Abstract:
PROBLEM TO BE SOLVED: To provide a nitrogen oxide/sulfur oxide removal system capable of removing both of nitrogen oxide and sulfur oxide included in gas as a treatment target, a nitrogen oxide/sulfur oxide removal method and a carbon dioxide recovery system.SOLUTION: A nitrogen oxide/sulfur oxide removal system includes a nitrogen oxide/sulfur oxide recovery tower for making gas including nitrogen oxide and sulfur oxide and an absorbing solution contact with each other to cause the absorbing solution to absorb the nitrogen oxide and the sulfur oxide in the gas. The system further includes a nitrogen component removal tank for removing a nitrogen component in the absorbing solution discharged from the nitrogen oxide/sulfur oxide recovery tower. The system further includes a sulfur component removal tank for removing a sulfur component in the absorbing solution discharged from the nitrogen component removal tank.
Abstract:
PROBLEM TO BE SOLVED: To provide a carbon dioxide separation and recovery system that measures an amount of heat supplied to an absorption liquid in a regeneration tower from a reboiler heating medium.SOLUTION: The heating medium discharged from a reboiler 6 is cooled by a cooler 120 and fully condensed. A device 100 for measuring the amount of reboiler input heat obtains the amount of heat that is supplied to the absorption liquid in the regeneration tower 5 from the heating medium by subtracting, from an amount of heat that is retained by the heating medium supplied to the reboiler 6, an amount of heat that is retained by the heating medium cooled by the cooler 120 and an amount of heat that is removed from the heating medium in the cooler 120.
Abstract:
PROBLEM TO BE SOLVED: To provide a purification device that efficiently removes impurities accumulated in an absorbing liquid used for a system for recovering the carbon dioxide in a combustion exhaust gas, and to provide a carbon dioxide recovery system using the same. SOLUTION: The carbon dioxide recovery system includes: an absorbing tower 103 for making the absorbing liquid absorb the carbon dioxide contained in the combustion exhaust gas; a regenerating tower 105 for regenerating the absorbing liquid by removing the carbon dioxide from the absorbing liquid discharged from the absorbing tower; and a purification device 10 for purifying the absorbing liquid by removing anions existing in the absorbing liquid from the absorbing liquid discharged from the regenerating tower. The purification device includes a support body comprising a metal mesh or a porous polymer membrane, wherein a compound layer including a barium compound is formed thereon, and makes the anions absorbing liquid pass through the absorbing liquid to react the anions with barium ions and fixes to the compound layer, and provides a purified absorbing liquid to the absorbing tower. COPYRIGHT: (C)2011,JPO&INPIT
Abstract:
PROBLEM TO BE SOLVED: To provide a carbon dioxide separating and recovery apparatus which prevents the deterioration in carbon dioxide absorbing performance of an absorption liquid. SOLUTION: The absorption liquid 104a that absorbs oxygen with a carbon dioxide in an absorption tower 103 is supplied to oxygen collecting parts 13 and 14. The oxygen collecting parts 13 and 14 contains argentine, and collects the oxygen in the absorption liquid 104a to remove the oxygen from the absorption liquid 104a. When the absorption liquid 104a is supplied to one of two oxygen collecting parts 13 and 14, a regeneration part 15 separates and recovers the oxygen which is collected to the other oxygen collecting part to regenerate the other oxygen collecting part. A continuous operation becomes possible by using two oxygen collecting parts 13 and 14 switched. COPYRIGHT: (C)2011,JPO&INPIT
Abstract:
PROBLEM TO BE SOLVED: To provide a system for recovering carbon dioxide capable of preventing the carbon-dioxide absorption capacity of its liquid absorbent from decreasing.SOLUTION: The system 1 for recovering carbon dioxide includes an absorption column 3 wherein carbon dioxide is absorbed by a liquid absorbent, a regeneration column 5 wherein the liquid absorbent supplied from the absorption column 3 is regenerated, and a condenser 17 that condenses and separates moisture present in a gas discharged from the reactivation column 5, in which system 1, the ratio of moisture present in the liquid absorbent circulating through the system for recovering carbon dioxide is prevented from increasing by controlling the amount of the condensate discharged from the condenser 17 based at least on either of the ratio of moisture in the liquid absorbent and the analysis values of the composition of the liquid absorbent.
Abstract:
PROBLEM TO BE SOLVED: To provide a method and an apparatus for recovering carbon dioxide, wherein energy required for expelling the carbon dioxide from an absorption liquid where the carbon dioxide is absorbed can be reduced. SOLUTION: There are provided the method and the apparatus for recovering the carbon dioxide, wherein a gas containing the carbon dioxide is brought into contact with a chemical absorption liquid to remove the carbon dioxide from the gas, and the CO 2 -rich chemical absorption liquid where the carbon dioxide is absorbed is brought into direct contact with a physical absorption liquid to regenerate the carbon dioxide, and the carbon dioxide is separated from the physical absorption liquid. COPYRIGHT: (C)2010,JPO&INPIT
Abstract:
PROBLEM TO BE SOLVED: To provide a method for evaluating "overall efficiency" indicating the energy supply efficiency of the whole system in power supply systems, for example, a microgrid power system, including natural energy sources such as wind power generation and photovoltaic power generation whose outputs are difficult to control. SOLUTION: The power supply system includes a generator set having both one or more generator equipment whose output can be controlled and one or more generator equipment whose output cannot be controlled and having one or more load so as to supply power with interconnection to or without interconnection to a commercial power system. In the method for evaluating the overall efficiency of the power supply system, at least one among overall efficiency, instantaneous overall efficiency, average overall efficiency, potential overall efficiency, operational efficiency and a supply-demand opportunity loss factor is calculated using predetermined mathematical expressions and the evaluation is performed by the calculated result. COPYRIGHT: (C)2009,JPO&INPIT
Abstract:
PROBLEM TO BE SOLVED: To provide satisfactory cell characteristics while suppressing a gas leakage and securing suitable joining strength under the driving conditions of a high temperature steam electrolytic cell or a solid oxide type fuel battery cell. SOLUTION: The reaction cell such as the high temperature steam electrolytic cell 20 supported by a supporting body 10 with a perforated part 12 formed at the end part 14 of the perforated part 12 comprises: an edge part 32 densely formed of a material having electronic insulating properties and ion conductivity and engaged with the end part 14; an electrolytic membrane 30 provided with an intermediate part 34 integrally molded with the edge part 32; a hydrogen pole 40 provided at the face of the intermediate part 34 on the side facing to the inside 16 of the supporting body 10; and an oxygen pole 50 provided at the face on the side opposite to the hydrogen pole 40 in the intermediate part 34. COPYRIGHT: (C)2009,JPO&INPIT
Abstract:
PROBLEM TO BE SOLVED: To provide an environment-friendly geothermal power generation system not almost discharging global warming gases such as carbon dioxide gas. SOLUTION: In this geothermal power generation system, the thermal energy of geothermal steam is taken out, and collected as electric energy by driving a turbine 7. A non-condensed gas 15 produced from a condenser 9 in which the geothermal steam after the turbine 7 is driven is cooled into a cold and hot water 12 is returned into the ground. COPYRIGHT: (C)2007,JPO&INPIT