System and method for ammonia synthesis

Abstract

Systems and methods are disclosed herein for synthesizing ammonia using nano-size metal or metal alloy catalyst particles. Hydrogen and nitrogen gases are passed through a system comprising, for example, a bed of magnetite supporting nano-size iron or iron alloy catalyst particles having an optional oxide layer that forms the catalyst.

Description

RELATED APPLICATION[0001]This application is a continuation of U.S. patent application Ser. No. 12 / 752,018, filed Mar. 31, 2010, which is a continuation-in-part of U.S. patent application Ser. No. 12 / 418,356, filed Apr. 3, 2009, which is a continuation-in-part of U.S. patent application Ser. No. 12 / 266,477, filed on Nov. 6, 2008, which claims priority from Provisional Application No. 60 / 985,855, filed on Nov. 6, 2007, the entire contents of each of which are hereby incorporated by this express reference.BACKGROUND[0002]1. Technical Field[0003]The disclosure relates generally to the synthesis of useful chemical byproducts and, more specifically, to the synthesis of ammonia using nano-size metal catalyst particles.[0004]2. Related Art[0005]Ammonia synthesis is an important industrial process. Ammonia is produced in huge quantities worldwide, for use in the fertilizer industry, as a precursor for nitric acid and nitrates for the explosives industry, and as a raw material for various in...

AI Technical Summary

Benefits of technology

"The invention is about a new method for making ammonia using nanoparticle catalysts on a support material. This method improves catalytic activity while reducing sintering of the catalyst particles, which means the particles can separate and function independently. The nanoparticle catalysts can be used in both traditional and new ammonia reactor designs. The new method allows for lower pressures and higher efficiency compared to the traditional Haber-Bosch process. The support material can be ferrous materials, such as magnetite or other ferrous materials, or other materials like silicon nitride or silicon dioxide. The support material can also contain promoter molecules to further enhance the interaction between the catalyst particles and the support material. The new method can be used in a plug flow reactor, a packed bed reactor, an adiabatic reactor, or an isothermal reactor. The invention also includes a NOx remediation system and a selective catalytic reduction system for reducing NO emissions."

Problems solved by technology

However, in practice, both high pressures and temperatures are used due to a sluggish reaction rate.

Due to overall low reaction efficiency when hydrogen and nitrogen are first passed over the catalyst bed, most ammonia production plants utilize multiple adiabatically heated catalyst beds with cooling between beds, typically with axial or radial flow.

High pressure favors the adsorption process as well, but at a cost of increased operational and capital costs.

Nevertheless, due in part to high pressures used in the process, ammonia production requires reactors with heavily-reinforced walls, piping and fittings, as well as a series of powerful compressors, all with high capital cost.

In addition, generation of those high pressures during plant operation requires a large expenditure in energy.

Use of this catalyst allowed the reactor pressure to be reduced, but the high cost of the precious metal ruthenium catalyst and the sensitivity of the catalyst to impurities in the hydrogen feed stock have prevented widespread use for ammonia synthesis.

Other catalysts being studied include cobalt doped with ruthenium, but few encouraging results have been exhibited to date.

Suggestions of reducing the processing pressures have been made, but have not been achieved economically.

U.S. Pat. No. 3,653,831 describes the addition of platinum to improve reaction efficiency, however given the expense of platinum this may not be feasible at large scales.

Retrofit and reconstruction of these plants could be costly should there be a need to change design based on catalyst properties, such as space velocity.

Non-ferrous catalysts in the above referenced prior art do not overcome all of these constraints because 1) catalyst cost increases more than catalyst efficiency, 2) the catalyst may not have the same properties that allow for seamless operation in existing ammonia production plants, or 3) the catalyst may have high activity but do not meet long term durability requirements.

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