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Method for highly producing benzene from C6 alkane

An alkane, high-yield technology, used in the purification/separation of hydrocarbons, chemical instruments and methods, including molecular sieve catalysts, etc. focus effect

Active Publication Date: 2018-07-03
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the addition of reformed raffinate to reformed raw materials leads to a decrease in the aromatization depth and octane number of reformed gasoline
Translated by Hu Yunlin (Catalytic aromatization of reformed raffinate, Catalytic Reforming Communication (1991) 4: 41-43) reported the catalytic aromatization of reformed raffinate, using reformed raffinate directly as raw material, Reforming was carried out with platinum-tin reforming catalysts, but the results showed that the aromatization of reformed raffinate containing C5-C7 hydrocarbons on traditional platinum-tin catalysts was very difficult and the selectivity was low
[0006] Combining the public information such as existing patents and papers, it is either related to the performance improvement of the platinum-supported basic L molecular sieve catalyst, or the refining of raw material desulfurization and dehydration to ensure the performance of the catalyst, or how to combine with the existing reformer to increase the performance of the catalyst. yield of aromatics, but none of them proposed a method for efficient utilization of unconverted alkanes, nor did they propose a method for solving the impact of heavy components produced during the reaction on catalyst stability
Therefore, the existing technology has not yet reached the ideal level, and there is still room for further improvement.

Method used

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  • Method for highly producing benzene from C6 alkane
  • Method for highly producing benzene from C6 alkane
  • Method for highly producing benzene from C6 alkane

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0055] In this embodiment, the attached figure 1 In all the shown process flow, the C6 raw material is introduced into the above-mentioned reaction and separation system. The composition of alkane C6 feedstock and reaction product is shown in Table 2 below. Reaction conditions for producing more benzene: reaction temperature 480°C, pressure 0.35MPa(g), hydrogen-oil volume ratio 600:1, raw material volume space velocity 2.5h -1. At this time, the conversion rate of methylpentane is about 47.34%, the conversion rate of n-hexane is about 58.78%, and the yield of benzene reaches 41%.

[0056] According to the process of the present invention, the reaction product is separated and the material after benzene is extracted and mixed with fresh C6 feed into the 5A molecular sieve adsorption system and the feed composition of the deisohexane tower after desorbing n-hexane is shown in Table 3. At this time, the adsorption temperature of the 5A molecular sieve system is 290°C, the adso...

Embodiment 2

[0068] In this embodiment, the attached figure 1 For all the shown process flow, the C6 raw material is introduced into the above-mentioned reaction separation system. The composition of alkane C6 feedstock and reaction product is shown in Table 6 below. Reaction conditions for prolific benzene: reaction temperature 490°C, pressure 0.40MPa(g), hydrogen to oil volume ratio 600:1, raw material volume space velocity 2.5h -1 . At this time, the conversion rate of methylpentane is about 48.21%, the conversion rate of n-hexane is about 59.58%, and the yield of benzene reaches 39.67%.

[0069] According to the process of the present invention, the reaction product is separated and the material after benzene is extracted and mixed with fresh C6 feed into the 5A molecular sieve adsorption system and the feed composition of the deisohexane tower after desorbing n-hexane is shown in Table 7. At this time, the adsorption temperature of the 5A molecular sieve system is 300°C, the adsorp...

Embodiment 3

[0080] In this embodiment, the attached figure 1 For all the shown process flow, the C6 raw material is introduced into the above-mentioned reaction separation system. The compositions of alkane C6 feedstock and reaction products are shown in Table 10 below. Reaction conditions for prolific benzene: reaction temperature 500°C, pressure 0.30MPa(g), hydrogen to oil volume ratio 600:1, raw material volume space velocity 2.5h -1 . At this time, the conversion rate of methylpentane is about 47.18%, the conversion rate of n-hexane is about 58.05%, and the yield of benzene reaches 40.67%.

[0081] According to the process of the present invention, the reaction product is separated and the material after benzene is extracted and mixed with fresh C6 feed into the 5A molecular sieve adsorption system and the feed composition of the deisohexane tower after desorbing n-hexane is shown in Table 11. At this time, the adsorption temperature of the 5A molecular sieve system is 310°C, the a...

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Abstract

The invention discloses a method for highly producing benzene from C6 alkane. The method comprises the following steps: heating C6 alkane raw materials, and sequentially removing n-hexane by virtue ofan adsorber, and light and heavy components by virtue of an iso-hexane removal tower; hydrating and heating lateral line components of the iso-hexane removal tower and hydrogen raw materials, and introducing the lateral line components and the hydrogen raw materials into a reactor system for reaction; carrying out gas-liquid separation I on a reaction product, pressurizing a gas phase, carrying out gas-liquid separation II, introducing the gas phase into a desorber for desorption of n-hexane, and introducing the gas phase into a reaction system; introducing a liquid phase in the gas-liquid separation I into a depentanizer, introducing a material flow at the top and a liquid phase obtained in the gas-liquid separation II into a debutanizer, and leading a pentane component at the bottom ofthe debutanizer and iso-hexane and heavy components removed from the iso-hexane removal tower out as gasoline blending components; and introducing the material flow at the bottom of the depentanizer into an extraction tower, extracting benzene, introducing the material flow at the bottom of the extraction tower into a separation system, separating benzene, and circularly introducing the material flow at top into the reaction system. According to the method, the utilization rates of active components in C6 alkane are substantially increased, most water in the raw materials is removed, and the problems that light and heavy components are accumulated in the reaction system are solved.

Description

technical field [0001] The present invention relates to a kind of method of cyclization of C6 alkane to produce benzene, more specifically, relate to a kind of through 5A molecular sieve adsorber to remove normal hexane and remove isohexane tower to separate low molecular light components and multi-branched chain hydrocarbons as The gasoline blending component enables reactive active paraffins to circulate, converts them into benzene in a maximum amount through hydrogenation, and improves the utilization rate of C6 paraffins, and belongs to the technical field of petrochemical industry. Background technique [0002] The target products of the catalytic reforming process are mainly high-octane gasoline components and aromatics, while by-product hydrogen. Currently used is a bifunctional catalyst, no matter it is platinum rhenium series or platinum tin series, the dehydrocyclization reaction performance of low-carbon paraffins (such as normal hexane, normal heptane) is all poo...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C5/41C07C7/00C07C7/04C07C7/13C07C15/04
CPCC07C5/417C07C7/005C07C7/04C07C7/13C07C2529/62C07C15/04
Inventor 潘罗其李楚新杜建文张玉红王嘉欣肖哲余卫勋
Owner CHINA PETROLEUM & CHEM CORP
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