为降低CO_(2)排放,提高能源利用效率,该文建立超超临界二次再热-碳捕集集成系统。利用碳捕集汽轮机排汽为再沸器提供能量,并在集成系统基础上提出3种优化方法。结果表明,3种优化方案都提高了机组效率和热力性能,热效率分别提高0.508%、1...为降低CO_(2)排放,提高能源利用效率,该文建立超超临界二次再热-碳捕集集成系统。利用碳捕集汽轮机排汽为再沸器提供能量,并在集成系统基础上提出3种优化方法。结果表明,3种优化方案都提高了机组效率和热力性能,热效率分别提高0.508%、1.314%和4.817%,对应煤耗分别降低4.514g/(kW×h)、11.428g/(kW×h)、39.440g/(kW×h)。当设定碳捕集率为96%、CO_(2)再生能耗为3.8GJ/t时,对集成系统及3种优化系统进行技术经济性分析与㶲分析。通过分析可知,方案III的平均发电成本(the levelized cost of energy,LCOE)和CO_(2)减排成本最低;㶲分析表明高压加热器的㶲效率、㶲损普遍高于低压加热器。3种方案中,方案Ⅲ的高压加热器㶲效率明显高于方案Ⅰ与方案Ⅱ,从系统各设备㶲分析对比来看锅炉㶲效率最低。与锅炉相比较汽轮机的㶲损失相对较小,其中超高压缸和低压缸㶲损失所占比例相对较大。展开更多
A novel power and cooling system combined system which coupled organic Rankine cycle(ORC) with vapor compression refrigeration cycle(VCRC) was proposed. R245 fa and butane were selected as the working fluid for the po...A novel power and cooling system combined system which coupled organic Rankine cycle(ORC) with vapor compression refrigeration cycle(VCRC) was proposed. R245 fa and butane were selected as the working fluid for the power and refrigeration cycle, respectively. A performance comparison and analysis for the combined system was presented. The results show that dual-pressure ORC-VCRC system can achieve an increase of 7.1% in thermal efficiency and 6.7% in exergy efficiency than that of basic ORC-VCRC. Intermediate pressure is a key parameter to both net power and exergy efficiency of dual-pressure ORC-VCRC system. Combined system can produce maximum net power and exergy efficiency at 0.85 MPa for intermediate pressure and 2.4 MPa for high pressure, respectively. However, superheated temperature at expander inlet has little impact on the two indicators. It can achieve higher overall COP, net power and exergy efficiency at smaller difference between condensation temperature and evaporation temperature of VCRC.展开更多
Dynamic performance is important to the controlling and monitoring of the organic Rankine cycle(ORC) system so to avoid the occurrence of unwanted conditions. A small scale waste heat recovery system with organic Rank...Dynamic performance is important to the controlling and monitoring of the organic Rankine cycle(ORC) system so to avoid the occurrence of unwanted conditions. A small scale waste heat recovery system with organic Rankine cycle was constructed and the dynamic behavior was presented. In the dynamic test, the pump was stopped and then started. In addition, there was a step change of the flue gas volume flow rate and the converter frequency of multistage pump, respectively. The results indicate that the working fluid flow rate has the shortest response time, followed by the expander inlet pressure and the expander inlet temperature.The operation frequency of pump is a key parameter for the ORC system. Due to a step change of pump frequency(39.49-35.24 Hz),the expander efficiency and thermal efficiency drop by 16% and 21% within 2 min, respectively. Besides, the saturated mixture can lead to an increase of the expander rotation speed.展开更多
Organic Rankine cycle(ORC) power plant operating with supercritical parameters supplied by low temperature slag-washing water(SWW) of blast furnace was investigated.A schematic of such installation was presented with ...Organic Rankine cycle(ORC) power plant operating with supercritical parameters supplied by low temperature slag-washing water(SWW) of blast furnace was investigated.A schematic of such installation was presented with a description of its operation and the algorithm of calculations of a supercritical power plant.Two typical organic fluids with sufficiently low critical parameters were selected as candidate working fluids in the plant to study the efficiency of the system with different organic fluids.An analysis of the influence on the effectiveness of operation of a plant was carried out.With the same temperature of slag-washing water,the specific work in turbine of fluid R143a is 45% higher than that obtained for the fluid R125,however,the specific work in pump of fluid R143a is approximate equal into that one of the fluid R125.展开更多
文摘为降低CO_(2)排放,提高能源利用效率,该文建立超超临界二次再热-碳捕集集成系统。利用碳捕集汽轮机排汽为再沸器提供能量,并在集成系统基础上提出3种优化方法。结果表明,3种优化方案都提高了机组效率和热力性能,热效率分别提高0.508%、1.314%和4.817%,对应煤耗分别降低4.514g/(kW×h)、11.428g/(kW×h)、39.440g/(kW×h)。当设定碳捕集率为96%、CO_(2)再生能耗为3.8GJ/t时,对集成系统及3种优化系统进行技术经济性分析与㶲分析。通过分析可知,方案III的平均发电成本(the levelized cost of energy,LCOE)和CO_(2)减排成本最低;㶲分析表明高压加热器的㶲效率、㶲损普遍高于低压加热器。3种方案中,方案Ⅲ的高压加热器㶲效率明显高于方案Ⅰ与方案Ⅱ,从系统各设备㶲分析对比来看锅炉㶲效率最低。与锅炉相比较汽轮机的㶲损失相对较小,其中超高压缸和低压缸㶲损失所占比例相对较大。
基金Project(12C0379)supported by the Scientific Research Fund of Hunan Province,ChinaProject(13QDZ04)supported by the Scientific Research Foundation for Doctors of Xiangtan University,China
文摘A novel power and cooling system combined system which coupled organic Rankine cycle(ORC) with vapor compression refrigeration cycle(VCRC) was proposed. R245 fa and butane were selected as the working fluid for the power and refrigeration cycle, respectively. A performance comparison and analysis for the combined system was presented. The results show that dual-pressure ORC-VCRC system can achieve an increase of 7.1% in thermal efficiency and 6.7% in exergy efficiency than that of basic ORC-VCRC. Intermediate pressure is a key parameter to both net power and exergy efficiency of dual-pressure ORC-VCRC system. Combined system can produce maximum net power and exergy efficiency at 0.85 MPa for intermediate pressure and 2.4 MPa for high pressure, respectively. However, superheated temperature at expander inlet has little impact on the two indicators. It can achieve higher overall COP, net power and exergy efficiency at smaller difference between condensation temperature and evaporation temperature of VCRC.
基金Project(2009Gk2009)supported by the Science and Technology Department Funds of Hunan Province,ChinaProject(12C0379)supported by the Scientific Research Fund of Hunan Province,ChinaProject(13QDZ04)supported by the Scientific Research Foundation for Doctors of Xiang Tan University,China
文摘Dynamic performance is important to the controlling and monitoring of the organic Rankine cycle(ORC) system so to avoid the occurrence of unwanted conditions. A small scale waste heat recovery system with organic Rankine cycle was constructed and the dynamic behavior was presented. In the dynamic test, the pump was stopped and then started. In addition, there was a step change of the flue gas volume flow rate and the converter frequency of multistage pump, respectively. The results indicate that the working fluid flow rate has the shortest response time, followed by the expander inlet pressure and the expander inlet temperature.The operation frequency of pump is a key parameter for the ORC system. Due to a step change of pump frequency(39.49-35.24 Hz),the expander efficiency and thermal efficiency drop by 16% and 21% within 2 min, respectively. Besides, the saturated mixture can lead to an increase of the expander rotation speed.
基金Project(2011FZ050) supported by the Applied Basic Research Program of Yunnan Provincial Science and Technology Department,ChinaProject(2011J084) supported by the Master Program of Yunnan Province Education Department,China
文摘Organic Rankine cycle(ORC) power plant operating with supercritical parameters supplied by low temperature slag-washing water(SWW) of blast furnace was investigated.A schematic of such installation was presented with a description of its operation and the algorithm of calculations of a supercritical power plant.Two typical organic fluids with sufficiently low critical parameters were selected as candidate working fluids in the plant to study the efficiency of the system with different organic fluids.An analysis of the influence on the effectiveness of operation of a plant was carried out.With the same temperature of slag-washing water,the specific work in turbine of fluid R143a is 45% higher than that obtained for the fluid R125,however,the specific work in pump of fluid R143a is approximate equal into that one of the fluid R125.
