MULTIFUNCTIONAL BIOMASS PYROLYSIS CATALYST AND METHOD OF USING THE SAME
A multi-functional catalyst for the conversion of biomass contains zeolite ZSM-5, zeolite USY, a metallic component, a basic material and a binder. The metallic component may be Cu, Ni, Cr, W, Mo, a metal carbide, a metal nitride, a metal sulfide or a mixture thereof. The basic material may be an alkaline-exchanged zeolite or an alkaline earth-exchanged zeolite having from about 40 to about 75% of exchanged cationic sites.
1 . A catalyst for the conversion of biomass, the catalyst comprising:
a) zeolite ZSM-5;
b) zeolite USY;
c) a metallic component selected from the group consisting of Cu, Ni, Cr, W, Mo, a metal carbide, a metal nitride, a metal sulfide and mixtures thereof;
d) a basic material selected from the group consisting of alkaline-exchanged zeolite, alkaline earth-exchanged zeolite, basic zeolite, alkaline earth metal oxide, cerium oxide, zirconium oxide, titanium dioxide, mixed oxides of alkaline earth metal oxides and combinations thereof and mixed oxides selected from the group of magnesia-alumina, magnesia-silica, titania-alumina, titania-silica, ceria-alumina, ceria-silica, zirconia-alumina, zirconia-silica and mixtures thereof and wherein the exchanged zeolite has from about 40 to about 75% of exchanged cationic sites; and
e) a binder wherein the binder is kaolin based, alumina based or silica based or a combination thereof.
2 . The catalyst of claim 1 , wherein the weight ratio of Si:Al in zeolite USY is from about 5 to about 200.
3 . The catalyst of claim 2 , wherein the weight ratio of Si:Al in zeolite USY is from about 20 to about 100.
4 . The catalyst of claim 1 , wherein the metallic component is a metal carbide selected from the group of chromium carbide, molybdenum carbide and tungsten carbide and mixtures thereof.
5 . The catalyst of claim 4 , wherein the metal carbide is molybdenum carbide
6 . The catalyst of claim 1 , further comprising L-zeolite.
7 . The catalyst of claim 1 , further comprising a promoter selected from the group consisting of phosphates, silica and metallic and mixtures thereof.
8 . The catalyst of claim 1 , wherein the metallic component is comprised of copper, nickel or a carbide of molybdenum or a mixture thereof.
9 . The catalyst of claim 8 , wherein the metallic component is a blend of copper and molybdenum carbide or a blend of nickel and molybdenum carbide.
10 . The catalyst of claim 1 , comprising from about 5 to about 40 wt. % zeolite ZSM-5; from about 5 to about 40 wt. % zeolite USY; from about 3 to about 30 wt. % of metallic material; and from about 5 to about 50 wt. % of basic material; the balance being the binder.
11 . The catalyst of claim 10 , wherein the basic material is an exchanged zeolite having 50% exchanged cationic sites.
12 . The catalyst of claim 10 , wherein the catalyst further comprises less than 20 wt. % of L-zeolite.
13 . The catalyst of claim 1 , wherein the binder comprises kaolin.
14 . The catalyst of claim 1 , comprising from about 5 to about 40 wt. % zeolite ZSM-5; from about 5 to about 40 wt. % zeolite USY; from about 5 to about 50 wt. % of basic material; from about 3 to about 30 wt. % of a blend of copper and the carbide of molybdenum or from about 3 to about 30 wt. % of a blend of nickel and the carbide of molybdenum; and the balance being the binder.
15 . The catalyst of claim 1 , wherein the metallic component is selected from the group of Cu, Ni, Cr, W, Mo, a metal carbide, a metal nitride, a metal sulfide and mixtures thereof and is supported by the basic material.
16 . A catalyst for the conversion of biomass, the catalyst comprising:
a) zeolite ZSM-5;
b) zeolite USY having a weight ratio of Si:Al from about 5 to about 200;
c) L-zeolite;
d) a metallic material comprising a metal carbide;
e) a basic material selected from the group consisting of alkaline-exchanged zeolite, alkaline earth-exchanged zeolite, basic zeolite, alkaline earth metal oxide, cerium oxide, zirconium oxide, titanium dioxide, mixed oxides of alkaline earth metal oxides and combinations thereof and mixed oxides selected from the group of magnesia-alumina, magnesia-silica, titania-alumina, titania-silica, ceria-alumina, ceria-silica, zirconia-alumina, zirconia-silica and mixtures thereof and wherein the exchanged zeolite has from about 40 to about 75% of exchanged cationic sites; and
f) a binder comprising a material selected from the group consisting of kaolin, alumina, silicic acid, polysilicic acid, silica gel, aluminum chlorohydrol, aluminum nitrohydrol and combinations thereof.
17 . The catalyst of claim 16 , further comprising a promoter selected from the group consisting of phosphates, silica and metallic and mixtures thereof.
18 . The catalyst of claim 16 , wherein the weight ratio of Si:Al in zeolite USY is from about 20 to about 100.
19 . The catalyst of claim 16 , wherein the metal carbide is selected from the group of chromium carbide, molybdenum carbide and tungsten carbide
20 . The catalyst of claim 16 , wherein the metallic component is supported by the basic material.
21 . A process of converting solid biomass to hydrocarbons comprising the step of feeding into a biomass conversion unit the catalyst of claim 1 and pyrolyzing the biomass in the biomass conversion unit.
22 . The process of claim 21 , wherein at least a portion of the catalyst fed into the biomass conversion unit is regenerated catalyst.