Knowledge (XXG)

Cyclonic separation

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spinner vanes. The secondary air flow enters from the top of the cyclone and moves downward toward the bottom, intercepting the particulate from the primary air. The secondary air flow also allows the collector to optionally be mounted horizontally, because it pushes the particulate toward the collection area, and does not rely solely on gravity to perform this function.
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stream, and thus strike the outside wall, then fall to the bottom of the cyclone where they can be removed. In a conical system, as the rotating flow moves towards the narrow end of the cyclone, the rotational radius of the stream is reduced, thus separating smaller and smaller particles. The cyclone geometry, together with
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separation of dust particulates. The pressure drop of multiple-cyclone separators collectors is higher than that of single-cyclone separators, requiring more energy to clean the same amount of air. A single-chamber cyclone separator of the same volume is more economical, but doesn't remove as much dust.
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Notice that if the density of the fluid is greater than the density of the particle, the motion is (-), toward the center of rotation and if the particle is denser than the fluid, the motion is (+), away from the center. In most cases, this solution is used as guidance in designing a separator, while
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This type of cyclone uses a secondary air flow, injected into the cyclone to accomplish several things. The secondary air flow increases the speed of the cyclonic action making the separator more efficient; it intercepts the particulate before it reaches the interior walls of the unit; and it forces
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The above equations are limited in many regards. For example, the geometry of the separator is not considered, the particles are assumed to achieve a steady state and the effect of the vortex inversion at the base of the cyclone is also ignored, all behaviours which are unlikely to be achieved in a
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An alternative cyclone design uses a secondary air flow within the cyclone to keep the collected particles from striking the walls, to protect them from abrasion. The primary air flow containing the particulates enters from the bottom of the cyclone and is forced into spiral rotation by stationary
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Multiple-cyclone separators remove more dust than single cyclone separators because the individual cyclones have a greater length and smaller diameter. The longer length provides longer residence time while the smaller diameter creates greater centrifugal force. These two factors result in better
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pattern, beginning at the top (wide end) of the cyclone and ending at the bottom (narrow) end before exiting the cyclone in a straight stream through the center of the cyclone and out the top. Larger (denser) particles in the rotating stream have too much inertia to follow the tight curve of the
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Multiple-cyclone separators consist of a number of small-diameter cyclones, operating in parallel and having a common gas inlet and outlet, as shown in the figure, and operate on the same principle as single cyclone separators—creating an outer downward vortex and an ascending inner vortex.
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of the cyclone. This is the size of particle that will be removed from the stream with a 50% efficiency. Particles larger than the cut point will be removed with a greater efficiency, and smaller particles with a lower efficiency as they separate with more difficulty or can be subject to
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More complete models exist, as many authors have studied the behaviour of cyclone separators., simplified models allowing a quick calculation of the cyclone, with some limitations, have been developed for common applications in process industries. Numerical modelling using
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Single-cyclone separators create a dual vortex to separate coarse from fine dust. The main vortex spirals downward and carries most of the coarser dust particles. The inner vortex, created near the bottom of the cyclone, spirals upward and carries finer dust particles.
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the separated particulate toward the collection area. The secondary air flow protects the separator from particulate abrasion and allows the separator to be installed horizontally because gravity is not depended upon to move the separated particulate downward.
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for separating the grease from the exhaust air in extraction hoods. Smaller cyclones are used to separate airborne particles for analysis. Some are small enough to be worn clipped to clothing, and are used to separate respirable particles for later analysis.
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Cyclone separators are found in all types of power and industrial applications, including pulp and paper plants, cement plants, steel mills, petroleum coke plants, metallurgical plants, saw mills and other kinds of facilities that process dust.
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The buoyant force component is in the inward radial direction. It is in the opposite direction to the particle's centrifugal force because it is on a volume of fluid that is missing compared to the surrounding fluid. Using
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is equal to the volume of the particle (as opposed to the velocity). Determining the outward radial motion of each particle is found by setting Newton's second law of motion equal to the sum of these forces:
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Airflow diagram for Aerodyne cyclone in horizontal position, an alternate design. Secondary air flow is injected to reduce wall abrasion, and to help move collected particulates to hopper for extraction.
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D. Benoni, C.L. Briens, T. Baron, E. Duchesne and T.M. Knowlton, 1994, "A procedure to determine particle agglomeration in a fluidized bed and its effect on entrainment", Powder Technology, 78, 33-42.
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and particle transport equations can be used to describe the behaviour of a cyclone. The air in a cyclone is initially introduced tangentially into the cyclone with an inlet velocity
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has also been used extensively in the study of cyclonic behaviour. A major limitation of any fluid mechanics model for cyclone separators is the inability to predict the
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is zero. This occurs when the radial velocity has caused enough drag force to counter the centrifugal and buoyancy forces. This simplification changes our equation to:
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Analogous devices for separating particles or solids from liquids are called hydrocyclones or hydroclones. These may be used to separate solid waste from water in
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forces. Given that the fluid velocity is moving in a spiral the gas velocity can be broken into two component velocities: a tangential component,
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This means that the established feed velocity controls the vortex rate inside the cyclone, and the velocity at an arbitrary radius is therefore:
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In non-equilibrium conditions when radial acceleration is not zero, the general equation from above must be solved. Rearranging terms we obtain
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are used to separate mixtures of solids and fluids. The method can also be used to separate fine droplets of liquid from a gaseous stream.
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Martin Huard, Cedric Briens, Franco Berruti, Thierry Gauthier, 2010, "A Review of Rapid Gas-Solid Separation Techniques", IJCRE, 8, R1.
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To simplify this, we can assume the particle under consideration has reached "terminal velocity", i.e., that its acceleration
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Airflow diagram for Aerodyne cyclone in standard vertical position. Secondary air flow is injected to reduce wall abrasion.
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If one considers an isolated particle circling in the upper cylindrical component of the cyclone at a rotational radius of
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preheaters. Cyclones are increasingly used in the household, as the core technology in bagless types of portable
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of fine particles with larger particles, which has a great impact on cyclone collection efficiency.
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Experimentally it is found that the velocity component of rotational flow is proportional to
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re-entrainment when the air vortex reverses direction to move in direction of the outlet.
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as the particle's density, the centrifugal component in the outward radial direction is:
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PhD Thesis: On the Potential of Large Eddy Simulation to Simulate Cyclone Separators
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PhD thesis: Experimental and Analytical Study of the Vortex in the Cyclone Separator
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The most common types of centrifugal, or inertial, collectors in use today are:
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Method of removing particulates from a fluid stream through vortex separation
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is distance per time, this is a 2nd order differential equation of the form
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from the cyclone's central axis, the particle is therefore subjected to
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A high-speed rotating (air)flow is established within a cylindrical or
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A partially demolished factory with dominating cyclonic separators
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As the cyclone is essentially a two phase particle-fluid system,
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PhD Thesis: Droplet collection in a scaled-up rotating separator
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separation. When removing particulate matter from liquid, a
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actual performance is evaluated and modified empirically.
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Martignoni, W. P.; Bernardo, S.; Quintani, C. L. (2007).
2153:"Cyclone design - Step by step guide - Powderprocess.net" 213:. Cyclones are also used in industrial and professional 1042:{\displaystyle m{\frac {dV_{r}}{dt}}=F_{d}+F_{c}+F_{b}} 2018:
Rust (fungus) § Management of rust fungi diseases
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from an air, gas or liquid stream, without the use of
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for the density of the fluid, the buoyant force is:
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Air flows in a 2271:High Efficiency Horizontal Dust Collection 2190: 2179:Brazilian Journal of Chemical Engineering 1929: 1923: 1891: 1882: 1873: 1860: 1854: 1824: 1811: 1805: 1781: 1775: 1745: 1724: 1707: 1686: 1680: 1645: 1640: 1634: 1621: 1611: 1605: 1585: 1572: 1567: 1557: 1547: 1537: 1517: 1507: 1505: 1470: 1457: 1439: 1434: 1428: 1417: 1412: 1406: 1396: 1387: 1381: 1357: 1351: 1321: 1306: 1301: 1295: 1289: 1284: 1267: 1258: 1243: 1238: 1232: 1226: 1221: 1204: 1195: 1182: 1167: 1135: 1122: 1109: 1103: 1069: 1059: 1057: 1033: 1020: 1007: 983: 973: 968: 943: 937: 908: 893: 888: 882: 870: 865: 852: 844: 817: 812: 806: 800: 790: 774: 768: 744: 738: 703: 698: 692: 686: 681: 671: 654: 649: 622: 617: 611: 599: 593: 569: 563: 536: 523: 501: 495: 467: 461: 440: 434: 402: 375: 369: 302:Learn how and when to remove this message 80:Learn how and when to remove this message 163: 155: 43:This article includes a list of general 2045: 197:to separate oils and gases, and in the 1954:cyclone at real operating conditions. 7: 2069:"How cyclone grease separators work" 1089:{\displaystyle {\frac {dV_{r}}{dt}}} 280:adding citations to reliable sources 2104:Introduction to particle technology 1836:{\displaystyle V_{t}\propto r^{2}.} 1760:{\displaystyle x''+c_{1}x'+c_{2}=0} 1150:{\displaystyle F_{d}+F_{c}+F_{b}=0} 221:Similar separators are used in the 49:it lacks sufficient corresponding 25: 2003:Helikon vortex separation process 185:Large scale cyclones are used in 1976: 1918:Subsequently, given a value for 252: 34: 2192:10.1590/S0104-66322007000100008 2306:Pollution control technologies 2281:alternate link to cited patent 1476: 1450: 1: 2311:Air pollution control systems 347:Secondary-air-flow separators 1960:computational fluid dynamics 327:Multiple-cyclone separators 2352: 2321:Waste treatment technology 2276:patent 2377524 (June 1945) 201:industry as components of 2127:Smith, J. L. Jr. (1959). 753:{\displaystyle \rho _{f}} 578:{\displaystyle \rho _{p}} 318:Single-cyclone separators 227:Fluid catalytic cracking 103:is a method of removing 2106:. John Wiley and Sons. 211:central vacuum cleaners 64:more precise citations. 2013:Hydrodynamic separator 1939: 1909: 1837: 1791: 1761: 1696: 1666: 1483: 1367: 1337: 1151: 1090: 1043: 953: 921: 832: 754: 721: 637: 579: 549: 477: 450: 411: 388: 387:{\displaystyle V_{in}} 335: 169: 161: 97: 1940: 1938:{\displaystyle V_{t}} 1910: 1838: 1792: 1790:{\displaystyle r^{2}} 1762: 1697: 1695:{\displaystyle V_{r}} 1667: 1484: 1368: 1366:{\displaystyle V_{r}} 1338: 1152: 1091: 1044: 954: 952:{\displaystyle V_{p}} 922: 833: 755: 722: 638: 580: 550: 478: 476:{\displaystyle V_{r}} 451: 449:{\displaystyle V_{t}} 412: 389: 334: 167: 159: 95: 2296:Solid-gas separation 1922: 1853: 1804: 1774: 1706: 1679: 1504: 1380: 1350: 1166: 1102: 1056: 967: 936: 843: 767: 737: 648: 592: 562: 494: 460: 433: 401: 368: 276:improve this section 146:volumetric flow rate 2331:Particle technology 2316:Particulate control 1650: 1577: 1444: 1422: 1311: 1294: 1248: 1231: 898: 875: 822: 708: 691: 627: 225:industry (e.g. for 215:kitchen ventilation 101:Cyclonic separation 2102:Rhodes M. (1998). 1949:Alternative models 1935: 1905: 1833: 1787: 1757: 1692: 1662: 1636: 1563: 1479: 1430: 1408: 1363: 1333: 1297: 1280: 1234: 1217: 1159:Which expands to: 1147: 1086: 1039: 949: 917: 884: 861: 828: 808: 750: 717: 694: 677: 633: 613: 575: 545: 473: 446: 407: 384: 336: 170: 162: 98: 18:Cyclonic separator 2113:978-0-471-98483-2 1900: 1654: 1627: 1579: 1545: 1532: 1448: 1426: 1404: 1315: 1275: 1252: 1212: 1084: 998: 902: 880: 826: 712: 662: 631: 410:{\displaystyle r} 312: 311: 304: 90: 89: 82: 16:(Redirected from 2343: 2326:Gas technologies 2258: 2255: 2249: 2248: 2246: 2236: 2230: 2229: 2227: 2226: 2220: 2214:. Archived from 2213: 2203: 2197: 2196: 2194: 2170: 2164: 2163: 2161: 2159: 2149: 2143: 2142: 2124: 2118: 2117: 2099: 2093: 2090: 2084: 2083: 2081: 2080: 2071:. 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Index

Cyclonic separator
references
inline citations
improve
introducing
Learn how and when to remove this message

particulates
filters
vortex
hydrocyclone
Rotational
gravity
conical
helical
volumetric flow rate


sawmills
sawdust
oil refineries
cement
kiln
vacuum cleaners
central vacuum cleaners
kitchen ventilation
oil refining
Fluid catalytic cracking
wastewater
sewage treatment

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