METHOD FOR PREPARING AN ORDERED POROUS CARBON MATERIAL WITH INEXPENSIVE CARBON BLACK, ORDERED POROUS CARBON MATERIAL AND USE THEREOF

Abstract

The present disclosure relates to a method for preparing an ordered porous carbon materials with inexpensive carbon black. The method comprises: dispersing carbon black into a concentrated nitric acid to obtain a uniform dispersion; placing the dispersion in a reactor to perform a reaction by a one-step hydrothermal process; and washing and drying the reaction mixture to obtain an ordered porous carbon material in a honeycomb-like arrangement and rich in oxygen defects. The present disclosure also relates to an ordered porous carbon material prepared by the method, a method for electrocatalytically reducing carbon dioxide to formic acid under ambient temperature and atmospheric pressure by using the ordered porous carbon material, and a method for electrocatalytically reducing nitrogen to ammonia under ambient temperature and atmospheric pressure by using the ordered porous carbon material as a supported catalyst.

Claims

1. A method for preparing an ordered porous carbon material with carbon black, comprising: dispersing carbon black into a concentrated nitric acid to obtain a uniform dispersion; placing the dispersion in a reactor to perform a reaction by a one-step hydrothermal process; and washing and drying the reaction mixture to obtain an ordered porous carbon material in a honeycomb-like arrangement and rich in oxygen defects.

2. The method according to claim 1, wherein the concentration of the concentrated nitric acid is 45% to 65% by mass.

3. The method according to claim 1, wherein the reaction is performed at a temperature of from 120 to 160 C. for 4 to 8 hours.

4. The method according to claim 3, wherein the reaction is performed at a temperature of from 120 to 150 C. for 5 to 6 hours.

5. The method according to claim 1, wherein said washing and drying the reaction mixture comprises adding water to the reaction mixture, and then subjecting the mixture to rotary evaporation and centrifugation.

6. The method according to claim 1, wherein said washing and drying are repeated for 3 to 5 times.

7. The method according to claim 1, wherein the carbon black is BP-2000, XC-72, N220, N330, N550, N660, N990, N110, N115, N234, N326, N339, N375, N539, N550, or N880.

8. The method according to claim 1, wherein the amount of the concentrated nitric acid used is 80 to 100 mL with respect to 1 g of the carbon black.

9. The method according to claim 1, wherein the ordered porous carbon material prepared has a thickness of 3 nm to 8 nm and an oxidation degree of 1.993 to 2.012.

10. The method according to claim 9, wherein the ordered porous carbon material prepared has a thickness of 3 nm and an oxidation degree of 2.012.

11. An ordered porous carbon material prepared by the method according to claim 1, wherein the ordered porous carbon material is in a honeycomb-like arrangement and rich in oxygen defects, and has an oxidation degree of 1.993 to 2.012.

12. A method for electrocatalytically reducing carbon dioxide to formic acid under ambient temperature and atmospheric pressure, comprising preparing a working electrode by using the ordered porous carbon material according to claim 11.

13. The method according to claim 12, comprising: preparing a three-electrode electrolytic cell separated by a proton exchange membrane, wherein a working electrode is prepared by mixing and sonicating the ordered porous carbon material, ethanol, and a Nafion solution to obtain a dispersion, and uniformly applying the dispersion onto a carbon paper; a platinum plate is used as a counter electrode; and a saturated calomel electrode is used as a reference electrode; charging an electrolyte solution into a cathode chamber and an anode chamber respectively, and introducing CO.sub.2 to saturation; and potentiostatically reducing CO.sub.2 with continuously introducing CO.sub.2, wherein the potential during potentiostatic reduction is controlled in a range of 0.38 V to 0.98 V vs. Reversible Hydrogen Electrode, the time for reduction is 4 to 6 h, and the electrolyte solution is a NaHCO.sub.3, KHCO.sub.3 or Na.sub.2SO.sub.4 solution.

14. A method for electrocatalytically reducing nitrogen to ammonia under ambient temperature and atmospheric pressure in the presence of a supported catalyst prepared by using the ordered porous carbon material according to claim 11.

15. The method according to claim 14, comprising: preparing the supported catalyst by adding ferric chloride and the ordered porous carbon material in distilled water, mixing them by sonication, then drying the mixture by rotary evaporation, placing the dried mixture in a tube furnace, and pyrolyzing the mixture under a nitrogen atmosphere; preparing a three-electrode electrolytic cell separated by a proton exchange membrane, wherein a working electrode is prepared by mixing and sonicating the prepared supported catalyst, ethanol, and a Nafion solution to obtain a dispersion, and uniformly applying the dispersion onto a carbon paper; a platinum plate is used as a counter electrode; and a saturated calomel electrode is used as a reference electrode; charging an electrolyte solution into a cathode chamber and an anode chamber respectively and introducing N.sub.2 to saturation; and potentiostatically reducing N.sub.2 with continuously introducing N.sub.2, wherein the potential during potentiostatic reduction is controlled in a range of 0.45 V to 0.85 V vs. Reversible Hydrogen Electrode, the time for reduction is 2 to 4 h, and the electrolyte solution is a H.sub.2SO.sub.4 solution.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0037] The present disclosure will be further explained in detail below with reference to the drawings and particular embodiments.

[0038] FIG. 1 is a Scanning Electron Micrograph of the porous carbon material prepared in Example 1 of the present disclosure;

[0039] FIG. 2 is a Transmission Electron Micrograph of the porous carbon material prepared in Example 1 of the present disclosure;

[0040] FIG. 3 is an Atomic Force Micrograph of the porous carbon material prepared in Example 1 of the present disclosure;

[0041] FIG. 4 is an Electron Paramagnetic Resonance spectrum of the porous carbon material prepared in Example 1 of the present disclosure;

[0042] FIG. 5 is a High Resolution X-ray Photoelectron Spectrum of the porous carbon material prepared in Example 1 of the present disclosure;

[0043] FIG. 6 is a Raman spectrum of the porous carbon material prepared in Example 1 of the present disclosure;

[0044] FIG. 7 is a Linear Scanning Voltammogram of reduction of N.sub.2 in the presence of the porous carbon material supported catalyst prepared in Example 3 of the present disclosure;

[0045] FIG. 8 is an ultraviolet absorption spectrum of reduction of N.sub.2 into NH.sub.3 at 0.55 V in the presence of the porous carbon material supported catalyst prepared in Example 3 of the present disclosure;

[0046] FIG. 9 is a Linear Scanning Voltammogram of reduction of CO.sub.2 in the presence of the porous carbon material prepared in Example 4 of the present disclosure;

[0047] FIG. 10 is a Nuclear Magnetic Resonance spectrum of catalytic reduction of CO.sub.2 into formic acid at 0.78 V in the presence of the porous carbon material prepared in Example 4 of the present disclosure; and

[0048] FIG. 11 is a Transmission Electron Micrograph of the porous carbon material prepared in Example 2 of the present disclosure.

DESCRIPTION OF EMBODIMENTS

[0049] The present disclosure provides a method for preparing an ordered porous carbon material with inexpensive carbon black, comprising:

[0050] dispersing carbon black into a concentrated nitric acid to obtain a uniform dispersion;

[0051] placing the dispersion in a reactor to perform a reaction by a one-step hydrothermal process; and

[0052] washing and drying the reaction mixture to obtain an ordered porous carbon material in a honeycomb-like arrangement and rich in oxygen defects.

[0053] Preferably, the concentration of the concentrated nitric acid is 45% to 65% by mass.

[0054] Preferably, the reaction is performed at a temperature of from 120 to 160 C. for 4 to 8 hours.

[0055] More preferably, the reaction is performed at a temperature of from 120 to 150 C. for 5 to 6 hours.

[0056] Preferably, said washing and drying the reaction mixture comprises adding water to the reaction mixture, and then subjecting the mixture to rotary evaporation and centrifugation.

[0057] Preferably, said washing and drying are repeated for 3 to 5 times.

[0058] Any commonly used carbon black in the art may be used in the method provided in the present disclosure. For example, carbon black of type BP-2000, XC-72, N220, N330, N550, N660, N990, N110, N115, N234, N326, N339, N375, N539, N550, or N880 may be used. Carbon black of type BP-2000 or XC-72 is most preferable.

[0059] Preferably, the amount of the concentrated nitric acid used is 80 to 100 mL with respect to 1 g of the carbon black.

[0060] Preferably, the ordered porous carbon material prepared has a thickness of 3 nm to 8 nm and an oxidation degree of 1.993 to 2.012. More preferably, the ordered porous carbon material prepared has a thickness of 3 nm and an oxidation degree of 2.012.

[0061] The present disclosure also provides an ordered porous carbon material prepared by the method as described above, wherein the ordered porous carbon material is in a honeycomb-like arrangement and rich in oxygen defects, and has an oxidation degree of 1.993 to 2.012.

[0062] The present disclosure also provides a method for electrocatalytically reducing carbon dioxide to formic acid under ambient temperature and atmospheric pressure, comprising preparing a working electrode by using the ordered porous carbon material as described above.

[0063] Preferably, the method for electrocatalytically reducing carbon dioxide to formic acid under ambient temperature and atmospheric pressure comprises:

[0064] preparing a three-electrode electrolytic cell separated by a proton exchange membrane, wherein a working electrode is prepared by mixing and sonicating the ordered porous carbon material, ethanol, and a Nafion solution to obtain a dispersion, and uniformly applying the dispersion onto a carbon paper; a platinum plate is used as a counter electrode; and a saturated calomel electrode is used as a reference electrode;

[0065] charging an electrolyte solution into a cathode chamber and an anode chamber respectively, and introducing CO.sub.2 to saturation; and

[0066] potentiostatically reducing CO.sub.2 with continuously introducing CO.sub.2,

[0067] wherein the potential during potentiostatic reduction is controlled in a range of 0.38 V to 0.98 V vs. Reversible Hydrogen Electrode (RHE), the time for reduction is 4 to 6 h, and the electrolyte solution is a NaHCO.sub.3, KHCO.sub.3 or Na.sub.2SO.sub.4 solution.

[0068] The present disclosure also provides a method for electrocatalytically reducing nitrogen to ammonia under ambient temperature and atmospheric pressure in the presence of a supported catalyst prepared by using the ordered porous carbon material as described above.

[0069] Preferably, the method for electrocatalytically reducing nitrogen to ammonia under ambient temperature and atmospheric pressure comprises:

[0070] preparing the supported catalyst by adding ferric chloride and the ordered porous carbon material in distilled water, mixing them by sonication, then drying the mixture by rotary evaporation, placing the dried mixture in a tube furnace, and pyrolyzing the mixture under a nitrogen atmosphere;

[0071] preparing a three-electrode electrolytic cell separated by a proton exchange membrane, wherein a working electrode is prepared by mixing and sonicating the prepared supported catalyst, ethanol, and a Nafion solution to obtain a dispersion, and uniformly applying the dispersion onto a carbon paper; a platinum plate is used as a counter electrode; and a saturated calomel electrode is used as a reference electrode;

[0072] charging an electrolyte solution into a cathode chamber and an anode chamber respectively and introducing N.sub.2 to saturation; and

[0073] potentiostatically reducing N.sub.2 with continuously introducing N.sub.2,

[0074] wherein the potential during potentiostatic reduction is controlled in a range of 0.45 V to 0.85 V vs. RHE, the time for reduction is 2 to 4 h, and the electrolyte solution is a H.sub.2SO.sub.4 solution.

[0075] The present disclosure will be explained in detail below with reference to the drawings.

EXAMPLE 1

Preparation of a Porous Carbon Material Having a Thickness of 3 nm

[0076] 1 g of carbon black BP-2000 was added into 100 mL of concentrated nitric acid with a concentration of 65% by mass. The mixture was sonicated with stirring for 1 hour until a uniformly dispersed solution was formed. Then, the solution was placed in a hydrothermal reactor and reacted at 150 C. for 5 hours. After the reactor was cooled to ambient temperature, the resultant was washed with distilled water and dried through rotary evaporation and centrifugation for 3-5 times, to obtain an ordered porous carbon material having a thickness of 3 nm and an oxidation degree (g value) of 2.012.

[0077] FIG. 1 is a Scanning Electron Micrograph of the porous carbon material prepared in Example 1 of the present disclosure. As can be seen from this figure, the pore structure of the porous carbon material prepared in Example 1 is in a honeycomb-like arrangement.

[0078] FIG. 2 is a Transmission Electron Micrograph of the porous carbon material prepared in Example 1 of the present disclosure. As can be seen from this figure, the porous carbon material prepared in Example 1 has a pore-rich structure, and is uniformly distributed and structurally ordered.

[0079] FIG. 3 is an Atomic Force Micrograph of the porous carbon material prepared in Example 1 of the present disclosure. As can be seen from this figure, the average thickness of the material is 3 nm.

[0080] FIG. 4 is an Electron Paramagnetic Resonance spectrum of the porous carbon material prepared in Example 1 of the present disclosure. As can be seen from this figure, the porous carbon material prepared by the present method has a very high oxidation degree, where the g value for oxidation is up to 2.012.

[0081] FIG. 5 is a High Resolution X-ray Photoelectron Spectrum of the porous carbon material prepared in Example 1 of the present disclosure. As can be seen from this figure, the porous carbon material prepared by the method of the present disclosure comprises plenty of oxygen-containing functional groups, in which the proportion of carboxyl group is the highest.

[0082] FIG. 6 is a Raman spectrum of the porous carbon material prepared in Example 1 of the present disclosure. As can be seen from this figure, the porous carbon material prepared by the method of the present disclosure has a very high defect degree.

EXAMPLE 2

Preparation of a Porous Carbon Material Having a Thickness of 8 nm

[0083] 1 g of carbon black XC-72 was added into 100 mL of concentrated nitric acid with a concentration of 45% by mass. The mixture was sonic ated with stirring for 1 hour until a uniformly dispersed solution was formed. Then, the solution was placed in a hydrothermal reactor and reacted at 120 C. for 6 hours. After the reactor was cooled to ambient temperature, the resultant was washed with distilled water and dried through rotary evaporation and centrifugation for 3-5 times, to obtain an ordered porous carbon material having a thickness of 8 nm and an oxidation degree (g value) of 2.005.

[0084] The carbon material prepared in this example is a uniformly distributed and honeycomb-like ordered porous carbon material. The carbon material can be used in electrocatalytic reduction of CO.sub.2 into formic acid, and used as a supported catalyst in electrocatalytic reduction of nitrogen into ammonia.

[0085] FIG. 11 is a Transmission Electron Micrograph of the porous carbon material prepared by using XC-72 as raw material in the present disclosure. This figure demonstrates that the porous carbon material having a pore-rich structure can also be obtained by treating XC-72 in the method of the present disclosure.

EXAMPLE 3

[0086] The method for electrocatalytically reducing nitrogen into ammonia in the presence of the porous carbon material comprises the steps as follows. 7.8 mg ferric chloride and 100 mg of the ordered porous carbon material were added into distilled water, and mixed by sonication for 30 min. Then, the mixture was dried through rotary evaporation. The dried mixture was placed in a tube furnace and pyrolyzed at 900 C. under a nitrogen atmosphere for 1 hour to obtain a supported catalyst. Subsequently, a three-electrode electrolytic cell separated by a proton exchange membrane was prepared, wherein a working electrode was prepared by mixing and sonicating the supported catalyst obtained, ethanol, and a Nafion solution to obtain a dispersion, and uniformly applying the dispersion onto a carbon paper; a platinum plate was used as a counter electrode; and a saturated calomel electrode was used as a reference electrode. An electrolyte solution was charged into a cathode chamber and an anode chamber respectively, and N.sub.2 was introduced to saturation. Then, N.sub.2 was potentiostatically reduced with continuously introducing N.sub.2, wherein the potential during potentiostatic reduction was controlled in a range of 0.45 V to 0.85 V vs. RHE, and the time for electrolytic reduction was 2 h. The above electrolyte solution was a H.sub.2SO.sub.4 solution.

[0087] FIG. 7 is a Linear Scanning Voltammogram of reduction of N.sub.2 in a H.sub.2SO.sub.4 solution in the presence of the porous carbon material supported catalyst prepared in Example 3 of the present disclosure. As can be seen from this figure, the material has a relatively large response to N.sub.2.

[0088] FIG. 8 is an ultraviolet absorption spectrum of reduction of N.sub.2 into NH.sub.3 at 0.55 V in the presence of the porous carbon material supported catalyst prepared in Example 3 of the present disclosure. This figure demonstrates that NH.sub.3 is indeed detected by ultraviolet absorption spectrum.

EXAMPLE 4

[0089] The method for electrocatalytically reducing carbon dioxide into formic acid in the presence of the porous carbon material comprises the steps as follows. A three-electrode electrolytic cell separated by a proton exchange membrane was prepared, wherein a working electrode was prepared by mixing and sonicating 5 mg of the ordered porous carbon material prepared in Example 1, ethanol and, a Nafion solution to obtain a dispersion, and uniformly applying the dispersion onto a carbon paper; a platinum plate was used as a counter electrode; and a saturated calomel electrode was used as a reference electrode. An electrolyte solution was charged into a cathode chamber and an anode chamber respectively, and CO.sub.2 was introduced to saturation. Then, CO.sub.2 was potentiostatically reduced with continuously introducing CO.sub.2, wherein the potential during potentiostatic reduction was controlled in a range of 0.38 V to 0.98 V vs. RHE, and the time for electrolytic reduction is 5 h. The above electrolyte solution is a KHCO.sub.3 solution.

[0090] The above electrolyte solution may also be replaced with a NaHCO.sub.3 or Na.sub.2SO.sub.4 solution. The time for electrolysis may be any time period within 4 to 6 hours.

[0091] FIG. 9 is a Linear Scanning Voltammogram of reduction of CO.sub.2 in a KHCO.sub.3 solution in the presence of the porous carbon material prepared in Example 4 of the present disclosure. As can be seen from this figure, said material has a relatively large response to CO.sub.2.

[0092] FIG. 10 is a Nuclear Magnetic Resonance spectrum of catalytic reduction of CO.sub.2 into formic acid at 0.78 V in the presence of the porous carbon material prepared in Example 4 of the present disclosure. This figure demonstrates that formic acid is indeed detected by H-Nuclear Magnetic Resonance (NMR) (AV 500).

EXAMPLE 5

Preparation of a Porous Carbon Material Having a Thickness of 6 nm

[0093] 1 g of carbon black N220 was added into 80 mL of concentrated nitric acid with a concentration of 50% by mass. The mixture was sonicated with stirring for 1 hour until a uniformly dispersed solution was formed. Then, the solution was placed in a hydrothermal reactor and reacted at 130 C. for 8 hours. After the reactor was cooled to ambient temperature, the resultant was washed with distilled water and dried through rotary evaporation and centrifugation for 3 to 5 times, to obtain an ordered porous carbon material having a thickness of 6 nm and an oxidation degree (g value) of 1.993.

[0094] The carbon material prepared in this example is a uniformly distributed and honeycomb-like ordered porous carbon material. The carbon material can be used in electrocatalytic reduction of CO.sub.2 into formic acid, and used as a supported catalyst in electrocatalytic reduction of nitrogen into ammonia.

EXAMPLE 6

Preparation of a Porous Carbon Material Having a Thickness of 5 nm

[0095] 1 g of carbon black N660 was added into 80 mL of concentrated nitric acid with a concentration of 60% by mass. The mixture was sonicated with stirring for 1 hour until a uniformly dispersed solution was formed. Then, the solution was placed in a hydrothermal reactor and reacted at 160 C. for 4 hours. After the reactor was cooled to ambient temperature, the resultant was washed with distilled water and dried through rotary evaporation and centrifugation for 3 to 5 times, to obtain an ordered porous carbon material having a thickness of 5 nm and an oxidation degree (g value) of 1.995.

[0096] The carbon material prepared in this example is a uniformly distributed and honeycomb-like ordered porous carbon material. The carbon material can be used in electrocatalytic reduction of CO.sub.2 into formic acid, and used as a supported catalyst in electrocatalytic reduction of nitrogen into ammonia.

[0097] The carbon black raw material used in the above examples may be replaced with carbon black of type N330, N550, N990, N110, N115, N234, N326, N339, N375, N539, N550, or N880. All of the above types of carbon black can be used to prepare a uniformly distributed and honeycomb-like ordered porous carbon material. And all the ordered porous carbon materials prepared can be used in electrocatalytic reduction of CO.sub.2 into formic acid and used as a supported catalyst in electrocatalytic reduction of nitrogen into ammonia.

[0098] Apparently, the above examples are only intended for illustrative purpose, but not to limit the embodiments. Other variations or modifications can be made by those skilled in the art based on the above description. There is no need and no way to exhaust all embodiments. Obvious variations or modifications on the embodiments fall within the protection scope of the present invention.