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Catalytic Converters

               Dr. K. C. Vora
                                 
                                 
 
Importance of Environment & Technologies



             Environment                                                   Technologies




                             2010                                                                                 System
                                                                                                                Integration
                                        Energy consumption
Importance




                                                               Functions
                      2000                                                          Electronics
                                                                                                                                 d System
                                                                                                                        Integrate
                                Emission CO2
               1990
                                                                                                          ics
                                                                                                  Electron

                   Emission CO/HC/NOx
                                                                                           m
                                                                                  lic Syste
                                                                            Hydrau



                                                        year                                                                          year
Air Quality Impact of
                 the Catalytic Converter




More than 8x108 tons of combined
HC, CO, NOx were abated by 2000

References: Heck and Farrauto
Monograph: Vora & Ghosh.
Great success stories are continuing


     100 % Engine Exhaust                The development of automotive
                                         emission control technology over the
                > 98 %
                                         last three and a half decades is one of
                                         the greatest environmental success
      <2%                                stories of this century.
                                   O2
                                   H2O
                                   CO2   Compared to the 1960s the emission
                                   N2
           Catalyst                      of motor vehicles has dropped to a
                                         fraction, the fuel economy has doubled.

< 0.05 %                     O2
                  > 1.95 %   H2O
                             CO2
            HC               N2
            CO
            NOx
A Catalytic Converter

• Catalytic converters transform NOx, CO and HC into

 N2, CO2 and H2O                 Can or shell
                                 Mat
                                 Ceramic Substrate with Catalytic Coating


  N2
  CO2
  H2O




                                                        NOX
                                                        CO
                                                        HC
Functional Diagram of a Catalytic Converter
The overall catalytic reactions
The overall catalytic reactions
OXIDATION:

2CO + O2            2CO2
Hydrocarbons + O2   CO2 + H2O
2H2 + O2            2H2O

REDUCTION:

NO + Hydrocarbons N2 + CO2 + H2O
2NO + 2CO          N2 + 2CO2
2NO + 2H2          N 2 + H2 O
2NO + 5H2          2NH3 + 2H2O
CO + H2O           H2 + 2CO2
H2O + Hydrocarbons H2 + 2CO2
Working: Theory of Active Sites


                                                                        The Energy
                                                                        Path of a
                                                                        Catalysed &
                                                                        Uncatalysed
                                                                        Reaction.


The active site may be viewed as the point on the catalyst material crystalline where the
electronic forces are optimum for the catalytic reaction to take place.

CO and O2 are chemisorbed on the catalyst and can react readily because of their proximity and
orientation. The process of adsorption also results in weakening of the bond between the atoms
within the CO molecule because some of the energy is shared with the surface. Thus, the
adsorbed atoms of the molecules are less tightly bonded to the molecule and more easily
attracted to other atoms such as oxygen. The reaction between CO and oxygen is thus easier
and more rapid. The products having achieved a lower energy state must desorb at the same
temperature, freeing the active site for additional reactions.
CONSTRUCTIONS OF CATALYTIC
               CONVERTERS
Partners for production
                        of Catalytic Converters
SUBSTRATE MANUFACTURERS:
Ceramic: Corning, NGK,
Silicon Carbide: Ibiden
Metallic: Emitec, Showa

COATERS:
Johnson Matthey, BSF (Engelhard), Umicore (Degussa),
Sud-Chemie (Vadodara)

SUBSTRATE+COATING: Kemira (Finland)

MAT MANUFACTURERS:3M, UNIFRAX

CANNERS:
Sharda Motors, Walker Exhaust (Tenecco), ARVIN Exhaust
Types of Catalytic Converters
PALLETIZED CATALYTIC CONVERTER
Ceramic Substrates:
                   Unique Extrusion Process


Range:

300 to 900 CPSI.
2 to 6 mil wall
thickness
(1 mil = 25.4
microns)
Substrate    Composition            Upper Temp. r   Shock        Strength   Trade Name            Manufacturer
                                    Limit, °C       Resistance

Cordierite   2MgO.2Al2O3.5SiO2      1200            +++          ++         Tliermacomb795        Amer. Lava
                                    1200            +++          ++         Celcor 9475 Poramic   Corning
                                    1200            +++          ++         Versagrid             W.R.Grace
                                    1400            ++           ++                               NGK

Mullite      3Al2O3.SiO2            1350 1700       +            ++         Torvex                DuPont
                                                    +            ++                               Coors

Zirconia     Zr02                   2200            ++           ++         -                     Corning

Silicon      SiC                    1650            ++           +++        Spectram-icRX384      Ibedin,
carbide                                                                                           Norton

Silicon      Si3N4                  1540            ++           +++        Spectram-icRX384      Norton
nitride

Metallic     Fe, 20 Cr, 5 Al with   1400            +++          ++         Aluchrome Y,          Emitec
             addition of 0.05%                                              Kantiial              KY Metal
             yttrium)
Metallic     Fe-Cr-Al-Yt            1250            +++          ++         Fecralloy             Johnson
                                                                                                  Matthey,
                                                                                                   Showa


    CHARACTERISTICS OF SOME COMMERCIAL MONOLITHS 
Metallic Substrates:
Unique High Temp Vacuum Brazing
HISTORY OF METALLIC SUBSTRATES
High cell density metal substrates
If the cell density is increased with the same construction
size, the effective surface is enlarged accordingly.
This considerably increases the efficiency of the system.
Range: 50 to 1000 CPSI / 0.03 to 0.05 mm foil thickness.
ELECTRICALLY
HEATED
CATALYSTS (EHCs)
FROM DIFFERENT
MANUFACTURERS
TURBULENT METALLIC SUBSTRATES
         These foils generate turbulence in the exhaust gas stream
             and so greatly increase the efficiency of the catalyst.
Types:

•Radial flow near the wall in
the channels (TS design®)

•A reduction of diffusion
paths and the hydraulic
diameter and a repeat of the
entrance flow (LS design)

•Radially open, perforated
structures (PE designTM)

•A combination of PE and
LS structures.
METALLIC & CERAMIC SUBSTRATES
EXHAUST BACK PRESSURE OF METALLIC v/s
         CERAMIC SUBSTRATE
Cell Density (cpsi)     200      300      400         236

Cell Shape              Square   Square   Square      Triangle

Wall Thickness (inch)   0.0105   0.0105   0.0065      0.0115
                                          (6.5 mil)
Hole Size (inch)        0.060    0.0475   0.0435      0.042

GSA(in2/in3)            48       57       70          56

Density (gins/ins3)     7.90     9.60     6.74        9.63

Open Frontal Area (%)   73       68       76          62



     COMPARISON OF GEOMETRIC PROPERTIES OF
              CERAMIC MONOLITHS 
DATA                           METALLIC     CERAMIC 
                                SUBSTRATE    SUBSTRATE 
                                              
 Wall thickness (mm) (uncoated)  0.04        0.2-0.15 
                                              
 Cell density (epsi)             400         400 
                                              
 Clear cross section (%)         91.6        67.1-76.0 
 (uncoated)                                   
 Specific surface area(m2/})     3,2         2.4-2.8 
                                              
 Thermal conductivity(W/m.K)  14-22          0,1-0.8 
                                              
 Heat capaeity (kJ/kg.K)         0.5         1.05 
                                              
 Density (g/cm3)                 7.4         2.2-2.7 
                                              
 Coefficient of Thermal          15          1 
 expansion (AL/LxlO"6/K)                      
 Max. short duration operating  1500         1200 
 temperature(°C)                              
  
COMPARISON BETWEEN METALLIC & CERAMIC SUBSTRATES
Parameters                Ceramic cell density    Metallic cell 
                          (cpsi)                  density (cpsi) 
                                                   
                          200  300  400           400  500  600 
                                                              
Cell area, mm2            2.30 1.43 1.21          1.50 1.10  0.97 
                                                              
Surface to volume ratio,  189 220 2790            323 3580 3940 
m"1                       0  5                    0           
                                                   
Open Frontal Area, %      70  60  76              89  86  83 
                                                              
Wall thickness, mm        0.28 0.30 0.15          0.05 0.05  0.05 
                                                              
 


COMPARISON BETWEEN CERAMIC AND METAL
       SUBSTRATE PARAMETERS 
                                       Pt     Pd     Rh 
                                                      
Mine Ratio, upper Deposit              100    40     8 
Catalyst Ratio, 1989 TWC               100    0      20 
                                                      
Approx, Cost in U.S,$/oz in 1989       600    140    1300 
                                                      
Approx. Cost in U.S,$/oz in 1994 [38]  400    140    800 
                                                      
 




     DISPARITY OF PGM RATIOS AND COSTS
MICROSCOPTC STRUCTURE OF A COATED TYPE
              CATALYST
BENCH TEST COMPARISON OF BASE METAL V/S
        NOBLE METAL CATALYST
Sr.    Noble Metal                                   Non-Noble Metal oxides 
No. 
1.     Technology well-known and proven.                 ot commercially proven so far. 
                                                       N
2.     Pt-Pd as 2 way converter catalyst.              Perovskite  oxides  LaCoOs/LaMnOs, 
                                                       Lai-xSixCoi-yMyOs complex oxides. 
3.     Pt-Pd/Rh  proven  combination  for  3  -way Binary Cu-Cr oxide not established My. 
       converter  (Ratio  10:1,  Europe  5:1,  Mine  
       Ratio 16.5:1), 
        
4.     Lower  light-off  temp.,  active  even  at Active from 250°C onwards. 
       100°C.                                           
5.     Conversion  efficiency  high  at  high Conversion  efficiency  tends  to  flatten 
       temperatures.                                   out  at  high  temperatures,  but 
                                                       modifications are equally active. 
6.     Narrow  A/F  for  efficient  3-way NO + CO-»1/2N2 + CO2  Possible in two 
       conversion.                                     stages. 
7.     Not  tolerant  to  high,  continuous  Pb  level Could  be  made  Pb-tolerant  by  a  right 
       in gasoline.                                    catalyst formulation. 
8.     Not  affected  by  SO2  (20  ppm  SO2  in Poisoned  by  SO2.  Development  of  SO2 
       exhaust for 0.03 wt% S in gasoline).            resistant formulations. 
9.     Ceramic  substrate,  washcoated  with No  Washcoat  on  ceramic  substrate. 
       alumina  and  deposited  with  Pt/Rh  (0. Direct  deposition  of  Oxide  precursors. 
       16/0.03 wt%Pt/Rh).                              (5-15 wt% as oxides). 
 
COMPARISON OF NOBLE V/S. NON-NOBLE CATALYST 
CLAMSHELL
CANNING OF
 CATALYTIC
CONVERTER

(Alternative
 method is
Terniquette)
REQUIREMENT OF CATALYTIC CONVERTER 
PARAMETERS WHICH INFLUENCE      
    THE CONVERSION EFFICIENCY 
CAUSE –EFFECT DIAGRAM FOR
    CATALYTIC DURABILITY 
FOUR WINDOWS OF CATALYTIC CONVERTER OPERATIONS 
INSTALLATION OF A METALLIC CONVERTER IN
               SILENCER
EFFECIENCY SCAN AN IMPORTED
      CATALYTIC CONVERTER
EFFECT OF EXHAUST PIPE LENGTH ON
                EXHAUST GAS TEMPERARURE 
EXHAUST GAS TEMPERATURE BEFORE
          & AFTER CONVERTER
ENDURANCE TEST OF
A NOBLE METAL CATALYTIC CONVERTER
  ON A CAR RUN WITH LEADED PETROL
PHOTOGRAPAPHS WITH ELECTRON MICTOSCORE
      AND ELECTRON DEFFRACTION
X-RAY DIFFRACTION CHARTS 
DETERIORATION & REJUVENATION OF
     CATALYTIC CONVERTER
SCHEMATIC SET-UP FOR CATALYTIC CONVERTER
                 TESTING 
DUAL-LINE VEHICLE EMISSION TEST SYSTEM FOR
      CATALYTIC CONVERTER TESTING 
MASS EMISSION TEST SET UP ON CHASSIS
          DYNAMOMETER
LAMBDA SENSOR
EFFECTIVENESS OF CLOSED-LOOP &
OPEN-LOOP THREE-WAY CATALYSTS 
EMISSION DATA OF 4-STROKE ENGINED
MOTORCYCLE FITTED WITH CATALYTIC CONVERTER
EMISSION DATA OF 2-STROKE ENGINED MOPED
   FITTED WITH CATALYTIC CONVERTER 
MICROSTRUCTURE OFA FRESH METALLIC                             MICROSTRUCTURE OFA FRESH CERAMIC
           CONVERTER                                                    CONVERTER 




                                     MICRO STRUCTURE AFTER
                                    WASHCOAT ADHESION TEST 




  MICROSTRUCTURE OFA FRESH
CERAMIC CONVERTER AFTER SOME                                       MICROSTRUCTURE SHOWING
     HOURS OF ENGINE RUN                                         POISONING BY CONTAMINANATS 
System Development Methodology
Advances in Automotive Exhaust
Catalysis


   Air-fuel management

   Cold-start strategies

   Catalyst formulation
(Heywood)
“Staying in the Window”
Closed-loop control with HEGO sensor & fuel injection




                                        (Eastwood)
Gasoline Emissions Standards - Comparison




                         Achievable Today
Automotive Substrates
Enabling Technology for Ultra-Low Emissions




      400/6.5 (Euro 2)     900/2 (Euro 4)
Catalyst light-off (A/F ≥ 14.7):
Automotive Emissions
                                  Importance of Cold Start

                          Tailpipe HC Emissions (FTP Bag 1)
                         0.025                                                     1500
Tailpipe HC Mass (g/s)




                                                                                          Temperature, (Deg F)
                          0.02                                                     1200


                         0.015                                                     900
                                          Catalyst "Light-Off"
                                     X    Temperature
                          0.01                                                     600


                         0.005                                                     300


                             0                                                     0
                                 0       100         200         300   400   500
                                                       Time (s)
Pre-turbo catalysts (PTC)
PTC system




Reference:
                                      Converter             Spec.
                                    PTC    PTC    0.04 L, 200 cpsi, 100 gpcf
                                                  Pt
                                           CCC    0.9 L, 400 cpsi, 70 gpcf Pt
                              CCC
                                           UFC    1.2 L, 400 cpsi, 90 gpcf Pt
                                    Ref.   CCC    0.7 L, 400 cpsi, 70 gpcf Pt
 2nd          1 Underfloor
               st
 Underfloor                                UFC1   1.0 L, 400 cpsi, 90 gpcf Pt
              catalyst UFC1
 catalyst                                  UFC2   1.2 L, 400 cpsi, 54 gpcf Pt
 UFC2
                                                                      60
Pre-turbo catalysts (PTC) ...
                                       Impact of pre-turbo catalyst (PTC1) on CO emission during
                                       NEDC
                             5.0




                             4.0                         Raw
Cumulative CO emission [g]




                                                         Emission post Hybrid-catalyst (CC1)
                                                         Emission post pre-turbo- (PTC1) and Hybrid-catalyst (CC1)


                             3.0




                             2.0
                                                                                                                      150




                                                                                                                            Velocity [km/h]
                                                                                                                      100
                             1.0

                                                                                                                      50

                             0.0                                                                                      0
                                   0           200      400              600           800           1000
                                                              Time [s]
                                                                                                                     61
Pre-turbo catalysts (PTC) ...
                          Emission results of reference, compared with and w.o. PTC


                       0,05
                                                                  Ref: Standard exhaust system CCC /
                                                                  UFC1 / UFC2; fresh
                                                                  Without PTC: CC1 / UC1; fresh
                                          0,042

                       0,04                       0,040
NEDC emission [g/km]




                                                                  With PTC: PTC1 / CC1 / UC1; fresh
                                 0,033




                       0,03




                                                                        0,021
                       0,02
                                                                0,016




                                                                                                 0,015

                                                                                                         0,015
                                                                                         0,015
                       0,01                                                     0,010


                       0,00
                                         HC                        CO/10                    NOx/10
                                                                                                                 62
Trends of Catalytic Converter Configuration
Advantages of Close Coupled Catalyst




                                (Umicore)
Closed Couple Catalyst Design Criteria
Exhaust System
Characteristics of PGM Catalysts
Improvement in Oxygen Storage Capacity
Thank You
….

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Dr. vora ppt chapter 4 aftertreatment

  • 1. Catalytic Converters Dr. K. C. Vora      
  • 2. Importance of Environment & Technologies Environment Technologies 2010 System Integration Energy consumption Importance Functions 2000 Electronics d System Integrate Emission CO2 1990 ics Electron Emission CO/HC/NOx m lic Syste Hydrau year year
  • 3. Air Quality Impact of the Catalytic Converter More than 8x108 tons of combined HC, CO, NOx were abated by 2000 References: Heck and Farrauto Monograph: Vora & Ghosh.
  • 4. Great success stories are continuing 100 % Engine Exhaust The development of automotive emission control technology over the > 98 % last three and a half decades is one of the greatest environmental success <2% stories of this century. O2 H2O CO2 Compared to the 1960s the emission N2 Catalyst of motor vehicles has dropped to a fraction, the fuel economy has doubled. < 0.05 % O2 > 1.95 % H2O CO2 HC N2 CO NOx
  • 5. A Catalytic Converter • Catalytic converters transform NOx, CO and HC into N2, CO2 and H2O Can or shell Mat Ceramic Substrate with Catalytic Coating N2 CO2 H2O NOX CO HC
  • 6. Functional Diagram of a Catalytic Converter
  • 8. The overall catalytic reactions OXIDATION: 2CO + O2 2CO2 Hydrocarbons + O2 CO2 + H2O 2H2 + O2 2H2O REDUCTION: NO + Hydrocarbons N2 + CO2 + H2O 2NO + 2CO N2 + 2CO2 2NO + 2H2 N 2 + H2 O 2NO + 5H2 2NH3 + 2H2O CO + H2O H2 + 2CO2 H2O + Hydrocarbons H2 + 2CO2
  • 9. Working: Theory of Active Sites The Energy Path of a Catalysed & Uncatalysed Reaction. The active site may be viewed as the point on the catalyst material crystalline where the electronic forces are optimum for the catalytic reaction to take place. CO and O2 are chemisorbed on the catalyst and can react readily because of their proximity and orientation. The process of adsorption also results in weakening of the bond between the atoms within the CO molecule because some of the energy is shared with the surface. Thus, the adsorbed atoms of the molecules are less tightly bonded to the molecule and more easily attracted to other atoms such as oxygen. The reaction between CO and oxygen is thus easier and more rapid. The products having achieved a lower energy state must desorb at the same temperature, freeing the active site for additional reactions.
  • 11. Partners for production of Catalytic Converters SUBSTRATE MANUFACTURERS: Ceramic: Corning, NGK, Silicon Carbide: Ibiden Metallic: Emitec, Showa COATERS: Johnson Matthey, BSF (Engelhard), Umicore (Degussa), Sud-Chemie (Vadodara) SUBSTRATE+COATING: Kemira (Finland) MAT MANUFACTURERS:3M, UNIFRAX CANNERS: Sharda Motors, Walker Exhaust (Tenecco), ARVIN Exhaust
  • 12. Types of Catalytic Converters
  • 14. Ceramic Substrates: Unique Extrusion Process Range: 300 to 900 CPSI. 2 to 6 mil wall thickness (1 mil = 25.4 microns)
  • 15. Substrate Composition Upper Temp. r Shock Strength Trade Name Manufacturer Limit, °C Resistance Cordierite 2MgO.2Al2O3.5SiO2 1200 +++ ++ Tliermacomb795 Amer. Lava   1200 +++ ++ Celcor 9475 Poramic Corning   1200 +++ ++ Versagrid W.R.Grace   1400 ++ ++ NGK Mullite 3Al2O3.SiO2 1350 1700 + ++ Torvex DuPont + ++ Coors Zirconia Zr02 2200 ++ ++ - Corning Silicon SiC 1650 ++ +++ Spectram-icRX384 Ibedin, carbide Norton Silicon Si3N4 1540 ++ +++ Spectram-icRX384 Norton nitride Metallic Fe, 20 Cr, 5 Al with 1400 +++ ++ Aluchrome Y, Emitec addition of 0.05% Kantiial KY Metal yttrium) Metallic Fe-Cr-Al-Yt 1250 +++ ++ Fecralloy Johnson Matthey, Showa CHARACTERISTICS OF SOME COMMERCIAL MONOLITHS 
  • 16. Metallic Substrates: Unique High Temp Vacuum Brazing
  • 17. HISTORY OF METALLIC SUBSTRATES
  • 18. High cell density metal substrates If the cell density is increased with the same construction size, the effective surface is enlarged accordingly. This considerably increases the efficiency of the system. Range: 50 to 1000 CPSI / 0.03 to 0.05 mm foil thickness.
  • 20. TURBULENT METALLIC SUBSTRATES These foils generate turbulence in the exhaust gas stream and so greatly increase the efficiency of the catalyst. Types: •Radial flow near the wall in the channels (TS design®) •A reduction of diffusion paths and the hydraulic diameter and a repeat of the entrance flow (LS design) •Radially open, perforated structures (PE designTM) •A combination of PE and LS structures.
  • 21. METALLIC & CERAMIC SUBSTRATES
  • 22. EXHAUST BACK PRESSURE OF METALLIC v/s CERAMIC SUBSTRATE
  • 23. Cell Density (cpsi) 200 300 400 236 Cell Shape Square Square Square Triangle Wall Thickness (inch) 0.0105 0.0105 0.0065 0.0115 (6.5 mil) Hole Size (inch) 0.060 0.0475 0.0435 0.042 GSA(in2/in3) 48 57 70 56 Density (gins/ins3) 7.90 9.60 6.74 9.63 Open Frontal Area (%) 73 68 76 62 COMPARISON OF GEOMETRIC PROPERTIES OF CERAMIC MONOLITHS 
  • 24. DATA  METALLIC  CERAMIC  SUBSTRATE  SUBSTRATE    Wall thickness (mm) (uncoated)  0.04  0.2-0.15      Cell density (epsi)  400  400      Clear cross section (%)  91.6  67.1-76.0  (uncoated)      Specific surface area(m2/})  3,2  2.4-2.8      Thermal conductivity(W/m.K)  14-22  0,1-0.8      Heat capaeity (kJ/kg.K)  0.5  1.05      Density (g/cm3)  7.4  2.2-2.7      Coefficient of Thermal  15  1  expansion (AL/LxlO"6/K)      Max. short duration operating  1500  1200  temperature(°C)        COMPARISON BETWEEN METALLIC & CERAMIC SUBSTRATES
  • 25. Parameters  Ceramic cell density  Metallic cell    (cpsi)  density (cpsi)        200  300  400  400  500  600                Cell area, mm2  2.30 1.43 1.21  1.50 1.10  0.97                Surface to volume ratio,  189 220 2790  323 3580 3940  m"1  0  5    0              Open Frontal Area, %  70  60  76  89  86  83                Wall thickness, mm  0.28 0.30 0.15  0.05 0.05  0.05                  COMPARISON BETWEEN CERAMIC AND METAL SUBSTRATE PARAMETERS 
  • 26.   Pt  Pd  Rh        Mine Ratio, upper Deposit  100  40  8  Catalyst Ratio, 1989 TWC  100  0  20          Approx, Cost in U.S,$/oz in 1989  600  140  1300          Approx. Cost in U.S,$/oz in 1994 [38]  400  140  800            DISPARITY OF PGM RATIOS AND COSTS
  • 27. MICROSCOPTC STRUCTURE OF A COATED TYPE CATALYST
  • 28. BENCH TEST COMPARISON OF BASE METAL V/S NOBLE METAL CATALYST
  • 29. Sr.  Noble Metal  Non-Noble Metal oxides  No.  1.  Technology well-known and proven.   ot commercially proven so far.  N 2.  Pt-Pd as 2 way converter catalyst.  Perovskite  oxides  LaCoOs/LaMnOs,    Lai-xSixCoi-yMyOs complex oxides.  3.  Pt-Pd/Rh  proven  combination  for  3  -way Binary Cu-Cr oxide not established My.    converter  (Ratio  10:1,  Europe  5:1,  Mine   Ratio 16.5:1),    4.  Lower  light-off  temp.,  active  even  at Active from 250°C onwards.    100°C.    5.  Conversion  efficiency  high  at  high Conversion  efficiency  tends  to  flatten    temperatures.  out  at  high  temperatures,  but    modifications are equally active.  6.  Narrow  A/F  for  efficient  3-way NO + CO-»1/2N2 + CO2  Possible in two    conversion.  stages.  7.  Not  tolerant  to  high,  continuous  Pb  level Could  be  made  Pb-tolerant  by  a  right    in gasoline.  catalyst formulation.  8.  Not  affected  by  SO2  (20  ppm  SO2  in Poisoned  by  SO2.  Development  of  SO2    exhaust for 0.03 wt% S in gasoline).  resistant formulations.  9.  Ceramic  substrate,  washcoated  with No  Washcoat  on  ceramic  substrate.    alumina  and  deposited  with  Pt/Rh  (0. Direct  deposition  of  Oxide  precursors.  16/0.03 wt%Pt/Rh).  (5-15 wt% as oxides).    COMPARISON OF NOBLE V/S. NON-NOBLE CATALYST 
  • 32. PARAMETERS WHICH INFLUENCE        THE CONVERSION EFFICIENCY 
  • 33. CAUSE –EFFECT DIAGRAM FOR CATALYTIC DURABILITY 
  • 35. INSTALLATION OF A METALLIC CONVERTER IN SILENCER
  • 36. EFFECIENCY SCAN AN IMPORTED CATALYTIC CONVERTER
  • 37. EFFECT OF EXHAUST PIPE LENGTH ON EXHAUST GAS TEMPERARURE 
  • 38. EXHAUST GAS TEMPERATURE BEFORE & AFTER CONVERTER
  • 39. ENDURANCE TEST OF A NOBLE METAL CATALYTIC CONVERTER ON A CAR RUN WITH LEADED PETROL
  • 40. PHOTOGRAPAPHS WITH ELECTRON MICTOSCORE AND ELECTRON DEFFRACTION
  • 42. DETERIORATION & REJUVENATION OF CATALYTIC CONVERTER
  • 43. SCHEMATIC SET-UP FOR CATALYTIC CONVERTER TESTING 
  • 44. DUAL-LINE VEHICLE EMISSION TEST SYSTEM FOR CATALYTIC CONVERTER TESTING 
  • 45. MASS EMISSION TEST SET UP ON CHASSIS DYNAMOMETER
  • 47. EFFECTIVENESS OF CLOSED-LOOP & OPEN-LOOP THREE-WAY CATALYSTS 
  • 48. EMISSION DATA OF 4-STROKE ENGINED MOTORCYCLE FITTED WITH CATALYTIC CONVERTER
  • 49. EMISSION DATA OF 2-STROKE ENGINED MOPED FITTED WITH CATALYTIC CONVERTER 
  • 50. MICROSTRUCTURE OFA FRESH METALLIC MICROSTRUCTURE OFA FRESH CERAMIC CONVERTER  CONVERTER  MICRO STRUCTURE AFTER WASHCOAT ADHESION TEST  MICROSTRUCTURE OFA FRESH CERAMIC CONVERTER AFTER SOME MICROSTRUCTURE SHOWING HOURS OF ENGINE RUN  POISONING BY CONTAMINANATS 
  • 52. Advances in Automotive Exhaust Catalysis  Air-fuel management  Cold-start strategies  Catalyst formulation
  • 54. “Staying in the Window”
  • 55. Closed-loop control with HEGO sensor & fuel injection (Eastwood)
  • 56. Gasoline Emissions Standards - Comparison Achievable Today
  • 57. Automotive Substrates Enabling Technology for Ultra-Low Emissions 400/6.5 (Euro 2) 900/2 (Euro 4)
  • 59. Automotive Emissions Importance of Cold Start Tailpipe HC Emissions (FTP Bag 1) 0.025 1500 Tailpipe HC Mass (g/s) Temperature, (Deg F) 0.02 1200 0.015 900 Catalyst "Light-Off" X Temperature 0.01 600 0.005 300 0 0 0 100 200 300 400 500 Time (s)
  • 60. Pre-turbo catalysts (PTC) PTC system Reference: Converter Spec. PTC PTC 0.04 L, 200 cpsi, 100 gpcf Pt CCC 0.9 L, 400 cpsi, 70 gpcf Pt CCC UFC 1.2 L, 400 cpsi, 90 gpcf Pt Ref. CCC 0.7 L, 400 cpsi, 70 gpcf Pt 2nd 1 Underfloor st Underfloor UFC1 1.0 L, 400 cpsi, 90 gpcf Pt catalyst UFC1 catalyst UFC2 1.2 L, 400 cpsi, 54 gpcf Pt UFC2 60
  • 61. Pre-turbo catalysts (PTC) ... Impact of pre-turbo catalyst (PTC1) on CO emission during NEDC 5.0 4.0 Raw Cumulative CO emission [g] Emission post Hybrid-catalyst (CC1) Emission post pre-turbo- (PTC1) and Hybrid-catalyst (CC1) 3.0 2.0 150 Velocity [km/h] 100 1.0 50 0.0 0 0 200 400 600 800 1000 Time [s] 61
  • 62. Pre-turbo catalysts (PTC) ... Emission results of reference, compared with and w.o. PTC 0,05 Ref: Standard exhaust system CCC / UFC1 / UFC2; fresh Without PTC: CC1 / UC1; fresh 0,042 0,04 0,040 NEDC emission [g/km] With PTC: PTC1 / CC1 / UC1; fresh 0,033 0,03 0,021 0,02 0,016 0,015 0,015 0,015 0,01 0,010 0,00 HC CO/10 NOx/10 62
  • 63. Trends of Catalytic Converter Configuration
  • 64. Advantages of Close Coupled Catalyst (Umicore)
  • 65. Closed Couple Catalyst Design Criteria
  • 68. Improvement in Oxygen Storage Capacity

Hinweis der Redaktion

  1. Together with Emitec, we evaluated the potential of such a preturbo catalyst, shown here on the picture in the left upper corner. The addition of these catalysts to the standard system allowed on a modern diesel car to further improve the tailpipe emissions by about 30 %, as is apparent from the cumulated emissions over the NEDC, the red line with preturbo catalyst and the blue line with only the standard system