Coupled medium-low temperature flue gas processing apparatus for fly ash washing

A coupled medium-low temperature flue gas processing apparatus for fly ash washing, comprising a reactor, wherein

• a stirring motor is arranged in a middle of a top end of the reactor, feeding tubes that are used for performing material guide work of fly ash and water are arranged on both sides of the top end of the reactor, an air inlet tube used for performing flue gas introduction is arranged on a side of the reactor, scraping rings are arranged at a position where an inner end of the reactor is close to a middle of the reactor, a bottom end of the stirring motor is coaxially connected with threaded rods that pass through middle positions of the scraping rings and keep a threaded connection with the scraping rings, bottom ends of the threaded rods are coaxially connected with stirring rods, and a collection assembly used for collecting a mixture of the fly ash and the water is arranged at a bottom end of the reactor;
• edge positions of bottom ends of the scraping rings keep fitting with the inside of the reactor, the stirring motor drives the stirring rods to rotate through the threaded rods so as to perform a stirring treatment on the fly ash and the water, when the stirring motor rotates forwards during stirring, the scraping rings are driven to move down along the inside of the reactor through the threaded rods, so the fly ash adhered to the inside of the reactor is scraped at the edge positions of the bottom ends of the scraping rings, and when the stirring motor rotates reversely, the scraping rings are driven to move up along the inside of the reactor through the threaded rods, to restore an initial position;
• the collection assembly comprises a filter funnel that is sleeved at the bottom end of the reactor and keeps communicating with the inner end of the reactor, a valve is arranged at a position where the inside of the reactor is close to the bottom end of the reactor, the valve is used for controlling a switch between the bottom end of the reactor and the inner end of the filter funnel, and a liquid tank is arranged at a bottom end of the filter funnel;
• fixed rings are arranged at bottom ends of the feeding tubes, section sizes of the fixed rings are greater than those of the feeding tubes, connecting rings are sleeved at positions where the feeding tubes are close to the bottom end, and a plurality of buffer springs are connected between the connecting rings and the fixed rings;
• a bottom end of the air inlet tube is an inclined structure, and the air inlet tube stretches downwards into the inner end of the reactor;
• a protective disk is arranged at an inner end of the air inlet tube, and a section size of the protective disk keeps fitting with that of the inner end of the air inlet tube;
• a threaded ring is arranged at a top end of the filter funnel, an internal thread is arranged inside the bottom end of the reactor, and the threaded ring keeps a threaded connection with the internal thread;
• wedge rings are arranged at the bottom ends of the scraping rings, and section sizes of bottom ends of the wedge rings are less than those of top ends of the wedge rings;
• effluent troughs are arranged at bottom ends of the wedge rings, inner slots for water flow storage are arranged at inner ends of the wedge rings, and the inner slots keep communicating with inner ends of the effluent troughs;
• sponge rings are arranged at inner ends of the inner slots, section sizes of the sponge rings keep consistent with those of the inner ends of the inner slots, a plurality of extrusion rods are arranged at top ends of the sponge rings, and the extrusion rods stretch out of the top ends of the scraping rings and are connected with the top end of the reactor;
• and
• limiting springs are arranged at top ends of the extrusion rods, and top ends of the limiting springs are connected with the top end of the reactor.