Method and the research and measurement installation for continuous, multivariate analysis of gaseous power fuels conversion and reforming processes, and the post-reaction gas pollution with nitrogen, carbon, sulfur and chlorine oxides

摘要

method for continuous wieloparametrowej analysis processing and reforming of gaseous fuels and energy status poreakcyjnego gas pollutants nitrogen oxides, carbon, sulphur, chlorine, using the measurement of the characteristic parameters of the processing gas symulu for the actual conditions of the process clear,that set of natural gas and alternative energy fuel and exhaust energy (g1), (g2).(gn) collected in the pressure containers station gas (sg), preferably in the form of methane, ch4, c2h6, c3h8, ethane, propane, ethyl alcohol c2h5oh, oxygen, o2, n2, co2, carbon dioxide, nitrogen, helium argon ar, he, carbon monoxide, sulphur oxide sox, nitrogen oxide, ammonia nh3 is made the choice of the test gas reaction or several gases reactionary.and then the measurement of their mass flow using digital mass flow controllers (mfc1), (mfc2). (mfcn) operated with out (wy9mc1...n) the device command and control (ks) of the measurement parameters (k2) of the selected reaction gas flow mass stabilized in the range 100 - 3000 ml / min is only reducing gas streams or transported wires with valves przeu0142u0105czanymi in s the opening preferably manually, or only the oxidative gas streams.transported wires with shut-off valves przeu0142u0105czanymi in open condition preferably manually.which are supplied to the intake channel (lw) thermal reactor (rt) either directly or through common channel pomostowym wielowlotowy favourably szeu015bciowlotowy valve (mv) of the dosage in the form of a loop (p) controlled signals zau0142u0105czaju0105cymi alternately dozowan ie gas stream from the oxidation (ut) or stream reduction from the (rd) administered with wyju015bcla (wy8mv) equipment, command and control (ks) of the measurement parameters (k2), at the same time to the channel inlet (lw) thermal reactor (rt) is metered by the tru00f3jwlotowy (v1) with a reduced size steam efficiency 0,1 - 25 mg / min with steam generator (gp) remote signal control quantity and temperature of steam output device (wy7gp) command and control (ks) of the measurement parameters (k2), after which the gas stream is dosed to the reactionary lubricated stationary deposits (ci) reactor t ermicznego (rt)with the catalytic material comminuted favourably in tablet form or in the form of monolitycznej structure conductive channels or pores, forming the catalyst carrier based on metal oxideswith in the process of reforming catalytic temperature of stationary (ci) contains in the range 700u00b0c - 1000u00b0c for gases and fuel respectively in the coupler 150u00b0c - 700u00b0c for exhaust gas energyand in the process of processing temperature catalytic stationary (ci) contains in the range 750u00b0c - 950u00b0c for fuel gas and a 350 - 750u00b0c for exhaust gas energy