发明名称 High efficiency double-effect chiller heater apparatus
摘要 The absorption chiller-heater apparatus of present invention utilizes a portion of direct heat, used to heat water, for providing the refrigeration effect. The external heat input required for providing refrigeration is minimal; hence, the efficiency of the apparatus is increased by 30-40% over the conventional systems. Further, as the quantum of the external heat source required for a new cycle is reduced, the size of the high temperature generator required, is smaller, which results in lower capital costs. The apparatus provides chilled water which can be used for various industrial purposes. The absorption chiller-heater reduces CO2 emissions and utilizes a single arrangement to produce both heating and refrigeration effect. Thus, additional electrical and heat input or separate components are not required.
申请公布号 US8839635(B2) 申请公布日期 2014.09.23
申请号 US201113032675 申请日期 2011.02.23
申请人 Thermax Limited 发明人 Radhakrishnan Blau;Panneerselvam Babu;Kulkarni Swapna
分类号 F25B15/00;F25B15/06;F25B29/00;F25B27/02 主分类号 F25B15/00
代理机构 Cowan, Liebowitz & Latman, P.C. 代理人 Cowan, Liebowitz & Latman, P.C. ;Montague Mark
主权项 1. An absorption chiller-heater apparatus, for providing heating and refrigeration, said apparatus comprising: a high temperature generator (102), a hot-water heat exchanger (104), a high temperature heat exchanger (106), a low temperature generator (110), a low temperature heat exchanger (108), a recovery heat exchanger (112), a condenser (114), an evaporator (116), and an absorber (118), and optionally comprising: a heat reclaimer (120);characterized in that: the high temperature generator (102) is selectively connected in communication with a first set of equipment selected from the group of sets of equipment consisting of: (i) the hot-water heat exchanger (104), the high temperature heat exchanger (106), the low temperature generator (110), and the heat reclaimer (120); and (ii) the hot-water heat exchanger (104), the high temperature heat exchanger (106), and the low temperature generator (110); the hot-water heat exchanger (104) is operatively connected to be in communication with a set of equipment selected from the high temperature generator (102) and the recovery heat exchanger (112), wherein, the hot-water heat exchanger (104) is operatively connected to at least one equipment selected from a group of equipments consisting of the condenser (114) and the evaporator (116), via the recovery heat exchanger (112); the high temperature heat exchanger (106) is selectively connected in communication with a second set of equipment selected from the group of sets of equipment consisting of: (i) the high temperature generator (102), the low temperature generator (110), and the low temperature heat exchanger (108); (ii) the high temperature generator (102), the low temperature generator (110), the low temperature heat exchanger (108), and the recovery heat exchanger (112); (iii) the high temperature generator (102), the low temperature heat exchanger (108), and the recovery heat exchanger (112); and (iv) the high temperature generator (102), the low temperature heat exchanger (108), and the absorber (118); the low temperature generator (110) is selectively connected in communication with a third set of equipment selected from the group of sets of equipment consisting of: (i) the high temperature generator (102), the high temperature heat exchanger (106), the low temperature heat exchanger (108), and the recovery heat exchanger (112); and (ii) the high temperature generator (102), the low temperature heat exchanger (108), and the recovery heat exchanger (112); the low temperature heat exchanger (108) is operatively connected to be in communication with the low temperature generator (110), the high temperature heat exchanger (106), and the absorber (118); the recovery heat exchanger (112) is selectively connected in communication with a fourth set of equipment selected from the group of sets of equipment consisting of: (i) the low temperature generator (110), the hot-water heat exchanger (104), the absorber (118), the condenser (114), and the heat reclaimer (120); (ii) the low temperature generator (110), the hot-water heat exchanger (104), the absorber (118), the condenser (114), and the high temperature heat exchanger (106); and (iii) the low temperature generator (110), the hot-water heat exchanger (104), the absorber (118), and the condenser (114); the heat reclaimer (120) is operatively connected to be in communication with the recovery heat exchanger (112) and the high temperature generator (102); the condenser (114) is operatively connected to be in communication with the recovery heat exchanger (112), the absorber (118), and the evaporator (116); the evaporator (116) is operatively connected to be in communication with the condenser (114); and the absorber (118) is selectively connected in communication with a fifth set of equipment selected from the group of sets of equipment consisting of: (i) the condenser (114), the low temperature heat exchanger (108), and the recovery heat exchanger (112); and (ii) the condenser (114), the low temperature heat exchanger (108), the recovery heat exchanger (112), and the high temperature heat exchanger (106).
地址 Maharashtra IN