Relevant bibliographies by topics / Permeace

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  2. Dissertations / Theses
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  4. Book chapters
  5. Conference papers
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Academic literature on the topic 'Permeace'

Author: Grafiati
Published: 4 June 2021
Last updated: 5 February 2022

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Journal articles on the topic "Permeace"

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Sawamura, Okamoto, and Todokoro. "Development of Mass Production Technology of Highly Permeable Nano-Porous Supports for Silica-Based Separation Membranes." Membranes 9, no. 8 (August 16, 2019): 103. http://dx.doi.org/10.3390/membranes9080103.

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Silica-based membranes show both robust properties and high-permeability, offering us great potential for applying them to harsh conditions where conventional organic membranes cannot work. Despite the increasing number of paper and patents of silica-based membranes, their industrial applications have yet to be fully realized, possibly due to their lack of technologies on scaling-up and mass production. In particular, quality of membrane supports decisively impacts final quality of silica-based separation membranes. In this study, therefore, we have developed mass producing technologies of nano-porous supports (φ 12 mm, length 400 mm) with surface center pore size distribution of 1–10 nm, which are generally used as supports for preparing separation membranes with a pore size of less than 1 nm. The developed mass production apparatuses have enabled us to reproducibly produce nano-porous silica-based supports with high permeance (e.g., N2 permeance of more than 10−5 mol m−2 s−1·Pa−1) minimizing effects of membrane defects less than 0.1% of the total flux. The developed nano-porous supports have enabled us to reproducibly produce silica-based separation membranes with high permeace and selectivity (e.g., H2 permeance of about 5 × 10−6 mol m−2 s−1 Pa−1 and H2/SF6 permeance ratio of more than 2000).
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SCHINGOETHE, D. J., D. P. CASPER, W. J. COSTELLO, and D. G. ROLLINS. "ULTRAFILTRATED WHEY PERMEATE PRODUCTS FOR GROWING-FINISHING STEERS." Canadian Journal of Animal Science 68, no. 4 (December 1, 1988): 1309–14. http://dx.doi.org/10.4141/cjas88-149.

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A 119-d field study with 50 Holstein steers weighing 408 ± 16 kg at the start evaluated feeding ultrafiltrated permeate of whey or three products made from additional processing of the permeate. Liquid permeates provided more than 17% of total dry matter intake while concentrated, ammoniated permeates provided more than 26% of crude protein intake. All whey permeate products tested were utilized well as indicated by weight gains, feed consumption, and carcass quality. Key words: Whey, whey products, cattle
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Koester, S., F. Roghmans, and M. Wessling. "Water vapor permeance: The interplay of feed and permeate activity." Journal of Membrane Science 485 (July 2015): 69–78. http://dx.doi.org/10.1016/j.memsci.2015.03.019.

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Beck, Thomas, Anja Schmidt, and Michael N. Hall. "Starvation Induces Vacuolar Targeting and Degradation of the Tryptophan Permease in Yeast." Journal of Cell Biology 146, no. 6 (September 20, 1999): 1227–38. http://dx.doi.org/10.1083/jcb.146.6.1227.

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In Saccharomyces cerevisiae, amino acid permeases are divided into two classes. One class, represented by the general amino acid permease GAP1, contains permeases regulated in response to the nitrogen source. The other class, including the high affinity tryptophan permease, TAT2, consists of the so-called constitutive permeases. We show that TAT2 is regulated at the level of protein stability. In exponentially growing cells, TAT2 is in the plasma membrane and also accumulates in internal compartments of the secretory pathway. Upon nutrient deprivation or rapamycin treatment, TAT2 is transported to and degraded in the vacuole. The ubiquitination machinery and lysine residues within the NH2-terminal 31 amino acids of TAT2 mediate ubiquitination and degradation of the permease. Starvation-induced degradation of internal TAT2 is blocked in sec18, sec23, pep12, and vps27 mutants, but not in sec4, end4, and apg1 mutants, suggesting that, upon nutrient limitation, internal TAT2 is diverted from the late secretory pathway to the vacuolar pathway. Furthermore, our results suggest that TAT2 stability and sorting are controlled by the TOR signaling pathway, and regulated inversely to that of GAP1.
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Aspiyanto, Aspiyanto, Agustine Susilowati, and Yati Maryati. "SEPARATION OF SAVORY FRACTION FROM AUTOLYSATE OF KIDNEY BEAN (Phaseolus vulgaris L.) FERMENTED BY Rhizopus sp-PL19 THROUGH CROSS-FLOW MICROFILTRATION (CFMF) MEMBRANE MODULE." Jurnal Kimia Terapan Indonesia 16, no. 1 (June 10, 2014): 39–48. http://dx.doi.org/10.14203/jkti.v16i1.7.

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Separation of savory fraction from autolysate of kidney bean (Phaseolus vulgaris L.) fermented by Rhizopus sp.-PL19 as potential seasoning agent was performed using cross-flow microfiltration (CFMF) technique in module scale. The goal of this experiment was to find out the effect of pressure and time on performance of MF membrane, and compositions of retentate and permeate. The result of experiment showed that separation and/or purification using CFMF technique gave permeate as savory fraction with better clearness and sharper aroma than retentate, but retentate had better composition than permeate. During separation increased total protein, dissolved protein and salt concentrations, but decreased total solid, reducing sugar and fat concentrations in permeate at pressure of 2 and 4 bar. Based on N-Amino concentration in permeate, the optimum condition of separation was reached at pump motor frequency of 10 Hz and room temperature with pressure of 2 and 4 bar for 10 minutes. This condition produced permeate with fluxes of 51.11 and 52.55 L/m2.hour, and concentrations of N-Amino of 5.50 and 9.80 mg/mL, dissolved protein of 1.01 and 0.97 mg/mL, total protein of 4.85 and 12.10 % (dry weight), reducing sugar of 55.75 and 53.75 mg/mL, salt of 1.16 and 1.06 %, fat of 0.41 and 0.65 %, and total solids of 7.82 and 6.35 %, respectively. Keywords : Autolysate, kidney bean (Phaseolus vulgaris L.), Rhizopus sp.-PL19, cross-flow microfiltration (CFMF), permeate, retentate. Pemisahan fraksi gurih dari autolisat kacang merah (Phaseolus vulgaris L.) terfermentasi oleh Rhizopus sp.-PL19 sebagai bahan seasoning potensial dilakukan menggunakan teknik mikrofiltrasi cross-flow (MFCF) pada modul.Penelitian bertujuan untuk mencari pengaruh tekanan dan waktu pemisahan terhadap kinerja membran mikrofiltrasi (MF) dan komposisi dalam retentat dan permeat. Hasil penelitian menunjukan bahwa pemisahan dan/atau pemurnian menggunakan teknik MFCF memberikan permeat sebagai fraksi gurih savory dengan kejernihan lebih baik dan aroma lebih tajam daripada retentat, tetapi retentat memiliki komposisi lebih baik daripada permeat. Pemisahan dengan waktu lama menaikkan konsentrasi total protein, protein terlarut dan garam, namun mengurangi konsentrasi total padatan, gula pereduksi dan lemak dalam permeat pada tekanan 2 dan 4 bar. Berdasarkan konsentrasi N-Amino dalam permeat, kondisi optimum pada pemisahan dicapai dibawah frekuensi motor pompa 10 Hz dan suhu ruang dengan tekanan 2 dan 4 bar selama 10 menit. Kondisi ini menghasilkan permeat dengan fluks masing-masing 51,11 dan 52,55 L/m2.jam serta konsentrasi N-Amino of 5,50 dan 9,80 mg/mL, protein terlarut 1,01 dan 0,97 mg/mL, total protein 4,85 dan 12,10 % (berat kering), gula pereduksi 55,75 dan 53,75 mg/mL, garam 1,16 dan 1,06 %, lemak 0,41 dan 0,65 % serta total padatan 7,82 dan 6,35 %. Kata kunci : Autolisat, kacang merah (Phaseolus vulgaris L.), Rhizopus sp.-PL19, mikrofiltrasi cross-flow (CFMF), permeat, retentat.
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Duan, Shuhong, Teruhiko Kai, and Shin-ichi Nakao. "Effect of Carbonic Anhydrase on CO2 Separation Performance of Thin Poly(amidoamine) Dendrimer/Poly(ethylene glycol) Hybrid Membranes." Membranes 9, no. 12 (December 5, 2019): 167. http://dx.doi.org/10.3390/membranes9120167.

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The effect of carbonic anhydrase (CA) on the separation performance of thin poly(amidoamine) (PAMAM) dendrimer/poly(ethylene glycol) (PEG) hybrid membranes was investigated. CA, a type of enzyme, was used to promote CO2 hydration and dehydration reactions and to assess whether these reactions were the rate-limiting step in CO2 permeation through the membrane. The relationship between the membrane thickness and the CO2 permeance was evaluated in CO2/H2 or CO2/He separation using PAMAM/PEG hybrid membranes (thickness: 10–100 μm) with and without CA. Without CA, the CO2 permeance of PAMAM/PEG hybrid membranes was not inversely proportional to the membrane thickness. On the other hand, with CA, the CO2 permeance was inversely proportional to the membrane thickness. It was implied that, without CA, the rate-limiting step of CO2 transport was either the CO2 hydration reaction at the feed side or the CO2 dehydration reaction at the permeate side. On the other hand, with CA addition, the rate-limiting step of CO2 transport was diffusion, and CO2 permeance could be increased without sacrificing the selectivity by reducing membrane thickness. The effect of the position of CA (i.e., on the surface and/or reverse surface) on CO2 separation performance was investigated to evaluate which reaction was the rate-limiting step of CO2 permeation through the membrane. It was suggested that the rate-limiting step of CO2 permeation was CO2 dehydration reaction at the permeate side.
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Tupasela, Tuomo, Heikki Koskinen, and Pirkko Antila. "Whey pretreatments before ultrafiltration." Agricultural and Food Science 3, no. 5 (September 1, 1994): 473–79. http://dx.doi.org/10.23986/afsci.72719.

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Whey is a by-product of cheesemaking. Whey dry matter contains mainly lactose, but also valuable whey proteins. The aim of this study was to develop improvements to whey protein membrane isolation processes. In our trials CaCl2 -added, pH-adjusted and heat-treated wheys were found to have MF (microfiltration) permeate fluxes about 30% higher than in untreated MF whey. The total solids and protein content of the MF permeates decreased compared to the original wheys. UF (ultrafiltration) trials were conducted using MF whey to compare it with centrifugally separated whey. The MF whey consistently maintained an UF flux about 1.5 to 2.5 times higher than that of the separated whey. Differently treated MF whey UF permeate fluxes also showed a difference. With CaCl2 addition, pH adjustment and heat treatment, the UF permeate fluxes were about 20 to 40% higher than when only MF was used. The total solids content decreased in each trial. The protein content of the UF concentrate also decreased compared to the MF permeate. The (β-lg (β-lactoglobulin) and α-la (α-lactalbumin) content was almost the same in UF concentrates as in MF permeates.
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Wong, T. Y., C. A. Murdock, S. P. Concannon, and T. D. Lockey. "Simultaneous uptake of galactose and glucose by Azotobacter vinelandii." Biochemistry and Cell Biology 69, no. 10-11 (October 1, 1991): 711–14. http://dx.doi.org/10.1139/o91-106.

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Azotobacter vinelandii growing on galactosides induced two distinct permeases for glucose and galactose. The apparent Vmax and Km of the galactose permease were 16 nmol galactose/min per 1010 cells and 0.5 mM, respectively. The apparent Vmax and Km of the glucose permease were 7.8 nmol glucose/min per 1010 cells and 0.04 mM, respectively. Excess glucose had no effect on the galactose uptake. However, excess galactose inhibited glucose transport. The galactosides-induced glucose permease also exhibited different uptake kinetics from that induced by glucose.Key words: Azotobacter, carbohydrate metabolism, melibiose, transport, galactose.
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Schreve, James L., Jennifer K. Sin, and Jinnie M. Garrett. "The Saccharomyces cerevisiae YCC5(YCL025c) Gene Encodes an Amino Acid Permease, Agp1, Which Transports Asparagine and Glutamine." Journal of Bacteriology 180, no. 9 (May 1, 1998): 2556–59. http://dx.doi.org/10.1128/jb.180.9.2556-2559.1998.

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ABSTRACT The yeast YCC5 gene encodes a putative amino acid permease and is homologous to GNP1 (encoding a high-affinity glutamine permease). Using strains with disruptions in the genes for multiple permeases, we demonstrated that Ycc5 (which we have renamed Agp1) is involved in the transport of asparagine and glutamine, performed a kinetic analysis of this activity, and showed that AGP1 expression is subject to nitrogen repression.
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Panopoulos, George, Golfo Moatsou, Chrysanthi Psychogyiopoulou, and Ekaterini Moschopoulou. "Microfiltration of Ovine and Bovine Milk: Effect on Microbial Counts and Biochemical Characteristics." Foods 9, no. 3 (March 4, 2020): 284. http://dx.doi.org/10.3390/foods9030284.

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The aim of this research work was to assess the effect of the microfiltration (ceramic membranes 1.4 μm, 50 °C) of partially defatted ovine milk (fat 0.4%) and bovine milk (fat 0.3%) characteristics. Feed milks, permeates and retentates were analyzed for microbial counts, gross composition, protein fractions, the indigenous enzymes cathepsin D and alkaline phosphatase and the behavior during renneting. It was showed that the microbial quality of both ovine and bovine permeate was improved by reduction of the total mesophilic microflora about 4 Log and 2 Log, respectively. The protein contents and the total solids contents of both permeates were significantly (p < 0.05) reduced. A further analysis of protein fractions by Reversed Phase -High Performance Liquid Chromatography (RP-HPLC) revealed lower αs1- and β-casein and higher κ-casein contents in permeates. The activity of alkaline phosphatase followed the allocation of the fat content, while activity of cathepsin D in permeates was not influenced, although somatic cells counts were removed. Regarding cheesemaking properties, the firmness of ovine curd made from the feed milk did not differ significantly from that made from the permeate. The obtained results suggested that microfiltration could be used for pre-treating of ovine milk prior to cheesemaking.
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Dissertations / Theses on the topic "Permeace"

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Brtníková, Jana. "Využití plynové chromatografie ke studiu permeace toxických látek bariérovými materiály." Doctoral thesis, Vysoké učení technické v Brně. Fakulta chemická, 2009. http://www.nusl.cz/ntk/nusl-233295.

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Transport phenomenon of gas and vapors through polymer barrier materials as well as the factors affecting permeability of gaseous and liquid toxic compounds were investigated and results are presented in this thesis. Permeation characteristics investigation methods were elaborated and verified with focusing on utilization of gas chromatographic method and its instrumental modifications.
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Dragana, Ilić-Udovičić. "Optimizacija tehnološkog procesa proizvodnje napitaka od enzimski hidrolizovanog permeata mleka." Phd thesis, Univerzitet u Novom Sadu, Tehnološki fakultet Novi Sad, 2015. http://www.cris.uns.ac.rs/record.jsf?recordId=95728&source=NDLTD&language=en.

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Valorizacija permeata kao sporednog proizvoda industrije mleka je od izuzetnog ekološkog, ekonomskog i tehnološkog značaja.Cilj doktorske disertacije je razvoj tehnološkog procesa prerade permeata, kao sporednog proizvoda dobijenog nakon ultrafiltracije mleka tokom proizvodnje feta sira i svežeg („mladog“) sira. Ispitana je mogućnost enzimske hidrolize laktoze u permeatu korišćenjem enzima β-galaktozidaze izolovanog iz Kluyveromyces lactis u koncentraciji 0,1, 0,3 i 0,5 g/100g na temperaturama 20º, 30º i 40 ºC. Praćene su promene sadržaja laktoze, D–galaktoze i D–glukoze u vremenskim intervalima tokom 60 minuta. Posebna faza istraživanja obuhvatila je matematičko modelovanje i kinetiku procesa hidrolize laktoze u permeatu pod dejstvom β –galaktozidaze i primenu hidrolizovanog permeata u proizvodnji mlečnih napitaka po odabranoj formulaciji. Predložen je tehnološki proces proizvodnje napitka na bazi hidrolizovanog permeata sa dodatkom voćnih baza. Utvrđeni su parametri kvaliteta i trajnosti napitaka tokom 60 dana skladištenja.Na temperaturi 40°C dodatkom enzima β -galaktozidaze u koncentraciji 0,1g/100g za 60 minuta postiže se 100% stepen hidrolize prisutne laktoze u permeatu. Sa većom koncentracijom enzima, 0,3 g/100g odnosno 0,5g/100g, na istoj temperaturi, isti efekat se postiže za 20 minuta.Ispitivanjem kinetike hidrolize laktoze potvrđena je kinetika prvog reda. Generalno posmatrano visoki koeficijenti determinacije pokazuju dobro poklapanje eksperimentalnih rezultata i matematičkog modela reakcije prvog reda. Vrednosti se kreću od 0,974 (temperatura 20°C) do preko 0,990 (na temperaturama 30°C i 40°C) pri koncentraciji enzima 0,1g/100g.Proizvedeni napici od hidrolizovanog permeata su delaktozirani i ne sadrže mlečnu mast. Od ukupnih šećera u svim napicima više od 50% čini glukoza: 50,16% - napitak šumsko voće, 50,42% - napitak pomorandža/šargarepa, 54,65% - napitak multivitamin, odnosno 55,13% - napitak crveno voće.Najveći sadržaj vitamina C nakon proizvodnje imao je napitak sa dodatkom voćne baze multivitamin 0,3972 mg/100g, zatim šumsko voće 0,2887 mg/100g i pomo-randža/šargarepa 0,1999 mg/100g.Najveću vrednost antioksidativne aktivnosti nakon proizvodnje pokazali su uzorci napitka sa multivitaminom i šumskim voćem. Tokom perioda skladištenja dolazi do smanjenja DPPH vrednosti. Najmanji pad je u napitku sa pomorandžom / šargarepom (smanjenje za 17%), a najveći u napitku sa šumskim voćem (za 39%). Analizirani uzorci sadrže ukupnih polifenola u intervalu od 47,84 do 120,38 mg GAE/l u zavisnosti od vrste napitka, odnosno dodatih voćnih baza.Generalno može se zaključiti da se prime-njenim tehnološkim procesom dobijaju napici stabilnog fizičko-hemijskog sastava tokom 60 dana skladištenja, visoke nutritivne i niske energetske vrednosti.
Valuation of the permeate as a by-product of the dairy industry is of great ecological, economic and technological importance.The aim of the PhD thesis is the development of the technological process of refining permeate, as a by-product obtained after ultrafiltration of milk during the production of feta cheese and fresh cheese. The possibility of enzymatic hydrolysis of the lactose in the permeate using the enzyme β-galactosidase isolated from Kluyveromyces lactis in a concentration of 0.1, 0.3 and 0.5 g / 100 g at a temperature of 20°, 30° and 40° C was examined. Changes in the content of lactose, D-galactose and D-glucose at intervals of 60 minutes were monitored. A special stage of the research included mathematical modeling and kinetics of lactose hydrolysis in the permeate under the influence of β-galactosidase and application of hydrolyzed permeate in the production of dairy products under the selected formulation. A technological process of producing a beverage on the basis of hydrolyzed permeate with the addition of fruit bases was suggested. Quality and durability parameters were determined for drinks during the 60 days of storage.Addition of the enzyme β-galactosidase at a concentration of 0.1 g / 100 g for 60 minutes at a temperature of 40 ° C a 100% degree of hydrolysis of lactose is achieved, present in the permeate. With a higher concentration of enzyme, 0.3 g / 100 g or 0.5 g / 100g, at the same temperature, the same effect can be achieved in 20 minutes.By examining the kinetics of lactose hydrolysis the first order kinetics was confirmed. Generally high coefficients of determination show good correspondence between the experimental results and the mathematical model of the first order reaction. Values range from 0.974 (at a temperature of 20° C) up to over 0.990 (at temperatures 30° C and 40° C) at a an enzyme concentration of 0.1g / 100g.Beverages produced from hydrolyzed permeate are lactose-free and fat-free products. More than half of the total sugar content in all beverages consists of glucose: 50.16%-forest fruit beverage, 50.42%-beverage orange/carrot, 54.65% beverage multivitamin and 55.13% - beverage red fruit.The highest vitamin C content after production was in a beverage with the addition of fruit base multivitamin (0.3972 mg/100g), followed by forest fruit (0.2887 mg/100g) and orange/carrot (0.1999 mg/100g).Beverage samples with multivitamin and forest fruits showed the highest value of antioxidant activity after production. During the storage period there is a reduction of DPPH values. The smallest decrease was in the beverage with orange/carrot (decreased 17%), and the biggest in the beverage with forest fruit (39%). The content of polyphenols in analyzed samples ranges from 47.84 to 120.38 mg GAE/L depending on the type of beverage and added fruit base.Overall it can be concluded that the applied technological process gives beverages of stable physical and chemical content during the 60 days of storage, of high nutritional value and low energy.
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Santos, Barbara Belodi dos. "Utilização do permeado de leite como adjunto na produção de cerveja de alta fermentação (ALE)." Universidade de São Paulo, 2016. http://www.teses.usp.br/teses/disponiveis/97/97132/tde-06072016-145942/.

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O Brasil ocupa o 3º lugar entre os maiores produtores mundiais de cerveja e o mercado consumidor vem aumentando progressivamente. Tendo em vista que o consumidor brasileiro está em busca de novos sabores e aromas para a cerveja, uma alternativa para a redução de custos explorando tais características reside no uso de adjuntos não convencionais que possam agregar valor à bebida, principalmente na obtenção de boas características sensoriais. Ainda, visando à sustentabilidade, estes adjuntos podem ser coprodutos do processamento de alimentos. O permeado concentrado de leite, um coproduto dos laticínios, é obtido através da ultrafiltração do leite, sendo composto por água, lactose e sais. Neste trabalho foi desenvolvido um processo para a produção de uma cerveja de alta fermentação (ale), utilizando o permeado concentrado de leite como adjunto de fabricação. Foram obtidas cervejas ale com a proporção malte/permeado de 55/45 e 90/10, utilizando para isso, permeado hidrolisado pela enzima ?-galactosidase e permeado não hidrolisado. A caracterização do permeado revelou que este possui três vezes mais lactose que o soro de queijo. A melhor condição de hidrólise enzimática da lactose presente no permeado foi obtida empregando-se 2,0 mL/L de ?-galactosidase em 90 minutos, alcançando 92,5% de hidrólise. Nas cervejas com permeado hidrolisado observou-se que a presença de galactose aumentou o tempo de fermentação para 168h e a atenuação real de fermentação dos mostos também foi maior em comparação as cervejas com permeado não hidrolisado, nos quais a lactose não foi fermentada. As cervejas 90/10 com permeado hidrolisado e não hidrolisado receberam as maiores notas na análise sensorial, tendo boa aceitação entre os provadores. Como não houve diferença estatística entre as duas, foi possível reduzir custo e tempo na produção da cerveja 90/10 em escala piloto (120L) por não ser necessário o processo de hidrólise enzimática. O permeado concentrado de leite mostrou-se um excelente adjunto na produção de cervejas ale e quando empregado em baixa concentração, produziu cervejas com boa aceitação sensorial.
Brazil ranks 3rd among the largest world producers of beer and the consumer market is increasing steadily. Considering that the Brazilian consumer is looking for new flavors and aromas to the beer, a possible solution for costs reduction exploring such characteristics is using unconventional adjuncts that can increase quality of the beverage, especially in getting good sensory characteristics. In addition, aiming at sustainability, such adjuncts can be coproducts of processing foods. The concentrated milk permeate, which is a dairy factory coproduct, is obtained by milk ultrafiltration, comprising water, lactose and salts. In this work it was development a process for the production of an ale beer using concentrated milk permeate as adjunct. Ale beers were obtained from the proportion malt/permeate 55/45 and 90/10, using both permeate hydrolyzed by ? - galactosidase enzyme and permeate not hydrolyzed. The characterization of the permeate revealed that it has three times more lactose than cheese whey. The best condition of enzymatic hydrolysis of lactose present in the permeate was obtained using 2.0 mL/L of ?-galactosidase within 90 minutes, reaching 92.5 % of hydrolysis. It was observed that the presence of galactose in beers wort with hydrolysed permeate increased fermentation time to 168 h and the real attenuation of fermentation were also higher compared with non-hydrolysed permeate beers, in which lactose is not fermented. The beers 90/10 with hydrolyzed and non-hydrolyzed permeate received the highest scores in sensory analysis, meaning a good acceptance among the tasters. Once there was no statistical difference between them, it was possible to reduce costs and time in beer 90/10 production on a pilot scale (120L) for not being necessary the enzymatic hydrolysis process. The concentrated milk permeate has proved to be an excellent adjunct in the production of ale beers. It produced ale beers with good sensory acceptance when used in low concentration.
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Fabricio, Mariana Fensterseifer. "Produção de ácidos graxos poli-insaturados pela levedura Meyerozyma Guilliermondii BI281a utilizando resíduos agro-industriais como substrato." reponame:Biblioteca Digital de Teses e Dissertações da UFRGS, 2018. http://hdl.handle.net/10183/180524.

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Leveduras oleaginosas possuem a capacidade de sintetizar grande quantidade de lipídeos em suas células, gerando produtos de alto valor agregado através de um processo sustentável. Um perfil de ácidos graxos poli-insaturados é de grande interesse por parte das industrias alimentícia e farmacêutica e têm sido alvo de diversos estudos em relação à sua produção e efeitos benéficos à saúde. O presente trabalho teve como objetivo produzir ácidos graxos poli-insaturados pela levedura Meyerozyma guilliermondii BI281 utilizando glicose, glicerol residual e permeado de soro de queijo como fontes de carbono. Avaliou-se o metabolismo da levedura em meios de cultivo com diferentes composições (“meio A” e “base YM”) e comparou-se o seu desempenho em razões C/N 100: 1 e 50:1. A levedura foi capaz de metabolizar todos os substratos testados e o meio de cultivo “A” com glicerol residual e razão C/N 50:1 mostrou-se o mais adequado, obtendo valores de 5,67 g.L-1 de biomassa e 1,04 g.L-1 de lipídeos, representando aproximadamente 18 % do peso da massa seca de biomassa. Esta condição foi escalonada para biorreator de 2 L, onde condições de aeração e controle de pH puderam ser avaliadas, apresentando quantidade semelhante de lipídeos (1,08 g.L-1) e uma maior produção de biomassa (7,05 g.L-1). Os ácidos graxos sintetizados apresentaram em sua composição ácido láurico (C12:0), ácido mistírico (C14:0), ácido palmítico (C16:0), ácido pamitoleico (C16:1), ácido esteárico (C18:0), ácido oleico (C18:1 n-9), ácido linoleico (C18:2 n-6) e ácido linolênico (C18:3 n-3).
Oleaginous yeasts are able to synthesize high amounts of lipids in their cells, producing high added-value products through a sustainable process. Food and pharmaceutical companies have great interest in polyunsaturated fatty acids depending on their profiles and many studies related to their production and health benefits have been carried out. The aim of this study was to produce polyunsaturated fatty acids by the yeast Meyerozyma guilliermondii BI281A using glucose, crude glycerol, and cheese whey permeate as carbon sources. Yeast metabolism was evaluated in different compositions of culture media (“A” and “YM”) and at different C/N ratios (100:1 and 50:1). The yeast was able to assimilate all substrates tested, and medium “A” with crude glycerol as carbon source at a C/N ratio of 50:1 had the most efficient result with biomass production of 5.67 g.L-1 and lipid production of 1.08 g.L-1, which represented 18 % of dry cell weight. This composition was scaled-up to a 2 L bioreactor, where it was possible to measure pH and aeration conditions, and showed similar lipid production (1.08 g.L-1) and higher biomass production (7.05 g.L-1). Fatty acids profile obtained was composed by lauric acid (C12:0), myristic acid (C14:0), palmitic acid (C16:0), palmitoleic acid (C16:1), stearic acid (C18:0), oleic acid(C18:1), linoleic acid (C18:2 n-6), and linolenic acid (C18:3 n-3).
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Santos, Jordana Dorca dos. "Tratamento de efluente de fecularia utilizando coagulação/floculação e separação por membranas." Universidade Estadual do Oeste do Paraná, 2016. http://tede.unioeste.br/handle/tede/3064.

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This research aimed to study the treatment of manipueira by combined process of coagulation/flocculation and membrane separation, targeting the non-potable reuse this water. For pretreatment of the effluent triage was performed using five natural coagulants (Acquapol WW, and S5T Tanfloc POP, ST, SG), a chemical (Al2SO4) and a cationic flocculant (Zetag ® 8185).Experimental designs Plackett & Burman (PB12) followed by a full factorial 2k was used in order to obtain the best experimental conditions in the process. The supernatant obtained in step of coagulation/flocculation under went a process of separation of micro-and ultrafiltration membranes varying pressures (0,6, 1 and 1,4 bar), permeate flows being analyzed, fouling and removal efficiency.The raw sewage and water resulting from treatment in the best conditions of coagulation/flocculation and filtration, under went a toxicity test using brine shrimp body. From the selected sorting the sedimentation time 15 minutes and Tanfloc POP among the natural coagulants.The best condition of operation of the coagulation/flocculation obtained through experimental planning was 1 min to 10 min, TMR TML, 180 rpm for VMR and 10 rpm of VML, pH of 8.5 and coagulant concentration of 440 mg L-1, with removals of 88,5% to turbidity and 78,9% color. The model adjusted to the data in the color parameter removal complete factorial planning using coagulant Tanfloc POP. The tests of filtration (MF and UF) presented on pressure of 1,4 bar, above 95% removal of colour and turbidity, and above 60% for nitrogen and COT, but with lower COD removal (less than 70%). The toxicityof that treated wastewater (66% and 100%) reported toxic to the test organism due to the presence of free cyanide. The permeated obtained (MF) could be used for less noble purposes among the classes (2, 3 and 4) suggested by the ABNT NBR 13,696/1997. The results obtained in this study demonstrate the potential of C/F, MF and UF, for treatment of manipueira.
Esta pesquisa teve como objetivo estudar o tratamento da manipueira por processo combinado de coagulação/floculação e separação por membranas, visando o reuso não potável desta água. Para o pré-tratamento do efluente foi realizada uma triagem utilizando cinco coagulantes naturais (Acquapol WW, S5T e Tanfloc POP, ST, SG), um químico (Al2SO4) e um floculante catiônico (Zetag 8185®). Planejamentos experimentais Plackett & Burman (PB12) seguido de um fatorial completo 2k foram utilizados a fim de obter as melhores condições experimentais no processo. O sobrenadante obtido na etapa de coagulação/floculação foi submetido a um processo de separação por membranas de micro e ultrafiltração variando-se as pressões (0,6, 1 e 1,4 bar), sendo analisados os fluxos de permeado, fouling e eficiência de remoção. O efluente bruto e a água resultante do tratamento nas melhores condições dos ensaios de coagulação/floculação e filtração, foram submetidos a um ensaio de toxicidade utilizando o organismo Artemia salina. A partir da triagem selecionou-se o tempo de sedimentação de 15 minutos e o Tanfloc POP dentre os coagulantes naturais. A melhor condição de operação da coagulação/floculação obtida através dos planejamentos experimentais foi de 1 min para TMR, 10 min de TML, 180 rpm para VMR e 10 rpm de VML, pH de 8,5 e concentração do coagulante de 440 mg L-1, com remoções de 88,5% para cor e 78,9% de turbidez. O modelo ajustou-se aos dados de remoção do parâmetro cor no planejamento fatorial completo utilizando o coagulante Tanfloc POP. Os ensaios de filtração (MF e UF) apresentaram na pressão de 1,4 bar, remoções acima de 95% de cor e turbidez, e acima de 60% para nitrogênio e TOC, porém com baixa remoção de DQO (menor que 70%). A toxicidade, do efluente mesmo tratado (66% e 100%) apresentou-se tóxico para o organismo teste devido à presença de cianeto livre. O permeado obtido (MF) poderia ser utilizado para fins menos nobres dentre as classes (2, 3 e 4) sugeridas pela ABNT NBR 13.969/1997. Os resultados obtidos neste estudo demonstram o potencial dos processos de C/F, MF e UF, para tratamento da manipueira.
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Howell, John Michael. "Whey permeate fouling of evaporators." Thesis, University of Canterbury. Chemical and Process Engineering, 1998. http://hdl.handle.net/10092/10686.

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Whey permeate fouling was studied to gain a better understanding of the processes involved and find methods of alleviation. An apparatus was built which allowed study of fouling under industrial conditions. It was found that pretreatment by heating at 80°C for two minutes and then centrifuging at 630 g reduced fouling in the apparatus by 94%. This was attributed to precipitation of calcium phosphate in the solution bulk during preheating, which reduced the level of supersaturation. Heat treatment with the same conditions but without centrifuging reduced fouling by only 39%. Precipitate which forms in the bulk of solution fouls in later heat treatment processes and separation of the precipitated mineral is needed to minimise fouling. Storage time affected fouling. In the short term (about 2 weeks), fouling slightly increased with storage time. When held for longer times (about 1 month) whey permeate did not appreciably foul. The use of additives was also found to be an effective alleviation method, reducing fouling by 66% with 0.1% addition (by dry weight) of tetrasodium pyrophosphate. This addition would increase the price of a ton of lactose by $16.32 /ton. Nanoftltration, ion dialysis and electrodialysis were also examined, but rejected as being uneconomic. By observing the effect of preheating and storage time it was proposed that calcium phosphate exists in whey in two forms. The majority of the minerals are associated with non-protein nitrogen (NPN) species, which tends to provide stability and prevent precipitation. In the other form the calcium phosphate is in solution as free ions. When the NPN species release minerals due to cleavage by enzymes or denaturation by heat, the concentration of ionic species increases past the solubility product and precipitation occurs.
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Silva, Layane Priscila de Azevedo. "Utiliza??o de membranas no p?s-tratamento de esgotos para reuso do permeado e aproveitamento do concentrado." Universidade Federal do Rio Grande do Norte, 2014. http://repositorio.ufrn.br:8080/jspui/handle/123456789/16012.

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The use of membrane filters in the post-treatment of sewage has been increasingly employed to obtain water quality, applicable to various forms of reuse. Despite the advantages presented using the permeate membranes, such as saving water and reducing water pollution, the concentrate generated in the process ends up being an inconvenience to the deployment of this technology due to lack of sustainable solutions for their management. Thus, the main objective of this research was to evaluate the use of membranes for microfiltration, ultrafiltration, nanofiltration and reverse osmosis concentrated in agriculture, using it as liquid fertilizer. The permeated membranes were also assessed in order to identify activities in which they could be reused. Five configurations were established from four types of membranes, so that each configuration represents a different system. The tests were conducted in batch mode, with triplicate for each configuration. The results indicated that permeated the microfiltration and ultrafiltration can be used in urban areas, in non-potable uses. Have the nanofiltration permeate can be reused in the industry, replacement cooling towers, and other non -potable uses required in the manufacturing unit. The permeate obtained in reverse osmosis met the intended uses for nanofiltration as well as the standards required for boiler feed, adding alkalizing being required to raise the pH to the recommended value. Concentrates generated in nanofiltration and reverse osmosis can be availed as liquid fertilizer in agriculture, but they must be diluted in the irrigation water, in order to adjust the salt concentration allowed for the least tolerant crops patterns
A utiliza??o de membranas filtrantes no p?s-tratamento de esgotos tem sido cada vez mais empregada para obten??o de ?gua com qualidade, aplic?vel a v?rias modalidades de re?so. Apesar das vantagens apresentadas com o uso do permeado de membranas, como a economia de ?gua e a redu??o da polui??o h?drica, o concentrado gerado no processo acaba sendo um inconveniente para a implanta??o dessa tecnologia, devido ? falta de solu??es sustent?veis para seu gerenciamento. Sendo assim, o principal objetivo dessa pesquisa foi avaliar o uso do concentrado de membranas de microfiltra??o, ultrafiltra??o, nanofiltra??o e osmose inversa na agricultura, utilizando-o como adubo l?quido. Os permeados das membranas tamb?m foram avaliados, a fim de identificar em que atividades os mesmos poderiam ser reutilizados. Foram estabelecidas cinco configura??es, a partir dos quatro tipos de membranas, de modo que cada configura??o representou um sistema distinto. Os ensaios foram realizados em batelada, com triplicata para cada configura??o. Os resultados indicaram que os permeados da microfiltra??o e ultrafiltra??o podem ser utilizados no meio urbano, em usos n?o pot?veis. J? o permeado da nanofiltra??o pode ser reutilizado na ind?stria, para reposi??o em torres de resfriamento, e nos demais usos n?o pot?veis requeridos na unidade fabril. O permeado obtido no processo de osmose inversa atendeu aos usos previstos para nanofiltra??o, bem como aos padr?es exigidos para alimenta??o de caldeiras, sendo necess?ria a adi??o de alcalinizante, para elevar o pH at? o valor recomendado. Os concentrados gerados na nanofiltra??o e osmose inversa podem ser aproveitados na agricultura como adubo l?quido, mas precisam ser dilu?dos na ?gua de irriga??o, a fim de adequar a concentra??o de sais aos padr?es permitidos para culturas menos tolerantes
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Neil, Teresa Kathleen. "Structural studies of oligopetide permease A." Thesis, University of York, 1992. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.306526.

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Dixon, Elizabeth Marie. "Whey Permeate, Delactosed Permeate, and Delactosed Whey as Ingredients to Lower Sodium Content of Cream Based Soups." NCSU, 2008. http://www.lib.ncsu.edu/theses/available/etd-11072008-113327/.

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The use of whey permeates as salt substitutes can help to decrease sodium and chloride intake, increase potassium, calcium and magnesium intakes and decrease hypertension risk. Five different whey permeates from 5 different manufacturers were analyzed with ICP for mineral content (Na, K, Ca, Mg, Fe, Zn). Two permeates are powder and three are liquid. Lactose and protein content were also analyzed by Lactose/D-Glucose UV kit from Roche and BCA protein assay, respectively. Chloride and phosphate were measured spectrophotometrically. Basic tastes and aromas were quantified by a trained sensory panel. Based on the highest âsalty tasteâ identified by the trained sensory panel, one liquid and one solid permeate were further investigated as sodium substitutes. The sodium content of the guideline solutions for comparing salty taste of the permeates were used to calculate the equivalent concentrations of salt and permeate for salty taste in aqueous solution. Two soup formulations were used to test the use of permeate as a salt substitute; one retorted, canned, condensed cream soup base, and one fresh cream soup base. Each formulation of soup was tested on a separate day by 75 consumer panelists who averaged between 20 and 30 years of age. Four samples were given each day 0%, 50%, 100% of the standard salt content in condensed soup, and permeate at a content calculated to be equal in salty taste to the standard salt content. The permeate soup was ranked in salty taste slightly lower than the 50% sample for the fresh soup. In the retorted soups, the permeate was ranked slightly higher than the 50% sample. However, the fresh and retorted soup formulations made from permeate actually contained 11% and 19% sodium as compared to the 100% salt recipe, respectively. The permeate soup was described as higher in salty taste than expected based on actual sodium content, but not as high as predicted from the salty taste of the permeate in aqueous solution. Potassium and magnesium levels were increased in the formulations with permeate. This research gives an optimistic view on the possibility of whey permeates and their capability of replacing sodium in cream soups and other processed foods.
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Downes, David. "Interactive models of electrical machines." Thesis, Nottingham Trent University, 2003. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.273777.

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Books on the topic "Permeace"

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Bussche, W. van den. Permeke. Antwerpen: Fonds Mercator, 1986.

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Bussche, W. van den. Permeke. Antwerpen: Mercatorfonds, 1986.

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Permeable Pavements Task Committee, ed. Permeable pavements. Reston, Virginia: American Society of Civil Engineers, 2015.

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Permeke, Constant. Constant Permeke. Lugano: Museo d'arte moderna, 1996.

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Bussche, W. van den. Permeke, 1886-1952. Jabbeke: Museum Constant Permeke, 1993.

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Morrison, S. Roy. Research on permeable barriers. 3rd ed. [Washington, D.C: U.S. Environmental Protection Agency], 1995.

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Popelier, Bert. De welgezinden van Permeke. [Antwerpen, Belgium]: Pandora, 2002.

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Bussche, Willy Van den. Retrospectieve Permeke: 20.12.1986 - 1.3.1987. Oostende: Provinciaal Museum voor Moderne Kunst, 1986.

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Sanmartí, Caterina Riba. Maria-Mercè Marçal: L'escriptura permeable. Vic: Eumo Editorial, 2014.

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New materials permeable to water vapor. Berlin: Springer, 1999.

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Book chapters on the topic "Permeace"

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Gooch, Jan W. "Permease." In Encyclopedic Dictionary of Polymers, 914. New York, NY: Springer New York, 2011. http://dx.doi.org/10.1007/978-1-4419-6247-8_14461.

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Barbieri, Giuseppe. "Permeance." In Encyclopedia of Membranes, 1–2. Berlin, Heidelberg: Springer Berlin Heidelberg, 2015. http://dx.doi.org/10.1007/978-3-642-40872-4_445-1.

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Barbieri, Giuseppe. "Permeate." In Encyclopedia of Membranes, 1. Berlin, Heidelberg: Springer Berlin Heidelberg, 2015. http://dx.doi.org/10.1007/978-3-642-40872-4_446-1.

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Gooch, Jan W. "Permeance." In Encyclopedic Dictionary of Polymers, 527. New York, NY: Springer New York, 2011. http://dx.doi.org/10.1007/978-1-4419-6247-8_8590.

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Gooch, Jan W. "Selectively Permeable." In Encyclopedic Dictionary of Polymers, 923. New York, NY: Springer New York, 2011. http://dx.doi.org/10.1007/978-1-4419-6247-8_14767.

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Han, Baoguo, Liqing Zhang, and Jinping Ou. "Permeable Concrete." In Smart and Multifunctional Concrete Toward Sustainable Infrastructures, 359–68. Singapore: Springer Singapore, 2017. http://dx.doi.org/10.1007/978-981-10-4349-9_21.

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Orosa, José A., and Armando C. Oliveira. "Permeable Coverings." In Passive Methods as a Solution for Improving Indoor Environments, 99–129. London: Springer London, 2011. http://dx.doi.org/10.1007/978-1-4471-2336-1_5.

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"Permease." In Encyclopedia of Genetics, Genomics, Proteomics and Informatics, 1468. Dordrecht: Springer Netherlands, 2008. http://dx.doi.org/10.1007/978-1-4020-6754-9_12572.

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Carpenter, Charles A. "“Permeate”." In Bernard Shaw as Artist-Fabian, 41–75. University Press of Florida, 2009. http://dx.doi.org/10.5744/florida/9780813034058.003.0004.

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"Permeance." In Encyclopedic Dictionary of Polymers, 709. New York, NY: Springer New York, 2007. http://dx.doi.org/10.1007/978-0-387-30160-0_8451.

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Conference papers on the topic "Permeace"

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Sun, Chengzhen, and Bofeng Bai. "Separation of Water Vapor From Methane by Nanoporous Graphene Membrane." In ASME 2016 5th International Conference on Micro/Nanoscale Heat and Mass Transfer. American Society of Mechanical Engineers, 2016. http://dx.doi.org/10.1115/mnhmt2016-6441.

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We study the separation process of gaseous H2O/CH4 mixtures using nanoporous graphene membranes via molecular dynamics simulations. We run the simulation in an equilibrium system 10 times with different initial atomic velocities to overcome the inefficiency brought by the low pressure of the system. The results show that the H2O molecules can permeate the graphene membrane with a linearly time-dependent crossing number. The permeance of the H2O molecules reaches to 9.5×10−4 mol/m2sPa, far exceeding that of the polymer gas separation membranes. High selectivity of H2O over CH4 is also observed. In summary, this study demonstrates that the specific NPG cloud be adopted as an efficient membrane in natural gas dehydration.
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Manzolini, G., J. W. Dijkstra, E. Macchi, and D. Jansen. "Technical Economic Evaluation of a System for Electricity Production With CO2 Capture Using a Membrane Reformer With Permeate Side Combustion." In ASME Turbo Expo 2006: Power for Land, Sea, and Air. ASMEDC, 2006. http://dx.doi.org/10.1115/gt2006-90353.

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The paper investigates the application of a novel concept, based on a membrane reactor with permeate side combustion (MRPC), to capture CO2, in a natural gas fuelled power plant. The MRPC combines the steam reforming reaction on the feed side and hydrogen separation through a dense hydrogen selective membrane, with combustion of part of the permeated hydrogen, using a mixture of steam, nitrogen and air as a sweep gas. The remaining hydrogen permeated is used in the gas turbine of the combined cycle. The unconverted fuel in the high pressure CO2 rich stream exiting from the membrane reactor is burned with oxygen to permit carbon dioxide sequestration. The thermodynamic performance and economic prospects of a power plant incorporating MRPC are investigated, with a sensitivity analysis on several parameters involved. The membrane surface area required is calculated using a membrane reactor model. The final results indicate a carbon capture ratio of 100% and a net overall efficiency close to 50%. If compared to a conventional natural gas fuelled combined cycle without CO2 capture, this technology leads to an increase in cost of electricity of about 30% and a CO2 avoidance cost of about 30 €/tCO2.
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Zhang, Shiping, and Litang Yan. "Development of an Efficient Oil Film Damper for Improving the Control of Rotor Vibration." In ASME 1990 International Gas Turbine and Aeroengine Congress and Exposition. American Society of Mechanical Engineers, 1990. http://dx.doi.org/10.1115/90-gt-257.

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An efficient oil film damper known as porous squeeze film damper (PSFD) was developed for more effective and reliable vibration control of high speed rotors based on the conventional squeeze film damper (SFD). The outer race of the PSFD is made of permeable sintered porous metal materials. The permeability allows some of the oil to permeate into and seep out the porous matix, with remarkebly improvement of the squeeze film damping properties. The characteristics of PSFD oil film stiffness and damping coefficients and permeability, also, the steady state unbalance response of a simple rigid rotor and flexible Jeffcott’s rotor supported on PSFD and SFD are investigated. A typical experiment is presented. Investigations show that the nonlinear vibration characteristis of the unpressurized SFD system such as bistable jump phenomena and “lockup” at rotor pin–pin critical speeds could be avoided and virtually disappear under much greater unbalance level with properly designed PSFD system. PSFD has the potential advantages to operate effectively under relative large unbalance conditions.
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Ahmad, Hafiz M., Atia E. Khalifa, and Mohamed A. Antar. "Water Desalination Using Direct Contact Membrane Distillation System." In ASME 2015 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2015. http://dx.doi.org/10.1115/imece2015-50171.

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Membrane distillation (MD) is a separation technique used for water desalination, which operates at low feed temperatures and pressures. Direct contact membrane distillation (DCMD) is one of the common MD configurations where both the hot saline feed stream and the cold permeate stream are in direct contact with the two membrane surfaces. An experimental study was performed to investigate the effect of operating conditions such as feed temperature, feed flow rate, permeate temperature, and permeate flow rate on the system output flux. To check the effect of membrane degradation, the MD system was run continuously for 48 hours with raw seawater as feed and the reduction in system flux with time was observed. Results showed that increasing the feed temperature, decreasing the permeate temperature, increasing the feed and permeate flow rate yield an increase in flux. The effects of feed temperature and feed flow rate are the most significant parameters. After 48 hours of system continuous operation flux was reduced by 42.4 % but the quality of permeate (as measured by its TDS) is still very high with salt rejection factor close to 100 %. For the DCMD system under consideration, the GOR values remain between 0.8 and 1.2, for the tested range of operating temperatures.
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Slavin, Thomas J., Tuan Q. Cao, and Mark H. Kliss. "Permeable Membrane Experiment." In International Conference On Environmental Systems. 400 Commonwealth Drive, Warrendale, PA, United States: SAE International, 1993. http://dx.doi.org/10.4271/932161.

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Trampenau, Thomas, Frank Göricke, and Arved J. Raudkivi. "Permeable Pile Groins." In 25th International Conference on Coastal Engineering. New York, NY: American Society of Civil Engineers, 1997. http://dx.doi.org/10.1061/9780784402429.166.

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Mule, Anisha, Ramin Dabirian, Srinivas Swaroop Kolla, Ram Mohan, and Ovadia Shoham. "In-Line Testing of Novel Filter Media for Oil-Water Mixtures." In ASME-JSME-KSME 2019 8th Joint Fluids Engineering Conference. American Society of Mechanical Engineers, 2019. http://dx.doi.org/10.1115/ajkfluids2019-5554.

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Abstract A novel non-fibrous filter media is evaluated for in-line oil-water separation. Outside-in-crossflow configuration incorporating the filter media is utilized in order to test the filter. All experiments are conducted with a hydrophilic-olephobic filter for water-continuous flow with low oil concentrations. The collected experimental data include permeate flow rate and purity as well as pressure drop. Values of permeate flow rate and pressure drop are averaged over the duration of the experiments, which is about 5 minutes, constituting the “initial average” of the permeate flow rate and the corresponding pressure drop. Totally twelve experimental runs are conducted for mixture velocities of 0.038 m/s, 0.055 m/s and 0.066 m/s, and oil concentrations of 0.6%, 0.83%, 1.1%, 7.9% and 9.1%. Permeate samples are analyzed for oil content, demonstrating a high separation efficiency of 98 ± 2%. The permeate flux across the filter cartridge ranges between 0.0739 (L/h)/cm2 to 0.216 (L/h)/cm2 owing to the low pressure drop across to filter. Oil concentration in to permeate water samples shows consistently increasing trend with an increase in inlet oil content, while maintaining high separation efficiency for all runs. The pressure drop across the membrane under flowing conditions ranges from 0.35 psid to 0.6 psid for flow rates between 0.1 L/min and 0.29 L/min, respectively. Also the data confirm that the filter membrane breakthrough pressure is 0.35 psid.
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Lakeh, Reza Baghaei, Keaton Cornell, Benny Ly, Aaron Chan, and Sepideh Jankhah. "Development and Testing of a Lab-Scale Air-Gap Membrane Distillation Unit for Water Desalination." In ASME 2018 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2018. http://dx.doi.org/10.1115/imece2018-87088.

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As the population grows, one issue that is continually being addressed is the lack of clean water resources. In order to explore viable solutions, rapid experimentation and research has been underway to alleviate the water crisis. With the addition of new emerging technology, the development, improvement, and understanding of various techniques used to treat non-potable water has expanded. One subcategory of water filtration in particular that has seen rapid growth is Membrane Distillation (MD). MD is a filtration process that utilizes thermal energy to desalinate and decontaminate water. Compared to current industry leading techniques such as reverse osmosis, MD does not require such large operating pressures, leading to less power consumption. MD is accomplished primarily by flowing contaminated feed water at elevated temperatures across semi-permeable membranes. The membranes used are made to allow water vapors to penetrate through and separate from the contaminated liquid portion. By maintaining a temperature difference across the membrane, a pressure gradient is created, which drives the vapor of feed water through the pores in the membrane. Once the vapor passes through the membrane, it condenses through various methods and is collected. Air Gap Membrane Distillation (AGMD) has shown significant ability to desalinate water effectively in small scales. The air gap between the membrane and condensation plate minimizes heat loss through conduction, making AGMD a more attractive option for upscaling. In this project a laboratory-scale test cell was developed to test AGMD using different membranes, and operational parameters. In order to test such parameters, a unique design with baffled channels to induce turbulence was designed and manufactured. Feed water and coolant temperature differences, flow rates, membrane porosity, and air gap thickness are among the parameters that has been studied in this research. Temperatures of the hot feed were varied from 40°C to 80°C while the cold feed temperature was kept at a near constant temperature of 0°C. Flow rates of feed water and coolant water range from 1 to 3 L/Min. It was observed that the permeate flux is an increasing function of feed water temperature and membrane porosity. The air gap thickness plays a major role in permeate flux and energy consumption of the system.
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Park, Danielle, Elnaz Norouzi, and Chanwoo Park. "Experimental and Numerical Study of Water Distillation Performance of Small-Scale Direct Contact Membrane Distillation System." In ASME 2017 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2017. http://dx.doi.org/10.1115/imece2017-72175.

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A small-scale Direct Contact Membrane Distillation (DCMD) system was built to investigate its water distillation performance for varying inlet temperatures and flow rates of feed and permeate streams, and salinity. A counterflow configuration between the feed and permeate streams was used to achieve an efficient heat exchange. A two-dimensional Computational Fluid Dynamics (CFD) model was developed and validated using the experimental results. The numerical results were compared with the experiments and found to be in good agreement. From this study, the most desirable conditions for distilled water production were found to be a higher feed water temperature, lower permeate temperature, higher flow rate and less salinity. The feed water temperature had a greater impact on the water production than the permeate water temperature. The numerical simulation showed that the water mass flux was maximum at the inlet of the feed stream where the feed temperature was the highest and rapidly decreased as the feed temperature decreased.
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Lee, Seung-Hyeon, In-Jun Yang, Won-Ho Kim, and Ik sang Jang. "Vibration Predicition using Relative Permeance of IPMSM." In 2020 IEEE Energy Conversion Congress and Exposition (ECCE). IEEE, 2020. http://dx.doi.org/10.1109/ecce44975.2020.9236207.

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Reports on the topic "Permeace"

1

Smiley, G. T., and H. Dettman. Analysis of ultrafiltration permeate (centrifuged produced water sample). Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1991. http://dx.doi.org/10.4095/304487.

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Russell, Renee L., Reid A. Peterson, Donald E. Rinehart, and William C. Buchmiller. PEP Support Laboratory Leaching and Permeate Stability Tests. Office of Scientific and Technical Information (OSTI), September 2009. http://dx.doi.org/10.2172/968206.

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3

Johnson, Carl H. Cell-permeable Circadian Clock Proteins. Fort Belvoir, VA: Defense Technical Information Center, June 2002. http://dx.doi.org/10.21236/ada405529.

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Russell, Renee L., Reid A. Peterson, Donald E. Rinehart, and William C. Buchmiller. PEP Support: Laboratory Scale Leaching and Permeate Stability Tests. Office of Scientific and Technical Information (OSTI), May 2010. http://dx.doi.org/10.2172/981576.

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5

Yang, Bo, Pamela Blackmore, and Yue Zhang. Charles City Permeable Streetscape Phase 1. Landscape Architecture Foundation, 2012. http://dx.doi.org/10.31353/cs0390.

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Lepage, R., and J. Lstiburek. Moisture Durability with Vapor-Permeable Insulating Sheathing. Office of Scientific and Technical Information (OSTI), September 2013. http://dx.doi.org/10.2172/1221053.

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Lepage, R., and J. Lstiburek. Moisture Durability with Vapor-Permeable Insulating Sheathing. Office of Scientific and Technical Information (OSTI), September 2013. http://dx.doi.org/10.2172/1260321.

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Bruening, Merlin. Electrically Driven Ion Separations in Permeable Membranes. Office of Scientific and Technical Information (OSTI), April 2017. http://dx.doi.org/10.2172/1352450.

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Balachandran, U., B. Ma, P. S. Maiya, J. T. Dusek, R. L. Mieville, and J. J. Picciolo. Oxygen-permeable ceramic membranes for gas separation. Office of Scientific and Technical Information (OSTI), February 1998. http://dx.doi.org/10.2172/631164.

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Strevett, Keith A., and M. S. Shaheed. Microbial Characteristics of a Reactive Permeable Barrier. Fort Belvoir, VA: Defense Technical Information Center, March 2001. http://dx.doi.org/10.21236/ada388008.

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