Metal alloy/oxide composite catalyst for ammonia decomposition
The present invention discloses a series of ammonia decomposition catalysts, the method of making such catalysts and the use of such catalysts. The said catalysts are made of composite metal or metal alloys supported on composite oxides or nitrides as the catalyst supports. The catalysts are useful in ammonia decomposition at various temperatures and pressures, including temperatures below 500° C. and pressures up to 30 atm.
1. A catalyst, adapted for use in ammonia decomposition, comprising:
a first element comprising cobalt; chromium, manganese, and vanadium;
a second element comprising nickel;
a support; and
a promoter;
wherein the first element and the second element are combined to form
an alloy;
wherein the alloy is supported on the support, the support comprising a mixed oxide of:
comprising at least two of magnesium oxide, calcium oxide, strontium oxide and barium oxide; and at least one of cerium oxide, lanthanum oxide, and praseodymium oxide; and
wherein the promoter is an alkali metal.
2. The catalyst of claim 1 , wherein the alkali metal of the promoter is at least one of potassium, cesium, sodium, lithium, and rubidium.
3. The catalyst of claim 1 , wherein the catalyst comprises the first element and the second element at a concentration between fifteen percent and eighty-five percent by mass.
4. The catalyst of claim 1 , wherein the alloy is a bimetallic nanocluster.
5. A system for decomposing ammonia, comprising:
a catalyst of claim 1 ;
a liquid comprising ammonia;
a pump;
a heat exchanger for vaporizing the liquid ammonia;
a reactor; and
a purification unit;
wherein the liquid is contained in a container, wherein the pump is configured to receive the liquid from the container and guide the liquid to a heat exchanger, wherein the heat exchanger is configured to vaporize the liquid into a vapor and feed the vapor to a reactor, wherein the reactor comprises the catalyst and is configured to decompose the vapor into a mixture comprising hydrogen and nitrogen, and wherein the reactor is configured to guide the mixture to the heat exchanger, wherein the heat exchanger is further configured to reduce a temperature of the mixture and guide the liquid to the purification unit, and wherein the purification unit is configured to separate the hydrogen from the mixture.
6. The system of claim 5 , wherein the heat exchanger is configured to adjust the temperature of the liquid to temperatures below 500 degrees Celsius.
7. The system of claim 5 , wherein the heat exchanger is configured to adjust the temperature of the liquid to temperatures at or above 500 degrees Celsius.
8. A system, comprising:
a liquid comprising ammonia; and
a catalyst of claim 1 .