Abstract:Membrane technology with advantages such as reduced energy consumption due to no phase change, low volume and high mass transfer, high separation efficiency for solution solutions, straightforward design of membranes, and ease of use on industrial scales are different from other separation methods. There are various methods such as liquid–liquid extraction, adsorption, precipitation, and membrane processes to separate contaminants from an aqueous solution. The liquid membrane technique provides a practical and… Show more
“…The electron charge, the charge of the soft layer species, the charge density of the functional groups in the soft layer, the soft layer’s friction coefficient, and the charge and concentration of the moving ionic species are represented by e , Z PEL , N PEL , γ, z j , and c j , respectively. The Faraday constant, global gas constant, and absolute temperature of the system are represented by F , R , and T , respectively. ,, In the expressed equations, i is equal to either 0, 1, or 2, to indicate that a parameter is outside the soft layer (0), the positive charge of soft layer (1), and the negative charge of soft layer (2) …”
Section: Theorymentioning
confidence: 99%
“…The Faraday constant, global gas constant, and absolute temperature of the system are represented by F, R, and T, respectively. 5,6,43 In the expressed equations, i is equal to either 0, 1, or 2, to indicate that a parameter is outside the soft layer (0), the positive charge of soft layer (1), and the negative charge of soft layer (2). 8 Equations 1−4 are solved using the boundary conditions shown in Figure 2a, where E.P stands for the electrostatic equation (eq 1), I.M.T stands for the mass transfer of ionic species equation (eq 2), and F.F stands for fluid flow equations (eqs 3 and 4).…”
Researchers are looking for new, clean, and accessible
sources
of energy due to rising global warming caused by the usage of fossil
fuels and the irreversible harm that this does to the environment.
Water salinity is one of the newest and most accessible renewable
energy sources, which has sparked a lot of interest. Reverse electrodialysis
(RED) has been utilized in the past to turn saline water into electricity.
NRED, a reverse electrodialysis method utilizing nanofluidics, has
gained popularity as nanoscale research advances. Developing and evaluating
NRED systems is time-consuming and expensive due to the method’s
novelty; thus, modeling is required to identify the best locations
for implementation and to comprehend its workings. In this work, we
examined the influence of bipolar soft layer and nanochannel geometry
on ion transfer and power production simultaneously. To achieve this,
the two trumpet and cigarette geometries were coated with a bipolar
soft layer so that both negative (type (I)) and positive (type (II))
charges could be positioned in the nanochannel’s small aperture.
After that, at steady state conditions, the Poisson–Nernst–Planck
(PNP) and Navier–Stokes (NS) equations were solved concurrently.
The findings revealed that altering the nanochannel coating from type
(I) to type (II) alters the channel’s selectivity from cations
to anions. An approximately 22-fold improvement in energy conversion
efficiency was achieved by raising the concentration ratio from 10
to 100 for the type (I) trumpet nanochannel. Type (I) cigarette geometry
is advised for maximum power output at low and medium concentration
ratios, whereas type (I) trumpet geometry is recommended for the maximum
power production at high concentration ratios.
“…The electron charge, the charge of the soft layer species, the charge density of the functional groups in the soft layer, the soft layer’s friction coefficient, and the charge and concentration of the moving ionic species are represented by e , Z PEL , N PEL , γ, z j , and c j , respectively. The Faraday constant, global gas constant, and absolute temperature of the system are represented by F , R , and T , respectively. ,, In the expressed equations, i is equal to either 0, 1, or 2, to indicate that a parameter is outside the soft layer (0), the positive charge of soft layer (1), and the negative charge of soft layer (2) …”
Section: Theorymentioning
confidence: 99%
“…The Faraday constant, global gas constant, and absolute temperature of the system are represented by F, R, and T, respectively. 5,6,43 In the expressed equations, i is equal to either 0, 1, or 2, to indicate that a parameter is outside the soft layer (0), the positive charge of soft layer (1), and the negative charge of soft layer (2). 8 Equations 1−4 are solved using the boundary conditions shown in Figure 2a, where E.P stands for the electrostatic equation (eq 1), I.M.T stands for the mass transfer of ionic species equation (eq 2), and F.F stands for fluid flow equations (eqs 3 and 4).…”
Researchers are looking for new, clean, and accessible
sources
of energy due to rising global warming caused by the usage of fossil
fuels and the irreversible harm that this does to the environment.
Water salinity is one of the newest and most accessible renewable
energy sources, which has sparked a lot of interest. Reverse electrodialysis
(RED) has been utilized in the past to turn saline water into electricity.
NRED, a reverse electrodialysis method utilizing nanofluidics, has
gained popularity as nanoscale research advances. Developing and evaluating
NRED systems is time-consuming and expensive due to the method’s
novelty; thus, modeling is required to identify the best locations
for implementation and to comprehend its workings. In this work, we
examined the influence of bipolar soft layer and nanochannel geometry
on ion transfer and power production simultaneously. To achieve this,
the two trumpet and cigarette geometries were coated with a bipolar
soft layer so that both negative (type (I)) and positive (type (II))
charges could be positioned in the nanochannel’s small aperture.
After that, at steady state conditions, the Poisson–Nernst–Planck
(PNP) and Navier–Stokes (NS) equations were solved concurrently.
The findings revealed that altering the nanochannel coating from type
(I) to type (II) alters the channel’s selectivity from cations
to anions. An approximately 22-fold improvement in energy conversion
efficiency was achieved by raising the concentration ratio from 10
to 100 for the type (I) trumpet nanochannel. Type (I) cigarette geometry
is advised for maximum power output at low and medium concentration
ratios, whereas type (I) trumpet geometry is recommended for the maximum
power production at high concentration ratios.
“…With the use of an external circuit, the diffusion current can be converted to an electric current. [38][39][40] With respect to the advancement of RED technology, nanoscale systems are attracting increasing attention from researchers primarily due to their higher power density than conventional systems. To understand how micro-/nanosystems activate as well as promote RED, researchers have conducted numerous experimental and theoretical studies.…”
Section: Introductionmentioning
confidence: 99%
“…With the use of an external circuit, the diffusion current can be converted to an electric current. 38–40…”
Salinity energy generation (SEG) studies have only been done under isothermal conditions at ambient temperature. The production of salinity energy can be improved under non-isothermal conditions, albeit preserving the energy...
“…Therefore, whether liquid sheeting technology can operate in a closed manner will be the focus of the research. The volatilization of the organic sheeting fluid is controlled, which can improve the dislodging percentage and stability [ 34 ].…”
A novel diphasic sheeting device (DSD) including complemental feeding stage and complemental disintegrating stage for dislodging features of Cd(II), was investigated. The complemental feeding stage included feeding liquor and Bis(2,4,4 trimethylamyl) dithiophosphonic acid (Cyanex-301) as the carrier in petroleum, and the complemental disintegrating stage included Cyanex-301 as the carrier in petroleum and hydrochloric acid as the disintegrating reagent. The impacts of volumetric ratio of sheeting liquor and feeding liquor(S/F), initial molarity of Cd(II) and ion intensity of the feeding liquor, pH, volumetric ratio of sheeting liquor and disintegrating reagent (S/D), molarity of hydrochloric acid liquor, Cyanex-301 molarity in the complemental disintegrating stage on dislodging of Cd(II), the virtues of DSD compared to the traditional sheeting device, the constancy of system, the reuse of sheeting liquor, and the retention of the sheeting stage were also investigated. Experimental results illustrated that the optimum dislodging conditions of Cd(II) were achieved as hydrochloric acid molarity was 4.00 mol/L, Cyanex-301 molarity was 0.150 mol/L, and S/D was 1:1 in the complemental disintegrating stage, S/F was 1:10, and pH was 5.00 in the complemental feeding stage. The ion intensity of the complemental feeding stage had no distinct impact on the dislodging feature of Cd(II). When initial Cd(II) molarity was 3.20 × 10−4 mol/L, the Cd(II) dislodging percentage was up to 92.9% in 210 min. The dynamic formula was inferred on the basis of the theorem of mass transferring and the interfacial chemistry.
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