Pharmaceutical Review

Total Page:16

File Type:pdf, Size:1020Kb

Pharmaceutical Review Pharmaceutical Review 3 Review Industrial application of impurity flocculation to streamline antibody purification processes Pharm. Bioprocess. Flocculation technologies offer significant benefits to industrial mammalian cell Michael Felo1, Yun Kenneth culture processes, including increased clarification efficiency, impurity removal and Kang*,2, James Hamzik1, Paul process simplification. In this paper, the application and performance of flocculation Balderes2 & Dale L Ludwig2 1 technologies employed in the harvest process of monoclonal antibody Chinese hamster Process Solutions, EMD Millipore, 290 Concord Road, Billerica, MA 01821, ovary cell culture are reviewed. Attention has been placed on technologies enhancing USA the removal of cells, cellular debris and reduction in impurities while maintaining the 2Bioprocess Sciences, Eli Lilly & Company, antibody in the product stream. Many flocculants are systematically evaluated with 450 East 29th Street, New York, respect to their mechanism of action, impact on downstream processing and product NY 10016, USA quality, and potential disadvantages. Practical considerations and future directions *Author for correspondence: Tel.: +1 646 638 5109 for application of flocculation in antibody manufacturing are discussed. Fax: +1 212 213 4785 [email protected] Flocculation is a process that has been time of harvest have dramatically increased, widely implemented in the chemical and though typically with corresponding eleva- food industries, as well as in waste water tions in cell density, cellular debris and treatment. To the contrary, it has only been related cellular impurities [5,6]. As a result, relatively recently that flocculation-based the challenges of separating cells and pretreatment of bacterial fermentation and debris now more closely parallel those of mammalian cell culture has been explored microbial fermentation processes. It is and, in several cases, implemented in order therefore not surprising that the evalua- to circumvent both harvest and purifica- tion of flocculation to enhance the perfor- tion challenges experienced in therapeutic mance of this step has become an area of protein production [1–3] . Flocculation has intense investigation. Specifically, floccu- been slow to gain acceptance in the manu- lants such as simple acids, divalent cations, facture of monoclonal antibodies (mAbs), polycationic polymers, caprylic acid and 2 where mammalian cell culture processes stimulus-responsive polymers have been are typically utilized. Until recently, com- evaluated for their ability to enhance cell mercial processes employing cell lines such culture clarification and reduce the levels of as CHO, NS0 and SP2/0 have only rarely DNA, host cell proteins (HCP) and viruses. 2015 reached cell densities where removal of sol- In this paper, the application and perfor- ids or cell-related soluble impurities during mance of various flocculation method in the the harvest step becomes excessively burden- harvest process of CHO cell culture produc- some. Standard unit operations such as cen- tion of mAbs are reviewed. Focus has been trifugation, depth filtration and microfiltra- placed on methodsthat enhance the removal tion, in most cases, have efficiently produced of cells, cellular debris and reduce impurity harvested cell culture fluid (HCCF) suitable levels while maintaining the antibody within for d ownstream purification [4]. the product stream. Though the process Through advances in mammalian cell cul- goals are similar for each of these flocculants, ture over the past 10–15 years, particularly the mechanisms of action, impact on product those in fed-batch and product-retaining quality and potential toxicity from residual perfusion processes, the mAb titers at the flocculant vary significantly. part of 10.4155/PBP.15.2 © 2015 Future Science Ltd Pharm. Bioprocess. (2015) 3(2), 115–125 ISSN 2048-9145 115 Review Felo, Kang, Hamzik, Balderes & Ludwig Key terms lead to further product loss and increases in process Flocculation: Flocculation is the agglomeration of costs for both filters and housings [10] . particles (cells, cell debris or colloids in mammalian cell In recent years, flocculation-based pretreatment culture) caused by a bridging effect induced by the of cell cultures for mAb production has been inves- flocculant. tigated [2,3,9,12–17]. Many flocculation agents, or floc- Stimulus-responsive polymer: Stimulus-responsive culants, ranging from simple electrolytes to synthetic polymers are high-performance polymers that change polyelectrolytes (or polymers) have been evaluated physical properties according to their environment. Such (Table 1). Flocculation is the agglomeration of particles materials can be sensitive to a number of factors, such as temperature, pH, conductivity and specific stimulus (cells, cell debris or colloids in mammalian cell culture) reagents. caused by a bridging effect induced by the flocculant. Flocculation agents bind to particles largely through Although the effectiveness of flocculation has been electrostatic charge interaction, although additional frequently demonstrated, adoption remains slow in bio- interactive forces such as hydrophobic interaction or pharmaceutical industrial applications. Critical issues hydrogen bonding may be involved [3,4,18]. Flocculated including platform process fit, flocculant clearance cell cultures have higher mean particle sizes compared downstream and regulatory concerns over implementa- with their untreated counterparts (Figure 1), which has tion have hindered routine incorporation of the technol- been observed to consistently correlate with improved ogy. Still, process and industry trends toward high cell centrate quality and filterability. Notably, positively density cell cultures, continuous processes, single-use charged flocculants, such as polyamines [14], cal- technologies and lower culture production volumes are cium chloride/potassium phosphate [16], chitosan [15], anticipated to continue to drive the development and polydiallyldimethyl ammonium chloride (PDAD- implementation of these flocculation technologies into MAC) [2,9,19] and stimulus-responsive polymers [3] have industrial biopharmaceutical m anufacturing processes. been shown to be successful in inducing flocculation, resulting in improved clarification efficiency, process Advances in cell culture processes drive yield and clearance of impurities during the primary development of flocculation for mAb mAb recovery process from mammalian cell culture. production process Advances in cell culture processes have significantly Performance, limitations & application of increased mAb titers to levels as high as 30 g/l. These flocculation methods for mAb production improvements have led to more challenging conditions processes for downstream processing, including cell densities (up Acid precipitation to 108 cells per ml), packed cell volume (up to 40% v/v) Reduction of cell culture pH at the time of harvest and increased levels of soluble impurities such as HCP is a straightforward approach to induce flocculation and high molecular weight (HMW) species [2,3,7–9]. and precipitation. This is accomplished through the Advances in mAb downstream processing are required introduction of concentrated acid solutions including in order to overcome the significant challenges posed acetic, phosphoric and citric acids. The acid solution by increased cell culture productivity. typically drives the cell culture fluid from a neutral pH Increases in cell mass, cell debris and colloids from to between pH 5.5 and 4.0, most commonly between high cell density culture, place a greater burden on the pH 5.0 and 4.5. This change in pH forces a transition clarification train, specifically on continuous disk-stack across the isoelectric points of some HCP impurities, centrifugation and depth filtration, which continue to rendering them insoluble through charge neutraliza- be routinely employed in the harvest step [10] . Cul- tion. However, this impurity reduction must be bal- ture suspensions containing high solid content with a anced with the stability and quality of the product wide particle size distribution and a high percentage under tested conditions during the harvest operation. of small particles further complicate the harvest unit The shift in particle size caused by acid precipita- operation, requiring significantly higher depth filter tion/flocculation is generally less pronounced than surface area and, in some cases, exceeding the existing that induced by polymer-based flocculation methods. filtration train capacity [11] . During the centrifugation Still, particle size increase induced by lower pH has process, high solid content in the cell culture feed leads been reported, leading to improved efficiency of con- to increases in pellet ejection interval and decreases tinuous disk-stack centrifugation [11] or microfiltration in product recovery due to volume losses. Submicron harvest processes [20]. For harvest processes utilizing particles are not easily removed by centrifugation and centrifugation, the larger particulates are more easily are left to the depth filtration, and perhaps sterilizing- removed from the cell culture, and the capacity of the grade filter, for removal. Increases in filtration areacan secondary depth filtration step has been increased by 116 Pharm. Bioprocess. (2015) 3(2) future science group Table 1. Comparison of different flocculants used to streamline cell culture harvest process and enhance the removal of impurities. Flocculant Mechanism
Recommended publications
  • Sedimentation and Clarification Sedimentation Is the Next Step in Conventional Filtration Plants
    Sedimentation and Clarification Sedimentation is the next step in conventional filtration plants. (Direct filtration plants omit this step.) The purpose of sedimentation is to enhance the filtration process by removing particulates. Sedimentation is the process by which suspended particles are removed from the water by means of gravity or separation. In the sedimentation process, the water passes through a relatively quiet and still basin. In these conditions, the floc particles settle to the bottom of the basin, while “clear” water passes out of the basin over an effluent baffle or weir. Figure 7-5 illustrates a typical rectangular sedimentation basin. The solids collect on the basin bottom and are removed by a mechanical “sludge collection” device. As shown in Figure 7-6, the sludge collection device scrapes the solids (sludge) to a collection point within the basin from which it is pumped to disposal or to a sludge treatment process. Sedimentation involves one or more basins, called “clarifiers.” Clarifiers are relatively large open tanks that are either circular or rectangular in shape. In properly designed clarifiers, the velocity of the water is reduced so that gravity is the predominant force acting on the water/solids suspension. The key factor in this process is speed. The rate at which a floc particle drops out of the water has to be faster than the rate at which the water flows from the tank’s inlet or slow mix end to its outlet or filtration end. The difference in specific gravity between the water and the particles causes the particles to settle to the bottom of the basin.
    [Show full text]
  • Crystallization of Oxytetracycline from Fermentation Waste Liquor: Influence of Biopolymer Impurities
    Journal of Colloid and Interface Science 279 (2004) 100–108 www.elsevier.com/locate/jcis Crystallization of oxytetracycline from fermentation waste liquor: influence of biopolymer impurities Shi-zhong Li a,1, Xiao-yan Li a,∗, Dianzuo Wang b a Environmental Engineering Research Centre, Department of Civil Engineering, The University of Hong Kong, Hong Kong, China b Chinese Academy of Engineering, Beijing 100038, China Received 28 January 2004; accepted 17 June 2004 Available online 29 July 2004 Abstract Organic impurities in the fermentation broth of antibiotic production impose great difficulties in the crystallization and recovery of antibi- otics from the concentrated waste liquor. In the present laboratory study, the inhibitory effect of biopolymers on antibiotic crystallization was investigated using oxytetracycline (OTC) as the model antibiotic. Organic impurities separated from actual OTC fermentation waste liquor by ultrafiltration were dosed into a pure OTC solution at various concentrations. The results demonstrated that small organic molecules with an apparent molecular weight (AMW) of below 10,000 Da did not affect OTC crystallization significantly. However, large biopolymers, especially polysaccharides, in the fermentation waste caused severe retardation of crystal growth and considerable deterioration in the pu- rity of the OTC crystallized. Atomic force microscopy (AFM) revealed that OTC nuclei formed in the solution attached to the surfaces of large organic molecules, probably polysaccharides, instead of being surrounded by proteins as previously thought. It is proposed that the attachment of OTC nuclei to biopolymers would prevent OTC from rapid crystallization, resulting in a high OTC residue in the aqueous phase. In addition, the adsorption of OTC clusters onto biopolymers would destabilize the colloidal system of organic macromolecules and promote particle flocculation.
    [Show full text]
  • State-Of-The-Art Water Treatment in Czech Power Sector
    membranes Article State-of-the-Art Water Treatment in Czech Power Sector: Industry-Proven Case Studies Showing Economic and Technical Benefits of Membrane and Other Novel Technologies for Each Particular Water Cycle Jaromír Marek Department of Chemistry, Faculty of Science, Humanities and Education, Technical University of Liberec, Studentská 1402/2, 461 17 Liberec, Czech Republic; [email protected]; Tel.: +420-732-277-183 Abstract: The article first summarizes case studies on the three basic types of treated water used in power plants and heating stations. Its main focus is Czechia as the representative of Eastern European countries. Water as the working medium in the power industry presents the three most common cycles—the first is make-up water for boilers, the second is cooling water and the third is represented by a specific type of water (e.g., liquid waste mixtures, primary and secondary circuits in nuclear power plants, turbine condensate, etc.). The water treatment technologies can be summarized into four main groups—(1) filtration (coagulation) and dosing chemicals, (2) ion exchange technology, (3) membrane processes and (4) a combination of the last two. The article shows the ideal industry-proven technology for each water cycle. Case studies revealed the economic, technical and environmental advantages/disadvantages of each technology. The percentage of Citation: Marek, J. State-of-the-Art technologies operated in energetics in Eastern Europe is briefly described. Although the work is Water Treatment in Czech Power conceived as an overview of water treatment in real operation, its novelty lies in a technological model Sector: Industry-Proven Case Studies of the treatment of turbine condensate, recycling of the cooling tower blowdown plus other liquid Showing Economic and Technical waste mixtures, and the rejection of colloidal substances from the secondary circuit in nuclear power Benefits of Membrane and Other plants.
    [Show full text]
  • Coagulation-Flocculation As a Submerged Biological Filter Pre-Treatment with Landfill Leachate
    Coagulation-flocculation as a submerged biological filter pre-treatment with landfill leachate A. Gálvez Perez1,2, A. Ramos1,2,3, B. Moreno1,2,3 & M. Zamorano Toro1,2 1Department of Civil Engineering, Granada University, Spain 2MITA Research Group 3Institute of Water Research Abstract Landfill leachate may cause environmental problems if it is not properly managed and treated. An appropriate treatment process of landfill leachate often involves a combination of physical, chemical and biological methods to obtain satisfactory results. In this study, coagulation-flocculation was proposed as a pre- treatment stage of partially stabilized landfill leachate prior to submerged biological filters. Several coagulants (ferric, aluminium or organic) and flocculants (cationic, anionic or non-ionic) were assayed in jar-test experiments in order to determine optimum conditions for the removal of COD and total solids. Among the cationic flocculants, that of highest molecular weight and cationicity (CV/850) showed highest removal efficiencies (15% COD and 8% TS). Organic and aluminium coagulants showed better results than ferric coagulants. Coagulant removal efficiencies were between 9% and 17% for COD and between 10% and 15% for TS. Doses of 1 ml/l of coagulant were preferred. Some combinations of coagulant and flocculant enhanced the process. The best combinations obtained were FeCl3+A30.L, Ferriclar+A20.L, SAL8.2+A30.L and PAX-18+A30.L, which presented COD removal efficiencies between 24% and 37% with doses between 10 and 18 ml/l. Keywords: landfill leachate, coagulation-flocculation, submerged biological filter pre-treatment. Waste Management and the Environment II, V. Popov, H. Itoh, C.A. Brebbia & S.
    [Show full text]
  • Integration of Aqueous Two-Phase Extraction As Cell Harvest and Capture Operation in the Manufacturing Process of Monoclonal Antibodies
    antibodies Article Integration of Aqueous Two-Phase Extraction as Cell Harvest and Capture Operation in the Manufacturing Process of Monoclonal Antibodies Axel Schmidt 1, Michael Richter 2, Frederik Rudolph 2 and Jochen Strube 1,* 1 Institute for Separation and Process Technology, Clausthal University of Technology, Leibnizstraße 15, 38678 Clausthal-Zellerfeld, Germany; [email protected] 2 Boehringer Ingelheim Pharma GmbH & Co. KG, Bioprocess + Pharma. Dev. Biologicals, Birkendorfer Strasse 65, 88397 Biberach an der Riss, Germany; [email protected] (M.R.); [email protected] (F.R.) * Correspondence: [email protected]; Tel.: +49-5323-72-2200 Received: 30 October 2017; Accepted: 20 November 2017; Published: 1 December 2017 Abstract: Substantial improvements have been made to cell culturing processes (e.g., higher product titer) in recent years by raising cell densities and optimizing cultivation time. However, this has been accompanied by an increase in product-related impurities and therefore greater challenges in subsequent clarification and capture operations. Considering the paradigm shift towards the design of continuously operating dedicated plants at smaller scales—with or without disposable technology—for treating smaller patient populations due to new indications or personalized medicine approaches, the rising need for new, innovative strategies for both clarification and capture technology becomes evident. Aqueous two-phase extraction (ATPE) is now considered to be a feasible unit operation, e.g., for the capture of monoclonal antibodies or recombinant proteins. However, most of the published work so far investigates the applicability of ATPE in antibody-manufacturing processes at the lab-scale and for the most part, only during the capture step.
    [Show full text]
  • Pretreatment Process Optimization and Reverse Osmosis Performances of a Brackish Surface Water Demineralization Plant, Morocco
    Desalination and Water Treatment 206 (2020) 189–201 www.deswater.com December doi: 10.5004/dwt.2020.26297 Pretreatment process optimization and reverse osmosis performances of a brackish surface water demineralization plant, Morocco Hicham Boulahfaa,*, Sakina Belhamidia, Fatima Elhannounia, Mohamed Takya, Mahmoud Hafsib, Azzedine Elmidaouia aLaboratory of Separation Processes, Department of Chemistry, Faculty of Sciences, Ibn Tofail University, P.O. Box: 1246, Kenitra 14000, Morocco, emails: [email protected] (H. Boulahfa), [email protected] (S. Belhamidi), [email protected] (F. Elhannouni), [email protected] (M. Taky), [email protected] (A. Elmidaoui) bInternational Institute for Water and Sanitation, National Office of Electricity and Potable water (ONEE-IEA), Rabat, Morocco, email: [email protected] (M. Hafsi) Received 6 January 2020; Accepted 29 June 2020 abstract In surface water reverse osmosis (RO) demineralization processes, pretreatment is a key step in achieving high performances and avoiding frequent membrane fouling. The plant studied includes conventional pretreatment and RO process. The aim of this study is the optimization of the coagulation–flocculation and the assessment of its effect on pretreated water quality upstream of the RO unit. The monitored parameters were turbidity, residual aluminum, and silt density index (SDI). Moreover, this paper presents the RO membrane performance in terms of feed pressure, pressure drop, permeate flow, and permeate conductivity after nearly 1 y of operation. The results obtained illustrate that the pretreatment optimization substantially reduces the residual alu- minum concentration and the SDI after the 5 μm cartridge filters. Likewise, the RO membranes exhibited high and steady performance.
    [Show full text]
  • The Safe Use of Cationic Flocculants with Reverse Osmosis Membranes
    Desalination and Water Treatment 6 (2009) 144–151 www.deswater.com 111 # 2009 Desalination Publications. All rights reserved The safe use of cationic flocculants with reverse osmosis membranes S.P. ChestersÃ, E.G. Darton, Silvia Gallego, F.D. Vigo Genesys International Limited, Unit 4, Ion Path, Road One, Winsford Industrial Estate, Winsford, Cheshire CW7 3RG, UK Tel. þ44 1372 741881; Fax þ44 1606 557440; emails: [email protected], [email protected], [email protected] Received 15 September 2008; accepted 20 April 2009 ABSTRACT Flocculants are used in combination with coagulants to agglomerate suspended particles for removal by filtration. This technique is used extensively in all types of surface waters to reduce the silt density index (SDI) and minimise membrane fouling. Although organic cationic floccu- lants are particularly effective, their widespread use in membrane applications is limited because of perceived problems with flocculant fouling at the membrane surface causing irreparable damage. Reference material from some of the major membrane manufacturers on the use of floc- culants is given. Autopsies show that more than 50% of membrane fouling is caused by inadequate, deficient or poorly operated pre-treatment systems. The Authors suggest that if the correct chemistry is con- sidered, the addition of an effective flocculant can be simple and safe. The paper discusses the use of cationic flocculants and the fouling process that occur at the membrane surface. The paper explains the types of coagulants and flocculants used and considers cationic flocculants and the way they function. Operational results when using a soluble polyquaternary amine flocculant (Genefloc GPF) developed by Genesys International Limited is presented.
    [Show full text]
  • Flotation and Flocculation - from Fundamentals to Applications
    Flotation and Flocculation - From Fundamentals to Applications Flotation and Flocculation deals of the International Workshop industrial flotation/flocculation with cutting-edge research in on Flotation and Flocculation cells. the science and engineering of held in Hawaii, July 2002. The two of the world’s key participants included some of This book is highly focused, separation processes. the most pre-eminent experts with transcripts of discussion Flotation and flocculation in this field throughout sessions aimed at identifying underpin the key material industry and academia. The exactly how practical and supply chains for technologies organisers were Professor John workable models can be that are central to minerals, Ralston, (Chair), University of developed to reduce the fuel cells, ceramics, South Australia, Professor Jan present uncertainty inherent in telecommunications, waste Miller, University of Utah and these vital separation removal/recycling processes Professor Jorge Rubio, processes. and many other industries. Universidade Federal do Rio This book captures and Grande do Sul. Major topics include: summerises the key outcomes Over the last decade there ♦ Bridging flocculation in have been major scientific wastewater and fine particle advances in understanding the treatment processes ISBN: 0-9581414-0-1 chemistry and physics of bubble and particle surfaces, ♦ Bubble-particle modelling bubble-particle encounters/models in flotation Within Australia encounter processes in various hydrodynamic regimes, and $210.00 per book (inc
    [Show full text]
  • Precipitation and Crystallization Processes
    Precipitation and Crystallization Processes Gordon Jarvenin Los Alamos National Laboratory Introduction Precipitation and crystallization refer to unit operations that generate a solid from a supersaturated solution. The non-equilibrium supersaturated condition can be induced in a variety of ways such as removal of solvent by evaporation, addition of another solvent, changes of temperature or pressure, addition of other solutes, oxidation-reduction reactions, or even combinations of these. The distinction between precipitation and crystallization is quite often based on the speed of the process and the size of the solid particles produced. The term precipitation commonly refers to a process which results in rapid solid formation that can give small crystals that may not appear crystalline to the eye, but still may give very distinct x-ray diffraction peaks. Amorphous solids (at least as indicated by x-ray diffraction) may also be produced. The term precipitation also tends to be applied to a relatively irreversible reaction between an added reagent and other species in solution whereas crystallization products can usually be redissolved using simple means such as heating or dilution. Precipitation processes usually begin at high supersaturation where rapid nucleation and growth of solid phases occur. In both precipitation and crystallization processes the same basic steps occur: supersaturation, nucleation and growth. Nucleation does not necessarily begin immediately on reaching a supersaturated condition, except at very high supersaturation, and there may be an induction period before detection of the first crystals or solid particles. Nucleation can occur by both homogeneous and heterogeneous processes. In general, homogeneous nucleation is difficult to achieve because of the presence of heteronuclei from colloids, dust, or other foreign material in the solution.
    [Show full text]
  • 1 Downstream Processing of Biotechnology Products
    1 1 Downstream Processing of Biotechnology Products 1.1 Introduction Biological products are important for many applications including biotransforma- tions, diagnostics, research and development, and in the food, pharmaceutical, and cosmetics industries. For certain applications, biological products can be used as crude extracts with little or no purifi cation. However, biopharmaceuticals typi- cally require exceptional purity, making downstream processing a critical compo- nent of the overall process. From the regulatory viewpoint, the production process itself defi nes the biopharmaceutical product rendering proper defi nition of effec- tive and effi cient downstream processing steps crucial early in process develop- ment. Currently, proteins are the most important biopharmaceuticals. The history of their development as industrial products goes back more than half a century. Blood plasma fractionation was the fi rst full - scale biopharmaceutical industry with a current annual production in the 100 - ton scale [1, 2] . Precipitation with organic solvents has been and continues to be the principal purifi cation tool in plasma fractionation, although, recently, chromatographic separation processes have also been integrated into this industry. Anti - venom antibodies and other anti - toxins extracted from animal sources are additional examples of early biopharmaceuti- cals, also purifi ed by a combination of precipitation, fi ltration and chromatogra- phy. In contrast, current biopharmaceuticals are almost exclusively produced by recombinant DNA technology. Chromatography and membrane fi ltration serve as the main tools for purifi cation for these products. Figure 1.1 shows the 2006 market share of various biopharmaceuticals. Approxi- mately one - third are antibodies or antibody fragments [3] , nearly 20% are erythro- poietins, and 14% are insulins.
    [Show full text]
  • UC Riverside UC Riverside Electronic Theses and Dissertations
    UC Riverside UC Riverside Electronic Theses and Dissertations Title Effect of Electrostatic Interactions on Performance of Electrically Conductive Ultrafiltration Membranes for Protein Fractionation Permalink https://escholarship.org/uc/item/79q015j9 Author Yeung, Raymond Kai-yen Publication Date 2017 License https://creativecommons.org/licenses/by/4.0/ 4.0 Peer reviewed|Thesis/dissertation eScholarship.org Powered by the California Digital Library University of California UNIVERSITY OF CALIFORNIA RIVERSIDE Effect of Electrostatic Interactions on Performance of Electrically Conductive Ultrafiltration Membranes for Protein Fractionation A Thesis submitted in partial satisfaction of the requirements for the degree of Master of Science in Bioengineering by Raymond Kai-yen Yeung September 2017 Thesis Committee: Dr. Victor G. J. Rodgers, Chairperson Dr. David Jassby Dr. Boris Hyle Park Copyright by Raymond Kai-yen Yeung 2017 The Thesis of Raymond Kai-yen Yeung is approved: Committee Chairperson University of California, Riverside ACKNOWLEDGEMENTS My sincerest gratitude goes to my advisor, Dr. Victor G. J. Rodgers, whose instruction and guidance have facilitated my development as a researcher and scholar. His advice, knowledge of the research area, and commitment to his students have been crucial in fostering my growth and challenging me to reach new heights. I deeply value the research opportunity and am grateful for his continuous support. I would like to thank the members of my thesis committee, Dr. David Jassby and Dr. Hyle Park, for their support and advice they have provided in my research and graduate studies. I would also like to thank Xiaobo (Ben) Zhu for patiently assisting me in the laboratory, Dr. Alexander Dudchenko for providing valuable feedback in our discussions, and Dr.
    [Show full text]
  • Flocculation Flocculation Is the Next Step in Most Treatment Plants (In-Line Filtration Plants Being the Exception)
    Flocculation Flocculation is the next step in most treatment plants (in-line filtration plants being the exception). Flocculation is the “snowballing” of small particles into larger particles (called “floc”). It is a time-dependent process that directly affects clarification efficiency by providing multiple opportunities for particles suspended in water to collide through gentle and prolonged agitation. The process generally takes place in a basin equipped with a mixer that provides agitation. This agitation should be thorough enough to encourage inter-particle contact, but gentle enough to prevent disintegration of existing flocculated particles. Particles grow by colliding with other particles, and sticking together. Detention time is necessary for the formation of floc. The longer the detention time, the larger the floc. Temperature and pH also affect the flocculation process. Several issues regarding flocculation should be evaluated by utilities to ensure optimal operation of flocculation basins. Effect on Turbidity As with coagulation, the purpose of flocculation is not to directly reduce turbidity or suspended solids, but to prepare the solids for subsequent removal. Flocculation reduces the number of suspended solids particles as smaller particles combine to form larger ones. This process may, or may not, result in reduced turbidity in the flocculation chamber. Slow Mixing Slow mixing is a key aspect of the flocculation process. In slow mixing, the water is stirred to encourage floc particles to clump together. Stirring too fast can break large particles apart, while stirring too slowly can prevent particles from clumping enough. A wide variety of flocculation- mixing mechanisms have been used in water treatment. They include vertical shaft mechanical mixers, horizontal shaft mechanical mixers, and hydraulic mixing systems.
    [Show full text]