Shale oil processing method for producing propylene

A processing method and technology for shale oil, which are applied in the petroleum industry, hydrotreating process, and bulk chemical production, etc. The process is simple and the effect of improving the yield of liquefied gas

Active Publication Date: 2012-05-23
CHINA PETROLEUM & CHEM CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

This patent does not cover the conversion of all liquid products in shale oil hydroprocessing products, and does

Method used

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  • Shale oil processing method for producing propylene
  • Shale oil processing method for producing propylene
  • Shale oil processing method for producing propylene

Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0040] Example 1

[0041] This example illustrates the effect of converting the shale oil hydrogenation liquid product into shale oil hydrogenated light oil and shale oil hydrogenated heavy oil at a cutting point of 265°C according to the method provided by the present invention.

[0042] The experiment was carried out in a medium-sized riser catalytic cracking unit with a configuration such as figure 1 Shown. The first riser reactor (riser reactor 1) of the medium-sized device has an inner diameter of 16 mm and a height of 3800 mm. The second riser reactor (riser reactor 2) has an inner diameter of 16 mm and a height of 3200 mm. The outlet of the second riser reactor is connected to a fluidized bed reactor. The inner diameter of the fluidized bed reactor 4 is 64 mm and the height is 600 mm. The test adopts a single pass mode (that is, the product is not refined). The high-temperature regenerant is introduced into the bottom of riser reactor 1 and riser reactor 2 from the regener...

Example Embodiment

[0044] Example 2

[0045] This example illustrates the effect of converting the shale oil hydrogenation liquid product into shale oil hydrogenated light oil and shale oil hydrogenated heavy oil according to the cutting point 350°C according to the method provided by the present invention.

[0046] The experimental device is the same as in Example 1, and the main operating conditions and results of the experiment are listed in Table 3.

Example Embodiment

[0047] Example 3

[0048] This example illustrates the effect of the method provided by the present invention that the shale oil hydrogenation liquid product is divided into shale oil hydrogenated light oil and shale oil hydrogenated heavy oil at a cutting point of 350° C. for catalytic cracking, and the reaction conditions are optimized at the same time.

[0049] The experimental device is the same as in Example 1, and the main operating conditions and results of the experiment are listed in Table 5.

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Abstract

The invention discloses a shale oil processing method for producing propylene. The method comprises the following steps of: hydrogenating shale oil, separating shale oil hydrogenation products to obtain gas and liquid reaction oils, and separating the liquid reaction oil into a shale oil hydrogenation light oil and a shale oil hydrogenation heavy oil; introducing the shale oil hydrogenation heavy oil into a first riser reactor for undergoing a catalytic pyrolysis reaction; and introducing a part of or all of the shale oil hydrogenation light oil into a second riser reactor for undergoing a catalytic pyrolysis reaction. The shale oil processing method provided by the invention has high propylene yield.

Description

technical field [0001] The invention relates to a shale oil processing method and a device thereof. Furthermore, the present invention relates to a method for deep conversion of shale oil to produce light olefins. Background technique [0002] Worldwide research reports on oil shale and shale oil stagnated for many years following the low oil prices of the 20th century. However, most of the shale oil refining patents reported before the early 1980s revolved around how to refine the quality of shale oil. It is a processing method of coking and then hydrotreating its liquid hydrocarbon products. US4218309 describes a method for reducing sulfur content during shale oil production. US4238320 introduces the method of using hydrogenation to reduce nitrogen content first, and then further denitrifying shale oil with ion exchange resin. [0003] US4344840 introduces a method for hydrocracking and hydrofining of shale oil in a multistage reactor to produce jet fuel and diesel oil...

Claims

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Application Information

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IPC IPC(8): C10G69/00C07C11/06C07C4/06
CPCY02P20/52
Inventor 高永灿谢朝钢崔琰朱金泉毛安国张久顺杨轶男马建国姜楠
Owner CHINA PETROLEUM & CHEM CORP
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