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Catalyst used for production of isobutene via isomerization of n-butene skeleton and combined production of propylene, and preparation method and applications thereof

A catalyst, n-butene technology, applied in the direction of isomerization hydrocarbon production, molecular sieve catalyst, chemical instruments and methods, etc., can solve the problem of low single-pass utilization rate of n-butene

Active Publication Date: 2014-05-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] In the above-mentioned method, hydrogen-type FER zeolite is used as a catalyst, and there is a low single-pass utilization rate of n-butene. In addition to the highly selective generation of isobutene, a small amount of high value-added propylene, ethylene and pentene are also generated, such as propylene and pentene in EP 0,501,577. The yield ratio of isobutene is 0.02; the highest yield ratio of propylene and isobutene in US 5,499,851 is 0.03

Method used

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  • Catalyst used for production of isobutene via isomerization of n-butene skeleton and combined production of propylene, and preparation method and applications thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1~3

[0018] Preparation of sodium potassium hydrogen type FER molecular sieve.

[0019] Ferrerite molecular sieves and NH with different concentrations of ammonium ions 4 Mix the Cl aqueous solution evenly and make a slurry, change the mass ratio of the ferrerite molecular sieve solid to the exchange liquid, stir at different temperatures for 2 hours, filter, and thoroughly rinse the obtained filter cake with deionized water 30 times the dry basis weight of the ferrerite molecular sieve, and dry it at 110°C Calcined at 550°C to obtain sodium potassium hydrogen type FER molecular sieves, which are marked as NaKH-1, NaKH-2 and NaKH-3 respectively. In percent by weight, adopt X-ray fluorescence spectrometry to measure the Na of the sodium potassium hydrogen type FER molecular sieve that makes. 2 O and K 2 O content. Preparation conditions and measured Na of sodium potassium hydrogen type FER molecular sieve 2 O and K 2 The O content is shown in Table 1.

[0020] Table 1 Preparat...

Embodiment 4

[0024] HZSM-5 molecular sieve preparation.

[0025] In the high-pressure hydrothermal synthesis kettle, add 1 part of sodium hydroxide, 1.5 parts of aluminum sulfate, 1.8 parts of tetrapropylammonium hydroxide, 30 parts of silica sol (containing 26% by weight of SiO 2 ) and 40 parts of water, stirred evenly, crystallized at 180°C for 72 hours, filtered and washed, dried at 110°C, roasted at 550°C for 6 hours in a nitrogen atmosphere, and then roasted in an air atmosphere at 550°C for 6 hours to prepare Get the original powder of ZSM-5. 200 g of ZSM-5 molecular sieves, 214 g of NH 4 Cl and 4000 g of deionized water were mixed evenly for beating, stirred at 75°C for 2 hours, filtered, and the above exchange process was repeated 3-5 times at 75°C, and filtered after the exchange, the obtained filter cake was used 30 times as much as ZSM-5 The molecular sieve was thoroughly rinsed with deionized water on a dry basis, dried at 110°C and calcined at 550°C to obtain a hydrogen-type...

Embodiment 5~8

[0027] Catalyst preparation.

[0028]After dry mixing the NaKH-FER molecular sieve powder prepared in Examples 1-3 and the HZSM-5 molecular sieve powder prepared in Example 4, mixed molecular sieves with different weight ratios of NaKH-FER / HZSM-5 were prepared. Palladium chloride-hydrochloric acid solution was used to impregnate the mixed molecular sieve powder with equal volume, impregnated at room temperature for 8 hours, then dried at 110°C for 24 hours, and then roasted at 550°C for 5 hours to finally obtain palladium-containing mixed molecular sieves with different palladium contents. Then knead the prepared palladium-containing mixed molecular sieve with SW-17 aluminum hydroxide powder, scallop powder, nitric acid and deionized water in a CD4X1TS multifunctional catalyst molding machine to form a thick paste, which is molded by a stainless steel with 1.5 mm holes Board extrusion. The obtained extrudates were first dried at room temperature for 24 hours, then dried at 11...

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Abstract

The invention discloses a catalyst used for production of isobutene via isomerization of n-butene skeleton and combined production of propylene. The catalyst is composed of a molecular sieve A, a molecular sieve B, a precious metal, and a binder; the total weight of the molecular sieve A and the molecular sieve B accounts for 50 to 90% of the weight of the catalyst; weight ratio of the molecular sieve A to the molecular sieve B ranges from 1:9 to 9:1; the weight of the precious metal accounts for 0.001 to 0.05% of the weight of the catalyst; the molecular sieve A is sodium-potassium-hydrogen-type FER molecular sieve, and comprises, by weight, 0.1 to 0.4% of Na2O, and 4.5 to 6.3% of K2O; the molecular sieve B is HZSM-5 molecular sieve; and the precious metal is platinum or palladium. The catalyst is capable of increasing both yield of isobutene and propylene at the same time.

Description

technical field [0001] The invention relates to a catalyst for producing isobutene and co-producing propylene through isomerization of n-butene and its preparation method and application. Background technique [0002] As the market demand for high-octane gasoline continues to grow, so too does the need for the incorporation of methyl tert-butyl ether (MTBE) as an octane booster. For example, China's gasoline output in 2011 was 81.411 million tons. Based on the average MTBE blending ratio of 4.5%, the total demand for MTBE exceeded 3.5 million tons. The high market demand of MTBE is bound to drive the demand for raw material isobutene, but the isobutene produced by traditional catalytic cracking and ethylene cracking routes is difficult to meet the market demand. On the other hand, the utilization rate of n-butene in C4 after MTBE by-product ether is low, and it is often mixed into civil liquefied gas and burned. [0003] The process of producing isobutene by skeletal isome...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/80C07C5/27C07C11/09C07C11/06C07C4/06
CPCY02P20/52
Inventor 周峰陈明张淑梅翟庆铜张宝国苏杰
Owner CHINA PETROLEUM & CHEM CORP