raw syngas stream and facilitates the removal of the removed matter via a fly ash conduit 222 unit 221 also provides additional cooling to the raw syngas stream moreover unit 221 converts at least a portion of cos in the raw syngas stream to h 2 s and co 2 via hydrolysis system 200 also includes a separation device 250 that is coupled in flow communication with unit 221 and that receives the cooled raw syngas stream via a raw syngas conduit 225 device 250 facilitates removing at least a portion of acid components not shown from the raw syngas stream as discussed in more detail below such acid gas components include but are not limited to co 2 cos and h 2 s moreover in one aspect device 250 is coupled in flow communication with a sulfur reduction subsystem 275 via a conduit 223 subsystem 275 also receives and facilitates the separation of at least some of the acid gas components into components that include but are not limited to co 2 cos and h 2 s the separation and removal of such co 2 cos and h 2 s via device 250 and subsystem 275 facilitates the production of.