Materials and methods for improved pyrolysis processing
The present disclosure relates to a catalyst that includes a support that includes a metal oxide and a metal deposited on the support, where the metal oxide includes at least one of TiO 2 , Al 2 O 3 , SiO 2 , CeO 2 , and/or ZrO 2 , the metal includes at least one of Pt, Pd, Ru Rh, Ni, and/or Mo, the metal is in the form of a particle, and the metal is present on the support at a concentration between about 0.1 wt % and about 5.0 wt %.
1. A catalyst consisting of:
a TiO 2 support; and
platinum deposited on the TiO 2 support, wherein:
the platinum is present on a surface of the TiO 2 support at a concentration between about 0.1 wt % and about 2.0 wt % relative to the TiO 2 support, and
the catalyst is characterized by:
a diameter between about 300 μm and about 1200 μm;
a total surface area between about 35 m 2 /g and about 75 m 2 /g;
a pore volume between about 0.20 cm 3 /g and about 0.55 cm 3 /g;
a median pore diameter between about 290 Å and about 380 Å; and
the catalyst is synthesized using a solution processing method using only TiO 2 , a platinum source, water, and a buffer.
2. The catalyst of claim 1 , wherein the catalyst is at least partially crystalline.
3. The catalyst of claim 2 , wherein the catalyst is between about 80 wt % crystalline and about 99 wt % crystalline.
4. The catalyst of claim 1 , wherein the catalyst has a diameter between about 470 μm and about 550 μm.
5. The catalyst of claim 1 , wherein the catalyst has a sphericity of at least 96.1%.
6. The catalyst of claim 1 , wherein the surface area is between about 50 m 2 /g and about 60 m 2 /g.
7. The catalyst of claim 1 , wherein the concentration of the platinum is greater than 0 wt % and less than 1 wt %.
8. A method comprising:
treating a pyrolysis vapor in an upgrading unit to produce an upgraded pyrolysis product comprising an oxygenated compound, wherein:
the treating comprises contacting the pyrolysis vapor with a catalyst consisting of:
a TiO 2 support; and
platinum deposited on the TiO 2 support, wherein:
the platinum is present on a surface of the TiO 2 support at a concentration between about 0.1 wt % and about 2.0 wt % relative to the TiO 2 support, and the catalyst is characterized by:
a diameter between about 300 μm and about 1200 μm;
a total surface area between about 35 m 2 /g and about 75 m 2 /g;
a pore volume between about 0.20 cm 3 /g and about 0.55 cm 3 /g;
a median pore diameter between about 290 Å and about 380 Å.
9. The method of claim 8 , wherein the treating is performed in a packed bed reactor.
10. The method of claim 9 , wherein:
the packed bed reactor comprises a first reactor and a second reactor,
while the first reactor is treating, the second reactor is regenerating the catalyst, and
while the second reactor is treating, the first reactor is regenerating the catalyst.
11. The method of claim 9 , wherein the packed bed reactor is operated at a pressure between about 1 Barr and about 10 Barr.
12. The method of claim 9 , wherein the packed bed reactor is operated at a weight hourly space velocity between about 1.0 grams of biomass per gram of catalyst per hour and about 5.0 grams of biomass per gram of catalyst per hour.