Porous carbon materials and methods of manufacturing the same
10454115 ยท 2019-10-22
Assignee
Inventors
Cpc classification
B01J37/0203
PERFORMING OPERATIONS; TRANSPORTING
Y02P70/50
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
H01M8/188
ELECTRICITY
C01B32/18
CHEMISTRY; METALLURGY
Y02E60/50
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
International classification
C01B32/18
CHEMISTRY; METALLURGY
B01J37/02
PERFORMING OPERATIONS; TRANSPORTING
H01M10/20
ELECTRICITY
Abstract
Provided is a porous carbon material having carbon nano-rods on the surface thereof. The porous carbon material has an increased specific surface area and an increased electrochemically active area, and thus may be expected to provide improved performance, when used as an electrode for electrochemical reactions. In addition, the carbon nano-rods of the porous carbon material are formed through an etching process using a catalyst for etching formed on the carbon material, and thus the carbon material may have various functions.
Claims
1. A porous carbon material comprising: carbon nano-rods formed on a surface of a carbon material, wherein the carbon nano-rods have a shape of a column, wherein the carbon nano-rods have a height of 10 nm-50 m and a diameter of 2-1,000 nm, and each carbon nano-rod is spaced apart from adjacent carbon nano-rods among the carbon nano-rods by a distance of 2-1,000 nm, and wherein the carbon nano-rods are extended in a longitudinal direction from the surface of the porous carbon material.
2. The porous carbon material according to claim 1, wherein the porous carbon material has a porosity of 1-98%.
3. The porous carbon material according to claim 1, wherein the porous carbon material has a specific surface area of 0.5-3,000 m.sup.2/g.
4. The porous carbon material according to claim 1, wherein the carbon nano-rods are formed by etching a carbon material.
5. The porous carbon material according to claim 1, which further comprises carbon nanotubes formed in the pores or on the surface of the carbon nano-rods.
6. The porous carbon material according to claim 1, wherein the carbon material comprises at least one selected from the group consisting of carbon felt, carbon paper, carbon cloth, carbon fibers, hollow carbon fibers, carbon nanotubes, graphene fibers, graphene sheets, graphene oxide fibers, graphene oxide sheets, graphite plates, graphite powder, graphite sheets, carbon black powder, active carbon powder and composite graphite comprising a polymer in combination with graphite.
7. An electrode for electrochemical reaction, comprising the porous carbon material of in claim 1.
8. A method for manufacturing a porous carbon material, comprising: providing a catalyst for etching the surface of a carbon material; and etching the carbon material with the catalyst for etching to obtain a porous carbon material comprising carbon nano-rods formed on a surface of the carbon material, wherein the carbon nano-rods have a shape of a column, wherein the carbon nano-rods have a height of 10 nm-50 m and a diameter of 2-1,000 nm, and each carbon nano-rod is spaced apart from adjacent carbon nano-rods among the carbon nano-rods by a distance of 2-1,000 nm, and wherein the carbon nano-rods are extended in a longitudinal direction from the surface of the porous carbon material.
9. The method for manufacturing a porous carbon material according to claim 8, wherein the catalyst for etching comprises at least one selected from the group consisting of nickel (Ni), cobalt (Co), iron (Fe), manganese (Mn), ruthenium (Ru), vanadium (V), titanium (Ti), chromium (Cr), copper (Cu), zinc (Zn), tin (Sn), aluminum (Al), silicon (Si), rhodium (Rh), molybdenum (Mo), zirconium (Zr), tungsten (W), osmium (Os), iridium (Ir) and oxides thereof.
10. The method for manufacturing a porous carbon material according to claim 9, wherein the catalyst for etching further comprises a cocatalyst, and the cocatalyst comprises at least one selected from the group consisting of lithium (Li), potassium (K), sodium (Na), rubidium (Rb), cesium (Ce), magnesium (Mg), calcium (Ca), strontium (Sr), barium (Ba) and radium (Ra).
11. The method for manufacturing a porous carbon material according to claim 8, wherein the porous carbon material has a specific surface area of 0.5-3,000 m.sup.2/g.
12. The method for manufacturing a porous carbon material according to claim 8, further comprising: pretreating a carbon material to carry out surface modification; dispersing a catalyst precursor on the pretreated carbon material; heat-treating the catalyst precursor at a temperature of 100-800 C. to form a catalyst for etching on the surface of the carbon material; and heat-treating the carbon material having the catalyst for etching thereon at a temperature of 250-1,000 C. to form a porous carbon material having carbon nano-rods on the surface thereof.
13. The method for manufacturing a porous carbon material according to claim 12, wherein the surface modification is carried out at a temperature of 200-900 C.
14. The method for manufacturing a porous carbon material according to claim 12, wherein the catalyst precursor comprises at least one selected from the group consisting of metal nitrates, metal acetates, metal sulfates, metal carbonates, metal oxides and metal chlorides.
15. The method for manufacturing a porous carbon material according to claim 12, wherein the carbon material is etched partially to form the carbon nano-rods, when the carbon material having the catalyst for etching thereon is heat-treated.
16. The method for manufacturing a porous carbon material according to claim 8, further comprising, after the porous carbon material is obtained, dispersing a catalyst for forming carbon nanotubes to the porous carbon material, followed by reaction with a carbon source to form carbon nanotubes in the pores or on the surface of the carbon nano-rods.
17. The method for manufacturing a porous carbon material according to claim 16, wherein the catalyst for forming carbon nanotubes comprises at least one selected from the group consisting of nickel (Ni), cobalt (Co), iron (Fe), manganese (Mn), ruthenium (Ru), vanadium (V), titanium (Ti), chromium (Cr), copper (Cu), zinc (Zn), tin (Sn), aluminum (Al), silicon (Si), rhodium (Rh), molybdenum (Mo), zirconium (Zr), tungsten (W), osmium (Os), iridium (Ir) and oxides thereof.
18. The method for manufacturing a porous carbon material according to claim 17, wherein the catalyst for forming carbon nanotubes further comprises a cocatalyst, and the cocatalyst comprises at least one selected from the group consisting of lithium (Li), potassium (K), sodium (Na), rubidium (Rb), cesium (Ce), magnesium (Mg), calcium (Ca), strontium (Sr), barium (Ba) and radium (Ra).
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION
(9) Exemplary embodiments now will be described more fully hereinafter with reference to the accompanying drawings, in which exemplary embodiments are shown. The present disclosure may, however, be embodied in many different forms and should not be construed as limited to the exemplary embodiments set forth therein.
(10) As used herein, carbon material is a generic term that means carbon-containing materials, such as graphite, carbon nanotubes, carbon felt, carbon paper, carbon cloth, or the like.
(11) As used herein, porous carbon material means a carbon material formed by partial etching of a carbon material through an etching process using a catalyst for etching, and a carbon material having carbon nano-rods on the surface thereof.
(12) As used herein, carbon nano-rods, mean a carbon material formed on the surface of the porous carbon material, which have a shape of a column.
(13) Method for Manufacturing Porous Carbon Material
(14) In one aspect, there is provided a method for manufacturing a porous carbon material, including: providing a catalyst for etching to the surface of a carbon material; and etching the carbon material at the region provided with the catalyst for etching to obtain a porous carbon material having carbon nano-rods formed on the surface thereof.
(15) Particularly, the method for manufacturing a porous carbon material may include: pretreating a carbon material to carry out surface modification thereof; dispersing a catalyst precursor on the pretreated carbon material; heat-treating the catalyst precursor at a temperature of 100-800 C. to form a catalyst for etching on the surface of the carbon material; and heat-treating the carbon material having the catalyst for etching thereon at a temperature of 250-1,000 C. to form a porous carbon material having carbon nano-rods on the surface thereof.
(16)
(17) First, the surface of a carbon material is pretreated to carry out surface modification. The pretreatment step is intended to introduce a functional group for adsorbing or binding a catalyst precursor to the surface of the carbon material.
(18) According to an embodiment, the pretreatment may be carried out through a heat-treatment process, chemical treatment process, physical treatment process, or the like.
(19) According to another embodiment, the pretreatment process may be a heat-treatment process carried out by introducing the carbon material to a heating furnace under air and heating the carbon material at a temperature ranging from 200 C. to 900 C. for 5 minutes to 12 hours. Particularly, the total heating time may be 12 hours or less. Through the heating process, the surface of the carbon material is modified to form a functional group adsorbed or bound to a catalyst precursor with ease.
(20) According to still another embodiment, the chemical treatment process may be carried out by surface modification using an acidic material, such as hydrochloric acid, hydrosulfuric acid, nitric acid or hydrogen peroxide, an alkaline material, such as sodium hydroxide, potassium hydroxide or aqueous ammonia, or the like. In addition, it is possible to add a functional group through an organic solvent. Further, the physical treatment process may be carried out by subjecting the carbon material to plasma treatment.
(21) Meanwhile, the pretreatment may be carried out by using a heat-treatment process, chemical treatment process and a physical treatment process alone or in combination.
(22) According to still another embodiment, the carbon material may include at least one selected from the group consisting of carbon felt, carbon paper, carbon cloth, carbon fibers, hollow carbon fibers, carbon nanotubes, graphene fibers, graphene sheets, graphene oxide fibers, graphene oxide sheets, graphite plates, graphite powder, graphite sheets, carbon black powder, active carbon powder and composite graphite including a polymer in combination with graphite.
(23) Next, a catalyst precursor is dispersed on the surface of the pretreated carbon material.
(24) Particularly, the pretreated carbon material may be introduced to a precursor solution containing a catalyst precursor and a solvent, followed by agitation, so that the catalyst precursor may be adsorbed onto or infiltrated into the carbon material with ease.
(25) According to still another embodiment, the catalyst precursor may include metal nitrates, metal acetates, metal sulfates, metal carbonates, metal oxides and metal chlorides. For example, the catalyst precursor may include at least one selected from the group consisting of cobalt acetate, cobalt nitrate, cobalt chloride, nickel acetate, nickel nitrate, nickel chloride, iron nitrate, iron chloride, manganese acetate, manganese nitrate, manganese chloride, ruthenium (Ru), vanadium (V), titanium (Ti), chromium (Cr), copper (Cu), zinc (Zn), tin (Sn), aluminum (Al), silicon (Si), rhodium (Rh), molybdenum (Mo), zirconium (Zr), tungsten (W), osmium (Os), iridium (Ir), or the like.
(26) According to still another embodiment, the concentration of the catalyst precursor may be determined by the type of the catalyst precursor. In addition, it is possible to adjust the size range of the finished catalyst depending on the concentration of the catalyst precursor.
(27) According to still another embodiment, an amphiphilic solvent, such as an alcohol, may be used in combination with water as solvent in order to increase the wetness on the hydrophobic carbon material surface and to facilitate adsorption of the catalyst precursor.
(28) Meanwhile, a surfactant may be further added to obtain uniform dispersibility of the carbon material. The surfactant may be selected from a cationic surfactant, anionic surfactant, amphoteric surfactant and a nonionic surfactant. Particular examples of the surfactant may include cetyltrimethylammonium bromide (CTAB), sodium dodecylbenzene sulfonate (SDBS), sodium lauryl sulfate (SLS), polyethylene oxide-polypropylene oxide (PEO-PPO) block copolymer, betaine compounds, alcohol compounds, or the like.
(29) According to still another embodiment, the dispersion may be carried out for about 5 minutes to 12 hours so that the carbon material may be impregnated with the catalyst precursor effectively. Therefore, the carbon material may be impregnated with the catalyst precursor effectively. After that, the carbon material may be dried under air for at least 12 hours.
(30) Then, the catalyst precursor may be heat-treated to form a catalyst for etching on the surface of the carbon material.
(31) Particularly, the carbon material impregnated with the precursor may be introduced into a heating furnace and heat-treated under adequate gas atmosphere to form a metal or metal oxide.
(32) Herein, it is possible to adjust the shape and dispersibility of the catalyst depending on heat-treatment temperature and time.
(33) According to still another embodiment, the catalyst preparation may be carried out at a temperature ranging from 100 to 800 C. Particularly, the catalyst preparation may be carried out at a temperature ranging from 200 to 300 C. When the temperature is lower than 100 C., catalyst particles may not be formed. When the temperature is higher than 800 C., catalyst particles may be formed to have an excessively large size or an undesired change may appear in the structure of the carbon material.
(34) Meanwhile, the catalyst preparation may be carried out for a time ranging from 5 minutes to 5 hours. When the time is less than 5 minutes, catalyst particles may not be formed. When the time is more than 5 hours, catalyst particles may be formed to have an excessively large size or an undesired increase in cost may occur.
(35) According to an embodiment, the catalyst for etching may include at least one selected from the group consisting of nickel (Ni), cobalt (Co), iron (Fe), manganese (Mn), ruthenium (Ru), vanadium (V), titanium (Ti), chromium (Cr), copper (Cu), zinc (Zn), tin (Sn), aluminum (Al), silicon (Si), rhodium (Rh), molybdenum (Mo), zirconium (Zr), tungsten (W), osmium (Os), iridium (Ir) and oxides thereof.
(36) Meanwhile, the catalyst for etching may further include a cocatalyst that functions to accelerate etching of carbon and to change the porous structure of carbon, wherein the cocatalyst may include at least one selected from the group consisting of lithium (Li), potassium (K), sodium (Na), rubidium (Rb), cesium (Ce), magnesium (Mg), calcium (Ca), strontium (Sr), barium (Ba) and radium (Ra).
(37) After that, the catalyst for etching is used to etch the surface of the carbon material.
(38) Particularly, the carbon material impregnated with the catalyst for etching may be subjected to additional heat-treatment to carry out etching of the carbon material. Thus, it is possible to form a porous carbon material having carbon nano-rods on the surface thereof.
(39) According to still another embodiment, the etching may be carried out at a temperature ranging from 250 to 1,000 C. Particularly, the etching may be carried out at a temperature ranging from 350 to 600 C. When the etching is carried out at a temperature lower than 250 C., it is not possible to carry out etching to a desired degree. When the etching is carried out at a temperature higher than 1,000 C., etching may be carried out excessively, resulting in collapse of carbon structure. Meanwhile, when the temperature condition is changed, the finally formed carbon nano-rods may have a different shape.
(40) According to still another embodiment, the etching may be carried out for a time ranging from 5 minutes to 5 hours. When the etching time is less than 5 minutes, it is not possible to carry out etching sufficiently. When the etching time is more than 5 hours, etching may be carried out excessively or a significant increase in cost may occur. Meanwhile, when the etching time is changed, the finally formed carbon nano-rods may have a different shape.
(41) According to still another embodiment, during the etching, at least one gas selected from the group consisting of oxygen, nitrogen, carbon dioxide, hydrogen, water and argon may be added to the reaction container. In addition, it is possible to control the etching degree of the carbon material by adjusting the proportion of the gas. In this case, the finally formed carbon nano-rods of the porous carbon material may have a different shape.
(42) Meanwhile, the operation of forming a catalyst for etching on the surface of a carbon material and the operation of etching the carbon material may be carried out at the same time.
(43) As a result, a porous carbon material having carbon nano-rods on the surface thereof may be formed.
(44) According to still another embodiment, a plurality of carbon nano-rods may be formed.
(45) After that, although it is not shown in the figures, an additional process may be carried out to form carbon nanotubes additionally in the pores or on the surface of the porous carbon material.
(46) Particularly, a catalyst for forming carbon nanotubes is dispersed into the pores or onto the surface of the porous carbon material having carbon nano-rods thereon. Then, the porous carbon material may be introduced to a high-temperature reactor and a carbon source is injected thereto to form carbon nanotubes in the pores or on the surface of the porous carbon material through a chemical vapor deposition (CVD) process.
(47) According to still another embodiment, the carbon source may include at least one selected from the group consisting of methane, ethane, propane, butane, butylene, acetylene, propylene, or the like.
(48) According to still another embodiment, the catalyst for forming carbon nanotubes may include at least one selected from the group consisting of nickel (Ni), cobalt (Co), iron (Fe), manganese (Mn), ruthenium (Ru), vanadium (V), titanium (Ti), chromium (Cr), copper (Cu), zinc (Zn), tin (Sn), aluminum (Al), silicon (Si), rhodium (Rh), molybdenum (Mo), zirconium (Zr), tungsten (W), osmium (Os), iridium (Ir) and oxides thereof.
(49) According to still another embodiment, the catalyst for forming carbon nanotubes may further include a cocatalyst, wherein the cocatalyst may include at least one selected from the group consisting of lithium (Li), potassium (K), sodium (Na), rubidium (Rb), cesium (Ce), magnesium (Mg), calcium (Ca), strontium (Sr), barium (Ba) and radium (Ra).
(50) Meanwhile, the catalyst for forming carbon nanotubes may further include a cocatalyst for accelerating the growth rate of carbon nanotubes or controlling the shape of carbon nanotubes, wherein the cocatalyst may include at least one selected from the group consisting of lithium (Li), potassium (K), sodium (Na), rubidium (Rb), cesium (Ce), magnesium (Mg), calcium (Ca), strontium (Sr), barium (Ba) and radium (Ra).
(51) As described above, the porous carbon material obtained according to an embodiment may be formed to have a high specific surface area, and thus to provide a high electrochemically active area. The method for manufacturing a porous carbon material is carried out under ambient pressure, uses no special gas and requires no ultrahigh temperature, thereby providing an advantage of high cost-efficiency. In addition, the method uses a wet process when applying a catalyst to the surface of the carbon material. Thus, it is possible to obtain a porous carbon material having carbon nano-rods formed on the surface thereof by using a carbon material having a complicated structure.
(52) Further, according to the method for manufacturing a porous carbon material, the shape of the nanostructure formed on the carbon surface may be affected by the concentration of a catalyst precursor for etching, the dispersibility of a catalyst for etching and the size of catalyst particles. Thus, when such conditions are changed, the surface structure of the carbon material may be controlled to a desired shape. Therefore, it is possible to obtain porous carbon materials having various shapes. In addition, it is possible to change the surface structure of a porous carbon material by adjusting the temperature and time while the catalyst is etched, and thus to obtain porous carbon materials having various shapes.
(53) Porous Carbon Material
(54) In another aspect, there is provided a porous carbon material having carbon nano-rods on the surface thereof.
(55) The porous carbon material has carbon nano-rods formed on the surface thereof, and may have high porosity and a high specific surface area. Thus, the porous carbon material may provide high performance, when used as an electrode for electrochemical reaction by virtue of an increase in electrochemically active surface area.
(56) In addition, the carbon nano-rods are etched by using a catalyst for etching, and the porous carbon material may be provided with additional functions depending on the type of the catalyst. Thus, it is possible to obtain carbon materials having various properties. Such additional functions may include those as an electrode for use in fuel cells or electrochemical conversion processes or as an electrode for secondary batteries.
(57) Hereinafter, the porous carbon material will be explained in more detail.
(58) According to an embodiment, the carbon material may include at least one selected from the group consisting of carbon felt, carbon paper, carbon cloth, carbon fibers, hollow carbon fibers, carbon nanotubes, graphene fibers, graphene sheets, graphene oxide fibers, graphene oxide sheets, graphite plates, graphite powder, graphite sheets, carbon black powder, active carbon powder and composite graphite including a polymer in combination with graphite.
(59) According to another embodiment, the carbon nano-rods may be formed by etching the carbon material having the catalyst for etching formed on the surface thereof.
(60) According to still another embodiment, the catalyst for etching may include at least one selected from the group consisting of nickel (Ni), cobalt (Co), iron (Fe), manganese (Mn), ruthenium (Ru), vanadium (V), titanium (Ti), chromium (Cr), copper (Cu), zinc (Zn), tin (Sn), aluminum (Al), silicon (Si), rhodium (Rh), molybdenum (Mo), zirconium (Zr), tungsten (W), osmium (Os), iridium (Ir) and oxides thereof.
(61) According to still another embodiment, the catalyst for etching may further include a cocatalyst, wherein the cocatalyst may include at least one selected from the group consisting of lithium (Li), potassium (K), sodium (Na), rubidium (Rb), cesium (Ce), magnesium (Mg), calcium (Ca), strontium (Sr), barium (Ba) and radium (Ra).
(62) According to still another embodiment, the carbon nano-rods may have a height of 10 nm-50 m and a diameter of 2-1,000 nm. In addition, a plurality of carbon nano-rods may be formed and each carbon nano-rod may be spaced apart from the adjacent carbon nano-rods by a distance of 2-1,000 nm. As a result, the porous carbon material may have an increased specific surface area and may provide an increased electrochemically active surface area.
(63) According to still another embodiment, the porous carbon material may have a specific surface area of 0.5-3,000 m.sup.2/g. When the specific surface area is smaller than 0.5 m.sup.2/g, it is difficult to expect the function of the porous carbon material as an electrode. When the specific surface area is larger than 3,000 m.sup.2/g, the structure of the carbon material becomes unstable and thus it is not possible to provide sufficient advantages derived from an increase in specific surface area.
(64) In addition, the porous carbon material may have a porosity of 1-98%. When the porosity is less than 1%, it is not possible to obtain an effect derived from an increase in specific surface area. When the porosity is larger than 98%, the carbon material may undergo degradation of structural stability.
(65) Exemplary embodiments now will be described more fully hereinafter with reference to the accompanying drawings, in which exemplary embodiments are shown for illustrative purposes only. The present disclosure may, however, be embodied in many different forms and should not be construed as limited to the exemplary embodiments set forth therein.
EXAMPLES
Example 1: Manufacture of Porous Carbon Material
(66) A catalyst is supported on carbon felt, followed by heat-treatment, and then etching is carried out by using the catalyst to form nano-structures on the surface of the carbon felt. First, carbon felt is introduced to a heating furnace, heated under air from room temperature at a rate of 10 C./min, maintained at 500 C. for 4 hours, and cooled down to room temperature. The pretreated carbon felt is dipped in aqueous ethanol solution containing cobalt acetate hydrate as a precursor of catalyst for etching for 1 hour and dried at room temperature under air for 12 hours. Then, the carbon felt having the metal oxide precursor adsorbed on the surface thereof is introduced to a heating furnace, warms under air from room temperature at a rate of 10 C./min and maintained at 300 C. for 1 hour to prepare a metal oxide. After that, the carbon felt having the metal oxide catalyst supported thereon is heated again under air from room temperature at a rate of 10 C./min, and maintained at 400 C. for 1 hour to form porous nano-structures having the shape of a plurality of carbon nano-rods on the surface through the surface etching of carbon felt in the presence of the metal oxide catalyst.
Examples 2 and 3
(67) Example 1 is repeated, except that the temperature during the etching process is set to 200 C. and 500 C. instead of 400 C. to provide the porous carbon materials according to Examples 2 and 3.
Examples 4 and 5
(68) Example 1 is repeated, except that the processing time during the etching process is set to 30 minute and 2 hours instead of 1 hour to provide the porous carbon materials according to Examples 4 and 5.
Examples 6-9
(69) Example 1 is repeated, except that cobalt nitrate, nickel acetate, iron nitrate and manganese acetate are used as the precursors of the catalyst for etching instead of cobalt acetate to provide the porous carbon materials according to Examples 6-9.
Example 10
(70) Example 1 is repeated, except that the carbon felt having the precursor of the catalyst for etching adsorbed on the surface thereof is introduced to a heating furnace, heated under air from room temperature at a rate of 10 C./min, and maintained at 400 C. for 1 hour or 2 hours so that synthesis of a catalyst for etching may be carried out simultaneously with etching. In this manner, the porous carbon material according to Example 10 is provided.
Comparative Example 1
(71) Bare carbon felt having no catalyst for etching is introduced to a heating furnace, heated under air from room temperature at a rate of 10 C./min, and maintained at 500 C. for 4 hours.
Comparative Example 2
(72) Example 1 is repeated to carry out heat-treatment of carbon felt, except that no catalyst precursor is supported on the carbon felt.
(73) In other words, in the same manner as Comparative Example 1, bare carbon felt is introduced to a heating furnace, warmed under air from room temperature at a rate of 10 C./min, heat-treated at 500 C. for 4 hours, and then cooled to room temperature (pretreatment process for carbon felt). In addition, the pretreated carbon felt is heated under air at a rate of 10 C./min, maintained at 300 C. for 1 hour, and cooled naturally to room temperature (heat-treatment conditions while the catalyst is supported on the carbon felt; no catalyst is supported in the carbon felt herein). Then, the carbon felt is warmed again under air at a rate of 10 C./min, maintained at 400 C. for 1 hour, and cooled to room temperature (heat-treatment is carried out in the same manner as the process for etching the carbon surface).
Test Example 1: Determination of Surface Structure of Porous Carbon Material
(74) The porous carbon materials according to Comparative Examples 1 and 2 and the carbon felt according to Example 1 are observed for their surfaces by using an electron microscope, and the results are shown in
(75)
(76) Referring to
(77) In addition, it can be seen from
(78) Meanwhile, referring to
Test Example 2: Determination of Change in Surface of Porous Carbon Material Depending on Etching Temperature
(79) The porous carbon materials obtained at an etching temperature of 200 C. and 500 C. according to Examples 2 and 3 are observed for their surfaces and are shown in
(80)
Test Example 3: Determination of Change in Surface of Porous Carbon Material Depending on Etching Time
(81) The porous carbon materials according to Examples 1, 4 and 5 are observed for their surfaces and are shown in
(82) Particularly,
(83) Referring to
Test Example 4: Determination of Change in Surface of Porous Carbon Material Depending on Change in Type of Precursor
(84) The porous carbon materials according to Examples 6, 7, 8 and 9 are observed for their surfaces and are shown in
(85) Particularly,
(86) As can be seen from the surface images of
Test Example 5: Determination of Porous Carbon Material when Carrying Out Catalyst Synthesis Simultaneously with Etching
(87) The porous carbon material according to Example 10 is observed for its surface and is shown in
(88)
(89) When comparing
Test Example 6: Evaluation of Performance of Vanadium Redox Flow Battery
(90) Vanadium redox flow batteries are provided by using the porous carbon material according to Example 1 and the porous carbon material according to Comparative Example 1.
(91) Particularly, each of the porous carbon material (Example 1) and the reference carbon material (Comparative Example 1) is mounted to a different unit cell having an electrode area of 25 cm.sup.2 to provide batteries. Herein, 50 mL of an electrolyte containing 1.5M VOSO.sub.4/3M H.sub.2SO.sub.4 is allowed to circulate in each vanadium battery at a rate of 50 mL/min, and each battery is subjected to charge/discharge cycles at a current density of 50 mA/cm.sup.2 under a state of charge (SOC) of 80%.
(92) Then, the performance of each battery is determined and the results are shown in the following Table 1.
(93) TABLE-US-00001 TABLE 1 Current density Energy efficiency Voltage efficiency (%) (%) (%) Comparative 92.8 84.2 83.8 Example 1 Example 1 96.8 88.2 91.2
(94) It can be seen from Table 1 that the battery using the porous carbon material according to Example 1 shows an energy efficiency increased by about 4% as compared to the battery using conventional carbon felt according to Comparative Example 1. It is thought that such a result is derived from an increase in an electrochemically active surface area of the modified carbon felt and an increase in redox reaction sites of vanadium ions, leading to improvement of redox reversibility of reactant species.
(95) While the exemplary embodiments have been shown and described, it will be understood by those skills in the art that various changes in form and details may be made thereto without departing from the spirit and scope of the present disclosure as defined by the appended claims. In addition, many modifications can be made to adapt a particular situation or material to the teachings of the present disclosure without departing from the essential scope thereof. Therefore, it is intended that the present disclosure not be limited to the particular exemplary embodiments disclosed as the best mode contemplated for carrying out the present disclosure, but that the present disclosure will include all embodiments falling within the scope of the appended claims.