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Cyclones

The simplest type of centrifugal device is the cyclone separator (Fig. 3.4), which consists of a vertical cylinder with a conical bottom. The centrifugal force is generated by the fluid motion. The mixture enters in a tangential inlet near the top, and the rotating motion so created develops centrifugal force which throws the particles radially toward the wall. [Pg.71]

Figure 3.4 A cyclone generates centrifugal force by the fluid motion. Figure 3.4 A cyclone generates centrifugal force by the fluid motion.
Cyclones. Cyclones are also primarily used as prefilters. These also were discussed in Chap. 3 and illustrated in Fig. 3.4. The particle-laden gas enters tangentially and spins downward and inward, ultimately leaving the top of the unit. Particles are thrown radially outward to the wall by the centrifugal force and leave at the bottom. [Pg.302]

Cyclones can be used under conditions of high particle loading. They are cheap, simple devices with low maintenance requirements. Problems occur when separating materials that have a tendency to stick to the cyclone walls. [Pg.302]

Centrifugal demister or cyclone) devices rely on high velocities to remove liquid particles and substantial pressure drops are required in cyclone design to generate these velocities. Cyclones have a limited range over which they operate efficiently this is a disadvantage if the input stream flowrate is very variable. [Pg.245]

Hydrocylones have become common on offshore facilities and rely on centrifugal force to separate light oil particles from the heavier water phase. As the inlet stream is centrifuged oil particles move to the centre of the cyclone, coalesce and are drawn off upwards, while the heavier water is taken out at the bottom. [Pg.249]

The efforts of the experts from Pivdenny have made it possible for Ukraine to become firmly established in the first three of space powers (after USA and Russia). More than 400 earth satellites developed in Pivdenny have been in space In recent years experts have developed the unique camer-rockets Zenith and Cyclone, capable of taking 4 and 14 tons into orbit, respectively. No other carrier-rockets of this type exist anywhere in the world, so they were selected for the international project Sea Start and Globalstar The NDT experts from Pivdenny have made a great contribution to these development, as practically all the parts and components of the carrier-rockets are subjected to thorough control. [Pg.970]

Almost everyone has a concept of pressure from weather reports of tlie pressure of the atmosphere around us. In this context, high pressure is a sign of good weather while very low pressures occur at the eyes of cyclones and hurricanes. In elementary discussions of mechanics, hydrostatics of fluids and the gas laws, most scientists leam to compute pressures in static systems as force per unit area, often treated as a scalar quantity. They also leam that unbalanced pressures cause fluids to flow. Winds are the flow of the atmosphere from regions of high to low... [Pg.1955]

From the tube dryer, fiber drops into a cyclone which separates the fiber from the moist, warm air. The fiber falls from the bottom of the cyclone into a large bin and in then moved to the mat forming line. If machine-blending of fiber with additives is used, it will occur at this point, immediately before the forming line. [Pg.389]

Includes cyclonic, dynamic, filtration, inertial impaction (wetted targets, packed towers, turbulent targets), spray chambers, and venturi. [Pg.386]

Fig. 2. Types of spiay towers (a) horizontal spray chamber (b) simple vertical spray tower (c) cyclonic spray tower, Pease-Anthony type (d) cyclonic spray... Fig. 2. Types of spiay towers (a) horizontal spray chamber (b) simple vertical spray tower (c) cyclonic spray tower, Pease-Anthony type (d) cyclonic spray...
Fig. 7. Cyclone generalized grade-efficiency curves. The soHd line is for the Lapple cyclone dimension ratios given in Figure 9. The dotted line is theoretical... Fig. 7. Cyclone generalized grade-efficiency curves. The soHd line is for the Lapple cyclone dimension ratios given in Figure 9. The dotted line is theoretical...
Fig. 8. Cyclone types commonly used (161) (a) conventional, large diameter, tangential inlet, axial discharge (b) smaller tube, tangential inlet, peripheral concentrated aerosol discharge (c) small tube axial inlet and discharge (d) smaller tube axial inlet, peripheral concentrated aerosol discharge. Fig. 8. Cyclone types commonly used (161) (a) conventional, large diameter, tangential inlet, axial discharge (b) smaller tube, tangential inlet, peripheral concentrated aerosol discharge (c) small tube axial inlet and discharge (d) smaller tube axial inlet, peripheral concentrated aerosol discharge.
Cyclone Efficiency. Most cyclone manufacturers provide grade-efficiency curves to predict overall collection efficiency of a dust stream in a particular cyclone. Many investigators have attempted to develop a generalized grade-efficiency curve for cyclones, eg, see (159). One problem is that a cyclone s efficiency is affected by its geometric design. Equation 15 was proposed to calculate the smallest particle size collectable in a cyclone with 100% efficiency (157). [Pg.395]

For smaller particles, the theory indicates that efficiency decreases according to the dotted line of Figure 7. Experimental data (134) (sofld line of Eig. 7) for a cyclone of Eig. 9 dimensions show that equation 15 tends to overstate collection efficiency for moderately coarse particles and understate efficiency for the finer fraction. The concept of particle cut-size, defined as the size of particle collected with 50% mass efficiency, determined by equation 16 has been proposed (134). [Pg.395]

This equation is for Eigure 9 cyclone dimension ratios. The term the effective number of spirals the gas makes in the cyclone, was found to be approximately 5 for Lapple s system (134). The soHd line grade-efficiency curve of Eigure 7 is also used with Lapple s cyclone, which is a somewhat taller, less compact cyclone than many commercial designs. [Pg.395]

Fig. 9. Dimension ratios ofLapple (134) cyclone design. From Ref. 160,... Fig. 9. Dimension ratios ofLapple (134) cyclone design. From Ref. 160,...
Table 6. Technique for Calculating Cyclone Overall Efficiency for Dust Particles ... Table 6. Technique for Calculating Cyclone Overall Efficiency for Dust Particles ...
Traditionally, cyclone dimensions are multiples of outiet pipe diameter D. Typical barrel diameters are 2D but efficiency increases at constant up to a 3Z9 barrel diameter. Efficiency also improves as barrel and cone length are increased at constant up to the natural length of the vortex. At constant inlet velocity, efficiency increases as outiet diameter (and all ratioed dimensions in a family of cyclones) is decreased. Improved efficiency is attained at the... [Pg.396]

Practically all cyclone performance data have been related to a present cyclone set of geometric ratios. One model for cyclone grade-efficiency curves has been tested against reported commercial cyclone efficiencies (159). A good fit was obtained. [Pg.397]

Cyclone Pressure Drop. Typical cyclone pressure drops range from 250 to 2000 Pa. Most data are reported for clean air flowing through the cyclone and these data are conservative for design purposes. Many investigators have unsuccessfully attempted to relate pressure drops to inlet and oudet dimension ratios. Manufacturers caUbration curves or experimental measurements on cyclones of similar dimension should be used where possible. If a rehable experimental measurement is available, however, the pressure drop at other conditions can be estimated by first evaluating the constant i in equation 17. [Pg.397]

Some empirical equations to predict cyclone pressure drop have been proposed (165,166). One (166) rehably predicts pressure drop under clean air flow for a cyclone having the API model dimensions. Somewhat surprisingly, pressure drop decreases with increasing dust loading. One reasonable explanation for this phenomenon is that dust particles approaching the cyclone wall break up the boundary layer film (much like spoiler knobs on an airplane wing) and reduce drag forces. [Pg.397]

Table 7. Dust Loadings and Cyclone Inlet Velocities above Which Erosion Is Excessive ... Table 7. Dust Loadings and Cyclone Inlet Velocities above Which Erosion Is Excessive ...
Other problems affecting cyclone efficiency are usually caused by abuse or poor maintenance. Problems may arise from temperature warpage, rough interior surfaces, overlapping plates and rough welds, or misalignment of parts, such as an uncentered (or cocked) vortex oudet in the barrel. [Pg.397]

Other Centrifugal Collectors. Cyclones and modified centrifugal collectors are often used to remove entrained Hquids from a gas stream. Cyclones for this purpose have been described (167—169). The rotary stream dust separator (170,171), a newer dry centrifugal collector with improved collection efficiency on particles down to 1—2 pm, is considered more expensive and hence has been found less attractive than cyclones unless improved collection in the 2—10-pm particle range is a necessity. A number of inertial centrifugal force devices as well as some others termed dynamic collectors have been described in the Hterature (170). [Pg.397]


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A Case Study the Effect of Cyclone Length

A Predicting the Effect of Solids Loading on Cyclone Efficiency

A Worked Example for Calculating Cyclone Pressure Drop

Air cyclones

Application to Cyclone or Swirl Tube Simulation

Atmospheric pollution cyclones

Attrition cyclone-produced

Attrition in cyclone

Axial flow cyclone

B Flow Distribution in Parallel Demisting Cyclones

B Predicting the Effect of Loading on Cyclone Pressure Drop

B Sample Cyclone Scaling Calculations

BED PARTICLE SIZE DISTRIBUTION AND CYCLONE DESIGN

Baltic cyclone

Bubble cyclones

Bulk Removal-Cyclones

CYCLONE DESIGN EXAMPLES

CYCLONE INLET AND OUTLET CONFIGURATIONS

CYCLONE® paraquat

Centrifugal separation cyclone

Centrifugal separators (cyclones)

Centrifuge cyclone separator

Circulating fluidized beds cyclones

Closed cyclones

Collection Efficiency of Cyclones

Collection cyclone condenser

Collection cyclonic separators

Collection system, cyclone

Combustion chamber, cyclone

Contents 12 Cyclone Design

Cycloketones s. Cyclones

Cycloketones s. Cyclones Ketones, cyclic

Cyclone (centrifuge

Cyclone Erosion

Cyclone Flow Pattern and Pressure Drop

Cyclone Operating Conditions

Cyclone Stairmand design

Cyclone Vortex flow pattern

Cyclone applications

Cyclone attrition

Cyclone attrition rate

Cyclone bioreactors

Cyclone boilers

Cyclone capacity

Cyclone capital cost

Cyclone cells

Cyclone classifier

Cyclone coal combustors, slag

Cyclone collector

Cyclone collector particulate removal

Cyclone collectors, pollutants

Cyclone cones

Cyclone cross-flow injection

Cyclone cut size

Cyclone design alternatives

Cyclone design factor

Cyclone design procedure

Cyclone diameter determination

Cyclone dipleg

Cyclone dryer

Cyclone dust

Cyclone dust separator particle collection efficiency

Cyclone dust separators

Cyclone dust separators collection efficiency

Cyclone dust separators configuration

Cyclone dust separators installation

Cyclone dust separators operating methods

Cyclone dust separators performance

Cyclone dust separators pressure drop

Cyclone efficiency

Cyclone geometry

Cyclone grade efficiency

Cyclone hearth

Cyclone inlet velocity

Cyclone inlets

Cyclone laminating mixer

Cyclone laminating mixing

Cyclone length

Cyclone micromixers

Cyclone mixer

Cyclone operating variables

Cyclone particle collectors

Cyclone preheater

Cyclone process description

Cyclone reaction vessel

Cyclone reactor experiments

Cyclone roof

Cyclone sampler

Cyclone scrubbers

Cyclone selection

Cyclone separations

Cyclone separators

Cyclone separators Design

Cyclone separators Hydroclones

Cyclone separators Pressure drop

Cyclone separators Scrubber

Cyclone separators calculation, example

Cyclone separators design factors

Cyclone separators dimensions

Cyclone separators inlet loading

Cyclone separators multiclones

Cyclone separators particle acceleration

Cyclone separators performance

Cyclone separators proportions

Cyclone separators solids loading

Cyclone separators theoretical particle size

Cyclone simulation

Cyclone sizing

Cyclone spray reactor

Cyclone stages

Cyclone system

Cyclone tangential injection

Cyclone train

Cyclone tube separators

Cyclone vapor-liquid separator

Cyclone, uniflow

Cyclone-Fired System

Cyclones abrasion

Cyclones blockages

Cyclones collection efficiency

Cyclones design

Cyclones design guidelines

Cyclones design, worked example

Cyclones discharge hoppers

Cyclones equation

Cyclones equipment

Cyclones flapper valve

Cyclones flow field

Cyclones gas-liquid

Cyclones geometric configuration

Cyclones in parallel

Cyclones in series

Cyclones overview

Cyclones performance

Cyclones performance curves

Cyclones phenols

Cyclones pressure drop

Cyclones principles

Cyclones reverse-flow

Cyclones reverse-flow cyclone

Cyclones scale

Cyclones schematic diagram

Cyclones separation efficiency

Cyclones separation factor

Cyclones theoretical analysis

Cyclones theory

Cyclones types

Cyclones uniform cyclone

Cyclones vortex radius

Cyclones worked example

Cyclones, atmospheric motion

Cyclones, reaction with dichlorocarbene

Cyclones/hurricanes

Cyclonic circulation regime

Cyclonic condenser

Cyclonic rotation

Cyclonic separators

Cyclonic separators, aerosol collection

Cyclonic spray chamber

Cylinder-on-Cone Cyclones with Tangential Inlet

Cyprus warm-core (anti-cyclonic) eddy

DIPLEG SIZING AND CYCLONE PRESSURE BALANCE

Deentrainment cyclone dimensions

Deentrainment cyclones

Demisting cyclones

Dense-media separation cyclone separator

Dense-phase fluidized beds cyclones

Diameter of cyclone

Dichlorocarbene cyclone reaction

Dust collection cyclone

Dust collection cyclone design factors

Dust collection cyclone efficiency

Dust collection cyclone separators

Dust separation cyclone arrangements

Dust separation cyclones

Effect on Separation Efficiency of Cyclones

Effect on the Pressure Drop of Cyclones

Efficiency cyclone separators

Efficiency of cyclones

Example 4-6 Cyclone System Pressure Drop

Flat bottom cyclones

Flow Field in a Cyclone

Flow in Cyclones

Flow-through cyclone

Fluid cracking cyclone separators

Fluidization cyclone

Foam-Breaking Cyclones

Furnace melting cyclone

Gas-Liquid Cylindrical Cyclone

Gas-Solid Contacting in Kilns, Moving Beds, and Cyclones

Gas-solid segregation cyclones

Gas-solid separation cyclones

Gas-solids separators cyclones

Gas—solid cyclones

How Cyclones Work

Hydrocyclones (liquid-cyclones)

Individual cyclones

Liquid-cyclone-processed

Liquid-cyclones

Liquid-solid cyclones

Liquid-solid particle, separators Cyclone

Mass transfer cyclone separators

Melting cyclone burner

Mini-cyclone

Modeling the Performance of Vapor-Liquid Cyclones

Multi-cyclones

Multi-inlet cyclone

North-Atlantic cyclones

Once-through cyclone

PFTR, Melting Cyclone Burner

Parallel cyclones

Particle Attrition in Cyclones

Particle collection cyclone separation

Particle removal cyclone collectors

Pressure loss, through cyclones

Reaction cyclone

Reactor cyclones

Regenerator cyclones

Reynolds number cyclones

Rhodes cold-core (cyclonic) eddy

Riser cyclone

Rotating Flow Cyclone Separator

Rough cut cyclone

Sampling cyclones

Scale-up of Cyclones

Scaling Cyclones in Practice

Scrubber wet cyclone

Scrubbers spray cyclone scrubber

Separation processes cyclones

Separation technologies/processes cyclone separators

Separation, energy requirement cyclones

Separators, gas-liquid cyclones

Series cyclones

Shape cyclone

Some Remarks on CFD in Cyclones

Some Vapor-Liquid Cyclone Design Geometries and Features

Spray chamber cyclone

Spray cyclone scrubber

Spray cyclones

Stairmand cyclones

Stokes number cyclones

Straight-through cyclone

Suspension burner, cyclonic

Suspension firing cyclone furnaces

Swirl cyclone-scrubbers

Tangential flow cyclones

Tangential inlet cyclone

Tropical cyclone

Two Main Classes—Cyclones and Swirl Tubes

Two-stage cyclones

Use of Cyclones

Venturi scrubber-cyclone

Venturi-Cyclonic spray scrubbers

Vortex (Cyclone) Reactor

Water spray cyclone scrubber

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