共查询到20条相似文献,搜索用时 78 毫秒
1.
2.
3.
4.
在移动式余热利用实验系统基础上,对移动式余热利用系统的实际应用规模进行了成本和收益估算。通过两项经济性指标(净现值和投资回收期)进行了系统经济性的分析研究,并结合蓄热器充热时间、热源距离、余热价格等因素进行了项目的敏感性分析。结果表明,对于案例中的移动式余热利用项目,当余热成本发生变化时折现率取7%、10%、12%和15%时,对应项目在系统运行年限内的净现值大于零。根据余热成本的不同,在4种折现率情况下最长的投资回收期分别为13 a、9 a、11 a和15 a。上述经济性指标表明案例中的移动式余热利用项目从经济性上考虑是可行的。蓄热器充热时间和热源距离对项目经济性的影响程度基本相同,均大于余热价格对项目经济性的影响。该经济性研究为移动式余热利用项目的决策提供了参考依据。 相似文献
5.
6.
简要介绍了武昌热电公司利用天然气的改扩建工程;着重分析了S109E联合循环热电冷联产的热经济性,结果表明,这一联产形式实现了能源梯级利用,使能源转换效率高达70%. 相似文献
7.
8.
9.
在火电机组中,汽轮机乏汽的热量被排放到环境中,致使机组冷源损失较大,机组发电热效率难以提升,并且会造成环境的热污染,为了回收大量循环水余热,以NZK660-24.2/566/566为例,利用热泵技术,拟将回收的循环水余热利用到本机组的给水系统之中,取代7号加热器的抽汽.建立余热回收的物理模型和数学模型,对机组进行热经济性分析与计算,并和原来机组进行对比,结果表明该模型提高了机组的热经济性.作为火电机组冷源优化方式的一种新的尝试,为火电机组余热回收的研究提供了参考. 相似文献
10.
11.
合理利用垃圾资源进行热电联产,是节能减排、改善环境的有力措施。以某2×750 t·d-1垃圾焚烧电厂为例,通过模型研究发现热电联产可以减少垃圾焚烧电厂的冷源损失,提高全厂热效率;利用一抽蒸汽进行热电联产可实现蒸汽品质的梯级利用,获得较高的经济效益;供热量为30 t·h-1,垃圾热值由4185.9 kJ·kg-1增加至8371.7 kJ·kg-1时,发电量越多,供热能力越强,年热电联产经济效益由7822.76万元增加到14641.07万元;垃圾热值为8371.7 kJ·kg-1,供热量从10 t·h-1增加到60 t·h-1时,垃圾焚烧电厂热效率从28.96%增加到48.50%,年经济效益从13602.74万元增加到15455.66万元。当该地区垃圾热值较高并具备供热条件时,实现垃圾热电联产具有较高的收益。 相似文献
12.
13.
14.
电厂循环水余热回收供暖节能分析与改造技术 总被引:1,自引:1,他引:0
在电厂余热利用的基础上,通过回收冷却塔散失的热量,对循环水余热回收供暖进行了节能分析,结合电厂对循环水余热回收供暖的应用,阐述循环水余热回收供暖的节能措施以及实施后的节能效果。实践证明,电厂循环水余热回收供暖具有显著的节能和环保效果。 相似文献
15.
综述火电厂低温余热利用技术的特点及应用现状,并对各种技术进行了对比分析,其中集中式吸收式热泵供热技术在当前应用最广泛,是最具发展前景的技术。苇湖梁电厂低温余热利用项目是集中式吸收式热泵125MW水冷机组技术在国内的首次工程应用,项目具有显著的节能效果,可实现年节约标煤41688t,节水65.88万t。 相似文献
16.
17.
Economic analysis of renewable heat and electricity production by sewage sludge digestion—a case study
下载免费PDF全文
![点击此处可从《国际能源研究杂志》网站下载免费的PDF全文](/ch/ext_images/free.gif)
In this paper, we assess the total cost of energy recovery from sewage sludge through anaerobic digestion with biogas utilization in combined heat and power (CHP) system. The important advantage of anaerobic digestion process is the production of biogas, which can be used to generate electricity and heat as a source of renewable energy. From this study, it can be retained that the generated thermal energy from the anaerobic digestion process meets the needs of the wastewater treatment plant (WWTP) and guarantees its self‐sufficiency in heat. The surplus of renewable heat produced by CHP is not a primary factor to improve the economic viability of the process. Moreover, the sales of electricity output represent about 76% of the operating costs of anaerobic digestion process. Renewable energy production is not economically viable by its own, without considering the wastewater treatment function and the associated incomes. Nevertheless, sludge digestion helps to reduce the wastewater treatment costs mainly by giving a good source of revenue via electricity production. Copyright © 2014 John Wiley & Sons, Ltd. 相似文献
18.
19.
This paper has proposed an improved liquefied natural gas (LNG) fuelled combined cycle power plant with a waste heat recovery and utilization system. The proposed combined cycle, which provides power outputs and thermal energy, consists of the gas/steam combined cycle, the subsystem utilizing the latent heat of spent steam from the steam turbine to vaporize LNG, the subsystem that recovers both the sensible heat and the latent heat of water vapour in the exhaust gas from the heat recovery steam generator (HRSG) by installing a condensing heat exchanger, and the HRSG waste heat utilization subsystem. The conventional combined cycle and the proposed combined cycle are modelled, considering mass, energy and exergy balances for every component and both energy and exergy analyses are conducted. Parametric analyses are performed for the proposed combined cycle to evaluate the effects of several factors, such as the gas turbine inlet temperature (TIT), the condenser pressure, the pinch point temperature difference of the condensing heat exchanger and the fuel gas heating temperature on the performance of the proposed combined cycle through simulation calculations. The results show that the net electrical efficiency and the exergy efficiency of the proposed combined cycle can be increased by 1.6 and 2.84% than those of the conventional combined cycle, respectively. The heat recovery per kg of flue gas is equal to 86.27 kJ s?1. One MW of electric power for operating sea water pumps can be saved. The net electrical efficiency and the heat recovery ratio increase as the condenser pressure decreases. The higher heat recovery from the HRSG exit flue gas is achieved at higher gas TIT and at lower pinch point temperature of the condensing heat exchanger. Copyright © 2006 John Wiley & Sons, Ltd. 相似文献
20.
介绍了向心式汽轮机的特点及大型铜冶炼厂余热利用系统,提出了饱和蒸汽发电系统方案,并将其与传统轴流式背压汽轮机系统方案进行经济技术比校. 相似文献