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    • 1. 发明专利
    • Method and device for setting charge
    • 用于设置充电的方法和装置
    • JP2005250709A
    • 2005-09-15
    • JP2004058306
    • 2004-03-03
    • Tokyo Gas Co Ltd東京瓦斯株式会社
    • SUZUKI KIWAMUOJI MASASHI
    • G06Q50/06G06Q30/04G06Q30/06G06Q50/00G06F17/60
    • PROBLEM TO BE SOLVED: To provide a charge setting method for averaging monthly payment charge in a predetermined period even when the monthly usage of gas, electricity and water service or the like is different. SOLUTION: In the beginning of a predetermined year starting with a predetermined month, first fixed charge to be paid monthly in one year of the predetermined year is calculated based on at least the total of the payment charge of the previous year of the predetermined year. After the lapse of the predetermined number of months from the beginning of the predetermined year, the fixed charge to be paid each monthly until the end of the predetermined year after the lapse of the predetermined number of months is updated from the first fixed charge to the second fixed charge based on at least one of a difference between the actual usage of every month or charge corresponding to that until the lapse of the predetermined number of months and the actual usage of every month or charge corresponding to that since the start of the previous year until the lapse of the predetermined number of months or predetermined predicted information. After the end of the predetermined year, a difference between the total of charge corresponding to the actual usage of every month in the predetermined year and the total of the charge paid every month in the predetermined year based on the first fixed charge and the second fixed charge is calculated. COPYRIGHT: (C)2005,JPO&NCIPI
    • 要解决的问题:提供一种用于在预定时段内平均每月支付费用的费用设定方法,即使当天然气,电力和水务等的每月使用不同时。

      解决方案:在从预定月份开始的预定年度开始时,基于预定年份的一年中的每月支付的第一固定费用,至少基于 预定年 在从预定年度开始经过预定月数之后,每个月直到预定月份之后的预定年度结束时支付的固定费用从第一固定费用更新为 第二固定费用基于每个月的实际使用量之间的差异或对应于直到预定月数的经过为止的费用和每个月的实际使用或与之前的开始相对应的费用中的至少一个 年,直到预定月数的经过或预定的预测信息。 在预定年度结束之后,基于第一固定费用和第二固定费用,在预定年份中对应于每月的实际使用量的总费用与预定年份中的每月支付的费用总额之间的差额 计算费用。 版权所有(C)2005,JPO&NCIPI

    • 2. 发明专利
    • PHOSPHORIC ACID FUEL CELL
    • JPH10172588A
    • 1998-06-26
    • JP33341896
    • 1996-12-13
    • TOKYO GAS CO LTD
    • ADACHI HARUHIKOITO TOSHIYUKIOJI MASASHI
    • C01B3/16H01M8/02H01M8/04
    • PROBLEM TO BE SOLVED: To prevent increase in concentration of CO in a returning part, increase hydrogen concentration to prevent voltage drop, and enhance the durability of a cell by installing a second shift converter in the returning part of an anode side gas flow path communicating with an anode outlet from an anode inlet constituted as a meandering flow path having the returning part. SOLUTION: An anode side flow path A of a cell 1 of a phosphoric acid fuel cell is connected to an inlet 2a of a first shift converter 2, and an outlet 2b is connected to an anode 1a of the cell 1. The cell 1 is connected to an inlet 4a of a meandering flow path 4 which is a returning part of the anode side flow path A, an outlet 4b of the meandering flow path 4 is connected to the cell 1 through an inlet 3a and an outlet 3b of a second shift converter 3, and communicated with an anode outlet 1b. By the action of the second shift converter 3, the concentration of CO is decreased, and voltage drop caused by CO poisoning of a catalyst is prevented.
    • 3. 发明专利
    • FUEL CELL POWER GENERATING DEVICE
    • JPH06150957A
    • 1994-05-31
    • JP29831592
    • 1992-11-09
    • TOKYO GAS CO LTD
    • URATA TATSUOOJI MASASHIIKEDA GENICHI
    • H01M8/04H01M8/06
    • PURPOSE:To effectively utilize heat of blow-down water by connecting the blow-down water circuit of a steam generator and a fuel gas circuit to a boosting mixer, and connecting the mixer circuit of the boosting mixer to a process steam circuit. CONSTITUTION:A blow-down water circuit L1 of blow-down water E is connected to a boosting mixer 7, and a fuel gas circuit L2, of fuel gas D is connected to the boosting mixer 7. The mixed gas circuit L3 of the boosting mixer 7 is connected to a process steam circuit L4 feeding the process steam C from a steam generator 5 to a fuel reformer 6. The boosting mixer 7 is constituted of an ejector. When the high-temperature, high-pressure blow-down water E is injected, the blow-down water E is diffused, decompressed, and converted into the vapor phase, and the fuel gas D is sucked. The mixed gas F mixed and boosted with the fuel gas D and moisture is fed to the fuel reformer 6 together with the steam C. The high-temperature blow-down water can be utilized without being discarded, and the power generating efficiency and high- temperature heat recovery percentage can be improved.
    • 4. 发明专利
    • FUEL CELL POWER GENERATING DEVICE
    • JPH06150956A
    • 1994-05-31
    • JP29830892
    • 1992-11-09
    • TOKYO GAS CO LTD
    • URATA TATSUOOJI MASASHIIKEDA GENICHI
    • H01M8/04H01M8/06
    • PURPOSE:To concurrently attain blow down and improve the power generating efficiency and high-temperature heat recovery percentage by connecting the blow-down water circuit of a steam generator and a fuel gas circuit to a boosting mixer, and connecting a mixer circuit to a fuel reformer CONSTITUTION:A blow-down water circuit L1 of blow-down water E of a steam generator 5 is connected to a boosting mixer 7, and a fuel gas circuit L2 of fuel gas is connected to the boosting mixer 7. A mixed gas circuit L3 of the boosting mixer 7 is connected to a fuel reformer 6. The boosting mixer 7 is constituted of an ejector. When the high-temperature, high-pressure blow-down water E is injected, the blow-down water E is diffused, decompressed, and converted into the vapor phase, and the fuel gas D is sucked. The fuel gas D and the moisture are mixed and boosted into the high-temperature mixed gas F and fed to the fuel reformer 6. Blow down is concurrently attained in a fuel cell power generating device, the heat quantity lost by blow down in the past is recovered as the high-temperature heat, and the power generating efficiency and high-temperature heat recovery percentage can be improved.
    • 5. 发明专利
    • Gas flow rate detection device
    • JP2004125634A
    • 2004-04-22
    • JP2002290601
    • 2002-10-03
    • Tokyo Gas Co Ltd東京瓦斯株式会社
    • SUZUKI KIWAMUOJI MASASHI
    • G01F3/22
    • PROBLEM TO BE SOLVED: To provide a gas flow rate detection device (a gas flow rate detection adapter) capable of obtaining a flow rate pulse according to a prescribed gas flow rate by installing the gas flow rate detection device to an existing membrane-type gas meter (a microcomputer gas meter). SOLUTION: This gas flow rate detection device 50 incorporates a magnetic sensor 51 and a signal processing part 52 inside a non-magnetic case. The gas flow rate detection device 50 is installed onto the front face or the upper face of the membrane-type gas meter 30 by bonding or the like. The magnetic sensor 51 detects a change of a magnetic field accompanying movement while drawing a loop-like track K interlockingly with movement of a membrane inside a measurement chamber, of a permanent magnet 8 fixed to a toggle inside the membrane-type gas meter 30. The signal processing part 52 generates and outputs the flow rate pulse on the basis of detection output of the magnetic sensor 51. Without changing the existing membrane-type gas meter for a gas meter with a flow rate pulse output function, the membrane-type gas meter can be made to deal with a system for remote meter reading, remote monitoring, remote management or the like. COPYRIGHT: (C)2004,JPO
    • 8. 发明专利
    • Exhaust heat utilizing device and control method
    • 排气加热装置及其控制方法
    • JP2006144582A
    • 2006-06-08
    • JP2004332657
    • 2004-11-17
    • Tokyo Gas Co Ltd東京瓦斯株式会社
    • IKO MASANORIOJI MASASHIOSAKABE NAOKI
    • F02G5/04H01M8/00
    • Y02E20/14Y02T10/166
    • PROBLEM TO BE SOLVED: To provide an exhaust heat utilizing device and a control method, wherein when the amount of exhaust heat generated in an exhaust heat generating side (primary side) is large with respect to heat demand of an exhaust heat utilizing side (secondary side) in an exhaust heat utilizing device such as a cogeneration system and the capacity of an exhaust heat utilizing heat exchanger for thermally coupling the exhaust heat generating side (primary side) and the exhaust heat utilizing side (secondary side) has an allowance, the allowance leads to economization of energy (energy savings). SOLUTION: The device has an exhaust heat utilizing heat exchanger (3) for thermally communicating between the exhaust heat generating side (primary side) and the exhaust heat utilizing side (secondary side). An exhaust heat circulating line (L1) on an exhaust heat generating side consists of a line by way of the exhaust heat utilizing heat exchanger (3) and a bypass line (Lb) for bypassing the exhaust heat utilizing heat exchanger (3). A heat medium circulating means (secondary side pump 5) is provided to the exhaust heat utilizing side. When a flow rate of exhaust heat fluid flowing through the bypass line exceeds a prescribed value, a circulation flow rate of the heat medium circulating means on the exhaust heat utilizing side (secondary side) is controlled to be reduced. COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供排气热利用装置和控制方法,其中当排气发热侧(初级侧)产生的排气热量相对于利用排气热的热量的需求量大时 在排气热利用装置如热电联产系统中的排气热侧换热器侧(二次侧)和排气发热侧(一次侧)和废热利用侧(二次侧)的热耦合的排气热利用热交换器的容量具有 津贴,津贴导致能源节约(节能)。 解决方案:该装置具有用于在排气发热侧(初级侧)和排气热利用侧(次级侧)之间热连通的排气热利用热交换器(3)。 废热发生侧的排气热循环管线(L1)由排气热利用热交换器(3)的生产线和用于旁通排气热利用热交换器(3)的旁通管线(Lb)组成。 在排气热利用侧设置有热介质循环装置(二次侧泵5)。 当流过旁通管路的废热流体的流量超过规定值时,可以控制排气热利用侧(二次侧)的热介质循环机构的循环流量的降低。 版权所有(C)2006,JPO&NCIPI
    • 9. 发明专利
    • CARBON DIOXIDE DEAERATPR FOR FUEL CELL
    • JPH06140069A
    • 1994-05-20
    • JP28978692
    • 1992-10-28
    • TOKYO GAS CO LTD
    • URATA TATSUOOJI MASASHIIKEDA GENICHI
    • H01M8/04H01M8/06
    • PURPOSE:To reduce a carbon dioxide quantity in recovery water by partitioning the inside of a moisture absorbing tower into two chambers by means to prevent bubbling air from being mixed with exhaust gas, and arranging an exhaust gas introducing port and a heat exchanger in one chamber and a bubbling air delivering port in the other chamber. CONSTITUTION:The inside of a moisture recovery tower 20 is partitioned into an upper chamber 22 and a lower chamber 23 by a water sealing film 21 being a mixing preventive means, and an exhaust gas pipe 24 is opened in the side bottom part of the upper chamber 22, and above it, a water cooling type heat exchanger 25 is arranged protrusively inside, and an air exhaust cylinder 26 is arranged protrusively in one corner of an upper wall. A feed air pipe 28 of a blower 27 is arranged protrusively in the lower part of the lower chamber 23, and a water discharge port 29 is arranged in one corner of the bottom wall, and an air exhaust pipe 30 is erected on the top wall, and this upper end part 31 is opened inside the air exhaust cylinder 26. In this way, combustion exhaust gas E and air electrode offgas F are sent to the upper chamber 22, and water condensed by the heat exchanger 25 is stored in the bottom part of the lower chamber 23 as recovery water G. Next, this water G is bubbled by air bubbles (b) from the blower 27, and carbon dioxide is deaerated, and is discharged from the air exhaust cylinder 26.
    • 10. 发明专利
    • FUEL CELL POWER GENERATING DEVICE
    • JPH06140059A
    • 1994-05-20
    • JP28978192
    • 1992-10-28
    • TOKYO GAS CO LTD
    • URATA TATSUOOJI MASASHIIKEDA GENICHI
    • H01M8/04
    • PURPOSE:To reduce a load on a cooling tower, and obtain high temperature recovery water by connecting an exhaust gas pipe of a boiler added to a heat utilizing equipment formed by using high temperature water from a fuel cell to a moisture recovery tower, and connecting a recovery water pipe to the fuel cell. CONSTITUTION:High temperature water C of a fuel cell 1 is supplied to a heat utilizing equipment 4, and a supply circuit from a boiler 5 is connected to the circuit L1. Exhaust gas E of the boiler 5 enters a moisture recovery tower 6, and recovery water F of the tower 6 is connected to the fuel cell 1. Cooling water G of a heat exchanger 7 of the tower 6 is circulated to a coolling tower 9. The exhaust gas E of the boiler 5 is stored in the bottom part as the recovery water F after moisture is condensed by the heat exchanger 7 in the tower 6, and is sent to the fuel cell 1. At this time, as for the exhaust gas E, since an air ratio is low and a dew point is high, a temperature at which the coolling water G goes in and out of the heat exchanger 7 is allowed to be high. Thereby, since a load on the cooling tower can be reduced, high temperature recovery water can be obtained, so that a use can be increased.