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21. 发明专利

JP2004053123A Exhaust gas charging type absorption chiller and heater 审中-公开
公开(公告)号：JP2004053123A
公开(公告)日：2004-02-19
申请号：JP2002210758
申请日：2002-07-19
申请人： Ebara Corp , 株式会社荏原製作所
发明人： INOUE OSAYUKI , ENDO TETSUYA
IPC分类号： F25B15/00 , F25B33/00
CPC分类号： Y02A30/277 , Y02B30/62
摘要： PROBLEM TO BE SOLVED: To provide an exhaust gas charging type absorption chiller and heater having an exhaust gas high temperature regenerator with the usage of a vertical heat transfer tube group with reduced size by smoothing solution circulation. SOLUTION: The solution from an absorber A is guided to the exhaust gas high temperature regenerator GHX through a low temperature heat exchanger X heated side and a high temperature heat exchanger XH heated side by a solution flow passage, and is guided to a low temperature regenerator G through XH heating side. Then, the solution is returned to the A through X heating side. The GHX is provided with the vertical heat transfer pipe group YP in an exhaust gas passage having a rectangle cross section. An air liquid chamber YG is provided on an upper part of the YP so as to cover an opening part of the YP, and a solution supply chamber YL is provided on a lower part of the YP so as to cover the opening part of the YP. A pipe of the solution flow passage connecting the heating side of the XH and the G and a pipe connecting the G and the X heating side are connected by a pipe 3 having a flow rate restricting mechanism (a throttling mechanism) 4. COPYRIGHT: (C)2004,JPO

22. 发明专利

JP2003336928A Absorption and compression type refrigerator 审中-公开
标题翻译：吸收和压缩式制冷机
公开(公告)号：JP2003336928A
公开(公告)日：2003-11-28
申请号：JP2002139645
申请日：2002-05-15
申请人： Ebara Corp , 株式会社荏原製作所
发明人： INOUE OSAYUKI , HASHIMOTO IZUMI , IRIE KIICHI , ENDO TETSUYA , AOYAMA ATSUSHI , UCHIMURA TOMOYUKI , FUKUZUMI YUKIHIRO
IPC分类号： F25B25/02
摘要： PROBLEM TO BE SOLVED: To provide a refrigerator usable also as an air conditioner capable of being economically and efficiently operated by controlling operating states. SOLUTION: This refrigerator comprises an absorption type refrigerator 1 having a regenerator G, a condenser C, an absorber A, and an evaporator E and a plurality of compression type refrigerating machines 2 to 5 having one or more of user side heat exchangers Ec, depressurizing mechanisms V, compressors M, first heat source side heat exchangers C1 for exchanging heat between a first heat source fluid and refrigerant, and second heat source side heat exchangers C2 connected in series and/or parallel with the first heat source side heat exchangers C1. The evaporator E of the absorbing refrigerating machine 1 exchanges heat with the second heat source side heat exchangers C2 of the compression refrigerating machines 2 to 5, and the heat exchangers C2 of the refrigerating machines 2 to 5 and the evaporator E of the refrigerating machine 1 are connected to each other in series and/or parallel with the flow of heat transfer medium. The refrigerating machine 1 comprises a means for detecting the temperature of the heat exchanger E or an equivalent physical amount, and may comprises a means for controlling the temperature or the corresponding physical value within a specified range. COPYRIGHT: (C)2004,JPO
摘要翻译：要解决的问题：提供一种也可以通过控制操作状态而经济有效地操作的空调机。解决方案：该冰箱包括具有再生器G，冷凝器C，吸收器A和蒸发器E的吸收式冰箱1和具有一个或多个用户侧热交换器的多个压缩式制冷机2至5 Ec，减压机构V，压缩机M，用于在第一热源流体和制冷剂之间进行热交换的第一热源侧热交换器C1和与第一热源侧热量串联连接和/或并联连接的第二热源侧热交换器C2 交换机C1。吸收式制冷机1的蒸发器E与压缩式制冷机2〜5的第二热源侧热交换器C2，制冷机2〜5的热交换器C2和制冷机1的蒸发器E进行热交换与传热介质的流动串联和/或并联连接。制冷机1包括用于检测热交换器E的温度或等效物理量的装置，并且可以包括用于在特定范围内控制温度或相应的物理值的装置。版权所有（C）2004，JPO

23. 发明专利

JP2003326272A Electric regenerative demineralizer 有权
标题翻译：电再生脱氧剂
公开(公告)号：JP2003326272A
公开(公告)日：2003-11-18
申请号：JP2002136605
申请日：2002-05-13
申请人： Ebara Corp , 株式会社荏原製作所
发明人： INOUE OSAYUKI , AOYAMA ATSUSHI
IPC分类号： B01D61/48 , B01J47/12 , C02F1/469
摘要： PROBLEM TO BE SOLVED: To provide an electric regenerative demineralizer which has a high removal perfor mance to a weak negative ion component and is relatively small-sized. SOLUTION: The electric regenerative demineralizer is provided with a cathode chamber 2 having a cathode 1, an anode chamber 4 having an anode 3, one or more concentration chambers 8 constituted by disposing cation exchange membranes 6 on the anode 3 side and the anion exchange membranes 5 on the cathode 1 side between both electrodes, and the desalting chambers 7 in which a plurality of desalting chambers 7 among the following desalting chambers (a)-(e) are disposed and the ion exchange membranes are packed in the inside disposed with the following (a)-(e): (a) the desalting chamber 7 in which the cation exchange membrane 6 is disposed on the cathode 1 side and the anion exchange membrane 5 is disposed on the anode 3 side, (b) the desalting chamber 7 in which the cation exchange membranes 6 are disposed on both sides, c the desalting chamber 7 in which the anion exchange membranes 5 are disposed on both sides, (d) the desalting chamber 7 in which the cation exchange membrane 6 is disposed on the cathode 1 side and a bipolar membrane is disposed on the anode 3 side, and (e) the desalting chamber 7 in which the bipolar membrane is disposed on the cathode 1 side and the anion exchange membrane 5 is disposed on the anode 3 side. The electric regenerative demineralizer has the single desalting chamber 7 in which the concentration chambers 8, the anode chambers 4 or the cathode chambers 2 are disposed on both sides and a desalting chamber 7 group in which the desalting chambers 7 are plurality arranged in the adjacent relation respectively by one or more without interposing the concentration chamber 8. Therein, the outlets of the desalting chamber 7 group are connected with the inlet of the single desalting chamber 7 or the outlet of the single desalting chamber 7 is connected with the inlets of the desalting chamber 7 group. COPYRIGHT: (C)2004,JPO
摘要翻译：要解决的问题：提供一种对弱负离子组分具有高去除性能并且尺寸相对较小的电再生脱盐装置。解决方案：电再生脱盐装置设置有阴极室2，阳极室4具有阳极3，一个或多个浓度室8，其通过在阳极3侧设置阳离子交换膜6和在两个电极之间的阴极1侧的阴离子交换膜5和其中设置以下脱盐室（a） - （e）中的多个脱盐室7的脱盐室7和离子交换膜包装在内部（a） - （e）：（a）阳极交换膜6设置在阴极1侧并且阴离子交换膜5设置在阳极3侧的脱盐室7，（b）其中阳离子交换膜6设置在两侧的脱盐室7，其中阴离子交换膜5设置在两侧的脱盐室7，（d）阳离子交换膜6为其的脱盐室7 迪在阳极3侧设置双极性膜，（e）在阴极1侧设置双极性膜的脱盐室7和阴极交换膜5配置在阳极3上侧。电再生脱盐装置具有单个脱盐室7，其中浓缩室8，阳极室4或阴极室2设置在两侧，并且脱盐室7组中脱盐室7以相邻的关系多个排列分别通过一个或多个而不插入浓缩室8.其中，脱盐室7组的出口与单个脱盐室7的入口连接，或者单个脱盐室7的出口与脱盐入口连接第7组。版权所有（C）2004，JPO

24. 发明专利

JP2003326270A Electric regenerative demineralizer 有权
标题翻译：电再生脱氧剂
公开(公告)号：JP2003326270A
公开(公告)日：2003-11-18
申请号：JP2002136603
申请日：2002-05-13
申请人： Ebara Corp , 株式会社荏原製作所
发明人： INOUE OSAYUKI , AOYAMA ATSUSHI
IPC分类号： B01D61/48 , B01J47/12 , C02F1/469
CPC分类号： Y02A20/134
摘要： PROBLEM TO BE SOLVED: To provide an electric regenerative demineralizer which has an improved removal performance to a weak negative ion component and can satisfactorily remove the weak negative ion component. SOLUTION: This electric regenerative demineralizer has a cathode chamber 2 and an anode chamber 4, cation exchange membranes 6 and anion exchange membranes 5 are disposed between both electrode chambers, desalting chambers 7 and concentration chambers 8 are formed by using the ion exchange membranes and chamber frames. The desalting chambers 7 are respectively divided into three small desalting chambers 71, 72, 73 in the flow direction of electricity by two sheets of the ion exchange membranes, ion exchangers are packed at least in the three small desalting chambers of the above desalting changers 7 and the three small desalting chambers are constituted in such a manner that outlet water of the small desalting chambers 71 is supplied to the inlets of the small desalting chambers 72 and outlet water of the small desalting chambers 72 is supplied to the inlets of the small desalting chambers 73. In the desalting chambers, the anion exchange membranes 5 are disposed on the anode sides and the cation exchange membranes 6 are disposed on the cathode sides and a plurality of sheets of the ion exchange membranes dividing the desalting chambers 7 are preferably single membranes or bipolar membranes of the cation exchange membranes 6 or the anion exchange membranes 5. COPYRIGHT: (C)2004,JPO
摘要翻译：解决的问题：提供一种对弱负离子成分具有改善的去除性能并可令人满意地除去弱负离子组分的电再生式脱盐剂。解决方案：该电再生脱盐装置具有阴极室2和阳极室4，阳离子交换膜6和阴离子交换膜5设置在两个电极室之间，脱盐室7和浓缩室8通过使用离子交换膜和腔室框架。脱盐室7通过两片离子交换膜在电流的流动方向分别分成三个小的脱盐室71,72,73，离子交换器至少装填在上述脱盐清洗器7的三个小的脱盐室中三个小型脱盐室由小型脱盐室72的入口供给小型脱盐室71的出口水，小型脱盐室72的出水被供给到小型脱盐室71的入口处。在脱盐室中，阴极交换膜5设置在阳极侧，阳离子交换膜6设置在阴极侧，分离脱盐室7的多个离子交换膜片优选为单膜或阳离子交换膜6或阴离子交换膜5的双极膜。版权所有（C）2004，JPO

25. 发明专利

JP2003322427A Exhaust heat input type single-double effective absorbing cold water heater 有权
标题翻译：排气式输入式单双吸收式冷水加热器
公开(公告)号：JP2003322427A
公开(公告)日：2003-11-14
申请号：JP2002128003
申请日：2002-04-30
申请人： Ebara Corp , 株式会社荏原製作所
发明人： INOUE OSAYUKI , ENDO TETSUYA
IPC分类号： F25B15/00
CPC分类号： Y02A30/277 , Y02B30/62
摘要： PROBLEM TO BE SOLVED: To provide an exhaust heat input type single-double effective absorbing cold water heater for forming a hot water evaporator for dispensing with an expensive water heater, and easily switching cooling and heating.
SOLUTION: This exhaust heat input type single-double effective absorbing cold water heater has an exhaust heat high temperature regenerator GH, an exhaust heat low temperature regenerator GR, a low temperature regenerator G, a condenser C, an absorber A, an evaporator E, a solution passage and a refrigerant passage for connecting these apparatuses, and is constituted so as to be capable of switching a cooling mode and a heating mode, and is provided with a pipe 22 having a valve V1 for operating at heating mode time for introducing refrigerant vapor to the E or the A from at least one apparatus in a pressure level apparatus of the E, and a pipe 17 having a valve V2 for operating at heating mode time for introducing a solution to the E from a circulating system of an absorbing solution. A pipe 20 for introducing the refrigerant vapor to the C via the heating side of the G is connected to the GH. A pipe having V3 for connecting a lower part of the E and the A or a pipe connected to the A can be arranged in the E.
COPYRIGHT: (C)2004,JPO
摘要翻译：要解决的问题：提供一种用于形成用于分配昂贵的热水器的热水蒸发器的排气热输入型单双吸收冷热水器，并且容易地切换冷却和加热。
解决方案：该排气热输入式单双吸收冷热水器具有排气高温再生器GH，排气低温再生器GR，低温再生器G，冷凝器C，吸收器A，蒸发器E，用于连接这些装置的溶液通道和制冷剂通道，并且被构造成能够切换冷却模式和加热模式，并且设置有具有用于在加热模式时间操作的阀V1的管22 用于在E的压力级装置中的至少一个装置将制冷剂蒸汽引入E或A，以及管17，其具有用于在加热模式时间操作的阀V2，用于将溶液从循环系统吸收解决方案。用于通过G的加热侧将制冷剂蒸汽引入C的管道20连接到GH。具有用于连接E的下部的V3和与A连接的管的管道可以布置在E.C版权：（C）2004，JPO

26. 发明专利

JP2003307364A Refrigerating equipment combined with absorption type and compression type 有权
标题翻译：与吸收类型和压缩类型组合的制冷设备
公开(公告)号：JP2003307364A
公开(公告)日：2003-10-31
申请号：JP2002111629
申请日：2002-04-15
申请人： Ebara Corp , 株式会社荏原製作所
发明人： INOUE OSAYUKI , HASHIMOTO IZUMI , IRIE KIICHI , ENDO TETSUYA , AOYAMA ATSUSHI , UCHIMURA TOMOYUKI , FUKUZUMI YUKIHIRO
IPC分类号： F25B1/00 , F25B25/02 , F25B27/02
CPC分类号： Y02A30/274
摘要： PROBLEM TO BE SOLVED: To provide refrigerating equipment combined with an absorption type and a compression type and efficiently driving by adjusting the driving state of a compression refrigerating machine according to the state of cooling loads and absorption refrigerating effects.
SOLUTION: This refrigerating equipment is formed by combining the absorption refrigerating machine having an evaporator E exhibiting the refrigerating effect using waste heat as a heat source, with a compression refrigerating machine having one or more compressors Mc, an evaporator Ec exhibiting the refrigerating effect, a first condenser cooling using outside air or cooling water, a second condenser connected to the evaporator E of the absorption refrigerating machine in a heat exchange relation, and, or a supercooling device; and is provided a means adjusting a load to the evaporator E and a temperature sensor detecting the temperature of the evaporator E. The plurality of compression refrigerating machines can be connected to the single absorption refrigerating machine and preferably, each compression refrigerating machine is provided with a means collectively, dividedly, or individually adjusting the load from the second condenser side and/or the supercooling device side to the evaporator E.
COPYRIGHT: (C)2004,JPO
摘要翻译：要解决的问题：通过根据冷却负荷和吸收制冷效果的状态调节压缩式制冷机的驱动状态，提供与吸收式和压缩式结合的制冷装置，并有效地进行驱动。解决方案：该制冷装置通过将具有表现出使用废热的冷却效果的蒸发器E作为热源的吸收式制冷机与具有一个或多个压缩机Mc的压缩式制冷机组合，形成冷藏效应，使用外部空气或冷却水的第一冷凝器冷却，与热交换关系的吸收式制冷机的蒸发器E连接的第二冷凝器，或过冷却装置; 并且设置了调节对蒸发器E的负荷的装置和检测蒸发器E的温度的温度传感器。多个压缩式制冷机可以连接到单个吸收式制冷机，并且优选地，每个压缩式制冷机设置有意味着共同地，分开地或单独地调节从第二冷凝器侧和/或过冷却装置侧到蒸发器E的负载。版权所有（C）2004，JPO

27. 发明专利

JP2003222428A REFRIGERATION UNIT USED IN COGENERATION SYSTEM 审中-公开
公开(公告)号：JP2003222428A
公开(公告)日：2003-08-08
申请号：JP2002021214
申请日：2002-01-30
申请人： EBARA CORP
发明人： INOUE OSAYUKI
IPC分类号： F02G5/04 , F04B49/06 , F25B25/02 , F25B27/02
摘要： PROBLEM TO BE SOLVED: To provide a refrigeration unit capable of adjusting an operation condition of a compression refrigerator in accordance with cooling load and a condition of absorption refrigeration effect and performing economical and efficient operation. SOLUTION: This refrigeration unit used in a cogeneration system is constituted by combining an absorption refrigerator having an evaporator E providing refrigeration effect using exhaust heat as a heat source, a compressor M c , a first condenser Cc1 cooling by outside air or cooling water, and the compression refrigerator having a first condenser Cc2 connected with the evaporator E of the absorption refrigerator and heat exchange relation and an evaporator Ec providing refrigeration effect. Electric power for operating the compressor M c is electricity before it is converted into commercial frequency and electricity generated by a generator or electricity which is not converted into commercial frequency. The refrigeration unit may be provided with a control means for operating the compressor when load for the evaporator Ec cannot be covered with refrigeration effect of the absorption refrigerator. COPYRIGHT: (C)2003,JPO

28. 发明专利

JP2003121021A DOUBLE EFFECT ABSORPTION REFRIGERATING MACHINE 审中-公开
公开(公告)号：JP2003121021A
公开(公告)日：2003-04-23
申请号：JP2001313895
申请日：2001-10-11
申请人： EBARA CORP
发明人： INOUE OSAYUKI
IPC分类号： F25B15/00
摘要： PROBLEM TO BE SOLVED: To provide a double effect absorption refrigerating machine sufficiently recovering heat from a heat source, sufficiently cooling a concentrated solution with a low temperature heat exchanger, and reducing a load to an absorber. SOLUTION: In the double effect absorption refrigerating machine using an outside heat source fluid 5 as a heat source, a passage through which the outside heat source fluid 5 heats and concentrates an absorption solution with a high temperature regenerator GH and is introduced into an exhaust heat recovery heat exchanger XA is installed, and through the solution passage, a dilute solution from an absorber A is introduced into a low temperature heat exchanger XL, and a branch point B1 is installed between an inlet of the dilute solution and an outlet of the low temperature heat exchanger XL, a part of the dilute solution is branched from the branch point B1 , introduced into the high temperature regenerator GH through a side to be heated of the exhaust heat recovery heat exchanger XA, the remaining dilute solution from the branch point B1 is introduced into the low temperature regenerator GL and/or the high temperature regenerator GH. The low temperature heat exchanger XL may be divided into two independent heat exchangers in the branch point B1 inside the heat exchanger, and the remaining dilute solution not branched in the low temperature heat exchanger XL can adopt optional flow of parallel, series, or reverse flow.

29. 发明专利

JP2003062403A Operating method for membrane degasifier 审中-公开
标题翻译：膜分离器的操作方法
公开(公告)号：JP2003062403A
公开(公告)日：2003-03-04
申请号：JP2001254530
申请日：2001-08-24
申请人： Ebara Corp , 株式会社荏原製作所
发明人： INOUE OSAYUKI , AOYAMA ATSUSHI , KAWAMOTO TAKAYOSHI , NAKANISHI OSAMU
IPC分类号： B01D61/36 , B01D19/00 , C02F1/20
摘要： PROBLEM TO BE SOLVED: To provide an operating method for a membrane degasifier capable of preventing a deterioration of a vacuum pump while reducing a pressure in a vapor phase of a deaerating membrane to a pressure of saturated vapor or lower of water to be treated.
SOLUTION: In the operating method for a membrane degasifier having a deaeration membrane module 1, a dry type vacuum pump 3, a vacuum piping 4 for connecting the above 1 and 3, and a gas-feeding means 5 for feeding a gas to the above 4 and removing a dissolved gas in water to be treated, while water 21 to be treated is passed through a liquid phase side 12 of the above 1 and a gas at the vapor phase side 11 of the above 1 is exhausted by the above 3 to carry out the deaeration treatment, the gas is intermittently or continuously fed to the vacuum piping 4 for connecting the above 1 and 3 from the gas-feeding means 5. An amount of gas fed from the above 5 into the above 4 can be determined by a pressure-measuring means 61 mounted to the above 4 or a flow rate measurement means 62 mounted to the above 5.
COPYRIGHT: (C)2003,JPO
摘要翻译：要解决的问题：提供一种能够防止真空泵劣化的膜脱水装置的操作方法，同时将脱气膜的气相中的压力降低至待处理的饱和蒸气或更低的水的压力。解决方案：在具有脱气膜组件1，干式真空泵3，连接上述1和3的真空管4以及用于将气体供给上述的气体供给装置5的膜脱脂器的操作方法中，并且将待处理的水21通过上述1的液相侧12，将上述1的气相侧11的气体排出到上述3，将其除去，进行脱气处理，将气体间歇地或连续地供给到用于从上述气体供给装置5连接上述1和3的真空管道4中。从上述5供给到上述4中的气体量可以由安装到上述4的压力测量装置61或安装在上述5上的流量测量装置62。

30. 发明专利

JP2003001261A Electrically regenerative desalter 审中-公开
标题翻译：电动再生塔
公开(公告)号：JP2003001261A
公开(公告)日：2003-01-07
申请号：JP2001192336
申请日：2001-06-26
申请人： Ebara Corp , 株式会社荏原製作所
发明人： INOUE OSAYUKI , AOYAMA ATSUSHI
IPC分类号： B01D61/46 , B01D61/48 , B01D61/52 , C02F1/42 , C02F1/44 , C02F1/469
CPC分类号： Y02A20/131 , Y02A20/134
摘要： PROBLEM TO BE SOLVED: To provide an electrically regenerative desalter which reduces a supply quantity of pole liquid to the utmost and enhances the recovery rate.
SOLUTION: This electrically regenerative desalter is provided with a cathode chamber 4 having a cathode 3 and an anode chamber 6 having an anode 5. The pole chambers 4, 6 are disposed at least by one chamber respectively and are made to be such a desalting chamber structure that, between the cathode chamber 4 and the anode chamber 6, a cation exchange membrane 8 and an anion exchange membrane 7 are arranged at least alternately in one part, a desalting chamber 9 and a concentration chamber 10 are formed, an ion exchanger is packed at least in the desalting chamber 9, the concentration chamber 10 is arranged adjacently to the pole chambers and the ions in the pole liquid are reduced. Therein, gas-liquid separating means 20 are disposed on the outlet side of the pole chambers, the quantity of the pole liquid which is supplied to the pole chambers is made almost zero, the pole liquid is supplied by the quantity which is decreased by the generation or scattering of air bubbles, the supplied water which is supplied to the pole chambers is one part of inlet water 12 or 14 which is supplied to the desalting chamber 9 or the concentration chamber 10, or one part of the treated water 13 which is desalted.
COPYRIGHT: (C)2003,JPO
摘要翻译：要解决的问题：提供一种电再生脱盐器，其最大限度地减少极性液体的供应量并提高回收率。解决方案：该电再生脱盐器设置有阴极室4和具有阳极5的阳极室6.阳极室4,6至少分别设置一个室，并被制成这样的脱盐室在阳极室4和阳极室6之间，阳离子交换膜8和阴离子交换膜7至少交替配置在一部分的形式，形成脱盐室9和浓缩室10，离子交换器为至少填充在脱盐室9中，浓缩室10与极室相邻设置，极性液体中的离子减少。其中，气液分离装置20设置在极室的出口侧，供给到极室的极性液体的量几乎为零，磁极液体被以气泡的产生或散射，供给到极室的供给水是供给到脱盐室9或浓缩室10的入口水12或14的一部分，或者是处理水13的一部分脱盐

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