Method and the research and measurement installation for continuous, multivariate analysis of non-catalytic and catalytic converter conversion of solid power fuels, and the post-reaction gas pollution with nitrogen, carbon and sulfur oxides

摘要

method of continuous analysis process of non catalytic and wieloparametrowej catalytic processing energy solid fuel and gas pollution status poreakcyjnego oxides of nitrogen, carbon, sulfur, using measurement of selected parameters considered wu0119glow fuel processing ego in conditions simulating the actual processing process is characterized by that,that set of atmospheric gases and exhaust energy (g1), (g2).(gn) collected in the pressure containers station gas (sg), preferably in the form of oxygen o2, nitrogen carbon dioxide argon co2, n2, ar, nitrogen dioxide no2, carbon monoxide, sulphur dioxide so2, ammonia nh3 is simulating the actual conditions katalit choice reaction gases ycznego or non catalytic conversion process of energy solid fuel.and then after their mass flow measurement using digital mass flow controllers (mfc1), (mfc2).(mfcn) operated with out of command and control (ks) of the measurement parameters (k2) is formed or only streams of gases reducing transported wires with shut-off valves in the open condition przeu0142u0105czanymi favourably manually, or just gas streams the oxidative transported wires with shut-off valves.przeu0142u0105czanymi in open condition preferably manually, after which the mass flow stabilized in the 500 - 10000 ml / min in the oxidising gas stream (ut) are supplied to the intake channel (lw) thermal reactor (rt) either directly or through the pomostowym wi elowlotowy, favourably szeu015bciowlotowy valve (mv) of the dosage in the form of a loop (p),controlled signals alternately oxidising gas stream zau0142u0105czaju0105cymi dosage gi (ut) or gas stream reduction (rd) administered with exit (wy8mv) equipment, command and control (ks) of the measurement parameters (k2) depending on the choice or you demolition process of non catalytic or only catalytic process processing energy fuel orawith / or continuous analysis of impurities in the sample gas outlet poreakcyjnego, simultaneously to the channel inlet (lw) thermal reactor (rt) is metered by the tru00f3jwlotowy (v1) of the shut-off valve, steam efficiency 0,1 - 25 g / mm with steam generator remote control signal quantity and temperature of steam exits (wy7gp) device control sterujacego (ks) with computer measurement parameters (k2), after which the gas stream is dosed to the lubricated reaction deposits (ci) in the thermal reactor (rt) at y what in the process of non catalytic processing of solid fuel.the stationary (ci) thermal reactor (rt) has a constant temperature in the 950u00b0c - 1050u00b0c and represents him comminuted solid fuel grain sizes of 250 - 5000 mm.