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Process for the conversion of oxygenates to olefins

a technology of oxygenates and olefins, which is applied in the direction of catalyst regeneration/reactivation, physical/chemical process catalysts, metal/metal-oxide/metal-hydroxide catalysts, etc., which can solve the problems of low space-time yield compared to zeolitic pellets, and the use of extrudates shaped to monoliths as catalysts is particularly disadvantageous

Inactive Publication Date: 2014-01-02
BASF AG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The patent text suggests that there is a need for new catalysts and processes that can improve selectivities and resist deactivation in methanol-to-olefin processes. This is important because such improvements can lead to higher efficiency of existing and new processes, and reduce coking of the catalyst. In simple terms, the patent aims to provide better solutions for the production of olefins.

Problems solved by technology

In the case of such catalytic conversions, the challenge is to refine the catalysts used therein, and also the process regime and parameters thereof, in such a way that a few very specific products form with maximum selectivity in the catalytic conversion.
At relatively low temperatures and relatively high space velocities, however, lower space-time yields are described compared to the zeolitic pellets.
However, Hammon et al. describes the use of extrudates shaped to monoliths as catalysts as being particularly disadvantageous due to rapid coking and correspondingly short service lives.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1

Preparation of a Support Coated with ZSM-5

[0101]An aqueous suspension having a solids concentration of 40% by weight of H-ZSM-5 zeolite (ZEO-cat PZ2-100 H from Zeochem) with Si / Al=50 was prepared and homogenized in an ultrasound bath. Cylindrical honeycomb pieces of cordierite (900 cpsi, diameter 0.9 cm, length=11 cm) were dipped into this suspension and then blown dry with compressed air. The coated supports were then dried at 110° C. for 1 h and subsequently calcined at 550° C. for 3 h. The coating step was repeated until a loading of 0.5 g of zeolite per honeycomb piece (0.071 g / cm3) was attained.

example 2

Methanol-to-Olefin Process with Preceding Conversion of Methanol to Dimethyl Ether

[0102]2 g of the catalyst prepared according to comparative example 1 were mixed with 24 g of silicon carbide and installed in a continuous, electrically heated tubular reactor, such that the bed in the reactor has a length of 30 cm and a diameter of 12 mm. For the tests using the catalyst prepared according to example 1, two of the coated honeycomb bodies were installed in the reactor and sealed at the tube wall with glass fiber cord.

[0103]Upstream of the test reactor, methanol vapor was produced to give a gas stream comprising 75% by volume of methanol and 25% by volume of N2, which was converted to dimethyl ether by means of a preliminary reactor charged with 34 ml of alumina spall at 275° C. and an (absolute) pressure of 1-2 bar. The stream comprising dimethyl ether was then passed into the tubular reactor, and converted therein at a temperature of 450 to 500° C., a WHSV (=weight hourly space veloc...

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Abstract

The present invention relates to a process for converting oxygenates to olefins, comprising(1) providing a gas stream comprising one or more ethers;(2) contacting the gas stream provided in (1) with a catalyst,the catalyst comprisinga support substrate anda layer applied to the substrate,the layer comprising one or more zeolites of the MFI, MEL and / or MWW structure type.

Description

[0001]The present invention relates to a process for converting ethers to olefins using a catalyst in the form of a coated support substrate and using a catalyst for conversion of ethers to olefins which is obtainable according to the present invention.INTRODUCTION[0002]In view of increasing scarcity of mineral oil deposits which serve as starting material for preparation of lower hydrocarbons and derivatives thereof, alternative processes for preparing such commodity chemicals are becoming increasingly important. In alternative processes for obtaining lower hydrocarbons and derivatives thereof, specific catalysts are frequently used in order to obtain lower hydrocarbons and derivatives thereof, such as unsaturated lower hydrocarbons in particular, with maximum selectivity from other raw materials and / or chemicals. In this context, important processes include those in which methanol as a starting chemical is subjected to a catalytic conversion, which generally gives rise to a mixtur...

Claims

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Application Information

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IPC IPC(8): B01J29/70C07C1/22
CPCB01J29/7088C07C1/22B01J29/70B01J29/7049B01J29/7038C07C1/20C07C2529/40B01J38/02B01J23/02B01J23/10B01J29/80B01J29/90B01J37/0215B01J2219/2404B01J19/2485B01J2219/2434B01J2219/2438B01J2219/2446Y02P20/584B01J29/40Y02P30/20Y02P30/40B01J35/56C07C11/02B01J38/04B01J37/0236B01J37/08C07C2523/78
Inventor SPANNHOFF, KIRSTENPATCAS, FLORINA CORINASCHWAB, EKKEHARDWECK, ALEXANDERBAY, KEREM
Owner BASF AG
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