Methods utilizing durable functional materials for chemical processes that include an oxidation step

Abstract

The present disclosure is directed to methods using durable functional materials for processes that include an oxidation step. The durable functional materials are redox active oxygen carrier materials that include a zirconia or yttria-stabilized-zirconia (YSZ) matrix containing a redox-active metal ion(s), such as, but not limited to Fe, Mn, Cu, Co and Cr. In an embodiment, these materials are used in chemical looping processes.

Claims

1. A method, comprising contacting a redox active oxygen carrier material with a fluid stream to reduce a redox active metal oxide in the redox active oxygen carrier material and oxidize a component in the fluid stream; and contacting the redox active oxygen carrier material with a second fluid stream to oxidize the reduced redox active metal; wherein redox active oxygen carrier material comprises a redox active metal ion atomically dispersed in a zirconia or yttria-stabilized zirconia matrix.

2. The method of claim 1, wherein the fluid stream comprises a carbon or hydrocarbon.

3. The method of claim 2, wherein the hydrocarbon is selected from a group consisting of methane, ethane, propane, butane, kerosene, diesel fuel, coke, biomass and coal.

4. The method of claim 1, further comprising: contacting the redox active oxygen carrier material with a second fluid stream to oxidize the reduced redox active metal oxide and form partially reduced products.

5. The method of claim 4, wherein the partially oxidized products are selected from a group consisting of hydrogen and carbon monoxide.

6. The method of claim 1, wherein the redox active metal ion is selected from a group consisting of ions of Fe, Mn, Cu, Co and Cr.

7. The method of claim 1, further comprising: wherein the second fluid stream comprises air; and reducing the redox active oxygen carrier material with a hydrocarbon or via thermal means, and reducing the redox oxygen carrier material to produce oxygen.

8. The method of claim 1, wherein the fluid stream comprises steam and a hydrocarbon.

9. The method of claim 1, wherein the fluid stream comprises carbon dioxide and a hydrocarbon.

10. The method of claim 1, wherein the fluid stream comprises steam and a hydrocarbon.

11. The method of claim 1, wherein the fluid stream comprises water and a hydrocarbon.

Description

DETAILED DESCRIPTION OF THE INVENTION

(1) The present disclosure is directed to chemical looping oxidation processes that use a composite or hybrid material composed of redox active metal oxide or oxides and a thermally stable oxygen-ion-conducting matrix. These materials may be referred to as redox active oxygen carrier materials. The redox active metal oxide is selected from a group including Fe, Mn, Cu, Co, Cr, and other transition metals and mixtures thereof. The redox active metal oxide is incorporated into crystalline zirconia or yttria-stabilized zirconia (YSZ) at the atomic scale; for example, the transition metal cation can substitute for Zr or occupy a vacant site in the crystal lattice. In this disclosure, this material may be referred to as the metal oxide/matrix material. In this material, the oxygen capacity is provided by the multiple redox states available to the redox metal. The zirconia or YSZ matrix provides a robust and thermally-stable structural foundation and accommodates the metal ion reduction by the formation of lattice oxygen vacancies; high oxygen conductivity facilitates oxygen mobility in and out of the matrix and ensures that the redox capacity can be fully realized. Additional additives may be used to manipulate metal solubility and other properties such as oxygen transport. For example, an additional solubility may be introduced by doping the metal oxide/matrix material with multiple reducible cations.

(2) The metal oxide/matrix materials form a single, active phase composite, in contrast to the prior art materials that consist of an active oxide supported on an inert carrier matrix. The material can be expected to have many of the favorable physical attributes of zirconia or YSZ. The transport properties of the YSZ or zirconia will minimize or eliminate the need for high surface area, e.g. porosity. There is no second active phase to migrate, infiltrate, volatilize, change in volume or experience other significant changes that may to degrade the performance, chemical or physical, over time. These issues are all bypassed by beginning with a material in a thermodynamically stable (or near-stable) condition.

(3) Using Fe as an example, the redox or oxygen storage capacity is largely limited by the amount of Fe that can be solubilized in the carrier matrix. Fe in excess of this concentration is less stable, and the mobility of the Fe cation could contribute over the long term to physical degradation. The approach to increase the oxygen capacity is to increase the amount of soluble redox capable metals via simple substitution and co-doping, for example with Mn and similar cations. The solubility of Mn in YSZ has reported to be 15 mol % in 8-YSZ (Mn/(Mn+Zr+Y)) and as high 32 mol % (Mn/(Mn+Zr)) in ZrO.sub.2 at elevated temperatures. Other reports suggest that single phase (by powder X-ray diffraction) Mn-, Co-, Cr-, Fe-, and Ni-doped cubic zirconia can all be prepared at 20 mol % transition metal (TM) concentration (TM/(TM+Zr)). In the case of Mn, one may expect the oxygen capacity to be increased relative to Fe not only by improved solubility, but also by the fact that the Mn could conceivably cycle between the +4 and +2 oxidation states (as opposed to +3 and +2 for Fe).

(4) In the Fe/zirconia and Fe/YSZ oxygen carrier systems described herein, the zirconia or yttria-stabilized zirconia can be doped with iron up to the solubility limit (about 10 mol % Fe depending on the temperature and redox state of the Fe). In these materials, the Fe is homogeneously dispersed throughout the zirconia or YSZ at the atomic scale. The redox active oxygen carrier maintains important properties of both parents; the dissolved Fe is redox active while the zirconia or YSZ provides transport of oxygen into and out of the bulk solid making the Fe highly accessible for reaction. This form of the material is highly stable and to the best of our knowledge can be chemically or thermally reduced and reoxidized indefinitely; there is no separate iron oxide phase to mobilize or agglomerate, and the reaction is not surface limited.

(5) The processes described herein provides benefit over conventional approaches to these materials wherein the Fe would be supported on the surface of a high surface area carrier, e.g alumina. As these materials are cycled and age, iron migrates and agglomerates (precipitates) to form ever larger particles. As the particles grow, the portion of the Fe that can be effectively utilized for reaction decreases, since the reaction becomes surface-limited. Though both systems contain Fe, the Fe in the conventional system remains largely as a phase that is distinct from the support at the temperatures of relevance to chemical looping.

(6) The disclosed chemical looping processes include two steps. In the first step, the solid redox-active oxygen carrier is exposed to a stream containing chemically reducing species such as carbons and hydrocarbons. A chemical reaction between the redox active materials and the reducing species occurs in which oxygen is transferred from the redox-active oxygen carrier to the reducing species. That is, the oxygen carrier is reduced, while the carbon/hydrocarbon is oxidized. An example is shown in equation 1 wherein methane reacts with a metal oxide.
4/MO.sub.x+CH.sub.4.fwdarw.4/MO.sub.(x-)+CO.sub.2+2H.sub.2O(1)

(7) In the above and following reactions, represents an oxygen nonstoichiometry.

(8) In the second step, the redox-active oxygen carrier is oxidized via exposure to and reaction with oxygen (equation 2). In an embodiment, the oxygen may be in an air stream (equation 2). This reaction regenerates the material so that it may once again be employed to accomplish reaction 1. The two reactions of the looping process, 1 and 2, sum to achieve a desired reaction (equation 3), in this example, the combustion of methane.
4/MO.sub.(x-)+2O.sub.2.fwdarw.4/MO.sub.x(2)
CH.sub.4+2O.sub.2.fwdarw.CO.sub.2+2H.sub.2O(3)

(9) Depending on the identity of the hydrocarbons and metal species in question, heat is generated in one or both steps of the reaction. This heat generated in reaction 2 can be used, for example, but not limited to process heat or removed to drive a power production cycle, or recycled to enhance system efficiency, or recycled to provide energy to the endothermic first step for example.

(10) Oxygen Separation

(11) The invention is further directed to an air separation process that uses the disclosed chemical looping process to accomplish an oxygen separation from air. As described above in equation 2, the reduced material reacts selectively with oxygen from air. By removing the solid from the air environment, and subsequently introducing it to a reducing environment as depicted in equation 1, oxygen is in effect provided for reaction free of the other components of air. The advantages of accomplishing this separation are well known. For example, air contains 79% nitrogen, and therefore the products from conventional hydrocarbon/air combustion (CO.sub.2 and H.sub.2O) are diluted in a large excess of nitrogen. Separating the CO.sub.2 from the nitrogen for subsequent use or sequestration requires significant investment and energy. If the combustion is accomplished via a chemical looping process instead, i.e. CLC, this separation is avoided.

(12) Chemical Looping Combustion (CLC)

(13) CLC, by oxidation of the fuel stream, produces heat and oxidation products. An example is provided above for methane in equations 1, 2, and 3. The reaction can be carried out with any combustible hydrocarbon or mixture of hydrocarbons, including gasses, liquids, and solids. For example, natural gas, diesel or kerosene fuels, biomass solids, or coke can be processed in such a way to provide useful heat with a nitrogen-free effluent stream. Further for example, CLC process may be used with methane, propane, ethanol, un-refined or partially refined petroleum products (liquid or gas), or coal, to produce predominantly CO.sub.2 and H.sub.2O, as well as heat, upon oxidation.

(14) Chemical Looping Partial Oxidation (CLPO)

(15) CLPO is an alternative to CLC that capitalizes on the fact that through manipulating the relative flow rates of air, hydrocarbon and oxide, the system can be made more or less oxidizing or reducing such that a carbon or hydrocarbon is converted partially or in full to partially oxidized products, e.g. CO and H.sub.2. Through these manipulations, coupled with proper materials composition selection, partial oxidations can be achieved. For example, methane can be partially oxidized to synthesis gas (complete combustion and other products may also be produced, i.e. the reaction may not be 100% selective) as shown in equation 4 and 5 (overall reaction is equation 6).
1/MO.sub.x+CH.sub.4.fwdarw.1/MO.sub.(x-)+CO+2H.sub.2(4)
1/MO.sub.(x-)+O.sub.2.fwdarw.1/MO.sub.x(5)
CH.sub.4+O.sub.2.fwdarw.CO+2H.sub.2(6)

(16) Examples of CLPO, are, but are not limited to natural gas and other light hydrocarbons to synthesis gas (mixtures including CO and H.sub.2), and coke and coal to synthesis gas, and other reactions such as, but not limited to forming ethane into ethylene. Further examples of CLPO include, but are not limited to partial oxidation of methane, propane, ethanol, un-refined or partially refined petroleum products (liquid or gas), or coal, which produce predominantly CO and H.sub.2 as well as heat upon partial oxidation.

(17) Chemical Looping Reforming (CLR) and Dry Reforming (CLDR)

(18) CLR and CLDR processes are analogous to CLC and CLPO except that H.sub.2O and CO.sub.2, respectively, are included in the reactants fed to the system. These processes can take two forms. In the first, steam (CLR) or CO.sub.2 (CLDR) are co-fed with a hydrocarbon. Equations 7-9 depict CLR for a generic hydrocarbon reacting with steam and an oxygen carrier to produce a mixture of product gasses.
MO.sub.x+hydrocarbon+H.sub.2O.fwdarw.MO.sub.(x-)+(CO+H.sub.2+CO.sub.2+H.sub.2O)(7)
MO.sub.(x-)+O.sub.2.fwdarw.MO.sub.x(8)
Hydrocarbon+O.sub.2+H.sub.2O.fwdarw.(CO+H.sub.2+CO.sub.2+H.sub.2O)(9)

(19) The second form of CLR and CLDR replaces the air with either steam or CO.sub.2 to produce relatively pure streams of H.sub.2 or CO. This process depicted with steam in equations 10, 11, and 12.
MO.sub.x+hydrocarbon.fwdarw.MO.sub.(x-)+CO.sub.2+H.sub.2O(10)
MO.sub.(x-)+H.sub.2O.fwdarw.MO.sub.x+H.sub.2(11)
Hydrocarbon+H.sub.2O.fwdarw.H.sub.2+CO.sub.2+H.sub.2O(12)

(20) This alternate case not only shifts the products from the reoxidation side of the system but also alters the energy balance. For these cases, the overall reactions are endothermic and therefore provisions must be made to add heat to the system whereas it is extracted in the combustion processes. A benefit of these alternate CLR and CLDR approaches is the production of high purity H.sub.2 (carbon free, reaction 11) and CO (hydrogen free, reaction 11 substituting CO.sub.2 and CO for H.sub.2O and H.sub.2) streams, respectively.

(21) While the invention has been described with reference to a preferred embodiment, it will be understood by those skilled in the art that various changes may be made and equivalents may be substituted for elements thereof without departing from the scope of the invention. In addition, many modifications may be made to adapt a particular situation or material to the teachings of the invention without departing from the essential scope thereof. Therefore, it is intended that the invention not be limited to the particular embodiment disclosed as the best mode contemplated for carrying out this invention, but that the invention will include all embodiments falling within the scope of the appended claims.