magnetic separators

magnetic separators

Some type of Magnetic Separatoris always advisable and should be a standard piece of equipment in every mill. When one (Suspended Type) Magnet is located just ahead of the primary jaw crusher, and another is placed before the intermediate crusher, all danger of damage to the crushers from tramp iron is eliminated. The tramp iron usually consists of stray bits from drills, hammerheads, and other tools which can seriously damage crushing equipment.

The suspended type of Magnetic Separatorhas its place where space is not the deciding factor. The suspension of the magnet above the ore conveyor preceding the jaw crusher allows it to be swung aside when replacing conveyor belt or working on the conveyor pulley; and also for periodical removal of adhering tramp iron to maintain maximum efficiency. The suspension principle makes this a low cost unit.

Care should be used in the selection of this type of magnet as the width of the conveyor belt, the proper depth of the ore being conveyed, and the average percentage of foreign material to be eliminated, determine the size of magnet used. The magnets are made in circular or rectangular types and may be suspended on either a trolley or crane, or on the stationary suspension principle. Let us make recommendations for the correct size and type of this low cost magnet best suited to your needs.

The Alnico Horseshoe Magnet is a small, extremely powerful, hand magnet. It is an alloy of aluminum, nickel, and cobalt, very high in retentivity, and many times stronger than the ordinary horseshoe magnet. It is extremely resistant to demagnetization and is affected only slightly by shock or temperatures as high as 1200 F. This magnet provides an invaluable tool for the assayer, mineralogist, and plant operator. Minerals that are even moderately magnetic may be separated from non-magnetic material with this magnet and it is small and light enough to carry about in your pocket.

The high intensity Magnetic Pulley is one of the most satisfactory and economical magnets in use today. It is a sure way of getting a practically iron-free product. The low cost of current consumption, positive operation, low maintenance, and moderate initial cost, all have a definite place in planning or improving every efficient milling, processing, or industrial plant.

The greatest asset of theMagnetic Pulley is the ability of this compact, efficient unit to attract and hold the tramp material to the surface of the drum until it is away from the material being conveyed. The weight of the iron brings it to the bottom of the conveyed material and it is thus in an ideal position to be attracted to the Magnetic Pulley more quickly. The tramp material is then disposed of when the revolving drum or cylinder reaches thedemagnetized field or dead spot on the under side of the drum and the iron isallowed to drop into a bin provided for this purpose.

No one type of Magnetic Pulley will be adaptable to every need, although there is a Magnetic Pulley for every specific application. The design used for collecting tramp iron is entirely different from that used for purification or concentration purposes. The construction of the Magnetic Pulley is such as to allow the maximum flux density to be obtained. Each section is a separate magnet (having a separate casting) with its own coil, core, and north and south poles. The Magnetic Pulley is cool operating which prolongs the life of the pulley and is necessary in order that the unit maintain its most efficient operation.

The Magnetic Pulley is used as a head pulley of a conveyor and very often the shaft of the Magnetic Pulley can be made to correspond with the shaft of the original pulley. It is necessary then only to place the Magnetic Pulley shaft into the existing bearings.

The collector ring housing is attached to any suitable bracket. The contact rings are in place on the shaft. The switch cabinet is completely wired, and the connection between it and the contact brushes is accomplished quickly.

Magnetic Pulleys operate on direct current only. They are wound for either 110 or 220 volts, although higher voltage can be used when specified. Alternating current is not suitable, and when direct current is not available, a generator, motor-generator set, or a rectifier is installed to convert the alternating current to direct current. However, these generator sets are of small size because of the nominal current requirements of the pulley.

A large range of sizes, both in diameter and width, is available and there is a capacity to suit every individual requirement. Pulley width required is determined by the width of the conveyor belt used and the diameter of a Magnetic Pulley determines its strength; the larger the diameter the greater the strength. Data necessary for recommendations is kind of material to be treated, size of material, amount to be handled per hour, whether wet or dry, purpose of separation, and characteristics of available current supply.

The Dings-Crockett High Intensity (Wet Type) Submerged Belt Magnetic Separator is designed for wet separations. It has found wide application in the concentration of magnetite, ilmenite, and other materials of similar magnetic susceptibility where it gives an amazingly clean-cut separation of tailings, middlings, and concentrates. Its magnetic efficiency is well above 99%.

The separator will efficiently handle large capacities of unsized ore from minus down to the finest dust. Control of the separator is simple, steady, and not critical. Feed rates may be varied over a wide range and practically the same results obtained.

The Dings Rowand-Wetherill Magnetic Separator handles many materials which cannot be handled satisfactorily by any other type of magnetic separator. Even the finest material can be readily separated with highest efficiency.

The material to be treated (which must be absolutely dry) flows from the hopper onto the feed roller which spreads it in a thin, uniform layer over the whole width of the conveyor belt as it travels toward the poles of the magnet system. As the material passes between the poles of the first magnet the magnetic particles are strongly attracted toward the upper pole and jump toward it. They are intercepted by the cross belt which removes them quickly from the influence of the magnets and allows them to drop into a receptacle provided at one side. The use of a series of magnets of different strengths permits the separation from one another of materials having different magnetic permeabilities, as well as the separation of magnetic materials. The separate removal of the strongest as well as the weakest magnetic mineral is possible.

The capacity of any magnetic separator depends on so many variables that it is impossible to estimate the exact tonnage until a test has been made and all necessary data received. Let us engineer your proposed installation.

The Stearns (Ring Type) Magnetic Separator differs materially from the cross belt type machine. A steel take-off ring is employed in place of a cross belt to intercept and carry the magnetic material beyond the conveyor belt to final delivery. It has been found in certain applications that the steel take-off ring actually improves the separation. The ring has a broad flat surface adjacent to the magnetic pole to receive and carry the flux built up by the magnet. The sides are shaped to form a parabolic curve ending in a defined peak where the concentrated field is produced. The magnetic material is attracted from the feed belt to the inductively magnetized moving ring, which forms a part of the magnet pole, while in the field. In moving away from the field the ring carries the magnetic particles beyond the conveyor belt, effecting an automatic discharge as it approaches the zero point between the plus and minus poles.

The magnetic gap on this unit can be opened or closed within fixed limits by a simple and very convenient adjustment. Adjustments are usually made while the machine is operating. This applies not only to the magnetic air gap, but also to the flux density of the magnetic field, as the power or attractive force of the magnet is regulated by a rheostat which controls the amount of current used. Such adjustments will accommodate a wide range of sizings and variable magnetic permeability of materials.

Capacities of magnetic separator units vary widely as their most efficient operation depends upon a large number of factors. It is therefore impossible to estimate the exact tonnage that can be handled without complete data and preliminary tests. Let us engineer your installation.

magnetic separator market: recycling industry set to become significant demand generator: global industry analysis (2014-2018) and opportunity assessment (2019-2029)

magnetic separator market: recycling industry set to become significant demand generator: global industry analysis (2014-2018) and opportunity assessment (2019-2029)

FMI delivers personalised research services by deploying a broad spectrum of research databases, resources, and methodologies. We offer customised research reports for various industry verticals and regions.

Magnetic separators are a vital part of the metal recycling industry. Metal recycling is the process of collecting and processing used metals to develop recycled metals. Metals can be recycled without altering their metallic properties, which comes as an advantage. The prominent reason for the usage of recycled metal is less energy consumption. Energy consumption for producing virgin ore is 20 times more than the recycled ore.

Moreover, metal recycling has advantages such as environmental benefits, energy conversion efficiency, and economic benefits. The manufacturing industry is more inclined towards using recycled metals as raw materials, owing to benefits such as effective cost and energy consumption rate. For recycled metal production, collection of metals from the waste is a crucial part, which is sorted with magnetic separators. The increased use of recycled metals in the manufacturing industry results in increasing usage of magnetic separators.

In the mining industry, bulk materials extracted from the mine are required to be reformed into the required size. Mining crushers are utilized for crushing the bulk material into the required material size. In the crushing process, tramp metal might damage the processing equipment such as crushers. This damage is estimated to impact the operational life and the maintenance cost of the equipment.

To avoid damage to the processing equipment from the tramp, magnetic separators are installed before the processing equipment to remove unwanted materials from the extraction mixture. Increasing usage of process equipment in the mining industry is anticipated to positively affect the utilization of magnetic separators.

Magnetic separators find significant applications in the cement industry to separate unwanted metallic particles from raw materials or processed cement. Increasing construction projects particularly, in developed countries is expected to fuel the growth of cement industries, subsequently increasing the demand for magnetic separators.

A key factor for our unrivaled market research accuracy is our expert- and data-driven research methodologies. We combine an eclectic mix of experience, analytics, machine learning, and data science to develop research methodologies that result in a multi-dimensional, yet realistic analysis of a market.

Magnetic separators market continues to witness significant gains owing to growing usage as an effective tool to separate unwanted material generated by mining extraction process. Growing rate of mining extraction process, coupled with increasing requirement of maintaining the purity of extracted material is driving the demand for magnetic separators in metal and mineral mining industry.

The magnetic separator market is envisaged to grow at a steady pace during the forecast period. Gains will be driven by growing adoption of magnetic separators as a viable instrument for the filtration and removal of ferromagnetic foreign bodies from product streams that ensure high product quality and prevent damage to machines. Increasing development of magnetic separators to maintain energy consumption level is likely to drive market growth.

East Asia will continue to spearhead magnetic separators market during the forecast period, owing to positive outlook for various end-use industries, such as metal and mineral mining, food and beverage, and recycling in the region.

Growing rate of adaption of technological advancement in the region has been generating increased demand for magnetic separators. South Asia holds high growth potential for magnetic separators market, owing to substantial growth in several processing industries in India and ASEAN.

Increasing demand for a high performance separation equipment, coupled with the growing focus of manufacturers on business expansion via establishing new distribution centers and sales offices to extend geographic presence likely to scale up the market value considerably. Growing application of magnetic separator in recycling facilities holds lucrative growth opportunities for stakeholders.

magnetic separator - an overview | sciencedirect topics

magnetic separator - an overview | sciencedirect topics

As magnetic separators progress toward larger capacity, higher efficiency, and lower operating costs, some subeconomic iron ores have been utilized in recent years. For example, magnetite iron ore containing only about 4% Fe (beach sands or ancient beach sands) to 15% Fe (iron ore formations) and oxidized iron ore of only about 10% Fe (previously mine waste) to 20% Fe (oxidized iron ore formations) are reported to be utilized. They are first crushed and the coarse particles pretreated using roll magnetic separators. The magnetic product of roll magnetic separators may reach 2540% Fe and then is fed to mineral processing plants.

As shown in Figure5, slurry is fed from the top of an inclined screen in a low-intensity magnetic field, with the mesh size of screen sufficiently larger than those of particles in slurry. As the slurry flows down the above surface of screen, magnetic particles agglomerate with the size of agglomerations increasingly growing and roll down as magnetic concentrate at the lower end of screen. The less- or nonmagnetic particles pass through the screen as tailings. Figure5 shows the operation of screen magnetic separators for cleaning of magnetite.

Commercial magnetic separators are continuous-process machines, and separation is carried out on a moving stream of particles passing into and through the magnetic field. Close control of the speed of passage of the particles through the field is essential, which typically rules out free fall as a means of feeding. Belts or drums are very often used to transport the feed through the field.

As discussed in Section 13.4.1, flocculation of magnetic particles is a concern in magnetic separators, especially with dry separators processing fine material. If the ore can be fed through the field in a monolayer, this effect is much less serious, but, of course, the capacity of the machine is drastically reduced. Flocculation is often minimized by passing the material through consecutive magnetic fields, which are usually arranged with successive reversals of the polarity. This causes the particles to turn through 180, each reversal tending to free the entrained gangue particles. The main disadvantage of this method is that flux tends to leak from pole to pole, reducing the effective field intensity.

Provision for collection of the magnetic and nonmagnetic fractions must be incorporated into the design of the separator. Rather than allow the magnetics to contact the pole-pieces, which then requires their detachment, most separators are designed so that the magnetics are attracted to the pole-pieces, but come into contact with some form of conveying device, which carries them out of the influence of the field, into a bin or a belt. Nonmagnetic disposal presents no problems; free fall from a conveyor into a bin is often used. Middlings are readily produced by using a more intense field after the removal of the highly magnetic fraction.

Conventional magnetic separators are largely confined to the separation or filtration of relatively large particles of strongly magnetic materials. They employ a single surface for separation or collection of magnetic particles. A variety of transport mechanisms are employed to carry the feed past the magnet and separate the magnetic products. The active separation volume for each of these separators is approximately the product of the area of the magnetised surface and the extent of the magnetic field. In order for the separators to have practical throughputs, the magnetic field must extend several centimetres. Such an extent implies a relatively low magnetic field gradient and weak magnetic forces.

To overcome these disadvantages HGMS has been developed. Matrices of ferromagnetic material are used to produce much stronger but shorter range magnetic forces over large surface areas. When the matrices are placed in a magnetic field, strong magnetic forces are developed adjacent to the filaments of the matrix in approximately inverse proportion to their diameter. Since the extent of the magnetic field is approximately equal to the diameter of the filaments the magnetic fields are relatively short range. However, the magnetic field produced is intense and permits the separation and trapping of very fine, weakly magnetic particles (Oberteuffer, 1979).

The transport medium for HGMS can be either liquid or gaseous. Dry HGMS processing has the advantage of a dry product although classification of the pulverised coal is required to ensure proper separation. Small particles tend to agglomerate and pass through the separator. It has been shown that individual particles of coal in the discharge of a power plant pulveriser flow freely and hence separate well only if the material below about 10 m is removed (Eissenberg et al., 1979). Even then drying of that part of run of mine coal to be treated by HGMS may be required to ensure good flow characteristics.

A schematic representation of a batch HGMS process is shown in Figure 11.5 (Hise, 1979, 1980; Hise et al., 1979). It consists of a solenoid, the core cavity of which is filled with an expanded metal mesh. Crushed coal is fed to the top of the separator. Clean coal passes through while much of the inorganic material is trapped to be released when the solenoid is later deactivated.

Data from a batch HGMS process of one size fraction of one coal are plotted in Figure 11.6 as weight per cent of material trapped in the magnetic matrix, the product sulphur and the product ash versus the independent variable of superficial transport velocity. At low superficial transport velocities the amount of material removed from the coal is high partly due to mechanical entrapment. As the velocity is increased the importance of this factor diminishes but hydrodynamic forces on the particles increase. These hydrodynamic forces oppose the magnetic force and the amount of material removed from the coal decreases (Hise, 1979).

For comparison, Figure 11.7 shows data from a specific gravity separation of the same size fraction of the same coal. While the sulphur contents of the products from the two separation processes are similar the ash content of the HGMS product is considerably higher than that of the specific gravity product. It should be emphasised that this comparison was made for one size fraction of one coal.

More recently dry HGMS has been demonstrated at a scale of 1 t/h on carousel type equipment which processes coal continuously (Figure 11.8; Hise et al., 1981). A metal mesh passes continuously through the magnetised cavity so that the product coal passes through while the trapped inorganics are carried out of the field and released separately.

Wet HGMS is able to treat a much wider range of coal particle sizes than dry HGMS. The efficiency of separation increases with decreasing particle size. However, depending on the end use a considerable quantity of energy may have to be expended in drying the wet, fine coal product. Wet HGMS may find particular application to the precleaning of coal for use in preparing coal water mixtures for subsequent combustion as both pulverising the coal to a fine particle size and transporting the coal in a water slurry are operations common to both processes.

Work at Bruceton, PA, USA has compared the pyrite reduction potential of froth flotation followed by wet HGMS with that of a two stage froth flotation process (Hucko and Miller, 1980). Typical results are shown in Figures 11.9 and 11.10. The reduction in pyritic sulphur is similar in each case although a greater reduction in ash content is achieved by froth flotation followed by HGMS than by two stage froth flotation. However, Hucko (1979) concludes that it is highly unlikely that HGMS would be used for coal preparation independently of other beneficiation processes. As with froth flotation there is considerable variation in the amenability of various coals to magnetic beneficiation.

In the magnetic separator, material is passed through the field of an electromagnet which causes the retention or retardation of the magnetic constituent. It is important that the material should be supplied as a thin sheet in order that all the particles are subjected to a field of the same intensity and so that the free movement of individual particles is not impeded. The two main types of equipment are:

Eliminators, which are used for the removal of small quantities of magnetic material from the charge to a plant. These are frequently employed, for example, for the removal of stray pieces of scrap iron from the feed to crushing equipment. A common type of eliminator is a magnetic pulley incorporated in a belt conveyor so that the non-magnetic material is discharged in the normal manner and the magnetic material adheres to the belt and falls off from the underside.

Concentrators, which are used for the separation of magnetic ores from the accompanying mineral matter. These may operate with dry or wet feeds and an example of the latter is the Mastermag wet drum separator, the principle of operation of which is shown in Figure 1.43. An industrial machine is shown in operation in Figure 1.44. A slurry containing the magnetic component is fed between the rotating magnet drum cover and the casing. The stationary magnet system has several radial poles which attract the magnetic material to the drum face, and the rotating cover carries the magnetic material from one pole to another, at the same time gyrating the magnetic particles, allowing the non-magnetics to fall back into the slurry mainstream. The clean magnetic product is discharged clear of the slurry tailings. Operations can be co- or counter-current and the recovery of magnetic material can be as high as 99.5 per cent.

An example of a concentrator operating on a dry feed is a rotating disc separator. The material is fed continuously in a thin layer beneath a rotating magnetic disc which picks up the magnetic material in the zone of high magnetic intensity. The captured particles are carried by the disc to the discharge chutes where they are released. The nonmagnetic material is then passed to a second magnetic separation zone where secondary separation occurs in the same way, leaving a clean non-magnetic product to emerge from the discharge end of the machine. A Mastermagnet disc separator is shown in Figure 1.45.

The removal of small quantities of finely dispersed ferromagnetic materials from fine minerals, such as china clay, may be effectively carried out in a high gradient magnetic field. The suspension of mineral is passed through a matrix of ferromagnetic wires which is magnetised by the application of an external magnetic field. The removal of the weakly magnetic particles containing iron may considerably improve the brightness of the mineral, and thereby enhance its value as a coating or filler material for paper, or for use in the manufacture of high quality porcelain. In cases where the magnetic susceptibility of the contaminating component is too low, adsorption may first be carried out on to the surface of a material with the necessary magnetic properties. The magnetic field is generated in the gap between the poles of an electromagnet into which a loose matrix of fine stainless steel wire, usually of voidage of about 0.95, is inserted.

The attractive force on a particle is proportional to its magnetic susceptibility and to the product of the field strength and its gradient, and the fine wire matrix is used to minimise the distance between adjacent magnetised surfaces. The attractive forces which bind the particles must be sufficiently strong to ensure that the particles are not removed by the hydrodynamic drag exerted by the flowing suspension. As the deposit of separated particles builds up, the capture rate progressively diminishes and, at the appropriate stage, the particles are released by reducing the magnetic field strength to zero and flushing out with water. Commercial machines usually have two reciprocating canisters, in one of which particles are being collected from a stream of suspension, and in the other released into a waste stream. The dead time during which the canisters are being exchanged may be as short as 10 s.

Magnetic fields of very high intensity may be obtained by the use of superconducting magnets which operate most effectively at the temperature of liquid helium, and conservation of both gas and cold is therefore of paramount importance. The reciprocating canister system employed in the china clay industry is described by Svarovsky(30) and involves the use a single superconducting magnet and two canisters. At any time one is in the magnetic field while the other is withdrawn for cleaning. The whole system needs delicate magnetic balancing so that the two canisters can be moved without the use of very large forces and, for this to be the case, the amount of iron in the magnetic field must be maintained at a constant value throughout the transfer process. The superconducting magnet then remains at high field strength, thereby reducing the demand for liquid helium.

Micro-organisms can play an important role in the removal of certain heavy metal ions from effluent solutions. In the case of uranyl ions which are paramagnetic, the cells which have adsorbed the ions may be concentrated using a high gradient magnetic separation process. If the ions themselves are not magnetic, it may be possible to precipitate a magnetic deposit on the surfaces of the cells. Some micro-organisms incorporate a magnetic component in their cellular structure and are capable of taking up non-magnetic pollutants and are then themselves recoverable in a magnetic field. Such organisms are referred to a being magnetotactic.

where mpap is the inertial force and ap the acceleration of the particle. Fi are all the forces that may be present in a magnetic separator, such as the magnetic force, force of gravity, hydrodynamic drag, centrifugal force, the friction force, surface forces, magnetic dipolar forces, and electrostatic forces among the particles, and others.

Workable models of particle motion in a magnetic separator and material separation must be developed separately for individual types of magnetic separators. The situation is complicated by the fact that many branches of magnetic separation, such as separation by suspended magnets, magnetic pulleys, or wet low-intensity drum magnetic separators still constitute highly empirical technology. Hesitant steps have been taken to develop theoretical models of dry separation in roll and drum magnetic separators. Alternatively, open-gradient magnetic separation, magnetic flocculation of weakly magnetic particles, and wet high-gradient magnetic separation (HGMS) have received considerable theoretical attention. A notable number of papers dealing with the problem of particle capture in HGMS led to an understanding of the interaction between a particle and a matrix element. However, completely general treatment of the magnetostatic and hydrodynamic behavior of an assembly of the material particles in a system of matrix elements, in the presence of a strong magnetic field, is a theoretical problem of considerable complexity which has not been completed, yet. Detailed description of particle behavior in various magnetic separators can be found in monographs by Gerber and Birss (1983) and Svoboda (1987, 2004).

The brick material ratio was: Slag(1.0mm<): Grog (3.0mm<): Ceramic Gravel (1.0mm<): Clay (1.0mm<) at 20 : 35 : 25 : 20. To this mixture, 2% of pigment were added. Kneading and blending was done by a Mller mixer for 15 minutes. Molding was done by a 200 ton friction press, and the bricks were loaded onto the sintering truck.

This paper presents preliminary results using the Magnetic Micro-Particle Separator, (MM-PS, patent pending) which was conceived for high throughput isothermal and isobaric separation of nanometer (nm) sized iron catalyst particles from Fischer-Tropsch wax at 260 oC. Using magnetic fields up to 2,000 gauss, F-T wax with 0.30.5 wt% solids was produced from 25 wt% solids F-T slurries at product rates up to 230 kg/min/m2. The upper limit to the filtration rate is unknown at this time. The test flow sheet is given and preliminary results of a scale-up of 50:1 are presented.

Most loads for flap valves, conveyors, vibrating feeders, crushers, paddle feeders, magnetic separators, fans and trash screens generally are supplied at 415 V three-phase 50 Hz from the 415 V Coal Plant Switchboard, although 3.3 kV supplies may be used when the duty demands. Stacker/reclaimer machines are supplied at 3.3 kV. Electrical distribution is designed to safeguard the independent operational requirements of the duplicated coal plant facilities and to ensure that an electrical fault will not result in the total loss of coal supplies to the boilers.

The first step in any form of scrubbing unit is to break the lumpy materials and remove tramp elements by a magnetic separator. The product is then led into the scrubbing unit. The dry scrubbing principle is to agitate the sand grains in a stream of air so that the particles shot-blast each other. A complete dry scrubbing plant has been described in a previous book of this library in connection with sodium silicate bonded sands.* For clay-bonded sands the total AFS clay content in the reclaimed sand varies from 05% to 25% clay depending on the design of the plant.

magnets & retrieval tools - harbor freight tools

magnets & retrieval tools - harbor freight tools

We have invested millions of dollars in our own test labs and factories. So our tools will go toe-to-toe with the top professional brands. And we can sell them for a fraction of the price because we cut out the middleman and pass the savings on to you. It's just that simple!

magnetic separator products - dings magnetics

magnetic separator products - dings magnetics

Separate aluminum, die-cast metal, or copper from nonmetallic material with Dings' new eddy current separator. Heavy duty, durable design for long life in demanding applications, and features easy adjustments and maintenance. LEARN MORE.....

maggie magnetic separator

maggie magnetic separator

The ZGF Magnetic Separator (Maggie), is an innovative and patented technology. The fully automatic, in-line, high intensity, self-cleaning, patented magnetic separator is the best available technology for separating magnetic contaminants from process fluids. Maggie can remove particles down to 1 micron without damaging critical process fluids such as machining coolants, cleaning / degreasing solutions or polymer quench fluids.

Zero Gravity Filters Maggie is an effective, efficient and environmentally responsible solution that can optimizelife-cycle costand minimize the environmental footprint of industrial operations where ferrous (magnetic) contaminants are present/introduced.

Media filters such as cartridge filters and roll media create a physical barrier which captures all particles larger than the micron opening. You dont want to remove everything! For example, you dont want to remove defoamer particles, surfactant micelles or emulsion droplets. You want to remove the contaminants, the ferrous fines and particles that deteriorate the process fluids, negatively impact quality and productivity, and drive up maintenance costs.

Take two minutes and watch the video below to better understand how the best-in-class Maggie Magnetic Separator technology works. After watching the video, we are sure you will be thinking of many processes andapplicationsin your facility where ZGF magnetic separation technology could provide significant value.

Maggies stainless-steel body houses our proprietary magnetic cores. The magnetic cores are thin walled, seamless stainless tubes that seal magnetic shuttle assemblies. Each magnetic core contains several magnet/pole combinations that generate a magnetic field greater than 10,000 Gauss at the surface of the tube. The magnetic cores are assembled into different Maggie sizes/models to best accommodate the flow and loading characteristics of the application/process.

All of Maggies wetted components (other than elastomers) are stainless steel. Maggie is compatible with a wide range of liquids and operating conditions up to 200oF and 100 psi. Maggie is available with four valve seat materials (Viton, Buna, EPDM and Teflon) and four O-ring materials (Viton, Buna, EPDM and ETP). Valve Seat and O-ring material selection is based upon compatibility with the process fluid.

Click on the desired Maggie modelMG100,MG300,MG600,MG1200,MG2600for a detailed product specification sheet. For a comprehensive overview of ZGF Maggie technology, click on theMaggie Product Data Sheet.

Three different types of Maggie controls provide an easy and convenient way to program Maggie to your exact specifications. All control system options feature automatic purge (i.e. self-cleaning cycle) based on time interval and manual override functionality. The Maggie Control options include:

The Maggie Watch allows for continuous monitoring and immediate notification should one or more Maggies experience a fault. The system provides capability for local and remote monitoring and alarm notification. Detection and early action will make the repairs much easier and prevent damage to Maggie components and downstream components.

Maggie is the best technology for removing ferrous contaminants from process fluids. The Maggie Magnetic Separator also maintains the lowest 10-year lifecycle cost and is extremely environmentally friendly; Maggies environmentally responsible design is the green standard and is highly respected throughout the industry.

Click on the linkSuccess Storiesto learn more about how our customers were able to realize value via implementation of ZGF Maggie technology. Weve probably helped somebody that has the same challenges as you! The table below outlines the features and benefits of ZGF Maggie technology.

The Maggie product family also includes theSmart Drum and Smart Drum PLUS (SD)fluid recovery devices. The purpose of the SD is to physically remove the magnetic fines from the Maggie purge fluid and return clean fluid back to the process.

When the Maggie and Smart Drum products are configured together as a system, ZGF can provide the best available & most environmentally responsible technology with the lowest 10-year lifecycle cost in the industry. TheMaggie / Smart Drum animationeffectively shows how these two innovative technologies work together.

As your preferred partner, ZGF understands that filtration should not be a burden, rather a tool that improves quality and reduces cost. Let us help you meet your objectives and make your job easier! Please contact us for a free consultation or request a quote for an in-depth price analysis today.

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