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Catalytic conversion method for improving productivity of low carbon olefin hydrocarbon

A catalytic conversion method and carbon olefin yield technology, which is applied in the field of low-carbon olefins, can solve problems such as the decline in propylene yield, and achieve the effects of increasing yield, wide application range, and wide source of raw materials

Active Publication Date: 2012-05-23
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the inventors have found through laboratory research that under the reaction conditions for preparing low-carbon olefins by catalytic conversion of hydrocarbon oils and the presence of acidic zeolites, propylene can be converted into other hydrocarbons, hydrogen and coke in large quantities and rapidly after generation, and then lead to Propylene yield decreased significantly

Method used

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  • Catalytic conversion method for improving productivity of low carbon olefin hydrocarbon
  • Catalytic conversion method for improving productivity of low carbon olefin hydrocarbon
  • Catalytic conversion method for improving productivity of low carbon olefin hydrocarbon

Examples

Experimental program
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Effect test

Embodiment 1

[0038] This example illustrates: using the method provided by the invention, when hydrogen (purity: 99.99% by volume) is injected into the reactor, the catalytic reaction activity of light olefins on a small-scale fixed fluidized bed experimental device.

[0039] The experiment uses raw material A as the raw material, and adopts the intermittent operation mode. The raw material, hydrogen and atomized steam are heated to about 350°C by the preheating furnace, and then enter the bottom of the fluidized bed reactor through the feeding nozzle, and contact with the hot catalyst for catalytic conversion reaction. . After the reaction product and hydrogen are separated from the catalyst, they enter the product separation system, and the reaction product is further separated into gas products and liquid products. After the reaction is completed, it enters the stripping stage, and the hydrocarbon products adsorbed on the unborn catalyst are stripped out by water vapor. After the strip...

Embodiment 2

[0045] This example illustrates: using the method provided by the present invention, heavy hydrocarbons are catalytically converted to produce ethylene and propylene when hydrogen-rich catalytic cracking dry gas (hydrogen content is 30.58% by volume) is injected into the reactor.

[0046] In the experiment, raw material B was used as the raw material, and the catalytic conversion experiment was carried out on a medium-sized riser device with continuous reaction-regeneration operation. The riser has an inner diameter of 16 mm and a height of 6 meters. Starting from the raw material nozzle of the riser, the effective length of the riser is defined as 100% along the flow direction of the raw material, and the injection position of the hydrogen-rich gas is 40% of the riser.

[0047] The experiment adopts the operation mode of one-way pass. The regenerated catalyst with a temperature of about 700°C enters the bottom of the reaction section of the riser through the regenerated incl...

Embodiment 3

[0050] This example illustrates: using the method provided by the present invention, heavy hydrocarbons are catalytically converted to produce ethylene and propylene when hydrogen-rich catalytic cracking dry gas (hydrogen content is 30.58% by volume) is injected into the reactor.

[0051] In the experiment, raw material B was used as the raw material, and the reaction device and main experimental steps used in the experiment were the same as those in Example 2. The hydrogen-enriched gas is injected at 70% of the riser.

[0052] The main operating conditions and results of the experiments are listed in Table 3. It can be seen from Table 3 that the yields of ethylene and propylene are as high as 4.62% by weight and 18.86% by weight respectively.

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Abstract

A catalytic conversion method for improving the yield of low-carbon olefin comprises the following steps: hydrocarbon oil raw material is injected into a riser or / and a fluidized bed reactor via a feed nozzle, comes into contact with catalyst containing shape-selective zeolite with an average pore size being smaller than 0.7 nm and reacts; gas rich in hydrogen is injected into the reactor; reaction oil gas and carbon deposited catalyst after reaction are separated, wherein the reaction oil gas is separated to obtain a target product containing ethylene and propylene; and the carbon deposited catalyst is returned to the reaction for reutilization after being stripped and regenerated. By injecting gas rich in hydrogen, the method can remarkably inhibit reconversion reaction of the generatedlow-carbon olefin to improve the yield of low-carbon olefin, particularly of propylene. When vacuum gas oil is adopted as raw material and double risers combined with a fluidized bed reactor are adopted, ethylene yield reaches 8.97 wt%, and propylene yield reaches 31.38 wt%, which are respectively improved by 2.93% and 6.81% in comparison with a process without injection of gas rich in hydrogen.

Description

technical field [0001] The invention belongs to a method for catalytic conversion of hydrocarbon oil, more specifically, a method for preparing low-carbon olefins such as ethylene and propylene through catalytic conversion of hydrocarbon oil under the action of a catalyst. Background technique [0002] At present, the traditional method of producing low-carbon olefins is the tube furnace steam cracking method, and the suitable raw materials for this method are light petroleum hydrocarbons such as ethane, propane, butane, naphtha or light diesel oil. As crude oil becomes heavier, the supply of light petroleum hydrocarbons is limited, forcing researchers to turn their attention to using a wider range of raw materials including heavy petroleum hydrocarbons to produce light olefins. [0003] In recent years, some patent documents have disclosed the method of producing light olefins by using raw materials such as heavy petroleum hydrocarbons, naphtha and C4-C6 light hydrocarbons ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C11/02C10G47/16
CPCY02P20/584
Inventor 李正龙军谢朝钢侯栓弟朱根权张执刚陈昀
Owner CHINA PETROLEUM & CHEM CORP
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