Eureka AIR delivers breakthrough ideas for toughest innovation challenges, trusted by R&D personnel around the world.

Catalyst for cracking methyl tertiary butyl ether, and preparation method and application of catalyst

A technology of methyl tert-butyl ether and catalyst, which is applied in the field of catalyst for cracking of methyl tert-butyl ether and its preparation and application, can solve the problems of increased by-products, high catalyst cost and high requirements for heating equipment, and achieve Effects of high isobutene and methanol selectivity, catalyst cost reduction, and high equipment utilization

Active Publication Date: 2014-06-04
EAST CHINA UNIV OF SCI & TECH
View PDF8 Cites 6 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The existing niobic acid system, such as JP6210603, uses pure niobic acid as the catalyst, when the LHSV is 4 h -1 1. When the reaction temperature is 250°C, the conversion rate of MTBE is 99.2%, but the cost of the pure niobic acid system catalyst itself is too high, and the reaction temperature of 250°C is not only too large in energy consumption, but also requires very high heating equipment, and It is easy to lead to an increase in by-products, affecting product purity, and increasing product distillation requirements and costs

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

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] 30 g γ-Al 2 o 3 Add to 40ml of 25% ammonia by weight for 2 hours, filter off the ammonia, wash in deionized water until the pH is about 8.5, dry the filter cake in an oven at 200°C for 3 hours; then soak the product in 100ml of 3% niobium oxalate Soak in salt solution for 5 hours, filter, dry in an oven at 150°C for 4 hours, and bake at 650°C for 5 hours; then soak the product in 50ml of 3% sodium fluoride solution, soak for 5 hours, filter, and Dry in an oven at 150°C for 4 hours, and bake at 800°C for 5 hours.

[0026] The above catalyst was added to 50ml 2% La(NO 3 ) 3 In the solution, the immersion time is 4 hours, after filtering, drying in an oven at 150°C for 4h, and roasting at 650°C for 5 hours; that is to obtain the multi-component La 2 o 3 / F / Nb 2 o 5 / Al 2 o 3 catalyst;

[0027] Put 20g of catalyst into a fixed-bed reactor with a diameter of Φ20mm, feed methyl tert-butyl ether with a liquid micro-sampling pump, and control the liquid space velocity...

Embodiment 2

[0029] 30 g γ-Al 2 o 3 Add it to 40ml of 10% ammonia by weight for 1 hour, filter off the ammonia, wash it in deionized water until the pH is about 8.5, and dry the filter cake in an oven at 200°C for 3 hours; then soak the product in 100ml of 8% niobium oxalate In ammonium solution, immersed for 5 hours, filtered, dried in an oven at 150°C for 4 hours, and roasted at 650°C for 5 hours; then the product was immersed in 50ml of 4% ammonium fluoride solution, immersed for 5 hours, filtered, and placed in Dry in an oven at 150°C for 4 hours, and bake at 800°C for 5 hours.

[0030] The above catalyst was added to 50ml 2% Ce(NO 3 ) 3 In the solution, the soaking time is 4 hours, after filtering, drying in an oven at 150°C for 4h, and roasting at 650°C for 5 hours, the multi-component Ce for preparing high-purity isobutene of the present invention is obtained 2 o 3 / F / Nb 2 o 5 / Al 2 o 3 catalyst;

[0031] Put 20g of catalyst into a fixed-bed reactor with a diameter of Φ20m...

Embodiment 3

[0033] 30 g γ-Al 2 o 3 Add it to 40ml of ammonia water with a weight concentration of 20% for 0.5h, filter off the ammonia water, wash in deionized water until the pH is about 8.5, and dry the filter cake in an oven at 200°C for 3h; then impregnate the product in 100ml of 5% fluorine Niobium chloride salt solution, immersed for 5 hours, filtered, dried in an oven at 150°C for 4 hours, and roasted at 650°C for 5 hours; then the product was immersed in 50ml of 5% hydrogen fluoride solution, immersed for 5 hours, filtered, and placed in Dry in an oven at 150°C for 4 hours, and bake at 800°C for 5 hours.

[0034] The above catalyst was added to 50ml 2% Sm(NO 3 ) 3 In the solution, the immersion time is 4 hours, after filtering, drying in an oven at 150°C for 4h, and roasting at 650°C for 5 hours, the multi-component Sm for preparing high-purity isobutene of the present invention is obtained. 2 o 3 / F / Nb 2 o 5 / Al 2 o 3 catalyst;

[0035] Put 20g of catalyst into a fixed-...

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 ZxOy / F / Nb2O5 / Al2O3 type solid acid catalyst for cracking methyl tertiary butyl ether to prepare high-purity isobutylene, and a preparation method of the catalyst. According to the preparation method, the catalyst comprises the following components in percentage by weight: 0.1-8 percent of ZxOy, 0.1-25 percent of F, 0.5-30 percent of Nb2O5 and 20-95 percent of Al2O3. Under the condition of ensuring high methyl tertiary butyl ether cracking conversion rate, the selectivity of the isobutylene and methyl alcohol nearly reaches 100 percent; meanwhile, inert matters such as water steam do not need to be added into a methyl tertiary butyl ether cracking reaction system, the reaction liquid space velocity of the catalyst is multiplied compared with the liquid space velocity of catalysts with the same type as that of the catalyst disclosed in the invetion, the energy consumption in the industrial production can be reduced, and the utilization rate of equipment is greatly improved.

Description

technical field [0001] The invention relates to the preparation and application of a catalyst for preparing high-purity isobutylene by cracking methyl tert-butyl ether, and mainly relates to a variety of active components loaded on Al 2 o 3 Z for the production of high-purity isobutene by cracking methyl tert-butyl ether x o y / F / Nb 2 o 5 / Al 2 o 3 type solid acid catalyst. Background technique [0002] Isobutene is widely used as an important chemical raw material. In recent decades, its social demand has been growing rapidly. It can not only be used to make gasoline and lubricating oil additives, but also can be used as an important auxiliary and raw material for other chemical products. For example, low-purity isobutylene is a raw material for antioxidants, pesticides, coatings, stabilizers and other fine chemicals. High-purity isobutylene is a monomer raw material for butyl rubber, isoprene rubber, polybutene resin, methyl methacrylate, etc. At the same time, ...

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 Applications(China)
IPC IPC(8): B01J27/125C07C11/09C07C1/20C07C31/04C07C29/00
CPCY02P20/52
Inventor 卢冠忠王筠松李运运朱耀国陆文龙郭杨龙郭耘王艳芹詹望成
Owner EAST CHINA UNIV OF SCI & TECH
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Eureka Blog
Learn More
PatSnap group products