Catalysis Today 55 (2000) 179187
Environmental catalysis into the 21st centuryR.J. Farrauto , R.M. Heck
Engelhard Corporation, 101 Wood Avenue, Iselin, NJ 08830-0770, USA
This paper describes existing catalyst technologies and trends in research as we enter the 21st century. Catalytic technologiesdeveloped during the 20th century for end-of-pipe clean up of pollutant emissions will continue for mobile and stationarysources. The catalytic problems associated with the fuel-efficient lean-burn engine, with lower emissions of greenhouse gases,offers significant challenges, especially for lean NOx reduction with on-board fuels. Monitoring pollutants using catalyticsensors will play a key role in controlling emissions from mobile and stationary sources. Decomposing ambient ozone usingpassive catalytic technologies will find increasing application by the year 2000. Photocatalysis will continue to be the subjectof research, but applied only in niche markets. The proton exchange membrane fuel cell will be a major focus for researchin electrocatalysis and catalytic fuel processing to make hydrogen from hydrocarbons. This technology holds great promisefor stationary and vehicular power generation. The manufacture (Green Chemistry) of chemicals with decreased waste andpollutants will continue to be actively pursued by many chemical manufacturers with increasing successes. The feasibility ofcatalytic combustion for stationary power generation with ultra-low emissions will be decided early in the 21st century.
Predictions for the possibility of commercial successes will be made. 2000 Elsevier Science B.V. All rights reserved.
Keywords: Lean NOx reduction; Ambient ozone destruction; Photocatalysis; Fuel cells; Green manufacturing; Catalytic combustion
Environmental catalysis research is undergoing atransition from pollution abatement to pollution pre-vention. Research for advanced fuel cells and catalyticcombustion, both promise power generation withultra-low emissions, are under intensive investiga-tion worldwide. New and cleaner catalytic routes arechanging the way in which bulk and fine chemicalsare made.
During this transitional phase, catalytic pollutionabatement technology will continue to be used com-
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mercially with further improvements in effectivenessrequired. Emissions from the internal combustion en-gine will remain a focal point for new technologies,which improve fuel economy and decrease emissionsof greenhouse gases (i.e. CO2). Lean-burn internalcombustion engines promise significant improvementsin fuel economy, but the problem of NOx abatementremains to be solved.
Monitoring pollutants to extremely low concen-trations in automobile exhausts, chemical processes,commercial and residential buildings is also under in-tense investigation using sensors which could containcatalysts.
The abatement of traces of pollutants from the airusing passive catalysis is a new and exciting way toimprove the quality of the air we breathe. Catalysts de-posited on heat-exchanger surfaces can be utilized to
0920-5861/00/$ see front matter 2000 Elsevier Science B.V. All rights reserved.PII: S0920 - 586 1 (99 )00237 -0
180 R.J. Farrauto, R.M. Heck / Catalysis Today 55 (2000) 179187
decompose ambient ozone and hydrocarbons. Photo-catalysis continues to show effectiveness, but for spe-cial applications only.
The objective of the current survey is to present thecatalytic technologies that will be the focus of researchas we enter the 21st century.
2. Catalysts for the 21st century automobile
The demands of a catalyst to function in the hos-tile environment of the automobile exhaust has re-sulted in the development of materials never beforeneeded in catalysis . During the latter part of the20th century, we have seen the widespread use of anentirely new structure; the ceramic and metallic mono-lithic substrate as a support for the catalytic washcoat.It allows high conversion efficiencies at high gaseousthroughput, provides a high geometric surface areawith lower pressure drop, excellent high-temperatureand thermal-shock resistance and can be convenientlyoriented in the exhaust train in any number of di-rections. The carrier material, most notably activatedhigh surface area Al2O3, has been modified by the useof oxide stabilizers, i.e. La, Si, Ba, etc. to maintainhigh surface areas after experiencing temperatures upto 1100C in the high H2O content of the automobileexhaust. The dispersion of the catalytically active pre-cious metal components has been stabilized againstsintering by using rare-earth metal oxides in the cata-lyst formulation.
The zirconia-based electrochemical O2 sensor pro-vides computer controlled feedback for the combus-tion process to maintain the engine air-to-fuel ratiowithin a narrow range for efficient three-way catal-ysis. Combinations of CeO2 and ZrO2 play an inte-gral role in providing oxygen storage capacity (OSC),which broadens the conversion efficiency for NOx ,CO and HC, during the rich/lean perturbations, as-sociated with the feedback control system. Truly, theautomobile catalyst has resulted in the developmentof materials durable under extreme environments pre-viously thought impossible in conventional catalyticprocesses. Further improvements, however, are still re-quired to meet evermore stringent emission standardsworldwide.
The precious metals used in modern three way cat-alysts (TWC) are primarily Pt and Rh combinations
or only Pd deposited on high surface area alumina. Ineach case, proprietary base-metal oxides are used topromote the activity and stability of the catalyst. Thecomposite washcoat is deposited on a ceramic honey-comb with 400600 cells per square inch with wallthickness of 0.0040.006 in. From the fundamentalunderstanding of the positive and negative interactionsthat occur in multi-component catalysts, some manu-facturers have developed segregated or layered wash-coat structures adding great flexibility in optimizingthe chemistry of the finished catalyst. A high Pd loadedcatalyst with small amounts of Pt and Rh is prepared intwo washcoat layers. Deactivation by compound for-mation between active species is virtually eliminatedby locating the Pd and Rh in separate layers. Further-more, the NOx reduction activity of the Rh functionis maintained by segregating it from the CeO2. Someof the Pd is deposited on the OSC to enhance oxygenstorage and the kinetics of CO oxidation and water gasshift reactions. The remainder of the Pd is depositedon the alumina, which provides better NOx and HCperformance . Thus the washcoat is formulated intwo distinct layers permitting the positive aspects ofeach function to be preserved .
The close-coupled catalyst has been a very sig-nificant technological advancement in meeting thecold-start hydrocarbon emission problem associatedwith the ultra-low emission vehicle (ULEV). Cata-lysts mounted close to the exhaust ports of the enginewill benefit from the hot exhaust and, thus, will reachhydrocarbon light-off temperatures within 10 s .A larger TWC catalyst is located downstream in anunderfloor position to function during other drivingmodes. The close-coupled design, however, exposesthe catalyst to hotter overall temperatures increasingthe likelihood of carrier and/or metal sintering. Onepreparation selectively oxidizes the HC with mini-mal CO oxidation to avoid high temperatures duringrich engine excursions and high CO concentrations.This novel Pd containing catalyst has temperaturestability to 1050C. Proprietary metal oxides areadded to stabilize the Al2O3 and Pd against excessivesintering. The more stringent test cycle (US 06 modi-fication to the US FTP to include aggressive drivingmodes of high speed and load) will add additionalhigh-temperature stress to close-coupled catalysts.This technology is expected to be incorporated intomodel year 2000 vehicles.
R.J. Farrauto, R.M. Heck / Catalysis Today 55 (2000) 179187 181
A major challenge for the next generation offuel-efficient engines is to develop a catalyst capableof NOx reduction with on-board fuel in the presenceof large excesses of O2 . If, and when, available,lean-burn gasoline engines with fuel efficiencies ap-proaching 25% greater than the stoichiometric enginecould be commercialized. Accompanying the fueleconomy benefits will be a proportionate decreasein CO2 emissions. Catalytic lean-NOx reduction isavailable for stationary engines with NH3 as the re-ductant; however, for automotive applications it ismore practical to use on-board derived fuel. Researchfor active, selective and stable catalysts, which willutilize on-board derived hydrocarbons as reductants,has not been successful , and although researchwill continue into the next century the likelihood ofsuccess is low.
In the absence of a lean NOx catalyst, the auto-mobile manufacturers have developed a hybrid partiallean-burn engine which operates lean during cruiseconditions, resulting in 510% fuel economy savings.The NOx generated during lean modes is stored in analkali-earth metal oxide, i.e. BaO, which is incorpo-rated into a TWC. Periodically, the air-to-fuel ratio isforced rich for a short time in which the stored NOx isreduced on the TWC . This system is commerciallyavailable in Japan, where low sulfur-containing fuelsare used. In locations where the gasoline sulfur contentis higher, i.e. US and Europe, the large concentrationof acidic sulfur oxides present in the exhaust adsorbmore strongly than the NOx , poisoning the alkalinesites. If the short rich pulse is conducted at tempera-tures in excess of 650C, almost complete regenerationis feasible. This engine management strategy, coupledwith new materials research, will continue into the21st century. In parallel, the petroleum companies areexpected to decrease sulfur levels in the gasoline to
182 R.J. Farrauto, R.M. Heck / Catalysis Today 55 (2000) 179187
Fig. 2. Ozone conversion is a function of space velocity throughthe radiator.
Fig. 3. Catalyzed coating can be applied to air conditioner con-densers.
heat-exchange surfaces. Field tests have also been con-ducted on catalyzed air-conditioner condensers. Thisconcept is depicted in Figs. 3 and 4. Ozone-containingair passes through the catalyzed heat exchanger ofan air condenser. The ozone conversion maintaineda steady rate over the summer test period at ca. 90%ozone destruction.
The regulatory and analytical framework for ad-dressing urban ozone has been historically based onreducing the emissions of ozone precursors (i.e. VOCand NOx). Additionally, regulatory programs and con-trol systems have generally focused on the ozone levelsat a downwind site, where the peak ozone level oftenoccurs after a series of complex photochemical reac-tions, atmospheric mixing, and transport of ozone and
Fig. 4. Summer long test on commercial air conditioner.
its precursors. The PremAir catalyst, on the otherhand, directly reduces ozone pollution and producesits most significant effects in the vicinities where mo-tor vehicle and population activity are most intense.An assessment of the PremAir catalyst should rec-ognize this difference when comparing its air qualitybenefits with those of other ozone control strategies.This technology is presently being considered for im-plementation on the ultra-low emission vehicles to off-set tailpipe emissions.
3.2. Photocatalytic destruction of hydrocarbons inair and waste waters
Photocatalytic destruction of hydrocarbons is anexcellent example of a practical passive application.Surfaces, such as windows, mirrors, indoor wall tiles,etc. are coated with a thin transparent film of photo-catalytic TiO2. Indoor hydrocarbons, originating fromequipment, cooking or smoking odors, adsorb on thephotocatalyst where sunlight assists in decompositionto carbon dioxide and water passively. Other candi-dates for this technology are sky scraper windows,traffic lights, road sign reflectors, computer and TVscreens, etc. .
Destruction of hydrocarbons in waste waters canbe accomplished by a combination of photocatalyticand activated carbon. Furthermore, heavy metal ionssuch as CrC6 can be reduced to less environmentallyharmful CrC3 using Fe-modified TiO2 in the presenceof sunlight . Studies showing the reduction of Cuions have been investigated using nanosized TiO2 pho-tocatalysts .
R.J. Farrauto, R.M. Heck / Catalysis Today 55 (2000) 179187 183
Fig. 5. Applications of catalytic sensors.
4. Catalytic sensors
Sensor technology for mobile applications has be-come a market opportunity since the operation of themotor vehicles is closely monitored using on-board di-agnostics (referred to as OBD). There are a number ofpossible applications for catalytic automotive sensorsas shown in Fig. 5.
The first true catalytic sensor for the automobile rev-olutionized the approach to engine control and emis-sions reduction. The oxygen sensor , introduced inthe 1970s, consists of a yttrium-doped ZrO2 dense ce-ramic (which has oxygen ion conductivity) formed inthe shape of a thimble and mounted on a spark plugassembly. The ceramic is coated on both sides withporous platinum electrodes forming an electrochemi-cal cell. The outer side is in the exhaust gas while theinner has reference air. A porous oxide layer is de-posited on the exhaust electrode as protection againsterosion and deposits. This electrochemical cell devel-ops a potential (E) as given by the Nernst equation(Eq. (1)), where E0 is the standard state voltage andR, T, n and F the universal gas constant, the absolutetemperature, the number of electrons transferred andthe Faraday constant, respectively. The voltage variesas the ratio of the partial pressure of O2 [PP O2] in airand exhaust.
E D E0 C
[PP O2.air/][PP O2.exhaust/]
The Pt catalyzes the conversion of the O2 by the COor HC and the voltage generated reflects the amountof O2 remaining at the surface of the electrode. Achange from an O2 deficiency to an excess results ina step change in EMF response of the electrochemical
Fig. 6. Voltage response for varying air-to-fuel ratios in the auto-motive oxygen sensor.
Fig. 7. Arrangement of dual oxygen sensor for on-board diagnosticmonitoring.
cell as shown in Fig. 6. This signal is fed back tothe engine control system which adjusts the air-to-fuelratio towards a stoichiometric mixture.
Currently, dual oxygen sensors, positioned before,and after, the catalyst, are used to sense or monitorthe hydrocarbon content of the exhaust via a corre-lation with the oxygen storage capacity of the TWC.The difference in voltage between the inlet and outletoxygen sensors is transmitted to the dashboard, alert-ing the driver of a malfunction of the catalyst. Such asystem is called on-board diagnostics (OBD)  asshown in Fig. 7.
The key to using the dual oxygen sensor for OBDis to find a suitable relationship between the change inoxygen storage of the TWC and hydrocarbon activityor conversion. Such a relationship has been developedand is as shown in Fig. 8, which depicts a region ofsensitivity where the dual oxygen sensor methodologycan be used to monitor hydrocarbon efficiency. Notethat there is substantial variability in this measurement
184 R.J. Farrauto, R.M. Heck / Catalysis Today 55 (2000) 179187
Fig. 8. Correlation of hydrocarbon efficiency and ratio of signalsfrom the dual oxygen sensor.
and the technique has not been proven for ultra-lowemission vehicles.
A sensor is under development for detecting NOxin automobile exhaust utilizing a combination of elec-trochemistry and catalysis. The O2 present in a smallsample of exhaust gas is electrolytically reduced at thePt/ZrO2 cathode. CO or HC then reduce the residualNOx over Rh. A signal correlating the amount of NOxreduced is measured .
With the increased use of sensors in many indus-trial applications, there will certainly be many futuremarkets for catalysts.
5. Benign manufacturing
Chemical companies are improving their processesby generating more desirable products with lessby-product waste. By eliminating pollution controlequipment and waste disposal, economic benefits areclearly derived. Green manufacturing will continueto be a high priority for chemical production well intothe 21st century. The field is extremely broad andmany details are confidential to specific manufactur-ers, but Anastas and Warner  describe the overallgoals in a new monograph.
There are many examples in the literature, but mostnoteworthy is the desire to replace mineral and Lewisacid catalysts with solid acid catalysts, especiallyfor alkylation reactions. Extensive research has beenconducted; however, little success has been achievedmainly due to coke formation and subsequent catalystdeactivation. Nevertheless, research will continue butwith little chance of commercial success.
There has been considerable commercial successin other areas of benign manufacturing. For exam-ple, phenylethanol was traditionally produced by thereaction of benzene with ethylene oxide over AlCl3.Product purification, disposal of the Lewis acid andthe special equipment needed to carry out the re-actions adds considerable expense to production.Hoelderich  has circumvented these disadvantageswhile producing the same product by hydrogenat-ing phenylethylene oxide using Cu and B promotedZSM-5 as the solid acid catalyst. Thus, the entiremanufacturing route has been improved by using theappropriate catalyst. Hoelderich  has recentlyprovided other examples.
Panov et al.  has reported that phenol can beproduced by reaction of benzene with nitrous oxide(produced during the production of adiponitrile for ny-lon) over Fe promoted ZSM-5. The uniqueness is thatN2O usually must be decomposed before dischargeinto the atmosphere, because it is a strong greenhousegas. Therefore, a by-product pollutant is now used asa reactant. This process will be commercialized byMonsanto .
Homogeneous catalysts perform special reactions,i.e. hydroformulation, chiral synthesis, etc. for whichheterogeneous catalysts are not as active or selective.The process difficulty is separation of the expensivecatalyst and ligands from the final reaction product,which often involves energy-consuming distillations.It, therefore, can be characterized as an environmentalissue. Attempts to bond homogenous catalysts to sup-ports in order to permit easy, low energy-consumingseparations while retaining activity, selectivity and re-sistance to leaching has been a goal for many years.Patent applications are now being filed  in whichclaims are made that heteropolyacids can be used aseffective binding agents for some homogeneous cata-lysts. This could have a major impact on the chemicaland pharmaceutical industries if indeed the claims canbe translated to real processes.
6. Catalysts for energy and power generation
6.1. The proton exchange membrane fuel cells
Considerable progress in fuel-cell systems hasbeen made over the last ten years, thus opening
R.J. Farrauto, R.M. Heck / Catalysis Today 55 (2000) 179187 185
Fig. 9. Proton exchange membrane fuel cell using H2 and O2 as fuels.
the commercial door for possible use in stationaryand mobile source applications . The fuel celldirectly converts chemical energy into electricity,thereby eliminating the mechanical process steps thatlimit thermodynamic efficiency. The fuel cell can betwo-to-three times as efficient as the internal com-bustion engine with little, if any, emission of primarypollutants; carbon monoxide, hydrocarbons and nitricoxides.
The key development has been the improved per-formance of the proton exchange membrane (PEM)fuel-cell electrochemical system . This includesdecreased Pt use in the anode and cathode as well asimprovements in CO tolerance of the anode. Hydrocar-bons cannot be directly converted electrochemically atthe anode but hydrogen, with a Pt electrocatalyst, issufficiently active. Therefore, it is necessary to convertreadily available fuels, such as natural gas (station-ary applications) and gasoline (mobile applications) toH2. With the improved efficiency of the fuel cell, theamount of CO2 generated during H2 production fromhydrocarbon processing is significantly decreased rel-ative to the internal combustion engine. The produc-tion of synthesis gas from hydrocarbons for ammoniaand methanol is widely practiced and, therefore, cata-lysts and process conditions are very well known .Desulfurization of the hydrocarbon fuel, steam reform-ing, water gas shift and purification of small amountsof CO present in the exit gas from low-temperature
shift are routinely addressed in large-scale manufac-ture of H2. These processes must now be modified andminiaturized for integration into the fuel cell . Re-duction in size, weight and cost are key factors thatmust be addressed to develop a cost-effective system.This challenge will require modified and/or improvedcatalysts and the reactor design.
The unit operations for a sulfur-containing hydro-carbon fuel are;
desulfurization ! steam reforming ! water gas shift! CO removal from H2 ! H2! anode compartment ! excess H2 combustion
A cartoon of the electrochemical system is shownin Fig. 9. Purified H2 (
186 R.J. Farrauto, R.M. Heck / Catalysis Today 55 (2000) 179187
processes. For this reason, a more CO tolerant Pt/Ruanode was developed, but still the CO must be de-creased to
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4. Fuel cells which directly convert hydrocarbonselectrochemically.
5. The application of PEM fuel cells for mobilesources.
6. Extensive use of photocatalysis.7. Catalytic combustion for ultra-low emissions.8. Catalytic zero emission vehicle
 R.M. Heck, R.J. Farrauto, Catalytic Air Pollution Control:Commercial Technologies, Van Nostrand Reinhold, NewYork, 1995.
 A. Punke, U. Dahle, S. Tauster, H. Rabinowitz, T. Yamada,SAE 950255 (1995).
 Z. Hu, C. Wan, Y. Lui, J. Dettling, J. Steger, Catal. Today30 (1996) 83.
 Z. Hu, R. Heck, SAE 950254 (1995). M. Misono, CATTECH 4, 183 (1998). M. Miyoshi, S. Matsumoto, K. Katoh, K. Tanaka, J. Harada,
N. Takahashi, K. Yokato, M. Sigiura, K. Kasahara, SAE950809 (1995).
 J. Hoke, D. Anderson, R. Heck, T. Poles, J. Steger, SAE960800 (1996).
 M. Wu, N. Kelley, Appl. Catal. B: Environm. 18(12) (1998),79, 93.
 L. Greger, M. Berequist, I. Gottberg, G. Wirmarn, R. Heck,J. Hoke, D. Anderson, W. Rudy, J. Adomaitis SAE 982728(1998).
 J.M. Hermann, Appl. Catal. B: Environm. 17(3) (1998)N7.
 J. Navio, G. Colon, M. Trillas, J. Peral, X. Domenech, J.Testa, J. Padros, D. Rodriguez, M. Litter, Appl. Catal. B:Environm. 16(2) (1998) 187.
 D. Bahnemann, Appl. Catal. B: Environm. 16(2) (1998) N8. Automotive Engineering, February 1998, p. 14. Automotive Engineering, September 1996, p. 123. P. Anastas, J. Warner, Green Chemistry: Theory and Practice,
Oxford University Press, 1998. W. Hoelderich, private communication (1998). W. Hoelderich, Abstracts from the Second World Congress
on Environmental Catalysis, November 1998, Miami Beach,FL, 129 p.
 G. Panov, A. Khovitonov, V. Sobolev, Appl. Catal. A: Gen.98 (1993) 1.
 Chemical Week, 8 (1997) 11. S. Tanielyan, R. Augustine, US Patent Application 08/994,
025 (1997). G. Acres, J. Frost, G. Hards, R. Potter, T. Ralph, D.
Thompson, G. Burstein, G. Hutchings, Catal. Today 38 (1997)393.
 R. Singh, Chem. Eng. Progr. 95(3) (1999) 59. M. Twigg, Catalyst Handbook, Wolfe Publishers, London,
1989, Chapters 47. S. Clarke, A. Dicks, K. Painton, T. Smith, A. Swarm, Catal.
Today 38 (1997) 411. Industrial Management and Technology, March 30, 1998 122
pp. Plug Power, Press Release, 23 December 1998. W. Pfefferle, U.S. Patent 3, 928, 961 (1974). R. Farrauto, M. Larkin, J. Fu, J. Feeley, Mat. Res. Soc. Sym.
Proc. 344 (1994) 101. J. Chambers, Mat. Res. Soc. Sym. Proc. 344 (1994) 1. R. Dalla Betta, F. Ribeiro, T. Shoji, K. Tsurumi, N. Ezawa,
S. Nicholas, U.S. Patent 5, 250,489 (1992). Ind. Catal. News, 98(11) (1998).