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Catalyst composition for selective hydrogenation with improved properties

A catalyst and selective technology, applied in the direction of hydrocarbons, physical/chemical process catalysts, organic compounds/hydrides/coordination complex catalysts, etc., can solve the problems of expensive ionic liquids, reduced activity, and large additional costs. Achieve the effect of high selectivity, small loss and high "runaway" temperature

Active Publication Date: 2017-05-10
CLARIANT PROD DEUT GMBH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This often results in the catalyst filling most of the pores and thus reducing the activity
Ionic liquids are also expensive, which leads to significant additional costs for the overall catalyst formulation

Method used

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  • Catalyst composition for selective hydrogenation with improved properties
  • Catalyst composition for selective hydrogenation with improved properties
  • Catalyst composition for selective hydrogenation with improved properties

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0077] Specimen A contains a BET surface area of ​​4.0m 2 0.017 wt% Pd on 1-2mm alumina spheres / g. To prepare sample A, 1100 g of α-alumina was added to 1075 mL of PdCl heated at 70 °C 2 solution (0.178 mg Pd / mL). After soaking the support in the solution for 1 hour, the solution was drained and the catalyst was washed 10 times with room temperature deionized water using a soak time of 5 minutes. After the final wash, the catalyst was calcined in air at 565° C. for 4 hours in a muffle furnace.

[0078] Sample A1 was prepared by adding 0.5% by weight of EMIM [EtSO 4 ] (1-Ethyl-3-methylimidazolium ethylsulfate) and prepared. To prepare Sample A1, Sample A (516.0 mg) was impregnated with 1-ethyl-3-methylimidazolium ethylsulfate aqueous solution (232 μL, 11.11 mg / mL) by incipient wetness. The catalyst was dried at 80 °C for 16 h and heated at 100 °C in 5% H 2 / N 2 Medium reduction for 1 hour.

[0079] Sample A2 was prepared by adding 0.5% by weight of BMIM[OTf] (1-butyl-3-...

Embodiment 2

[0101] Sample B1 was prepared by adding 0.001% by weight EMIM [EtSO 4 ] (1-Ethyl-3-methylimidazolium ethylsulfate) and prepared. To prepare Sample B1, Sample A (485.8 mg) was impregnated with an aqueous solution of 1-ethyl-3-methylimidazolium ethylsulfate (219 μL, 0.022 mg / mL) by incipient wetness. The catalyst was dried at 80 °C for 16 h and heated at 100 °C in 5% H 2 / N 2 Medium reduction for 1 hour.

[0102] Sample B2 was added by adding 0.007 wt% EMIM[EtSO 4 ] (1-Ethyl-3-methylimidazolium ethylsulfate) and prepared. To prepare sample B2, sample A (505.1 mg) was impregnated with an aqueous solution of 1-ethyl-3-methylimidazolium ethylsulfate (227 μL, 0.16 mg / mL) by incipient wetness. The catalyst was dried at 80 °C for 16 h and heated at 100 °C in 5% H 2 / N 2 Medium reduction for 1 hour.

[0103] Sample B3 was prepared by adding 0.025% by weight EMIM [EtSO 4] (1-Ethyl-3-methylimidazolium ethylsulfate) and prepared. To prepare sample B3, sample A (512.8 mg) was imp...

Embodiment 4

[0112] Sample A, Samples A1-A22, Samples B1-B6, and Control Samples C, C1, and C2 were tested in the as-prepared form in a microreactor test setup under typical front-end hydrogenation conditions . In the test, a simulated depropanizer feed containing 0.35 mol% acetylene, 15 mol% hydrogen, 0.02 mol% CO, 47 mol% ethylene, and balance nitrogen was fed at a total pressure of 478 psig (34 bar) and 7000 h -1 260 μL of the catalyst bed was passed at gas hourly space velocity (GHSV) while gradually increasing the bed temperature from about 45°C. The acetylene concentration at the reactor outlet was monitored by on-line gas chromatography (GC). The acetylene concentration at the reactor outlet continued to decrease with increasing temperature until it reached 2% due to increased non-selective reaction of hydrogen with ethylene. The temperature range between T1 and T2 is called the "operating window". The test results of Sample A, Samples A1-A22, Samples B1-B6 and Control Samples C,...

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Abstract

The present invention relates to heterogeneous catalysts useful for the selective hydrogenation of unsaturated hydrocarbons, which comprise palladium and optionally a cocatalyst supported on a substrate and have an uncoated BET surface area of ​​<9 m2 / g, wherein the surface is coated coated with ionic liquid. Also described are methods of preparing the catalysts and methods of selectively hydrogenating acetylene in a front-end mixed olefin feed.

Description

[0001] field of invention [0002] The present invention relates to a catalyst composition for selective hydrogenation, for example for the selective hydrogenation of acetylene in the gas phase, comprising a BET surface area ≤ 9m 2 / g and a heterogeneous catalyst with ionic liquid applied on its surface. The catalyst composition has improved properties, such as improved selectivity for desired products and better thermal stability. [0003] Background of the invention [0004] Ethylene and propylene are important monomers used to produce plastics such as polyethylene or polypropylene. Ethylene and propylene are mainly derived from petroleum and petroleum products obtained by thermal or catalytic cracking of hydrocarbons. However, the ethylene or propylene obtained by means of the cracking process contains an undesirably high proportion of acetylenic compounds, such as ethylene or methylacetylene (propyne), which can have a negative effect on the downstream ethylene or propyle...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J31/02B01J23/44B01J37/02C07C5/09C07C7/167
CPCB01J23/44B01J31/0277B01J31/0279B01J31/0281B01J31/0282B01J31/0284B01J37/0215C07C7/167B01J2531/824B01J21/04B01J23/50B01J2231/645Y02P20/52B01J35/612C07C11/04
Inventor N·斯则斯尼R·菲舍尔A·哈格梅尔F·格罗斯曼H·C·侯J·博伊尔孙明永M·乌本希克C·鲁戈梅尔D·M·洛维
Owner CLARIANT PROD DEUT GMBH