| 摘要 |
Pressure vessels (1 ) containing a charge are preheated at pressure of 2 to 5 kPa with liquid heat carrier (8) to maximally 120° C and they are afterheated in another place to maximally 550° C, the pressure vessels (1 ) are continually added and/or replaced and generated gasses are continuously drawn off, cooled to maximally 60° C and separated oily condensate, residual gasses and solid residues are burned after treatment in a cogeneration unit (20). The device comprises preheating unit (2) and afterheating unit (3) with an interconnected liquid heat carrier (8) and with beds (9) containing pressure vessels (1) equipped with an - outlet (5) to a gas pipeline (7). There are preferably a cooler (17) and gas tank/tanks (19) connected on the gas pipeline (7). Condensate pipeline (16) and the gas pipeline (7) are emptying into the cogeneration unit (20) and, as the case may be, a heat exchanger (15) connected to the liquid heat carrier (8) is contained. |
