Abstract: Redox flow battery 1 include cell frame 20 having recess 21, 22, at least one sheet-like electrode 11, 13 received in recess 21, 22, membrane 15 stacked on cell frame 20 to cover recess 21, 22, and bipolar current collecting member 40 penetrating cell frame 20 at recess 21, 22 and electrically connected to at least one electrode 11, 13, wherein cell frame 20 has flow channels 31-38 communicating with recess 21, 22 so as to allow a fluid containing an active material to flow through recess 21, 22 parallel to membrane 15, and wherein at least one electrode 11, 13 is disposed in recess 21, 22 at an angle where at least one electrode 11, 13 intersects membrane 15.

Abstract: Redox flow battery includes cell frame 20 including frame body 21 and bipolar plate 23, frame body 21 having rectangular opening 22 divided into a plurality of small openings 22a-22c along first direction X parallel to a longitudinal direction of opening 22, bipolar plate 23 divided into a plurality of regions 23a-23c, each of regions 23a-23c disposed within each of small openings 22a-22c to form a plurality of recesses, and electrode 11 divided into a plurality of regions 11a-11c, each of regions 11a-11c received in each of the recesses, wherein each of small openings 22a-22c has a rectangular shape whose longitudinal direction is parallel to first direction X.

Abstract: Cell frame 20 includes: frame body 21 having an opening 22, frame body 21 including through-hole 31 for passage of a fluid containing an active material, through-hole 31 penetrating from one surface of frame body 21 to the other surface thereof around opening 22, and groove-like slit 35 formed in one surface or the other surface and connecting through-hole 31 and opening 22; and rotor 40 made of an insulating material, rotor 40 received in slit 35 and forced to rotate by the flow of the fluid through slit 35 between through-hole 31 and opening 22.

Abstract: Redox flow battery 1 includes cell stack 2, first positive-electrode tank 11, second positive-electrode tank 12, first negative-electrode tank 21, and second negative-electrode tank 22. Cell stack 2 is divided into a plurality of cell groups 3, each of which consists of a plurality of cells 4. The plurality of cell groups 3 are connected to first and second positive-electrode tanks 11, 12 such that a positive-electrode fluid containing positive-electrode active material flows in parallel through the plurality of cell groups 3, and are connected to first and second negative-electrode tanks 21, 22 such that a negative-electrode fluid containing negative-electrode active material flows in parallel through the plurality of cell groups 3. The plurality of cells 4 in each cell group 3 are connected to each other such that the positive-electrode fluid flows in series through a plurality of positive cells 5 and such that the negative-electrode fluid flows in series through a plurality of negative cells 6.

Abstract: Redox flow battery 1 includes cell stack 2, first positive-electrode tank 11, second positive-electrode tank 12, first negative-electrode tank 21, and second negative-electrode tank 22. Cell stack 2 is divided into a plurality of cell groups 3, each of which consists of a plurality of cells 4. The plurality of cell groups 3 are connected to first and second positive-electrode tanks 11, 12 such that a positive-electrode fluid containing positive-electrode active material flows in parallel through the plurality of cell groups 3, and are connected to first and second negative-electrode tanks 21, 22 such that a negative-electrode fluid containing negative-electrode active material flows in parallel through the plurality of cell groups 3. The plurality of cells 4 in each cell group 3 are connected to each other such that the positive-electrode fluid flows in series through a plurality of positive cells 5 and such that the negative-electrode fluid flows in series through a plurality of negative cells 6.

Abstract: Chemical heat pump system 1 includes: endothermic unit 3 that contains a slurry containing a solid product and that absorbs heat supplied from an outside to perform an endothermic reaction at first pressure P1; exothermic unit 2 that contains a slurry containing a solid reactant and that performs an exothermic reaction at a second pressure P2 that is higher than the first pressure P1 to generate heat; gas recovery supply unit 4 that recovers a gas reactant that has been decomposed in endothermic unit 3 and that supplies the gas reactant to exothermic unit 2; and circulation unit 5 that supplies the slurry containing the solid reactant, that has been decomposed in endothermic unit 3, to exothermic unit 2 after pressurizing the slurry from first pressure P1 to second pressure P2, and that supplies the slurry containing the solid product, that has been produced in exothermic unit 2, to endothermic unit 3 after depressurizing the slurry from second pressure P2 to first pressure P1, so as to circulate the slurry b

Abstract: Chemical heat storage system 1 based on an exothermic reaction that produces a solid product from a solid reactant and a gas reactant and an endothermic reaction that decomposes the solid product into the solid reactant and the gas reactant, includes: endothermic unit 3 that contains a slurry containing the solid product and that absorbs heat supplied from the outside to perform the endothermic reaction; exothermic unit 2 that contains a slurry containing the solid reactant and that performs the exothermic reaction to generate heat; and gas recovery supply unit 4 that recovers the gas reactant that has been decomposed in endothermic unit 3 and that supplies the gas reactant to exothermic unit 2.

Abstract: The duty of internal heat exchange can be flexibly adjusted without impairing energy saving performance of a HIDiC. A method of adjusting the duty of heat exchange in a heat exchange structure of a HIDiC includes totally condensing a portion of the vapor fed to a heat exchange structure in a heat exchange structure; and providing a liquid control valve downstream of the heat exchange structure on the first line, without providing a control valve on a vapor-flowing part of first and second lines of the HIDiC, and adjusting a flow rate of a portion of the compressor outlet vapor flowing into the heat exchange structure by using the control valve, while compensating for a pressure loss needed for the control valve by using a liquid head of a condensate, and/or by using pressurization by a pump.

Abstract: A distillation apparatus of the present invention includes high-pressure column 1 corresponding to a region above a heat exchanging section located at a lowermost part of a region including a trayed section or a packed bed section, which is used as a rectifying section; and low-pressure column 2 that is located above as seen from high-pressure column 1, which integrates a region including a trayed section or a packed bed section which is used as a stripping section, with rectifying section corresponding portion 2g that corresponds to a region locating below the heat exchanging section located at the lowermost part in the rectifying section. Rectifying section corresponding portion 2g is located on top 2c of the stripping section in low-pressure column 2 so that rectifying section corresponding portion 2g continues to the stripping section.

Abstract: A distillation apparatus includes a first distillation column and one or more second distillation columns. A higher-pressure part of the first distillation column includes at least part of a rectifying section, and performs gas-liquid contact at a relatively high pressure. A lower pressure-part of the first distillation column includes at least part of a stripping section and performs gas-liquid contact at a relatively low pressure. A vapor line, which includes a pressurizing means, directs a vapor discharged from a column top of the lower-pressure part to a column bottom of the higher-pressure part. A liquid line directs a liquid discharged from the column bottom of the higher-pressure part to the column top of the lower pressure part. Corresponding heat exchange structures transfer heat in both directions between the rectifying section of the first distillation column and at least one second distillation column.

Abstract: The duty of internal heat exchange can be flexibly adjusted without impairing energy saving performance of a HIDiC. A method of adjusting the duty of heat exchange in a heat exchange structure of a HIDiC includes totally condensing a portion of the vapor fed to a heat exchange structure in a heat exchange structure; and providing a liquid control valve downstream of the heat exchange structure on the first line, without providing a control valve on a vapor-flowing part of first and second lines of the HIDiC, and adjusting a flow rate of a portion of the compressor outlet vapor flowing into the heat exchange structure by using the control valve, while compensating for a pressure loss needed for the control valve by using a liquid head of a condensate, and/or by using pressurization by a pump.

Abstract: A distillation apparatus includes a rectifying column, a stripping column, a first pipe that communicates a column top of the stripping column with a column bottom of the rectifying column, and a compressor configured to compress vapor from the stripping column and then to feed the compressed vapor to the rectifying column. The distillation apparatus further includes a heat exchanger located at a predetermined stage of the rectifying column, a liquid withdrawal unit located at a predetermined stage of the stripping column and configured to withdraw a part of liquid from the predetermined stage to an outside of the column, a second pipe that introduces the liquid from the liquid withdrawal unit to the heat exchanger, and a third pipe that introduces fluids introduced through the second pipe to the heat exchanger and then discharged out of the heat exchanger to a stage directly below the liquid withdrawal unit.

Abstract: A distillation apparatus includes a rectifying column, a stripping column located above seen from the rectifying column, a liquid sump unit located at a predetermined stage of the stripping column and configured to hold liquid that has flowed downward, a heat exchanger located in the liquid sump unit, a second pipe for introducing vapor in the rectifying column to the heat exchanger of the stripping column, and a third pipe for introducing fluids flowing out from the heat exchanger of the stripping column to the rectifying column. Further, a flare line having lower pressure than pressure in the rectifying column is connected to a downstream side of the third pipe. The distillation apparatus can switch a first flow toward an inside of the rectifying column through the third pipe to a second flow branching from the third pipe toward a pipe at a lower pressure side.

Abstract: In a heat integrated distillation column (HIDiC), the product purity can be stably maintained against various disturbances. Provided is a method for controlling a distillation apparatus, which includes a high-pressure part including the whole or a part of a rectifying section and performing gas-liquid contact at a relatively high pressure; a low-pressure part including the whole or a part of a stripping section and performing gas-liquid contact at a relatively low pressure; a line for directing overhead vapor of the low-pressure part to a column bottom of the high-pressure part; a line for directing a column bottom liquid of the high-pressure part to a column top of the low-pressure part; and a heat exchange structure for transferring heat from the rectifying section to the stripping section, wherein the method includes controlling a flow rate of the column bottom liquid to be directed from the high-pressure part to the low-pressure part.

Abstract: A distillation apparatus includes a first distillation column and one or more second distillation columns. A higher-pressure part of the first distillation column includes at least part of a rectifying section, and performs gas-liquid contact at a relatively high pressure. A lower pressure-part of the first distillation column includes at least part of a stripping section and performs gas-liquid contact at a relatively low pressure. A vapor line, which includes a pressurizing means, directs a vapor discharged from a column top of the lower-pressure part to a column bottom of the higher-pressure part. A liquid line directs a liquid discharged from the column bottom of the higher-pressure part to the column top of the lower pressure part. Corresponding heat exchange structures transfer heat in both directions between the rectifying section of the first distillation column and at least one second distillation column.

Abstract: In a heat integrated distillation column (HIDiC), the product purity can be stably maintained against various disturbances. Provided is a method for controlling a distillation apparatus, which includes a high-pressure part including the whole or a part of a rectifying section and performing gas-liquid contact at a relatively high pressure; a low-pressure part including the whole or a part of a stripping section and performing gas-liquid contact at a relatively low pressure; a line for directing overhead vapor of the low-pressure part to a column bottom of the high-pressure part; a line for directing a column bottom liquid of the high-pressure part to a column top of the low-pressure part; and a heat exchange structure for transferring heat from the rectifying section to the stripping section, wherein the method includes controlling a flow rate of the column bottom liquid to be directed from the high-pressure part to the low-pressure part.

Abstract: The present invention provides a method for operating a stripper that is provided for a separating process in an aromatic component processing apparatus in which the stripper separates a component that is lighter than an aromatic component from the aromatic component via a distillation operation. In the method, using a HIDiC as the stripper, the pressure of the column top of rectifying section (201) of the HIDiC is determined, and the pressure of the column top of stripping section (202) of the HIDiC is set to be lower than the pressure of the column top of rectifying section (201).

Abstract: A distillation apparatus of the present invention includes high-pressure column 1 corresponding to a region above a heat exchanging section located at a lowermost part of a region including a trayed section or a packed bed section, which is used as a rectifying section; and low-pressure column 2 that is located above as seen from high-pressure column 1, which integrates a region including a trayed section or a packed bed section which is used as a stripping section, with rectifying section corresponding portion 2g that corresponds to a region locating below the heat exchanging section located at the lowermost part in the rectifying section. Rectifying section corresponding portion 2g is located on top 2c of the stripping section in low-pressure column 2 so that rectifying section corresponding portion 2g continues to the stripping section.