Microfibrous entrapment of small reactive particulates and fibers for high contacting efficiency removal of contaminants from gaseous or liquid streams
A microfibrous matrix with embedded supporting particulates/fibers and chemically reactive materials is provided as a filtration system for the removal of contaminants and other harmful agents from liquid and gaseous streams. Such materials may include chemically reactive materials as high surface area carbons, zeolites, silicas, aluminas, inorganic metal oxides, polymer resins, ZnO, ZnO/Carbon, Pt/γ-Al 2 O 3 , PtCo/γ-Al 2 O 3 , ZnO/SiO 2 and various other catalysts, sorbents or reactants. The invention may be used to protect the intolerant anodes and cathodes of fuel cells from damaging H 2 S while simultaneously aiding the selective conversion of CO to CO 2 in fuel streams predominated by hydrogen, to provide a highly efficient gas and/or liquid separation and purification methodology for gas masks, building filtration systems, and/or as polishing media located downstream of traditional packed bed filtration systems.
1. A filtration system comprising:
a) a plurality of layers, each layer being reactive and including a matrix of sinter-bonded microfibers;
b) support, adsorbent or reactive particulates and/or fibers entrapped within said matrix;
c) a pre-selected reactive material impregnated into said matrix and supported by said particulates and/or fibers;
d) wherein thin sheets of the matrix with the supporting particulates, reactants, adsorbents and/or fibers and the pre-selected reactive materials impregnated therein are chemically functionalized and then stacked in a pre-defined sequence; and
e) wherein the predefined sequence has an upstream packed bed of larger diameter reactive catalyst and sorbent particulates and a downstream polishing layer of smaller diameter microfibrous entrapped reactive catalyst and sorbent particulates; and
f) wherein the filtration system removes contaminants from liquid and gaseous streams.
2. The filtration system of claim 1 , wherein said thin sheets are less than a three millimeters in thickness.
3. The filtration system of claim 1 wherein said thin sheets provide high contacting efficiency and small critical bed depth such that said thin sheets may be made extremely thin and still achieve high levels of saturation, reaction and/or contaminant removal.
4. The filtration system of claim 3 wherein said adsorption and reaction levels provide greater than a 5-log differential in concentration between inlet and outlet concentrations of said contaminants.
5. The filtration system of claim 3 wherein said thin sheets comprise a sorbent system of specified gas life capacity and volume, wherein the pressure drop through said bed depth decreases with the square of said bed depth's cross-sectional area.
6. The filtration system of claim 4 wherein said thin sheets are sealed into a chemically protective hood for human use so as to permit small volume/mass packaging via folding into an easily carried package and wherein said hooded thin sheets are laminated with a thin sheet of HEPA filtration media so as to provide both particulate and gas removal/protection for the wearer.
7. The filtration system of claim 3 wherein said filtration system advantageously utilizes the volume loading capacity of said packed bed and the overall contacting/removal efficiency of the polishing layer.
8. The filtration system of claim 2 wherein said reactive materials are a PROX CO catalyst.
9. The filtration system of claim 2 wherein said reactive materials include optimized multiple H 2 S removal sorbents/reactants for both low and high temperature performance and regenerability.
10. The filtration system of claim 9 wherein said reactive materials comprising said optimized multiple H 2 S removal sorbents/reactants include ZnO/Carbon and ZnO/SiO 2 , respectively.
11. The filtration system of claims 6 or 7 or 8 or 9 wherein said reactive materials are layered to achieve pre-determined operations capabilities with regard to temperature, selectivity, and outlet gas performance/compositions.
12. The filtration system of claim 1 wherein loading of the reactive material within said matrix and the corresponding intra-layer void volume, the matrix thickness and its cross-sectional area are pre-selected to maximize the reaction rate per unit volume, the reaction rate per unit mass, and/or the reaction rate per unit pressure drop.
13. The filtration system of claim 1 wherein said microfibers of said matrix are metal fibers and wherein said microfibers impart high temperature operational characteristics, certain malleability and joining/bonding capabilities, and/or electrical conductivity and IR self-heating attributes to said filtration system.
14. The filtration system of claim 1 wherein said microfibers of said matrix are polymer, glass and/or ceramic fibers and wherein said micro fibers impart specific corrosion/chemical resistance, thermal stability behavior, mechanical properties, specific cost factors, and overall density attributes to said filtration system.
15. The filtration system of claim 1 wherein said matrix is pleated or similarly structured so as to reduce the effective face velocity of incoming reactant streams, increase intra-layer residence times, and reduce overall pressure drop.