Activation of waste metal oxide as an oxygen carrier for chemical looping combustion applications

1. A process for combustion using a chemical looping combustion unit while producing a product stream comprising the steps of:

forming a black powder oxygen carrier by,

removing and collecting black powder that is formed in a gas pipeline;

pre-treating the collected black powder; and

activating the collected black powder to increase the reactivity and for the black powder oxygen carrier;

delivering fuel into a fuel reactor that contains an oxygen carrier which comprises the black powder oxygen carrier;

reducing the oxygen carrier in the presence of the fuel to provide gas-phase oxygen in the fuel reactor;

combusting the fuel under oxycombustion conditions within the fuel reactor to produce a product stream;

oxidizing the reduced oxygen carrier with air in the air reactor to produce the oxygen carrier; and

delivering the oxidized oxygen carrier back to the fuel reactor.

2. The process of claim 1 , wherein the black powder oxygen carrier comprises a fixed bed that is disposed in the fuel reactor and the fixed bed is fluidized by a stream of gas.

3. The process of claim 1 , wherein the fuel is a fuel selected from the group consisting of a gas feed, a liquid feed, and a solid feed.

4. The process of claim 3 , wherein the fuel is a solid fuel selected from the group consisting of coal and petcoke.

5. The process of claim 1 , wherein the black powder comprises iron hydroxides, iron oxides, and iron carbonates recovered from gas pipelines.

6. The process of claim 1 , wherein the black powder is removed from a gas pipeline and collected using at least one of a separator and cyclone device such that gas laden with black powder passes through the separator or cyclone, and black powder particles are knocked out of the gas stream to walls of the separator or cyclone, where they fall and are collected internally within the separator or cyclone in a collection media.

7. The process of claim 1 , wherein the collected black powder is pretreated via a synthesis method.

8. The process of claim 7 , wherein the synthesis method consists one of a spray drying process and a freeze granulation process.

9. The process of claim 1 , wherein the activation of the black powder comprises the step of:

using a flue gas to reduce the black powder and activate the black powder by increasing porosity and surface area of the black powder for improved gas-solid contact, thereby improving the reactivity of the black powder towards other gas, liquid or solid fuels.

10. The process of claim 9 , wherein the flue gas contains at least 10-50% of H 2 and at least 10-50% of CO.

11. The process of claim 1 , wherein the activation of the black powder comprises the step of mixing the black powder with one or more other metal oxides to increase the reactivity of the black powder.

12. The process of claim 11 , wherein the other metal oxide comprises a copper oxide, manganese oxide or a combination thereof.

13. The process of claim 1 , wherein the activation step includes passing a flue gas through the pre-treated black powder to produce the oxygen carrier, whereby the activation step increases porosity and surface area of the black powder for improved gas-solid contact, thereby improving the reactivity of the black powder towards other gas, liquid or solid fuels.

14. The process of claim 13 , wherein the activation step is a multi-stage step in which the flue gas is injected into the chemical looping combustion unit in five consecutive cycles to activate the pre-treated black powder.