基于换热成本比的R410A风冷式冷凝器优化

在对R410A空调用风冷式冷凝器进行实验研究的基础上,以换热量成本比为优化目标,分析了换热器结构参数变化对冷凝器性能的影响,进行了基于稳态分布参数模型的换热器仿真计算.通过比较,得出冷凝器换热量和传热系数随换热器的结构参数变化的情况,给出了冷凝器在一定运行条件下的单变量和多变量优化结果.研究表明,换热成本比随翅片厚度、翅片间距和管内径的减小而增大.

基于换热成本的U形地下换热器经济性评估研究

分析地下换热器的埋管方式、钻孔深度、U形管内流体流量及设计进水温度对地下换热器的初投资和热泵运行费用的影响,提出地下换热器单位换热量的换热成本指数的概念,并推导其具体的计算式。利用地下换热器的换热成本指数可以评估不同设计方案的经济性。最后通过计算换热成本指数评估不同设计方案的经济性。

U型管换热性能影响因素研究

建立了钻井单位井深换热量与钻井深度、流量变化关系的计算模型.通过实例计算,分析了在流量不变时钻井的单位井深换热量随钻井深度的变化以及50 m,100 m,150m和200 m钻井单位井深换热量随流量的变化.得出在设计地源热泵地下换热器时,需要合理的选择钻井深度、U型管内的流体流量来保证钻井的换热经济性.最后提出单位井深换热成本指数作为U型管换热经济性评价指标.

土壤源热泵系统模拟和经济性评估研究

在线源理论的基础上建立了土壤源热泵系统的模拟模型,该模型可以用于土壤源热泵系统的全年运行模拟,预测土壤源热泵系统的能耗情况;对于土壤源热泵系统的经济性评估,提出了地下换热器换热成本的概念,并导出了地下换热器换热成本的通用计算方法。本文中的模型可以对土壤源热泵系统的设计方案进行经济性评估,以便设计人员选取经济性较好的方案。

Strong self-flushing technique for heat exchanger of sewage source heat pump system

To better remove the contamination on the surface of a heat-exchanger in urban sewage source heat pump system （USSHPS）, this paper analyzes the feasibility of strong self-flushing on the basis of experiments and presents a new on-line self-flushing technique, which alternately flushes part of heat transfer tubes. In addition, operation principles and the structure of the new heat-exchanger are introduced and the feasible economi- cal and technological cleaning plans are given by design calculation and scheme comparison. The result shows that keeping each tube washed for one minute with 5 m/s, the operating cost is lower than ￥5 and when one flushing pump ahemately flushes 10-20 heat exchangers, the saved costs of flushing 10 tubes alternately are over 4 times of the increased costs.

Minimizing investment cost for multi-period heat exchanger network retrofit by matching heat transfer areas with different strategies

Multi-period heat exchanger network(HEN) retrofit is usually performed by targeting and matching heat transfer areas. In this paper, based on the reverse order matching method we proposed previously, three strategies of matching heat transfer areas are proposed to minimize the investment cost for the retrofit of HEN in multiperiod, in which replacement of heat exchangers, addition of heat exchangers and addition of heat transfer areas are performed. We demonstrate the procedures through three scenarios, including maximum number of substituted heat exchangers after retrofit, minimum additional heat transfer areas in the retrofitted HEN, and minimum investment cost for retrofit. The strategies are extended to a single period HEN retrofit problem. The results of multi-period and single period HEN retro fit problems indicate the effectiveness of the strategies. Moreover, these results are better than those reported in literature. The strategies are simple and easy to implement,which are of great benefit to large-scale HEN retrofit in practice.

Standardized Elemental Basis for Gas-Turbine Engine Heat Exchangers is the Key Factor for Their Cost Reduction

The competitiveness of the small gas turbine units (GTUs) (Ne<300 kW) in the world power market is dependent on bath the maintenance expenses and the capital costs of production. Reduction in the maintenance expenditures could be achieved by increasing the plant efficiency. This task could be solved by some methods: increasing the cycle inlet temperature TIT, getting the cycle more complex (use of heat regeneration and compressed air intermediate cooling), cutting the power consumption on heat-stressed parts cooling. Putting the above into effect is linked with introduction of novel structural materials, a sharp increase in the mass-size values and the plant manufacture expenditures, in particular, at provision of its self-regulation. In connection with the above, the development of the combined metal-ceramic airheaters and standardization of the elemental basis of the metal gas-gas heat exchangers will promote reduction in the expenditures of the maintenance and the manufacture of the small-size independent power GTEs.

New method for the determination of convective heat transfer coefficient in fully-developed laminar pipe flow

Convective heat transfer coefficient is one of the most vital parameters which reveals the thermal efficiency of a pipe flow.To obtain such coefficients for problems with variable pipe wall temperature,numerical iterative methods should be used which could be time-consuming and less accurate.In this paper,thermophysical properties of fluids are assumed to be constant.We define a variable related to the temperature gradient of the pipe wall and study the varying law of the local coefficient.Then,a sample-based scheme is proposed to avoid the calculation of a time-consuming problem in the use of solutions with low computing cost.To verify its accuracy,several problems in normal circle pipes with variable factors,such as the various temperatures of the pipe wall,the different radius of the pipe,and various velocities of fluid flow,are well resolved.Meanwhile,its validity in a convergent pipe is also studied.From the obtained results,the high accuracy and efficiency of the proposed scheme can be confirmed.Therefore,the proposed scheme for determining the convective heat transfer coefficient has great potential in engineering problems.