Cyclonic separation is a method of removing particulates from an air, gas or liquid stream, without the use of filters , through vortex separation. When removing particulate matter from liquid, a hydrocyclone is used; while from gas, a gas cyclone is used. Rotational effects and gravity 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.
72-407: A high-speed rotating (air)flow is established within a cylindrical or conical container called a cyclone. Air flows in a helical 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
144-453: A non-Newtonian fluid can leave a "hole" behind. This will gradually fill up over time—this behavior is seen in materials such as pudding, oobleck , or sand (although sand isn't strictly a fluid). Alternatively, stirring a non-Newtonian fluid can cause the viscosity to decrease, so the fluid appears "thinner" (this is seen in non-drip paints ). There are many types of non-Newtonian fluids, as they are defined to be something that fails to obey
216-402: A plane that does not contain the apex. Depending on the author, the base may be restricted to be a circle , any one-dimensional quadratic form in the plane, any closed one-dimensional figure , or any of the above plus all the enclosed points. If the enclosed points are included in the base, the cone is a solid object ; otherwise it is a two-dimensional object in three-dimensional space. In
288-498: A cube. This formula cannot be proven without using such infinitesimal arguments – unlike the 2-dimensional formulae for polyhedral area, though similar to the area of the circle – and hence admitted less rigorous proofs before the advent of calculus, with the ancient Greeks using the method of exhaustion . This is essentially the content of Hilbert's third problem – more precisely, not all polyhedral pyramids are scissors congruent (can be cut apart into finite pieces and rearranged into
360-417: 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. 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
432-399: A great impact on cyclone collection efficiency. Conical A cone is a three-dimensional geometric shape that tapers smoothly from a flat base (frequently, though not necessarily, circular) to a point called the apex or vertex . A cone is formed by a set of line segments , half-lines , or lines connecting a common point, the apex, to all of the points on a base that is in
504-409: A particular property—for example, most fluids with long molecular chains can react in a non-Newtonian manner. The constant of proportionality between the viscous stress tensor and the velocity gradient is known as the viscosity . A simple equation to describe incompressible Newtonian fluid behavior is where For a Newtonian fluid, the viscosity, by definition, depends only on temperature , not on
576-420: A quick calculation of the cyclone, with some limitations, have been developed for common applications in process industries. Numerical modelling using computational fluid dynamics 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 agglomeration of fine particles with larger particles, which has
648-410: 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 spinner vanes. The secondary air flow enters from the top of the cyclone and moves downward toward the bottom, intercepting the particulate from
720-415: A subdiscipline of fluid mechanics that deals with fluid flow —the science of liquids and gases in motion. Fluid dynamics offers a systematic structure—which underlies these practical disciplines —that embraces empirical and semi-empirical laws derived from flow measurement and used to solve practical problems. The solution to a fluid dynamics problem typically involves calculating various properties of
792-407: Is a "generatrix" or "generating line" of the lateral surface. (For the connection between this sense of the term "directrix" and the directrix of a conic section, see Dandelin spheres .) The "base radius" of a circular cone is the radius of its base; often this is simply called the radius of the cone. The aperture of a right circular cone is the maximum angle between two generatrix lines; if
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#1732791233100864-461: Is a Newtonian fluid, because it continues to display fluid properties no matter how much it is stirred or mixed. A slightly less rigorous definition is that the drag of a small object being moved slowly through the fluid is proportional to the force applied to the object. (Compare friction ). Important fluids, like water as well as most gasses, behave—to good approximation—as a Newtonian fluid under normal conditions on Earth. By contrast, stirring
936-415: Is a cone (with apex at the origin) if for every vector x in C and every nonnegative real number a , the vector ax is in C . In this context, the analogues of circular cones are not usually special; in fact one is often interested in polyhedral cones . An even more general concept is the topological cone , which is defined in arbitrary topological spaces. Fluid mechanics Fluid mechanics
1008-452: Is a subdiscipline of continuum mechanics , as illustrated in the following table. In a mechanical view, a fluid is a substance that does not support shear stress ; that is why a fluid at rest has the shape of its containing vessel. A fluid at rest has no shear stress. The assumptions inherent to a fluid mechanical treatment of a physical system can be expressed in terms of mathematical equations. Fundamentally, every fluid mechanical system
1080-452: Is an idealization , one that facilitates mathematical treatment. In fact, purely inviscid flows are only known to be realized in the case of superfluidity . Otherwise, fluids are generally viscous , a property that is often most important within a boundary layer near a solid surface, where the flow must match onto the no-slip condition at the solid. In some cases, the mathematics of a fluid mechanical system can be treated by assuming that
1152-461: Is assumed to obey: For example, the assumption that mass is conserved means that for any fixed control volume (for example, a spherical volume)—enclosed by a control surface —the rate of change of the mass contained in that volume is equal to the rate at which mass is passing through the surface from outside to inside , minus the rate at which mass is passing from inside to outside . This can be expressed as an equation in integral form over
1224-468: Is devoted to this approach. Particle image velocimetry , an experimental method for visualizing and analyzing fluid flow, also takes advantage of the highly visual nature of fluid flow. The study of fluid mechanics goes back at least to the days of ancient Greece , when Archimedes investigated fluid statics and buoyancy and formulated his famous law known now as the Archimedes' principle , which
1296-421: Is distance per time, this is a 2nd order differential equation of the form x ″ + c 1 x ′ + c 2 = 0 {\displaystyle x''+c_{1}x'+c_{2}=0} . Experimentally it is found that the velocity component of rotational flow is proportional to r 2 {\displaystyle r^{2}} , therefore: This means that
1368-406: Is found by setting Newton's second law of motion equal to the sum of these forces: To simplify this, we can assume the particle under consideration has reached "terminal velocity", i.e., that its acceleration d V r d t {\displaystyle {\frac {dV_{r}}{dt}}} is zero. This occurs when the radial velocity has caused enough drag force to counter
1440-450: Is fundamental to hydraulics , the engineering of equipment for storing, transporting and using fluids . It is also relevant to some aspects of geophysics and astrophysics (for example, in understanding plate tectonics and anomalies in the Earth's gravitational field ), to meteorology , to medicine (in the context of blood pressure ), and many other fields. Fluid dynamics is
1512-434: 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. 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
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#17327912331001584-412: Is on a volume of fluid that is missing compared to the surrounding fluid. Using ρ f {\displaystyle \rho _{f}} for the density of the fluid, the buoyant force is: In this case, V p {\displaystyle V_{p}} is equal to the volume of the particle (as opposed to the velocity). Determining the outward radial motion of each particle
1656-409: Is sometimes called a double cone . Either half of a double cone on one side of the apex is called a nappe . The axis of a cone is the straight line passing through the apex about which the base (and the whole cone) has a circular symmetry . In common usage in elementary geometry , cones are assumed to be right circular , where circular means that the base is a circle and right means that
1728-448: Is termed a non-Newtonian fluid , of which there are several types. Non-Newtonian fluids can be either plastic, Bingham plastic, pseudoplastic, dilatant, thixotropic, rheopectic, viscoelastic. In some applications, another rough broad division among fluids is made: ideal and non-ideal fluids. An ideal fluid is non-viscous and offers no resistance whatsoever to a shearing force. An ideal fluid really does not exist, but in some calculations,
1800-415: Is the angle "around" the cone, and h ∈ R {\displaystyle h\in \mathbb {R} } is the "height" along the cone. A right solid circular cone with height h {\displaystyle h} and aperture 2 θ {\displaystyle 2\theta } , whose axis is the z {\displaystyle z} coordinate axis and whose apex
1872-402: Is the branch of physics concerned with the mechanics of fluids ( liquids , gases , and plasmas ) and the forces on them. It has applications in a wide range of disciplines, including mechanical , aerospace , civil , chemical , and biomedical engineering , as well as geophysics , oceanography , meteorology , astrophysics , and biology . It can be divided into fluid statics ,
1944-475: Is the height. This can be proved by the Pythagorean theorem . The lateral surface area of a right circular cone is L S A = π r ℓ {\displaystyle LSA=\pi r\ell } where r {\displaystyle r} is the radius of the circle at the bottom of the cone and ℓ {\displaystyle \ell } is the slant height of
2016-418: Is the origin, is described parametrically as where s , t , u {\displaystyle s,t,u} range over [ 0 , θ ) {\displaystyle [0,\theta )} , [ 0 , 2 π ) {\displaystyle [0,2\pi )} , and [ 0 , h ] {\displaystyle [0,h]} , respectively. In implicit form,
2088-481: Is the surface created by the set of lines passing through a vertex and every point on a boundary (also see visual hull ). The volume V {\displaystyle V} of any conic solid is one third of the product of the area of the base A B {\displaystyle A_{B}} and the height h {\displaystyle h} In modern mathematics, this formula can easily be computed using calculus — it is, up to scaling,
2160-591: The Reynolds number is small. For more complex cases, especially those involving turbulence , such as global weather systems, aerodynamics, hydrodynamics and many more, solutions of the Navier–Stokes equations can currently only be found with the help of computers. This branch of science is called computational fluid dynamics . An inviscid fluid has no viscosity , ν = 0 {\displaystyle \nu =0} . In practice, an inviscid flow
2232-576: The cement industry as components of kiln preheaters. Cyclones are increasingly used in the household, as the core technology in bagless types of portable vacuum cleaners and central vacuum cleaners . Cyclones are also used in industrial and professional kitchen ventilation 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. Similar separators are used in
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2304-469: The dot product . In the Cartesian coordinate system , an elliptic cone is the locus of an equation of the form It is an affine image of the right-circular unit cone with equation x 2 + y 2 = z 2 . {\displaystyle x^{2}+y^{2}=z^{2}\ .} From the fact, that the affine image of a conic section is a conic section of
2376-450: The kinematic viscosity ν {\displaystyle \nu } . Occasionally, body forces , such as the gravitational force or Lorentz force are added to the equations. Solutions of the Navier–Stokes equations for a given physical problem must be sought with the help of calculus . In practical terms, only the simplest cases can be solved exactly in this way. These cases generally involve non-turbulent, steady flow in which
2448-473: The oil refining industry (e.g. for Fluid catalytic cracking ) to achieve fast separation of the catalyst particles from the reacting gases and vapors. 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 wastewater and sewage treatment . The most common types of centrifugal, or inertial, collectors in use today are: Single-cyclone separators create
2520-413: The assumption is justifiable. One example of this is the flow far from solid surfaces. In many cases, the viscous effects are concentrated near the solid boundaries (such as in boundary layers) while in regions of the flow field far away from the boundaries the viscous effects can be neglected and the fluid there is treated as it were inviscid (ideal flow). When the viscosity is neglected, the term containing
2592-461: The axis passes through the centre of the base at right angles to its plane. If the cone is right circular the intersection of a plane with the lateral surface is a conic section . In general, however, the base may be any shape and the apex may lie anywhere (though it is usually assumed that the base is bounded and therefore has finite area , and that the apex lies outside the plane of the base). Contrasted with right cones are oblique cones, in which
2664-409: The axis passes through the centre of the base non-perpendicularly. A cone with a polygonal base is called a pyramid . Depending on the context, "cone" may also mean specifically a convex cone or a projective cone . Cones can also be generalized to higher dimensions . The perimeter of the base of a cone is called the "directrix", and each of the line segments between the directrix and apex
2736-409: The behaviour of a cyclone. The air in a cyclone is initially introduced tangentially into the cyclone with an inlet velocity V i n {\displaystyle V_{in}} . Assuming that the particle is spherical, a simple analysis to calculate critical separation particle sizes can be established. If one considers an isolated particle circling in the upper cylindrical component of
2808-415: The case of a solid object, the boundary formed by these lines or partial lines is called the lateral surface ; if the lateral surface is unbounded, it is a conical surface . In the case of line segments, the cone does not extend beyond the base, while in the case of half-lines, it extends infinitely far. In the case of lines, the cone extends infinitely far in both directions from the apex, in which case it
2880-408: The centrifugal and buoyancy forces. This simplification changes our equation to: F d + F c + F b = 0 {\displaystyle F_{d}+F_{c}+F_{b}=0} Which expands to: Solving for V r {\displaystyle V_{r}} we have Notice that if the density of the fluid is greater than the density of the particle,
2952-489: The characteristic length scale of the system, but large in comparison to molecular length scale. Fluid properties can vary continuously from one volume element to another and are average values of the molecular properties. The continuum hypothesis can lead to inaccurate results in applications like supersonic speed flows, or molecular flows on nano scale. Those problems for which the continuum hypothesis fails can be solved using statistical mechanics . To determine whether or not
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3024-528: The cone. The surface area of the bottom circle of a cone is the same as for any circle, π r 2 {\displaystyle \pi r^{2}} . Thus, the total surface area of a right circular cone can be expressed as each of the following: The circular sector is obtained by unfolding the surface of one nappe of the cone: The surface of a cone can be parameterized as where θ ∈ [ 0 , 2 π ) {\displaystyle \theta \in [0,2\pi )}
3096-559: The continuum hypothesis applies, the Knudsen number , defined as the ratio of the molecular mean free path to the characteristic length scale , is evaluated. Problems with Knudsen numbers below 0.1 can be evaluated using the continuum hypothesis, but molecular approach (statistical mechanics) can be applied to find the fluid motion for larger Knudsen numbers. The Navier–Stokes equations (named after Claude-Louis Navier and George Gabriel Stokes ) are differential equations that describe
3168-442: The control volume. The continuum assumption is an idealization of continuum mechanics under which fluids can be treated as continuous , even though, on a microscopic scale, they are composed of molecules . Under the continuum assumption, macroscopic (observed/measurable) properties such as density, pressure, temperature, and bulk velocity are taken to be well-defined at "infinitesimal" volume elements—small in comparison to
3240-532: The cyclone at a rotational radius of r {\displaystyle r} from the cyclone's central axis, the particle is therefore subjected to drag , centrifugal , and buoyant forces. Given that the fluid velocity is moving in a spiral the gas velocity can be broken into two component velocities: a tangential component, V t {\displaystyle V_{t}} , and an outward radial velocity component V r {\displaystyle V_{r}} . Assuming Stokes' law ,
3312-413: 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 re-entrainment when the air vortex reverses direction to move in direction of the outlet. An alternative cyclone design uses
3384-408: The density of the gas does not change even though the speed and static pressure change. A Newtonian fluid (named after Isaac Newton ) is defined to be a fluid whose shear stress is linearly proportional to the velocity gradient in the direction perpendicular to the plane of shear. This definition means regardless of the forces acting on a fluid, it continues to flow . For example, water
3456-441: The drag force in the outward radial direction that is opposing the outward velocity on any particle in the inlet stream is: Using ρ p {\displaystyle \rho _{p}} as the particle's density, the centrifugal component in the outward radial direction is: The buoyant force component is in the inward radial direction. It is in the opposite direction to the particle's centrifugal force because it
3528-472: The established feed velocity controls the vortex rate inside the cyclone, and the velocity at an arbitrary radius is therefore: Subsequently, given a value for V t {\displaystyle V_{t}} , possibly based upon the injection angle, and a cutoff radius, a characteristic particle filtering radius can be estimated, above which particles will be removed from the gas stream. The above equations are limited in many regards. For example,
3600-472: The fluid outside of boundary layers is inviscid, and then matching its solution onto that for a thin laminar boundary layer. For fluid flow over a porous boundary, the fluid velocity can be discontinuous between the free fluid and the fluid in the porous media (this is related to the Beavers and Joseph condition). Further, it is useful at low subsonic speeds to assume that gas is incompressible —that is,
3672-673: The fluid, such as velocity , pressure , density , and temperature , as functions of space and time. It has several subdisciplines itself, including aerodynamics (the study of air and other gases in motion) and hydrodynamics (the study of liquids in motion). Fluid dynamics has a wide range of applications, including calculating forces and movements on aircraft , determining the mass flow rate of petroleum through pipelines, predicting evolving weather patterns, understanding nebulae in interstellar space and modeling explosions . Some fluid-dynamical principles are used in traffic engineering and crowd dynamics. Fluid mechanics
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#17327912331003744-501: The force balance at a given point within a fluid. For an incompressible fluid with vector velocity field u {\displaystyle \mathbf {u} } , the Navier–Stokes equations are These differential equations are the analogues for deformable materials to Newton's equations of motion for particles – the Navier–Stokes equations describe changes in momentum ( force ) in response to pressure p {\displaystyle p} and viscosity, parameterized by
3816-410: The forces acting upon it. If the fluid is incompressible the equation governing the viscous stress (in Cartesian coordinates ) is where If the fluid is not incompressible the general form for the viscous stress in a Newtonian fluid is where κ {\displaystyle \kappa } is the second viscosity coefficient (or bulk viscosity). If a fluid does not obey this relation, it
3888-444: The formula for volume becomes The slant height of a right circular cone is the distance from any point on the circle of its base to the apex via a line segment along the surface of the cone. It is given by r 2 + h 2 {\displaystyle {\sqrt {r^{2}+h^{2}}}} , where r {\displaystyle r} is the radius of the base and h {\displaystyle h}
3960-439: The generatrix makes an angle θ to the axis, the aperture is 2 θ . In optics , the angle θ is called the half-angle of the cone, to distinguish it from the aperture. A cone with a region including its apex cut off by a plane is called a truncated cone ; if the truncation plane is parallel to the cone's base, it is called a frustum . An elliptical cone is a cone with an elliptical base. A generalized cone
4032-399: 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 cyclone at real operating conditions. More complete models exist, as many authors have studied the behaviour of cyclone separators., simplified models allowing
4104-404: The integral ∫ x 2 d x = 1 3 x 3 {\displaystyle \int x^{2}\,dx={\tfrac {1}{3}}x^{3}} Without using calculus, the formula can be proven by comparing the cone to a pyramid and applying Cavalieri's principle – specifically, comparing the cone to a (vertically scaled) right square pyramid, which forms one third of
4176-417: The limit as the apex goes to infinity, one obtains a cylinder, the angle of the side increasing as arctan , in the limit forming a right angle . This is useful in the definition of degenerate conics , which require considering the cylindrical conics . According to G. B. Halsted , a cone is generated similarly to a Steiner conic only with a projectivity and axial pencils (not in perspective) rather than
4248-534: 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 actual performance is evaluated and modified empirically. In non-equilibrium conditions when radial acceleration is not zero, the general equation from above must be solved. Rearranging terms we obtain Since V r {\displaystyle V_{r}}
4320-427: The other), and thus volume cannot be computed purely by using a decomposition argument. The center of mass of a conic solid of uniform density lies one-quarter of the way from the center of the base to the vertex, on the straight line joining the two. For a circular cone with radius r and height h , the base is a circle of area π r 2 {\displaystyle \pi r^{2}} and so
4392-482: The particulate before it reaches the interior walls of the unit; and it forces 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. As the cyclone is essentially a two phase particle-fluid system, fluid mechanics and particle transport equations can be used to describe
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#17327912331004464-641: 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. 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. Large scale cyclones are used in sawmills to remove sawdust from extracted air. Cyclones are also used in oil refineries to separate oils and gases, and in
4536-508: The projective ranges used for the Steiner conic: "If two copunctual non-costraight axial pencils are projective but not perspective, the meets of correlated planes form a 'conic surface of the second order', or 'cone'." The definition of a cone may be extended to higher dimensions; see convex cone . In this case, one says that a convex set C in the real vector space R n {\displaystyle \mathbb {R} ^{n}}
4608-505: The same principle as single cyclone separators—creating an outer downward vortex and an ascending inner vortex. 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 separation of dust particulates. The pressure drop of multiple-cyclone separators collectors
4680-586: The same solid is defined by the inequalities where More generally, a right circular cone with vertex at the origin, axis parallel to the vector d {\displaystyle d} , and aperture 2 θ {\displaystyle 2\theta } , is given by the implicit vector equation F ( u ) = 0 {\displaystyle F(u)=0} where where u = ( x , y , z ) {\displaystyle u=(x,y,z)} , and u ⋅ d {\displaystyle u\cdot d} denotes
4752-411: The same type (ellipse, parabola,...), one gets: Obviously, any right circular cone contains circles. This is also true, but less obvious, in the general case (see circular section ). The intersection of an elliptic cone with a concentric sphere is a spherical conic . In projective geometry , a cylinder is simply a cone whose apex is at infinity. Intuitively, if one keeps the base fixed and takes
4824-622: The study of fluids at rest; and fluid dynamics , the study of the effect of forces on fluid motion. It is a branch of continuum mechanics , a subject which models matter without using the information that it is made out of atoms; that is, it models matter from a macroscopic viewpoint rather than from microscopic . Fluid mechanics, especially fluid dynamics, is an active field of research, typically mathematically complex. Many problems are partly or wholly unsolved and are best addressed by numerical methods , typically using computers. A modern discipline, called computational fluid dynamics (CFD),
4896-426: The study of the conditions under which fluids are at rest in stable equilibrium ; and is contrasted with fluid dynamics , the study of fluids in motion. Hydrostatics offers physical explanations for many phenomena of everyday life, such as why atmospheric pressure changes with altitude , why wood and oil float on water, and why the surface of water is always level whatever the shape of its container. Hydrostatics
4968-399: The tight curve of the 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 volumetric flow rate , defines the cut point of
5040-500: Was continued by Daniel Bernoulli with the introduction of mathematical fluid dynamics in Hydrodynamica (1739). Inviscid flow was further analyzed by various mathematicians ( Jean le Rond d'Alembert , Joseph Louis Lagrange , Pierre-Simon Laplace , Siméon Denis Poisson ) and viscous flow was explored by a multitude of engineers including Jean Léonard Marie Poiseuille and Gotthilf Hagen . Further mathematical justification
5112-518: Was provided by Claude-Louis Navier and George Gabriel Stokes in the Navier–Stokes equations , and boundary layers were investigated ( Ludwig Prandtl , Theodore von Kármán ), while various scientists such as Osborne Reynolds , Andrey Kolmogorov , and Geoffrey Ingram Taylor advanced the understanding of fluid viscosity and turbulence . Fluid statics or hydrostatics is the branch of fluid mechanics that studies fluids at rest. It embraces
5184-516: Was published in his work On Floating Bodies —generally considered to be the first major work on fluid mechanics. Iranian scholar Abu Rayhan Biruni and later Al-Khazini applied experimental scientific methods to fluid mechanics. Rapid advancement in fluid mechanics began with Leonardo da Vinci (observations and experiments), Evangelista Torricelli (invented the barometer ), Isaac Newton (investigated viscosity ) and Blaise Pascal (researched hydrostatics , formulated Pascal's law ), and
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