Gasifiers are generally classified according to the fluidization regime in the gasifier; moving bed, fluidized bed, and entrained flow. This chapter provides examples of each type of gasifier. The Lurgi gasifier is the oldest gasifier technology that is still widely used in commercial practice.

1. TYPES OF GASIFIER

2. GASIFICATION
 Gasification is a partial oxidation process whereby a carbon source such as
coal, natural gas or biomass is broken down into carbon monoxide (CO)
and Hydrogen (H2) plus carbon dioxide (CO2) and possibly hydrocarbon
molecules such as methane (CH4)
 This mix of gas is known as producer gas and the precise characteristics of
the gas will depend on the gasification parameters such as temperature and
also the oxidizer used
 The oxidizer may be air, in which case the producer gas will also contain
Nitrogen (N2) or steam or oxygen

3. GASIFIER
• Gasifier is an equipment which can gasify a variety of biomass such as
wood waste, agricultural wastes like stalks and roots of various crops,
maize cobs, etc.
• The gasifier is essentially a chemical processes take place. Biomass gets
dried, heated, pyrolyzed, partially oxidized and reduced, as it flows
through it.
• The gas produced in the gasifier is a clean burning fuel having calorific
value of about 950 to 1200 Kcal/m3.
• Hydrogen(18 - 20 %)and carbon - monoxide (18 - 24%) are the main
constituents of the gas.
• The advantages of a gasifier are very easy to operate, maintain, sturdy in
construction and reliable in operation

4. GASIFIER

5. 1. Grate
2. Throat
3. Air nozzle/air distribution system
4. Ash removal system/ash removal port
5. Gas outlet
6. Ignition port
7. Biomass feeding port
8. Hopper
COMPONENTS OF THE GASIFIER

6. PROCESS OF GASIFICATION

7. CONVERSION OF BIOMASS INTO PRODUCER GAS

8. TYPES OF GASIFIER
FIXED BED
o UPDRAFT GASIFIER (COUNTER CURRENT GASIFIER)
o DOWN DRAFT GASIFIER (CO-CURRENT GASIFIER)
o CROSS DRAFT GASIFIER
FLUDIZED BED GASIFIER (Bubbling or circulating)

9. Updraft Down draft Cross draft
TYPES OF GASIFIER

10. UP DRAFT GASIFIER
Reaction zones in an up draft gasifier
An up draft gasifier is characterized by a counter current flow of fuel and
air or gas in the reactor. The producer gas exits from the top of the gasifier

11. FEATURES OF UPDRAFT GASIFIER
• The biomass enters the top of the reaction chamber while steam and air or
oxygen enter from bottom through grate
• The fuel flows downward and up-flowing hot gases pyrolyze it. some of the
resulting charcoal residue falls to the grate, where it burns, producing heat
and giving off carbon dioxide and water vapor
• The CO2 and H2O react with other charcoal particles, producing carbon
monoxide and hydrogen gases
• The gases exit from the top and ashes fall through the grate
• The updraft design is relatively simple and can handle biomass fuels with
high ash and moisture content
• The gas contains 10-20 percent volatile oils making the gas unsuitable for
use in engines or gas turbines

12. TYPICAL ZONAL CHEMICAL REACTIONS AND
PRODUCTS IN A UP-DRAFT GASIFIER

13. THERMO-CHEMICAL REACTIONS OCCURRING
IN GASIFICATION
REDUCTION ZONE
Products of partial combustion – H2O, CO2 and uncombusted and partially cracked
pyrolytic products undergo the following chemical reactions in the red-hot charcoal
bed
C + CO2 = 2CO (- 164.9 MJ/kg mole) [Boudouard reaction]
C +H2O = CO + H2 (- 122.6 MJ/kg mole) [water gas ]
CO + H2O = CO + H2 (+ 42 MJ/kg mole) [water shift reaction]
C + 2H2 = CH4 (+ 75 MJ/kg mole) [Methane reaction]
CO2 + H2 = CO + H2O (- 42.3 MJ/kg mole)
 Low reduction zone temperature yields low calorific value of gas
 Average temp is 850 0C

14. UPDRAFT GASIFICATION DESIGN
• Simple design
• Not sensitive to fuel selection
• Has a long start time
• Delay in response
• Best used for large, long use
applications

15. REACTIONS, TEMPERTURES AND GAS COMPOSITION IN
UPDRAFT GASIFIER

16. Down draft gasifier is characterized by co-current flow of air or gas and the
fuel. Fuel and air or gas move in the same direction
Reaction zones in a down draft gasifier
DOWN DRAFT GASIFIER
• Can use high tar fuels (wood, peat)
• Quicker in response
• Has shorter start time
• Complex design
• Can’t use high ash content fuels
• Fuel pellet size must be uniform

17. FEATURES OF DOWN DRAFT GASIFIER
• Gasifier requires drying of biomass fuel to a moisture content of less than 20
percent
• Fuel and air or oxygen enter the top of the reaction chamber
• Down-flowing fuel particles ignite, burning intensely and leaving a
charcoal residue
• The charcoal which is about 5 to 15 percent of the mass of original fuel,
then reacts with the combustion gases, producing CO and H2 gases
• These gases flow down and exit from the chamber below a grate
• The producer gas leaving the gasifier is at a high temperature
• Combustion ash falls through the grate
• The advantage of the downdraft design is the very low tar content of the
producer gas

18. REACTIONS, TEMPERTURES AND GAS COMPOSITION IN
DOWNDRAFT GASIFIER

19. DOWNDRAFT GASIFICATION ANALYSIS
The general idea behind this design is that the
tarry oils and vapors given off in the distillation zone
are highly unstable at high temperatures. In order to
reach the gas outlet they must pass through the partial
combustion zone where a high amount of tar will be
cracked and reduced to non-condensable gaseous
products before leaving the gasifier
Although the general principle behind this
seems convincing easily, in practice it requires some
testing and high skill to come up with a downdraft gas
producer capable of generating a tar free gas under
equilibrium conditions

20. Down draft gasifier without throat
Down draft gasifier with throat is not suitable for
gasification of agro-residues like paddy husk, groundnut shell etc.
A down draft gasifier without throat can be used for the
gasification of paddy husk, groundnut shell, maize cob, etc.
Down draft gasifier with throat
Gasifier has narrow section below air entrance point in the
reactor, which is called throat. Due to decrease in the cross-
sectional area at the throat, air velocity increases resulting in high
and better temperature distribution in the oxidation zone
.
SIGNIFICANCE OF THROAT IN A DOWN DRAFT GASIFIER

21. DOWNDRAFT GASIFICATION SYSTEM

22. This gasifier can operate with wide
variety of fuels compared to an up draft
or a down draft gasifier
High gas exit temperature, higher gas
velocity at the gas exit
Poor CO2 reduction are certain
characteristics of this type of gasifier
This type of gasifier has been used for
gasification of coal
CROSS DRAFT GASIFIER

23. CROSS DRAFT GASIFICATION ANALYSIS
• Can’t use high tar fuels
• Quicker in response
• Has shorter start time
• Complex design
• Can’t use high ash content fuels
• Fuel pellet size must be uniform

24. FLUIDIZED BED GASIFICATION
A fluidization bed is a chamber with a perforated floor
having pressurized air flowing vertically where a particle
medium usually sand, is contained. The pressurized and flowing
air helps the medium allowing it to act as a fluid

25. • Can use most fuels (wood, peat and coal)
including agriculture waste such as straw, corn
stover and manure
• Has potential to use municipal waste such as
garbage
• Quicker in response
• Has shorter start time
• Complex design
• Lends itself to complete combustion applications
which would allow it to use liquid wastes such as
used engine oil, non-recyclable plastics & old
shoes, garbage for generation of heat
PRINCIPLE OF FLUIDIZED BED GASIFICATION

26. Fluidized bed gasifier is a homogeneous reactor bed of some inert sand
material. The fuel is introduced in the inert bed material and air at the bottom of
the bed in the reactor. This gasifier is characterized by high gas exit temperature,
very high solid particulate matter in the gas and relatively low efficiency. The
gasifier can operate with low bulk density materials such as agro-residues, leaves,
etc.
FLUIDIZED BED GASIFIER

27. REACTIONS, TEMPERTURES AND GAS COMPOSITION IN
FLUIDIZED BED GASIFIER

28. Sr. No Gasifier Type Advantages Disadvantages
1 Updraft • Small pressure drop
• Good thermal efficiency
•Little tendency towards slag
formation
•Great sensitivity to tar
•Moisture and moisture content of fuel
• Relatively long time required for start up of IC engine
• Poor reaction capability with heavy gas load
2 Downdraft • Flexible adaptation of gas
production to load
• Low sensitivity to charcoal
dust and tar content of fuel
• Design tends to be tall
- not feasible for very small
particle size of fuel
3 Cross-draft • Short design height
• Fast response time to load
• Flexible gas production
• Very high sensitivity to slag formation
• High pressure drop
COMPARISON ON THE PERFORMANCE OF GASIFIERS

32. PRODUCER GAS
THERMAL AND POWER OPTIONS

33. THANK YOU