-
公开(公告)号:US06993933B2
公开(公告)日:2006-02-07
申请号:US10831542
申请日:2004-04-23
IPC分类号: F25B15/00
CPC分类号: F25B15/008 , F25B2333/003 , Y02A30/277 , Y02B30/62 , Y02P80/152
摘要: Even when the efficiency of a low temperature heat exchanger is raised to reduce the required heat capacity inputting to the absorption refrigerating machine and the temperature of cooling water supplied to an absorber falls suddenly as it is, and thereby the temperature of a diluted absorbent solution falls suddenly, an absorption refrigerating machine without abnormally increasing the temperature of the concentrated absorbent solution and crystallizing the solution is disclosed. A heat recovery device 8 is provided between a low temperature heat exchanger 6 and a high temperature heat exchanger 7 of an absorbent solution pipe 13 for connecting a high temperature regenerator 1 and an absorber 5 with the low temperature heat exchanger 6, the high temperature heat exchanger 7 and an absorbent solution pump 14 therebetween. Further, the heat recovery device 9 is provided between the low temperature heat exchanger 6 and the absorbent solution pump 14. High temperature and high-pressure vapor is supplied through a heat source fluid supply pipe 10 to a heat exchanger pipe 1A provided within the high temperature generator 1 to thereby heat and boil a diluted absorbent solution within the high temperature regenerator 1 and radiate heat. Then, high temperature drain, which has been condensed by heat radiation and discharged to an exhaust heat fluid pipe 10A, is supplied to the heat recovery devices 8, 9 to thereby heat a diluted absorbent solution delivered from the absorber 5 through the absorbent solution pipe 13 to the high temperature regenerator 1 by an absorbent solution pump 14.
摘要翻译: 即使当提高低温热交换器的效率以减少对吸收式制冷机的所需热容量输入时,供应给吸收器的冷却水的温度也会立即下降,从而稀释的吸收剂溶液的温度下降 公开了一种不会使浓缩吸收剂溶液的温度异常升高并使溶液结晶化的吸收式制冷机。 在低温热交换器6和用于将高温再生器1和吸收器5连接到低温热交换器6的吸收剂溶液管13的高温热交换器7之间设置有热回收装置8,高温热 交换器7和其间的吸收剂溶液泵14。 此外,热回收装置9设置在低温热交换器6和吸收剂溶液泵14之间。 将高温高压蒸汽通过热源流体供给管10供给到设置在高温发生器1内的热交换管1A,从而对高温再生器1内的稀释吸收剂溶液进行加热和沸腾,并且散热。 然后,通过热辐射冷凝并排出到排气热流体管道10A的高温排放物被供应到热回收装置8,9,从而通过吸收剂溶液加热从吸收器5输送的稀释吸收剂溶液 管13通过吸收剂溶液泵14连接至高温再生器1。
-
公开(公告)号:US06250100B1
公开(公告)日:2001-06-26
申请号:US09538422
申请日:2000-03-29
申请人: Hideki Funai , Kazuhiro Yoshii , Hisao Miyazaki , Kazuya Sawakura , Daisaku Chou
发明人: Hideki Funai , Kazuhiro Yoshii , Hisao Miyazaki , Kazuya Sawakura , Daisaku Chou
IPC分类号: F25B3300
CPC分类号: F25B33/00 , F25B2333/003 , Y02A30/274
摘要: A dual heat source high-temperature regenerator to solve problems involved in two types of conventional high-temperature regenerators for carrying out heating by using a dedicated burner as the heat source and by using exhaust gas supplied from outside systems as the heat source; namely, the former type has a problem of higher running costs, and the latter a problem of narrower ranges for capacity control. The dual heat source high-temperature regenerator arranges two inner shells and inside an outer shell to form combustion and exhaust gas flues, respectively. The combustion gas flue has a sideways U shape as a whole. The lower end is equipped with a burner, and the upper end connected to an exhaust duct. The exhaust gas flue 62 has a horizontal, straight shape as a whole. One end is provided with an exhaust gas inlet, and the other end connected to an exhaust duct. The portions where a dilute absorbent liquor collects heat easily are the vertical-stroke portion on the sideways U of the combustion gas flue and the vicinity of the end of the exhaust gas flue making the exhaust gas inlet. The vertical-stroke portion and the exhaust gas inlet are collected to the same side so that the convection current of the dilute absorbent liquor produces a smooth circulation of the liquor as shown by broken lines in the drawings.
摘要翻译: 一种双重热源高温再生器,用于解决两种用于通过使用专用燃烧器作为热源进行加热并通过使用从外部系统供应的废气作为热源的常规高温再生器所涉及的问题; 即前者具有运行成本较高的问题,后者是容量控制范围较窄的问题。 双热源高温再生器分别设置两个内壳和外壳内部,形成燃烧和排气烟道。 燃烧气体烟道整体具有侧向U形。 下端配有燃烧器,上端连接到排气管。 废气烟道62整体上具有水平的直线形状。 一端设有排气入口,另一端与排气管连接。 稀释吸收剂容易收集的部分是燃烧气体烟道的侧面U上的垂直行程部分和排气进口的废气烟道末端附近。 垂直行程部分和排气入口被收集到同一侧,使得稀释的吸收液体的对流电流产生液体的平滑循环,如图中虚线所示。
-
公开(公告)号:US20050016205A1
公开(公告)日:2005-01-27
申请号:US10831542
申请日:2004-04-23
CPC分类号: F25B15/008 , F25B2333/003 , Y02A30/277 , Y02B30/62 , Y02P80/152
摘要: Even when the efficiency of a low temperature heat exchanger is raised to reduce the required heat capacity inputting to the absorption refrigerating machine and the temperature of cooling water supplied to an absorber falls suddenly as it is, and thereby the temperature of a diluted absorbent solution falls suddenly, an absorption refrigerating machine without abnormally increasing the temperature of the concentrated absorbent solution and crystallizing the solution is disclosed. A heat recovery device 8 is provided between a low temperature heat exchanger 6 and a high temperature heat exchanger 7 of an absorbent solution pipe 13 for connecting a high temperature regenerator 1 and an absorber 5 with the low temperature heat exchanger 6, the high temperature heat exchanger 7 and an absorbent solution pump 14 therebetween. Further, the heat recovery device 9 is provided between the low temperature heat exchanger 6 and the absorbent solution pump 14. High temperature and high-pressure vapor is supplied through a heat source fluid supply pipe 10 to a heat exchanger pipe 1A provided within the high temperature generator 1 to thereby heat and boil a diluted absorbent solution within the high temperature regenerator 1 and radiate heat. Then, high temperature drain, which has been condensed by heat radiation and discharged to an exhaust heat fluid pipe 10A, is supplied to the heat recovery devices 8, 9 to thereby heat a diluted absorbent solution delivered from the absorber 5 through the absorbent solution pipe 13 to the high temperature regenerator 1 by an absorbent solution pump 14.
摘要翻译: 即使当提高低温热交换器的效率以减少对吸收式制冷机的所需热容量输入时,供应给吸收器的冷却水的温度也会立即下降,从而稀释的吸收剂溶液的温度下降 公开了一种不会使浓缩吸收剂溶液的温度异常升高并使溶液结晶化的吸收式制冷机。 在低温热交换器6和用于将高温再生器1和吸收器5连接到低温热交换器6的吸收剂溶液管13的高温热交换器7之间设置有热回收装置8,高温热 交换器7和其间的吸收剂溶液泵14。 此外,热回收装置9设置在低温热交换器6和吸收剂溶液泵14之间。高温高压蒸气通过热源流体供给管10供给到设置在高温热交换器6内的热交换管1A 从而对高温再生器1内的稀释吸收剂溶液进行加热和沸腾,并且散热。 然后,通过热辐射冷凝并排出到排气热流体管10A的高温排放物被供应到热回收装置8,9,从而通过吸收剂溶液管加热从吸收器5输送的稀释吸收剂溶液 13通过吸收剂溶液泵14连接到高温再生器1。
-
-