Abstract: A method for evaluating a conductive material for use in a rechargeable battery is provided. The rechargeable battery includes an electrode plate in which a mixture layer, containing an active material and the conductive material, is formed on a substrate. The method includes preparing a paste containing simulated primary particles and the conductive material. The simulated primary particles are formed of an insulative material that simulates the active material of the rechargeable battery. The method further includes applying the prepared paste to a simulated substrate that simulates the substrate of the rechargeable battery, drying the applied paste to prepare a test coating containing the simulated primary particles, and measuring a coating resistance RS (?·cm) to evaluate the conductive material. The coating resistance corresponds to a surface resistance of the test coating.

Abstract: Carbon nanotubes have a bulk density X of 0.095 g/cm3 or more and 0.125 g/cm3 or less, a Zr content of 5 ppm or more and 500 ppm or less, and a maximum solvent absorption capacity Y of carbon nanotubes defined by formula (5) below of 8.0 or more, Y = W / V forumla ? ( 5 ) (in formula (5), V is a mass (g) of carbon nanotubes, and W is a maximum mass (g) of N-methyl-2-pyrrolidone absorbed by carbon nanotubes when N-methyl-2-pyrrolidone is added dropwise to V (g) of carbon nanotubes in a 25° C. environment).

Abstract: Carbon nanotubes have a bulk density X of 0.095 g/cm3 or more and 0.125 g/cm3 or less, a Zr content of 5 ppm or more and 500 ppm or less, and a maximum solvent absorption capacity Y of carbon nanotubes defined by formula (5) below of 8.0 or more, Y=W/V??formula (5) (in formula (5), V is a mass (g) of carbon nanotubes, and W is a maximum mass (g) of N-methyl-2-pyrrolidone absorbed by carbon nanotubes when N-methyl-2-pyrrolidone is added dropwise to V (g) of carbon nanotubes in a 25° C. environment).

Abstract: An object is to provide a PHA production method which enables efficient filtration. The above problem is solved by providing a PHA production method including a filtration step of subjecting, to dead-end filtration, an aqueous PHA suspension having a pH of 2.5 to 5.5 with use of a filter medium having an air permeability of 0.01 cc/cm2/sec to 5.0 cc/cm2/sec, the aqueous PHA suspension containing PHA surface adhesion protein in an amount of not more than 2,000 ppm, the aqueous PHA suspension having a liquid density of 0.50 g/mL to 1.08 g/mL in the filtration step.

Abstract: An object is to provide a PHA production method which enables efficient filtration. A PHA production method is provided, the PHA production method including: a heating step of heating an aqueous PHA suspension containing a specific additive and having a pH of 2.5 to 5.5 such that the aqueous PHA suspension has a temperature of 60° C. to 95° C.; a cooling step of cooling the aqueous PHA suspension obtained in the heating step to a specific temperature; and a filtration step of subjecting, to dead-end filtration, the aqueous PHA suspension obtained in the cooling step, with use of a filter medium having an air permeability of 0.01 cc/cm2/sec to 5.0 cc/cm2/sec, so that the above problem is solved.

Abstract: An objective of the present invention is to provide a production method that enables PHA (e.g. PHA powder) to be produced with high productivity. The above is achieved by providing: a method for producing a polyhydroxyalkanoate, including the steps of (a) preparing an aqueous suspension that contains a polyhydroxyalkanoate and an alkylene oxide-based dispersing agent and has a pH of not more than 7 and (b) spray-drying the aqueous suspension prepared in the step (a); and the like.

Abstract: Provided are: a dispersant which has good dispersibility and reduces electronic resistance; and a battery having excellent characteristics, which uses this dispersant and is decreased in the ionic resistance and the reaction resistance. A dispersant contains a triazine derivative represented by general formula (1), and an amine or an inorganic base (in general formula (1), R1 is as defined in the description).

Abstract: Provided are: a dispersant which has good dispersibility and reduces electronic resistance; and a battery having excellent characteristics, which uses this dispersant and is decreased in the ionic resistance and the reaction resistance. A dispersant contains a triazine derivative represented by general formula (1), and an amine or an inorganic base (in general formula (1), R1 is as defined in the description).

Abstract: A method for producing chlorinated polyvinyl chloride includes bringing chlorine gas into contact with a mixture comprising a polyvinyl chloride powder and at least one inorganic filler; and irradiating the mixture with UV light to perform a chlorination reaction. At least one inorganic filler is selected from the group consisting of silica, carbon black, and talc.

Abstract: A method for producing chlorinated polyvinyl chloride includes bringing chlorine gas into contact with a mixture comprising a polyvinyl chloride powder and at least one inorganic filler; and irradiating the mixture with UV light to perform a chlorination reaction. At least one inorganic filler is selected from the group consisting of silica, carbon black, and talc.

Abstract: A cell catalyst composition according to the present invention includes a carbon catalyst granule and a binder resin, and at least a part of the binder resin includes a resin (B) including a hydrophilic functional group. The carbon catalyst granule is (i) a carbon catalyst granule wherein carbon catalyst (A) particles are bound to each other by using at least the resin (B), or/and (ii) a carbon catalyst granule wherein carbon catalyst (A) particles form a sintered body and are thereby bound to each other. The carbon catalyst (A) includes a carbon element, a nitrogen element, and a base metal element as constituent elements. Further, an average particle diameter of the carbon catalyst granule is 0.5 to 100 ?m, and a sphericity of the carbon catalyst granule is equal to or greater than 0.5.

Abstract: A sludge receiving facility is provided with upper and lower structures respectively having inner spaces communicating with each other, wherein sludge tanks each having a sludge charging port are provided in the lower structure, and a partition wall configured to partition a carrying-in space of the upper structure from the inner space is provided, the sludge receiving facility including: outside air blowing means; air circulating means configured to enable the inner space and the carrying-in space to communicate with each other; first exhausting means configured to exhaust air from an upper part of the carrying-in space; second exhausting means configured to exhaust air above the sludge charging port; and third exhausting means configured to exhaust air inside the sludge tanks, wherein opening/closing means are respectively provided in the circulating means and the first to third exhausting means.

Abstract: A sludge receiving facility is provided with upper and lower structures respectively having inner spaces communicating with each other, wherein sludge tanks each having a sludge charging port are provided in the lower structure, and a partition wall configured to partition a carrying-in space of the upper structure from the inner space is provided, the sludge receiving facility including: outside air blowing means; air circulating means configured to enable the inner space and the carrying-in space to communicate with each other; first exhausting means configured to exhaust air from an upper part of the carrying-in space; second exhausting means configured to exhaust air above the sludge charging port; and third exhausting means configured to exhaust air inside the sludge tanks, wherein opening/closing means are respectively provided in the circulating means and the first to third exhausting means.