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Artykuły w czasopismach na temat „Milk UF permeate”

Autor: Grafiati
Data publikacji: 4 czerwca 2021
Data aktualizacji: 20 lutego 2023

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1

Paredes Valencia, Adriana, Alain Doyen, Scott Benoit, Manuele Margni, and Yves Pouliot. "Effect of Ultrafiltration of Milk Prior to Fermentation on Mass Balance and Process Efficiency in Greek-Style Yogurt Manufacture." Foods 7, no. 9 (September 4, 2018): 144. http://dx.doi.org/10.3390/foods7090144.

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Ultrafiltration (UF) can be used to concentrate yogurt to produce Greek-style yogurt (GSY) (UF-YOG), but this generates acid whey permeate, which is an environmental issue. However, when UF is applied before fermentation (UF-MILK), a nonacidified whey permeate is generated. For this study, two model GSYs (UF-YOG and UF-MILK) were produced to compare the composition, UF performance, and energy consumption of the two processes. For UF-MILK, skim milk was ultrafiltered with a 30 kDa spiral-wound UF membrane to achieve a 3× volume reduction factor (VRF). The retentate was fermented to a pH of 4.5.
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CAYLE, THEODORE, JULES H. GUTH, JOHN T. HYNES, EUGENE P. KOLEN, and MAXINE L. STERN. "Penicillin Distribution During Cheese Manufacture and Membrane Treatment of Whey." Journal of Food Protection 49, no. 10 (October 1, 1986): 796–98. http://dx.doi.org/10.4315/0362-028x-49.10.796.

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Milk containing 0.005 U of benzyl 14C-penicillin G was used to make Cheddar cheese, and the whey was subsequently treated with ultrafiltration (UF) and reverse osmosis (RO). The distribution of labelled penicillin was monitored throughout milk and whey processing. The antibiotic concentrated in the moisture phases. Eight-six percent was recovered from the whey fraction, and approximately 12% from the cheese. Similar distribution patterns were detected for the whey UF permeate and retentate; 84% of the penicillin was in the permeate, and 19% remained in the retentate. The balance of penicillin
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McSweeney, David J., Valentyn Maidannyk, Sharon Montgomery, James A. O’Mahony, and Noel A. McCarthy. "The Influence of Composition and Manufacturing Approach on the Physical and Rehydration Properties of Milk Protein Concentrate Powders." Foods 9, no. 2 (February 22, 2020): 236. http://dx.doi.org/10.3390/foods9020236.

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This study investigated the physical and rehydration properties of milk protein concentrate (MPC) powders with five different protein contents (i.e., 38.9, 53.7, 63.6, 74.1, and 84.7%, w/w) prepared by recombining the ultrafiltration (UF) retentate and UF permeate of skim milk. Powder density and flowability increased, while the powder particle size decreased with decreasing powder protein content. The amount of non-wetting MPC powder decreased with decreasing protein content, demonstrating greater wettability for lower protein powders. At protein contents >65% (w/w), the dispersibility and
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Puri, Ritika, Upendra Singh, and James A. O’Mahony. "Influence of Processing Temperature on Membrane Performance and Characteristics of Process Streams Generated during Ultrafiltration of Skim Milk." Foods 9, no. 11 (November 23, 2020): 1721. http://dx.doi.org/10.3390/foods9111721.

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The effects of processing temperature on filtration performance and characteristics of retentates and permeates produced during ultrafiltration (UF) of skim milk at 5, 20, and 50 °C were investigated. The results indicate that despite higher flux at 50 °C, UF under these conditions resulted in greater fouling and rapid flux decline in comparison with 5 and 20 °C. The average casein micelle diameter was higher in retentate produced at 5 and 20 °C. The retentate analysed at 5 °C displayed higher viscosity and shear thinning behaviour as compared to retentate analysed at 20 and 50 °C. Greater per
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5

I., El-Batawy, Samar Mahdy, and M. Abo El-Naga. "Utilization of Cheese Whey and UF Milk Permeate in Manufacture of Egyptian Baladi Bread." Alexandria Journal of Food Science and Technology 15, no. 1 (June 1, 2018): 9–22. http://dx.doi.org/10.21608/ajfs.2018.16345.

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Fayed, Atef, Mohamed Abo El-Naga, Mohamed Khallaf, and Marwa Eid. "VALUE ADDITION TO FROZEN DESSERTS THROUGH INCORPORATION OF PUMPKIN SOLIDS AND UF MILK PERMEATE." Arab Universities Journal of Agricultural Sciences 28, no. 3 (September 30, 2020): 857–70. http://dx.doi.org/10.21608/ajs.2020.153600.

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HAGGERTY, PATRICIA, and NORMAN N. POTTER. "Growth and Death of Selected Microorganisms in Ultrafiltered Milk." Journal of Food Protection 49, no. 3 (March 1, 1986): 233–35. http://dx.doi.org/10.4315/0362-028x-49.3.233.

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Studies were made to compare the growth and death of Staphylococcus aureus, Streptococcus faecalis and Escherichia coli in skim milk concentrated by ultrafiltration to that in unconcentrated skim milk. Skim milk was volume concentrated to 2× in laboratory-scale stirred UF cells. Behavior of the organisms was analyzed in four inoculated milk samples: 2× retentate, 1× water-diluted retentate, milk equivalent (retentate plus permeate) and unconcentrated skim milk. Growth of each organism and of total aerobes did not vary in the four milk samples at either 7 or 13°C. For S. faecalis and E. coli, D
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8

KORNACKI, JEFFREY L., and ELMER H. MARTH. "Thermal Inactivation of Staphylococcus aureus in Retentates from Ultrafiltered Milk." Journal of Food Protection 52, no. 9 (September 1, 1989): 631–37. http://dx.doi.org/10.4315/0362-028x-52.9.631.

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Cells of Staphylococcus aureus strains 196E, 481, and 425 were thermally stressed at 56°C for 10 min in milk and enumerated on Plate Count Agar (PCA), Mannitol Salt Agar (MSA), and PCA with an overlay of MSA. PCA recovered more S. aureus 196E and 481 than did PCA/MSA, which recovered more than MSA. PCA/MSA recovered slightly more S. aureus 425 than did PCA, which recovered more than MSA. At 58°C, in order of decreasing heat resistance, the four strains of S. aureus originally isolated from food were 425 > 100 and 481 > 196E. Their D-values were 26,14,13, and 3.0 min, respectively
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9

Salunke, Prafulla, Chenchaiah Marella, and Lloyd E. Metzger. "Microfiltration and Ultrafiltration Process to Produce Micellar Casein and Milk Protein Concentrates with 80% Crude Protein Content: Partitioning of Various Protein Fractions and Constituents." Dairy 2, no. 3 (July 19, 2021): 367–84. http://dx.doi.org/10.3390/dairy2030029.

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The objective of the study reported in this research paper was to produce micellar casein concentrate (MCC) and milk protein concentrate (MPC) with 80% crude protein relative to total solids (TS) using MF and UF processes respectively. Additionally, capillary gel electrophoresis (CGE) was used to study the protein fractions in retentate and permeate. For MCC production, 227 L of pasteurized SM was subjected to MF using 0.5-micron spiral wound polyvinylidene fluoride membrane. During the process, diafiltration (DF) water was added at six intervals, totaling 100% of the feed volume. For MPC prod
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10

Özcan, Merve, Ece Büyükgümüş, and Selda Bulca. "Membran Seperasyon Tekniklerinin Süt Teknolojisinde Kullanımı ve Süt Ürünlerindeki Etkileri." Turkish Journal of Agriculture - Food Science and Technology 10, no. 11 (November 29, 2022): 2115–24. http://dx.doi.org/10.24925/turjaf.v10i11.2115-2124.5188.

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Membrane separation techniques are used to separate certain components (protein, fat, water, etc.) in liquid products such as milk and to obtain these components in pure form, and also to remove microorganisms in these liquid products. In addition, these techniques are used to concentrate milk in the dairy industry. In membrane separation, components pass through pores of a certain size and are separated according to molecular weights. The basic principle in separation techniques is based on the fact that the liquid is passed through the pores of the membrane under certain pressure, the desire
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11

Bick, A., J. G. P. Tuttle, S. Shandalov, and G. Oron. "Immersed Membrane BioReactor (IMBR) for treatment of combined domestic and dairy wastewater in an isolated farm." Water Science and Technology 51, no. 10 (May 1, 2005): 327–34. http://dx.doi.org/10.2166/wst.2005.0382.

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In many regions dairy farms and milk processing industries discharge large quantities of their wastes to the surroundings posing serious environmental risks. This problem is mostly faced in small dairy farms and isolated communities lacking both central collection and conventional wastewater treatment systems. Dairy wastewater is characterized by high concentrations of organic matter, solids, nutrients, as well as fractions of dissolved inorganic pollutants, exceeding those levels considered typical for high strength domestic wastewaters. With the purpose of treating the combined dairy and dom
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12

Kaombe, Divina D., Yanhong Du, and Michael J. Lewis. "Mineral partitioning in milk and milk permeates at high temperature." Journal of Dairy Research 79, no. 1 (September 13, 2011): 1–6. http://dx.doi.org/10.1017/s0022029911000616.

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The soluble phase of milk was separated at 20 and 80°C using ultrafiltration. The resulting permeates were then subjected to further ultrafiltration and dialysis at close to these two temperatures. It was found that pH, Ca2+ and soluble Ca decreased as the separation temperature increased both in original UF permeates and in dialysates obtained from these permeates, but P decreased only slightly. The major reason for these changes was due to the precipitation of calcium phosphate/citrate complexes onto the casein micelle with concomitant release of H+. The pH of both permeates and dialysates f
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13

Yalcin, F., I. Koyuncu, I. Oztürk, and D. Topacik. "Pilot Scale UF and RO Studies on Water Reuse in Corrugated Board Industry." Water Science and Technology 40, no. 4-5 (August 1, 1999): 303–10. http://dx.doi.org/10.2166/wst.1999.0604.

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The coloured effluents from pulp and paper mill industry are treated anaerobically and/or aerobically by a two stage membrane system with high efficiency. Three different types of membranes (UF and RO (BW and SW)) were used in the experiments. Surface area of each membrane was 2 m2. The combination of ultrafiltration (UF) and reverse osmosis (RO) treatment achieve a very high removals of COD (98-99%), colour and conductivity. At the end of a single pass with RO using seawater (SW) membrane, the initial COD, colour and conductivity values were reduced to 10–20 mg/l, 0–100 Pt-Co units and 200–30
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14

Quezada, Rafael, Claudio Mudado Silva, Ana Augusta Passos Rezende, Leif Nilsson, and Mauro Manfredi. "Membrane treatment of the bleaching plant (EPO) filtrate of a kraft pulp mill." Water Science and Technology 70, no. 5 (July 2, 2014): 843–50. http://dx.doi.org/10.2166/wst.2014.304.

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The objective of this study was to evaluate the use of membrane technology to treat oxygen and peroxide-reinforced extraction stage (EPO) filtrate from a kraft pulp mill bleach plant. Three different types of tubular membranes were tested in a pilot plant: (i) tight ultrafiltration (UF); (ii) open UF followed by nanofiltration (UF + NF); and (iii) nanofiltration (NF). According to the separation performance, considering the chemical oxygen demand (COD) and colour removal, permeate flux, operational simplicity and cost, the results indicated that the best option for treatment of (EPO) filtrates
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15

Sierka, R. A., S. P. Cooper, and P. S. Pagoria. "Ultrafiltration and reverse osmosis treatment of an acid stage wastewater." Water Science and Technology 35, no. 2-3 (February 1, 1997): 155–61. http://dx.doi.org/10.2166/wst.1997.0507.

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The Weyerhaeuser Grande Prairie pulp mill produces 300,000 tons per year of bleached kraft for the tissue and specialty grade paper markets. Alberta Environmental Protection has given the mill stringent limits for Color (90 kilograms/admt) BOD (3 kg/admt), TSS (5 kg/admt), and AOX (1.5 kg/admt). Several technologies and combinations are being studied to ensure that the mill meets future requirements to minimize environmental impact including: oxygen delignification, ozone treatment, chemical coagulation, and membrane separation. The specific research objectives were to: (1) employ ultrafiltrat
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16

Conidi, Egea-Corbacho, and Cassano. "A Combination of Aqueous Extraction and Polymeric Membranes as a Sustainable Process for the Recovery of Polyphenols from Olive Mill Solid Wastes." Polymers 11, no. 11 (November 12, 2019): 1868. http://dx.doi.org/10.3390/polym11111868.

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Polyamide commercial membranes in flat-sheet configuration and with molecular weight cut-off (MWCO) in the range of ultrafiltration (UF) to nanofiltration (NF) were tested for the recovery of phenolic compounds from clarified olive mill solid waste (OMSW) aqueous extracts. The performance of selected membranes was evaluated in terms of productivity (permeate flux) and selectivity towards biologically active compounds (such as phenolic compounds, flavanols, and hydroxycinnamic acids derivatives) and total antioxidant activity (TAA) as a function of transmembrane pressure (TMP). NF membranes pro
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17

Condezo Castro, Tatiana Aurora, Claudio Mudadu Silva, Jorge Luiz Colodette, and Ann H. Mounteer. "Biological treatment and ultrafiltration of woodchip pre-hydrolysis liquor from dissolving pulp mills." Nordic Pulp & Paper Research Journal 33, no. 2 (July 26, 2018): 358–64. http://dx.doi.org/10.1515/npprj-2018-3022.

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Abstract Dissolving pulps could be considered as the future biorefineries, which normally generate liquor during the wood chip pre-hydrolysis (PHL). PHL has high chemical oxygen demand (COD) and biochemical oxygen demand (BOD). Mills do not have efficient means for disposal of PHL, being in general burned in the recovery boiler with a high cost due to its low consistency. The objectives of this work were to evaluate i) the biotreatability of PHL and the effects it would have on a kraft mill effluent biological treatment plant and ii) the use of ultrafiltration (UF) membrane to treat the PHL pr
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18

Dagar, Sumit, Santosh Kumar Singh, and Manoj Kumar Gupta. "Integration of Pre-Treatment with UF/RO Membrane Process for Waste Water Recovery and Reuse in Agro-Based Pulp and Paper Industry." Membranes 13, no. 2 (February 6, 2023): 199. http://dx.doi.org/10.3390/membranes13020199.

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This recent study aims to evaluate the efficacy of membrane filtration on recovery of water resource from agro-waste such as bagasse, crop-based pulp and paper mill waste. A mini pilot scale membrane system having a combination of pre-treatment filter unit (pre-filter, sediment filter and pre-carbon filter), ultra-filtration and reverse osmosis with spiral wound configuration were employed to evaluate the water reuse efficacy of effluent coming from the secondary clarifier of the conventional treatment plant of the mill. The operational conditions were optimized using Taguchi method at pH 8, t
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19

Ribeiro, B., I. Torrado, S. Di Berardino, S. M. Paixão, M. J. Rusan, A. Bani Amer, S. Zuraiqi, and A. Eusébio. "Jet-loop reactor with cross-flow ultrafiltration membrane system for treatment of olive mill wastewater." Water Practice and Technology 13, no. 2 (June 1, 2018): 247–56. http://dx.doi.org/10.2166/wpt.2018.004.

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Abstract Olive oil extraction is one of the ancient agricultural industries all over the Mediterranean area and even today it is of fundamental economic importance for many industries found over the whole Mediterranean. However, this industry generates large amounts of olive mill wastewater (OMW) and due to its physicochemical characteristics it causes severe environmental concerns and management problems in the Mediterranean area, which is facing water scarcity. Technologies to reuse this wastewater will have a high impact at the economic and environmental level. The work presented aims to im
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20

Ahmad, Mohd Azwan, Bidattul Syirat Zainal, Nashrah Hani Jamadon, Thomas Choong Shean Yaw, and Luqman Chuah Abdullah. "Filtration analysis and fouling mechanisms of PVDF membrane for POME treatment." Journal of Water Reuse and Desalination 10, no. 3 (June 29, 2020): 187–99. http://dx.doi.org/10.2166/wrd.2020.101.

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Abstract Palm oil mill effluent (POME) is a hazardous wastewater which contains high organic constituents and salt concentrations. The ultrafiltration (UF) process is a promising treatment design used for secondary treatment such as POME. However, membrane fouling is the major problem which limits the performance of the UF. This paper describes a detailed investigation of polyvinylidiene fluoride (PVDF) membrane for the treatment of POME. The fouling behavior was analyzed by water flux, fouling mechanism, scanning electron microscopy (SEM), particle size distribution (PSD) and Energy Dispersiv
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21

Zaidi, A., H. Buisson, S. Sourirajan, and H. Wood. "Ultra- and Nano-Filtration in Advanced Effluent Treatment Schemes for Pollution Control in the Pulp and Paper Industry." Water Science and Technology 25, no. 10 (May 1, 1992): 263–76. http://dx.doi.org/10.2166/wst.1992.0254.

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The kraft pulp and paper industry is currently faced with the challenge of substantially reducing the discharge of conventional and toxic pollutants to the receiving environment without compromising its competitiveness. Ultrafiltration (UF) and nanofiltration (NF) are among the various unit processes that are being investigated by researchers interested in developing alternative schemes for meeting this challenge. The objectives of the work presented here were: (i) to review the potential uses for UF and NF in the kraft pulp and paper industry and (ii) to evaluate the performance of eleven UF
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22

Mänttäri, M., M. Kallioinen, A. Pihlajamäki, and M. Nyström. "Industrial membrane processes in the treatment of process waters and liquors." Water Science and Technology 62, no. 7 (October 1, 2010): 1653–60. http://dx.doi.org/10.2166/wst.2010.940.

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A review on pulp and paper industrial membrane processes using a variety of modules and processes is presented. Membranes are mostly used today to purify process waters and to recover coating colours. Ultrafiltration using tubular membrane modules or cross-rotational (CR) filtration has been widely applied for the purification of process waters. The reuse of UF membrane permeate has decreased the fresh water consumption to lower than 6 m3/t of paper in some paper machines. Some industrial membrane processes also recover valuable products from different streams (e.g lignosulphonates). Membranes
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23

Wang, Jin, Qaisar Mahmood, Jiang-Ping Qiu, Yin-Sheng Li, Yoon-Seong Chang, Li-Na Chi, and Xu-Dong Li. "Zero Discharge Performance of an Industrial Pilot-Scale Plant Treating Palm Oil Mill Effluent." BioMed Research International 2015 (2015): 1–9. http://dx.doi.org/10.1155/2015/617861.

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Palm oil is one of the most important agroindustries in Malaysia. Huge quantities of palm oil mill effluent (POME) pose a great threat to aqueous environment due to its very high COD. To make full use of discharged wastes, the integrated “zero discharge” pilot-scale industrial plant comprising “pretreatment-anaerobic and aerobic process-membrane separation” was continuously operated for 1 year. After pretreatment in the oil separator tank, 55.6% of waste oil in raw POME could be recovered and sold and anaerobically digested through 2 AnaEG reactors followed by a dissolved air flotation (DAF);
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Kołtuniewicz, A. "The new concept of flux enhancement during cell separation with MF/UF processes." Water Supply 1, no. 5-6 (June 1, 2001): 381–86. http://dx.doi.org/10.2166/ws.2001.0137.

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The microfiltration and ultrafiltration processes are considered as matured membrane processes that are well established in industrial practice. Nevertheless, the main obstacles of their further development in the new competitive implementations are the economical problems. The key economic factors are permeate flux and energy consumption. However, although the cross-flow systems enable us to attain higher flux, it is usually very expensive. The high energy is consumed to maintain circulation velocity of the retentate that is sufficient for sweeping out the retained component from the membrane
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Abo El-Naga, Mohamed, Atef Fayed, Mohamed Khallaf, and Marwa Eid. "VALUE ADDITION TO FROZEN DESSERTS THROUGH INCORPORATION OF PUMPKIN SOLIDS AND UF MILK PERMEATE." Arab Universities Journal of Agricultural Sciences, August 20, 2020, 0. http://dx.doi.org/10.21608/ajs.2020.29556.1202.

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Ng, W. Q., S. O. Lai, K. C. Chong, S. S. Lee, C. H. Koo, and W. C. Chong. "Reduction of Total Suspended Solids, Turbidity and Colour of Palm Oil Mill Effluent using Hybrid Coagulation-Fltrafiltration Process." Journal of Applied Membrane Science & Technology 23, no. 1 (December 5, 2018). http://dx.doi.org/10.11113/amst.v23n1.144.

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High consumption and production of palm oil have led to the massive generation of palm oil mill effluent (POME). This study was intended to reduce the total suspended solids (TSS), turbidity and colour using hybrid coagulation-ultrafiltration process. POME was pre-treated with coagulation process using polyaluminium chloride (PAC) and optimization of operating condition for coagulation process was performed. The coagulation results revealed that optimum pH, dosage of coagulant and rapid mixing speed were pH 4, 600 mg/L and 200 rpm, respectively. It achieved the highest percent reduction of TSS
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Innocenzi, Valentina, Giuseppe Mazziotti di Celso, and Marina Prisciandaro. "Techno-economic analysis of olive wastewater treatment with a closed water approach by integrated membrane processes and advanced oxidation processes." Journal of Water Reuse and Desalination, December 15, 2020. http://dx.doi.org/10.2166/wrd.2020.066.

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Abstract In this paper, a reliable treatment process for olive mill wastewaters (OMWW) is proposed. In order to develop a more sustainable process with polyphenols recovery and water reuse, two treatment schemes have been simulated by using a process simulator (SuperPro Designer®), depending on wastewater characteristics; the first applied for ‘biological’ effluents by using membrane technology (microfiltration MF, ultrafiltration UF, nanofiltration NF and reverse osmosis RO), the second for wastewaters containing pesticides, in which RO is replaced with an advanced oxidation process for pesti
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