not only polymerize themselves, but also react with other hydrocarbons to form coking precursors such as colloids. While hydrogenation removes diolefins in raw oil, it can avoid or reduce olefin polymerization reaction. Steam cracking to ethylene and refineries by-product a large amount of C 4 、C 5 Distillate, its yield and composition vary with the type of cracking raw material, cracking depth and cracking process. where C 4 、C 5 After the diolefins are separated from hydrocarbons and used as chemical raw materials, the rest is used in the fields of alkylate oil, petroleum resin, etc. The excess can only be used as fuel, an...

Claims

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Application Information

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IPC IPC(8): C10G45/36B01J23/887
CPCB01J23/002B01J23/882B01J23/8872B01J23/8873B01J2523/00C10G45/36B01J2523/22B01J2523/31B01J2523/3706B01J2523/41B01J2523/68B01J2523/845B01J2523/847B01J2523/15B01J2523/27
Inventor 肖真勇
Owner 兰州金润宏成新材料科技有限公司