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Chapter 5
INORGANIC AND FINE
CHEMICALS
Contents
Sulfuric Acid
The Chlor-Alkali Industry
Cement Industry
Glass Industry
Fertilizer
Sulfuric Acid
Largest tonnage
Raw material is sulfur
Sources:
Direct mining of underground deposits
Desulfurization of oil and gas (off-gases containing H2S
or SO2)
By-product of metal extraction (copper process, ore
such CuFeS2)
Produced in various strengths
Sulfuric Acid Manufacturing Process
Three major steps in sulfuric acid manufacturing:
1. Burning of sulfur in air:
S + O2 SO2
2. Reaction of SO2 and O2:
2 SO2+ O2 2SO3
3. Absorption of SO3 into water to produce a sulfuric
acid (H2SO4)
Oxidation of Sulfur 1) S + O2 SO2
Air
93% H2SO4
Sulfur
10-12% SO2
Steam
Water
Primary Generation of SO2
-79% Combustion of Sulfur
-9% Recovery from Metallurgic Processes
- 5% Regeneration of Spent Acids
Process:
- Air drying tower with acid
- Air and sulfur are injected into burner
- Reaction temperature 2000°F
- Exothermic reaction must be cooled
- Steam is produced from recovered heat
Oxidation of Sulfur
molten
Oxidation of Sulfur Dioxide SO2 + ½ O2 SO3
Because of the large effect temperature plays on the reaction, multiple catalyst
layers are used (vanadium pentoxide catalyst), with cooling between each step.
As the partial pressure of SO3 increases, further reaction is limited. This is
overcomed by removing the SO3 after the third stage to drive the reaction to
completion.
Gas
Cooling
SO3 Gas
SO3 Gas
SO2 Gas
93% H2SO4
SO2 Gas
Oxidation of Sulfur Dioxide
Oleum
Air
Oxidation of Sulfur Dioxide
• Kinetic Effects
- Oxidation of sulfur dioxide is slow and reversible
- The reaction requires a catalyst and 426.7°C temperatures
-The reaction is exothermic and sensitive to excessive heat
• Equilibrium Constant (The degree at which the reaction proceeds is temp. dependent)
log Kp = 4.956 - 4.678
T
T = absolute temp. in kelvin
Kp = equilibrium constant as a function of partial pressure of gases
Kp = ( PSO3 )
PSO2 PO2
0.5
Absorption of SO3
Sulfuric acid is obtained from the absorption of SO3 and water into
H2SO4 (with a concentration of at least 98%).
The efficiency of the absorption step is related to:-
– The H2SO4 concentration of the absorbing liquid (98.5-99.5%)
– The range of temperature of the liquid (normally 70°C-120°C)
– The technique of the distribution of acid
Dilution of absorber acids The acid produced, normally 95.5%-96.5% or 98.5%-99.5%, is diluted
with water or steam condensate down to the commercial concentrations:
25%, 37%, 48%, 78%, 96% and 98% H2SO4.
The dilution can be made in a batch process or continuously through
in-line mixing.
Sulfuric Acid Contact Process
Oxidation of SO2 is thermodynamically favored by
low temperatures
All SO2 must be converted for environmental
reasons
Catalytic oxidation in adiabatic fixed bed reactors
Multiple catalyst beds with intermediate cooling
Heat from combustion of sulfur is recovered as HP
steam
Sulfuric Acid Contact Process
water
Oleum Production
Oleum is produced in the contact process, where sulfur is oxidized to
sulfur trioxide which is subsequently dissolved in concentrated sulfuric
acid. Sulfuric acid itself is regenerated by dilution of part of the oleum.
20% Oleum contains 20% SO3 by weight in the oleum
Common strengths of oleum are 20, 30, 40, 65 percent.
To produce 20 and 30 percent oleum, only requires an additional
absorption tower.
Oleum is used in reactions where water is excluded
SO3 + H2SO4 H2S2O7 (disulfuric acid)
Oleum Production
Uses of H2SO4
Manufacture of phosphoric acid for fertilizer
Production of ammonium sulfate
Production of ethanol from ethylene
One method of producing TiO2
Production of hydrofluoric acid from calcium
fluoride
Aluminum sulfate
15
The Chlor-Alkali Industry
The Chlor-Alkali Industry
Sodium hydroxide, sodium carbonate, and chlorine are substances
produced on a large scale by the chemical industry.
The term CHLOR-ALKALI PROCESS refers to the industrial
production of (alkali sodium hydroxide, NaOH, and chlorine, Cl2 from
the common salt (sodium chloride, NaCl).
The importance of these chemicals, produced in the millions of tons
annually, is illustrated by the table next slide. However, this part includes:
1. NaOH (Caustic Soda)
2. Chlorine
3. HCl
4. Sodium Hypochlorite (NaOCl)
Uses for NaOH, NaOCl, Na2CO3 and Cl2
NaOH Na2CO3 Cl2
Manufacture of
Soap
Ceramics
Numerous organic chemicals
Various sodium salts
NaOCl
Manufacture of
dairies
Paper and laundries as a bleaching agent
Manufacture of
Paper
Glass
Various sodium salts
Manufacture of:
Plastics
Paper industry
Insecticides
Hydrochloric acid
Numerous organic chemicals
Used for:
Bleaching
Water purification
18
Electrolysis of sodium chloride:
Sodium hydroxide and chlorine are produced industrially by the electrolysis
of brine, which is a near-saturated solution of sodium chloride, NaCl. The
reactions involved are
When a current is passed through brine (an aqueous solution of sodium
chloride), hydrogen gas is produced at the cathode, since H+ ions are more
easily discharged than Na+ ions. The depletion of H+ ions near the cathode
means that hydroxide(OH-) ions, as sodium hydroxide, accumulate in the
cathode compartment. Chlorine gas is produced at the anode. Three
processes are used, 1- the MEMBRANE CELL,
2- the DIAPHRAGM CELL,
3- the MERCURY PROCESS.
20
Sulphate Removal
Demin. Water
Chlorine Packing, Filling
Vaporization
Hypo Product
Chlorine Storage
Brine Saturation
Primary Treatment
Secondary Treatment
Brine Dechlorination
Electrolysis
Salt
DC Rectification
AC Power Supply
Demineralized Water
Hydrogen Handling
Caustic Storage
Chlorine Compression
Chlorine Drying
HCl Storage
Chlorine Liquefaction
Caustic Product
HCl Product
Hypo Production
Hypo Destruction
Chlorine Product
Sodium Sulphite
Chlorate Destruction
Hypo Storage
HCl Production
Caustic Concentration
Sulphuric Acid Carbon Dioxide
To Hypo HCl
HCl
Sulphuric Acid
NaOH
NaOH
Electrolysis
Types of Electrolytic Cells
Three important types of cells are employed:
Mercury
Diaphragm
Membrane
Mercury Cells1/4
Saturated sodium chloride solution is fed continuously into a container
fitted with titanium anodes. The bottom of the cell consists of a layer of
mercury, circulated by means of a pump. This layer serves as cathode.
Under the conditions that prevail, sodium ions are preferentially discharged.
The sodium metal dissolves in the mercury to form an amalgam. This
amalgam is reacted with water in a "decomposer", producing hydrogen gas
and sodium hydroxide solution:
De Nora CELL Mercury Cells2/4
mercury
Mercury Cells3/4
Mercury Cell Operation
Mercury Cells4/4
Advantages
Lower brine purity requirements
High purity NaOH and KOH product
NaOH and KOH produced directly at 50% concentration
Disadvantages
Highest power consumption
Mercury Emissions
27
In the diphragm (Nelson) cell, saturated sodium chloride solution is fed
continuously into a steel-mesh container lined with an asbestos diaphragm
in which a carbon anode is placed. Chlorine gas is produced at the carbon
anode, and escapes out of the cell for further treatment.
Hydrogen is produced on the outside of the asbestos, and escapes out of
the cell, where it is collected.
A steam is used to create a heated environment, and, through condensation
on the steel mesh, washes out the sodium hydroxide, which is collected at
the bottom of the cell, from where it is drawn off.
This process is being phased out, as asbestos is harmful to the workers,
causing fatal lung diseases generally called ASBESTOSIS.
Diaphragm Cells1/3
Diaphragm Cells2/3
Diaphragm Cells3/3
Advantages
Lower brine purity requirements than membrane cells
Lower power consumption than mercury cells
Simpler cell equipment than mercury cells
Disadvantages
NaOH and KOH produced at ~25% concentration, ie low product purity
Solid salt produced during evaporation
Asbestos traditionally used for diaphragm, which is harmful
The membrane cell is the most modern and has economic and
environmental advantages.
The two other processes generate hazardous wastes (containing
mercury or asbestos).
In the membrane process, the chlorine (at the anode) and the
hydrogen (at the cathode) are kept apart by a selective polymer
membrane that allows the sodium ions to pass into the cathodic
compartment and react with the hydroxyl ions to form caustic
soda
Membrane Cells1/4
31
In the membrane process, the anode and cathode compartments are
separated by an ION EXCHANGE MEMBRANE that allows water and
sodium ions to diffuse through, but not chloride ions.
•In the anode compartment, chloride ions migrate to the titanium anode,
where they are discharged to form chlorine gas.
•In the cathode compartment, hydrogen ions migrate to a nickel cathode,
where hydrogen is produced.
•Electrical neutrality is maintained by sodium ions moving through the
membrane from the anode compartment to the cathode compartment.
•This is the preferred industrial method for the preparation of chlorine and
sodium hydroxide. A very pure product NaOH is obtained, with minimal
effects on the environment. The energy requirements of this cell are said
to be more advantageous than with the diaphragm or mercury cells.
Membrane Cells2/4
32
Membrane Cells3/4
Membrane Cells4/4
Advantages
Lowest power consumption
High purity NaOH and KOH product
No mercury or asbestos emissions
Disadvantages
Significantly higher brine purity requirements
NaOH and KOH produced at ~30% concentration, ie low
product purity
High capital cost
34
Polymer membrane of Membrane Cells
Electricity Consumption by Production Process
Sodium Hypochlorite Production
The most common method for manufacturing sodium
hypochlorite is by the treatment of sodium hydroxide
solution with gaseous chlorine.
2NaOH + Cl2 → 2NaOCl + NaCl + H2O
Sodium hypochlorite is employed as:
a disinfectant and deodorant in dairies, creameries, water
supplies, sewage disposal, and households.
It is also used as bleach in laundries. As a bleaching agent,
it is very useful for cotton, linen, jute, rayon, paper pulp,
and oranges.
Cement Industry
WHAT IS CEMENT????
Material with adhesive and cohesive
properties
Any material that binds or unites -
essentially like glue
• Cement is a basic material for building and civil
engineering construction.
FUNCTION OF CEMENT
to bind the sand and coarse aggregate
together
to fill voids in between sand and coarse
aggregate particle
to form a compact mass
Types of Cement
Two types of cement normally used in
building industry are as follows:
a) Hydraulic Cement
b) Non-hydraulic Cement
Hydraulic Cement
Hydraulic Cement sets and hardens by
action of water. Such as Portland Cement
In other words it means that hydraulic
cement are:
“ Any cements that turns into a solid product
in the presence of water (as well as air)
resulting in a material that does not
disintegrate in water.”
Non-hydraulic Cement
Any cement that does not require water to
transform it into a solid product.
2 common Non-hydraulic Cement are
a) Lime
- derived from limestone / chalk
b) Gypsum
PORTLAND CEMENT
Chemical composition of Portland Cement:
a) Tricalcium Silicate (50%)
b) Dicalcium Silicate (25%)
c) Tricalcium Aluminate (10%)
d) Tetracalcium Aluminoferrite (10%)
e) Gypsum (5%)
FUNCTION :TRICALCIUM SILICATE
Hardens rapidly and largely responsible for
initial set & early strength
The increase in percentage of this compound
will cause the early strength of Portland
Cement to be higher.
A bigger percentage of this compound will
produces higher heat of hydration and
accounts for faster gain in strength.
FUNCTION :DICALCIUM SILICATE
Hardens slowly
It effects on strength increases occurs at ages
beyond one week .
Responsible for long term strength
FUNCTION :TRICALCIUM ALUMINATE
Contributes to strength development in the
first few days because it is the first compound
to hydrate .
It turns out higher heat of hydration and
contributes to faster gain in strength.
But it results in poor sulfate resitance and
increases the volumetric shrinkage upon drying.
Cements with low Tricalcium Aluminate
contents usually generate less heat,
develop higher strengths and show greater
resistance to sulfate attacks.
It has high heat generation and reactive
with soils and water containing moderate
to high sulfate concentrations so it’s least
desirable.
FUNCTION: TETRACALCIUM
ALUMINOFERRITE
Assist in the manufacture of Portland Cement
by allowing lower clinkering temperature.
Also act as a filler
Contributes very little strength of concrete
eventhough it hydrates very rapidly.
Also responsible for grey colour of Ordinary
Portland Cement
49
gypsum is used to assist in retard the
setting time of cement when it is mixed
with water.
FUNCTION: GYPSUM
MANUFACTURING OF PORTLAND
CEMENT
The 3 primary constituents of the raw
materials used in the manufacture of
Portland Cement are:
a) Lime
b) Silica
c) Alumina
Lime is derived from limestone or chalk
Silica & Alumina from clay, shale or bauxite
There are four main steps for cement manufacturing
1- Quarry,
2- raw grinding,
3- burning, grinding,
4- storage & packing
THE CEMENT MANUFACTURING PROCESS
1. BLASTING : The raw materials that are used to manufacture cement (mainly limestone and clay)
are blasted from the quarry.
2. TRANSPORT : The raw materials are loaded into a dumper
3. CRUSHING AND TRANSPORTATION : The raw materials, after crushing, are transported to the
plant by conveyor. The plant stores the materials before they are homogenized.
Quarry face
1. BLASTING 2. TRANSPORT
quarry
3. CRUSHING & TRANSPORTATION
crushing
conveyor
dumper
storage at the
plant
loader
THE CEMENT MANUFACTURING PROCESS
1. RAW GRINDING
Raw grinding and burning
2. BURNING
1. RAW GRINDING : The raw materials are very finely ground in order to produce the raw mixture.
mostly, using raw mill.
2. BURNING : The raw mix is preheated, using cyclone, before it goes into the kiln, which is heated by
a flame that can be as hot as 2000 °C. The raw mix burns at 1500 °C producing clinker which, when
it leaves the kiln, is rapidly cooled with air fans. So, the raw mix is burnt to produce clinker : the basic
material needed to make cement. Natural gas, petroleum or coal are used for burning.
conveyor Raw mix
kiln
cooling
preheating
clinker
storage at the
plant
Raw mill
THE CEMENT MANUFACTURING PROCESS
1.GRINDING : The clinker and the gypsum are very finely ground , using ball mill , giving a “pure
cement”. Other secondary additives materials can also be added to make a blended cement.
2. STORAGE, PACKING, DISPATCH :The cement is stored in silos before being dispatched either in
bulk or in bags to its final destination.
1. GRINDING
Grinding, storage, packing, dispatch
2. STORAGE, PACKING, DISPATCH
clinker
storage
Gypsum and the secondary additives are added to
the clinker.
silos
dispatch
bags
Finish grinding
CEMENT CLINKERS
1. The cement manufacturing process begins when limestone,
the basic raw material used to make cement, from the
limestone quarry is transported to the cement plant.
2. The limestone is combined with clay, ground in a crusher and
fed into the additive silos. Sand and iron are then combined
with the limestone and clay in a carefully controlled mixture
which is ground into a fine powder in a 2000 hp roller mill.
3. Next, the fine powder is heated as it passes through the
Pre-Heater Tower into a large kiln, which is about 100 meters
length and up to 4 meters in diameter. In the kiln, the powder is
heated to 1500oC, and the created new product is called
clinker.
4. The clinker is combined with small amounts of gypsum and
limestone and finely ground in a finishing mill.
5. The cement is, then, stored in silos before being dispatched
either in bulk or in bags to its final destination.
The mill is a large revolving cylinder containing 250 tones of
steel balls that is driven by a 4000 hp motor. The finished
cement is ground to a fine product.
Fuel: Natural gas, petroleum or coal are used
for burning. High fuel requirement may make
it uneconomical compared to dry process.
Process Type
There are two main process that can be used in manufacturing of Portland Cement, the raw material process and the clinker burning process are each classified into:
i) wet process
ii) dry process
Wet Process
Raw materials are homogenized by crushing,
grinding and blending so that approximately
80% of the raw material pass a No.200 sieve.
The mix will be turned into form of slurry by
adding 30 - 40% of water.
It is then heated to about 1510ºC in
horizontal revolving kilns (76-153m length
and 3.6 - 4.8 m in diameter).
Dry Process
Raw materials are homogenized by crushing,
grinding and blending so that approximately
80% of the raw material pass a No.200 sieve.
Mixture is fed into kiln & burned in a dry state
This process provides considerable savings in
fuel consumption and water usage but the
process is dustier compared to wet process
that is more efficient than grinding
Dry process kilns may be as short as half in
length of that in wet process.
In the kiln, water from the raw material is
driven off and limestone is decomposed into
lime and Carbon Dioxide.
limestone lime + Carbon Dioxide
In the burning zone, portion of the kiln, silica
and alumina from the clay undergo a solid
state chemical reaction with lime to produce
calcium aluminates.
silica & alumina + lime calcium aluminates
Dry Process & Wet Process-kiln Reactor
The rotation and shape of kiln allow the
blend to flow down the kiln, submitting it to
gradually increasing temperature.
As the material moves through hotter regions
in the kiln, calcium silicates are formed
These products, that are black or greenish
black in color are in the form of small
pellets, called cement clinkers
Cement clinkers are hard, irregular and ball
shaped particles about 18mm in diameter.
The cement clinkers are cooled to about
51ºC and stored in clinker silos.
When needed, clinker are mixed with 2-5%
gypsum to retard the setting time of cement
when it is mixed with water.
Then, it is grounded to a fine powder and
then the cement is stored in storage bins
or cement silos or bagged.
Cement bags should be stored on pallets in
a dry place.
KILN
CEMENT SILO
Chemistry
Common
Name
Chemical Name Chemical
Formul
a
Glass
Compon
ent
Sand Silica or Silicon
Dioxide
SiO2 SiO2
Soda Ash Sodium Carbonate Na2CO3 Na2O
Limestone Calcium Carbonate CaCO3 CaO
What is Glass? Glass is a manufactured material formed when a
mixture of sand, soda, and lime is heated to a high
temperature and assumes a molten, or liquid, state.
69
Glass Manufacturing
Commercially produced glass can be classified as
soda-lime glass, since it constitutes 77 percent of total
glass production.
The manufacture of such glass is carried out in four
phases:
(1) preparation of raw material,
(2) melting in a furnace,
(3) forming and
(4) finishing.
See diagram for typical glass manufacturing, next slide
70
71
Glass production
involves two main methods –
The float glass process, which produces sheet glass, and
The glassblowing which produces bottles and other containers.
Glass container production
Modern glass container factories are three-part operations:
1- batch house : handles the raw materials
2- hot end : handles the manufacture proper: in which the molten glass
is formed into glass products, beginning when the batch is fed into the
furnace at a slow, controlled rate. The furnaces are natural gas- or fuel
oil-fired, and operate at temperatures up to 1,575°C. then, to the
annealing ovens, and forming machines;
3- Cold end
The role of the cold end is to inspect the containers for defects,
package the containers for shipment and label the containers.
72
Annealing
As glass cools it shrinks and solidifies. Uneven cooling
causes weak glass due to stress. Even cooling is achieved
by annealing. An annealing oven (known in the industry as
a Lehr)
The glass cools to approximately 600 oC by the time it
actually enters the annealing lehr. Inside the lehr, the
glass undergoes a controlled cooling process, depending
on the glass thickness, over a 20 – 6000 minute period
Float Glass
In 1952 Alistair Pilkington invented the float glass
process. The float glass process is the most common
method of flat glass production in the world.
This process involves melting recycled glass, silica
sand, lime, potash and soda in a furnace and floating
it onto a large bed of molten tin. This mass slowly
solidifies over the molten tin as it enters the
annealing oven where it travels along rollers under a
controlled cooling process.
From this point the glass emerges in one continuous
ribbon where it is then cut and further processed to
customer's needs.
Float Glass Process1/4
Batching of raw materials
The main components of Soda Lime glass:
Silica sand (73%),
Calcium oxide (9%),
Soda (13%) and
Magnesium (4%),
All are weighed and mixed into batches
to which recycled glass (cullet) is added.
Melting of raw materials in the furnace
The batched raw materials pass from a mixing silo to a five-chambered furnace where they become molten at a temperature of approximately 1500°C. Every operation is carefully monitored.
Drawing the molten glass onto the tin bath
The molten glass is "floated" onto a bath of molten tin at a temperature of about 1000°C. It forms a ribbon with a working width of 3210mm which is normally between 3 and 25mm thick. The glass which is highly viscous and the tin which is very fluid do not mix and the contact surface between these two materials is perfectly flat.
Float Glass Process2/4
Cooling the molten glass in the annealing lehr
On leaving the bath of molten tin, the glass - now at a temperature of 600°C - has cooled down sufficiently to pass to an annealing chamber called a lehr.
The glass is now hard enough to pass over rollers and is annealed, which modifies the internal stresses enabling it to be cut and worked in a predictable way and ensuring flatness of the glass.
As both surfaces are fire finished, they need no grinding or polishing.
Float Glass Process3/4
Float Glass Process4/4
Quality checks, automatic cutting, storage
After cooling, the glass undergoes rigorous quality checks and is washed. It is then cut into sheets up to 6000mm x 3210mm which are in turn stacked and stored ready for transport.
The entire production process from the batching of raw materials to cutting and stocking is fully automatic controlled.
Glass Recycling
The used glass containers which you recycle at curb-side or take to your local recycling station are easily recycled into new containers at the glass factory.
Glass companies depend upon local communities and various glass recyclers, usually located near our manufacturing facilities, to supply quality used glass, known as cullet, for their factories.
Already separated by color, the cullet is placed into a hopper and fed onto a belt. The belt carries the cullet through a powerful magnet to remove bottle tops and other metals. It then passes through picking stations to remove contaminants such as ceramic, Pyrex, and other items that cannot be removed mechanically. The final step in processing cullet is to crush the cullet into finer glass particles which will then be added to the Raw Materials as they are fed into the glass furnace.
79
Fertilizer Industry
80
Fertilizer
Most producers of compound fertilizers in the world are producing nitrate based
mineral compound fertilizers under the product name “NP” or “NPK”. These
products contain nitrogen in ammoniacal (NH4) and nitrate (NO3) form,
phosphorus expressed as P2O5, and normally also potassium expressed as K2O.
The content of nutrients (N + P2O5 + K2O) will normally be between 40 and 50%.
In addition the fertilizers may contain magnesium, boron, sulphur and micro-
nutrients.
These compound fertilizers are made by one of the two following important
production routes:
1– The nitric acid route or nitro-phosphate process,
2– The sulfuric acid route or mixed-acid process,
The two processes are based on different technologies, having different investment
costs, economic impact, energy consumptions, emission values and process
integration
Sources for the three primary nutrients are given in Figure next two slide.
Fertilizer
83
Fertilizer Materials
2-Mixed Fertilizers
•The primary advantage of mixed fertilizers is that they contain
all three primary nutrients—nitrogen, phosphorus, and
potassium—and require a smaller number of applications. They
can be liquids or solids.
•The overall percentage of the three nutrients must always be
stated on the container. The grade designation is %N-%P2O5-
%K2O. It is commonly called the NPK value.
•Note that it is an elemental percentage only in the case of
nitrogen. Phosphorus and potassium are expressed as oxides.
Thus an NPK value of 6-24-12 means that 6% by weight is
elemental nitrogen, 24% is phosphorus pentoxide, and 12% is
potash.
85
LIQUIDS VS. SOLIDS
There are many different types of liquid and solid fertilizers but we give
only some generalizations about advantages of each.
Liquid fertilizers:
Are a clear solution, a suspension of a solid in a liquid (aided by a
suspending agent), or a simple slurry of a solid in a liquid, account for 20%
of all NPK mixed fertilizers
Solid fertilizers:
Contain no liquid, Mixed solid fertilizers can be made by either direct
granulation methods or bulk blending.
Bulk blending is made by mechanical mixing of the separate granular
intermediate materials. It is usually done in small plants near the point of
use. This technique is employed because the fertilizer can be "tailor-made"
to fit the exact requirements of the user.
Table next slide summarizes the advantages of liquids and solids
Liquids Solids
Lower capital investment Less corrosion for the equipment
Less labor, handling and conditioning
costs
Better economics of smaller volume
storing cost
More inform composition Solubility restrictions are not present
More uniform distribution on land No crystallization problem in cold weather