Abstract: A carbon material for a catalyst carrier of a polymer electrolyte fuel cell, in which a nitrogen adsorption/desorption isotherm exhibits two hysteresis loops having a first hysteresis loop and a second hysteresis loop in a range where a relative pressure P/P0 is 0.4 or more.

Abstract: A support for a polymer electrolyte fuel cell catalyst satisfying the following requirements (A), (B), (C), and (D), and a producing method thereof, as well as a catalyst layer for a polymer electrolyte fuel cell and a fuel cell: (A) a specific surface area according to a BET analysis of a nitrogen adsorption isotherm is from 450 to 1500 m2/g. (B) a nitrogen adsorption and desorption isotherm forms a hysteresis loop in a range of relative pressure P/P0 of more than 0.47 but not more than 0.90, and a hysteresis loop area ?S0.47-0.9 is from 1 to 35 mL/g; (C) a relative pressure Pclose/P0 at which the hysteresis loop closes is more than 0.47 but not more than 0.70; and (D) a half-width of a G band detected by Raman spectrometry in a range of from 1500 to 1700 cm?1 is from 45 to 75 cm?1.

Abstract: The present invention is a carbon material for a catalyst carrier of a polymer electrolyte fuel cell, which has a three-dimensional dendritic structure, and simultaneously satisfies the following (A), (B), and (C). (A) By a laser Raman spectroscopic analysis with a wavelength of 532 nm, a standard deviation ?(R) of an intensity ratio (R value) of an intensity of a D-band (near 1360 cm?1) to an intensity of a G-band (near 1580 cm?1) measured with a beam diameter of 1 ?m at 50 measurement points is from 0.01 to 0.07. (B) A BET specific surface area SBET is from 400 to 1520 m2/g. (C) A nitrogen gas adsorption amount VN:0.4-0.8 during a relative pressure (p/p0) from 0.4 to 0.8 is from 100 to 300 cc(STP)/g. A method of producing such a carbon material for a catalyst carrier is also included.

Abstract: Provided are a carbon material for a catalyst carrier of a polymer electrolyte fuel cell, the carbon material being a porous carbon material and simultaneously satisfying (1) an intensity ratio (I750/Ipeak) of an intensity at 750° C. (I750) and a peak intensity in a vicinity of 690° C. (Ipeak), in a derivative thermogravimetric curve (DTG) obtained by a thermogravimetric analysis when a temperature is raised at a rate of 10° C./min under an air atmosphere, is 0.10 or less; (2) a BET specific surface area, determined by BET analysis of a nitrogen gas adsorption isotherm, is from 400 to 1,500 m2/g; (3) an integrated pore volume V2-10 of a pore diameter of from 2 to 10 nm, determined by analysis of the nitrogen gas adsorption isotherm using Dollimore-Heal method, is from 0.4 to 1.5 mL/g; and (4) a nitrogen gas adsorption amount Vmacro at a relative pressure of from 0.95 to 0.99 in the nitrogen gas adsorption isotherm is from 300 to 1,200 cc(STP)/g, as well as a method of producing the same.

Abstract: A support for a polymer electrolyte fuel cell catalyst satisfying the following requirements (A), (B), (C), and (D), and a producing method thereof, as well as a catalyst layer for a polymer electrolyte fuel cell and a fuel cell: (A) a specific surface area according to a BET analysis of a nitrogen adsorption isotherm is from 450 to 1500 m2/g. (B) a nitrogen adsorption and desorption isotherm forms a hysteresis loop in a range of relative pressure P/P0 of more than 0.47 but not more than 0.90, and a hysteresis loop area ?S0.47-0.9 is from 1 to 35 mL/g; (C) a relative pressure Pclose/P0 at which the hysteresis loop closes is more than 0.47 but not more than 0.70; and (D) a half-width of a G band detected by Raman spectrometry in a range of from 1500 to 1700 cm?1 is from 45 to 75 cm?1.

Abstract: A carbon material for use as a catalyst carrier for a polymer electrolyte fuel cell which is a porous carbon material and satisfies at the same time (1) the content of a crystallized material is 1.6 or less, (2) the BET specific surface area obtained by a BET analysis of a nitrogen gas adsorption isotherm is from 400 to 1500 m2/g, (3) the cumulative pore volume V2-10 with respect to a pore diameter of from 2 to 10 nm obtained by an analysis of a nitrogen gas adsorption isotherm using the Dollimore-Heal method is from 0.4 to 1.5 mL/g, and (4) the nitrogen gas adsorption amount Vmacro between a relative pressure of 0.95 and 0.99 in a nitrogen gas adsorption isotherm is from 300 to 1200 cc(STP)/g, and the method of producing the same.

Abstract: The present invention is a carbon material for a catalyst carrier of a polymer electrolyte fuel cell, which has a three-dimensional dendritic structure, and simultaneously satisfies the following (A), (B), and (C). (A) By a laser Raman spectroscopic analysis with a wavelength of 532 nm, a standard deviation ?(R) of an intensity ratio (R value) of an intensity of a D-band (near 1360 cm?1) to an intensity of a G-band (near 1580 cm?1) measured with a beam diameter of 1 ?m at 50 measurement points is from 0.01 to 0.07. (B) A BET specific surface area SBET is from 400 to 1520 m2/g. (C) A nitrogen gas adsorption amount VN:0.4-0.8 during a relative pressure (p/p0) from 0.4 to 0.8 is from 100 to 300 cc(STP)/g. A method of producing such a carbon material for a catalyst carrier is also included.