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Process and system for preparing alpha-olefin by catalytic conversion of fatty acid ester

A fatty acid ester, catalytic conversion technology, applied in the field of fatty acid ester conversion, can solve the problems of complex product composition, low single-pass conversion rate, long separation process, etc., and achieve low separation difficulty, high raw material conversion rate, and simple product composition Effect

Pending Publication Date: 2020-09-18
SICHUAN LUTIANHUA +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method obtains C4-30 linear α-olefins, the product composition is more complex, and the separation process is longer
[0008] (3) Internal olefin isomerization method: there is a problem that the composition of the product is relatively complex and the subsequent separation is relatively difficult
[0009] (4) Alkane dehydrogenation method: both domestic and foreign technologies have the problems of low single-pass conversion rate and short lifespan (such as: UOP technology, Xconv, s=10-15%, lifespan cat.=~40 days). There is a problem of high energy consumption in the separation of the reacted alkane feedstock and α-olefins
[0018] To sum up, so far, there are still few techniques for directly synthesizing high-carbon α-olefins using typical raw materials such as vegetable oils and / or animal oils and biological oils.

Method used

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  • Process and system for preparing alpha-olefin by catalytic conversion of fatty acid ester
  • Process and system for preparing alpha-olefin by catalytic conversion of fatty acid ester
  • Process and system for preparing alpha-olefin by catalytic conversion of fatty acid ester

Examples

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Effect test

Embodiment 1

[0056] A system for producing α-olefins by catalytic conversion of fatty acid esters in this embodiment includes a fatty acid ester hydrogenation unit, a fatty alcohol separation unit, a fatty alcohol dehydration unit, and an α-olefin separation unit;

[0057] The fatty acid ester hydrogenation unit is used for the contact reaction of fatty acid ester, hydrogen and a fatty acid ester hydrogenation catalyst, and is filled with a fatty acid ester hydrogenation catalyst;

[0058] The fatty alcohol separation unit is used to separate the reaction product of the fatty acid ester hydrogenation unit to obtain fatty alcohol, unreacted hydrogen and unreacted fatty acid ester;

[0059] The fatty alcohol dehydration unit is used for the contact reaction between the fatty alcohol and the fatty alcohol dehydration catalyst, and is filled with a fatty alcohol dehydration catalyst;

[0060] The α-olefin separation unit is used to separate the reaction product of the fatty alcohol dehydration...

Embodiment 2

[0072] A system for producing α-olefins by catalytic conversion of fatty acid esters in this embodiment is the same as that in Embodiment 1.

[0073] A kind of process of catalytic conversion of fatty acid ester of the present embodiment prepares α-olefin, comprises the following steps:

[0074] Step 1, hydrogenation of fatty acid esters: mix 2.2g of carbon octafatty acid methyl esters with 68.0NL of hydrogen (the molar ratio of hydrogen to fatty acid esters is 200:1), add 2.2g of copper-zinc catalysts to the reaction system, and At 300°C, under pressure of 3MPa, carry out hydrogenation reaction of fatty acid ester under pressure;

[0075] Step 2, fatty alcohol separation: separate the product obtained in step 1 to obtain unreacted hydrogen, unreacted fatty acid ester and fatty alcohol, and add unreacted fatty acid ester to the fatty acid ester in step 1 In the hydrogenation reaction system, most of the unreacted hydrogen is circularly added to the fatty acid ester hydrogenat...

Embodiment 3

[0080] A system for producing α-olefins by catalytic conversion of fatty acid esters in this embodiment is the same as that in Embodiment 1.

[0081] A kind of process of catalytic conversion of fatty acid ester of the present embodiment prepares α-olefin, comprises the following steps:

[0082] Step 1, hydrogenation of fatty acid esters: mix 1.5g carbon ten fatty acid methyl esters with 35.0NL hydrogen (the molar ratio of hydrogen to fatty acid esters is 180:1), add 2.0g of copper-zinc catalyst to the reaction system, at temperature At 250°C, under the pressure of 3MPa, carry out hydrogenation reaction of fatty acid ester;

[0083] Step 2, fatty alcohol separation: separate the product obtained in step 1 to obtain unreacted hydrogen, unreacted fatty acid ester and fatty alcohol, and add unreacted fatty acid ester to the fatty acid ester in step 1 In the hydrogenation reaction system, most of the unreacted hydrogen is circularly added to the fatty acid ester hydrogenation rea...

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Abstract

The invention relates to the technical field of fatty acid ester conversion, in particular to a process and system for preparing alpha-olefin through catalytic conversion of fatty acid ester. The process comprises fatty acid ester hydrogenation, fatty alcohol separation, fatty alcohol dehydration and alpha-olefin separation, the process expands the source of raw materials for synthesizing alpha-olefin, the product composition is simple, and the subsequent separation difficulty is low. The system comprises a fatty acid ester hydrogenation unit, a fatty alcohol separation unit, a fatty alcohol dehydration unit and an alpha-olefin separation unit, which are connected in sequence. According to the process and the system, through reasonable circulation arrangement of unreacted substances (circulation of a small part of unreacted hydrogen and oxygen-containing substances), generation of the oxygen-containing substances is reduced, and meanwhile, low emission and even zero emission of the oxygen-containing substances are realized.

Description

technical field [0001] The invention relates to the technical field of fatty acid ester conversion, in particular to a process and system for preparing α-olefins by catalytic conversion of fatty acid ester. Background technique [0002] Linear α-olefins usually refer to C4 and above linear terminal olefins. They are an important class of organic chemical raw materials that have developed rapidly in the past 30 years. Since the industrialization of ethylene oligomerization to produce α-olefins in the 1990s , Its application fields continue to expand, and comonomers are widely used, synthetic lubricant base oils, surfactants, plasticizers, fungicides and emulsifiers and other chemical products. [0003] With the rapid development of the world economy, the α-olefin market is still showing a trend of rapid development, and some new devices are still under construction. In 2016, the world's main production capacity of α-olefins was 5.56 million tons, and its consumption was 5.37...

Claims

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Application Information

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IPC IPC(8): C07C11/107C07C11/02C07C1/24C07C7/00
CPCC07C1/24C07C7/00C07C29/149C07C11/107C07C11/02C07C31/125
Inventor 李德宝夏铭肖勇赵永清朱德林贾丽涛倪杰侯博
Owner SICHUAN LUTIANHUA