C2 fraction selective hydrogenation method

A selective hydrogenation and fractionation technology, applied in hydrocarbons, chemical instruments and methods, purification/separation of hydrocarbons, etc., can solve problems such as insufficient loading of active components, impact on catalyst activity, and increase in catalyst cost , to achieve excellent hydrogenation activity and stability

Active Publication Date: 2016-07-13
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Using this patented method, the carrier adsorbs a specific polymer compound through the chemical adsorption of the hydroxyl group of alumina and the polymer, and the amount of the polymer compound adsorbed by the carrier will be limited by the number of hydroxyl groups of alumina; the functionalized polymer and Pd The complexation effect is not strong, and sometimes the loading capacity of the active components does not meet the requirements, and some active components remain in the impregnation solut...

Method used

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  • C2 fraction selective hydrogenation method
  • C2 fraction selective hydrogenation method
  • C2 fraction selective hydrogenation method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0049] Weigh Φ3.4, the specific surface area is 21.0m 2 / g, pore volume 0.31mL / g, bulk density 0.81g / ml spherical α-Al 2 o 3 Carrier 500g.

[0050] Dissolve 52.37g of 4,4-dihydroxy-2,2-bipyridine in 500mL ethanol solution, impregnate the above-mentioned carrier in the above-mentioned solution, and let it stand for 2.5h to make 4,4-dihydroxy-2,2-bipyridine completely After being loaded on the alumina support, it was dried at 80°C for 8 hours to obtain the hydroxyl-bipyridine / Al 2 o 3 Prebody.

[0051] Weigh 0.37gPd(NO 3 ) 2 , 1.47gPb(NO 3 ) 2 Dissolve in 500mL deionized water, slowly add 10mL concentrated nitric acid, stir until completely dissolved, adjust pH to 2.2, and prepare a mixed solution. The above-mentioned hydroxyl-bipyridine / Al 2 o 3 The precursor was added to the prepared solution, stirred for 10 minutes, left to stand for 2.5 hours, and the residue was poured out to obtain PdPb-hydroxy-bipyridine / Al 2 o 3 Precursor (number of moles of hydroxyl-bipyrid...

Embodiment 2

[0068] Weigh Φ3.8mm, height 3.8mm, specific surface area is 54.0m 2 / g, cylindrical θ-Al with a pore volume of 0.46ml / g and a bulk density of 0.69g / ml 2 o 3 Carrier 500g.

[0069] Dissolve 2.01g of 4,4-dihydroxy-2,2-bipyridine in 650mL ethanol solution, immerse the above-mentioned carrier in the above-mentioned solution, and let the dihydroxy-2,2-bipyridine be completely loaded on the alumina carrier after standing for 8 hours After drying at 90°C for 8 hours, the hydroxyl-bipyridine / Al 2 o 3 Prebody.

[0070] Weigh 0.73gPd(NO 3 ) 2 , 4.61gPb(NO 3 ) 2 Dissolve in 650mL deionized water, adjust the pH value to 2.8, and make a mixed solution. The above-mentioned hydroxyl-bipyridine / Al 2 o 3 Add the precursor to the prepared solution, stir for 60 minutes, let stand for 8 hours, pour out the residual liquid, and dry the remaining solid at 100°C for 6 hours to obtain PdPb-hydroxy-bipyridine / Al 2 o 3 Precursor (hydroxyl-bipyridine moles: (Pd+Pb)=1).

[0071] The precurs...

Embodiment 3

[0088] Weigh Φ3.0mm, the specific surface area is 34.0m 2 / g, the pore volume is 0.25ml / g, and the heap ratio is 500g of the toothed spherical carrier of 0.76g / ml, in which Al 2 o 3 460g, titanium oxide 40g, Al 2 o 3 It is a mixed crystal form of θ and α.

[0089] Dissolve 98.45g of 6,6'-dihydroxy-3,3'-bipyridine in 700mL ethanol solution, impregnate the above carrier in the above solution, and let 6,6'-dihydroxy-3,3'- After the bipyridine was completely loaded on the alumina carrier, it was dried at 120°C for 4 h to obtain the hydroxyl-bipyridine / Al 2 o 3 Prebody.

[0090] Weigh 0.40gPd(NO 3 ) 2 ,0.74gPb(NO 3 ) 2 Dissolve in 600mL deionized water, adjust the pH value to 3.2, and make a mixed solution. The above-mentioned hydroxyl-bipyridine / Al 2 o 3 Add the precursor to the prepared solution, stir for 60 minutes, let stand for 8 hours, pour out the residue, and dry at 100°C for 8 hours to obtain PdPb-hydroxy-bipyridine / Al 2 o 3 Precursor (number of moles of hyd...

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Abstract

The invention relates to a C2 fraction selective hydrogenation method. A fixed bed reactor used for hydrogenation is positioned behind a demethanation tower, allows a C2 material from a front deethanization tower in an ethylene device to undergo pressurization hydrogen matching, enter a heat insulation bed reactor and undergo selective hydrogenation; the fixed bed reactor is filled with a Pd-Pb series catalyst, and hydroxydipyridine combined to a carrier and an active component form a metal complex through the combination of an alumina series carrier and a hydroxy group-containing dipyridine derivative in the preparation method of the catalyst. The hydrogenation reaction activity of the method provided by the invention is greatly better than that of traditional hydrogenation methods, and the generation amount of green in the hydrogenation process is greatly reduced. Reduction of the green oil makes the active site of the catalyst not be covered with byproducts and the activity and the selectivity of the catalyst be well kept; and when a hydrogenation raw materials contains 1000ppm or below of a C4 fraction, the catalyst also has an excellent hydrogenation performance.

Description

technical field [0001] The invention relates to a selective hydrogenation method, in particular to a carbon-two selective hydrogenation method in a sequential separation process. Background technique [0002] The production of polymer grade ethylene is the leader of the petrochemical industry, and polymer grade ethylene and propylene are the most basic raw materials for downstream polymerization units. Among them, the selective hydrogenation of acetylene has an extremely important impact on the ethylene processing industry. In addition to ensuring that the acetylene content at the outlet of the hydrogenation reactor reaches the standard, the selectivity of the catalyst is excellent, which can make ethylene generate as little ethane as possible, which is beneficial to improving the entire process. It is of great significance to improve the ethylene yield of the process and improve the economic benefits of the device. [0003] The cracked carbon distillate contains acetylene ...

Claims

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Application Information

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IPC IPC(8): C07C11/04C07C7/167B01J23/62
CPCY02P20/141Y02P20/52
Inventor 梁玉龙车春霞钱颖谭都平韩伟张峰高源张忠东常晓昕黄德华景喜林袁华斌蔡小霞王芳景丽
Owner PETROCHINA CO LTD
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