ライフサイエンスコーパス: osmosis

1 be a next generation membrane for engineered osmosis.

2 ge and viscous drag forces caused by electro-osmosis.

3 ld a next generation membrane for engineered osmosis.

4 for treatment of brackish water than reverse osmosis.

5 this in turn drives water transport by local osmosis.

6 nd Cl(-) transport and the water flux due to osmosis.

7 sed on Hulett's view, the only valid view of osmosis.

8 kinetically selective organic liquid reverse osmosis.

9 anced Treatment trains incorporating reverse osmosis.

10 ges to induce liquid crystal-enabled electro-osmosis.

11 s research has demonstrated that the reverse osmosis and advanced oxidation processes (AOPs) used to

12 crater have included evaporite dissolution, osmosis and evaporation from heating associated with the

13 Because of this observation, reverse osmosis and FO tests that are commonly used for measurin

14 fluent, two types of recycled water (reverse osmosis and ozonation/activated carbon filtration), stor

15 ing energy from sea water: pressure-retarded osmosis and reverse electrodialysis.

16 Fouling experiments in both forward osmosis and reverse osmosis modes are performed with thr

17 gmaurea) was measured by independent induced osmosis and solvent drag methods.

18 Hulett's understanding of osmosis and the means by which the water was altered by

19 mpulse conduction that appear to result from osmosis and to indicate accumulation of ions in the peri

20 oplastics that are commonly used for reverse osmosis and water purification membranes, medical equipm

21 st physical principles of electroneutrality, osmosis, and conservation of particles or a combination

22 xchange membranes (namely, co-ion transport, osmosis, and electro-osmosis) can detrimentally lower ef

23 e study of fluid transport, shows that local osmosis best accounts for water movement.

24 challenge, as their growth is influenced by osmosis, buoyancy, and reaction-diffusion processes.

25 Yet if osmosis can explain some anomalies, there is no need to

26 But whether osmosis can have a significant effect on the pressure of

27 mely, co-ion transport, osmosis, and electro-osmosis) can detrimentally lower efficiency by up to 26%

28 The movement of water by osmosis causes pressure differences that drive the trans

29 minants in industrial wastewater and reverse osmosis concentrate from municipal wastewater recycling

30 Additionally, reverse osmosis desalination experiments in a cross-flow system

31 e membrane filter (RCNT-MF), for the reverse osmosis desalination that can turn salt water into fresh

32 is (e.g., forward osmosis, pressure-retarded osmosis, direct osmosis) has emerged as a new platform f

33 active sodium absorption plays a key role in osmosis-driven fluid uptake.

34 Moreover, an osmosis-driven process for encapsulation of proteins in

35 and the plasma membrane results in anomalous osmosis during pressure clamp measurements.

36 y colleagues, and the literature and through osmosis during seminars and scientific meetings.

37 Engineered osmosis (e.g., forward osmosis, pressure-retarded osmosi

38 ith their analog separation process (reverse osmosis, electrodialysis, and capacitive deionization, r

39 les isolated using the novel coupled reverse osmosis/electrodialysis method.

40 transport due to the combination of electro-osmosis, electrophoresis, and inherent pressure.

41 the major challenge that hinders engineered osmosis (EO) development.

42 By mitigating osmosis, faradaic and round-trip energy efficiency are m

43 In fertilizer-drawn forward osmosis (FDFO) desalination, the final nutrient concentr

44 lutions hindered competition between forward osmosis (FO) and pressure retarded osmosis (PRO) with ex

45 driven membrane processes (including forward osmosis (FO) and pressure retarded osmosis (PRO)) have r

46 ite (TFC) hollow fiber membranes for forward osmosis (FO) applications is presented in this study.

47 s via interfacial polymerization for forward osmosis (FO) applications.

48 VC), membrane distillation (MD), and forward osmosis (FO) as the technologies best suited for desalin

49 reverse divalent cation diffusion in forward osmosis (FO) biofouling.

50 Forward osmosis (FO) desalination technology is emerging for fre

51 igated the feasibility of applying a forward osmosis (FO) dewatering process for nutrient recovery fr

52 Forward osmosis (FO) has attracted wide attention in recent year

53 Forward osmosis (FO) has been recognized in recent years as a ro

54 Forward osmosis (FO) is an emerging membrane process with potent

55 Forward osmosis (FO) is an emerging membrane separation process

56 In the process, a forward osmosis (FO) membrane and a microfiltration (MF) membran

57 m uses both ultrafiltration (UF) and forward osmosis (FO) membranes in parallel to simultaneously ext

58 ectrode in thin-film composite (TFC) forward osmosis (FO) membranes.

59 and the performance was evaluated in forward osmosis (FO) mode with various feed solutions: nanopure

60 e irreversible membrane fouling in a forward osmosis (FO) process.

61 Forward osmosis (FO) was applied as an "osmotic concentration" p

62 For the first time, forward osmosis (FO) was performed using a porous membrane with

63 mperature (UCST) as a draw solute in forward osmosis (FO) was successfully demonstrated here experime

64 Unlike forward osmosis (FO), an important feature of PRO is the applica

65 m combining electrodialysis (ED) and forward osmosis (FO), driven by renewable energy (solar energy),

66 bustness and treatment capacity of a forward osmosis (FO)-membrane distillation (MD) hybrid system fo

67 nes that translate the advantages of reverse osmosis for aqueous separations to the separation of org

68 ing considered as a key component of reverse osmosis-free advanced treatment trains for potable waste

69 In the FO stream, water is drawn by osmosis from activated sludge through an FO membrane int

70 organic matter that was isolated by reverse osmosis from the Suwannee River in southeastern Georgia.

71 esponse to different urea gradients (induced osmosis) gave sigmaurea approximately 0.3 for the UT3 pa

72 on application of an electric field, electro-osmosis generates bulk fluid flow in the device, and a p

73 of energy storage, the transport of water by osmosis has a very significant negative impact on the fa

74 Electroosmotic flow (EOF) or electro-osmosis has been shown to exhibit a hysteresis effect un

75 d osmosis, pressure-retarded osmosis, direct osmosis) has emerged as a new platform for applications

76 Recently developed electro-osmosis-inhibiting matrix polymers have simplified the p

77 icrograms/ml amphotericin B, indicating that osmosis is not limited by unstirred layers.

78 pilot-level trials using 1kD, loose reverse osmosis (LRO) and reverse osmosis (RO) spiral-wound memb

79 We report a hybrid microfiltration-forward osmosis membrane bioreactor (MF-FOMBR) for direct phosph

80 aromatic polyamide active layer of a reverse osmosis membrane upon exposure to free chlorine was quan

81 aromatic polyamide active layer of a reverse osmosis membrane upon exposure to free chlorine.

82 ough an asymmetric cellulose acetate forward osmosis membrane.

83 oncept of a polyelectrolyte-promoted forward osmosis-membrane distillation (FO-MD) hybrid system was

84 of polyamide (PA) nanofiltration and reverse osmosis membranes by chlorine needs to be understood in

85 t of water across apposing liquid menisci in osmosis membranes comprising short hydrophobic nanopores

86 superhydrophilic thin-film composite forward osmosis membranes functionalized with surface-tailored n

87 layers are deposited onto commercial reverse osmosis membranes without damaging them and they exhibit

88 ranes is particularly outstanding in forward osmosis mode where the driving force for water flux is a

89 When operated in forward osmosis mode, the GO membrane exhibited fouling performa

90 eriments in both forward osmosis and reverse osmosis modes are performed with three model organic fou

91 amide membranes, in both reverse and forward osmosis modes.

92 and expand gradually to their full size via osmosis of surrounding tissue fluid, with up to a 10-fol

93 there is no direct evidence for either local osmosis or aquaporin gene expression in enterocytes.

94 nland brackish water desalination by reverse osmosis or RO, concentrate or reject disposal poses a ma

95 Engineered osmosis (e.g., forward osmosis, pressure-retarded osmosis, direct osmosis) has

96 Pressure retarded osmosis (PRO) and reverse electrodialysis (RED) are emer

97 Next-generation pressure-retarded osmosis (PRO) approaches aim to harness the energy poten

98 inable energy by combining pressure-retarded osmosis (PRO) as a power generation stage and membrane d

99 stigate the performance of pressure retarded osmosis (PRO) at the module scale, accounting for the de

100 Osmotic power generated by pressure-retarded osmosis (PRO) has attracted global attention as a clean,

101 Pressure retarded osmosis (PRO) has the potential to produce clean, renewa

102 Pressure-retarded osmosis (PRO) is a promising source of renewable energy

103 Pressure retarded osmosis (PRO) is one of the methods proposed to generate

104 on tested under the FO and pressure retarded osmosis (PRO) modes, respectively, while consistently ma

105 lution tested under FO and pressure retarded osmosis (PRO) modes, respectively, while maintaining low

106 high power density in the pressure-retarded osmosis (PRO) process experimentally and theoretically.

107 power generation with the pressure-retarded osmosis (PRO) process.

108 smotic power generation by pressure-retarded osmosis (PRO) processes, fouling on PRO membranes must b

109 e practical application of pressure retarded osmosis (PRO) technology for renewable blue energy (i.e.

110 n forward osmosis (FO) and pressure retarded osmosis (PRO) with existing water purification and power

111 g forward osmosis (FO) and pressure retarded osmosis (PRO)) have received increasing attention in rec

112 ane for fouling control in pressure-retarded osmosis (PRO), an emerging engineered osmosis process wh

113 he foremost technologies - pressure retarded osmosis (PRO), reverse electrodialysis (RED), and capaci

114 al technologies, including pressure-retarded osmosis (PRO), reverse electrodialysis (RED), and capaci

115 by thermal separation, and pressure retarded osmosis (PRO), which converts the energy of mixing to el

116 cers on the performance of pressure retarded osmosis (PRO).

117 that can be achieved using pressure-retarded osmosis (PRO).

118 y using a process known as pressure-retarded osmosis (PRO).

119 ning the centrifugal force propelled reverse osmosis process and the porous CNT-based fine scale sele

120 r polymer hydrogels as draw agent in forward osmosis process has been investigated.

121 their advantages as draw solutes in forward osmosis process in terms of high water flux, minimum rev

122 tarded osmosis (PRO), an emerging engineered osmosis process whose advancement has been much hindered

123 re energy-efficient than the current reverse osmosis process.

124 agent in the polymer hydrogel-driven forward osmosis process.

125 or GR activity attenuation; however, reverse osmosis removed GR activity to levels below the limits o

126 Hulett's theory of osmosis requires that the solute alter the water at the

127 ty in the polyamide active layers of reverse osmosis (RO) and nanofiltration (NF) membranes, to predi

128 As reverse osmosis (RO) and nanofiltration polyamide membranes beco

129 nown to be insufficiently removed by reverse osmosis (RO) and nanofiltration polyamide membranes that

130 Reverse osmosis (RO) as a potential technique to improve the ant

131 In this work, a high-performance reverse osmosis (RO) composite thin membrane using multi-walled

132 s a promising way to improve current reverse osmosis (RO) concentrate treatment processes and enables

133 energy consumption (SEC) in seawater reverse osmosis (RO) desalination due to improvements made in hy

134 is a major operational challenge in reverse osmosis (RO) desalination, motivating a search for impro

135 designed and constructed to evaluate reverse osmosis (RO) energy reduction that can be achieved using

136 Reverse osmosis (RO) membrane fouling is not a static state but

137 ely enhanced nanofiltration (NF) and reverse osmosis (RO) membrane permeate flux and salt rejection r

138 and separation on a typical seawater reverse osmosis (RO) membrane.

139 n of a thin-film composite polyamide reverse osmosis (RO) membrane.

140 The top polyamide layer of composite reverse osmosis (RO) membranes has a fascinatingly complex struc

141 Swelling of the active layer of reverse osmosis (RO) membranes has an important effect on permea

142 s into the polyamide active layer of reverse osmosis (RO) membranes is one of the three membrane prop

143 ts, applied to control biofouling of reverse osmosis (RO) membranes, result in membrane performance d

144 imethylamine (NDMA) by six different reverse osmosis (RO) membranes, suggesting that boron can be use

145 and development of biofilm bodies on reverse osmosis (RO) membranes.

146 nts such as ultrafiltration (UF) and reverse osmosis (RO) on dissolved organic matter (DOM) is still

147 The AOP treatment of reverse osmosis (RO) permeate often includes the de facto UV/chl

148 Nanofiltration (NF) and reverse osmosis (RO) processes are used for drinking water purif

149 Reverse osmosis (RO) seawater desalination is currently a widesp

150 1kD, loose reverse osmosis (LRO) and reverse osmosis (RO) spiral-wound membranes showed LRO membrane

151 A reverse osmosis (RO) system is then used to reconcentrate the di

152 d biofilm formation in a bench-scale reverse osmosis (RO) system using the same feedwater.

153 dimethylamine (NDMA) passing through reverse osmosis (RO) units within advanced treatment trains for

154 Yet, reverse osmosis (RO), which is the most widely used for desalina

155 other organic matter (OM) isolates (reverse osmosis, RO; and "transphilic", XAD-4) from several rive

156 es new mechanism of highly efficient electro-osmosis rooted in space charging of regions with distort

157 n comparison with original water and reverse osmosis samples.

158 tage enhanced tertiary processes and reverse osmosis, simultaneously increased eutrophication indirec

159 ry compared with a combined OMBR and reverse osmosis system.

160 zed, agitated, electrodialysis, and reversed osmosis systems in design and theory.

161 ological model which includes water entry by osmosis, the incorporation of cell wall material and the

162 k (MOF) for mitigating biofouling in forward-osmosis thin-film composite (TFC) membranes.

163 formed to study the rates of AS transfer and osmosis through the membrane, and the operational parame

164 R) is an emerging technology that uses water osmosis to accomplish separation of biomass from the tre

165 microfiltration/ultrafiltration and reverse osmosis utilize porous membranes to remove suspended par

166 es,'artificial muscle' actuators and reverse-osmosis water purifiers.

167 e MWF) and one non-MCC isolate (from reverse osmosis water).

168 ater, deionised water, spring water, reverse osmosis water, and distilled water at 95 degrees C, and

169 a also perturbs epithelial ion transport and osmosis, which may be important for the long-term surviv