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Treatment of cha-type molecular sieves and their use in the conversion of oxygenates to olefins

A technology of molecular sieves and oxygenates, applied in molecular sieve catalysts, including molecular sieve catalysts, and producing hydrocarbons from oxygen-containing organic compounds, etc., can solve the problems of reducing MTO performance and high selectivity

Inactive Publication Date: 2011-12-14
EXXONMOBIL CHEM PAT INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0019] Despite these synthetic advances, many of the resulting high silica CHA framework-type molecular sieves, and especially those synthesized in the absence of HF, show reduced MTO performance, such as undesired coke and methane ground height selectivity

Method used

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  • Treatment of cha-type molecular sieves and their use in the conversion of oxygenates to olefins
  • Treatment of cha-type molecular sieves and their use in the conversion of oxygenates to olefins
  • Treatment of cha-type molecular sieves and their use in the conversion of oxygenates to olefins

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0116] Example 1: Synthesis of high silica chabazite (no use of fluoride)

[0117] 42.72 g of N, N, N-trimethyladamantyl ammonium hydroxide (TMAAOH) 11.9 wt % aqueous solution was added to 9.24 g of deionized water, and then 8.04 g of 233 silica (PPG Industries, USA) was added to the mixture. Stir the mixture until a homogeneous gel results. 233 silica contains 0.53 wt% Na, 0.01 wt% K, 0.42 wt% alumina, and 82.2 wt% silica (the material has a Si / Al ratio of 164), and thus the composition of the gel is as follows:

[0118] 0.2TMAA:(1 / 120)Na 2 O:(1 / 328)Al 2 o 3 :1.0SiO2 2 :22H 2 o

[0119] The gel was divided into four equal fractions, denoted A-D, and each fraction was crystallized as described below.

[0120] Part A was aged at room temperature for 2 hours before adding 200PPM colloidal LEV seeds (14 wt% solids content, Si / Al=6 for the molecular sieve) based on the weight of the gel. The resulting mixture was sealed in a 23 mL Teflon-lined Parr autoclave and heated ...

Embodiment 2

[0127] Example 2: Calcination and NH 4 exchange

[0128] Calcined product A using the following protocol: (a) in flowing nitrogen, ramp to 400 °C at 10 °C / min and hold for 30 minutes; (b) switch to flowing air and start ramp at 10 °C / min to a temperature of 650°C and hold at 650°C for 4 hours. The calcined samples were ion-exchanged twice with 5 wt% ammonium chloride solution. Elemental analysis gave the following data (wt%) for the calcined and exchanged samples: Na 0.0125; Al 2 o 3 0.531 and SiO 2 84.4, which corresponds to Na 0.05 al 1.00 Si 134 .

Embodiment 3

[0129] Example 3: Gentle Steam Treatment

[0130] Calcination from Example 2 and NH 4 The exchanged samples were loaded into two enamel-bottomed quartz tubes with the enamel in the middle of the quartz tubes. The large pipe and two smaller pipes are arranged vertically in the pipe furnace. Nitrogen alone or nitrogen and steam in a molar ratio of 660:100 are fed into the pipe from the bottom of the large pipe. The total pressure is atmospheric pressure, and the temperature is increased rapidly to 500°C at a rate of 10°C / min, while continuing to feed nitrogen. After the temperature had stabilized at 500° C., feeding of nitrogen with steam was started. A first sample was recovered after 48 hours of steaming and a second sample was recovered after 96 hours. The MTO performance of these samples as well as the non-steamed samples prepared in Example 2 was tested.

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Abstract

A method is disclosed of treating a crystalline material comprising a CHA framework-type molecular sieve, wherein said crystalline material has a composition and involving the molar relationship: (n)X2O3:YO2, where X is a trivalent element, Y is a tetravalent element, and n is less than 0.07, and wherein the crystalline material does not comprise a silicoaluminophosphate, is substantially free of framework phosphorus, or both. The method can comprise treating the crystalline material with steam under conditions such that the prime olefin selectivity of the treated material in an oxygenate conversion process is greater than the prime olefin selectivity of the untreated material in the same process.

Description

technical field [0001] The present invention relates to a method for treating chabazite framework molecular sieves and the use of the treated molecular sieves in converting oxygenates into olefins. Background technique [0002] The conversion of oxygenates to olefins (OTO) is currently the subject of intense research because of its potential to replace the long-standing steam cracking technology, which is today the industry standard for producing world-scale quantities of ethylene and propylene. The very large volumes involved suggest that there is a significantly large economic incentive for alternative technologies that can transport high production quantities of light olefins in a cost-effective manner. Whereas steam cracking relies on non-selective thermal reactions of naphtha-range hydrocarbons at very high temperatures, OTO utilizes the catalytic and microstructural properties of acidic molecular sieves at relatively mild temperature conditions to produce high yields o...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/70B01J37/10C01B39/00C10G3/00C07C1/20
CPCC10G3/49B01J37/10C01B39/026C10G2300/807C07C1/20C01B39/46B01J29/7015C07C2529/70B01J2229/36C10G2400/20C10G3/62B01J2229/24C01B39/48Y02P30/20
Inventor 曹光M·J·沙赫
Owner EXXONMOBIL CHEM PAT INC