Particulate Emission Control by Mechanical Separation & Wet Gas Scrubbing | Environmental Engineering - Civil Engineering (CE) PDF Download

PARTICULATE EMISSION CONTROL BY MECHANICAL SEPARATION

The basic mechanism of removing particulate matter from gas stream is classified as: 1) gravitational settling 2) centrifugal impaction 3) inertial impaction 4) direct interception 5) diffusion and 6) electrostatic precipitation.
 Equipment presently available, which make use of one or more of the above mechanisms, fall into the following five broad categories: 1) gravitational settling chambers 2) cyclone separators 3) fabric filters 4) electrostatic precipitator  

[A] Gravitational Settling Chambers 

Gravitational settling chambers are generally used to remove large, abrasive particles (usually >50 µm) from gas stream. It provides enlarged areas to minimize horizontal velocities and allow time for the vertical velocity to carry the particle to the floor. The usual velocity through settling chambers is between 0.5 to 2.5 m/s. 

Figure 2.2.1: Gravitation settling chamber

Advantage: Low pressure loss, simplicity of design and maintenance. 

Disadvantage: Requires larger space and efficiency is low. Only larger sized particles are separated out. 

Design of a gravitational settling chamber

If we assume that Stokes law applies we can derive a formula for calculating the minimum diameter of a particle collected at 100% theoretical efficiency in a chamber of length L. 

  (2.2.1)  

Where v_t=terminal settling velocity, m/s 

(2.2.2)  
   Where, g=gravitational constant, m/s²; ρ_p=density of particle, kg/m³; ρ_a=density air, kg/m³; d_p=diameter of particle, m; µ_a=viscosity of air, kg/m s; H=height of settling chamber, m; v_h=horizontal flow-through velocity, m/s; and L=length of settling chamber, m. 

Solving for d_p gives an equation that predicts the largest-size particle that can be removed with 100% efficiency from a settling chamber of given dimension. 

(2.2.3)  
 All particles larger than d_p will also be removed with 100% efficiency, while the efficiency for smaller particles is the ratio of their settling velocities to the settling velocity of the d_p particle. 

[B] Cyclone Separators

A cyclone separator consists of a cylindrical shell, conical base, dust hopper and an inlet where the dust-laden gas enters tangentially. Under the influence of the centrifugal force generated by the spinning gas, the solid particles are thrown to the wall of the cyclone as the gas spirals upward at the inside of the cone. The particles slide down the walls of the cone and into the hopper. The operating efficiency of a cyclone depends on the magnitude of the centrifugal force exerted on the particles. The greater the centrifugal force, the greater the spreading efficiency. The magnitude of the centrifugal force generated depends on particle mass, gas velocity within the cyclone, and cyclone diameter.  

         (2.2.4) 
 Where, F_c=centrifugal force, N; M_p=particulate mass, Kg; V_i equals particle velocity and R equals radius of the cyclone, m/s. From this equation, it can be seen that the centrifugal force on the particles, and thus the collection efficiency of the cyclone collector can be increased by decreasing R. Large-diameter cyclone have good collection efficiencies for particles 40 to 50 µm in diameter.  

Advantage: Relatively inexpensive, simple to design and maintain; requires less floor area; low to moderate pressure loss. 

Disadvantage: Requires much head room; collection efficiency is low for smaller particles, quite sensitive to variable dust loading and flow rates. 

[C] Fabric Filters

In a fabric filter system, the particulate-laden gas stream passes through a woven or felted fabric that filters out the particulate matter and allows the gas to pass through. Small particles are initially retained on the fabric by direct interception, inertial impaction, diffusion, electrostatic attraction, and gravitational settling. After a dust mat has formed on the fabric, more efficient collection of submicron particle is accomplished by sieving. Filter bags usually tubular or envelope-shaped, are capable of removing most particles as small as 0.5µm and will remove substantial quantity of particles as small as 0.1µm. Filter bags ranging from 1.8 to 9 m long, can be utilized in a bag house filter arrangement.  As particulates build up on the inside surface of the bags, the pressure drop increases. Before the pressure drop becomes too severe, the bag must be relieved of some of the particulate layer. Fabric filter can be cleaned intermittently, periodically, or continuously.  

Fabric and Fibre Characteristics: Fabric filter may be classified according to filtering media: woven fabric or felt cloth. Woven fabrics have a definite long range repeating pattern and have considerable porosity in the direction of gas flow. These open spaces must be bridged by impaction of interception to form a true filtering surface. Felted cloth consists of randomly oriented fibres, compressed into a mat and needled to some loosely woven backing material to improve mechanical strength. The choice of fabric fibre is based primarily on operating temperature and the corrosiveness or abrasiveness of the particle. Cotton is the least expensive fibre, and is preferably used in low temperature dust collection service. Silicon coated glass fibre cloth is commonly employed in high temperature applications. The glass fibre must be lubricated to prevent abrasion. All fibre may be applied to the manufacture of woven and felt type fabrics. 

Fabric Filter System: Fabric filter systems typically consist of a tubular bag or an envelope, suspended or mounted in such manner that the collected particles fall into hopper when dislodged from fabric. The structure in which the bags are hanged is known as a bag-house.

Generally, particle laden gas enters the bag at the bottom and passes through the fabric while the particles are deposited on the inside of the bag. The cleaning is accomplished by shaking at fixed intervals of time .  

Figure 2.2.2: Typical bag-house

Advantage: Fabric filters can give high efficiency, and can even remove very small particles in dry state.

Disadvantage: High temperature gasses need to be cooled. The flue gasses must be dry to avoid condensation and clogging. The fabric is liable to chemical attacks. 

[D] Electrostatic Precipitator

The electrostatic precipitator is one of the most widely used device for controlling particulate emission at industrial installations ranging from power plants, cement and paper mills to oil refineries. Electrostatic precipitator is a physical process by which particles suspended in gas stream are charged electrically and, under the influence of the electrical field, separated from the gas stream. 

The precipitator system consists of a positively charged collecting surface and a high voltage discharge electrode wire suspended from an insulator at the top and held in passion by weight t the bottom. At a very high DC voltage, of the order of 50kV, a corona discharge occurs close to the negative electrode, setting up an electric field between the emitted and the grounded surface .  
 The particle laden gas enters near the bottom and flows upward. The gas close to the negative electrode is, thus, ionized upon passing through the corona. As the negative ions and electrons migrate toward the grounded surface, they in turn charge the passing particles. The electrostatic field then draws the particles to the collector surface where they are deposited. Periodically, the collected particles must be removed from the collecting surface. This is done by rapping or vibrating the collector to dislodge the particles. The dislodged particles drop below the electrical treatment zone and are collected for ultimate disposal . 

Advantage:  

• Maintenance is nominal, useless corrosive and adhesive materials are present in flue gases.  
•  They contain few moving parts.  
• They can be operated at high temperature up to 300^oC-450^oC. 

Disadvantage: 

• Higher initial cost.  
• Sensitive to variable dust loading and flow rates.  
• They use high voltage, and hence may pose risk to personal safety of the staff. 
• Collection efficiency reduces with time. 

PARTICULATE EMISSION CONTROL BY WET GAS SCRUBBING

Wet scrubber removes particulate matter from gas streams by incorporating the particles into liquid droplets directly on contact. The basic function of wet scrubber is to provide contact between the scrubbing liquid, usually water and, the particulate to be collected. This contact can be achieved in a variety of ways as the particles are confronted with so-called impaction target, which can be wetted surface as in packed scrubbers or individual droplets as in spray scrubbers . 

The basic collection mechanism is the same as in filters: inertial impaction, interception and diffusion. Generally, impaction and interception are the predominant mechanism for particles of diameter above 3 µm, and for particle of diameter below 0.3µm diffusion begins to prevail. There are many scrubber designs presently available where the contact between the scrubbing liquid and the particles is achieved in a variety of ways. The major types are: plate scrubber, packed-bed scrubber, spray scrubber, venturi scrubber, cyclone scrubber, baffle scrubber, impingement-entrainment scrubber, fluidized-bed scrubber. 

[A] Plate scrubber

It contains a vertical tower containing one or more horizontal plates (trays). Gas enters the bottom of the tower and must pass through perforations in each plate as it flows countercurrent to the descending water stream. Collection efficiency increases as the diameter of the perforations decreases. A cut diameter, that collected with 50% efficiency, of about  µm aerodynamic diameter can be achieved with 3.2-mm-diameter holes in a sieve plate. 

[B] Packed –bed scrubber 

Operates similarly to packed-bed gas absorber. Collection efficiency increases as packing size decreases. A cut diameter of 1.5 µm aerodynamic diameter can be attained in columns packed with 2.5 cm elements. 

Figure 2.4.1: Packed–bed scrubber

[C] Spray scrubber 

Particles are collected by liquid drops that have been atomized by spray nozzles. Horizontal and vertical gas flows are used, as well as spray introduced co-current, countercurrent, or cross-flow to the gas.  Collection efficiency depends on droplet size, gas velocity, liquid/gas ratio, and droplet trajectories. For droplets falling at their terminal velocity, the optimum droplet diameter for fineparticle collection lies in the range 100 to 500 µm.  Gravitational settling scrubbers can achieve cut diameters of about 2.0 µm. The liquid/gas ratio is in the range 0.001 to 0.01 m³/ m³ of gas treated. 

[D] Venturi scrubber

A moving gas stream is used to atomize liquids into droplets. High gas velocities (60 to 120 m/s) lead to high relative velocities between gas and particles and promote collection.  

[E] Cyclone scrubber

Drops can be introduced into the gas stream of a cyclone to collect particles. The spray can be directed outward from a central manifold or inward from the collector wall. 

[F] Impingement-

Entrainment Scrubber: The gas is forced to impinge on a liquid surface to reach a gas exit. Some of the liquid atomizes into drops that are entrained by the gas. The gas exit is designed so as to minimize the loss of entrained droplets. 

[G] Fluidized-bed scrubber

A zone of fluidized packing is provided where gas and liquid can mix intimately. Gas passes upward through the packing, while liquid is sprayed up from the bottom and/or flows down over the top of the fluidized layer of packing .