Method for preparing aromatic hydrocarbons from methanol with low carbon olefin as byproduct, and apparatus thereof

A low-carbon olefin and methanol technology, which is applied in the direction of hydrocarbon production from oxygen-containing organic compounds, ethylene production, bulk chemical production, etc., can solve the problems of low yield of aromatics, large output of dry gas and liquefied gas, etc. Increased efficiency, improved continuous operability, and good economic benefits

Active Publication Date: 2014-12-31
SINOPEC LUOYANG PETROCHEM ENG CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

It has solved the problems of low yield of aromatics and large output of dry gas and liquefied gas in the prior art, and at the same time can make the device operate continuously

Method used

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  • Method for preparing aromatic hydrocarbons from methanol with low carbon olefin as byproduct, and apparatus thereof
  • Method for preparing aromatic hydrocarbons from methanol with low carbon olefin as byproduct, and apparatus thereof
  • Method for preparing aromatic hydrocarbons from methanol with low carbon olefin as byproduct, and apparatus thereof

Examples

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Embodiment Construction

[0046] Such as figure 1 Shown is a simple schematic flow chart of a methanol-to-aromatics process with by-product light olefins. The device for producing aromatics from methanol and by-producting low-carbon olefins includes a riser reactor 6 and a fluidized bed reactor 7, the top of the riser reactor 6 is connected to the top of the fluidized bed reactor 7, and the fluidized bed reactor 7 The lower part is the separation tank 8 at the bottom of the fluidized bed reactor, and the upper part of the separation tank 8 at the bottom of the fluidized bed reactor is communicated with the upper part of the fluidized bed reactor 7 through the cyclone separator 11 and the separation device 22, and the bottom of the fluidized bed reactor is separated The bottom of the tank 8 is connected to the top of the charring tank 9 , and the bottom of the charring tank 9 is connected to the bottom of the riser reactor 6 . Or the bottom of the coke tank 9 is connected to the bottom of the riser rea...

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Abstract

The invention discloses a method for preparing aromatic hydrocarbons from methanol with low carbon olefin as a byproduct, and an apparatus thereof. The problems of low yield of the aromatic hydrocarbons, large output of dry gas and liquefied gas, and the like in the prior art are solved in the invention. The method comprises the following steps: preheating the raw material methanol to 350-500DEG C, adding the preheated methanol to a riser reactor, carrying out a contact reaction on the preheated methanol and a catalyst in the riser reactor for 0.8-4.0s, allowing the reaction product of the riser reactor to enter a deep catalysis reactor (such as a fluidized bed, moving bed or fixed bed reactor) to carry out a reaction, returning C2-C5 alkanes in the reaction products of the deep catalysis reactor to the deep catalysis reactor in order to re-process the C2-C5 alkanes, and discharging other products from the apparatus, wherein the catalyst is a ZSM-5 / SAPO-34 catalyst modified by Ga, Zn, P and Ag.

Description

technical field [0001] The invention belongs to the field of preparing aromatics from methanol, and relates to a method for preparing aromatics from methanol and by-producting low-carbon olefins and a device used in the method. Background technique [0002] Low-carbon aromatics mainly include benzene, toluene and xylene, generally referred to as BTX, which are important basic chemical raw materials, of which p-xylene (PX) accounts for about 45% of the total consumption of BTX, and about 95% of aromatics production in industry comes from Petrochemical, a small amount comes from coal tar processing. In 2010, my country's BTX output was about 14.2 million tons, and the apparent consumption reached 19 million tons. The gap between supply and demand was about 4.8 million tons, of which the self-sufficiency rate of PX was only 61.6%, and the net import was 3.32 million tons. In order to fill the gap in the aromatics market and reduce the dependence of aromatics on petroleum resourc...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C1/20C07C15/04C07C15/06C07C15/08C07C11/04C07C11/06
CPCY02P20/52Y02P20/584Y02P30/20Y02P30/40
Inventor 李康魏小波郝代军韩海波毛继平张国良刘雪芬
Owner SINOPEC LUOYANG PETROCHEM ENG CORP
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