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method autotermicznej biomass or organic waste and adjustment device autotermicznej valorisation of biomass or organic waste
method autotermicznej biomass or organic waste and adjustment device autotermicznej valorisation of biomass or organic waste
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机译:方法自动调节生物量或有机废物和调节装置自动调节生物量或有机废物的价
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摘要
method autotermicznej valorisation of biomass or organic waste is characterized by the fact that pre prepared biomass or organic waste moves on surfaces successively at least two located on each other, conveyors in closed reactor chamber, podgrzewan s from the bottom przepu0142ywaju0105cymi exts.wymieszanymi with air exhaust temperature from 180 to 320 degrees c within 30 to 60 minutes, with the combustion gases from the autotermicznej adjustment compound in a reactor in cyklonowej combustion chamber with controlled air flow is where exhaust gas is discharged from the heating chamber r eaktora chimney,however, toryfikat after leaving the reactor is cooled to a temperature of at least 70 oc and is discharged into the tank.device for adjustment of autotermicznej biomass or organic waste has a reactor (1) with a chamber (2), having an inside located over the conveyor zgrzebu0142owe, upper (14) and a bottom (17) of toryfikowanej mixture (44), the interior of which (16, 17) and the upper tape {15,18) are heated with combustion exhaust gas from the chamber toryfikacji cyklonowej (21) with the burner (22) in its bottom (23) and kru00f3u0107cami wylotowymi (24, 25), by cooperating channels, upper (36) and lower (37) and respectively by the inlets (6, 7) in the sidewall (5) the chamber (2) having walls y: the upper (3) from the inlet (4), cooperating with podajnikiem celkowym (34).connected by conveyor (33) with cochlear bunker use (32) waste, the bottom (12) of the outlet (13) toryfikatu (45), discharged through the conveyor cochlear (35) to the container (43) and rear (10) with the outlet (11) of the gas mixture by toryfikowanej channel (31) into the chamber cyklonowej (21) supplied with air from the fans, the main (27) and secondary (29) respectively by a channel (28),the channel (30) and an inlet (26), where the exhaust gas outlets (8, 9) in the sidewall (5) are connected respectively through channels (38, 40) and outlets (39, 41) of the stack (52), and a pump (42) is connected with podajnikiem u015blimakowym (33) toryfikatu and cyklonowa chamber, the chamber (2) of the reactor (1) and kan ed exhaust chimney (52) and conveyor (35) toryfikatu are respectively fitted with thermocouples t1 (46), t2 (47).t3 (48), (49) t4 and t5 (50), and also in the automatic exhaust gas analyzer (51) vented to the stack (52).
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