Page 521 - Book Hosokawa Nanoparticle Technology Handbook
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18 DEVELOPMENT OF HIGH-PERFORMANCE ELECTROCHEMICAL REACTORS                   APPLICATIONS

                                  Catho de  :  2NO + 4e - -  N 2 2  + 2 O 2- 2-
                                                       N + 2O
                                  Cathode : 2NO + 4e
                                          2NO    N2
                                                        Ag
                              Cathode    2e -            CGO + NiO
                            Electrolyte
                                            2O 2-          CGO
                              Anode       2e -           Ag
                                                         CGO + Ag
                                                        graphite
                                                  CO 2
                                                     CO
                                    Anode : C + 2O
                                                          + 4e
                                    A nod e  :  C + 2O 2- 2-  CO + 4e - -
                                                        2 2
                  Figure 18.4
                  Schematics and photographs of anode for simultaneous removal of NO /PM in an electrochemical cell.
                                                                     x
                                                           50                                3000
                                      5cm
                                                                   NO -400 ppm-200 ml/min, O -4.7%
                                                                     x
                                                                                       2
                                                                                             2500
                                                           40    Calculated Voltage
                                                         NO x  Decomposition (%)  20  after DC applying  1500  Cell Voltage (mV)
                                  de NO  cell              30                                2000
                                       x





                               Thermo electric                                               1000
                               module                      10  Measured voltage              500

                                                                    Before applying DC voltage at 2V
                                                            0                                0
                                                               500   600  700   800   900  1000
                                                                       Temperature (°C)
                  Figure 18.5
                  Demonstration of de-NO using the converted energy from the exhaust gas heat without any external electrical power.
                                    x


                  (2) Interactive ceramic reactor made of the de-NO  shows an interactive ceramic reactor made of the
                                                       x
                  electrochemical cell with a power module of thermoelectric  de-NO electrochemical cell with a power module
                                                                      x
                                                                 of thermoelectric energy conversion ceramics.
                  energy conversion ceramics
                                                                 Without any external electrical power, 20% of NO x
                  The electrochemical cells for de-NO reaction have  decomposition was achieved continuously using the
                                                x
                  properties well suited for the de-NO /PM purifica-  electrical current produced from the thermoelectric
                                                 x
                  tion; particularly, their electrical power consump-  power module, which performed energy conversion
                  tion is very low for the application. With an attempt  from the waste heat in the hot exhaust gas.  This
                  to develop an autonomous continuous purification  experiment indicates that a complete purification of
                  system, the concept of operating the device for envi-  exhaust gas is possible by stacking up a number of
                  ronment purification without energy consumption  thermoelectric power modules.
                  was finally materialized through the improvement  Promoting energy efficiency in the transportation
                  and assembly of the ceramic materials. Fig. 18.5  sector is crucial to achieve the goal of CO emission
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