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Hybrid Membrane Plant Design and Operation

Project name DI Water RO system Permeate flow 53.00 tn/h [Pg.285]

HP pump flow Recommended pump pressure 70.7 mVh 8.0 bar Raw water flow 70.7 mVh [Pg.285]

Feed pressure Feed water temperature 6.0 bar 25.0°C (77°F) Permeate recovery ratio 75.0% [Pg.285]

Acid dosage, ppm (100%) 0.0 H2SO4 Flux decline % per year 7.0 [Pg.285]

Acidified feed CO2 4.2 Salt passage increase, % per year 10.0 [Pg.285]

Membrane systems can also be integrated into traditional units. The design of a hybrid membrane separation system is determined by several considerations, such as membrane permeance and selectivity, CO2 concentration of the inlet gas and the target required, the gas value (per ca. 30 N m, the price of gas in 2007 was 6- 7 in the United States, whereas in Nigeria, which is far from being well-developed gas market, it may be as low as 0.50 if the gas can be used at all), and the location of the plant (on an offshore platform, the weight, footprint, and simplicity of operation are critical onshore, the total cost is more significant). ... [Pg.81]

See other pages where Hybrid Membrane Plant Design and Operation is mentioned: [Pg.283]    [Pg.285]    [Pg.287]    [Pg.289]    [Pg.291]    [Pg.293]    [Pg.295]    [Pg.305]    [Pg.309]    [Pg.311]    [Pg.313]    [Pg.319]    [Pg.323]    [Pg.325]    [Pg.329]    [Pg.331]    [Pg.333]    [Pg.335]    [Pg.283]    [Pg.285]    [Pg.287]    [Pg.289]    [Pg.291]    [Pg.293]    [Pg.295]    [Pg.305]    [Pg.309]    [Pg.311]    [Pg.313]    [Pg.319]    [Pg.323]    [Pg.325]    [Pg.329]    [Pg.331]    [Pg.333]    [Pg.335]    [Pg.283]    [Pg.283]    [Pg.283]    [Pg.282]    [Pg.78]    [Pg.494]    [Pg.15]    [Pg.232]    [Pg.426]   


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Design and operation

Hybrid operation

Hybrid plants

Membrane hybridization

Membrane operation

Membranes design

Plant design

Plant design and operation

Plant operation

Plant operators

Plants hybridization

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