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Water treatment Water treatment With increased population, as it includes operations such as expanding manufacturing and separation, fl oatation, settling, growing regulatory requirements the fi ltration, neutralisation, absorption, demand for industrial wastewater ion exchange and chlorination. treatment services is projected to grow by around 5.3% a year for the At SMC we have local teams of next fi ve years. specialists who understand these needs and can help you fi nd the right Wastewater is commonly used by solutions. many industry sectors including chemical, pharmaceutical, oil and If you’re using reverse osmosis gas, food, pulp and paper, metal, devices or have micro/ultra/nano mining and power generation. And fi ltration applications or ozone with each industry using different systems check out some of our latest processes, the technologies used for cutting edge products that have treating wastewater are numerous. been designed and developed to help you. However, the operation and control part of the process is generally considered to be the main focus 3 Water treatment process Primary treatment 3 Coagulator-fl occulator Preliminary treatment 4 Primary clarifi er 1 Bar screen 2 Sand/grease trap Sludge treatment 4 12 Sludge digester 13 Sludge dewatering 3 2 13 1 12 1 Bar screen Preliminary treatment 2 Sand/grease trap 3 Coagulator-fl occulator Primary treatment 4 Primary clarifi er 5 Biological reactor Secondary treatment 6 Secondary clarifi er 7 Pre-fi ltration 8 Micro/nano/ultrafi ltration Tertiary treatment 9 Reverse osmosis 10 Ozonation 11 Chlorination 12 Sludge digester Sludge treatment 13 Sludge dewatering 4 Process Water treatment industry Secondary treatment 5 Biological reactor 9 8 6 Secondary clarifi er 10 7 11 6 5 Tertiary treatment 7 Pre-fi ltration 8 Micro/nano/ultrafi ltration 9 Reverse osmosis 10 Ozonation 11 Chlorination Circulating Directional Industrial Pressure Flow Process Fluid control Cylinders Positioners Pumps Fittings Tubing fi lters switches switches valves Temperature valves Controller 5 SMC products for the water treatment industry Low maintenance fi lter Quick change fi lter for FN1/FN4 Series cleaning solvent · Nominal fi ltration rating: 5, FQ1 Series 20 µm · Nominal fi ltration rating: 0.2 · Flow rate: FN1: 40 and 80 l/ to 105 µm min; FN4: 250 l/min. · Flow rate: 5 to 30 l/min. High precision fi lter Bag fi lter FGH Series FGF Series · Nominal fi ltration rating: 0.2 · Nominal fi ltration rating: 5 to to 13 µm 100 µm · Flow rate: 5 to 70 l/min. · Flow rate: 400 to 2000 l/min. Industrial fi lters High fl ow fi lter Medium fl ow fi lter FGG Series FGE Series · Nominal fi ltration rating: 0.5 · Nominal fi ltration rating: 0.5 to 120 µm to 120 µm · Flow rate: 160 to 370 l/min. · Flow rate: 45 to 230 l/min. Low fl ow fi lter Applications FGD Series · Pre-fi ltration · Reverse osmosis device · Nominal fi ltration rating: 0.5 · Highly purifi ed water to 120 µm systems · Flow rate: 11 to 63 l/min. Our FN4 series combines an eco-friendly reusable stainless steel fi ltration element with a back-fl ush capability, which means that both fi ltering and back-fl ushing can be performed in parallel. 6 SMC products Water treatment industry Our customers are particularly satisfi ed with our latest pressure switches; with their design functionality and ease of use. The information accuracy and its rapid availability assist them in their daily decision making. Furthermore, customers fi nd the energy effi ciency and cost effectiveness features advantageous. 2-colour display digital High-precision digital pressure switch pressure switch with ZSE20C/ISE20C Series IO-Link २ २ · Pressure range: ISE7 /7 G Series vacuum: [-0.1, 0] MPa; · Rated pressure: compound: [-0.1, +0.1] MPa 1 MPa (ISE70) and positive: [-0.1, 1] and [-0.1, 1.6 Mpa (ISE71) for air; 2] MPa 1 MPa (ISE70G), 2 MPa · Stainless steel construction. (ISE75G), 5 MPa (ISE76G) and 10 MPa (ISE77G) for general fl uids - Output: IO-Link and NPN/ PNP. General purpose Pressure sensor pressure switch PSE560 Series ISG Series · Pressure range: positive · Pressure range: positive pressure [0, 500] kPa [0.02, 0.3] MPa, [0.05, and [0, 1] MPa, vacuum 0.7] MPa, [0.1, 1] MPa; [0, -101] kPa, compound vacuum [-10, -100] kPa pressure [-100, 100] kPa · Wetted material: stainless · Wetted material: SUS316L. Pressure steel 316, brass/phosphor switches, bronze. sensors & Pressure sensor Multi-channel digital monitors PSE570 Series pressure sensor · Pressure range: vacuum monitor [-0.1, 0 MPa]; compound PSE200 Series [-0.1, +0.1 MPa]; positive · Controller for 4 sensor [-0.1, 1 MPa] and [-0.1, inputs 2 MPa] · Automatic sensor · Stainless steel construction. recognition. Applications · Reverse osmosis device 2-colour display digital 3-screen display sensor · Ozone systems · Chlorine dioxide device pressure sensor monitor · Micro/ultra/nano fi ltration monitor PSE300AC Series · Vacuum distillation PSE300 Series · Highly purifi ed water · Visualisation of settings systems · 2 colour display determined · Easy screen switching. · Bernoulli fi lter by switching status · Bilge water · 2 switch outputs and · Electrodeionisation analogue output. 7 3-Colour Display Digital 3-Colour Display Flow Switch Electromagnetic Type PF3W Series Digital Flow Switch · Flow range: Up to 250 l/min LFE Series · Applicable fl uids: water, · Flow range: 0.5 to 20 l/min, deionized water, chemical, 2.5 to 100 l/min, 5 to etc. 200 l/min · Applicable fl uids: water, water-soluble coolant. Diaphragm Style Flow Digital Flow Switch for Switch De-ionised Water and IFW5 Series Chemicals · Flow range: 1 to 10 l/min, 10 PF2D Series to 20 l/min, 20 to 50 l/min · Flow range: 0,4 to 4 l/min, · Applicable fl uids: water, 1.8 to 20 l/min, 4 to 40 l/min non-corrosive liquid. · Applicable fl uids: de- Flow ionised water and switches & chemicals. monitors Paddle Style Flow Digital Flow Monitor for Switch Water IF3 Series PF3W3 Series · Flow range: 14 to 60 l/ · The settings of the master min, 20 to 1500 l/min, 36 to sensor can be copied to the 2600 l/min slave sensors · Applicable fl uids: water, non · Applicable to e-con. corrosive liquid. 4-channel Flow Monitor 3-colour Display Digital PF2D200 Series Flow Monitor Applications · Multiple sensors (max. 4 LFE0 Series pcs.) can be managed · Ozone systems · Top screen displays collectively · Chlorine dioxide device instantaneous fl ow rate · Micro/ultra/nano fi ltration · Applicable to e-con. · Lower screen can be set · Vacuum distillation to display: set value, fl ow · Highly purifi ed water direction, accumulated systems value, line name, peak/ · Sand fi ltration bottom value. Our LFE series can manage conductive fl uids, such as water and water-soluble coolant, or fl uids that have at least 5 µS/cm conductivity. This is due to the fact that the materials that come into contact with those fl uids are PPS, FKM and brass. 8 SMC products Water treatment industry Air operated Angle seat valve 2-port valve for steam VXB Series VND Series · Port size: 3/8” to 3/4“; orifi ce · Port size: 1/8” to 2”; orifi ce size: 11 to 18 mm size: 7 to 50 mm · Body materials: stainless · Body materials: stainless steel and bronze. steel (316L) and bronze. Direct air operated 2-port valve for fl ow 2-port valve control VXA Series VNB Series · Port size: 1/8” to 1/2”; orifi ce · Port size: 1/8” to 2“; orifi ce size: 3 to 10 mm size: 7 to 50 mm · Body materials: brass and · Body materials: bronze, stainless steel. stainless steel and aluminium. High purity chemical liquid valve LVA/LVC/LVH Series · Port size: 1/8” to 1“; orifi ce size: 2 to 22 mm · Body material: new PFA, stainless steel and PPS. Direct operated 2-port solenoid valve Compact 2-port VX2 Series solenoid valve Process · Port size: port size: 1/8” to VDW Series 1/2”; one -touch fi tting: 6 to · Body materials: aluminium, valves 12 mm; orifi ce diameter: 2 resin, brass and stainless to 10 mm steel · Body materials: aluminium, · Port size: M5 to 1/8”; resin, brass and stainless one-touch fi tting: 3.2 to steel. 6 mm; orifi ce diameter: 1 to 3.2 mm. Compact/lightweight 2/3 port media 2-port solenoid valve separated valve VDW30/40-XF Series LVMK Series · One-touch fi tting: Ø 4 to · Body material: PPS Ø 10; quick fastener: P7 to · Orifi ce diameter: 2 mm. P10; orifi ce size: 1 to 6 mm · Body materials: PPS. Energy saving type 2-Port Solenoid Valve 2-port solenoid valve with built-in Y-strainer VXE Series VXK Series Applications · Port size: 1/8” to 1”; orifi ce · Port size: 1/8” to 3/8”; diameter: 2 to 25 mm Orifi ce diameter: 2 to 8 mm · Reverse osmosis device · Body materials: brass and · Body materials: brass. · Ozone systems stainless steel. · Chlorine dioxide device · Micro/ultra/nano fi ltration · Vacuum distillation 3-port solenoid valve 2/3 port solenoid valve · Highly purifi ed water VX3 Series for chemicals systems · Bilge water · Port size: 1/8” to 3/8”; orifi ce LVM Series · Sludge treatment diameter: 1.5 to 4 mm · Port size: M5, M6 and 1/4- · Sand fi ltration · Body materials: brass and · Bernoulli fi lter 28 UNF; orifi ce diameter: stainless steel. · Pre-fi ltration 1,1 to 2 mm · Electrodeionisation · Body materials: PFA and · Flocculation PEEK. 9 Pilot operated 2-port solenoid valve Zero differential VXD Series pressure type 2-port Process · Port size: 1/4” to 1”; one solenoid valve -touch fi tting: 10 to 12 mm; VXZ Series valves orifi ce diameter: 10 to · Port size: 1/4” to 1”; one 50 mm -touch fi tting: 10 to 12 mm; · Body materials: aluminium, Applications Orifi ce diameter: 10 to resin, brass and stainless 25 mm · Reverse osmosis device steel.
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

    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.
  • Crystallization of Oxytetracycline from Fermentation Waste Liquor: Influence of Biopolymer Impurities

    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.
  • State-Of-The-Art Water Treatment in Czech Power Sector

    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.
  • Coagulation-Flocculation As a Submerged Biological Filter Pre-Treatment with Landfill Leachate

    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.
  • Integration of Aqueous Two-Phase Extraction As Cell Harvest and Capture Operation in the Manufacturing Process of Monoclonal Antibodies

    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.
  • Pretreatment Process Optimization and Reverse Osmosis Performances of a Brackish Surface Water Demineralization Plant, Morocco

    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.
  • The Safe Use of Cationic Flocculants with Reverse Osmosis Membranes

    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.
  • Flotation and Flocculation - from Fundamentals to Applications

    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
  • Precipitation and Crystallization Processes

    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.
  • 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 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.
  • 6.3 Coagulation and Flocculation Coagulation and Flocculation Are Used to Remove Colour, Turbidity, Algae and Other Micro- Organ

    6.3 Coagulation and Flocculation Coagulation and Flocculation Are Used to Remove Colour, Turbidity, Algae and Other Micro- Organ

    6.3 Coagulation and flocculation Coagulation and flocculation are used to remove colour, turbidity, algae and other micro- organisms from surface waters. The addition of a chemical coagulant to the water causes the formation of a precipitate, or floc, which entraps these impurities. Iron and aluminium can also be removed under suitable conditions. The floc is separated from the treated water by sedimentation and filtration, although flotation processes may be used in place of sedimentation. The most commonly used coagulants are aluminium sulphate and ferric sulphate, although other coagulants are available. Coagulants are dosed in solution at a rate determined by raw water quality near the inlet of a mixing tank or flocculator. The coagulant is rapidly and thoroughly dispersed on dosing by adding it at a point of high turbulence. The water then passes into the sedimentation tank to allow aggregation of the flocs, which settle out to form sludge. The advantages of coagulation are that it reduces the time required to settle out suspended solids and is very effective in removing fine particles that are otherwise very difficult to remove. Coagulation can also be effective in removing many protozoa, bacteria and viruses. The principal disadvantages of using coagulants for treatment of small supplies are the cost and the need for accurate dosing and frequent monitoring. Coagulants need accurate dosing equipment to function efficiently and the dose required depends on raw water quality that can vary rapidly. The efficiency of the coagulation process depends on the raw water properties, the coagulant used and operational factors including mixing conditions, coagulant dose rate and pH value.
  • Stormwater Best Management Practice: Polymer Flocculation

    Stormwater Best Management Practice: Polymer Flocculation

    Stormwater Best Management Practice Polymer Flocculation Polymer Flocculation for Reducing Minimum Measure Stormwater Turbidity and Its Aquatic Life Construction Site Stormwater Runoff Control Toxicity Subcategory Flocculation is the process where a chemical agent (flocculant) Sediment Control is used to reduce the turbidity of a liquid by binding suspended particles in the liquid together to form larger particles (flocs) Stormwater Turbidity and Its Aquatic Life that are heavy enough to settle to the bottom of the liquid. Toxicity When the liquid is stormwater runoff, this particle binding and settling process reduces soil erosion and the runoff’s turbidity, Turbidity is a measure of the amount of suspended material in as well as the aquatic life toxicity associated with turbidity. a liquid. In stormwater or a natural waterbody (e.g., river, lake, Some polymers are good flocculants. Polymers are chemical or estuary), turbidity depends on the amount of suspended compounds that have very large molecules composed of one sediment, dissolved organic matter, and plankton in the water. or more structural units that are joined together in a repeating Turbid stormwater entering a natural waterbody can significantly pattern to form long chain-like macromolecules. The two degrade the habitat of fish and other aquatic life. Reductions red wavy ribbons in Figure 1 represent polymer molecules in light levels may reduce submerged aquatic vegetation that provides the cover necessary for survival of the prey species. Soil Or reduced visibility may make it difficult for predators to find - - + + evasive prey. Gravel on the bottom of a riverbed, which is + + + + necessary for salmon to spawn successfully, may be covered - - Ion Bridge - - Cationic Polymer Soil Chains with sediments.