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A method for converting topped oil light hydrocarbons

A technology for light hydrocarbons and oils, which is used in the production of diolefins and high-octane gasoline components, can solve the problems of low utilization rate of isomerized olefins, and achieve the effect of increasing added value and improving utilization rate.

Active Publication Date: 2019-08-02
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the process of producing diolefins by oxidative dehydrogenation, normal olefins make the main contribution, and the utilization rate of isomeric olefins is low

Method used

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  • A method for converting topped oil light hydrocarbons

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Experimental program
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Effect test

Embodiment 1

[0047] Catalytic dehydrogenation catalyst adopts Haitai company HTPB-DH dehydrogenation catalyst, in which Al 2 o 3 As the carrier, Pt and Cl are used as active components, wherein the mass content of Pt is 1%, the mass content of chlorine is 2%, and the specific surface area is 200m 2 / g, pore volume 0.5ml / g, diameter 1.59mm, bulk density 0.6g / cm 3 . The catalyst for oxidative dehydrogenation of olefins was prepared by the preparation method of Example 2 in the patent CN102671714A. The specific preparation method was as follows: Dissolve 17 grams of magnesium nitrate hexahydrate in 20 ml of distilled water, then add 20 grams of zirconia, and carry out the above mixed solution at 80 ° C. After evaporation and drying for 12 hours, the resulting solid sample was heated in an air atmosphere at 550° C. for 3 hours in a muffle furnace, and then the sample was impregnated with an ammonium metavanadate aqueous solution. The ammonium metavanadate aqueous solution is prepared by dis...

Embodiment 2

[0049]The catalytic dehydrogenation catalyst is prepared by the method of Example 4 in CN101940922A. The specific steps are as follows: first weigh 117.5 grams of chromium oxide, dissolve it in deionized water and stir thoroughly, and prepare a chromium oxide solution with a weight concentration of 47%. Then configure a potassium nitrate aqueous solution with a weight concentration of 3.86%. Then 55.0 grams of pseudo-boehmite and 2.2 grams of bentonite were fully mixed with 7.59 grams of prepared chromium oxide solution, kneaded and extruded into pellets. Then dry at 120°C for 3 hours, then keep at 500°C for 3 hours, keep at 620°C for 2 hours, and finally bake at 760°C for 4 hours under 20% water and 80% air. Then take 11.39 g of the prepared chromium oxide solution, soak the roasted sample for 20 minutes, dry at 120°C for 3 hours, and roast at a constant temperature of 550°C for 5 hours. Then take the prepared potassium nitrate aqueous solution for dipping, dry at 120°C for...

Embodiment 3

[0051] The catalytic dehydrogenation catalyst was prepared by the method of Example 1 in the patent CN 101618319. Dissolve 2.24 grams of calcium oxide and 3.1 grams of polyethylene glycol in 120ml of deionized water, heat treatment at 240°C for 24 hours, and burn it at 600°C for 5 hours, then add it with an appropriate amount of absolute ethanol, 7.2 grams of chromium nitrate, 6 grams of trisodium Aluminum oxide is mixed evenly, dried for 12 hours, ground evenly, burned at 550°C for 3 hours, and then used for later use. The oxidative dehydrogenation catalyst of olefins was prepared by the method of Preparation Example 2 in patent 200780013916.9, and the specific steps were as follows: 69 grams of ammonium molybdate was dissolved in 500 ml of distilled water and stirred, and then 108.1 grams of bismuth nitrate was added to 5.3% nitric acid solution After stirring in the medium until completely dissolved, it was added dropwise to the ammonium molybdate solution. Then ammonia wa...

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Abstract

The present invention provides a topped oil-based light hydrocarbon conversion method, particularly a method for producing butadiene and pentadiene from topped oil, coking light naphtha, an oil field light hydrocarbon, pentane oil and other components using C4 / C5 / C6 alkane as a main component, and concurrently producing high octane number gasoline components. According to the present invention, the by-product hydrocarbon stream obtained after the production of butadiene and pentadiene through catalytic dehydrogenation and oxidative dehydrogenation enters the etherification reactor to produce the high-quality high octane number gasoline components; and compared to the method in the prior art, the method of the present invention has the following advantage that the utilization rate and the added value of the C4 / C5 / C6 alkane-rich streams are further improved.

Description

technical field [0001] The invention provides a process for producing diolefins and high-octane gasoline components from light hydrocarbons such as refinery top oil by combining catalytic dehydrogenation technology, oxidative dehydrogenation technology and etherification technology. Background technique [0002] Entering the "12th Five-Year Plan", with PetroChina Guangdong Petrochemical 20 million tons / year refining, Kunming 10 million tons / year refining, Sichuan Petrochemical refining and chemical integration project, Fushun Petrochemical 800,000 tons / year ethylene, Daqing Petrochemical 1.2 million tons With the advancement of projects such as ethylene reconstruction and expansion, PetroChina's refining capacity and ethylene production capacity will be further expanded, and the output of top oil, pentane oil, coking naphtha, etc. by-products of refineries will also increase significantly. Top oil, pentane oil, coker naphtha, etc. with alkanes as the main components are main...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C11/16C07C11/173C07C7/00C07C5/48C10G3/00
CPCY02P20/10Y02P30/20
Inventor 孙世林王卫东黄剑锋李长明马应海程亮亮田亮程琳李博刘飞王玫张松显孔祥冰景媛媛李秋颖许江
Owner PETROCHINA CO LTD