The '423 patent, however, fails to protect the quench ring from the harsh thermal elements of the reactor.
Although a portion of the
assembly is insulated, it does not provide an effective barrier which would avoid contact between the hot effluent
stream and the cold quench ring surface.
There are several problems that are encountered due to the high temperature conditions within the gasifier.
Among those problems are the development of thermal stresses, which often result in damage to the quench ring as a result of the ring's close proximity to the hot effluent
stream, and the lack of protection of the
metal surfaces of the quench ring.
These problems are often manifested in the form of cracks and fissures which develop in parts of the quench ring.
One problem that may be experienced in gasifiers is the propensity of
molten slag to harden and freeze in the gasifier's constricted
throat.
This undesirable chilling action can, under particular circumstances, severely block the constricted
throat opening, thereby precluding further operations.
Another problem with prior art quench ring and dip tube
assembly arrangements includes the inability to repair or partially replace the quench ring while the gasifier is still fairly hot.
Repairing or replacing the quench ring when the entire gasifier has cooled down to approximately less than 100OF significantly delays resumption of the operation of the gasifier.
Yet another problem with the prior art quench ring and dip tube
assembly arrangements includes small or ineffectively configured drip edges in the refractory lining above the quench ring.
These drip edges are easily damaged and thus permit the flow of
molten slag down along the
throat surface and onto the inner
diameter surface of the quench ring and even the dip tube instead of inducing the
slag to
free fall through the dip tube and into the quench bath as intended.
When the flow is misdirected, the
molten slag can stick to and freeze on the dip tube inner surface, thereby creating a “shadow” effect wherein the quench water from the quench ring will not adequately coat the inner
diameter surface of the dip tube below the frozen
slag.
An uncoated, unprotected portion of the dip tube such as this can lead to overheating and burn-through of the dip tube.
Overheating and burn-through are very serious problems for several reasons, not the least of which is that hot, unquenched
syngas will subsequently flow into downstream units of the gasification processes that are not equipped for the high temperature unquenched gasses.
Another problem with some prior art is the sharp edges on the quench rings.
These sharp edges are not as effectively cooled by the flowing quench water as are curved or flat surfaces since they result in localized stagnant regions within the flow field.
Accordingly, the sharp edges tend to run hotter, thereby increasing thermal stresses within the quench ring structure.