| 摘要 |
<p>Pyrolysis coke obtained by pyrolysis process, is claimed, where the process following the loading of pyrolysis furnace with pyrolyzable goods in the form of pellets-filled reaction vessel (2) comprises heating single or all heating elements (9) of pyrolysis ovens (1) in a first phase of the pyrolysis at a first heating temperature, controlling the heating elements by a control unit according to the adjustment of a second heating temperature predetermining on a second phase of the pyrolysis, controlling all heating element using the control unit and cooling the pyrolysis coke. Pyrolysis coke obtained by pyrolysis process, is claimed, where the process following the loading of pyrolysis furnace with pyrolyzable goods in the form of used tires and/or biomass in the form of pellets-filled reaction vessel (2) comprises heating single or all heating elements (9) of pyrolysis ovens (1) in a first phase of the pyrolysis at a first heating temperature of 650-820[deg] C, where a pyrolysis gas evolution is detected by a sensor for the detection of the pyrolysis gas evolution, during the detection of a pyrolysis gas evolution, controlling the heating elements by a control unit according to the adjustment of a second heating temperature predetermining on a second phase of the pyrolysis at 450-520[deg] C that lies below the first heating temperature and/or according to the adjustment of individual groups of heating elements to the processing condition, where a predermining pyrolysis gas temperature is detected by a temperature sensor, during the detection of a predetermined pyrolysis gas temperature of below 140[deg] C, controlling all heating element of the process condition by using the control unit and after a cooling of the pyrolysis coke, the reaction container is taken out to obtain the pyrolysis coke. An independent claim is included for use of an adsorbent in water treatment, purification of contaminated water and/or preservation of purified water.</p> |
