초록 ▼

A cyclic char gasifier process and apparatus are described wherein reactant gases are first compressed into the pores of a char fuel to react and then the reacted gases are expanded out of the char fuel pores. This cycle of compression and expansion is repeated with fresh reactant gases supplied for

A cyclic char gasifier process and apparatus are described wherein reactant gases are first compressed into the pores of a char fuel to react and then the reacted gases are expanded out of the char fuel pores. This cycle of compression and expansion is repeated with fresh reactant gases supplied for each compression and with reacted gases removed at each expansion. Air and steam are preferred reactant gases when the char fuel is to be gasified by oxidation. Reacted gases from such an oxidation gasifier plant are preferred reactant gases when the char fuel is to be partially gasified by devolatilization. Rapid reaction to a rich product gas can occur over the large surface area inside the char pores and the undesirable Neumann reversion reaction is suppressed by the strongly reducing conditions prevailing therein. The gases of devolatilization gasification can be used to enrichen the gases of oxidation gasification by using two cyclic char gasifier plants in a combination system. The char fuel can be placed into sealed pressure vessel containers or can be gasified in place within an underground coal formation. These cyclic char gasifier plants and systems can produce a network output, one or more fuel gases, a devolatilized char, and a partially oxidized coke as principal products and the proportions of these products can be adjusted over a wide range to match market needs.

대표청구항 ▼

A process for gasifying at least two char fuel masses within separate containers, comprising the steps of: preheating each of said at least two char fuel masses to that temperature at which said char reacts rapidly with oxygen in adjacent compressed reactant gases; compressing at least one reactant

A process for gasifying at least two char fuel masses within separate containers, comprising the steps of: preheating each of said at least two char fuel masses to that temperature at which said char reacts rapidly with oxygen in adjacent compressed reactant gases; compressing at least one reactant gas into the pores of at least one of said char fuel masses; while concurrently expanding reacted gases out of the pores of at least one other of said char fuel masses; alternating said compression process with said expansion process for each char fuel mass, with but one of said compression or expansion processes being applied to any one char fuel mass at any one time; repeating said compression process alternated with said expansion process several times for each of said at least two char fuel masses; continuing said compression process continuously to at least one char fuel mass at a time; continuing said expansion process continuously to at least one char fuel mass at a time; removing substantially all reacted gases as product gases, which have expanded outside the pores, from continued contact with said char fuel, during each expansion on each char fuel mass; supplying at least one fresh reactant gas for each compression on each char fuel mass, said reactant gases comprising a gas containing appreciable oxygen gas.