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Recent Progress in Qantum Dots Containing Thin Film Composite Membrane for Water Purification

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Online ISSN: 2288-7253 DOI: https://doi.org/10.14579/MEMBRANE_JOURNAL.2020.30.5.293

1. Introduction 1)

Demand for clean freshwater is increasing as the consequences of climate change continue to take its toll

around the world and more and more contaminants are finding their way into water sources. There has been great potential to improve the performance of semi- permeable membranes to filter water as a portion of

Corresponding author(e-mail: [email protected], http://orcid.org/0000-0002-3820-141X)

양자점이 합체된 복합 박막을 이용한 정수의 최근 발전

박 신 영ㆍ라즈쿠마 파텔

*

,†

연세대학교 언더우드국제대학 융합과학공학부 나노과학공학,

*

연세대학교 언더우드국제대학 융합과학공학부 에너지환경과학공학

(2020년 10월 8일 접수, 2020년 10월 21일 수정, 2020년 10월 22일 채택)

Recent Progress in Qantum Dots Containing Thin Film Composite Membrane for Water Purification

Shinyoung Park and Rajkumar Patel *

,†

Nano Science and Engineering, Integrated Science and Engineering Division (ISED), Underwood International College, Yonsei University, 85 Songdogwahak-ro, Yeonsu-gu, Incheon 21983, South Korea

*Energy and Environmental Science and Engineering (EESE), Integrated Science and Engineering Division (ISED), Underwood International College, Yonsei University, 85 Songdogwahak-ro, Yeonsu-gu, Incheon 21983, South Korea

(Received October 8, 2020, Revised October 21, 2020, Accepted October 22, 2020)

요 약: 물 부족을 포함한 기후 변화의 해로운 결과는 효과적인 정수에 대한 관심을 가져왔다. 또한, 수질 오염 수준이 높 아지고 환경 파괴 수준이 심해지면서 오염 물질을 제거하려는 방안들이 요구되고 있다. 물을 정화하기 위해 반투막을 통한 삼투압 절차들을 사용할 수 있으며, 최근 연구에 따르면 탄소 양자점(CQD), 그래핀 양자점(GQD) 및 산화 그래핀 양자점 (GOQD)을 포함한 나노입자를 복합 박막(TFC)에 합체하면 유사한 수준의 염 거부율을 유지하면서 물흐름을 증가시킬 수 있 다. 이러한 효과 외의 여러 가지 효과가 있지만 그 중에서도 친수성을 높이고, 살균 성질을 보이고, 방오 특성으로 인해 박테 리아 및 기타 미생물의 축적을 방지하면서 막의 효과가 감소하는 것을 막는 것을 보여준다. 이 보고서는 양자점이 합체된 정 수용 복합 막에서 양자점의 제조 과정, 응용, 기능성, 성질 및 역할을 논의한다.

Abstract: Increasing harmful effects of climate change, such as its effect on water scarcity, has led to a focus on developing effective water purification methods to obtain pure water. Additionally, rising levels of water pollution is increasing levels of environmental degradation, calling for sources of water treatment to remove contaminants. To purify water, osmotic processes across a semipermeable membrane can take place, and recent studies are showing that incorporating nanoparticles, including carbon quantum dots (CQDs), graphene carbon dots (GQDs), and graphene oxide quantum dots (GOQDs) are making thin film composite (TFC) membranes more effective by increasing water flux while maintaining similar levels of salt rejection, increasing the hydrophilicity of the membrane surface, showing bactericidal properties, exhibiting antifouling properties to prevent accumulation of bacteria or other microorganisms from reducing the effectiveness of the membrane, and more. In the review, the synthesis process, applications, functionality, properties, and the role of several types of quantum dots are discussed in the composite membrane for water purification.

Keywords: thin film composite membrane; carbon quantum dots, graphene quantum dots; desalination, hollow

fiber membrane

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the nanoparticles studied before had shown to be not very compatible nor have good dispersibility in the pol- yamide (PA) layer of thin film nanocomposite (TFN) membranes[1-19]. TFC membranes, the precursor to TFN membranes before quantum dot (QD) loading, can be formed through the interfacial polymerization method using both trimesoyl chloride (TMC) and piperazine (PIP). CQDs, GQDs, or GOQDs, are generally found to be synthesized through the direct pyrolysis or heat- ing of citric acid (CA) and would then be incorporated onto TFC membranes at differing weight percentages to determine the effectiveness of the newly-formed TFN membranes regarding a variety of factors compared to the initial TFC membranes.

TFN membranes can be used in water purification by a variety of membrane separation processes including forward osmosis reverse osmosis. Forward osmosis has the benefit of being a natural process where the water flows through the membrane because of a natural con- centration gradient, but the effectiveness in the solute separation from pure water could be lower than reverse osmosis. Reverse osmosis has the benefit of being able to force water through a membrane to separate it from the solutes initially dissolved in it regardless of con- centration gradient, but it requires high pressure; thus, it requires much more energy than forward osmosis processes. After the incorporation of QDs onto mem- branes for a certain membrane separation process, the performance of the membrane generally improved. To give an example, for an ultrafiltration (UF) process, one type of QDs, GOQDs, was shown to act as good nano- fillers based on the antifouling capability, permeability, and hydrophilicity on polysulfone (PSF) UF membranes after GOQD loading[30]. Additionally, by changing the process in which CQDs are made, the size and the functional groups of CQDs can differ, making them have different properties. According to which proper- ties are desired for a certain application, one can adjust the synthesis process to get the desired size and prop- erties of CQDs. The incorporation of quantum dots in- to the PA layer has shown unique characteristics in changing the properties of the membrane, such as de-

creasing the roughness of the surface, increasing hy- drophilicity of the PA layer, increasing the water flux, and displaying improved antifouling performance over- all when graphene quantum dots (GQDs) are incorpo- rated into the membrane, indicating the potential of quantum dots in this area[19]. Functionalizing CQDs with Na

+

ions were shown to have even better pure water permeability and water flux than regular CQDs while maintaining a similar percentage of salt rejection.

QDs are so versatile that they are finding applications in other areas besides water filtration. Not only can QDs be used in water treatment, but when applied to TFN hollow fiber membranes in pressure retarded os- mosis (PRO), it has displayed better osmotic power generation[20]. Greater power density was reported for TFC membranes incorporated with Na-CQDs than ones without them. QDs also found application in solvent-re- sistant nanofiltration for the separation of organic mix- tures and in direct methanol fuel cells (DMFCs) to im- prove their performance. DMFCs with CQDs showed increased peak power density, electro-chemical selectivity, proton conductivity, and more compared to their coun- terparts without CQDs. One category of QDs, GOQDs, have polar functional groups that are oxygenated, and can be even used for dehydration[21]. Loading silver ions (Ag

+

) with GOQDs onto a PA layer was also shown to improve the bactericidal property of the membrane [22], even though incorporation of QDs already made the membrane less prone to antifouling.

2. Quantum Dots

Quantum dots are 0D nanoparticles that are less than 10 nm in size and exhibit novel properties.

2.1. Graphene quantum dots

For the synthesis of GQDs that would be incorporated

into TFN membranes, CA was decomposed thermally

by putting it into a crucible and heating it for 15 min

at 200°C in an electric oven[19]. The solid citric acid

turned into liquid during thermal treatment and GQDs

formed through certain forces operating at the nano-

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Fig. 1. Schematic diagram of the quantum dots embedded thin film composite membrane.

scale from the molecules that were decomposed from citric acid. For the membranes, initially poly(ether sul- fone) support membranes were prepared through non-sol-

vent induced phase separation (NIPS). These membranes were then turned into several different PIP - TMC TFN membranes with varying levels of GQD incorporation through the method of interfacial polymerization. This method of polymerization was done at the interface of PIP and TMC to create a PA layer. More specifically, the support membranes were first immersed into aque- ous solutions that had 0.1% PIP by weight percentage (wt) and varying amounts of GQDs. Then, the mem- branes were taken out and any excess liquid was re- moved. After this, the membranes were dipped in a 0.1 wt% TMC/n-heptane solution for two minutes, forming a polyamide layer. To evaporate the n-heptane fully and

Thin layer of

TFC

Monomer (Diamine)

Monomer

(Acid chloride) Filler Pristine polymer water flux

(L/m2ㆍh) Reference

Polyamide PIP TMC GQDs 15.0 [19]

Polyamide MPD TMC CQDs and Na+

functionalized CQDs 66.59 when P = 0 [20]

Sodium alginate

(SA) - - GOQDs 149,644 (g m2 h) [21]

Polyamide MPD TMC GOQDs loaded with

silver phosphate 25.8 [22]

Polyamide MPD TMC GQDs 15~20 for 0.5

draw solution concentration [23]

Polyamide PEI TMC GQDs 6~7.5 [24]

Tannic acid (TA) - - GOQDs 15.81 ± 0.2

(0.2 MPa driven pressure) [27]

Polyamide PIP TMC GOQDs

110.3 (Na2SO4), 110.4 (MgSO4), 115.5 (NaCl), 112.5 MgCl2

all for 100 psi

[28]

Amino modified polyvinylidene

fluoride

- - GOQDs (7.07 ± 0.24) × 103 L m-2 h-1 bar-1

(pure water permeability coefficient) [29]

Polysulfone (PSF) - - GOQDs 82.52 LMH bar-1 [30]

Polymer PEI TMC CDs

19.2 (isopropanol), 16.1 (ethyl acetate), 8.0 (acetone), 5.9 (toluene), and 4.2 (n-heptane)

for 4 bar

[31]

Polyamide MPD TMC CQDs and Na-CQDs 24.252.80 at 15 bar,

39.223.62 at 23 bar [32]

Polyamide PIP TMC

Carboxylic CQD (CCQD), amino CQD (NCQD), and sulfonated CQD (SCQD)

18.0 at 0.6MPa [33]

Trimesoyl chloride (TMC); m-phenylenediamine (MPD); piperazine (PIP); polyethylenimine (PEI); graphene quantum dots (GQDs); carbon quantum dots (CQDs); graphene oxide quantum dots (GOQDs), carbon dots (CDs); carbon quantum dots (CQDs)

Table 1. Summary of Membrane

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for more polymerization, the membranes were then air-dried for 15 min. in an oven at 60°C. Characterization of the GQDs was done via TEM, FTIR was used to determine functional groups located on the surfaces of the membranes, XPS was used to analyze surface ele- mental compositions of the membranes, and the mor- phology was seen through SEM. When looking at the XPS results, the O/C ratios of the GQDs/PIP-TMC TFN membrane were higher than that of PIP-TMC nano- filtration (NF) membranes without any GQDs, and a possible explanation for this is the contribution of oxy- gen-containing functional groups from GQDs and changes in the number of interconnecting groups in the PA active layer. Looking at the SEM, the PIP-TMC NF membrane had a surface that was rugged and dense, while the GQDs/PIP-TMC membranes were smoother.

The incorporation of GQDs in TFN membranes was shown to have the effect of increasing water flux with the GQDs/PIP-TMC membrane having a water flux of 102.0 L/(m

2

h), 6.8 times higher compared to the pris- tine membrane of PIP-TMC NF [15.0 L/(m

2

h)]. The easy fabrication process, eco-friendliness, high NF effi- ciency, and good properties for preventing the accumu- lation of materials on surfaces in water regarding these membranes makes this study of potential use in appli- cations of water treatment.

Forward osmosis is another important area for water desalination. In this work, GQDs were incorporated to the TFNs for potential applications in wastewater treat- ment and desalination by studying their bactericidal properties and effect on forward osmosis (FO)[23].

GQDs were produced through the pyrolysis of CA, and the interfacial polymerization process between 1,3-phe- nylendiamine (MPD) and TMC was used to prepare TFC/TFN membranes for FO on substrates made up of polyethersulfone (PES). ATR-FTIR spectra of TFC and TFN membranes were taken, and after increasing the amount of GQDs on the membranes, there was an effect of considerably lowered intensity of peaks with some peaks disappearing completely. In general, nanomaterials that are carbon-based have great antimicrobial proper- ties because of their mechanisms that are harmful to

cells. Included in this category are GQDs, and their in- corporation onto TFNs made the selective layer more hydrophilic, which had the effect of lowering the con- tact angle as the TFC membrane had a contact angle of 72.9° while for the TFN membrane it was 51°. This is strategically beneficial to lower adhesion of foulants, thus improving the antifouling property of the membrane.

It was also shown that incorporating a higher concen- tration of GQDs to the TFN membrane made the poly- amide selective layer thicker than before while also creating a denser layer than the pristine TFC membranes, making the membrane much less permeable and creat- ing a blockage of the surface. Permeability of water increased at the beginning, with 29% permeability for TFN-0.05 and 49% for TFN-0.1, but then went down as the concentration of GQDs increased to TFN-0.5.

Additionally, TFN-0.5 showed greater than 90% bacte- rial inactivation for E. coli and greater than 95% bac- terial inactivation for S. aureus compared to a pristine TFC membrane. The reason for this was because of the uniform dispersion that the GQDs had with a low tendency to form clusters, as well as increasing the number of active edges on the membrane surface, lead- ing to increased surface cytotoxicity.

Compared to RO and other energy-intensive desali-

nation and water treatment processes, FO has benefits

of needing a smaller amount of energy to run, good

water recovery, and low fouling levels as it only uses

the osmotic pressure difference that occurs naturally

between the high and low saline solutions separated by

a semipermeable membrane[24]. However, the main is-

sue with FO processes is the problem of internal con-

centration polarization (ICP). ICP can make the water

flux much lower by lowering the osmotic pressure gra-

dient by having solute molecules aggregate near the ac-

tive and support layer. Through the study, it was found

that incorporating GDQs into the membranes improved

water permeability and MgCl

2

rejection compared to

the pure TFC-0 membrane. GQDs were synthesized

through the direct pyrolysis of GQDs through the uti-

lization of a “bottom-up” approach. Interfacial polymer-

ization was used to prepare TFC membranes by putting

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polyacrylonitrile (PAN) substrates that were hydrolyzed in a 2.0M NaOH solution immersion (H-PAN) into an aqueous monomer solution. These substrates were then dried in air and then also put in a 0.20 w/v% TMC/

n-hexane organic monomer solution, allowing for the synthesis of a PA layers on the surface of the H-PAN substrates. FTIR showed that the created GQDs had an aromatic rings, and TEM imaging showed no visible agglomeration of GQDs, showing instead GQDs that were dispersed well and a structure of 2D sheets. Going more in detail, the diffusion resistance went down as the content of GQDs went up to 0.050 wt%, indicating that the addition of GDQs enhanced mass transfer, leading to lower ICP. Increasing GQD wt% past 0.050, the diffusion resistance went up gradually, signaling a gradual increase of ICP, and this may have been caused by the accumulation of GQDs. Additionally, at 0.050 wt%, the membrane demonstrated best performance re- garding separation and the highest flux at 12.9 L m

-2

h

-1

. Water flux increased 22.0% and reverse salt flux went down 32.2% compared to the pure TFC-0 mem- brane.

Nanofiber membrane are another kind of filtering membrane, and a process of incorporating GDQs in the PAN nanofibers will be discussed. GDQs were synthe- sized by treating pyrene with nitrate so that it could convert into 1,3,6-trinitropyrene[25]. This mixture was then subjected to dilution with deionized water (DI) and filtration through a nylon membrane. After ultra- sonication in a DI solution with ammonia and hydra- zine hydrate, the suspension was placed into an auto- clave and heated for 8h at 200°C. Nanofibrous mem- branes were prepared through an electrospinning pro- cess. Imaging from TEM and AFM seemed to indicate that the GQDs were made up of 2~5 layers. With a wide range of potential applications in the environ- mental and biological field, GQDs have garnered inter- est to function as sensors. Over the surface of the membrane, GQD-PAN membranes had uniform dis- persion of GQDs. Even under light irradiation that was ongoing, luminescence levels of immersed and dry GQD-PAN membranes were shown to have high sta-

bility for the duration of two months. Regarding the decrease of the intensity of light emission of the mem- brane from free chlorine, the process was rapid and conspicuous in a visual manner when placed below UV light. The photoluminescence (PL) quenching by GQDs that is not able to be reversed makes the related sensing platforms only able to be used once, but the concentration of chlorine in real-time found in networks for water distribution may still be measured through the filtering membranes that were fabricated by electro- spinning.

Solvent-resistant nanofiltration (SRNF), also known as organic solvent nanofiltration (OSN), is a technique that at the molecular level can separate mixtures of or- ganic substances[26]. These membranes can potentially be used when separating substances containing organic compounds from organic solvents. However, the main problem holding back the effectiveness of SRNF mem- branes is the low solvent resistance of these membranes.

The study examines a new TFN membrane that is based on polyimide (PI), which demonstrated better solvent resistance than previous findings. Regarding the syn- thesis of GQDs, a solution containing GQDs was passed through the PAN UF membrane to remove any im- purities that may have been in the solution with a size that was greater than 10.0 nm. To prepare the making of nanocomposite membranes that would be doped with GQDs, the PI substrate was affixed to a glass plate and a MPD solution was then poured on top. Then, the 1,2,4,5-Benzenetet- racarboxylic acyl chloride (BTAC) solution was applied on top to form a polyamic acid (PAA) active layer with GQDs embedded into it. Based on the thickness of the GQDs that were observed (0.8

~2.0 nm), it was hypothesized that the GQDs were

made up of 1~3 layers of graphene. In addition, TEM

imaging showed an average GQD size of 1.9 nm, and

such a small size allowed for a greater water flow be-

cause of additional pathways from an increase in spe-

cific surface area. The SRNF membranes that were pre-

pared, named (PI-GQDs-50/PI)

X

, was shown to have

almost a 50% higher permeability of ethanol compared

to membranes without any GQDs with identical prepa-

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Fig. 2. SEM and AFM images of the surface of the pre- pared (PIGQDs-0/PI)

X

(a,e), (PI-GQDs-25/PI)

X

(b,f), (PI- GQDs-50/PI)

X

(c,g), and (PI-GQDs-75/PI)

X

(d,h) TFN SRNF membranes. periods: pure water flux for 12 h, 0.1 g/L BSA solution flux for 12 h, and pure water flux after hydraulic washing for 0.5 h. Graphene Quantum Dots-Doped Thin Film Nanocomposite Polyimide Membranes with En- hanced Solvent Resistance for Solvent-Resistant Nanofil- tration (Reproduced with permission from Li et al., 26, Copyright 2017, American Chemical Society).

ration conditions and no negative effect to dye rejection.

After the solvent was activated using N,N-dimethylfor- mamide (DMF) for 30 min at 80°C, the permeability of ethanol even increased 8-fold to 22.6 L m

-2

h

-1

MPa

-1

. The potential for application of OSN was further shown when a solution of rhodamine B (RB)/DMF was fil- tered through this membrane for 100 hours. Results of this test showed an observation of DMF permeability of 18.3 L m

-2

h

-1

MPa

-1

and the rejection of RB to be at 99.9%.

2.2. Graphene oxide quantum dots

Zhang et al. fabricated GOQDs through direct py- rolysis of CA where using a heating mantle, 2 g of CA was heated at a temperature of 200°C[27]. The fab- rication of GOQDs was able to be confirmed after the CA changed its phase from a solid to a liquid and its color as a liquid changed from being colorless to a pale yellowish color, later turning into orange, all with- in a period of 30 minutes. After undergoing dialysis to get rid of excess CA, GOQDs were able to be ob- tained through freeze-drying the solution. GOQDs can be applied in areas such as low-pressure NF, UF, mi- crofiltration, pervaporative dehydration, and water treat- ment through incorporation onto preexisting membranes to improve hydrophilicity, antibiofouling and bacter- icidal performance, and water permeability, to give a few examples.

GOQDs were used to enhance NF performance[27].

GOQDs were formed through the method of direct pyrolysis. Interfacial polymerization was utilized to form TA/GOQDs TFM membranes. Findings that were reported using FTIR showed that through covalent linking, GOQDs were able to be incorporated success- fully into the separation layer made of tannic acid (TA).

GOQDs were spread throughout a TA film on TFN membranes for NF at low pressure. Compared to the pure TA TFC membrane, the membrane with GOQDs had improved antifouling properties and a maximum pure water flux of 23.33 L/m

2

h at 0.2 MPa, 1.5 times more compared to the membrane without GOQDs.

Rejection of Congo Red was established at 99.8% and

methylene blue at 97.6%. Normally, NF processes are

very susceptible to being fouled and having low per-

meability, as well as being expensive in general. As a

result, developing NF membranes with good antifouling

properties under low pressure is important. Several dyes

were tested in this study, and the rejection rate was the

highest for Congo Red and lowest for methylene blue,

which can be explained by the Donnan exclusion theo-

ry that states that as water molecules permeate across

the membrane because of the pressure applied, the

membrane surface with TA/GOQDs will be electrostati-

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Fig. 4. (a) Preparation process of TA/GOQDs TFN mem- brane. (b) Scheme of reaction mechanism among TA, GOQDs, and IPDI (Reproduced with permission from Zhang et al., 27, Copyright 2017, American Chemical Society).

Fig. 5. (a) Raman spectra of as-prepared GOQDs, (b) XRD patterns of GOQDs, (c) TEM image of as-prepared GOQDs, (d) the corresponding size distribution of GOQDs shown in panel c, (e) AFM image of GOQDs, and (f) the corre- sponding height profile along the black line shown in pan- el e (Reproduced with permission from Zhang et al., 27, Copyright 2017, American Chemical Society).

Fig. 6. Schematic illustration of the separation process for TA/GOQDs TFN membrane (Reproduced with permission from Zhang et al., 27, Copyright 2017, American Chemical Society).

cally attracted to methylene blue as it is positively charged and electrostatically repulsed to Congo Red.

These rates of rejection went up as the concentration of GOQDs increased up to a concentration of 0.5g/L. As for the stability of these TA/GOQDs TFN membranes long-term, TA/GOQDs-0.5 TFN membranes exhibited no clear degradation in water flux and rejection of Na

2

SO

4

, indicating good durability and stability.

Li et al. focused on the antibacterial properties of

thin films that are used in RO processes. Considerable

efforts have been undertaken to incorporate metallic

nanoparticles onto TFC membranes, such as Fe, TiO

2

,

and Ag nanoparticles, and these can control micro-

organisms’ growth[22]. Silver phosphate (AP) is anoth-

er substance that can be considered in this category of

antibacterial nanoparticles, and it is becoming more

widely known because of its good photo-oxidation and

great quantum efficiency in the presence of visible

light. A drawback of AP, however, is that because of

its morphology that cannot be controlled and low sta-

bility, it tends to lump together. This prevents uniform

dispersion on the surface of the membrane, lowering

the membrane’s separation performance. To overcome

this, a nanocomposite of GOQD and AP may be used,

Fig. 3. Synthesis of GOQDs (Reproduced with permission from Zhang et al., 27, Copyright 2017, American Chemical Society).

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as lots of negative charges on GOQD can be used as sites of reaction for Ag

+

to control the initial growth and morphology of AP for synthesis, improving dis- tribution of AP on the membrane while improving the antibacterial property of the membrane. GOQD/AP was found to improve the permeability of water across the membrane and have low adsorption of contaminants that were hydrophobic because of the many hydrophilic groups on the TFN membrane, such as carboxyl and hydroxyl groups. Regarding the antibacterial property of the membranes, the synergistic effect between AP and GOQD led to the significantly higher prevention of bacterial growth. Results showed that GOQD/AP in- corporation could improve the TFN membrane’s anti- fouling property from raised surface electronegativity.

Regarding the fabrication of GOQDs, a heterogeneous mixture containing GOQDs was treated with ultrasonic waves to make it into a homogeneous mixture. Then, in order to place Ag

+

onto the surface of the GOQDs, which were negatively charged, AgNO

3

solution was added drop by drop into the mixture while the mixture was being mixed magnetically. After continued mag- netic stirring even after adding Na

2

HPO

4

⋅12H

2

O, the precipitate was washed and freeze-dried to produce GOQD/AP. Interfacial polymerization was used to cre- ate the TFC and TFN membranes incorporated with GOQD/AP nanocomposites. After looking at SEM im- ages of the surface and cross sections of the membrane, structures resembling valleys and ridges were observed, indicating a complete reaction between MPD and TMC.

A filtration method assisted by pressure was used to physically coat GOQDs onto TFN NF membranes to enhance permeability of water and the rejection of salts and dyes[28]. At a pressure of 100 psi with room tem- perature, aqueous solutions that had a concentration of 500 ppm of Na

2

SO

4

, MgSO

4

, NaCl, and MgCl

2

were used to test the effectiveness of GOQDs on the separa- tion of ions of NF membranes. With the coating of GOQDs, water flux went up by approximately 15 LMH for all the salt aqueous solutions. Permeability of water increased from the improved surface attraction to water that led to the increase of water solubilization. The ef-

fect of different Na

2

SO

4

solutions for ion separation was also studied, and it was observed that with in- creasing concentration, the salt rejection as well as the water flux decreased, owing to greater osmotic pressure and greater polarization of concentration. Compared to the pure NF membranes, the GOQD/NF membranes had better salt rejection and water flux. Additionally, with GOQDs, rejection of methyl orange went up to 97% from 89.2% while rejection of methylene blue went down to 71% from 75.4%. Regarding potential changes in antifouling properties with the addition of GOQDs, no blatant difference was found, and the NF membranes were shown to have good antifouling prop- erties in general. The GOQD coating and NF mem- brane were also shown to have good stability with on- ly low fluctuations of salt rejection and water flux over time. For this study, the coating of the GOQDs to make the salt/dye rejection and permeability of water better was made through a method of pressure-assisted filtration. TEM imaging of GOQDs showed near spher- ical shapes of GOQDs and a good crystalline structure as clear lattice outer edges could be seen. After coating the surface of NF membranes that had a total area of 14.6 cm

2

with 50 µg of GOQDs, SEM imaging dis- played a much rougher membrane surface for these membranes compared with NF membranes without any GOQD coating. The GOQD coated membranes were free of any spots not having the GOQD coating.

A new type of membrane with improved antibiofoul- ing and antibacterial properties has been observed through the incorporation of GOQDs into amino modi- fied polyvinylidene fluoride (PVDF) membranes[29].

Here, instead of pyrolysis, a hydrothermal oxidation

process was used to synthesize GOQDs from carbon

black. In order to create a GOQDs-PVDF membrane,

the surface of the PVDF membrane was first hydroxy-

lated and then administered with 3-aminopropyl-trime-

thoxysilane (APTMS). SEM imaging indicated uniform

dispersion of nanoparticles on the surface of PVDF,

which suggested GOQDs were immobilized. After a

filtration time of 10 hours, the relative flux decrease of

GOQD/PVDF was 23%, much lower than pure PVDF

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Fig. 7. SEM images for normal E. coli cells at the surface of pristine PVDF membrane (a,b) and GOQDs-PVDF membrane (c,d) (Reproduced from Zeng et al., 29).

Fig. 8. SEM images of (a,b) pristine PVDF, (c) PEG mo- dified PVDF, (d) APTMS modified PVDF, (e) GOQDs- PVDF and (f) GOQDs-PVDF membranes after 15 min ul- trasonication treatment (Reproduced from Zeng et al., 29).

at 86% and graphene oxide (GO)-sheet modified PVDF at 62%. Owing to the uniform dispersion and structure of GOQDs, GOQD/PVDF showed good antibiofouling, and the modified membrane had stability and durability over a long period of time thanks to strong covalent forces that exist between GOQDs and PVDF. 0D GOQDs bonded to PVDF were also shown to have

better antibacterial properties compared to previous studies with 2D GO sheets and polymer membranes with 1D carbon nano-tubes. After the addition of GOQDs onto PVDF, hydrophilicity increased as the water con- tact angle went down to 34.3° as the water contact an- gle of pure PVDF was 118.5°. Over a filtration time of 12 hours, the decrease of flux was 24.3% for GOQD/

PVDF while flux decreased 88.4% for pure PVDF, suggesting that PVDF incorporated with GOQDs has much better antibiofouling properties compared with pure PVDF. Additionally, even past 10 hours of filtra- tion, the value of permeation was stable for GOQD/

PVDF. Regarding the proliferation of S. aureus and E.

coli, after being attached to GOQD/ PVDF for one hour, the metabolic activity for E. coli cells decreased 88.9%, but for the PVDF membrane modified with 2D GO, it decreased by only 69.2%.

For all the membranes that were fabricated in this study, a phase-inversion method, which gets rid of a liquid polymer solution to form a solid polymer mem- brane that is porous, was used for their fabrication[30].

PSF membranes incorporated with GOQDs for the pur- pose of UF at various weight percentages of 0.1~0.5 were created. For background, UF is a process utilized for the filtration of water and is useful for its simplicity in operation, effectiveness of cost, high efficiency, and no detectable production of harmful byproducts. PSF is a membrane with good chemical, mechanical, and ther- mal stability that is commonly used in UF. Unfortuna- tely, as PSF is hydrophobic in nature, the membrane fouls severely and pores are blocked off, lowering wa- ter flux. The materials that cause fouling that lead to a severe decrease of flux were observed to accumulate in the troughs of membrane surfaces that were charac- terized to be rougher. At 0.5 wt%, irreversible fouling was at 10.3% and flux recovery ratio at 89.7%, the low- est out of all the GOQD-incorporated PSF membranes.

Interestingly, at 0.1 and 0.3 wt% of GOQDs, porosity of the membranes went up, while at an increased wt%

of 0.5 the porosity went down. Comparing pure PSF

membrane porosity with the GOQD enhanced mem-

branes, the former had 55.7% porosity and the latter

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85.9% porosity. Water flux at 0.3 wt% was 130.54 LMH bar

-1

while at 0.5% it was lower at 85.79 LMH bar

-1

. The increased porosity for the membrane with 0.1 and 0.3 wt% had more space in which water could flow through and lowered the resistance for the flow of water, whereas a 0.5 wt% resulted in a denser structure with less permeability than the lower wt%

membranes. XPS results indicated that the number of functional groups on GO sheets is much lower than GOQDs, and this can be explained through edge effects found in GOQDs. Additionally, increasing the weight percentage of GOQDs led to a significant increase of viscosity, which had the effect of the membrane struc- ture being denser and thicker.

A new nanocomposite membrane was developed by incorporating GOQDs into a sodium alginate (SA) ma- trix for the dehydration of ethanol for application in pervaporative dehydration[21]. The synthesis of GOQDs involved the direct pyrolysis of CA, and the SA-GOQDs nanocomposite membranes had their preparation done on dry PAN substrates through a spin-coating method.

TEM imaging indicated that the GOQDs were uni- formly distributed quite fairly and dispersed nicely.

SEM imaging showed smooth surface structures of the SA-GOQDs/PAN membranes at the microlevel, thanks to the GOQDs being nanosized. This smooth surface structure at the microlevel was similar for the SA/PAN membrane as well. Because of the nanoscale size and the high attraction to water of the GOQDs, the mem- brane showed good performance regarding ethanol de- hydration that was 60% higher compared to a pure al- ginate membrane, as the membrane achieved 2432 ± 58 g m

-2

h

-1

of total permeation flux at 2 wt%. A

“bottom-up” method was utilized in the synthesis of GOQDs through the pyrolysis of citric acid. For the preparation of nanocomposite membranes, GOQDs were incorporated into SA. SA has excellent performance when it comes to dehydration separation. At higher loadings of GOQDs, the permeation flux goes down as the separation factor remains nearly constant. Results showing an increase in permeation flux suggests that shorter and less winded pathways through stacks of

GOQDs favor the transport of water.

3. Carbon Quantum Dots

CQDs were produced by heating CA in fine powder form for 3 h at 180 in a container made of class that was loosely covered[32]. After heating, the material was then brought down to room temperature. Dissolving this material in water, it was then dialyzed against DI wa- ter and then freeze-dried to obtain the CQDs. CQDs can be functionalized with Na

+

ions, and upon incorporation to a PA membrane, it was found to increase the pure water permeability while maintaining a high NaCl re- jection percentage of 97.7%. CQDs show promise in applications of both membrane separation and power generation through osmosis.

NF is also one important technique for the purpose of organic solvent nanofiltration (OSN)[31]. Here, CQDs with differing degrees of carbonation were prepared us- ing pyrolysis that was microwave-assisted. CQDs of smaller sizes than 5 nm with different degrees of car- bonation were able to be made by altering the amount of ultra-purified water that CA was dissolved in. The higher the amount of ultra-purified water, the lower the carbonation degree. H-PAN had a mixture of homoge- neous polyethyleneimine-carbon dots (PEI-CDs) cast onto it. After removing excess PEI-CDs solution, a sol- ution of n-hexane and TMC was cast on top of the PEI-CDs layer. SEM imaging suggested a homoge- neous and smooth PAN/PEI surface that was free of apparent defects or voids. The networks of PEI were cross-linked, and they conferred onto composite mem- branes great solvent resistance and rejection of solute.

CDs on these membranes functioned to accelerate sol- vent molecules across the membrane. CDs that were carbonated without glycerol with water as the solvent even achieved an increase for solvent flux of 54.3%

and an increase of 40.5% for solvent uptake. However, the adsorption and permeability of non-polar solvents was lowered when using these CDs, improving the permeation when it came to polar solvents as a result.

Gai et al. reported on TFN membrane containing

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functionalized carbon quantum dots[32]. Carbon quan- tum dots are prepared by finely grinding citric acid powder and heated at 180°C for 3 h in air. This prod- uct was then cooled to room temperature and placed in deionized water to dissolve. The desired solute was separated by the difference in permeability with other solutes through a semipermeable membrane and then freeze dried to make the CQDs. Regarding the fab- rication of the membrane, interfacial polymerization was used to place a PA layer on each substrate’s inner surface. TFN membranes incorporated with CQDs are one kind of these membranes to create PA layers with- out any defects. For the use of desalination of brackish water, CQDs functionalized with sodium ions were used in a hollow fiber configuration as opposed to a flat sheet. TEM images showed spherical CQDs and Na-CQDs with sizes from 2~6 nm that did not ag- gregate in clumps, but instead were dispersed well.

Compared to a regular TFC membrane, it was found that the membrane with Na-CQDs incorporation had a 47.1% increase in the permeability of pure water. This increase may have resulted because of a decrease in membrane thickness, increase in space among PA chains, higher effective surface area, and a greater number of hydrophilic groups that have oxygen. The optimal mem- brane was found to be TFN membranes incorporated with 1% wt Na-CQDs, 57.65 ± 3.26 LMH as the meas- ured water flux, and a salt rejection percentage of 98.6% when the feed solution had 2000 ppm NaCl.

Three different CQDs were synthesized by Sun et al.

For carboxylic carbon quantum dots (CCQDs), they were prepared through direct pyrolysis of citric acid[33].

Amino carbon quantum dots (NCQDs) were formed through pyrolysis at low temperature of citric acid with branched polyethyleneimine (BPEI) around. Sulfonated carbon quantum dots (SCQDs) were synthesized through pyrolysis of citric acid and poly(sodium 4-styrene sul- fonate) (PSS). The interfacial polymerization method was utilized in the formation of TFC/TFN membranes incorporated with the various types of CQDs, and through TEM imaging, the NCQD and SCQD sizes were found to be larger than CCQD and all of the CQDs

were found to be dispersed well and have a near spherical shape. The synthesized three different func- tionalized CQDs were added to TFN membranes, more specifically the PA layer. The addition of these differ- ent CQDs onto TFN membranes gave these membranes differing properties according to which group they were functionalized with. Among these groups, the TFN-SCQD membrane exhibited the highest water flux at 42.1 L m

-2

h

-1

with rejection percentage of Na

2

SO

4

at 93.6%. The membrane with SCQD also had the best antifouling effect. The lowest water flux was attributed to the TFN-NCQD membrane at 31.5 L m

-2

h

-1

. For all the membranes incorporated with these groups, the wa- ter flux measurement linearly increased with the pres- sure applied, but it is of note that the CQD’s func- tional groups do have a role in determining the TFN membrane permeability.

Gai et al. reported power generation through the PRO process using thin film composite membranes[20].

CQDs wewe prepared by heating citric acid powder that was grinded for 3 h at 180°C in order to make original CQDs (O-CQDs) that were altered at the sur- face with carboxyl groups. Using the method of inter- facial polymerization, a polyamide selective layer was formed in the hollow interior surface of the PES fiber substrates. Through TEM characterization, the structures of O-CQDs and CQDs functionalized with Na

+

were seen to be spherical with sizes around 3~9 nm, with all three categories of CQDs having great hydrophilic properties because of the small size of CQDs and the presence of groups with Na and O, allowing for good CQD dispersion in the medium of aqueous solutions.

Having set a mixture of deionized water and 1.0 M

NaCl as the feed solution, the study was able to gen-

erate a maximum power density of 34.20 W/m

2

at a

pressure of 23 bar with a novel TFC membrane, and

this power density was the highest to be reported in

literature, according to the authors. Because water flows

from higher concentration to a lower concentration

across a semipermeable membrane because of chemical

potential difference, power can be generated by using

the hydrostatic potential. This study incorporated CQDs

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onto PA layers and tested these layers for their per- formance regarding PRO. Some films were incorporated with Na

+

functionalized CQDs at 1% wt and at a pH of 5 and 9. The highest water flux was obtained with the TFC-(Na-CQD-5)-1, which stands for Na

+

function- alized CQDs incorporated onto TFC with 1% wt and at a pH of 5. The study determined the increased power density and water flux CQDs with Na

+

functionalization to be because of a lower thickness of the PA layer in TFC-(Na-CQD-5)-1 and TFC-(Na-CQD-9)-1, more groups of oxygen that were hydrophilic in the PA lay- ers, greater surface area, and a PA network that was looser. Ultimately, TFC-(Na-CQD-9)-1 was found to be the most optimal, in terms of high-power density and water flux and low reverse salt flux.

Prathiban et al. reported the applicability of CQDs in direct methanol fuel cells (DMFCs)[33]. This study in- vestigated the functionality of CQDs to reduce methanol transport from the anode to the cathode in DMFCs by potentially acting as an inorganic filler. DMFCs have been garnering interest as a possibly better alternative to Li-ion batteries because of its great specific energy density to power electronic devices. However, a major problem of DMFCs is methanol crossover, and in order to reduce this, many polymer electrolyte membranes have been proposed, including Nafion composite mem- branes, which were found to be the best among all others because of high proton conductivity and the high stability of Nafion. Adding CQDs to Nafion could enhance ionic conductivity from hydrogen bonding be- tween hydrophilic groups in CQDs and sulfonic acid groups in Nafion. The preparation of CQDs was ach- ieved by mixing 1.8 g Gelatin with 80 mL of water, and this was then placed in an autoclave. To produce a hydrothermal process, the autoclave was put into a fur- nace for 3 h at 200°C. To make the hybrid membrane of Nafion-CQDs, a mixture of CQDs and 5 wt% of Nafion ionomer that was mechanically mixed for 4 h and ultrasonically dispersed for 1h was cast in a petri dish made of glass and underwent drying in a vacuum.

Upon looking at the pattern of X-ray diffraction, the experimenters were able to see indications of the amor-

phous nature of GQDs, and this is from the abundant functional groups that can be found within CQDs. This combined membrane was found to have 33% lower methanol crossover and around 30% greater proton conductivity compared to the pure Nafion membrane.

Using it in a DMFC, 113 mW cm

-2

of maximum power density was achieved at 70°C under ambient pressure, which performance-wise was around 75% greater than the pure Nafion membrane under the same con- ditions.

The optimal content of the Nafion-CQDs as a filler in the study was discovered to be at 1.5 wt%.

4. Conclusions

QDs have generally been shown to improve mem- brane performance for applications in water reclama- tion, osmotic power generation, direct methanol fuel cells, sensing technology, and more. The QDs that have been studied were made up of a couple of different materials depending on the study, including carbon, gra- phene, or graphene oxide. These QDs can also be func- tionalized with Ag

+

, Na

+

, or various amino acid groups onto different types of membranes, such as hollow fi- ber membranes, nanocomposite membranes, etc., to ex- hibit better desired properties compared to the original membrane. The superb hydrophilicity, antifouling prop- erty, and other great properties of QDs combined with their low cost, environmental friendliness, low toxicity, and ability to be applied in various applications makes the study of QDs very appealing for the future of membrane technology. In this review, the utility of dif- ferent quantum dots in composite membrane were dis- cussed.

References

1. M. Kumar, M. A. Khan, and H. A. Arafat, “Recent developments in the rational fabrication of thin film nanocomposite membranes for water purification and desalination”, ACS Omega, 5, 3792 (2020).

2. U. A. Rani, L. Y. Ng, C. Y. Ng, and E. Mahmoudi,

“A review of carbon quantum dots and their appli-

(13)

cations in wastewater treatment”, Adv. Colloid Interf.

Sci., 278, 102124 (2020).

3. G. Liu, W. Jin, and N. Xu, “Graphene-based mem- branes”, Chem. Soc. Rev., 44, 5016 (2015).

4. H. Saleem and S. J. Zaidi, “Nanoparticles in reverse osmosis membranes for desalination: A state of the art review”, Desalination, 475, 114171 (2020).

5. Y. Wen, J. Yuan, X. Ma, S. Wang, and Y. Liu,

“Polymeric nanocomposite membranes for water treatment: A review”, Environ. Chem. Lett., 17, 1539 (2019).

6. I. Mohmood, C. B. Lopes, I. Lopes, I. Ahmad, A.

C. Duarte, and E. Pereira, “Nanoscale materials and their use in water contaminants removal - A review”, Environ. Sci. Pollut. Res., 20, 1239 (2013).

7. L. Y. Ng, C. Y. Ng, E. Mahmoudi, C. B. Ong, and A. W. Mohammad, “A review of the manage- ment of inflow water, wastewater and water reuse by membrane technology for a sustainable production in shrimp farming”, J. Water Process Eng., 23, 27 (2018).

8. D. W. Kim, “Review on graphene oxide-based na- nofiltration membrane”, Membr J., 29, 130 (2019).

9. H. Jang, “Technology trend on commercial poly- meric membranes for water treatment”, Membr J.,

29, 11 (2019).

10. J. Kim, H. J. Park, K.-H. Lee, B. Kwon, S. Kwon, and J.-L. Lim, “Impact analysis of water blending to reverse osmosis desalination process”, Membr J., 30, 190 (2020).

11. S. H. Kim, Y. S. Kim, D. Y. Kim, S. M. Kim, and J. F. Kim, “Solvent filtration performance of thin film composite membranes based on poly- ethersulfone support”, Membr J., 29, 348 (2019).

12. Y. K. Lee, and R. Patel, “Two dimensional (2D) nanomaterials based composite membrane for de- salination”, Membr J., 30, 111 (2020).

13. Y. Na, J. Lee, S. H. Lee, P. Kumar, J. H. Kim, and R. Patel, “Removal of heavy metals by polysa- ccharide: A review”, Polym. Plast. Technol. Mater.,

59(16), 1770 (2020).

14. R. Patel, M. Patel, J.-S. Sung, and J. H. Kim, “Pre-

paration and characterization of bioinert amphiphilic P(VDF-co-CTFE)-g-POEM graft copolymer”, Polym.

Plast. Technol. Mater., 59, 1077 (2020).

15. W. J. Lau, S. Gray, T. Matsuura, D. Emadzadeh, J. Paul Chen, and A. F. Ismail, “A review on pol- yamide thin film nanocomposite (TFN) membranes:

History, applications, challenges and approaches”, Water Res., 80, 306 (2015).

16. X. Qu, P. J. J. Alvarez, and Q. Li, “Applications of nanotechnology in water and wastewater treat- ment”, Water Res., 47, 3931 (2013).

17. D. L. Zhao, and T. S. Chung, “Applications of carbon quantum dots (CQDs) in membrane tech- nologies: A review”, Water Res., 147, 43 (2018).

18. D. L. Zhao, S. Japip, Y. Zhang, M. Weber, C.

Maletzko, and T. S. Chung, “Emerging thin-film nanocomposite (TFN) membranes for reverse os- mosis: A review”, Water Res., 173, 115557 (2020).

19. R. Bi, Q. Zhang, R. Zhang, Y. Su, and Z. Jiang,

“Thin film nanocomposite membranes incorporated with graphene quantum dots for high flux and anti- fouling property”, J. Membr. Sci., 553, 17 (2018).

20. W. Gai, D. L. Zhao, and T. S. Chung, “Novel thin film composite hollow fiber membranes incorporated with carbon quantum dots for osmotic power gen- eration”, J. Membr. Sci., 551, 94 (2018).

21. M. Wang, F. Pan, L. Yang, Y. Song, H. Wu, X.

Cheng, G. Liu, H. Yang, H. Wang, Z. Jiang, and X. Cao, “Graphene oxide quantum dots incorporated nanocomposite membranes with high water flux for pervaporative dehydration”, J. Membr. Sci., 563, 903 (2018).

22. S. Li, B. Gao, Y. Wang, B. Jin, Q. Yue, and Z.

Wang, “Antibacterial thin film nanocomposite re- verse osmosis membrane by doping silver phos- phate loaded graphene oxide quantum dots in poly- amide layer”, Desalination, 464, 94 (2019).

23. S. F. Seyedpour, A. Rahimpour, A. A. Shamsabadi,

and M. Soroush, “Improved performance and anti-

fouling properties of thin-film composite polyamide

membranes modified with nano-sized bactericidal

graphene quantum dots for forward osmosis”, Chem.

(14)

Eng. Res. Des., 139, 321 (2018).

24. S. Xu, F. Li, B. Su, M. Z. Hu, X. Gao, and C.

Gao, “Novel graphene quantum dots (GQDs)-incor- porated thin film composite (TFC) membranes for forward osmosis (FO) desalination”, Desalination,

451, 219 (2019).

25. V. Ruiz, A. Pérez-Marquez, J. Maudes, H. J.

Grande, and N. Murillo, “Enhanced photostability and sensing performance of graphene quantum dots encapsulated in electrospun polyacrylonitrile nano- fibrous filtering membranes”, Sens Actuators, B Chem., 262, 902 (2018).

26. S. Li, C. Li, X. Song, B. Su, B. Mandal, B. Prasad, X. Gao, and C. Gao, “Graphene quantum dots-doped thin film nanocomposite polyimide membranes with enhanced solvent resistance for solvent-re- sistant nanofiltration”, ACS Appl. Mater. Interfaces,

11, 6527 (2019).

27. C. Zhang, K. Wei, W. Zhang, Y. Bai, Y. Sun, and J. Gu, “Graphene oxide quantum dots incorporated into a thin film nanocomposite membrane with high flux and antifouling properties for low-pres- sure nanofiltration”, ACS Appl. Mater. Interfaces,

9, 11082 (2017).

28. G. Zhao, R. Hu, Y. He, and H. Zhu, “Physically coating nanofiltration membranes with graphene oxide quantum dots for simultaneously improved water permeability and salt/dye rejection”, Adv.

Mater. Interfaces, 6(5), 1801742 (2019).

29. Z. Zeng, D. Yu, Z. He, J. Liu, F. X. Xiao, Y.

Zhang, R. Wang, D. Bhattacharyya, and T. T. Y.

Tan, “Graphene oxide quantum dots covalently func- tionalized PVDF membrane with significantly-en- hanced bactericidal and antibiofouling perform- ances”, Sci. Rep., 6, 20142 (2016).

30. G. Zhao, R. Hu, J. Li, and H. Zhu, “Graphene ox- ide quantum dots embedded polysulfone membranes with enhanced hydrophilicity, permeability and an- tifouling performance”, Sci. China Mater., 62, 1177 (2019).

31. Z. Yuan, X. Wu, Y. Jiang, Y. Li, J. Huang, L. Hao, J. Zhang, and J. Wang, “Carbon dots-incorporated composite membrane towards enhanced organic sol- vent nanofiltration performance”, J. Membr. Sci.,

549, 1 (2018).

32. W. Gai, D. L. Zhao, and T. S. Chung, “Thin film nanocomposite hollow fiber membranes comprising Na

+

-functionalized carbon quantum dots for brackish water desalination”, Water Res., 154, 54 (2019).

33. H. Sun and P. Wu, “Tuning the functional groups of carbon quantum dots in thin film nanocomposite membranes for nanofiltration”, J. Membr. Sci., 564, 394 (2018).

34. V. Parthiban, S. K. Panda, and A. K. Sahu, “Highly

fluorescent carbon quantum dots-Nafion as proton

selective hybrid membrane for direct methanol fuel

cells”, Electrochim Acta, 292, 855 (2018).

수치

Fig.  1.  Schematic  diagram  of  the  quantum  dots  embedded  thin  film  composite  membrane.
Fig.  2.  SEM  and  AFM  images  of  the  surface  of  the  pre- pre-pared  (PIGQDs-0/PI) X   (a,e),  (PI-GQDs-25/PI) X   (b,f),  (PI-  GQDs-50/PI) X   (c,g),  and  (PI-GQDs-75/PI) X   (d,h)  TFN  SRNF  membranes
Fig.  6.  Schematic  illustration  of  the  separation  process  for  TA/GOQDs  TFN  membrane  (Reproduced  with  permission  from  Zhang  et al.,  27,  Copyright  2017,  American  Chemical Society).
Fig.  7.  SEM  images  for  normal  E. coli  cells  at  the  surface  of  pristine  PVDF  membrane  (a,b)  and  GOQDs-PVDF  membrane  (c,d)  (Reproduced  from  Zeng  et al.,  29).

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