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Catalyst and preparation method

A catalyst and catalytic metal technology, applied in molecular sieve catalysts, chemical instruments and methods, separation methods, etc., can solve problems such as a large amount of hydrocarbon storage, reduced conversion efficiency, and catalyst HC leakage.

Inactive Publication Date: 2016-12-14
GENERAL ELECTRIC CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, beyond the temperature range of 300°C to 400°C, the conversion efficiency may decrease
In addition, this technology may have HC leakage in the catalyst, transport and store a large amount of hydrocarbons on site, and may release HC at atmospheric pressure

Method used

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  • Catalyst and preparation method
  • Catalyst and preparation method
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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0105] Embodiment 1: Preparation of silver nanocrystals

[0106]At a temperature of about 25°C (room temperature), silver acetate (4 mmol, SA), oleic acid (4 ml, OA, technical grade, 90%, Aldrich) and trioctyl were added to a 3-neck flask equipped with a stirrer. Amine (15 mL, TOA). The resulting mixture was heated to a temperature of about 60°C under a vacuum of 1 mm Hg. As the temperature increases, silver acetate begins to dissolve in trioctylamine. Bubbling was observed in the flask due to the boiling of water present as an impurity in the reaction mass. Water is removed under vacuum as water vapor. When the temperature was raised to 60°C, silver acetate was completely dissolved in trioctylamine, and the resulting solution turned brown-grey-black, indicating that silver acetate decomposed and silver nanocrystals were formed. The temperature was then raised to 90°C and the mixture was maintained at this temperature for about 2 hours to ensure completion of the reaction....

Embodiment 2-3

[0113] Embodiment 2-3: Preparation of silver nanocrystals

[0114] Examples 2 and 3 were performed in a manner similar to that described above for Example 1, except that they were performed on a relatively larger scale. The amounts of silver acetate, oleic acid and trioctylamine used and the concentration of the resulting AgNCs in hexane and the PSD of the AgNCs are included in Table 3 below. Examples 2 and 3 show that a PSD of less than 10% can be achieved even in large scale batches.

[0115] table 3

[0116]

Embodiment 4-7

[0117] Example 4-7: Preparation of the first catalytic composition

[0118] To a 3-neck flask equipped with a stirrer was added aluminum tri-sec-butoxide (50 g) and IPA (200 mL). Then, a predetermined amount of AgNC in a hexane solution containing 43.1 grams (0.4 moles) of AgNC in hexane was added to the flask to form a first solution. The predetermined amount of AgNC in the added hexane solution and the resulting loading of AgNC in the catalyst composition are included in Table 4 below. After addition to the flask, in a separate flask with a mechanical stirrer turned on at about 60 rpm, ethyl acetoacetate (2.65 g), Triton X-114 (14 g) and 65 mL of isopropanol were added , to form the second solution. Then pour the second solution into the first solution. The resulting mixture was stirred at a temperature of about 25° C. at a speed of about 180 rpm for about 30 minutes. During 30 min of stirring, a mixture of 7.5 mL of distilled water and 85 mL of isopropanol was added dro...

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Abstract

A catalyst system comprising a first catalytic composition comprising a homogeneous solid mixture comprising at least one catalytic metal and at least one metal inorganic support. The pores of the solid mixture have an average pore size of from about 1 nanometer to about 15 nanometers. Catalytic metals include nanocrystals.

Description

technical field [0001] The systems and techniques include embodiments involving catalysts. They also include embodiments involving the preparation of catalysts and systems that may contain catalysts. Background technique [0002] Exhaust streams from fossil fuel combustion (e.g., furnaces, ovens, and engines) contain a variety of potentially unwanted combustion products, including nitrogen oxides (NO x ), unburned hydrocarbons (HC) and carbon monoxide (CO). NO x , although thermodynamically unstable, cannot decompose spontaneously without a catalyst. The exhaust stream may utilize an exhaust treatment device to remove NO from the exhaust stream x . [0003] Examples of exhaust treatment devices include catalytic converters (e.g., three-way catalysts, oxidation catalysts, selective catalytic reduction (SCR) catalysts, etc.), evaporative emissions devices, scrubbers (e.g., hydrocarbons (HC), sulfur, etc.), particulate Filter / trap, adsorber / absorber, plasma reactor (eg, n...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/50B01J23/30B01J29/69B01J23/46B01J35/10B01D53/94B01D53/56F01N3/08F01N3/28
Inventor M·殷L·N·路易斯O·P·西克罗文D·汉库B·H·温克勒D·G·诺尔顿A·B·马德什瓦
Owner GENERAL ELECTRIC CO