Gyratory equipment, used in mechanical screening and sieving is based on a circular motion of the machine. Unlike other methods, gyratory screen operates in a gentler manner and is more suited to handle fragile things, enabling it to produce finer products. [1] This method is applicable for both wet and dry screening.
A distinct difference to other techniques is that the gyratory motion applied here depends on eccentric weights instead of vibrations, [2] which can be varied based on individual process requirement.
In the early 1930s, most vibratory separators had a rectangular or square design employing simple reciprocating movement. After the introduction of machines utilizing gyratory motion with orbital movements, there was a huge change in machinery industry due to the much greater screen area usage and capacity per unit mesh area. [3]
The gyratory equipment contains decks of cards on top of each other with the coarsest screen on top and the finest below. The feed is inserted from the top and gyratory motion triggers the penetration of particles into the next deck through screen openings. [4]
Casings are inclined at relatively low angles (< 15°) to the horizontal plane, with gyrations occurring in the vertical plane. [5] The eccentric masses can be varied in such as the increase of top eccentric mass leads to an increase in horizontal throw, promoting the discharge of oversize materials. Increment in bottom eccentric mass boosts the material turn over on the screen surface, maximizing the quantity of undersize-material penetration. [6] Oversize materials are discharged via tangential outlet.
The option to select number of decks enables gyratory equipment to accurately separate materials consisting particles that are very close in size. This advantage is unrivalled and proves to be significant in the powder processing industry where fine materials are involved. High separating efficiency and ease of maintenance puts gyratory screening ahead compared to other processes in terms of product quality. [5]
Existing gyratory equipment designs are already on the market, more to come with further development. Recent studies have shown that potential improvements are available for cost-saving and effective separation process. [7]
Common applications include separation used in the process industry, food industry, chemical industry and pharmaceuticals. This includes screening, classification, sifting, fiber recovery, filtration, and scalping. Gyratory screening is capable of separating finer materials as compared to other methods, and is therefore more suitable to treat fragile materials. Several applications in respective industries are shown in the table [8] below.
Industry | Applications |
---|---|
Process | Processing ceramics, pulp and paper mill, paints, sand, starch slurry |
Food | Screening of refined table salt, papaya cubes, turmeric pigment; clarification of alkaline extracts |
Chemical | Screening hydrate lime, effluent overflow from hydrocyclone; classification of polyester beads, anhydrous aluminium chloride |
General and industrial heavy duty models are available for gyratory equipment, with wooden frames for general models aiming to save cost. Industrial heavy duty models are constructed with carbon steel or stainless steel. Screen capacities vary with model sizes over a huge range to satisfy individual application requirements such as material size, bulk density, moisture contamination, etc. Models consist up to seven decks with screenings up to 325 meshes, allowing it to perform accurate separations for the finest materials. This feature comes in handy in the powder processing industry where fine powders with relatively close sizes are involved. Screens openings for different decks are to be calculated accurately to ensure accurate separation.
General models, installed with wooden frames indicating lesser reinforcements, are used for applications involving materials with distinct difference in sizes. An example for this is the removal of impurities from wood chips for biomass fuel production. In this case, the desired product will be discharged at the coarsest screen, leaving smaller impurities to sink to the bottom frames. These models are selected for more economical purposes and are less common.
The low amount of power required to run a gyratory screener enables an overall low cost of operation for this machine. This is due to the relatively lower energy required for gyratory motion compared to vibrating a massive frame. The low running cost as well as the low purchasing cost of gyratory equipment make it one of the more commonly used machines for solid-solid mechanical separation. [9]
As a gyratory screening machine employs the use of smaller stacked screen frames, the screens can be accurately placed to the precise requirements of each separation. This puts a gyratory screener at an advantage over a number of other mechanical screening devices, as many other devices would require the use of additional equipment to cope with a different type of feed. [10]
A gyratory screener can be used in many situations, regardless of whether the solid-solid mixture to be separated consists of a binary mixture, or a multi-fraction mixture. This is because the flexibility of usage of the gyratory sifter screens eliminates the need for excess screen materials, cleaners or other forms of additional apparatus. [10]
The lack of vertical motion in the mechanism of a gyratory sifter, coupled with its relatively gentle motion enables a higher accuracy in the separation of materials in the solid-solid mixture. The longer stroke involved in gyratory machines allows the finer particles to settle down and spread out. This, coupled with the horizontal motion used maximises the opportunity for the finer particles to pass, thus enhancing the quality and efficiency of separation. [11]
Most modern day gyratory screening machines employ the use of screen cleaners, which act to prevent any clogging of the gyratory sifters. The motion and mechanism of a gyratory screener enables more energy to be imparted onto the cleaners, thus actively preventing the occurrence of build-up on the gyratory sifters. In the long run, the prevention of build-up in the sifters would enable the gyratory screener to have a longer lifespan. [9]
Vibration at the vertical component by the bottom eccentric weight significantly reduces screen blinding. Additional ball trays and Kleen rings can further reduce screen blinding.[ citation needed ]
The large area of the gyratory screen requires a large floor space to be reserved. This may cause logistical problems in cases where space needs to be optimised and efficiently used. [9]
The gyratory sifter has a complex flow pattern, as well a complex drive mechanism, which is more complex than most other sifters. This could pose problems, as the complexity of the operating mechanism makes the unit harder to operate. [11]
The gyratory sifter operates at a gentle pace, and has a non-robust motion during operation. The gentle motion involved will not break up any lumps or agglomerates found in the feed. Thus, the lumps in the feed would be discarded in the top frame discharge, along with other large particles. [9]
Gyratory equipment is divided to a top and a bottom unit. The unit on top consists of screening frames supported with rugged springs attached to the circular base, which allows free vibration of the top unit. Secondary support springs are attached to for heavy duty operation, preventing the vibration of the top unit from reaching the floor. The base of the machine (bottom unit) consists of top and bottom eccentric weights attached to a heavy duty motor. Minimum energy is consumed with the installation of double extended shafts on the motors, which are attached to both the top and bottom eccentric weights. Screen decks can be mounted on top of another within the machine assembly with spacing frames connected together via stainless steel quick release clamps. [12]
There are large amounts of gyratory equipment designs available with some possible design characteristics include: [13] [14]
Gyratory equipment is capable of handling feeds of 500 tons/(h·m2) with separation efficiency up to 98% for dry processes, with feed materials to be separated not below a diameter of 4 μm.
Wet processes in the other hand can only manage a relatively high efficiency (85%) if the moisture content is above 70%.
Eccentric weights can be varied accordingly to obtain desired ratio of coarse vs fine products.
Separation efficiency factor is given by the equation: [15]
(1) |
where is the fraction of undersize in oversize and is the mass of oversize in feed.
However, correction coefficient factor is to be included in the event of multiple decks are involved, as stated in the table [15] below.
Deck Position | Correction Factor |
---|---|
Top deck | 1.0 |
2nd deck | 0.9 |
3rd deck | 0.8 |
4th deck | 0.7 |
This is due to the error carried forward for every deck. Efficiency factor is multiplied by the correction factor to obtain a more accurate estimate.
The degree of removal of wet processes is lower than their dry counterparts, which is explained by the change in physico-mechanical properties of the body.
The trend of the curve displays that feed materials with a moisture content above 70% is more suited for gyratory screening.
Both top and bottom eccentric weights play a big role in sorting a ratio of coarse versus fine products. Kinetic moment produced by the additional eccentric weights changes the oscillation swing, hence producing outputs of different rates and compositions. Increasing the upper eccentric weight promotes discharge of the coarse material. An increase in the lower eccentric weight maximizes the quantity discharged below. The relationships are demonstrated in the table below for a fixed design:
Kinetic Moment (kg·cm) | Output (Top:Bottom) | Kinetic Moment (kg·cm) | Output (Top:Bottom) |
---|---|---|---|
0 | 1.00 | 0 | 1.00 |
0.37 | 1.23 | 0.37 | 0.589 |
0.80 | 1.41 | 0.80 | 0.430 |
1.05 | 1.53 | 1.05 | 0.386 |
1.39 | 1.73 | - | - |
1.74 | 1.85 | - | - |
The kinetic moment is linked to eccentric weights with the equations: [17]
(2) |
(3) |
(4) |
where is the lower or upper wheel position (rad), is the phase angle (rad), is the mass of wheel, is the motor shaft input speed (rpm) and is the force transfer coefficient.
Gyratory equipment is only invalid if two or more materials to be separated are finer than 4 μm, which varies with different machine dimensions. The proposed value of 4 μm was calculated using the dimensions of the largest available model with the largest possible gyration radius. The critical velocity, which cannot be exceeded by the materials or else the operation fails, is given by the equation: [5] [18] [19]
(5) |
where is the length of side of aperture and is the particle diameter.
Gyration inertia formulae allow the calculations for different models with different dimensions.
Typical gyratory equipment operation circulates around eccentric weight and screen frames. Materials are distributed along the screen surface and undersize materials are allowed to penetrate the screen. A rule of thumb is to be followed for high separation efficiency and smooth operation:
Inclination Angle (°) | Output [tons/(h·m2)] | Separation Efficiency (%) |
---|---|---|
2 | 20.20 | 86 |
4 | 22.35 | 92 |
6 | 24.21 | 95 |
8 | 28.40 | 97 |
10 | 35.12 | 98 |
12 | 46.02 | 98 |
14 | 53.60 | 96 |
16 | 66.55 | 92 |
Screening can be carried out in dry or wet basis. Wet screening often requires post treatment, drying as a preparation for the downstream process. In most cases, drying is often used in the final stage of the process, however this can be varied due to the need of the process. Drying process involves the removal of water or other solutes, whereby most of the process are done by vaporization with the aid of heat supply. Thus, efficiency of heat supply equipment plays an important role to optimize the drying process.
Furthermore, this treatment can be applied on the waste stream prior the disposal. Drying greatly reduce the total volume mass of the solid waste, which simplify the handling process and reduce the transportation cost.
The list below states the examples of dryers available for industrial process: [23]
Gyratory screener separates solids from liquid or other dry solids according to the particle sizes. Screening is one of the crucial pre-treatment to several industries, such as chemical, food, mining, pharmaceutical, and waste. [8]
Application | Waste stream |
---|---|
Powdered detergent |
|
Citrus juice [24] |
|
Iron ore processing |
|
Antibiotic |
|
Wastewater [21] |
|
The table above presents the waste stream for several processes that are commonly use in different industries. The example given for chemical industry is the powdered detergent production where gyratory screener is used to filter out the oversized granules found in end product to improve product appearance and dissolve rate. Citrus juice production is the example of food industry. Gyratory screener available in multi-layered planes eliminates all the wastes in several stages. Juice sacs are the desirable element to produce citrus juice. Screening in food industry significantly increases the product quality. Among the ore processing, gyratory screener is used after crushing to filter out the oversized ore particles. These unfavourable particles can be regarded as waste or recycle back to the process. Similarly, in pharmaceutical industry, gyratory screener removes undissolved particles from liquid pharmaceuticals or fine powder that stick on the capsule surface to ease the capsule stamp. As for wastewater treatment, removal of coarse solid wastes from the wastewater stream is exclusively to protect the downstream equipment from damages. Fine solid waste removal acts as pre-treatment for the process, more specifically a primary clarification. The overall screening process enhances system performance, minimize the cost and reduce the need for cleaning of the filter in other equipment. [24]
The waste materials usually travel through a discharge chute for disposal depending on the design of the gyratory screener. There will be at least one outlet for every deck of gyratory screener. [25]
Filtration is a physical separation process that separates solid matter and fluid from a mixture using a filter medium that has a complex structure through which only the fluid can pass. Solid particles that cannot pass through the filter medium are described as oversize and the fluid that passes through is called the filtrate. Oversize particles may form a filter cake on top of the filter and may also block the filter lattice, preventing the fluid phase from crossing the filter, known as blinding. The size of the largest particles that can successfully pass through a filter is called the effective pore size of that filter. The separation of solid and fluid is imperfect; solids will be contaminated with some fluid and filtrate will contain fine particles. Filtration occurs both in nature and in engineered systems; there are biological, geological, and industrial forms.
Spray drying is a method of forming a dry powder from a liquid or slurry by rapidly drying with a hot gas. This is the preferred method of drying of many thermally-sensitive materials such as foods and pharmaceuticals, or materials which may require extremely consistent, fine particle size. Air is most commonly used as the heated drying medium; however, nitrogen may be used if the liquid is flammable or if the product is oxygen-sensitive.
A crusher is a machine designed to reduce large rocks into smaller rocks, gravel, sand or rock dust.
A sieve, fine mesh strainer, or sift, is a tool used for separating wanted elements from unwanted material or for controlling the particle size distribution of a sample, using a screen such as a woven mesh or net or perforated sheet material. The word sift derives from sieve.
Froth flotation is a process for selectively separating hydrophobic materials from hydrophilic. This is used in mineral processing, paper recycling and waste-water treatment industries. Historically this was first used in the mining industry, where it was one of the great enabling technologies of the 20th century. It has been described as "the single most important operation used for the recovery and upgrading of sulfide ores". The development of froth flotation has improved the recovery of valuable minerals, such as copper- and lead-bearing minerals. Along with mechanized mining, it has allowed the economic recovery of valuable metals from much lower-grade ore than previously.
Mineral processing is the process of separating commercially valuable minerals from their ores in the field of extractive metallurgy. Depending on the processes used in each instance, it is often referred to as ore dressing or ore milling.
Shale shakers are components of drilling equipment used in many industries, such as coal cleaning, mining, oil and gas drilling.They are the first phase of a solids control system on a drilling rig, and are used to remove large solids (cuttings) from the drilling fluid ("mud").
Mechanical screening, often just called screening, is the practice of taking granulated or crushed ore material and separating it into multiple grades by particle size.
Gravity separation is an industrial method of separating two components, either a suspension, or dry granular mixture where separating the components with gravity is sufficiently practical: i.e. the components of the mixture have different specific weight. Every gravitational method uses gravity as the primary force for separation. One type of gravity separator lifts the material by vacuum over an inclined vibrating screen covered deck. This results in the material being suspended in air while the heavier impurities are left behind on the screen and are discharged from the stone outlet. Gravity separation is used in a wide variety of industries, and can be most simply differentiated by the characteristics of the mixture to be separated - principally that of 'wet' i.e. - a suspension versus 'dry' -a mixture of granular product. Often other methods are applied to make the separation faster and more efficient, such as flocculation, coagulation and suction. The most notable advantages of the gravitational methods are their cost effectiveness and in some cases excellent reduction. Gravity separation is an attractive unit operation as it generally has low capital and operating costs, uses few if any chemicals that might cause environmental concerns and the recent development of new equipment enhances the range of separations possible.
The term spiral separator can refer to either a device for separating slurry components by density, or for a device for sorting particles by shape.
Sensor-based sorting, is an umbrella term for all applications in which particles are detected using a sensor technique and rejected by an amplified mechanical, hydraulic or pneumatic process.
Tumbler screening is a separation method that uses three-dimensional elliptical movement to separate very fine particles from larger ones.
A pusher centrifuge is a type of filtration technique that offers continuous operation to de-water and wash materials such as relatively in-compressible feed solids, free-draining crystalline, polymers and fibrous substances. It consists of a constant speed rotor and is fixed to one of several baskets. This assembly is applied with centrifugal force that is generated mechanically for smaller units and hydraulically for larger units to enable separation.
The peeler centrifuge is a device that performs by rotating filtration basket in an axis. A centrifuge follows on the principle of centrifugal force to separate solids from liquids by density difference. High rotation speed provides high centrifugal force that allows the suspended solid in feed to settle on the inner surface of basket. There are three kinds of centrifuge, horizontal, vertical peeler centrifuge and siphon peeler centrifuge. These classes of instrument apply to various areas such as fertilisers, pharmaceutical, plastics and food including artificial sweetener and modified starch.
A circle-throw vibrating machine is a screening machine employed in processes involving particle separation. In particle processes screening refers to separation of larger from smaller particles in a given feed, using only the materials' physical properties. Circle throw machines have simple structure with high screening efficiency and volume. However it has limitations on the types of feed that can be processed smoothly. Some characteristics of circle-throw machines, such as frequency, vibration amplitude and angle of incline deck also affect output.
A trommel screen, also known as a rotary screen, is a mechanical screening machine used to separate materials, mainly in the mineral and solid-waste processing industries. It consists of a perforated cylindrical drum that is normally elevated at an angle at the feed end. Physical size separation is achieved as the feed material spirals down the rotating drum, where the undersized material smaller than the screen apertures passes through the screen, while the oversized material exits at the other end of the drum.
Vibratory Fluidized Bed (VFB) is a type of fluidized bed where the mechanical vibration enhances the performance of fluidization process. Since the first discovery of vibratory fluidized bed, its vibration properties proves to be more efficient in dealing with fine particles which appears to be very difficult to achieve with normal fluidized bed. Even though numerous publications and its popularity in industrial applications, the knowledge about vibratory dynamics and properties are very limited. Future research and development are needed to further improve this technology to bring it to another level.
High-frequency vibrating screens are the most important screening machines primarily utilised in the mineral processing industry. They are used to separate feeds containing solid and crushed ores down to less than 200 μm in size, and are applicable to both perfectly wetted and dried feed. The frequency of the screen is mainly controlled by an electromagnetic vibrator which is mounted above and directly connected to the screening surface. Its high-frequency characteristics differentiate it from a normal vibrating screen. High-frequency vibrating screens usually operate at an inclined angle, traditionally varying between 0° and 25° and can go up to a maximum of 45°. They should operate with a low stroke and have a frequency ranging from 1500 to 9000 RPM. Frequency in High frequency screen can be fixed or variable. Variable High Frequency screen is more versatile to tackle varied material condition like particle size distribution, moisture and have higher efficiency due to incremental increase in frequency. G force plays important role in determining specific screening capacity of screen in terms of TPH per sqm. G force increases exponentially with frequency.
A conical plate centrifuge is a type of centrifuge that has a series of conical discs which provides a parallel configuration of centrifugation spaces.
Screen/Scroll centrifuge is a filtering or screen centrifuge which is also known as worm screen or conveyor discharge centrifuge. This centrifuge was first introduced in the midst of 19th century. After developing new technologies over the decades, it is now one of the widely used processes in many industries for the separation of crystalline, granular or fibrous materials from a solid-liquid mixture. Also, this process is considered to dry the solid material. This process has been some of the most frequently seen within, especially, coal preparation industry. Moreover, it can be found in other industries such as chemical, environmental, food and other mining fields.