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    Wyświetlanie 1-11 z 11
    Tytuł:
    Water demineralization by membrane distillation utilizing cooling water from municipal waste incinerator
    Autorzy:
    Gryta, M.
    Powiązania:
    https://bibliotekanauki.pl/articles/779741.pdf
    Data publikacji:
    2018
    Wydawca:
    Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
    Tematy:
    demineralized water
    membrane distillation
    scaling
    waste incinerator
    Opis:
    The membrane distillation performance was studied for production of demineralized water from surface water (river). Hot water from cooling water system of municipal waste incinerator was considered as an energy source for membrane distillation. The integration of membrane installation with such cooling water system allows to re-use up to 18 kW per 1 m2  of the membranes. The studies were performed with the application of polypropylene capillary membranes Accurel PP S6/2. The membrane modules were supplied with the feed heated to a temperature of 310 K and 330 K. The permeate flux obtained for these temperatures was 2.8 and 9.7 L/m2  h, and the distillate conductivity was 6 and 4 S/cm, respectively. The water demineralisation process was carried out for 1200 h without module cleaning. The behaviour of the permeate flux and distillate conductivity indicate that used membranes maintained their non-wettability over tested period. The performed SEM-EDS examinations confirmed, that the deposits did not fill the pores and were mainly formed on the membrane surface. The scaling intensity was definitely smaller for lower temperature (310 K) of the feed. The amorphous deposits containing beside Ca also substantial amounts of the Si were mainly formed under these conditions, whereas at higher feed temperature dominated CaCO3  scaling.
    Źródło:
    Polish Journal of Chemical Technology; 2018, 20, 3; 65-74
    1509-8117
    1899-4741
    Pojawia się w:
    Polish Journal of Chemical Technology
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
    Tytuł:
    Separation of volatile compounds from fermentation broth by membrane distillation
    Autorzy:
    Gryta, M.
    Barancewicz, M.
    Powiązania:
    https://bibliotekanauki.pl/articles/778881.pdf
    Data publikacji:
    2011
    Wydawca:
    Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
    Tematy:
    fermentacja
    etanol
    destylacja membranowa
    fermentation
    ethanol
    membrane distillation
    Opis:
    The diluted ethanol solutions and fermentation broth (Saccharomyces cerevisiae) were separated by membrane distillation (MD). Hydrophobic macroporous (pore size 0.2 ěm) capillary polypropylene membranes, Accurel PP V8/2 HF and Accurel PP S6/2, were used for these studies. The MD process can be successfully applied to remove the volatile components from the fermentation broth. Besides ethanol, propionic and acetic acids were moved from the broth to the distillate. Therefore, the course of the fermentation carried out in a membrane distillation bioreactor considerably accelerate its rate and increase the efficiency by a selective removal of fermentation products. It was found that the broth subjected to the separation did not affect the hydrophobic properties of the polypropylene membrane assembled in the MD modules.
    Źródło:
    Polish Journal of Chemical Technology; 2011, 13, 3; 56-60
    1509-8117
    1899-4741
    Pojawia się w:
    Polish Journal of Chemical Technology
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
    Tytuł:
    Separation of HCl from the mixture of KCl and HCl using membrane distillation
    Autorzy:
    Tomaszewska, M.
    Mientka, A.
    Powiązania:
    https://bibliotekanauki.pl/articles/779695.pdf
    Data publikacji:
    2008
    Wydawca:
    Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
    Tematy:
    wydzielanie HCl
    destylacja membranowa
    HCl separation
    membrane distillation
    Opis:
    Membrane distillation (MD) was applied for the concentration of solutions containing hydrochloric acid and potassium chloride. The studies of the concentration and separation of HCl through the hydrophobic membrane were performed. In the investigations plate and frame or capillary modules, equipped with membranes from polytetrafluoroethylene and polypropylene were applied, respectively. The feed temperature amounted to 333 K or 343 K and permeate 293 K at the inlet of the module. Under the MD operation conditions the transfer of water vapour and hydrogen chloride from potassium chloride and hydrochloric acid solutions through the hydrophobic membranes took place, whereas the potassium chloride as a nonvolatile component underwent concentration in the feed. The influence of acid concentration and salt presence in the feed on the HCl molar flux through the membrane was systematically studied. The increase of the temperature and salt concentration in the feed caused higher partial pressure volatile of HCl and the resultant HCl Flux through a membrane was higher. During MD for the initial concentration in the feed equal 50 g KCl/dm3 and 40g HCl/dm3, at the feed temperature 343K, the permeate flux decreased from 353 dm3/m2d to 289 dm3/m2d, whereas the HCl flux increased to 6 mol/m2d for the capillary module. At higher KCl concentration in the feed, amounting to 100g KCl/dm3 and under the same operation conditions, the permeate flux decreased to 285 dm3/m2d, but the molar flux HCl increased to 18 mol/m2d. The results were compared with the data obtained for the plate and frame module.
    Źródło:
    Polish Journal of Chemical Technology; 2008, 10, 2; 27-32
    1509-8117
    1899-4741
    Pojawia się w:
    Polish Journal of Chemical Technology
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
    Tytuł:
    Concentration of FeSO4 spent solutions by membrane distillation
    Autorzy:
    Gryta, M.
    Powiązania:
    https://bibliotekanauki.pl/articles/779957.pdf
    Data publikacji:
    2007
    Wydawca:
    Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
    Tematy:
    destylacja membranowa
    ścieki
    FeSO4
    membrane distillation
    wastewater
    Opis:
    The possibility of potential application of membrane distillation for the concentration of waste salt solutions has been presented in this work. It was found that the oxidation of iron compounds takes place during the process that was associated with the formation of a layer of oxides on the membrane surface. A fast decline of the permeate flux was observed due to the scaling phenomena. The problem of scaling was eliminated by the acidification with H2SO4 of the feed to the pH value of 2.
    Źródło:
    Polish Journal of Chemical Technology; 2007, 9, 2; 15-18
    1509-8117
    1899-4741
    Pojawia się w:
    Polish Journal of Chemical Technology
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
    Tytuł:
    Membranowy moduł kapilarny z podwójnie uszczelnioną głowicą
    Capillary membrane module with a double sealing head
    Autorzy:
    Gryta, M.
    Powiązania:
    https://bibliotekanauki.pl/articles/2070863.pdf
    Data publikacji:
    2010
    Wydawca:
    Stowarzyszenie Inżynierów i Techników Mechaników Polskich
    Tematy:
    moduł membranowy
    membrana kapilarna
    destylacja membranowa
    membrane module
    capillary membranes
    membrane distillation
    Opis:
    Przedstawiono głowicę modułu kapilarnego z dwoma warstwami klejenia membran kapilarnych, rozdzielonymi szczeliną powietrzną. Uszkodzenie klejenia powoduje przeciek do komory pomiędzy klejeniami, skąd ciecz swobodnie wypływa na zewnątrz nie zanieczyszczając destylatu. Skuteczność pracy nowej konstrukcji modułu potwierdzono w badaniach długoterminowych.
    A new design of capillary module head with two layers of epoxy resin separated by air-gap was presented. In case of potting failure the leakage of feed into the air-gap proceeds. The feed flows out from this air-gap preventing distillate contamination. The long-tenn investigations confirmed a good efficiency of the design presented.
    Źródło:
    Inżynieria i Aparatura Chemiczna; 2010, 1; 45-46
    0368-0827
    Pojawia się w:
    Inżynieria i Aparatura Chemiczna
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
    Tytuł:
    Evaluation of Performance of Hybrid Photolysis-DCMD and Photocatalysis-DCMD Systems Utilizing UV-C Radiation for Removal of Diclofenac Sodium Salt From Water
    Autorzy:
    Mozia, S.
    Darowna, D.
    Przepiórski, J.
    Morawski, A.W.
    Powiązania:
    https://bibliotekanauki.pl/articles/779272.pdf
    Data publikacji:
    2013
    Wydawca:
    Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
    Tematy:
    photocatalytic membrane reactor,
    direct contact membrane distillation
    photolysis
    photocatalysis
    diclofenac sodium salt
    Opis:
    The removal of a non-steroidal anti-inflammatory drug (NSAID) diclofenac sodium salt (DCF, C14H10Cl2NNaO2) from water in two hybrid systems coupling photolysis or photocatalysis with direct contact membrane distillation (DCMD) is presented. A UV-C germicidal lamp was used as a source of irradiation. The initial concentration of DCF was in the range of 0.005-0.15 mmol/dm3 and the TiO2 AeroxideŽ P25 loading (hybrid photocatalysis-DCMD) ranged from 0.05 to 0.4 g/dm3. Regardless of the applied hybrid system and the initial concentration of DCF, the model drug was completely decomposed within 4h of irradiation or less. Mineralization was less efficient than photodecomposition. In case of the hybrid photolysis-DCMD process the efficiency of TOC degradation after 5h of irradiation ranged from 27.3-48.7% depending on the DCF initial concentration. The addition of TiO2 allowed to improve the efficiency of TOC removal. The highest degradation rate was obtained at 0.3 gTiO2/dm3. During the process conducted with the lowest DCF initial concentrations (0.005-0.025 mmol/dm3) a complete mineralization was obtained. However, when higher initial amounts of DCF were used (0.05-0.15 mmol/dm3), the efficiency of TOC degradation was in the range of 82.5-85%. The quality of distillate was high regardless of the system: DCF was not detected, TOC concentration did not exceeded 0.7 mg/dm3 (1.9 mg/dm3 in permeate) and conductivity was lower than 1.6 žS/cm.
    Źródło:
    Polish Journal of Chemical Technology; 2013, 15, 1; 51-60
    1509-8117
    1899-4741
    Pojawia się w:
    Polish Journal of Chemical Technology
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
    Tytuł:
    Technological improvement of the Sorghum saccharatum syrup production by membrane technologies
    Autorzy:
    Chibrikov, Vadym
    Vakuliuk, Polina
    Hryhorenko, Nataliia
    Gunko, Sergiy
    Sobczuk, Henryk
    Powiązania:
    https://bibliotekanauki.pl/articles/2174335.pdf
    Data publikacji:
    2022
    Wydawca:
    Instytut Technologiczno-Przyrodniczy
    Tematy:
    juice clarification
    juice concentration
    membrane distillation
    Sorghum saccharatum
    sweet sorghum syrup
    ultrafiltration
    Opis:
    Easy-to-handle and effective methods of juice clarification and concentration by membrane technologies are still under exploration. The current article presents results of research on the technological development of an alternative natural sweetener of high biological value and improved organoleptic properties. Sorghum saccharatum stem juice is used in research. It is pre-clarified enzymatically with α-amylase and glucoamylase, clarified by ultrafiltration, and concentrated by the direct contact membrane distillation in various temperature ranges. The study shows the efficacy of membrane methods for improving juice purity, total soluble solids (TSS), and total sugar (TS) content in the syrup obtained. Clarification depends on membrane characteristics at the beginning of the process, as there are no differences at the end of it. Juice concentration at high-temperature differences allows to accelerate the process by approx. 60% comparing to low-temperature differences. A lower temperature difference (∆Т = 20-30°С) in the concentration process results in a longer process and syrup acidisation, whereas a higher temperature difference (∆Т = 70°С) affects physicochemical properties of syrup due to local overheating and formation of Maillard reaction products. The juice concentration at ∆Т = 50-60°С allows to obtain high values of total soluble solids without significant degradation of physicochemical and organoleptic properties.
    Źródło:
    Journal of Water and Land Development; 2022, 54; 131--137
    1429-7426
    2083-4535
    Pojawia się w:
    Journal of Water and Land Development
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
    Tytuł:
    Scaling diminution by heterogeneous crystallization in a filtration element integrated with membrane distillation module
    Autorzy:
    Gryta, M.
    Powiązania:
    https://bibliotekanauki.pl/articles/779308.pdf
    Data publikacji:
    2009
    Wydawca:
    Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
    Tematy:
    destylacja membranowa
    moduł kapilarny
    odsalanie wody
    membrane distillation
    capillary module
    scaling
    water desalination
    Opis:
    Water desalination by membrane distillation is restricted by calcium carbonate precipitation on the membrane surface, what resulted in a progressive decline of the permeate flux. The module rinsing by HCl solution removed this deposit, however, such operation could cause the membrane wettability, associated with lowering of the permeate flux. This phenomenon was inhibited when the membrane modules with prefiltration element, assembled directly at the inlet to module, were used. The salt deposits were formed mainly on the surface of the filtration element (nets area constituted over 10% of the membranes area), what protected the membranes assembled inside the module. The filter efficiency decreased when the deposit layer covered the entire surface of pre-filter element, and after a few hours (period of 10-20 h) the formation of crystallite on the membrane surface was also observed. Therefore, the formed deposit was systematically removed (at every 5 h) from this pre-filter by 3 wt.% HCl solutions. The periodical rinsing of nets by acid did not have a negative influence on the membrane.
    Źródło:
    Polish Journal of Chemical Technology; 2009, 11, 2; 60-65
    1509-8117
    1899-4741
    Pojawia się w:
    Polish Journal of Chemical Technology
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
    Tytuł:
    The investigation of ethanol separation by the membrane distillation process
    Autorzy:
    Tomaszewska, M.
    Białończyk, L.
    Powiązania:
    https://bibliotekanauki.pl/articles/778875.pdf
    Data publikacji:
    2011
    Wydawca:
    Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
    Tematy:
    destylacja membranowa
    bioreaktor
    etanol
    zanurzone membrany kapilarne
    membrane distillation
    bioreactor
    ethanol
    immersed capillary membranes
    Opis:
    Separation of ethanol from solutions with different concentrations in a BIOTRON bioreactor integrated with the direct contact membrane distillation system has been investigated. The experiments were carried out using immersed, capillary polypropylene membranes. The permeability of the membrane at the feed inlet temperatures of 308, 318 and 333K was determined. The permeate and ethanol flux was strongly affected by the vapour pressure which increased with the feed temperature and it was also associated with ethanol concentration in the feed. It was found that the membrane distillation can be successfully applied for the separation of volatile components such as ethanol.
    Źródło:
    Polish Journal of Chemical Technology; 2011, 13, 3; 66-69
    1509-8117
    1899-4741
    Pojawia się w:
    Polish Journal of Chemical Technology
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
    Tytuł:
    Zatężanie roztworów 1,3-propanodiolu metodą destylacji membranowej
    Concentration of 1,3-propanediol solutions by membrane distillation
    Autorzy:
    Gryta, M.
    Powiązania:
    https://bibliotekanauki.pl/articles/2072388.pdf
    Data publikacji:
    2013
    Wydawca:
    Stowarzyszenie Inżynierów i Techników Mechaników Polskich
    Tematy:
    destylacja membranowa
    1,3-propanodiol
    glicerol
    zatężanie roztworów
    membrane distillation
    1,3-propanediol
    glycerol
    solution concentration
    Opis:
    Proces destylacji membranowej wykorzystano do zatężania roztworów 1,3-propanodiolu, uzyskując ponad 99,6% zatrzymanie alkoholu w koncentracie. W procesie zastosowano kapilarne membrany Accurel PP. Przeprowadzone długoterminowe badania zatężania (ponad 600 h) wykazały dobrą odporność użytych membran polipropylenowych na zwilżanie.
    Membrane distillation process was utilized for the concentration of 1,3-propanediol solutions resulting in the retention of alcohol in retentate by more than 99.6%. Long-term studies of the concentration carried out for over 600 h had demonstrated a good resistance to wettability of used polypropy¬lene Accurel PP membranes.
    Źródło:
    Inżynieria i Aparatura Chemiczna; 2013, 5; 421--422
    0368-0827
    Pojawia się w:
    Inżynieria i Aparatura Chemiczna
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
    Tytuł:
    Application of pervaporation and osmotic membrane distillation to the regeneration of spent solutions from the osmotic food dehydration
    Autorzy:
    Kujawski, W.
    Gierszewska-Drużyńska, M.
    Warczok, J.
    Güell, C.
    Powiązania:
    https://bibliotekanauki.pl/articles/779332.pdf
    Data publikacji:
    2009
    Wydawca:
    Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
    Tematy:
    przetwórstwo spożywcze
    roztwory odpadowe
    zarządzanie odpadami
    perwaporacja
    destylacja membranowa
    destylacja osmotyczna
    food processing
    spent solution management
    pervaporation
    osmotic membrane distillation
    Opis:
    Results of pervaporation (PV) of sucrose and calcium chloride spent solutions were presented. Additionally, osmotic membrane distillation (OMD) of sucrose solutions was investigated. It was found that the regeneration of spent sucrose solution for the reuse is possible by using PV or OMD processes. However, OMD process produces another spent stream i.e. CaCl2. Pervaporation membranes showed fluxes in the range of 0.5 - 0.9 kg m^-2 h^-1 in contact with 40° Brix sucrose solution, whereas OMD water permeate fluxes were in the range of 4 - 5 kg m^-2 h^-1 for the same feed concentration. Two different hybrid processes were suggested: i) pretreatment followed by OMD reconcentration of spent sucrose solution and independently PV for CaCl2 regeneration; ii) membrane pretreatment (MP) followed by PV of sucrose solution. Based on the experimental results, the membrane areas for both systems were calculated and compared. MP-PV system seems to be a better solution for the spent mixtures management.
    Źródło:
    Polish Journal of Chemical Technology; 2009, 11, 2; 41-45
    1509-8117
    1899-4741
    Pojawia się w:
    Polish Journal of Chemical Technology
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
      Wyświetlanie 1-11 z 11

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