Catalyst for selective hydrogenation and olefin removal of reformed generated oil as well as preparation method and application

A technology of reforming to generate oil and catalyst, applied in the direction of selective hydrofining, metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, etc., can solve solvent oil bromine index and copper sheet corrosion Unqualified tests, unqualified bromine index and pickling color of aromatic products, affecting the smooth progress of the separation process, etc., to shorten the start-up time, avoid the hazards of operators and the environment, and reduce the initial activity.

Active Publication Date: 2014-09-03
SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The technical effect described this patented technology relates to reducing or eliminating certain substances that may contaminate refinery products during processing. By distributing these materials onto specific areas inside a special structure made up mostly of tiny shell shapes called lopsheets, they help prevent them getting trapped between layers within the reactor vessel. These small structures make sure more expensive rare metal atoms get exposed while still allowing valuable molecules like naphtha (naprothene) to escape. Additionally, adding agents helps decrease the starting activity at startup and prolongs their lifespan. Overall, this new type of catalytic material used in chemical processes has improved efficiency, safety, and productivity compared to existing methods such as acid treatment alone.

Problems solved by technology

This patented technical solution describes various techniques for efficiently separating impurities like oxygen compounds during upgrading crude oil without causing harmful side effects over existing technologies. These involve reactors called fluid bed type reactors where heavy materials have difficulty reaching downstream devices while maintaining desired properties within these systems. Previous attempts were either limited throughput or resulted in poor quality final products containing unwanted substances. To address these issues, researchers explored alternative ways including increasing the number of platinum atoms per unit weight of feedstock, adding another atom to increase acid functionality, adjusting the concentration of unsymmetrical carbon residues, and controlling the hydroxynthesis efficiency of alcohol crackings.

Method used

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  • Catalyst for selective hydrogenation and olefin removal of reformed generated oil as well as preparation method and application
  • Catalyst for selective hydrogenation and olefin removal of reformed generated oil as well as preparation method and application
  • Catalyst for selective hydrogenation and olefin removal of reformed generated oil as well as preparation method and application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] Weigh 0.21g ruthenium trichloride and 0.43g palladium nitrate, dissolve it with deionized water to make the solution concentration 0.5mol / L, and heat it to 40°C. Slowly add oxalic acid to the mixed solution to make the pH 4.0. Stir uniformly, add 98.7g of alumina carrier for impregnation, keep stirring during the impregnation process, after 12h, filter out the impregnated catalyst and dry, slowly increase from room temperature to 120℃, the heating rate is 10℃ / h, under 120℃ Dry at constant temperature for 18h. The dried catalyst was calcined at 500°C for 5 hours to obtain the desired catalyst. The indicators of the catalyst are shown in Table 1, and the eggshell thickness is shown in Photo 1 of the cross section of the catalyst.

[0037] Weigh 20g of catalyst in a fixed-bed reactor with temperature programmed reduction activation, the activation conditions are: hydrogen pressure is 2.0MPa, volumetric space velocity is 1500h -1 , Reducing at 250℃ for 5h, heating rate is 10℃

Embodiment 2

[0039] Weigh 0.35g platinum tetrachloride, 3.80g copper nitrate trihydrate, 11.78g calcium nitrate tetrahydrate, dissolve it with deionized water to make the solution concentration 0.8mol / L, and heat to 70℃, slowly add acetic acid to the mixed solution , To make the pH of 3.0, stir the solution evenly, add 96.8g of alumina carrier to impregnate, keep stirring during the impregnation process, after 18h, filter out the impregnated catalyst and dry, slowly increase from room temperature to 130℃, the heating rate is 10℃ / h, drying at 130℃ for 10h. The dried catalyst is calcined at 450°C for 6 hours to obtain the desired catalyst. The indicators of the catalyst are shown in Table 1, and the eggshell thickness is shown in Photo 2 of the cross section of the catalyst.

[0040] Weigh 20g of catalyst in a fixed bed reactor for temperature-programmed reduction activation, the activation conditions are: hydrogen pressure is 2.5MPa, volumetric space velocity is 800h -1 , Reducing at 180℃ for

Embodiment 3

[0042] Weigh 0.08g palladium chloride, 0.21g chloroplatinic acid, 0.21g ruthenium trichloride, 14.82g flowing water cobalt nitrate, dissolve it with deionized water so that the concentration of the solution is 0.26mol / L, and heat it to 50℃, Slowly add hydrochloric acid to make the pH 1.9, stir the solution evenly, add 96.8g of alumina carrier for impregnation, keep stirring during the impregnation process, after 15h, filter out the impregnated catalyst and dry it, slowly increase from room temperature to 120℃ , The heating rate is 10℃ / h, and it is dried at 120℃ for 15h. The dried catalyst is calcined at 450°C for 12 hours to obtain the desired catalyst. The indicators of the catalyst are shown in Table 1, and the eggshell thickness is shown in the photo 3 of the cross section of the catalyst.

[0043] Weigh 20g of catalyst in a fixed-bed reactor with temperature programmed reduction activation, the activation conditions are: hydrogen pressure is 2.0MPa, volumetric space velocity

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Abstract

The invention provides a catalyst for selective hydrogenation and olefin removal of reformed generated oil. The catalyst comprises an active component oxide, an auxiliary agent oxide and a carrier, wherein according to the content of metal, the content of the components is as follows in percentage by mass: 0.05-0.5wt% of the active component oxide, 0.5-10wt% of the auxiliary agent oxide and the residual amount of the carrier; the active component oxide is at least one of oxides of noble metal Pt, Pd and Ru; the auxiliary agent oxide is one or two of oxides of Na, K, Mg, Ca, Co, Fe, Ni, Mo and Cu; the carrier is Al2O3. The catalyst has the advantages of high activity, good selectivity, long service life and low cost.

Description

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Claims

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Application Information

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Owner SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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