Carbon foams, doped carbon composites, processes for fabricating carbon foams and doped carbon composites, and uses thereof
Embodiments of the present disclosure generally relate to carbon foams, processes for forming carbon foams, doped carbon composites, processes for forming doped carbon composites, and uses thereof, e.g., as electrodes. Processes described herein relate to fabrication of carbon foam and materials derived from the pyrolyzation of biomass at supercritical and subcritical conditions for CO 2 , N 2 , H 2 O, or combinations thereof. The process includes exposing biomass to CO 2 , N 2 , H 2 O, or combinations thereof under various parameters for temperature, pressure, heating rate and fluid flow rate. Silicon-carbon composites and sulfur-carbon composites for use as, e.g., electrodes, are also described.
1. A process for forming a carbon foam, comprising:
processing lignocellulosic biomass into a feedstock, the feedstock comprising a plurality of particles having a particle size of about 30 μm to about 1 mm, the feedstock further comprising a sulfur source, a silicon source, or a combination thereof different from the lignocellulosic biomass;
loading the feedstock into a reactor, the reactor disposed inside a furnace;
pyrolyzing the feedstock to form the carbon foam, comprising:
pressurizing the reactor with CO 2 , N 2 , H 2 O, or combinations thereof, the CO 2 , N 2 , H 2 O, or combinations thereof in a supercritical state or subcritical state, the pressure of the reactor is from about 4.1 MPa to about 10.5 MPa;
contacting the feedstock with the CO 2 , N 2 , H 2 O, or combinations thereof;
heating the furnace at a heat rate of about 10° C./min to about 50° C./min until the reactor reaches a specified temperature of about 450° C. to about 550° C.; and
exposing the reactor to the specified temperature for a period of about ten minutes to about 1 hour to form the carbon foam; and
collecting a bio-oil during or after exposing the reactor to the specified temperature for a period of about ten minutes to about 1 hour, wherein the carbon foam has:
a bulk density of about 0.2 g/mL to about 0.6 g/mL;
a plurality of pores, the pores having an average pore diameter of about 20 μm to about 200 μm;
an ultimate compressive strength of about 0.1 MPa to about 20 MPa;
an electrical conductivity of about 1×10 −8 to about 9×10 5 S/m; or
combinations thereof.
2. The process of claim 1 , wherein the feedstock is formed into pellets prior to pyrolyzing the feedstock.
3. The process of claim 1 , wherein pressurizing the reactor is performed at a pressure such that the CO 2 , N 2 , H 2 O, or combinations thereof is in the supercritical state.
4. The process of claim 1 , wherein pressurizing the reactor is performed at a pressure such that the CO 2 , N 2 , H 2 O, or combinations thereof is in the subcritical state.
5. The process of claim 1 , further comprising heat treating the carbon foam at a temperature of about 700° C. to about 1100° C. after pyrolyzing the feedstock to form a heat treated carbon foam.
6. A process for forming a carbon foam, comprising:
processing lignocellulosic biomass into a feedstock, the feedstock comprising a plurality of particles having a particle size of about 30 μm to about 1 mm, the feedstock further comprising a sulfur source, a silicon source, or a combination thereof different from the lignocellulosic biomass;
loading the feedstock into a reactor, the reactor disposed inside a furnace; and
pyrolyzing the feedstock to form the carbon foam, comprising:
pressurizing the reactor with CO 2 , N 2 , H 2 O, or combinations thereof, the CO 2 , N 2 , H 2 O, or combinations thereof in a supercritical state or subcritical state, the pressure of the reactor is from about 4.1 MPa to about 10.5 MPa;
contacting the feedstock with the CO 2 , N 2 , H 2 O, or combinations thereof;
heating the furnace at a heat rate of about 10° C./min to about 50° C./min until the reactor reaches a specified temperature of about 450° C. to about 550° C.; and
exposing the reactor to the specified temperature for a period of about ten minutes to about 1 hour to form the carbon foam.
7. The process of claim 6 , wherein the feedstock further comprises a surfactant.
8. The process of claim 6 , further comprising heat treating the carbon foam at a temperature of about 700° C. to about 1100° C. after pyrolyzing the feedstock to form a heat treated carbon foam.
9. A process for forming a carbon foam, comprising:
processing biomass into a feedstock, the feedstock comprising a plurality of particles having a particle size of about 30 μm to about 1 mm, wherein the feedstock further comprises a sulfur source, a silicon source, or a combination thereof, the sulfur source, silicon source, or combination thereof different from the biomass;
loading the feedstock into a reactor, the reactor disposed inside a furnace; and
pyrolyzing the feedstock to form the carbon foam, comprising:
pressurizing the reactor with CO 2 , N 2 , H 2 O, or combinations thereof at a pressure such that the CO 2 , N 2 , H 2 O, or combinations thereof is in a subcritical state;
contacting the feedstock with the CO 2 , N 2 , H 2 O, or combinations thereof;
heating the furnace at a heat rate of about 10° C./min to about 50° C./min until the reactor reaches a specified temperature of about 450° C. to about 550° C.; and
exposing the reactor to the specified temperature for a period of about ten minutes to about 1 hour to form the carbon foam.
10. The process of claim 9 , wherein the feedstock further comprises a surfactant.
11. The process of claim 9 , further comprising heat treating the carbon foam at a temperature of about 700° C. to about 1100° C. after pyrolyzing the feedstock to form a heat treated carbon foam.
12. A process for forming a carbon foam, comprising:
processing biomass into a feedstock, the feedstock comprising a plurality of particles having a particle size of about 30 μm to about 1 mm, wherein the feedstock further comprises a sulfur source, a silicon source, or a combination thereof, the sulfur source, silicon source, or combination thereof different from the biomass;
loading the feedstock into a reactor, the reactor disposed inside a furnace;
pyrolyzing the feedstock to form the carbon foam, comprising:
pressurizing the reactor with CO 2 , N 2 , H 2 O, or combinations thereof, the CO 2 , N 2 , H 2 O, or combinations thereof in a supercritical state or subcritical state, the pressure of the reactor is from about 4.1 MPa to about 10.5 MPa;
contacting the feedstock with the CO 2 , N 2 , H 2 O, or combinations thereof;
heating the furnace at a heat rate of about 10° C./min to about 50° C./min until the reactor reaches a specified temperature of about 450° C. to about 550° C.; and
exposing the reactor to the specified temperature for a period of about ten minutes to about 1 hour to form the carbon foam; and
heat treating the carbon foam at a temperature of about 700° C. to about 1100° C. after pyrolyzing the feedstock to form a heat treated carbon foam.
13. The process of claim 12 , wherein the feedstock further comprises a surfactant.