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7/29/2019 Equipments Regarding Absorption
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EQUIPMENTS REGARDING ABSORPTIONAbsorption, or gas absorption, is a unit operation used in the chemical industry
to separate gases by washing or scrubbing a gas mixture with a suitable liquid. The
fundamental physical principles underlying the process of gas absorption are the
solubility of the absorbed gas and the rate of mass transfer. One or more of theconstituents of the gas mixture dissolves or is absorbed in the liquid and can thus be
removed from the mixture. In some systems, this gaseous constituent forms a physical
solution with the liquid or the solvent, and in other cases , it reacts with the liquid
chemically.
The purpose of such scrubbing operations may be any of the following: gas
purification (eg, removal of air pollutants from exhausts gases or contaminants from
gases that will be further processed), product recovery, or production of solutions of
gases for various purposes.
Gas absorption is usually carried out in vertical counter current columns. The
solvent is fed at the top of the absorber; whereas the gas mixture enters from the
bottom .The absorbed substance is washed out by the solvent and leaves the absorber
at the bottom as a liquid solution. The solvent is often recovered in a subsequent
stripping or desorption operation. This second step is essentially the reverse of
absorption and involves counter current contacting of the liquid loaded with solute
using and inert gas or water vapor.
The absorber may be a packed column, plate column, spray column, venturi
scrubbers, bubble column, falling films, wet scrubbers, or stirred tanks.
PACKED COLUMN
The packed column is a shell either filled with
randomly packed elements or having a regular solid structuredesigned to disperse the liquid and bring it Dumped-type
packing elements come in a great variety of shapes and
construction materials, which are intended to create a large
internal surface but a small pressure drop. Structured ,or
arranged packings may be made of corrugated metal or
plastic sheets providing a large number of regularly arranged
channels ,but a variety of other geometries exists.
Packing materials may be classified as follows:
rock 3-coke 4-stonaware shapes 4a-raching rings 4b-berl saddle 4c-sprial rings 1-wood slats 2-broken 4d-grid bloks 5-miscalloneous material
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Rashing rings are the most widely used form of tower packing. They are cylindrical
rings, of the some length as the diameter of the cylinder and with the walls as thin as
the material will permit. Rashing rings are almost always dumped into the tower at
random and not stacked regularly. They offer the best combination of low weight per
unit volume, free volume, free cross section and total surface of any type of packing.
A packed bed column contains a support plate, a liquid distributor, and a misteliminator. Mist eliminators are used to condense any vaporized scrubbing liquid.
Support plates hold the packing in place.
The advantages of packed columns include simple and, as long as the tower
diameter is not too large, usually relatively cheaper construction. These columns are
preferred for corrosive gases because packing, but not plates, can be made from
ceramic or plastic materials. Packed columns are also used in vacuum applications
because the pressure drop, especially for regularly structured packings, is usually less
then through plate columns.
Packed columns are used mostly in air pollution control, for instance, the water
soluble ethylene gas is hydrolyzed to ethylene glycol.Packed columns are also used in the chemical, petrochemical, food, pharmaceutical,
paper, and aerospace industries.
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TRAY COLUMN
Tray absorbers are used in applications
where tall columns are required, because tall,
random-type packed towers are subject to
channeling and misdistribution of the liquid
streams. Plate towers can be more easilycleaned. Plates are also preferred in
applications having large heat effects since
cooling coils are more easily installed in plate
towers and liquid can be withdrawn more
easily from plates than from packings for
external cooling. Tray columns have got some
disadvantage. These are slow reaction rate
processes, higher pressure drops than packed
beds and plugging and fouling may be occur.
Tray absorbers are used in applications
where tall columns are required, because tall,
random-type packed towers are subject to
channeling and misdistribution of the liquid
streams. Plate towers can be more easily
cleaned. Plates are also preferred in
applications having large heat effects since
cooling coils are more easily installed in plate
towers and liquid can be withdrawn more
easily from plates than from packings for
external cooling.Tray columns are used in a refinery dehexanizer to decrease the benzene content in
the naphtha feed to the process. This result in lower automobile exhaust emissions.
STIRRED TANKS
If the absorbtion process includes a slow
liquid-phase chemical reaction, or close control
of the process is needed, stirred tanks are
used.the gas is introduced directly into the liquid
and mixed by the stirred in a stirred tank.
Stirred tanks can be used in lime slurrycarbonation, paper stock chlorication, regular oil
hydrogenation, fermentation broth aeration,
penicilin production, citric acid production,and
aeration of activated sludge.
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BUBBLE COLUMN
Structured catalytic bubble columns are new, very promising types of multiphase
reactors. Their configuration lies basically between slurry reactors and trickle bed
reactors. The solid phase, consisting of catalyst particles, is enclosed in fixed wire gauze
wraps, which are mounted along the height of the column. The gas phase is dispersed
into the liquid phase and it flows in the empty passages between adjacent envelopes.The liquid phase may be operated in a batch manner or it may also circulate in co-
current or counter-current manner to the gas flow.
The main advantages of this reactor type with respect with the conventional
slurry bubble column are:
1. no problems for separating catalyst from the liquid;2. improved conversion and selectivity due to staging of the liquid phase;3. no scale up problems because the hydrodynamics is dictated by the size
of the open channels of the catalytic structure.
Bubble columns can be used to purify
nitroglycerin with water, in the chemical industry for
hydrogenation, oxidation, chlorination, and
alkylation, and in the biotechnological field for
effluent treatment, single-cell protein productin,
animal cell culture, and antibiotic fermentation.
Bubble columns can be used for radioactive elements
because there are no moving parts.
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VENTURI SCRUBBERS
Adjustable-throat venturi scrubber with movable plate
Venturi scrubbers can be used for removing gaseous pollutants; however, they
are not used when removal of gaseous pollutants is the only concern. The high inlet gas
velocities in a venturi scrubber result in a very short contact time between the liquid
and gas phases. This short contact time limits gas absorption. However, becauseventuris have a relatively open design compared to other scrubbers, they are very useful
for simultaneous gaseous and particulate pollutant removal, especially when:
Scaling could be a problem A high concentration of dust is in the inlet stream The dust is sticky or has a tendency to plug openings The gaseous contaminant is very soluble or chemically reactive with the liquidTo maximize the absorption of gases, venturis
are designed to operate at a different set of
conditions from those used to collect particles.
The gas velocities are lower and the liquid-to-gas
ratios are higher for absorption.
For a given venturi design, if the gas velocity is
decreased, then the pressure drop (resistance to
flow) will also decrease and vice versa. Therefore,
by reducing pressure drop, the gas velocity is
decreased and the corresponding residence time
is increased. Liquid-to-gas ratios for these gas
absorption applications are approximately 2.7 to
5.3 l/m3
(20 to 40 gal/1000 ft3). The reduction in
gas velocity allows for a longer contact timebetween phases and better absorption.
Increasing the liquid-to-gas ratio will increase
the potential solubility of the pollutant in the
liquid.
FOLDED ELBOW
Venturi scrubbers can have the highest
particle collection efficiencies (especially for very
small particles) of any wet scrubbing system.They are the most widely used scrubbers
because their open construction enables them to
remove most particles without plugging or scaling.
Venturis can also be used to absorb pollutant gases;
however, they are not as efficient for this as are
packed or plate towers.
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Venturi scrubbers have been designed to collect particles at very high collection
efficiencies, sometimes exceeding 99%. The ability of venturis to handle large inlet
volumes at high temperatures makes them very attractive to many industries;
consequently, they are used to reduce particulate emissions in a number of industrial
applications.
This ability is particularly desirable for cement kiln emission reduction and forcontrol of emissions from basic oxygen furnaces in the steel industry, where the inlet
gas enters the scrubber at temperatures greater than 350 C (660 F).
Venturis are also used to control fly ash and sulfur dioxide emissions from industrial
and utility boilers.
FALLING FILM
With high efficiency in absorbing HCl (hydrochloric) gas, H2S, HF, SO2, NH3 gas,
graphite falling film absorbers comprise of absorption liquid distributor, cooling and
absorption section and Gas-Liquid separator.
Absorption liquid distributor is for film forming and flow into absorption tube in
cooling and absorption section.
On request, cooling and absorption section has two models basis of its heat transfer
unit -Shell and Tube and Block. Gas-Liquid separator is to separate tail gas and product.
Its convincing advantages and disadvantages are the following:
Advantages: High efficiency of absorption drop Low outlet temperature; No need after-
cooling; Low flow resistance; Easy maintenance
Disadvantages: High efficiency of absorption drop; Low outlet temperature; No need
after-cooling; Low flow resistance; Easy maintenance
SPRAY COLUMNSpray columns are differential contactors. The liquid
stream enters the column through one or more spray nozzles
at different heights in the column. The droplets formed
provide a large surface area for exposure to the gas stream,
with smaller droplets resulting in a greater Exchange area.
The liquid and gas streams can flow counter-currently or in
parallel. An optimum droplet velocity is essential because low
velocity will lead to low contact or turbulence and high
velocity may cause flooding.
A mist eliminator is used to separate any liquid that isentrained into the gaseous phase. Spray columns are used to
absorb SO2 from coal-fired boiler exhaust gases.
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WET SCRUBBERS
Wetted packed towers are the simplest and most
commonly used approaches to gas scrubbing. The principle of
this type of scrubber is to remove contaminants from the gas
stream by passing the stream through a packed structure
which provides a large wetted surface area to induce intimatecontact between the gas and the scrubbing liquor. the
contaminant is absorbed into or reacted with the scrubbing
liquor.
The packing of the tower is normally a proprietary loose fill
random packing designed to encourage dispersion of the liquid
flow without tracking, to provide maximum contact area for
the 'mass transfer' interaction and to offer minimal back
pressure to the gas flow. The reactivity between the
contaminant and the scrubbing liquor influences the system
designer's determination of gas and liquor flow and the height and diameter of the
packed bed.
A demister is fitted at the top of the
tower to prevent entrainment of droplets
of the scrubbing liquor into the extraction
system or stack.
Wetted packed towers can be designed
for very high efficiencies with relatively low
capital and running costs. The low pressure
drop associated with packed bed scrubbers
permits the use of smaller more
economical fans. Although efficiency maybe affected, a packed tower will usually
function when gas or liquor flows vary
from its original design parameters.
Wet scrubbers are used by the food
industry, such as in cheese proessing for
dust and ambient moisture removal.