An experimental investigation on a crushing and washing-free freezing desalination system based on brine extraction during melting
被引:4
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作者:
Rashad, Muhammad I.
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Alexandria Univ, Fac Engn, Dept Math & Phys Engn, Alexandria, EgyptAlexandria Univ, Fac Engn, Dept Math & Phys Engn, Alexandria, Egypt
Rashad, Muhammad I.
[1
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Farahat, Mohamed A.
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机构:
Menoufia Univ, Fac Engn, Mech Power Eng Dept, El Menofia 32511, EgyptAlexandria Univ, Fac Engn, Dept Math & Phys Engn, Alexandria, Egypt
Farahat, Mohamed A.
[2
]
Faiad, Hend A.
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SUBZERO PURE llc, Houston, TX 77082 USAAlexandria Univ, Fac Engn, Dept Math & Phys Engn, Alexandria, Egypt
Faiad, Hend A.
[4
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Ahmed, Shehab
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King Abdullah Univ Sci & Technol, CEMSE Div, Thuwal 23955, Saudi Arabia
SUBZERO PURE llc, Houston, TX 77082 USAAlexandria Univ, Fac Engn, Dept Math & Phys Engn, Alexandria, Egypt
Ahmed, Shehab
[3
,4
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机构:
[1] Alexandria Univ, Fac Engn, Dept Math & Phys Engn, Alexandria, Egypt
[2] Menoufia Univ, Fac Engn, Mech Power Eng Dept, El Menofia 32511, Egypt
[3] King Abdullah Univ Sci & Technol, CEMSE Div, Thuwal 23955, Saudi Arabia
Freezing desalination has regained attention due to its potential to lower energy usage compared to other methods. However, the freezing technology faces major challenges that hinder its commercialization. One is the significant mass loss due to washing the product's ice. Also, most freezing systems require a crushing stage to obtain the desired ice, limiting mass production. This work proposes a freezing desalination system based on brine extraction during melting. The proposed system can use multiple stages of a brine extraction and can be implemented using multiple cycles of the full process. The experiments were carried out at different feed water salinities. The results have shown that the system has the potential to produce low-salinity water with a relatively low number of stages and without the need for washing or crushing. To get product water at 90 ppm from 45000 ppm feed water, the system requires 3, 4, and 7 cycles (of the full process) for three, two, and single stages of brine extraction, respectively. When considering recovery rates between 60 and 90%, specific energy con-sumption is reduced to a range of 15-89 kWhr/m3 with COP from 4 to 6, respectively.
机构:
Diyala Univ, Coll Engn, Dept Elect Engn, Diyala, IraqMinist Elect, State Co Elect Prod Northern Reg, Baiji 34007, Iraq
Mohammed, Khalid G.
Kamil, Mohammed
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机构:
Univ Sharjah, Mech & Nucl Engn Dept, POB 27272, Sharjah, U Arab Emirates
Univ Sharjah, Res Inst Sci & Engn, Sustainable Energy Dev Res Grp, Sharjah, U Arab EmiratesMinist Elect, State Co Elect Prod Northern Reg, Baiji 34007, Iraq
机构:
Minist Elect, Training & Energy Res Off, Baghdad, IraqMinist Elect, State Co Elect Prod Northern Reg, Baiji 34007, Iraq
Kasim, Naseer K.
Tahseen, Tahseen Ahmad
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机构:
Kirkuk Univ, Coll Engn, Dept Mech Engn, Kirkuk, IraqMinist Elect, State Co Elect Prod Northern Reg, Baiji 34007, Iraq
Tahseen, Tahseen Ahmad
Awad, Omar, I
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机构:
Tsinghua Univ, State Key Lab Automot Safety & Energy, Beijing, Peoples R ChinaMinist Elect, State Co Elect Prod Northern Reg, Baiji 34007, Iraq
Awad, Omar, I
Mekhilef, Saad
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机构:
Univ Malaya, Dept Elect Engn, Power Elect & Renewable Energy Res Lab PEARL, Kuala Lumpur, MalaysiaMinist Elect, State Co Elect Prod Northern Reg, Baiji 34007, Iraq