Solar heat pipe ETC integrated with solar still system for water treatment and hot water production: novel hybrid experimental approach

被引:3
|
作者
Pathak, Atin K. [1 ]
Chopra, K. [1 ,2 ]
Tyagi, V. V. [1 ]
Anand, Sanjeev [1 ]
Kothari, Richa [3 ]
Sari, Ahmet [4 ,5 ]
Pandey, A. K. [6 ,7 ]
机构
[1] Shri Mata Vaishno Devi Univ, Sch Energy Management, Katra 182320, J&K, India
[2] Shri Mata Vaishno Devi Univ, Sch Mech Engn, Katra 182320, J&K, India
[3] Cent Univ Jammu Rahya Suchani Bagla, Dept Environm Sci, Samba 181143, J&K, India
[4] Karadeniz Tech Univ, Dept Met & Mat Engn, TR-61080 Trabzon, Turkiye
[5] King Fahd Univ Petr & Minerals, Renewable Energy Res Inst, Ctr Res Excellence, Dhahran 31261, Saudi Arabia
[6] Sunway Univ, Res Ctr Nanomat & Energy Technol RCNMET, Sch Engn & Technol, 5 Jalan Univ,Bandar Sunway, Petaling Jaya 47500, Selangor, Malaysia
[7] Saveetha Univ, Saveetha Inst Med & Tech Sci, Ctr Transdisciplinary Res CFTR, Chennai, India
关键词
Hybrid system; Distilled water productivity; Thermal efficiency; Solar vacuum tube collector; Exergy efficiency; Heat pipe; EVACUATED TUBE COLLECTOR; FLAT-PLATE COLLECTOR; PERFORMANCE ANALYSIS; PARABOLIC TROUGH; ENERGY; STORAGE; EXERGY;
D O I
10.1007/s10973-023-12281-3
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this manuscript, the innovative design of a hybrid system is investigated for distilled water and hot water production using the heat pipe-equipped vacuum tube collector system assimilated with solar still (HTP-ETCS-SS). The proposed hybrid system is compared with traditional solar still (SS) in context of energy, exergy and financial analysis with two different depths, i.e., 40%, and 60%, and varying flow rate (4, 8, and 12 LPH). The results show a rise in distilled water productivity by 152.9%, 108%, and 51.9% with 40% depth and 162%, 152.5%, and 92.3% with 60% depth with a varying flow rate of 4, 8, and 12 LPH, respectively, in contrast to traditional solar still. The improvement in energy and exergy efficiency for distilled water output is gained between 40-22.2% and 0.7-4.1%, respectively, with the designed system. However, the system's energy and exergy efficiency lie between 64.8-42.4% and 28.4-16.4%, respectively, for both distilled water and hot water productivity. The 8 LPH flow rate is found optimum in terms of distilled productivity and hot water production. The designed system's distilled water and hot water unit costs are 0.1037$ and 0.0276$, respectively. [GRAPHICS] .
引用
收藏
页码:8969 / 8989
页数:21
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