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    • 1. 发明申请
    • IMPROVED HEAT PUMP AND PROCESS OF HEAT PUMPING
    • 改进的热泵和热泵过程
    • WO2017146570A1
    • 2017-08-31
    • PCT/NL2017/050106
    • 2017-02-22
    • FRAMES RENEWABLE ENERGY SOLUTIONS B.V.
    • REXWINKEL, GlennTEN ASBROEK, Nick Antonius Maria
    • F25B25/02F25B49/04F25B41/00
    • F25B25/02F25B41/003F25B49/043
    • The heat pump comprises a closed circuit configured for flow of a solvent and a refrigerant, which closed circuit comprises an evaporator and an absorber, which are mutually interconnected with a first line configured for the transport of vapour from the evaporator to the absorber, a second line configured for the transport of a primarily liquid stream from the evaporator to the absorber, and a third line configured for transport of an enriched liquid from the absorber towards the evaporator, wherein said evaporator is typically in heat communication with an input stream for transmission of heat into the evaporator and wherein said enriched liquid being brought in heat communication with a output stream for transmission of heat thereto, particularly at high pressure, wherein a compressor is arranged in the first line and an expansion device is arranged in the third line. Herein, a first refrigerant inlet and a second refrigerant inlet are present and are configured for supply of a first and a second refrigerant. This is configured such that the first refrigerant and the second refrigerant react with each other in the absorber, leading overall to liberation of condensation heat and reaction heat.
    • 所述热泵包括闭合回路,所述闭合回路构造成用于溶剂和制冷剂的流动,所述闭合回路包括蒸发器和吸收器,所述闭合回路与第一管线相互连接,所述第一管线构造成用于从 蒸发器至吸收器,第二管线被配置用于将主要液体流从蒸发器输送至吸收器,以及第三管线,其被配置用于将富集液体从吸收器朝蒸发器输送,其中所述蒸发器通常处于加热状态 与输入流连通,用于将热量传输到蒸发器中,并且其中所述富集液体与输出流进行热交换以便向其传输热量,特别是在高压下,其中压缩机布置在第一管路中并且膨胀装置 安排在第三行。 这里,存在第一制冷剂入口和第二制冷剂入口并且构造成供应第一制冷剂和第二制冷剂。 这被配置为使得第一制冷剂和第二制冷剂在吸收器中彼此反应,总体上导致冷凝热量和反应热量的释放。
    • 2. 发明申请
    • PROCESS FOR THE PURIFICATION OF A GAS
    • 气体净化过程
    • WO2017099581A2
    • 2017-06-15
    • PCT/NL2016/000022
    • 2016-12-08
    • FRAMES RENEWABLE ENERGY SOLUTIONS B.V.
    • REXWINKEL, GlennTEN ASBROECK, Nick Antonius Maria
    • B01D53/14
    • B01D53/1475B01D53/1425B01D53/1487B01D2257/304B01D2257/504B01D2257/708B01D2257/80B01D2258/05Y02A50/235Y02C10/06Y02E50/346
    • The system for the purification of feed gas comprises a compressor (20) with an inlet for feed gas (A), an inlet for a recirculation gas stream (86), and an outlet for compressed gas; cooling means (22) for cooling the compressed gas; a gas-liquid separator (30) arranged downstream of the cooling means (22) for removal of condensate (37) formed during treatment of the compressed gas with the cooling means (22); a solvent absorber (40) for absorbing impurities including volatile organic compounds (VOCs) and carbon dioxide from the compressed and at least partially dried gas, and a separation unit (80) provided with a recirculation outlet for a recirculation gas stream (86), and an outlet for the thus purified gas (B). The solvent absorber (40) is arranged in a solvent circulation circuit (10) comprising a first and a second treatment means (140, 240) for regeneration of the solvent to remove absorbed impurities, said first treatment means (140) being configured for operating at a higher pressure than the second treatment means (240). The solvent recirculation circuit (10) is configured for splitting off a removal stream (145), and a reclaimer unit (60) is present for reducing the VOC concentration of the removal stream (145), a solvent outlet (65) of the reclaiming unit (60) being coupled to the solvent recirculation circuit (10). The system is used for the process of purification of feed gas.
    • 用于净化进料气体的系统包括具有用于进料气体(A)的入口,用于再循环气流(86)的入口和用于压缩气体的出口的压缩机(20) 冷却装置(22),用于冷却压缩气体; 一个布置在冷却装置(22)下游的气液分离器(30),用于除去在用冷却装置(22)处理压缩气体期间形成的冷凝物(37); 用于从压缩和至少部分干燥的气体中吸收包括挥发性有机化合物(VOC)和二氧化碳的杂质的溶剂吸收器(40),以及设有用于再循环气流(86)的再循环出口的分离单元(80) 和用于如此净化的气体(B)的出口。 所述溶剂吸收器(40)布置在溶剂循环回路(10)中,所述溶剂循环回路包括用于溶剂再生以去除吸收的杂质的第一处理装置和第二处理装置(140,240),所述第一处理装置(140) 处于比第二处理装置(240)更高的压力下。 溶剂再循环回路(10)构造成用于分离去除流(145),并且存在用于降低去除流(145)的VOC浓度的回收装置单元(60),回收装置的溶剂出口(65) 单元(60)连接到溶剂再循环回路(10)。 该系统用于原料气净化过程。
    • 3. 发明申请
    • PROCESS AND SYSTEM FOR THE PURIFICATION OF GAS
    • 用于净化气体的方法和系统
    • WO2017099581A3
    • 2017-06-15
    • PCT/NL2016/000022
    • 2016-12-08
    • FRAMES RENEWABLE ENERGY SOLUTIONS B.V.
    • REXWINKEL, GlennTEN ASBROECK, Nick Antonius Maria
    • B01D53/14
    • The system for the purification of feed gas comprises a compressor (20) with an inlet for feed gas (A), an inlet for a recirculation gas stream (86), and an outlet for compressed gas; cooling means (22) for cooling the compressed gas; a gas-liquid separator (30) arranged downstream of the cooling means (22) for removal of condensate (37) formed during treatment of the compressed gas with the cooling means (22); a solvent absorber (40) for absorbing impurities including volatile organic compounds (VOCs) and carbon dioxide from the compressed and at least partially dried gas, and a separation unit (80) provided with a recirculation outlet for a recirculation gas stream (86), and an outlet for the thus purified gas (B). The solvent absorber (40) is arranged in a solvent circulation circuit (10) comprising a first and a second treatment means (140, 240) for regeneration of the solvent to remove absorbed impurities, said first treatment means (140) being configured for operating at a higher pressure than the second treatment means (240). The solvent recirculation circuit (10) is configured for splitting off a removal stream (145), and a reclaimer unit (60) is present for reducing the VOC concentration of the removal stream (145), a solvent outlet (65) of the reclaiming unit (60) being coupled to the solvent recirculation circuit (10). The system is used for the process of purification of feed gas.
    • 用于净化进料气体的系统包括具有用于进料气体(A)的入口,用于再循环气流(86)的入口和用于压缩气体的出口的压缩机(20) 冷却装置(22),用于冷却压缩气体; 一个布置在冷却装置(22)下游的气液分离器(30),用于除去在用冷却装置(22)处理压缩气体期间形成的冷凝物(37); 用于从压缩和至少部分干燥的气体中吸收包括挥发性有机化合物(VOC)和二氧化碳的杂质的溶剂吸收器(40),以及设有用于再循环气流(86)的再循环出口的分离单元(80) 和用于如此净化的气体(B)的出口。 所述溶剂吸收器(40)布置在溶剂循环回路(10)中,所述溶剂循环回路包括用于溶剂再生以去除吸收的杂质的第一处理装置和第二处理装置(140,240),所述第一处理装置(140) 处于比第二处理装置(240)更高的压力下。 溶剂再循环回路(10)构造成用于分离去除流(145),并且存在用于降低去除流(145)的VOC浓度的回收装置单元(60),回收装置的溶剂出口(65) 单元(60)连接到溶剂再循环回路(10)。 该系统用于原料气净化过程。