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A kind of C2 pre-hydrogenation catalyst containing composite carrier and preparation method thereof

A composite carrier and catalyst technology, which is applied in the direction of hydrogenation hydrocarbon production, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problem of low dispersion of catalyst active component Pd, specific surface and pore size distribution not suitable for catalyst requirements, catalyst The problem of high surface acidity can improve the ability of anti-heavy metal poisoning, the surface acidity is low, and the effect of avoiding the reduction of activity is achieved.

Active Publication Date: 2014-10-15
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] In the prior art, the carrier with bimodal pore size distribution is used to prepare carbon dioxide pre-hydrogenation catalysts, and there are defects that the specific surface and pore size distribution do not meet the requirements of the catalyst, resulting in a low dispersion of the active component Pd of the catalyst, or a high acidity on the surface of the catalyst Shortcomings

Method used

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  • A kind of C2 pre-hydrogenation catalyst containing composite carrier and preparation method thereof
  • A kind of C2 pre-hydrogenation catalyst containing composite carrier and preparation method thereof
  • A kind of C2 pre-hydrogenation catalyst containing composite carrier and preparation method thereof

Examples

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Effect test

Embodiment 1

[0046] Under stirring, containing 1286g NaAlO 2 solution and containing 950g of TiCl 4 The solution was mixed at 50°C, then neutralized with NaOH solution, aluminum-titanium hydroxide co-precipitated, stirred for 10 hours to make the aluminum-titanium hydroxide form uniform fine particles, filtered and washed with distilled water to remove Na + and Cl - ions, adding 7.65% citric acid as a pore-expanding agent, extruding after kneading to make a Φ4mm strip, drying at 120°C for 4 hours and then roasting at 1250°C for 5 hours to obtain the composite carrier S-1 of alumina and titania, where α -Al 2 o 3 and TiO 2 The weight ratio is 8:2, the bulk density is 0.87g / ml, the pore volume is 0.502ml / g, and the specific surface area is 18.9m 2 / g (mercury intrusion method), the carrier has a bimodal distribution at 90nm and 410nm, and the average pore size is 176nm. The carrier pore size distribution is as follows: less than 10nm is 0.19%; 10-100nm is 71.11%; greater than 100nm but...

Embodiment 2

[0048] 700g of alumina, 150g of titanium oxide, 20g of citric acid and 30g of carbon black were stirred in a mechanical stirrer, extruded into strips of Φ4.2mm, dried at 110°C for 5 hours, and then calcined at 1250°C for 4 hours to obtain Aluminum oxide and titanium oxide mixed carrier, pore volume 0.419ml / g, bulk density 0.92g / ml, specific surface area 14.5m 2 / g; the carrier has a bimodal distribution at 110nm and 520nm, and the average pore size is 273nm; the carrier pore size distribution is as follows: 0.10% for less than 10nm; 63.06% for 10-100nm; 36.66% for greater than 100nm and less than or equal to 1000nm; 0.18% for greater than 1000nm . The carrier pore size distribution diagram is detailed in figure 2 .

Embodiment 3

[0050] Under stirring, containing 402g NaAlO 2 solution and containing 1187g of TiCl 4 The solution was mixed at 50°C, then neutralized with KOH solution, aluminum-titanium hydroxide co-precipitated, stirred for 10 hours to make the aluminum-titanium hydroxide form uniform fine particles, and the product was filtered and washed with deionized distilled water to remove Na + and Cl - ions, adding 15% polyvinyl alcohol as a pore-expanding agent, rolling the ball after kneading, drying at 130°C for 2h and then calcining at 1350°C for 6 hours to obtain a composite carrier of alumina and titania, in which α-Al 2 o 3 and TiO 2 The weight ratio is 5:5, the bulk density is 1.03g / ml, the pore volume is 0.357ml / g, and the specific surface area is 7.5m 2 / g, the carrier has a bimodal distribution at 125nm and 760nm, and the average pore size is 360nm. The carrier pore size distribution is as follows: less than 10nm is 0%; 10-100nm is 58.50%; greater than 100nm and less than or equal ...

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Abstract

The invention relates to a C2 front-end hydrogenation catalyst containing a composite carrier, the C2 front-end hydrogenation catalyst comprises the following components by taking the mass of the carrier as 100%, 0.02-0.15 parts of palladium and silver, the mass ratio of silver to palladium is 9-1:1, by taking element mass of palladium and silver, the carrier of the catalyst is an alumina-titanium oxide composite carrier with two peaks distribution. by calculating the carrier mass as 100%, the carrier comprises 1-95% of alumina and 5-99% of titanium oxide, and the carrier has the following physical properties: the bulk density is 0.7 to 1.1g / ml, the pore volume is 0.2 to 0.6ml / g, the specific surface area is 3 to 60m<2> / g, the average pore size is 80 to 400nm, 20-370nm preferably; and the carrier has two peaks when the pore size is 60 to 130nm and 400 to 800nm. The invention also discloses the preparation method of the hydrogenation catalyst.

Description

technical field [0001] The invention relates to a catalyst and a preparation method thereof, in particular to a catalyst containing alumina-titania composite oxide as a carrier and a preparation method thereof. Background technique [0002] The pyrolysis gas produced in the steam cracking process of petroleum hydrocarbons often contains a small amount of impurities such as acetylene, propyne and propadiene, and their existence will affect the high-efficiency polyethylene and polyethylene used in the homogeneous polymerization and copolymerization processes in the subsequent sections to varying degrees. Propylene catalyst. According to the requirements of polyethylene, ethylene propylene rubber, polypropylene and other post-processing procedures, the mole fraction of acetylene in polymer grade ethylene must be lower than 5ppm, and the mole fraction of acetylene in ethylene must be lower than 1ppm in the production of ethylene glycol. Catalytic selective hydrogenation is the ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/50B01J23/66B01J35/10C07C7/163C07C7/167C07C5/09C07C5/05C07C11/04C07C11/06
CPCY02P20/52
Inventor 梁玉龙谭都平梁琨车春霞李赫韩伟高源景喜林张峰常晓昕颉伟黄德华林宏钱颖李晓银付含琦
Owner PETROCHINA CO LTD