Supercharge Your Innovation With Domain-Expert AI Agents!

Fluidized bed device and method for converting methanol into aromatics with different functions

A methanol conversion and fluidized bed technology, applied in chemical instruments and methods, hydrocarbon production from oxygen-containing organic compounds, condensation hydrocarbon production with dehydrocarbons, etc., can solve the inability to achieve complete methanol conversion and the decline in methanol conversion rate , waste water treatment and other problems, to achieve the effect of less recycled materials, reduced recycled materials, and increased aromatics content

Active Publication Date: 2020-12-01
TSINGHUA UNIV
View PDF7 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, if there is a trace amount of methanol, the difficulty of wastewater treatment will increase significantly
At the same time, with the deactivation of carbon deposits on the catalyst, the conversion rate of methanol will also decrease. In a fluidized bed with severe gas-solid back-mixing, the complete conversion of methanol cannot be achieved.

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Fluidized bed device and method for converting methanol into aromatics with different functions

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] Fill catalyst (zinc oxide, lanthanum oxide, ZSM-5, kaolin, aluminum oxide, its mass fraction is respectively 3%, 7%, 70%, 10%, 10% in the three-stage fluidized bed 1 by catalyst filling port 8 %). After preheating to 250°C, feed methanol-containing material (50% methanol, 50% C 2 -C 10 Mixed ester), through the gas inlet 2 and the porous distribution plate one 3, between the porous distribution plate one 3 and the porous distribution plate two 4, the catalyst accumulation area between the porous distribution plate two 4 and the gas outlet 9, and control the temperature The reaction was carried out at 380°C, 580°C, and 500°C respectively, and the catalyst space velocity was 0.1kg methanol / kg catalyst / hour. After the reaction, water, mixtures of aromatic hydrocarbons, light hydrocarbons and hydrogen are generated, and the three-stage fluidized bed 1 is discharged from the gas outlet 9 .

[0038] The deactivated catalyst is taken out through the deactivated catalyst out...

Embodiment 2

[0041] Fill catalyst (gallium, copper, cerium oxide, ZSM-5, silicon oxide, aluminum oxide, its mass fraction is respectively 3%, 7%, 20%, 30% in the three-stage fluidized bed 1 by catalyst filling port 8 , 10%, 30%). After preheating to 300°C, feed methanol-containing material (80% methanol, 14% acetone, 1% ethyl acetate, 5% pentane, 7% cyclohexene, 3% glycerol) from the gas inlet 2, followed by After passing through the catalyst accumulation area between the gas inlet 2 and the porous distribution plate 1 3, between the porous distribution plate 1 3 and the porous distribution plate 2 4, and between the porous distribution plate 2 4 and the gas outlet 9, the control temperature is 490°C, The reaction was carried out at 550°C and 450°C, and the catalyst space velocity was 20kg methanol / kg catalyst / hour. After the reaction, water, mixtures of aromatic hydrocarbons, light hydrocarbons and hydrogen are generated, and the three-stage fluidized bed 1 is discharged from the gas out...

Embodiment 3

[0045] Catalysts (ZSM-12, silicon oxide, the mass fractions of which are 30% and 70% respectively) are loaded into the three-stage fluidized bed 1 from the catalyst replenishment port 8 . After preheating to 300°C, methanol is introduced from gas inlet 2, and passes through gas inlet 2 and porous distribution plate 1 in sequence, between porous distribution plate 1 3 and porous distribution plate 2 4, and between porous distribution plate 2 4 and gas In the catalyst accumulation area between the outlets 9, the temperature is controlled at 450°C, 550°C, and 450°C for the reaction, and the catalyst space velocity is 0.3kg methanol / kg catalyst / hour. After the reaction, water, mixtures of aromatic hydrocarbons, light hydrocarbons and hydrogen are generated, and the three-stage fluidized bed 1 is discharged from the gas outlet 9 .

[0046] The deactivated catalyst is drawn out through the deactivated catalyst outlet 7, and regenerated at 600°C by passing air on other devices. Then...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention discloses a fluidized bed device for converting methanol into aromatic hydrocarbons in a partitioning manner according to different functions and a method of the device. The device comprises a three-stage fluidized bed, and the device is divided into a first reaction zone, a second reaction zone and a third reaction zone from the bottom to the top and an overflow and degassing pipe connected with the first reaction zone and the third reaction zone; the three reaction zones are filled with a same catalyst, temperatures in the three reaction zones are separately controlled, so thataromatization of methanol is completed in the first reaction zone, aromatization of light hydrocarbons is completed in the second reaction zone, and aromatization of olefins and alkylation of micro methanol are completed in the third reaction zone; and at the same time, a regenerated high-temperature catalyst enters the second reaction zone, and the temperature of the second reaction zone is maintained higher than that of the first reaction zone and the third reaction zone. According to the device and method provided by the invention, a high-activity low-carbon-deposition catalyst is distributed in the second reaction zone, and a lower-activity higher-carbon-deposition catalyst is distributed in the first and third reaction zones, so that activity of each catalyst can be well matched withone corresponding temperature zone, high-efficient methanol conversion can be realized, a yield of aromatic hydrocarbons can be improved, and the content of propane in an outlet of a reactor can be reduced; and the device has the characteristics of less recycled materials and low energy consumption.

Description

technical field [0001] The invention belongs to the technical field of chemical process and equipment, and in particular relates to a fluidized bed device and method for converting methanol into aromatic hydrocarbons with different functions. Background technique [0002] Methanol aromatization technology is an emerging aromatics production process, which uses methanol as the main raw material to generate aromatics (mainly benzene, toluene, xylene) on molecular sieve, metal-molecular sieve, or metal oxide-molecular sieve catalysts. , trimethylbenzene, etc.) process. The product is controlled by the double-pool hydrocarbon mechanism in the molecular sieve. The primary products include the above-mentioned aromatics, and small molecular olefins and alkanes, resulting in a low primary yield of aromatics. It has been reported that the above products are separated and transformed separately. However, when alkanes are transformed into aromatics again, it is a high-temperature, st...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): B01J8/18B01J8/24C07C1/20C07C2/76C07C15/02
CPCY02P20/584
Inventor 骞伟中陈兆辉侯一林宋文龙
Owner TSINGHUA UNIV
Features
  • R&D
  • Intellectual Property
  • Life Sciences
  • Materials
  • Tech Scout
Why Patsnap Eureka
  • Unparalleled Data Quality
  • Higher Quality Content
  • 60% Fewer Hallucinations
Social media
Patsnap Eureka Blog
Learn More