Catalytic forms and formulations

a catalytic and form technology, applied in the field of catalytic forms and formulations, can solve the problems of reducing the yield of undesired side products, affecting the reaction rate, and often limiting the adsorption rate of reactants,

Inactive Publication Date: 2014-05-01
SILURIA TECH INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0010]In brief, catalytic forms and formulations and related methods are disclosed. In one embodiment, the disclosure provides a catalytic material comprising a plurality of catalysts in combination with a diluent or support, for example in some embodiments the catalysts are catalytic nanowires. The catalytic materials find utility in various catalytic reactions. In one particular embodiment, the catalytic materials are useful for petrochemical catalysis, such as the oxidative coupling of methane.

Problems solved by technology

Thus, at a given temperature, a positive catalyst tends to increase the yield of desired product while decreasing the yield of undesired side products.
Although catalysts are not consumed by the reaction itself, they may be inhibited, deactivated or destroyed by secondary processes, resulting in loss of catalytic activity.
This transport and adsorption of reactants is often the rate limiting step in a heterogeneous catalysis reaction.
To date, the OCM reaction has not been commercialized, due in large part to the lack of effective catalysts and catalytic forms.
The use of heterogeneous catalysts, for example in the OCM reaction, presents a number of challenges, especially on a commercial scale.
However, when a fixed bed of heterogeneous catalyst is used, the pressure drop across the catalytic bed prevents operation under the high gas space velocities demanded of a commercial operation.
In addition, many commercially important catalytic reactions, such as OCM, are exothermic and controlling the exotherm (i.e., hotspots) within the catalytic bed can be difficult.

Method used

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Examples

Experimental program
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example 1

Preparation of Supported MnWO4 Nanowire Catalysts

[0414]Supported MnWO4 nanowire catalysts are prepared using the following general protocol. MnWO4 nanowires are prepared using the method described in U.S. Pub. No. 2012 / 0041246. Manganese tungstate nanowires, support, and water are slurried for 6 h at room temperature. The manganese tungstate to support ratio ranges from 2-10 wt %. The mixture is dried in a 65° C. oven and then calcined in a muffle oven in air: load in the furnace at room temperature, ramp to 400° C. with 5° C. / min rate, dwell for 2 h, ramp to 850° C. with 5° C. / min rate, dwell for 8 h, cool to room temperature. The following is a list of exemplary supports that may be used: SiO2, Al2O3, SiO2—Al2O3, ZrO2, TiO2, HfO2, Silica-Aluminum Phosphate, and Aluminum Phosphate.

example 2

Preparation of Catalytic Material Comprising Cordierite Honeycomb Ceramic Supported Nd2O3 Nanowires

[0415]Nd2O3 nanowires are prepared using the methods described in U.S. Pub. No. 2012 / 0041246.

[0416]A 400 mg aliquot of Nd2O3 nanowires is mixed with 2 g of DI water and placed into a 5 ml glass vial containing 2 mm Yttria Stabilized Zirconia milling balls. The vial is placed on a shaker at 2000 RPM and agitated for 30 minutes. A thick slurry is obtained.

[0417]A ⅜ inch diameter core is cut along the channel direction into a 400 CPSI (channel per square inch) cordierite honeycomb monolith and cut in length so the core volume is approximately 1 ml.

[0418]The core is placed into a ⅜ inch tube, and the catalyst slurry is fed on top of the ceramic core and pushed with compressed air through the monolith channel. The excess slurry is captured into a 20 ml vial. The coated core is removed from the ⅜ inch tube and placed into a drying oven at 200° C. for 1 hour.

[0419]The coating step is repeated...

example 3

Preparation of Catalytic Material Comprising Silicon Carbide Ceramic Foam Supported Nd2O3 Nanowires

[0420]Nd2O3 nanowires were prepared using the methods described in U.S. Pub. No. 2012 / 0041246.

[0421]A 400 mg aliquot of Nd2O3 nanowires is mixed with 2 g of DI water and placed into a 5 ml glass vial containing 2 mm Yttria Stabilized Zirconia milling balls. The vial is placed on a shaker at 2000 RPM and agitated for 30 minutes. A thick slurry is obtained.

[0422]A ⅜ inch diameter core is cut from a 65 PPI (Pore Per Inch) SiC foam and cut in length so the core volume is approximately 1 ml.

[0423]The core is placed into a ⅜ inch tube and the catalyst slurry is fed on top of the ceramic core and pushed with compressed air through the monolith channel. The excess slurry is captured into a 20 ml vial. The coated core is removed from the ⅜ inch tube and placed into a drying oven at 200° C. for 1 hour.

[0424]The coating step is repeated two more times with the remaining slurry followed by drying ...

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Abstract

Catalytic forms and formulations are provided. The catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed.

Description

BACKGROUND[0001]1. Technical Field[0002]This invention is generally related to catalytic forms and formulations and, more specifically, to catalytic forms and formulations useful in a variety of catalytic reactions, such as the oxidative coupling of methane.[0003]2. Description of the Related Art[0004]Catalysis is the process in which the rate of a chemical reaction is either increased or decreased by means of a catalyst. Positive catalysts increase the speed of a chemical reaction, while negative catalysts slow it down. Substances that increase the activity of a catalyst are referred to as promoters or activators, and substances that deactivate a catalyst are referred to as catalytic poisons or deactivators. Unlike other reagents, a catalyst is not consumed by the chemical reaction, but instead participates in multiple chemical transformations. In the case of positive catalysts, the catalytic reaction generally has a lower rate-limiting free energy change to the transition state th...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): B01J29/70B01J27/188C07C2/06B01J23/10C07C2/82B01J27/224B01J23/34
CPCC07C2523/02C07C2/84C07C2523/30C07C2523/34C07C2527/224C07C2523/10B01J37/0018B01J29/7049B01J23/10B01J23/34B01J27/188B01J27/224C07C2/06C07C2/82B01J35/023B01J35/04B01J35/06B01J35/1009B01J35/1014B01J35/1033B01J37/0009C07C11/04B01J37/0234B01J29/06B01J35/0013B01J35/026B01J37/0211B01J37/0215B82Y30/00Y02P20/52
Inventor CIZERON, JOEL M.ZURCHER, FABIO R.MCCORMICK, JARODGAMORAS, JOELVOGEL, ROGERVINCENT, JOEL DAVIDNYCE, GREGSCHAMMEL, WAYNE P.SCHER, ERIK C.ROSENBERG, DANIELRAS, ERIK-JANFREER, ERIK
Owner SILURIA TECH INC
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