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    • 1. 发明专利
    • Control device and control method for absorption refrigerating device
    • 用于吸收制冷装置的控制装置和控制方法
    • JP2007187417A
    • 2007-07-26
    • JP2006007400
    • 2006-01-16
    • Kawasaki Heavy Ind LtdKawasaki Thermal Engineering Co Ltd川崎重工業株式会社川重冷熱工業株式会社
    • MORI YOSHINOBUHASHIMOTO MASARUMURAKAMI SHOJIHIROMASA KAZUSHIHIRAI AKIRATAKAHARA TAKAHARUOTA MASUOMI
    • F25B15/00
    • Y02A30/277Y02B30/62
    • PROBLEM TO BE SOLVED: To provide a control device for an absorption refrigerating device capable of attaining energy saving in addition to maintaining high temperature controllability.
      SOLUTION: A control means 55 switchingly controls to carry out combustion and to stop combustion at a regenerator 5 based on an outlet temperature T
      CHOUT , a combustion start temperature T
      ON SP and a combustion stop temperature T
      OFF SP . Further in carrying out combustion, the control means 55 switchingly controls high combustion and low combustion to bring the outlet temperature T
      CHOUT close a target temperature TO. The control means 55 further acquires a load state from the time ratio of the combustion state and corrects the combustion start temperature T
      ON SP , the combustion stop temperature T
      OFF SP and the target temperature TO so that the time of the combustion stop state and low combustion state becomes long only in a medium and low load state.
      COPYRIGHT: (C)2007,JPO&INPIT
    • 解决的问题:提供除了保持高温可控性之外,能够实现节能的吸收式制冷装置的控制装置。 解决方案:控制装置55基于出口温度T CHOUT 切换控制以进行燃烧并停止在再生器5处的燃烧,燃烧开始温度T ON SP < SB>和燃烧停止温度T OFF SP 。 此外,在进行燃烧时,控制装置55切换地控制高燃烧和低燃烧,使出口温度T CHOUT 接近目标温度TO。 控制装置55还根据燃烧状态的时间比例来获取负载状态,并且将燃烧开始温度T ON SP ,燃烧停止温度T OFF SP 和 目标温度TO,使得燃烧停止状态和低燃烧状态的时间仅在中等和低负载状态下变长。 版权所有(C)2007,JPO&INPIT
    • 2. 发明专利
    • Method and device for controlling switching of set number of absorption chiller/heater
    • 用于控制吸烟机/加热器组数量切换的方法和装置
    • JP2010243044A
    • 2010-10-28
    • JP2009091370
    • 2009-04-03
    • Kawasaki Thermal Engineering Co Ltd川重冷熱工業株式会社
    • HIRAI AKIRATAKAHARA TAKAHARUKUMAMOTO MIKIOYOSHIOKA TETSUJIMURAKAMI SHOJIMORI YOSHINOBUHASHIMOTO MASARU
    • F24F11/02F25B15/00
    • Y02A30/277Y02B30/62
    • PROBLEM TO BE SOLVED: To improve the accuracy of load estimating calculation by estimating a necessary cooled/heated water flow rate based on the relationship between a combustion amount and a cooled/heated water temperature without installing a sensor for measuring the flow rate. SOLUTION: A number switching control device is composed of individual control devices 31, 32, 33 for controlling respective absorption chiller/heaters and a number control device 35 for outputting start/stop commands to the individual control devices. The number control device determines the number of operating absorption chiller/heaters suitable for a load condition based on cooled/heated water inlet/outlet temperatures and combustion ratios transmitted from the individual control devices, and transmits the start/stop commands to the individual control devices. The individual control devices determine fuel input amounts so that the cooled/heated water outlet temperatures of the absorption chiller/heaters become temperatures set beforehand, and carries out the inputting/blocking of fuel to the absorption chiller/heaters according to the start/stop commands from the number control device. COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:为了通过基于燃烧量和冷却/加热水温之间的关系估计必要的冷却/加热水流量来提高负荷估计计算的精度,而不安装用于测量流量的传感器 。 解决方案:数字切换控制装置由用于控制各个吸收式制冷机/加热器的单独的控制装置31,32,33和用于向各个控制装置输出启动/停止命令的数字控制装置35组成。 数字控制装置基于从各个控制装置发送的冷却/加热的水入口/出口温度和燃烧比确定适合于负载条件的操作的吸收式制冷机/加热器的数量,并将启动/停止命令发送到各个控制装置 。 单独的控制装置确定燃料输入量,使得吸收式制冷机/加热器的冷却/加热水出口温度预先设定为温度,并且根据启动/停止命令对吸收式制冷机/加热器执行燃料的输入/阻断 从号码控制装置。 版权所有(C)2011,JPO&INPIT
    • 3. 发明专利
    • Water supply control method and water supply control device of boiler
    • 锅炉供水控制方法及供水控制装置
    • JP2013228147A
    • 2013-11-07
    • JP2012100694
    • 2012-04-26
    • Kawasaki Thermal Engineering Co Ltd川重冷熱工業株式会社
    • TAKAHARA TAKAHARUHAMAZAKI HIROBUMIISHII YOHEIMURATA TETSUHIKOHASHIMOTO MASARUAKIYAMA HAYATA
    • F22D5/18
    • PROBLEM TO BE SOLVED: To provide a water supply control method and a water supply control device of a boiler capable of being easily applied even to an existing boiler since any new control equipment is not added, and controlling the water level fluctuation of the boiler in a low load zone.SOLUTION: A water supply control device of a boiler includes a water supply flow rate calculation unit 10, a water supply pump rotation number calculation unit 20, and a water supply operation amount calculation unit 30. The water supply flow rate calculation unit 10 calculates a water supply flow rate from deviation between a water level set value and a water level measurement value. The water supply pump rotation number calculation unit 20 calculates the number of rotation of a water supply pump based on the calculated water supply flow rate and a boiler pressure measurement value. The water supply operation amount calculation unit 30 calculates a water supply operation amount from the calculated number of rotation of the water supply pump, and controls the number of rotation of the water supply pump by the operation amount.
    • 要解决的问题:提供一种能够容易地应用于现有锅炉的锅炉的供水控制方法和供水控制装置,因为不添加任何新的控制设备,并且控制锅炉的水位波动 低负荷区域。解决方案:锅炉的供水控制装置包括供水流量计算单元10,供水泵转数计算单元20和供水运行量计算单元30.供水流量 计算单元10从水位设定值和水位测量值之间的偏差来计算供水流量。 供水泵转数计算单元20基于计算的供水流量和锅炉压力测量值来计算供水泵的旋转次数。 供水运行量计算单元30根据计算出的供水泵的转数来计算供水运行量,并且通过运转量来控制供水泵的转数。
    • 4. 发明专利
    • Method of operating absorption water chiller/heater
    • 吸水式冷水机/加热器的操作方法
    • JP2010243014A
    • 2010-10-28
    • JP2009090531
    • 2009-04-02
    • Kawasaki Thermal Engineering Co Ltd川重冷熱工業株式会社
    • HASHIMOTO MASARUMORI YOSHINOBUMURAKAMI SHOJIHIRAI AKIRAOTA MASUOMITAKAHARA TAKAHARU
    • F25B15/00
    • Y02A30/277Y02B30/62
    • PROBLEM TO BE SOLVED: To prevent crystallization of an absorbing solution while using cooling water at low temperature and thus, appropriately obtain energy saving effects. SOLUTION: Set temperature of cooling water for cooling an absorber 16 and a condenser 13 is determined based on temperature allowance which is a difference between crystal temperature in absorber inlet absorbing solution concentration (temperature to achieve crystallization of the absorbing solution having the concentration) and actual absorber inlet absorbing solution temperature (at each time point during operation). The absorber inlet absorbing solution concentration may be calculated from refrigerant temperature in the evaporator 15, absorber outlet absorbing solution temperature, absorbing solution temperature in a low-temperature regenerator 11 and refrigerant condensation temperature in the condenser 13. COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:为了防止在低温下使用冷却水时吸收溶液的结晶,从而适当地获得节能效果。 解决方案:用于冷却吸收器16和冷凝器13的冷却水的设定温度是根据作为吸收剂入口吸收液浓度的结晶温度(达到浓度的吸收液的结晶温度 )和实际的吸收剂入口吸收溶液温度(在操作期间的每个时间点)。 吸收剂入口吸收液浓度可以从蒸发器15中的制冷剂温度,吸收器出口吸收溶液温度,低温再生器11中的吸收溶液温度和冷凝器13中的制冷剂冷凝温度来计算。版权所有(C) 2011年,JPO&INPIT