72-iJ Emissions Prom the Methanol Fueled Stanford University Gremlim August 1971 H. Anthony Ashby Office of Air Programs ENVIRONMENTAL PROTECTION AGENCY ------- Background The metHanoi-fueled AMC Gremlin built by Stanford University students was named winner in the Liquid Fuel Division of the 1970 Clean Air Car Race. For this reason the car was evaluated by the Test and Evaluation Branch, as a prototype vehicle under the Federal Clean Car Incentive Program, between March 1 and March 19, 1971. Control Technique The use of methanol as a fuel is the basic technique used in the Stanford Gremlin for control of pollutant emissions. Carburetor jets were changed to furnish air-fuel ratios slightly on the lean side of stoichiometric. .The intake manifold was modified to supply ad'dTtional heat to the mixture. An Engelhard catalyst was placed about six inches downstream of the exhaust manifold. An exhaust gas recirculation system was installed, but not used during the course of our tests. Test Program The test car was an American Motors Gremlin with a 232 cubic- inch six-cylinder engine and standard three-speed transmission. Methanol fuel was obtained from a local'chemical supply company. Test procedures included the 1972 Federal Test Procedure (per the November 10, 1970, Federal Register), the 1970 FTP, and the 9x7 procedure, all with hot starts as well as cold starts. At the start of the program lead-free gasoline was used as the fuel for one 1972 FTP and one 9x7 test, to provide baseline emission data. After testing at Ypsilanti was completed, the car was delivered to the Division of Chemistry arid Physics, Fairfax Facility, Cincinnati, Ohio, for a thorough characterization of hydrocarbons and determination of aldehyde emissions. Results Results of the emissions tests are presented in Tables 1 and 2. Table 1 is from the 1972 FTP, while 7-mode cycle results are in Table 2. In the 1972 FTP and the 9x7 procedures, HC data are determined by FID, and NOX emissions by two techniques: chemiluminescence (C.L.) and Saltzman. In the 1970 FTP all data are determined by NDIR. All NO^ emissions data presented in Tables 1 and 2 are reported as N02, corrected to 75 grains humidity. ------- 1__- , The 1972 FTP mass emissions data show good control of emissions, as the car comes very close to meeting the 1975-76 Federal standards of .41 gm/mi HC, 3..4 gm/mi CO, and .4 gm/mi NOx. Re'sul ts from the testing at DCP Cincinnati are summarized in this report as Appendix A. Appreciation is extended to John Sigsby for these data. Conclusion .. The results of these tests indicate that the use of methyl alcohol as fuel can result in very low emissions. The most noticeable change on this car was in the reduction of NOx when changing from gasoline to methanol. This maybe due chiefly to the higher heat of vaporization of methanol, leading to a lower flame temperature. ------- Tab Ie I Stanford Methanol Gremlin Mass Emissions 1972 Federal Test Procedure Test No. HC CO NOx NOx Comments gm/mi gm/mi C.L. Saltzman gm/mi gm/mi "12-1350 .33 1.30 .20 .31 Standard Test 12-1361 .50 13.13 no data .29 Standard Test 12-1368 .58 4.57 .22 .24 Standard Test 12-1376 " .43 5.77 no data 5.23* Standard Test 12-1378 .64 12.61 .22 .25 Standard Test "12-1408 .24 3.55 .30 .30 Standard Test --1353 .09 .20 .17 .37 Hot Start 12-1370 .06 .92 .20 .23 Hot Start 12-1377 .04 .50 .09 2.22* Hot Start 12-1409 .04 .49 .26 .27 Hot Start 12-1331 .34 5.44 4. 74 4.27 Cold, Gasoline * Saltzman data believed not correct. _.=:--'''''''-~''--''''-~''------~-~---'--.-._, '-- . ~, -- ~ - - - -~. "-_.,~;C - --~ -. - -. ,,-' , ------- Table 2 Stanford Methanol Gremlin Mass Emissions 7 - Mo de Driving Cycle Test No. HC CO NOx NOx Comments gm/mi gm/mi C.L. Sa1 tzman gm/mi gm/mi 12-1391 .32 3.87 .39 .32 9 x 7 12-1400 1. 58 9.46 .20 .36 9 x 7 12 -136 7 12-1401 .05 .10 1.37 .23 12-1333 .28 7.25 6-0618 6-0622 .32 1. 59 2.17 .47 6-0615 6-0623 .19 .34 .20 .16 .04 .55 .41 .46 9 x 7 Hot 9 x 7 Hot 2.80 2.41 9 x 7 Cold, Gasoline .09 by NDIR .15 by NDXR 70 FTP 70 FTP . no data 70 FTP Hot .10 by NDIR 70 FTP Hot ------- 1. Appendix A Tests were performed using the proposed 1972-3 Federal cycle from both a cold ahd a hot start. A 3500 lb. fly- wheel was used. The hot start consisted of insuring that the car was thoroughly warmed up; turning it off, and within ten minutes re-running the Federal cycle. The cold starts. were run after an overnight soak on the dynamometer. After these runs were made, the catalyst was removed and one run each was made from both a cold and a hot start. One false sta~t, i.e., the engine died at the beginning of the cycle, occurred on each of the cold starts except C7. The vehicle was restarted and the test begun over. The effluent was defined by the constant volume sampler. . The summary of these results is shown in the attached tables. 2. As expected, few aldehydes other than formaldehyde, were present in appreciable quantities. DNPH derivatives were made arid gas chromatographed to determine the distribution of the aldehydes formed. This confirmed the wet chemical tests which are shown in the tables. Formaldehyde was the only specific aldehyde that could be quantitatively measured, traces of higher aldehydes were also seen with acetaldehyde being the most abundant. 3. A remarkable number of other hydrocarbons were seen over background. Concurrent background samples were collected and analyzed for each run. The values are confirmed by the runs which were made with the catalyst removed. As might be expected, the primary hydrocarbons produced were olefinic' in nature. Any reactivity consideration must be based on the reactivity of methanol which overrides any other compound in concentration. . 4. The largest effect of the catalyst was to reduce the methanol 90% for cold starts and 96% for hot. The catalyst also re- duced CO by about 70% while having no effect on the oxides of nitrogen. Aldehydes were reduced 75 to 80%. Methane ,...as not measureable above background in the hot start tests. It was very low in the cold starts accounting for 4% of the total. Nethanol accounted for 95% and 97% of the hydrocarbons. seen from cold and hot starts respectively. 5. 6. The largest difference between cold and hot starts were in hydrocarbons and CO which decreased between 80 and 90%. Aldehydes were only reduced 30% and C02 and NOx about 10%. The NOx emissions were predominately NO with little NOx or reduced nitrogen present. 7. ~~--':'.,-.~-----+-;.~.- -,.-,~-;c;--- .~-.---=-=---,-- -- ---..~=~-,-~>~-; .,.' .- ~.~ - r" - -,'~-~-~-'.<-._"':_-:;:::-~" -, ------- ~ ' Appendix A Stanford Methanol Gremlin With Catalyst Cold Start Tests Run # C4 C5 C7 Average Compound ppmc ppmc ppmc Methanol 137 220 127 161 l>lethane 5.6 9.1 5.2 6.6 Ethylene 0.47 1.0 0.47 0.6 Butene-1/2 0.44 0.62 0.01 0.4 Methyl Propene Propylene 2.2 0.71 Ethane 0.31 .0.44 obutane 0.31 trace 0.37 Acetylene 0.08 N-Pentane 0.07 TOTAL 144 233 134 170 Mass Emissions grams/mile Hydrocarbon 0.17 0.22 0.14 0.18 CO 2.88 3.51 3.35 3.3 C02 545 541 548 545 NOx 0.54 0.57 0.54 0.55 Total Aldehydes 0.077 0.099 0.093' 0.090 rmaldehyde 0.075 0.089 0.086 0.083 ------- Appendix A Stanford Methariol Gremlin I With Catalyst Hot Start Tests - I Run # C3 C6 C8 Avera,ge Compound ppmc ppmc ppmc Methanol 27 26 33 29 ~Iethane Ethylene 0.47 0.18 0.47- 0.37 .' Butene-l/2 methyl 0.03 Propene Isobutane 1.0 -.06 N-Pentane 0: 76 ! -i T~o pentane 1.0 : J. J.'opyl.ene ., 0.01 Ethane trace TOTAL 27.5 28.8 33.6 30 Mass Emissions grams/mile Hydrocarbon 0.02 0.02 Not Measured 0.02 CO 0.61 0.46 0.75 0.61 C02 490 506 486 494 NOx - 0.506 0.48 0.45 0.48 Total Aldehyde 0.033 0-.076 0.085 0.065 Formaldehyde 0.019 0.072 0.079 0.057 . - - - -~. -- <- --~.._~ - -"..... -...,.-, ,--,------,- . ------- Appendix A Stanford Methanol Gremlin Catalyst Removed - Run # COLD START C9 . HOT START C10 Compound . ~lethano1 ppmc ppmc ~lethane 1580. 7.8 810 Not measured Ethylene Butene-1/2 Methyl Propene 4.2 5.0 .obutane 0.49 trace ! trace ., 0.09 1. 72 0.10 1600 0.28 0.21 Propylene Ethane trace 0.40 Acetylene 1.16 0.03 N-Pentane TOTAL HYDROCARBON 820 Mass Emissions grams/mile Hydrocarbon 1.33 0.77 CO 10.8 2.6 C02 520 488 NOx 0.45 0.43 Total Aldehyde 0.36 0.33 Formaldehyde 0.34 0.30 ..,. ....0 --7- ------- |