1998
DOI: 10.1016/s0011-9164(98)00079-4
|View full text |Cite
|
Sign up to set email alerts
|

A new approach to membrane and thermal seawater desalination processes using nanofiltration membranes (Part 1)

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

0
59
0

Year Published

2008
2008
2019
2019

Publication Types

Select...
5
3
1

Relationship

0
9

Authors

Journals

citations
Cited by 196 publications
(60 citation statements)
references
References 9 publications
0
59
0
Order By: Relevance
“…7.5 -9.5 Source: [18,36,55,56,87,88] It is assumed that cleaning or replacement takes place simultaneously for all passes, there are no pressure losses from pump to membrane, every pass contains the same number of membrane modules, = 2000, cleaning is performed every 6 months, replacement is recommended every 5 years, and the annual operation is 300 days a year (Table 3). The electricity charge, , has a value of 0.08 $/kWh to accommodate any future increments from the U.S Energy Information Administration [91] review and to consider literature values [36].…”
Section: Given Datamentioning
confidence: 99%
“…7.5 -9.5 Source: [18,36,55,56,87,88] It is assumed that cleaning or replacement takes place simultaneously for all passes, there are no pressure losses from pump to membrane, every pass contains the same number of membrane modules, = 2000, cleaning is performed every 6 months, replacement is recommended every 5 years, and the annual operation is 300 days a year (Table 3). The electricity charge, , has a value of 0.08 $/kWh to accommodate any future increments from the U.S Energy Information Administration [91] review and to consider literature values [36].…”
Section: Given Datamentioning
confidence: 99%
“…NF membranes extend the applications of membrane processes and are considered promising for many future applications, including water treatment, wastewater reuse [1], and desalination applications [2]. Moreover, NF membrane processes have many desirable features such as low operation pressure, high flux, high retention of multivalent anion salts and dissolved organic molecular compounds [3] with relatively low molecular weight (200-1,000 g mol −1 ), relatively low investment, operation, and low maintenance costs.…”
Section: Introductionmentioning
confidence: 99%
“…The NF270 membrane had a rejection between 11 and 29 %, while the NF30 membrane had rejections ranging from 3 to 6 %. Hassan et al (1998) used NF as a pretreatment to RO for seawater and found that Ca 2? decreased from 481 to 93 mg/L, Mg 2?…”
Section: Nanofiltrationmentioning
confidence: 99%