Kawasaki Jukogyo Kabushiki Kaisha

Masaki Tsuzawa

Noriaki Izumi

Hironori Tajiri

Hiromasa Kusuda

Koji Fukumoto

Fuminori Ando

Shoji Tsujita

Mariko Yamashita

Hiroaki Osawa

Chie Nakajima

Masahiro Sugata

Ryosuke Nagai

Hideto Matsuyama

Takashi Nishino

Shoji Takada

A system for processing a waste lithium-ion battery includes: a first aqueous solution generator that includes a first elution tank storing water, and that immerses an active material taken out from the waste lithium-ion battery in the water in the first elution tank and subjects the active material to carbon dioxide bubbling in the first elution tank to generate an aqueous solution of pH 5.5 to 8.5, in which lithium contained in the active material is eluted; a first solid-liquid separator that removes a solid component from the aqueous solution generated by the first aqueous solution generator; a first crystallizer that causes lithium carbonate to be deposited from the aqueous solution, from which the solid component has been removed by the first solid-liquid separator; and a second solid-liquid separator that performs solid-liquid separation on slurry containing the lithium carbonate deposited in the first crystallizer to take out the lithium carbonate.

System for and method of processing waste lithium-ion battery

A system for and a method of processing a waste lithium-ion battery make it possible to improve heat treatment efficiency and to heat-treat a large-sized waste lithium-ion battery without disassembling the battery. One example of the system for processing a waste lithium-ion battery includes a heater that heat-treats a waste lithium-ion battery at a heating temperature of lower than 400° C. to decompose and remove an electrolyte solution from the waste lithium-ion battery.

A method of producing a saccharified solution, in which saccharified slurry is obtained by hydrothermally treating cellulosic biomass slurry in a supercritical state or a subcritical state by a continuous reactor. The method reduces the risk of a pressure reducing valve becoming clogged when the high-temperature and high-pressure slurry is flash-evaporated after being hydrothermally treated. Also provides an apparatus for producing a saccharified solution and a continuous reactor. At the time of hydrothermally treating the cellulosic biomass slurry by the continuous reactor continuously, the slurry is intensely stirred in a front part of the continuous reactor, and stirred in a rear part of the continuous reactor by a stirring device with low propelling force, such that the plug flow in the axial direction is kept while the slurry is being uniformly mixed with respect to the cross section perpendicular to the mixing axis.

Method of and apparatus for producing saccharified solution by using biomass as raw material, and continuous reactor

A saccharification-reaction apparatus includes: a reactor which causes a saccharification-reaction of a raw material; and a raw material charging device which charges the raw material into the reactor at a predetermined interval; the reactor includes: a heating steam feeder which increases a temperature of the raw material charged from the charging device to a saccharification-reaction temperature; and a feeding mechanism which sequentially feeds each of the charged raw materials toward an outlet-port in a predetermined short period of time while causing the saccharification-reaction of each raw material under a high temperature and pressure; the raw material charging-device charges into the reactor, the raw material with a suitable bulk density for a saccharification-reaction speed of the reactor; in this manner, the saccharification-reaction apparatus charges the raw material in a hydrolytic saccharification state into the reactor by the raw material charging device; and hydrolytically saccharifying the raw material efficiently in the reactor.

Saccharification reaction apparatus

A saccharide recovering method for recovering saccharides from a saccharified slurry obtained after subjecting a slurry of cellulosic biomass to a hot water treatment and to provide a washing device for washing a saccharified slurry residue suited for conducting such a saccharide recovery method is provided. Saccharified slurry of cellulosic biomass is fed on a conveyor having a net conveyor belt, the saccharified slurry is dehydrated, washing water is sprayed to dissolve saccharides remaining in the residue into the washing liquid. The residue is washed by a plurality of washing water spraying units disposed in series in such a manner that the moving direction of the residue and the moving direction of the washing water are opposite to each other. The washing water having washed the residue is used as washing water for washing water spraying unit in the direction opposite to the moving direction of the conveyor.

Method for recovering saccharide from saccharified slurry, and washing device for washing residue

A dope solution for membrane production comprising polyethersulfone having high strength, high water permeability, a high rejecting ability and excellent contamination resistance, a separation membrane, and a process for producing the separation membrane are provided. The dope solution for membrane production contains a polyethersulfone and a solvent for thermally induced phase separation selected from the group consisting of 3-pyridinemethanol, 4-methyl-1,3-dioxolane-2-one, 4-benzylpiperidine, trimethyl phosphate, 1,3-dioxolane-2-one and mixtures thereof.

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Kobe, Japan

Masaki Tsuzawa