混合吸收式制冷循环的Yong分析

新型混合吸收式制冷循环的特点是能够运用中低温热源，热源的可利用温差大，制冷系数较高。本文利用Yong效率法对新型混合吸收式制冷循环进行了分析，得出新型混合吸收式制冷循环的Yong效率比两效吸收式循环高，可达0．292。同时得出系统各个部件的Yong损失，分析吸收式制冷系统在能量的转移过程中的薄弱环节，为混合吸收循环系统的优化提供了前提。     

新型混合吸收式制冷循环的实验研究

在理论分析的基础上对混合系统的热源可利用温差进行了实验研究.实验表明,新型混合吸收式制冷循环的热源可利用温差比两级吸收式制冷提高16.7～34.5℃(没有考虑结晶情况下).新型混合吸收式制冷循环对太阳能空调实用化具有很大的意义.     

新型太阳能降压吸收式制冷空调系统特性的理论分析

在两级溴化锂吸收式制冷的基础上提出了一种新型高效的降压吸收式制冷循环,能够有效利用太阳能实现制冷,解决传统吸收式太阳能空调系统存在的弊端。其特点是在传统的两级吸收式循环的基础上,将高压发生器发生出的LiBr溶液与低压吸收器的吸收后的溶液混合,在发生温度与压力允许的范围内,使高压吸收器的吸收剂浓度较两级吸收式循环高,从而在相同的冷凝条件下减小了其压力。分析了新型空调系统的性能特性,理论计算结果表明影响新型系统整体效率的主要因素是LiBr溶液的浓度及驱动热源的可利用温差。新型吸收式循环热源可利用温差最高可达33.5℃,整体效率比两级吸收式系统有较大提高,最大提高46.4%,其集热面积单耗最大减小47.1%,热源单耗是两级系统的0.21,效果较明显。     

三压力喷射吸收式制冷循环分析

本文分析了新型的三压力喷射吸收式制冷循环的特点,以R600/DMF,R22/DEF TEG为例说明了新循环相对于传统的吸收式制冷循环的突出优点,同时指出了利用混合制冷工质有利于新循环制冷效率的进一步提高。     

有限热源四温位不可逆吸收式制冷循环模型及性能分析

建立了热源热容量有限、综合考虑热源与环境间的热漏、热源与循环工质问的热阻以及循环内部不可逆性时的不可逆四温位吸收式制冷循环模型，并导出了循环制冷率和制冷系数间的一般关系式；利用数值算例，分析了吸收式制冷机的一般性能和优化性能，得出了热漏、内不可逆性和工质放热量分配率对循环性能的影响规律。所得结论可为吸收式制冷机的设计和优化提供一些新的理论指导。     

内可逆四热源制冷系统的性能分析和优化

在恒温热源条件下内可逆四热源吸收式制冷循环的基础上 ,考虑传热服从线性唯象定律 ,导出了循环的制冷率和制冷系数的基本优化关系和最大制冷率及相应的制冷系数 ;并通过数值计算 ,得出循环参数对循环的制冷率、制冷系数的影响。     

太阳能吸收式空调性能优化分析

分析影响太阳能两级吸收式空调系统的整体性能的主要因素：集热器进出口热水的温度、各设备中溴化锂溶液的浓度与压力。根据两级吸收式循环的特点，可以运用溶液混合观点构造新型高效的太阳能吸收式制冷空调。运用仿真程序得出了太阳能两级吸收式空调在集热器出口温度在77．5℃左右时可以得到最大的整体效率，为太阳能空调系统的优化奠定了理论基础。     

传质换热过程的溴化锂吸收式制冷循环分析

本文提出了传质换热过程的单效溴化锂吸收式制冷循环,运用能量守恒和质量守恒原理对循环各部件建立热力学模型,使用EES编程对其与常规单效吸收循环进行模拟计算与比较。结果表明,传质回热循环的COP在大部分工况下有所提升,其发生所需热源温度有所降低。该循环不仅可以利用常规单效循环所不能利用的低品位热源,而且减少了冷却水的消耗。同时,该循环开拓了吸收式制冷循环新的研究方向,并丰富了其理论研究的内容。     

新型双温驱动吸收制冷循环性能

针对跨临界CO_2压缩制冷系统制取冷量以消耗高品位能量为代价的问题,本文依据能量梯级利用原理,提出双温低品位热源驱动的新型CO_2-[emim][Tf_2N]吸收式制冷循环的新流程,在构建该制冷循环数学模型的基础上,搭建测试双温驱动吸收制冷循环性能的实验装置,利用模拟和实验方法分析了操作参数对系统性能的影响规律。在定流量的条件下,研究驱动热源温度、冷却水入口温度以及载冷剂入口温度等操作参数对新系统性能的影响规律,结果表明双温驱动新型吸收制冷系统不仅可实现高效制冷,而且最低制冷温度可达到-15.2℃,研究结果为CO_2-离子液体制冷系统的理论设计计算提供实用的数据基础。     

采用离子液体-水工质对的GAX吸收式制冷循环性能研究

热驱动的吸收式制冷技术是太阳能利用和工业余热回收的重要途径,其中GAX(吸收发生换热)吸收式循环具有高效、效率可随热源温度变化的特点。本文提出采用无结晶风险的离子液体工质对,并使用NRTL模型对离子液体工质对性质进行计算,并对GAX吸收式制冷循环进行性能计算。结果表明:采用1,3-二甲基咪唑磷酸二甲酯盐([DMIM][DMP]/水工质对可以使用GAX吸收式循环,且在发生温度较高的情况下COP能够达到约1.02,比相同特定工况下的单效循环COP提升27.5%,比采用溴化锂/水工质对的吸收式循环具有更加优异的性能。     

两级双效溴化锂制冷-热泵复合循环

在热电冷联产系统中,溴化锂吸收式制冷机在制冷过程中排放了大量的废热,这些废热品味低,难以直接回收利用。在此提出了两级双效溴化锂制冷-热泵复合循环,该循环具有冷凝温度较高的特点,便于直接回收冷凝排放热。系统以背压汽轮机的背压蒸汽为热源,制冷的同时利用循环所排出的废热加热锅炉补充水至较高温度。以具有相同功效的双效溴冷机与单效溴化锂热泵联合运行作为对比循环,制冷-热泵复合循环系统省去了一台蒸发器与冷凝器,减少了两个换热温差,并且通过热力计算、能量分析和分析表明,该循环的能量利用率与效率均有很大的提高,效率比对比循环提高了45%。     

A theoretical study on a novel solar based integrated system for simultaneous production of cooling and heating

An integrated system for simultaneous production of triple-effect cooling and single stage heating is proposed in this paper to harness low grade solar energy. The proposed system combines the heliostat field with a central receiver and the ejector-absorption cycle with the shaft power driven transcritical CO₂ cycle. A parametric study based on first and second laws of thermodynamics is carried out to ascertain the effect of varying the exit temperature of duratherm oil, turbine inlet pressure, and evaporators temperature on the energy and exergy output as well as on the energy and exergy efficiencies of the system. The results obtained indicate that major source of exergy destruction is the central receiver where 52.5% of the inlet solar heat exergy is lost followed by the heliostat where 25% of the inlet exergy is destroyed. The energy and exergy efficiencies of the integrated system vary from 32% to 39% and 2.5%–4.0%, respectively, with a rise in the hot oil outlet temperature from 160 °C–180 °C. It is further shown that increase in evaporator temperature of transcritical CO₂ cycle from −20 °C to 0 °C increases the energy efficiency from 27.45% to 43.27% and exergy efficiency from 2.51% to 2.97%, respectively. The results clearly show how the variation in the values of hot oil outlet temperature, turbine inlet pressure, and the evaporator temperature of transcritical CO2 cycle strongly influences the attainable performance of the integrated system.     

定环境温度下冷库的氨蒸汽压缩制冷系统的火用分析

本文通过对定环境温度条件下的冷库中的氨蒸汽单级压缩系统进行火用分析,利用线性拟合的方法对氨的物性进行模拟,并对定蒸发温度和变蒸发温度时,制冷系统的各部件的火用损失和系统的火用效率进行计算分析,得出在冷库氨蒸汽压缩系统中的蒸发器中的火用损失最大,压缩机和冷凝器次之的结果。提出要对冷库氨蒸汽压缩系统的性能进行改进,必须首先考虑提高其蒸发器、压缩机和冷凝器的火用效率着手;从而提出定环境温度条件下,提高蒸发温度是提高系统火用效率的较好的改进措施之一。     

A novel ejector-absorption combined refrigeration cycle

This paper presents a novel ejector-absorption combined refrigeration cycle. When the temperature of the heat source is high enough, this cycle will work as a double-effect cycle. If the temperature of the heat source is lower than required temperature of heat source used to drive conventional double-effect absorption refrigeration cycle but much higher than required temperature of heat source used to drive conventional single-effect absorption refrigeration cycle, the COP of new cycle will also be higher than that of conventional single-effect absorption refrigeration cycle. Simulation results show that the COP of the cycle is 30% higher than that of the conventional single-effect absorption refrigeration cycle at some working conditions even in the later case.     

制冷剂/吸收剂在管内流动及换热过程能耗与(火用)损研究

本文研究分析了水 /二甘醇热泵工质对在管内流动及换热过程 ,建立了描述能量损失与火用损失的数学模型。通过对模型的理论分析、求解和实验研究 ,获得了能耗与火用损失变化规律 ,比较了粘性耗散和导热引起的能耗与火用损     

Investigation on gradient thermal cycle for power and refrigeration cogeneration

In order to improve energy utilization efficiency of low grade heat, a novel gradient thermal cycle for power and refrigeration cogeneration is proposed. The cycle is cascaded with two stages based on different thermal driven temperature. The first stage is pumpless Organic Rankine Cycle (PRC) while the second stage is two-stage sorption refrigerator. R245fa is selected as the working fluid of PRC, whereas CaCl₂-BaCl₂-NH₃ working pair is chosen for two-stage sorption refrigerator. Different heat source temperatures from 80°C to 95°C are adopted for analysis and comparison. Results indicate that the highest average power output and cooling effect are able to reach 204 W and 0.91 kW under the condition of 95°C heat source temperature and 10°C refrigeration temperature. For different heat source temperatures, total energy and exergy efficiency of the gradient thermal cycle for power and refrigeration cogeneration range from 9.49% to 9.9% and 10.9% to 11.8%, respectively. For gradient thermal cycle exergy efficiency of heat utilization ranges from 24% to 18.8% which is 126.5% and 70.9% higher than the PRC and two-stage sorption refrigerator, respectively, when the heat source temperature is 80°C.     

A theoretical study of an innovative ejector powered absorption–recompression cycle refrigerator

This paper describes a novel cycle which uses a steam ejector to enhance the concentration process by compressing the vapour from the lithium bromide solution to a state that it can be used to re-heat the solution from which it came. The energy efficiency and the performance characteristics of the novel cycle are theoretically investigated in this paper. The theoretical results show that the coefficient of performance (COP) of the novel cycle is better than the conventional single-effect absorption cycle. The characteristics of the cycle performance show its promise in using high temperature heat source at low cost.     

Thermodynamic performance assessment of a novel air cooling cycle: Maisotsenko cycle

This study presents energy and exergy analyses and sustainability assessment of the novel evaporative air cooling system based on Maisotsenko cycle which allows the product fluid to be cooled in to a dew point temperature of the incoming air. In the energy analysis, Maisotsenko cycle’s wet-bulb and dew point effectiveness, COP and primary energy ratio rates are calculated. Exergy analysis of the system is then carried out for six reference temperatures ranging from 0 °C to 23.88 °C as the incoming air (surrounding) temperature. The specific flow exergy, exergy input, exergy output, exergy destruction, exergy loss, exergy efficiency, exergetic COP, primary exergy ratio and entropy generation rates are determined for various cases. Furthermore, sustainability assessment is obtained using sustainability index method. As a result, maximum exergy efficiency is found to be 19.14% for a reference temperature of 23.88 °C where the optimum operation takes place.     

Exergy analysis of gas turbine trigeneration system for combined production of power heat and refrigeration

A conceptual trigeneration system is proposed based on the conventional gas turbine cycle for the high temperature heat addition while adopting the heat recovery steam generator for process heat and vapor absorption refrigeration for the cold production. Combined first and second law approach is applied and computational analysis is performed to investigate the effects of overall pressure ratio, turbine inlet temperature, pressure drop in combustor and heat recovery steam generator, and evaporator temperature on the exergy destruction in each component, first law efficiency, electrical to thermal energy ratio, and second law efficiency of the system. Thermodynamic analysis indicates that exergy destruction in combustion chamber and HRSG is significantly affected by the pressure ratio and turbine inlet temperature, and not at all affected by pressure drop and evaporator temperature. The process heat pressure and evaporator temperature causes significant exergy destruction in various components of vapor absorption refrigeration cycle and HRSG. It also indicates that maximum exergy is destroyed during the combustion and steam generation process; which represents over 80% of the total exergy destruction in the overall system. The first law efficiency, electrical to thermal energy ratio and second law efficiency of the trigeneration, cogeneration, and gas turbine cycle significantly varies with the change in overall pressure ratio and turbine inlet temperature, but the change in pressure drop, process heat pressure, and evaporator temperature shows small variations in these parameters. Decision makers should find the methodology contained in this paper useful in the comparison and selection of advanced heat recovery systems.     

复叠式低温制冷箱的(火用)分析

根据实验得到的低温箱降温过程和稳定工作过程状态点参数,以R502/R13复叠式低温制冷箱为例对低温箱系统进行了(火用)分析计算.计算得出系统能效系数和(火用)损失随时间变化情况,更好的考察了系统各部件能耗状况,得到其中高低温级压缩机和蒸发冷凝器的(火用)损失所占比重最大,从而为设备改进提供借鉴和参考.