Gasification in Detail – Types of Gasifiers
Fixed (Moving) Bed Gasifiers
|source: Electric Power Research Institute
In moving-bed gasifiers, large coal particles move slowly downward through a bed while reacting with gases moving in the opposite direction going upward through the bed. Coarse particles are used in moving-bed gasifiers to ensure good bed permeability and help to avoid excess pressure drop and chemical burning. Reactions within the gasifier occur in different “zones”. In the “drying zone” at the top of the gasifer, the entering coal is heated and dried, while cooling the product gas before it leaves the reactor. The coal is further heated and devolatized by the higher temperature gas as it descends through the “carbonization zone”. In the next zone, the “gasification zone”, the devolatized coal is gasified by reaction with steam and carbon dioxide. Near the bottom of the gasifier, in the “combustion zone”, which operates at the highest temperature, oxygen reacts with the remaining char.
Moving-bed gasifiers operate in two different modes. In the dry-ash mode of operation (e.g., Lurgi dry ash gasifier), the temperature is moderated to below the ash-slagging temperature by reaction of the char with excess steam. The ash below the combustion zone is cooled by the entering steam and oxidant (oxygen or air) and produced as a solid ash. In the slagging mode of operation (e.g., British Gas/Lurgi or BGL gasifier), much less steam is used, and as the result, a much higher temperature is achieved in the combustion zone, melting the ash and producing it in the form of a solid slag.
Moisture content of the fuel is the main factor which determines the discharge gas temperature. Lignite, which has very high moisture content, produces raw gas at a temperature of around 600 °F. Lower moisture bituminous coal produces gas temperatures of over 1000 °F. Typically, the product gas leaving the gasifier is quenched by direct contact with recycle water to condense and remove tars and oils. After quench, heat can be recovered from the gas by generation of low pressure steam.
Moving-bed gasifiers share the following characteristics:
- Relatively low oxidant (oxygen or air) requirement
- Less complex feedstock preparation with the use of coarse coal particles
- Product gas at relatively low temperature, thus no need for expensive heat recovery equipment
- Suitable to handle coals with high reactivity and moisture
- Limited ability to handle coal fines
- Caking coals require design modifications to the gasifier
- Hydrocarbon liquids such as tars and oils are produced
- High “cold-gas” thermal efficiency, when the heating value of the produced hydrocarbon liquids is accounted for
- High methane content in product gas
- Lurgi Dry-Ash Gasifier
- BGL Gasifier
- SVZ Schwarze Pumpe Plant in Germany
- Lurgi Multi Purpose Gasification (MPG)