CC BY
8
UDC 676.038.2+628.1
DOI https://doi.Org/10.35546/kntu2078-4481.2023.4.20
I. V. TREMBUS
Candidate of Technical Sciences, Associate Professor, Associate Professor at the Department of Ecology and Technology
of Plant Polymers National Technical University of Ukraine "Igor Sikorsky Kyiv Polytechnic Institute" ORCID: 0000-0001-7481-4144
A. S. HONDOVSKA
Postgraduate Student at the Department of Ecology and Technology
of Plant Polymers National Technical University of Ukraine "Igor Sikorsky Kyiv Polytechnic Institute" ORCID: 0000-0002-9795-768X
N. V. MYKHAILENKO
Master at the Department of Ecology and Technology of Plant Polymers National Technical University of Ukraine "Igor Sikorsky Kyiv Polytechnic Institute" ORCID: 0009-0004-8342-7540
STUDY PROPERTIES OF POLYSULFONAMIDE MEMBRANE
In this work, the properties of the polysulfonamide membrane UPM-20 were studied for the purpose of further purification of contaminated water from suspended fine particles and dissolved impurities that cause turbidity and color of water. The influence ofpressure from 1 to 5 atmospheres and filtration time from 20 to 100 minutes on specific productivity, selectivity and turbidity and color values of the permeate was shown. It was found thatfor all pressure values there are three periods in the filtration process of the model sodium humate solution: a sharp change, a slow decrease in parameters and no significant changes in permeate parameters. An increase in pressure and an increase in the duration of the sodium humate filtration leads to a decrease in the productivity indexfrom 87 to 2.7 m2/(m3 h)102. The selectivity ofthe membrane in terms of color and turbidity was calculated. It is shown that the highest selectivity for color is in the range of 95.2 to 96 % for filtration at a pressure of 5 atmospheres and a duration of80-100 minutes; respectively, for selectivity for turbidity, this indicator is 97.2 % for sodium humate filtration at a pressure of 5 atmospheres and a process duration of 90 minutes. A mathematical model of the filtration process of the model solution, sodium humate, was constructed using the Python programming language and the Matplotlib library for constructing mathematical dependencies. It was found that the purification of sodium humate on the UPM-20 membrane follows a non-linear dependence. Mathematical equations were obtained that adequately describe the dependence of the output variables on the selected technological factor of the filtration process. It is shown that these equations are in the form of a third-order polynomial, a cubic model, which can be used to describe the process of sodium humate filtration using the UPM-20 membrane at different pressures, from 1 to 5 atmospheres.
Key words: UPM-20 membrane, humate solution, filtration, specific productivity, selectivity, permeate, turbidity, color, mathematical model
I. В. ТРЕМБУС
кандидат техшчних наук, доцент, доцент кафедри екологп та технологи рослинних полiмерiв Нацюнальний техшчний ушверситет Украши «Кшвський пол^ехшчний шститут iменi 1горя Сшорського» ORCID: 0000-0001-7481-4144
А. С. ГОНДОВСЬКА
асшрант кафедри екологп та технологп рослинних полiмерiв Нацюнальний техшчний ушверситет Украши «Кшвський пол^ехшчний шститут iменi 1горя Сшорського» ORCID: 0000-0002-9795-768X
Н. В. МИХАЙЛЕНКО
мапстр кафедри екологй та технологи рослинних полiмерiв Нацюнальний техшчний ушверситет Украши «Кшвський полiтехнiчний шститут iменi 1горя Сшорського» ORCID: 0009-0004-8342-7540
ДОСЛ1ДЖЕННЯ ВЛАСТИВОСТЕЙ ПОЛ1СУЛЬФОНАМ1ДНО1 МЕМБРАНИ
В po6omi було проведено до^дження властивостей полiсульфонамiдноi мембрани УПМ-20 з метою подальшого очищення забруднених вод eid зважених дрi6нодисnерних частинок та розчинених домшок, що обумовлюють каламуттсть i кольоровють води. Показано вплив тиску вiд 1 до 5 атмосфер та тривалостi процесу фтьтрування вiд 20 до 100 хвилин на показники питомо'1' продуктивностi, селективностi та значення каламутностi i кольоровостi пермiату. Встановлено, що для вах значень тиску притаманна наявнкть трьох перiодiв проходження процесу фтьтрацИ модельного розчину гумату натрiю: ргзка змта, повтьне зниження параметрiв та без значних змт в показниках пермiату. Зростання тиску i збтьшення тривалостi фтьтрування гумату натрт призводить до зниження показника продуктивностi вiд 87 до 2,7 м2/(м3^год)^102. Розраховано показники селективностi мембрани за кольоровютю i каламутнктю. Показано, що найбтьша селективнiсть за кольоровютю знаходиться в межах вiд 95,2 до 96 % для фтьтрування за тиску 5 атмосфер, тривалютю 80-100 хвилин, вiдповiдно для селективностi за каламуттстю даний показник для фтьтрацИ гумату натрiю становить 97,2 % за тиску 5 атмосфер, тривалостi процесу 90 хвилин. Було побудовано математичну модель процесу фтьтрування модельного розчину - гумату натрт за допомогою мови програмування Python i 6i6лiотеки Matplotlib для побудови математичних залежностей. Встановлено, що очищення гумату натрю на мем6ранi УПМ-20 вiд6уваeться за нелiнiйною залежтстю. Отримано математичнi рiвняння, що адекватно описують залежностi вихiдних змтних вiд обраного технологiчного чинника процесу фтьтрування. Показано, що ц рiвняння мають вигляд полiнома третього порядку, це ку6iчна модель, що може бути використана для опису процесу фтьтрування гумату натрю з використанням мембрани УПМ-20 за р1зного тиску - вiд 1 до 5 атмосфер.
Ключовi слова: мембрана УПМ-20, розчин гумату, фiльтрацiя, питома продуктивнiсть, селективтсть, пермiат, каламуттсть, кольоровiсть, математична модель.
Formulation of the problem
More than 100 different materials for membrane production are known nowadays [1]. The main problem during purification with using membranes is to choose membrane which will be possible to work according tasks and conditions of separation method as much as possible. The progress of membrane separation usage is closely related to development various technologies which connected with production membranes with separate characteristics like porous structure and surface properties [2].
Analysis of recent research and publications
New technologies of formation porous polymer membranes make possible to create various specialized membranes thereby expanding and deepening fields of membrane technologies application [3, 4]. Polymer membranes have high chemical and thermal stability, low specific resistance and high mechanical properties [5, 6]. It is worth noting that issue of membrane formation is closely related to patterns and features mass transfer studies through porous polymer membranes surfaces. Polysulfones (PSF), polyethersulfones (PES), polysulfonamides (PSA) are very important polymers for membrane production (Fig. 1) [2]. It should be noted that they have high chemical and thermal stability at their glass transition temperature (PSF - T = 190 °C; PES - T = 230 °C, PSA - T = 288 °C) [3, 4]. Therefore, these polymers are widely used as basic materials for ultrafiltration membranes manufacture as well as substrates for composite membranes. So, aromatic polysulfone usage is promising field for functional polymers and membranes production based on them due to high film-forming properties [7].
Polysulfonamide membranes for ultrafiltration purification UPM-20 type have become widely used. Polysulfonamide (PSA) is type of aromatic co-polyamide and an organic high-temperature resistant material which have special molecular structure. PSA have excellent properties in terms of heat resistance, dimensional stability, high temperature resistance and fire resistance [8].
UPM-20 membranes consist of three different layers of polymeric materials namely aromatic polysulfone and thermoplastic materials which provide their strength and durability. Mixture of polyethylene terephthalate (PED) and polypropylene (PP) are polymeric thermoplastic materials which used for UPM-20 membrane production Fig. 2. [8]. Average pore size in UPM-20 membrane is 20 nm and thickness is 150 ^m. These material is very strong and resistant to various types of contaminants and chemicals.
P o ly e t hersu 1 fone
————Ç3)—NMOC—^^—
P olysulfonamide Fig. 1. Polymers structural formulas for membrane production
Fig. 2. UPM 20 polysulfonamide membrane model
Fillers and stabilizers can be used as additional substances for this type membrane production. Carbonate filler, namely calcium carbonate, is usually included in UPM-20 membranes. It gives mechanical strength and tear resistance for them [9].
Stabilizers are added to UPM-20 composition to ensure their resistance to ultraviolet radiation and other factors that can cause material destruction over time. In general, UPM-20 membranes are very effective materials for water purification due to their complex structure [10]. They are used in filter systems where water is passed through a membrane which ensures the screening of impurities.
UPM-20 can be used both for cleaning drinking water and for cleaning water from industrial and chemical pollution. The usage of UPM-20 membranes in filter systems make possible to effectively purify water from various types of pollutants, including bacteria, viruses, chemical compounds and other substances [11].
The purpose of the work was to evaluate cleaning properties of UPM-20 membrane at pressures from 1 to 5 atm using simulation of cleaning process on example model solution of sodium humate.
Presenting main material
The research of membrane samples was carried out on laboratory setup in non-flow installation (Fig. 3) at different pressure and during experiment each membrane was changed to new one for research reliability. Working surface of membrane is 11.3^10-3 m2. The efficiency of purification through membrane was evaluated by values of permeate turbidity, color, residual turbidity, concentrate color, selectivity variable and specific productivity.
Fig. 3. Laboratory installation for studying operational membranes properties
The turbidity of original solution was 170 mg/dm3; chroma 1940 degrees. Filtration was carried out under pressure from 1 to 5 atm. Permeate was sampled at regular intervals every 10 min. Filtration continued until stabilization of monitored parameters, namely the volume and specific productivity (transmembrane flow rate) y, which was determined by formula, m3/(m2^hour):
Y =
AV 5 At
(1)
where AV - permeate volume, m3; S - filtering area, m2; At - filtering time, hours.
Residual color and turbidity determination of permeate was carried out on KFK-2 calorimeter. Turbidity was determined at wavelength at 670 nm, chroma at 400 nm. The obtained values of optical density were translated into chroma and turbidity units using graduation graphs method.
The selectivity 9 according to turbidity (color) of UPM-20 membrane was determined by formula, %:
SL =
1 -
C
100, %
(2)
where Ci, C2 - turbidity (color) of the original solution and permeate, mg/dm3 (degree).
The mathematical model construction of filtering process was carried out using Python programming language using the sklearn library for calculation and Matplotlib for constructing relevant dependencies [12-15].
As a result of the research (Fig. 4) it can be seen that each pressure value is characterized by presence of three periods of filtration process. The first period is characterized by sharp change, the second one by slower decrease in membrane parameters. As for the third period, it is characterized by almost constant process without significant changes in permeate parameters. The sharpest decrease is observed in the first 20 minutes in permeate characteristics for all pressures. During this period the material structure is maximally compacted and pores in membrane are clogged under the action of pressure.
The filtration process have stabilized after 80 minutes which can be observed from membrane performance values. Sharp drop in this indicator which happened at the beginning of the process indicates that membrane structure is compacted under pressure, porosity of sample decreases, pores in membrane become clogged and productivity decreases accordingly. It can also be assumed that pressure increasing contributes to increasing content of bound water in pores which in such conditions has higher viscosity. This also leads to decreasing in permeability in membrane material.
Membrane selectivity is important aspect during investigating membrane filtering capabilities in terms to color and turbidity. The residual color and turbidity changes of permeate is shown in Fig. 5.
The lowest residual color of permeate for UPM-20 membrane is observed in pressure of 5 atm. Permeate color remains almost unchanged after entering constant filtration mode for all investigated pressures. Pressure and duration increasing during filtration process leads to decreasing in turbidity of permeate.
Fig. 4. Dependence of specific productivity on filtration duration of concentrate at different pressures
Pressure increasing leads to selectivity increases both in terms to color and turbidity (Fig. 6. (a) and (b)).
210
1W
170
•Jl
V. 150
«■
130
c U HP
to
7a
50
< -1 atm ■ ■ 3 atm. »- 5 atm.
V
0.2 04 os o« i.o
filtralion time. Iiour
12
1.J
21Q 190 170 150 130 110 BOTOSO
1 atm. 3 atm 5 atm
42 0.4 AG DB 10 12 IM'riUioL lime, buur
b
Fig. 5. Permeate color (a) and turbidity (b) dependence on filtration duration at different pressures
The best results of selectivity in terms to color were obtained for pressure 5 atm and was equal to values in range from 95.2 to 96% (filtration duration from 80 to 100 minutes). Selectivity in terms to turbidity has the highest indicators for sodium humate filtration at pressure 5 atm with duration 90 minutes and has value 97.2%.
Sampling every 10 minutes and permeate turbidity are important parameters for evaluating effectiveness of filtering process and for these parameters mathematical models were built (Fig. 7).
The dependence of experimental studies data and prediction values of mathematical model which were built using linear regression method were shown in Fig. 7 [16]. Humate purification on membrane occurs according to non-linear dependence. Non-linear equations were constructed for each studied parameter at different pressures (x - filtration duration, min.; Y1 - filtration volume, ml; Y2 - turbidity ml/l; R2 - approximation reliability) to confirm this model.
a
■
»■
BZ -
I BO-
■7/ M SS -
Ô se
SJ
- /
8Î ■ /
!
BO j 1
— ■— I 3tm. >— 3 atm.
- i 5 atm.
Oí
5.4
ae at id
Filtration time, hciui
11
■ - 1 atm. ♦ - 3 Btm. - 5 atm
o 6 OS l.Q
":1|J;ICLLML [IIIILV Iichit b
1 2
VJ
Fig. 6. Selectivity dependence in terms to color (a) and turbidity (b) of permeate on filtration duration at different pressures
Mathematical model of sodium humate filtration process:
Y ^x ^ &Q x+^2 x +&3 x
(3)
This is curve equation of third degree or which has third degree polynomial form with respect to variable Y. This is typical cubic model example that can be used to describe sodium humate filtering process through UPM-20 membrane at pressure from 1 to 5 atm.
As a result of experimental data mathematical processing equations that describe dependence of output variables on selected technological filtering process factor were obtained:
a) Mathematical model based on volume indicator for filtering at 1 atm.
Y1 = 61.583 - 1.219x + 0.0199X - 0.000106x3 (R2 = 0.9299)
Mathematical model based on the turbidity index for filtering at 1 atm.
Y2 = 16.983 - 0.576x + 0.00955X - 4.924 • 10-5x3 (R2 = 0.9572)
b) Mathematical model based on volume indicator for filtering at 3 atm.
Yi = 168.952 - 3.371x + 0.0366X - 0.000139X (R2 = 0.9758)
Mathematical model based on the turbidity index for filtering at 3 atm.
Y2 = 16.556 - 0.216x + 0.000985X + 1.684 • 10-6x3 (R2 = 0.9567)
c) Mathematical model based on volume indicator for filtering at 5 atm
Yi = 184.0476 - 3.833x + 0.0339X2 - 9.596 • 10-5x3 (R2 = 0.9852)
Mathematical model based on the turbidity index for filtering at 5 atm.
Y2 = 15.212 - 0.405x + 0.00666x2 - 3.636 • 10-5x3 (R2 = 0.9933)
It can be concluded that in case of pressure increasing the volume at the initial point of filtration namely in first 10 minunes the biggest. This indicates that UPM-20 membrane pores are not blocked at the beginning of humate purification process. The coefficient ai decreases in case of bigger pressure value which indicates decreasing in permeate volume during further filtering due to clogging pores in UPM-20 membrane with pollutants from concentrate. Filtering process continues with non-linear dependence, so pores in UPM-20 membrane become clogged with increasing filtration duration.
Similar dependence is observed during permeate turbidity index determining. Value of coefficient ao shows that pressure increasing in filtration process has slight effect on permeate turbidity value. Coefficient a1 for 5 atm. has smaller value than at 1 and 3 atm which indicates filtering efficiency at high pressures and at the same time coefficients a2 and a3 have low values due to nonlinear dependence presence only at the beginning of sodium humate purification process.
a
i ,
S "9
% 100 H
90 SO
to
g
J 120
<5
SO
10
a (1)
Amiel vjIiios ---I^rc dieted lain«
i-
i12 —
11 10
JO w co so
FilliTiup ri 11"ii_'. mill
a (2)
■\mifll viiliio; I'istiiusti haLuii
M
i:
60 50
Tillcrmjc I i :33c. jlihi
20
b(l)
' Actual value»
---i'reilicird
40 60 S-0
FLIlcxinie Lunc. iilui
b (2)
Actual values - - ■ P№l{cit(l vfiliKi
40
№ SO
rilkTii: t lirnt miii
100
a (3)
b (3)
Fig. 7. Dependence of permeate volume (a) and turbidity (b) on duration filtering at different pressures:
1 - 1 atm; 2 - 3 atm; 3 - 5 atm
Conclusions
Conducted studies of filtering properties polysulfonamide membrane UPM-20 using model solution of sodium humate showed that membrane performance decreases with increasing process pressure and duration. Membrane selectivity increases to 96.0 and 97.2% respectively in terms of permeate color and turbidity. The efficiency of removing contaminants through membrane stay better with pressure increasing but at the same time with decreasing in membrane performance.
The construction of mathematical model of filtration process was carried out. A nonlinear dependence of filtration process was obtained. Results indicates that effectiveness UPM-20 membrane under stable conditions, constant pressure have high degree of permeate purification.
Bibliography
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2. Barth C. Asymmetric polysulfone and polyethersulfone membranes: effects of thermodynamic conditions during formation on their performance. Membr. Science, 2000. Vol. 169. P. 287-299. URL: https://doi.org/10.1016/ S0376-7388(99)00344-0
3. Gardi I., Mishael Y. G. Designing a regenerable stimuli-responsive grafted polymer-clay sorbent for filtration of water pollutants. Science and Technology of Advanced Materials, 2018. Vol. 19 (1). P. 588-598. URL: https://doi.org/10 .1080/14686996.2018.1499381
4. Medici S., Peana M., Grisponi G., Nourchi V Silver coordination compounds: A new horizon in medicine. Coordination Chemistry Reviews, 2016. Vol. 327-32. P. 349-359. URL: http://dx.doi.org/10.1016/j.ccr.2016.05.015
5. Fionah A., McLarney K., Judd A., Escobar I. Effects of the Applied Potential on the Performance of Polysulfone Membranes Functionalized with Sulfonated Polyether Ether Ketone Polymers. Membranes, 2023. Vol. 13(7). P. 1-24. URL: https://doi.org/10.3390/membranes13070675
6. D. M. Warsinger, S. Chakraborty, E. W. Tow, D. Jassby. A review of polymeric membranes and processes for potable water reuse. Progress in Polymer Science, 2018. Vol. 81. P. 209-234.
7. Mou P., Jons S. D. Chemistry and fabrication of polymeric nanofiltration membranes. Polymer, 2016. Vol. 103. P. 417-456. URL: http://dx.doi.org/10.1016/j.polymer.2016.07.085
8. Templeman K., Casanova S., Benes N. E. The effect of hydrocarbon pollution on polysulfone-based membranes in aqueous separations. Separation and Purification Technology, 2019. Vol. 224. P. 348-355. URL: http://dx.doi. org/10.1016/j.seppur.2019.05.013
9. Kim I. C., Yun H. G., Lee K. H. Preparation of asymmetric polyacrylonitrile membrane with small pore size by phase inversion and post-treatment process. Journal of Membrane Science, 2002. Vol. 199. P. 75-84.
10. Tai-Horng Y., Jhi-Hsien H., Wen-Yuan C. Effect of evaporation temperature on the formation of particulate membranes from crystalline polymers by drycast process. Eur. Polym. J., 2002. Vol. 388(1). P. 63-72. URL: http://dx.doi. org/10.1016/S0014-3057(01)00183-5
11. Feng L., Jun Z., Xiaolin W., Jianfei C., Zhongzi X. Gaofenzi xuebao. Acta. Polym. Sin, 2002. Vol. 5. P. 566-571.
12. He Y., Uehara S., Takana H., Nishiyama H. Numerical Modelling and Simulation of Chemical Reactions in a Nano-Pulse Discharged Bubble for Water Treatment. Plasma Science and Technology, 2016. Vol.18 (9). P. 924-932. URL: http://dx.doi.org/10.1088/1009-0630/18/9/09
13. Nadezhdin I., Papasidero D., Goryunov A., Manenti F. Optimisation of EDM process for water purification. Chemical Engineering Transactions, 2016. Vol. 52. P. 325-330. URL: https://doi.org/10.3303/CET1652055
14. Oleynik O., Airapetian T., Kurganska S. Evaluation of the performance of aerotanks due to add-on attached biocenosis. Science and Transport Progress, 2019. Vol. 4(82). P. 37-46. URL: https://doi.org/10.15802/stp2019/175883
15. Rezakazemi M., Ghafarinazari A., Shirazian S., Hoshsima A. Numerical Modeling and Optimization of Wastewater Treatment Using Porous Polymeric Membranes. Polymer Engineering and Science, 2013. Vol. 53(6). P. 1272-1278. URL: http://dx.doi.org/10.1002/pen.23375
16. Viccione G., Evangelista S. Experimental and numerical analysis of the hydraulic performance of filtering cartridges for water treatment. HIC 2018. 13th International Conference on Hydroinformatics. EPiC Series in Engineering. Palermo, Italy, July 1-6, 2018. P. 2187-2195. URL: https://doi.org/10.29007/b26c
References
1. Hoffman C., Silau H., Pinelo M., Woodley J. M., Daugaard A. E. (2018). Surface modification of polysulfone membranes applied for a membrane reactor with immobilized alcohol dehydrogenase. Separation and Purification Technology, 14, 82-89. http://dx.doi.org/10.1016/j.mtcomm.2017.12.019
2. Barth C. (2000). Asymmetric polysulfone and polyethersulfone membranes: effects of thermodynamic conditions during formation on their performance. Membr. Science, 169, 287-299. https://doi.org/10.1016/S0376-7388(99)00344-0
3. Gardi I., Mishael Y. G. (2018). Designing a regenerable stimuli-responsive grafted polymer-clay sorbent for filtration of water pollutants. Science and Technology of Advanced Materials, 19(1), 588-598. https://doi.org/10.1080A 4686996.2018.1499381
4. Medici S., Peana M., Grisponi G., Nourchi V. (2016). Silver coordination compounds: A new horizon in medicine. Coordination Chemistry Reviews, 327-32, 349-359. http://dx.doi.org/10.1016/j.ccr.2016.05.015
5. Fionah A., McLarney K., Judd A., Escobar I. (2023). Effects of the Applied Potential on the Performance of Polysulfone Membranes Functionalized with Sulfonated Polyether Ether Ketone Polymers. Membranes, 13(7), 1-24. https://doi.org/10.3390/membranes13070675
6. D. M. Warsinger, S. Chakraborty, E. W. Tow, D. Jassby. (2018). A review of polymeric membranes and processes for potable water reuse. Progress in Polymer Science, 81, 209-234.
7. Mou P., Jons S. D. (2016). Chemistry and fabrication of polymeric nanofiltration membranes. Polymer, 103, 417-456. http://dx.doi.org/10.1016/j.polymer.2016.07.085
8. Templeman K., Casanova S., Benes N. E. (2019). The effect of hydrocarbon pollution on polysulfone-based membranes in aqueous separations. Separation and Purification Technology, 224, 348-355. http://dx.doi.org/10.1016/j. seppur.2019.05.013
9. Kim I. C., Yun H. G., Lee K. H. (2002). Preparation of asymmetric polyacrylonitrile membrane with small pore size by phase inversion and post-treatment process. Journal of Membrane Science, 199, 75-84.
10. Tai-Horng Y., Jhi-Hsien H., Wen-Yuan C. (2002). Effect of evaporation temperature on the formation of particulate membranes from crystalline polymers by drycast process. Eur. Polym. J., 388(1), 63-72. http://dx.doi.org/10.1016/ S0014-3057(01)00183-5
11. Feng L., Jun Z., Xiaolin W., Jianfei C., Zhongzi X. (2002) Gaofenzi xuebao. Acta. Polym. Sin, 5, 566-571.
12. He Y., Uehara S., Takana H., Nishiyama H. (2016). Numerical Modelling and Simulation of Chemical Reactions in a Nano-Pulse Discharged Bubble for Water Treatment. Plasma Science and Technology, 18 (9), 924-932. http://dx.doi. org/10.1088/1009-0630/18/9/09
13. Nadezhdin I., Papasidero D., Goryunov A., Manenti F. (2016). Optimisation of EDM process for water purification. Chemical Engineering Transactions, 52, 325-330. https://doi.org/10.3303/CET1652055
14. Oleynik O., Airapetian T., Kurganska S. (2019). Evaluation of the performance of aerotanks due to add-on attached biocenosis. Science and Transport Progress, 4(82), 37-46. https://doi.org/10.15802/stp2019/175883
15. Rezakazemi M., Ghafarinazari A., Shirazian S., Hoshsima A. (2013). Numerical Modeling and Optimization of Wastewater Treatment Using Porous Polymeric Membranes. Polymer Engineering and Science, 53(6), 1272-1278. http:// dx.doi.org/10.1002/pen.23375
16. Viccione G., Evangelista S. (2018). Experimental and numerical analysis of the hydraulic performance of filtering cartridges for water treatment. HIC 2018.13th International Conference on Hydroinformatics. EPiC Series in Engineering. Palermo, Italy, July 1-6, 2187-2195. https://doi.org/10.29007/b26c
