[PA-600/3-77-110
 ctober 1977
Ecological Research Series
                                                            INSWOG
                                              US,

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                RESEARCH REPORTING SERIES

Research reports of the Office of Research and Development, U.S. Environmental
Protection Agency, have been grouped into nine series. These nine broad cate-
gories were established to facilitate further development and application of en-
vironmental technology.  Elimination of traditional grouping was  consciously
planned to foster technology transfer and a maximum interface in related fields.
The nine series are:

      1.  Environmental  Health Effects Research
      2.  Environmental  Protection Technology
      3.  Ecological Research
      4.  Environmental  Monitoring
      5.  Socioeconomic Environmental Studies
      6.  Scientific and Technical Assessment Reports (STAR)
      7  Interagency Energy-Environment Research and Development
      8.  "Special" Reports
      9.  Miscellaneous Reports

This report has been assigned to the ECOLOGICAL RESEARCH series. This series
describes research on the effects of pollution on humans, plant and animal spe-
cies, and materials. Problems  are assessed for their long- and short-term influ-
ences. Investigations include formation, transport, and pathway studies to deter-
mine the fate of pollutants and their effects. This work provides the technical basis
for setting standards to minimize undesirable changes in living organisms in the
aquatic, terrestrial, and atmosphe'ric environments.
This document is available to the public through the National Technical Informa-
tion Service, Springfield, Virginia 22161.

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                                        EPA-600/3-77-110
                                        October 1977
       MEASUREMENT OF RATE CONSTANTS
           OF IMPORTANCE  IN  SMOG

                     by

      John R. Barker, Sidney W. Benson,
  G. David Mendenhall, and David M. Golden

              SRI International
   (formerly Stanford Research  Institute)
        Menlo Park, California  94025
              Grant No. R802288

               Project Officer
               Marcia C.  Dodge
 Atmospheric Chemistry and  Physics  Division
 Environmental Sciences Research  Laboratory
Research Triangle Park, North Carolina   27711
 ENVIRONMENTAL SCIENCES  RESEARCH LABORATORY
     OFFICE OF RESEARCH  AND  DEVELOPMENT
    U.S. ENVIRONMENTAL PROTECTION AGENCY
RESEARCH TRIANGLE  PARK,  NORTH  CAROLINA  27711
           Tj  =; O7 V ,\ "O"'*7
           JUf.il..;>A v'^J-Jri' J.
           U.  S. £!:V;:.;.,t ..;.';,;L FRGTECIiON
           EpissK & L

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                               DISCLAIMER








     This report has been reviewed by the Chemistry and Physics Laboratory,



U.S. Environmental Protection Agency, Research Triangle Park, North



Carolina, and approved for publication.   Approval  does not  signify that



the contents necessarily reflect the views and policies of  the U.S.



Environmental Protection Agency, nor does mention  of trade  names or



commercial products constitute endorsement or recommendation for use.
                                   ii

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                               PREFACE






     For some time, considerable effort has been devoted to understanding



and characterizing the complex phenomenon of photochemical smog.  This



effort has encompassed several different areas of study so as to take



full advantage of the wide range of expertise  in the scientific



community.  The extensive experience accumulated using smog chambers to



simulate smog conditions, and the results of field observation indicate



that a complete understanding of smog depends on the development and



validation of reliable chemical mechanisms consisting of elementary




reactions.





     Since the polluted atmosphere is highly complex and depends sensi-



tively on parameters such as solar irradiance, temperature, pollutant



concentration, and transport phenomena, any errors in the reaction



mechanisms are likely to be magnified at the extremes of the parameter



ranges.  A general approach to formulating general reaction mechanisms



is to include all elementary reactions thought to be important,  and then



test them using smog chamber simulations.  Although smog chamber simu-



lations are designed to be simplified versions of the polluted atmosphere,



the gas mixtures are so complex and spurious chamber effects often are



so important that the technique cannot be used to ascertain elementary



rate processes and can only be used for validation purposes.





     To develop a reliable chemical mechanism describing smog, elementary



reaction rate constants are needed.  Such rate constants preferably can



be obtained by direct experimentation, but estimates can sometimes be



made if sufficient experimental data on related reactions are available.



Such rate constants, once obtained, are often useful, not only for
                                  iii

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understanding smog chemistry,  but also for  understanding  pollutant



formation in combustion processes,  and the  like.  As  rate constant



measurements of higher quality are performed,  inaccurate  rate  constants



are superceded and the general understanding of  photochemical  smog  is



improved.





     In the absence of good elementary reaction  rate  studies,  one must



resort to estimation techniques to formulate an  overall reaction scheme.



Such estimation techniques draw upon data available for reactions



analogous to the one of interest.  If no analogous  reactions have been



studied, the estimated rate parameters must be considered highly



uncertain.  A-factors can be estimated much more reliably and  readily



than activation energies, but even A-factors can be in error if the true



chemical nature of a reaction is misunderstood.   Hence, it is  desirable



to observe the products of elementary reactions  in  order  to guarantee



that the chemistry is correct.  Until more  complete data  of higher



quality become available, estimation techniques, like those illustrated



in this report, will be valuable adjuncts to experiments.





     No satisfactory substitute for experimental determinations for



elementary reaction rate constants is available, however.  All estimates



are subject to errors that can distort the  results  of computer simulations



of photochemical smog.   The experiments described  in this report were



intended to help refine estimates of unmeasured  reaction  rate  constants.
                                  IV

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                                ABSTRACT

     In an effort to understand elementary reactions of importance in

smog, we have carried out a three-part investigation: (1)  experimental

determinations of certain elementary reaction rate constants, (2)  develop-

ment of general techniques for estimating elementary reaction rate

constants, and (3) estimation of rate parameters for many reactions

important in smog.

     The experimental studies determined rate constants for the following

reactions:
                     CH3CH2CH2ON02   1±   CH3CH2CH20 + N02
                                   -a
                                    b
                           t-BuONO   ;»   t-BuO + NO
                                   -b

                          CH3OOCH3   £   2CH30
                                   -c

                    CH3  + CH3OOCH3   ^   CH3OH + CH2OOCH3


                        CH30 + N02   5   CH3ONO2
                                   (M)

                        CH3O + N02   £  CH2O + HONO


                         CH30 + 02   *  CH20 + H02


     Specific estimated  rate constants  included the following reactions:

          (1)  Decomposition of alkoxy  radicals

          (2)  Isomerization of alkoxy  radicals

          (3)  Reactions of alkoxy  radicals with oxygen
                                      (M)
          (4)  The reaction H02 + NO2  ^  HO2NO2

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                              CONTENTS

Preface	   i i i
Abstract  	     V
Figures	    IX
Tables	    .x
                                                                 XT.1
Abbreviations and Symbols 	     '
Acknowledgments	XI11
   1.  Introduction	     1
   2.  Conclusions and Recommendations  	     3
   3.  Experimental Studies 	     5
         A.  The Very Low-Pressure Pyrolysis  (VLPP)  of
             n-Propyl Nitrate, tert-Butyl Nitrite, and
             Methyl Nitrite.  Rate Constants  for Some
             Alkoxy Radical Reactions 	     5
                  Experimental  	     6
                  Results—n-Propyl Nitrate  	     8
                  Results—tert-Butyl Nitrite	    10
                  Results—Methyl  Nitrite  	    11
                  Results—Methyl  Peroxide and N02	    11
                  Discussion	    12
                  Thermochemistry  	    19
         B.  The Decomposition of  Dimethyl Peroxide  and
             the Rate Constant for CH3O + 02  -* CH20  + HO2  ...    20
                  Experimental  	    23
                  Results and  Discussion   	    26
                       Dimethyl Peroxide Decomposition   ....    26
                       Dimethyl Peroxide with Added  N02  ....    32
                       Dimethyl Peroxide with Added  NOg  and 02 .    42
                  Summary	    50

   4.  Estimation Methods   	    51
         A.  Methods for the Estimation of Rate Parameters   .  .    51
                  Transition State Theory  	    52
                  A-Factors and Entropies of  Activation  ....    54
                  A-Factors for Metathesis Reactions  	    60
                  Addition Reactions  	    68
                  Recombination Reactions Involving  Atoms  ...    71
                  Activation Energies 	    77
                                Vll

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         B.  Rate Parameter Evaluation and  Estimates   	    80
                  Alkoxyl Radical Decomposition Reactions  ...    81
                  Alkoxyl Radical Reactions with Oxygen  ....    89
                  Alkoxyl Radical Isomerization Reactions  ...    92
                  Reaction of NO2 with HO2   	    96
                  Simulations of Smog Chamber Experiments  .  .  .    102
                       Reactions of n-Butane  	    104
                       Reactions of Propene   	    Ill
                       Conclusions	    113
References and Footnotes  	    116

Appendix A:  VLPP Unimolecular Rate Theory	    123
                                 vm

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FIGURES
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15

16

17
18

19
20
21

nPrON02 Pyrolysis 	
tBuONO Pyrolysis 	
Schematic Diagram of Apparatus 	
Decomposition of Initially Pure DMP 	
Arrhenius Plot Summarizing Data for DMP Decomposition. .
Decomposition of DMP with Added NO2 	
Gas Chromatography Results Demonstrating Mass Balance. .
-kjj"1 (dP/dt) vs. [DMP]0 for Four Temperatures 	
Decomposition of DMP with Added NO2 and 02 	
Arrhenius Plot of Data for k17 	
t-BuO1 H Me + Acetone 	
EtO' H Me + CH20 	
i-PrO- M, Me + MeCHO 	
s-BuO- 51 Et + MeCHO 	
Correlation Between Activation Energy E and
Enthalpy of Reaction ^HR 	
Falloff Calculated by RRKM Theory as a Function
of Activation Energy for the Reaction HO2NO2 -• HO2 + NO2

(a) Simulation of Run EC-41 in Reference 90 	
(b) Simulation of Run EC-41 as in (a) 	
Simulation of Run EC-41 in Reference 90 	
Reactions of Propene 	
Simulation of Run EC-121 in Reference 90 	
Appendix: VLPP Unimolecular Weight Theory 	
Page
9
9
24
28
30
34
36
38
43
48
83
83
84
84

86

101
105
108
108
109
112
114
123
   IX

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                               TABLES

Number                                                          Page

    I  Reactor Parameters 	       7

   II  Decomposition of Dimethyl Peroxide in the
         Presence of Nitrogen Dioxide 	      13

  III  Molecular Parameters Used for RRKM Calculations;
         Molecular Parameters for n-PrON02 and tert-BuONO  .  .      14

   IV  Thermochemical Quantities  	      15

    V  Rate Constants	      15

   VI  Rate Constants for Computer Calculation  	      31

  VII  Dimethyl Peroxide Rate Constants 	      31

 VIII  Data Summary for MeO + O2 - H02  + CH2O	      46

   IX  Standard Entropies and Heat Capacities at  300°K
         of Some Structurally Similar Molecules 	      57

    X  Standard Entropies and Heat Capacities of  Some Complex
         but Structurally Similar Molecules 	      58

   XI  Standard Entropies and Heat Capacities of  Some Complex
         but Structurally Similar Molecules 	      58

  XII  Arrhenius Parameters for Some Metathesis Reactions
         Involving H-Atoms  	      62

 XIII  Arrhenius Parameters for Metathesis Reactions
         Involving Atoms  	      63

  XIV  Arrhenius Parameters for Some Metathesis
         Reactions of Radicals  	      66

   XV  Arrhenius Parameters for Some Addition Reactions
         of Atoms and Radicals to Pi Bonds	      69

  XVI  Experimental Values for RO' Decomposition  Rates  ...      82

 XVII  Estimated RO' Decomposition Rates	      87
XVIII  Estimates: RO' + O2 Reactions	      91
                                x

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Number

   XIX  RO' Isomerization Reactions—Estimation
          Procedure	     94

    XX  Estimated RO' Isomerization Reaction Rates 	     95

   XXI  Frequency Assignment for H02N02  	     98

  XXII  RRKM Calculated k/koo for H02NO2 Decomposition	     99
                                 xi

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                   LIST OF ABBREVIATIONS AND SYMBOLS


BuO   - Butoxy Free Radical

BMP   - Dimethyl Peroxide (CH3OOCH3)

EtO   - Ethoxy Free Radical

Me    - Methyl Free Radical or Substituent Group

MeO   - Methoxy Free Radical

Omega (cu) - Collision Frequency

PrO   - Propoxy Free Radical

RO    - Alkoxy (Alkoxyl) Free Radical

RRKM  - Rice, Ramsperger, Kassell, and Marcus Theory of
        Unimolecular Reaction Rate

VLPP  - Very Low-Pressure Pyrolysis Experimental Technique
                                  xii

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                           ACKNOWLEDGMENTS








      Thanks go to Karan Lewis  for  preparing many batches of dimethyl




peroxide and to Dr. L.  Batt,  H. Niki, and J. G. Calvert for permission




to use some of their respective results prior to publication.
                                  xm"

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                               SECTION  1





                              INTRODUCTION






      To develop an explicit mechanism for photochemical smog formation,



it is desirable to have experimental determinations of elementary reaction



rate constants.  In the absence of such experimental data, estimation



techniques must be developed and utilized for estimating appropriate rate



parameters.   This report summarizes efforts made in both these areas.





      The experimental studies reported below were conducted to elucidate



the chemical reactions of alkoxyl radicals in the polluted atmosphere.1



These radicals are present, not only in the atmosphere, but also in flames



and combustion processes where they are potential chain carriers and



propagators.





      Alkoxy radical rates with the free radical traps, nitric oxide and



nitrogen dioxide, had been reported2a to be about two orders of magnitude



slower than for other similar reactions.2*5  An investigation was under-



taken to test this unexpected result, and it is described in Section 3.A



of this report.





      Another reaction of particular importance is that of alkoxyl radicals



with molecular oxygen.  The prototype alkoxy radical —CH3O— was used to



determine the rate constant in a study described in Section 3.B.  This




reaction is important in the oxidation of nitric oxide to form NO



according to the following sequence:





                           RH + OH  -»  R + H20



                            R + 02  $i  R02



                          RO2 + NO  -  RO + N02

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                            RO + O2 -*  HO2 + carbonyl

                          HO2  + NO  -  OH + NO2



      Other reactions of alkoxyl radicals can compete under certain

circumstances, and their rates must be estimated to achieve formulation

of a proper chemical mechanism.   General procedures for estimating rate

constants are described in  Section 4.A, and specific applications are

presented in the remaining sections.


      Alkoxyl radicals larger than methoxy can undergo ^-cleavage, and

the rates for such processes were estimated on the basis of data in the

literature, as described in Section 4.B.  For still larger alkoxy free

radicals, isomerization reactions are possible,  leading to the sequential

oxidation and degradation of hydrocarbons (Section 4.B).  The relative

rates of these competing processes are important in developing an explicit

reaction mechanism, and the resulting mechanism appears to be a relatively

good representation of reality.

                                                                 M
      A reaction for which virtually no data exists is H02 + N02 ^ HOON02 .

The technique described in Section 4.A was used to estimate the forward

and back rates of this reaction, and the sensitivity of the reaction

mechanism to variations of these rates are presented in Section 4 .B .


      Each section of this report contains a detailed discussion of the

background behind each rate, along with a thorough description of the

experimental technique or estimation procedure used and a discussion of

the result.

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                               SECTION 2




                    CONCLUSIONS AND RECOMMENDATIONS






     In the course of this work, a number of elementary reaction rate



parameters have been measured :
     (a)  CH3CH2CH2ON02     CH3CH2CH2O + N02



          log ka(sec-1)  =  16.5 - 40.0 kcal mole'1 /2. 3 RT



          log k_a(M-J s-1)  =  9.5


                   b
     (b)  t-BuONO  &  t-BuO + NO

                  ~b

          log kb (sec"1) = 15.8 - 39.3 kcal mole-1 /2 . 3 RT



          log k  (M-1 s-1) =  9.8
                b



     (c)  CH3OOCH3   £  2CH30

                   ~c

          log k_ (sec-1)  = (15.7 ±0.5) - (37.1 ± 0.9) kcal mole-V2.3 RT
               c


               -c
log k_c(M-1 s-1)  =  9.7 ±.0.5
     (d)   CH3  + CH3OOCH3   -  CH3OH + CH2OOCH3



          kd(400 K)  w 5 x 104 M-1 s~l




     (e)   CH0 + N0    "  CHON0
     (f)   CH30 + N02   -  CH2O + HONO



          k./k  = 0.30 + 0.05
           i   e        ~~
          If log ke(M~1  s-1)  = 9.8 ± 0.5,  then log kf(M~1 s-1)  = 9.3 ± 0.5




     (g)   CH30 + 02   -  CH20  + H02



          log kg(M-1  s-1)  = (8.5 ± 1.5)  - (4.0 ± 2.8)  kcal mole-1/2.3 RT




     The  rate parameters for  reaction (g)  are the most uncertain, and



 further  investigations  are desirable.

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     In addition to the experimental determination of rate constants,  an

effort has been made to develop general techniques for estimating unknown
rate constants by using data from analogous reactions.  Applications of
these techniques have been quite successful, and their utility has been

demonstrated for the following reactions:

     (1)  Decomposition of alkoxy radicals

     (2)  Isomerization of alkoxy radicals

     (3)  Reactions of alkoxy radicals with oxygen
                                  M
     (4)  The reaction H02 + N02  &  HOONO2


     Application of the estimated rate constants to butane and propene

smog chamber experiments shows fair agreement and indicates sensitive

areas for further work:

     (1)  Experimental determination of the rate parameters
          for HOON02 decomposition and association.

     (2)  Experimental determination of the photolysis rates
          of aldehydes and ketones in oxygen gas.

     (3)  Experimental determination of the products of the
          reaction of olefins with OH, 0,  and 03 under
          conditions of atmospheric interest.

     Although a great effort has been expended to understand photochemical
smog formation, the phenomenon is so complex that much work remains to be
done.  Until more experimental data become available, the estimation
technique described in this report will play an important role.

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                               SECTION  3

                          EXPERIMENTAL STUDIES


A.   THE VERY LOW-PRESSURE PYROLYSIS (VLPP) OF n-PROPYL NITRATE,
     tert-BUTYL NITRITE, AND METHYL NITRITE.  RATE CONSTANTS FOR
     SOME ALKOXY RADICAL REACTIONS

     Although alkoxy radicals play a central role in the oxidative degrad-
ation of hydrocarbons, few absolute rate constants of reactions involving
these radicals have been reported in the literature.  The reasons for this
situation include their lack of distinctive spectral features, high
reactivity, and complexities introduced into most systems due to multiple
pathways available for their decomposition and secondary reactions of
products.  This situation has recently become more acute because of the

use of alkoxy rate constants in smog-modeling studies,1 and the assignment
of certain rates, e.g., that for the reaction leading to PAN, on the basis
of the former.

     We initially had hoped to generate methoxy radicals in a VLPP reactor
and directly observe their reaction rate with oxygen.  (Higher alkoxy
radicals undergo 3-cleavage under these conditions—see Section 4.1., this
report.)  A variety of precursors, including dimethyl peroxide, methyl
nitrite, methyl hyponitrite, and methyl t-butyl peroxide, were decomposed
between 400°K and 800°K, and with quartz, carbon, Teflon, and boric acid
coated surfaces.  A small signal at m/e = 31 (at low ionization voltage)
was observed when methyl t-butyl peroxide was decomposed in a boric acid
coated reactor, but the intensity was too low to be useful.

     The rate constant for a reaction X + OR -» ROX can be calculated from

the rate of reverse reaction if the thermodynamic parameters are known.

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This method was used by Gray, Shaw, and Thynne2a to derive recombination



rates for CH3O + NO and CH3O + N02.  These,  however,  were based on rates



for the reverse reactions which have been questioned.^





     By pyrolysis of tert-butyl nitrite and  n-propyl nitrate we have



derived recombination rates that are ~ 102 higher than the earlier values.



Recently Batt, McCulloch, and Milne3 in a paper on several nitrites



reported results for tert-butyl nitrite pyrolysis by a separate technique



that are in excellent agreement with ours.





     In a separate study with a conventional static system,  we determined



the yield of methyl nitrate from methyl peroxide and N02  as a function of



total pressure, in order to determine whether the reaction of methoxy



radicals with NO2 is in the high-pressure region at atmospheric pressure.






Experimental





     n-Propyl nitrate (Eastman Kodak) and tert-butyl nitrite (Frinton



Laboratories) were fractionally distilled on a vacuum line.  The center



1/3 was stored in a large bulb wrapped in Al foil.  Methyl nitrate was



synthesized on 1/10 the scale reported by Delepine4 and fractionally dis-



tilled as above.  Dimethyl peroxide was synthesized by the procedure of



Hanst and Calvert5 and fractionally distilled to remove dimethyl ether



(m/e 46).  The gas detonated twice during handling and transfer, though at



low pressures in a seasoned vessel it was stable for weeks.  Methyl nitrite



and methyl-d3 nitrite were synthesized by adding 200 p,l of 25% by volume



H2S04 in water to the requisite alcohols (1  cc) and excess NaNO2 at —78°



and distilling the product into a bulb on a  vacuum line.6  Other reagents



and gases were commercial samples.

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     The static system for the methoxy radical-NO2 work has been described.7

Product analysis was accomplished by glc (F and M Model 720, thermal conduc-
tivity detector, 10 ft. x 0.25 in. column of 20% di-(2-ethyl hexyl)sebacate

on 60-80 M chromasorb at 25°; detector at 100°).  Seven percent of the reaction

mixture was removed with each aliquot, and 42% of the aliquot was swept onto

the glc column.  The peak areas were related to concentrations in the reactor

with appropriate factors and a linear calibration curve made from peak areas

of various pressures of pure CH3ONO2.

     The theory and practice of the VLPP technique have been described
previously.8  Essentially this involves the pyrolysis of a gas flowing through

a heated reactor with three different possible apertures (1-mm, 3-mm, and 10-mm)

diameters).  The pressure of the gas in the reactor is very low (~ 0.1-1.0 JJL) ,

such that the flow is molecular, gas-gas collisions are few and most secondary

reactions are eliminated.  The characteristics of the reactor are given in

Table I, and the exact VLPP unimolecular rate theory is presented in Appendix A,

where it is shown that ordinary RRKM theory is adequate.


                        TABLE I.  Reactor Parameters

   Volume,  V = 130 cm3; Surface Area, A^, = 160 cm2; Collision Frequency, u> =
                        4.48 x 103 (T/M)1/2 sec-1
   Aperture Diameter (cm)         0.115          0.305          0.995

   kg/sec-1                       0.4 (T/M)1/V!   1.8 (T/M)1/2  12 (T/M)1/2

   Collision Number = Z          11,200          2,470           387

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Results—n-Propyl Nitrate

     Rate constants for the unimolecular disappearance were obtained for
n-propyl nitrate over a 220° temperature range, and with a 100-fold vari-
ation in flow rates.  The M-29 peak at 76 amu was monitored (see Figure 1).

     The complete reaction is assumed to involve P-scission or isomerization:

                       n-CH2CH2ON02  -  n-CH3CH2CH2O' + NO2            (1)
                        CH3CH2CH20'  -*  CH3CH2'+CH20
                                     -  'CH2CH2CH2OH  -  C2H4 + tH2OH
of n-propoxy and subsequent reactions, perhaps on the walls, between N02 ,
formaldehyde and ethyl radicals.  Due to the spectral similarity of the
products we did not analyze quantitatively for them in this case, although
intense signals were observed at the masses where they appear.  We did show
quantitatively in two runs that propionaldehyde (yield < 10%) and propylene
(yield < 3.7%) were not significant products.  This observation indicates
that neither of two anti-Markovnikov reactions were occurring:

                    n-CH3CH2CH2ON02  -  CH3CH=CH2 + HON02
                                     -  CH3CH2CH=0  + HONO

      That P-scission (or isomerization followed by scission)  is the predom-
 inant fate of n-propoxy can be determined from an RRKM  calculation,9  Using
 values of the Arrhenius parameters determined recently  by Batt   et  al.,3  and
 a value of s = (C°-4R)/R for the number of "effective oscillators," the
 values for k(3-scission)  are much greater than the escape rate  constant.
 B:iU :|  et al.  report log k ~ 16-17/6.  For nPrO',10 Cp ~ 33;  thus, s  = 12.5,
 B = E/RT = 12 at 700°K, and D = log A, log uu ~ 16 - 4 = 12 under VLPP  condi-
 tions,  k/k^ ~ 8 x 10~8 , and thus k ~ 400 sec"1 , which  is rapid compared  to
 escape from the reactor.  The parameters  for isomerization are  not  as  well
 known, but if we estimate log kisom ~ 12-12/9, this reaction followed  by
 scission would precede escape as well.

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  >>  O  O   f-
 i-i   o  t-   oo
  O   N  'J1   CO
 O
 cA
•H
 03


rH   O  O   t-
 O   O  t*   00

 fc   N.  «   «

ft   rH  (M
O
s
%
o
     II

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Results—tert-Butyl Nitrite






     Rate constants for the unimolecular disappearance of t-BuONO were



obtained over a 240° temperature range and with a 100-fold variation in



Ilow rates.  The peak at M-15 (88 amu) was monitored.





     Above 650°K the data lie on a smooth curve of the type expected in



a unimolecular homogeneous process (Figure 2).   Between 525 and 650°K



the rates are relatively too fast and exhibit considerable scatter.





     At the higher temperature we observe fragments at m/e 58, 43, and



15, corresponding to the reactions:






                         tert-BuONO  -  tert-BuO + NO                 (2)



                           tert-BuO  -  CH3COCH3 + CH3






     At the lower temperatures no methyl radicals were observed, and the



principal organic product is isobutylene:







                         tert-BuONO  -  HONO + (CH3)2C=CH2






Batt and coworkers3 have also reported this reaction.  A significant



signal at m/e 59 in the product spectrum was ascribed to tert-butyl alcohol,



though the yield was measured as only 1.67o in one case.  Under the reaction



conditions, tert-butanol decomposed to give isobutylene (kun^ =1.5 sec"1



at 672°K, Z = 20,000) .





     RRKM curves were accordingly fitted to the data >650°K, and the presence



of small side reactions does not affect the result for the alkoxy forming



reaction.
                                    10

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Results—Methyl Nitrite





     The  decomposition  of methyl nitrite was studied briefly in a search



 for  methoxy  radicals.   At 650°K we observed intense signals at m/e 30 and 31



 with low-ionizing  voltage.  Either of  two reactions were considered possible;






                             CH3ONO  - CH30 + NO



                                        m/e 31  30





                                     - CH20 + HNO



                                        m/e 30  31






     To resolve  the question we prepared methyl-d3 nitrite and found under



 these conditions product signals at m/e 30, and 32, with a smaller increase



 at m/e 36  (CD3OD).   A  signal at m/e 34, corresponding to CD3O, did not



 appear.
     At 650°K methyl nitrite gave a 42% yield of methanol (Z = 200, 3 x 1016




                           uni
molec/sec).   The value of k  ± was 20 sec'1.   From Batt's3  data,  we predict
 k«5o K = 93 sec"1 for the fission into RO and NO, and RRK calculations indi-
 CO


 cate kuni/k  is about 10~5, so we cannot be observing a homogeneous process.






Results—Methyl Peroxide and NO9





     At two temperatures, 121° and 163°K methoxy radicals, produced thermally



 from dimethyl peroxide, give methyl nitrate by coupling with NO2 in the system,



 An  alternate reaction is disproportionation:
                        CH3OOCH3	..  2CH30





                      CH30 + N02  —~*-  CH3ON02





                                  _—	*.  CH20 + HONO
                                   11

-------
At  the reaction temperatures NO2 reacts further with formaldehyde.  There is




some scatter in the data in Table II, particularly at 163°, where  the



reaction was carried  to greater conversion, but a trend to higher  yields



of  CH3ON02 as  the  total pressure rises  is  indicated at both temperatures.



When we attempted  to  pressurize a mixture  of peroxide and N02 at 163°



with air, the  reaction vessel was destroyed in an explosion.








Discussion






     The frequencies  of the molecules and  activated complexes are  given



in  Table III.  These  provide the input  for a computer program based on



the RRKM theory, which computes values  of  the apparent first-order rate



constant as a  function of  pressure and  temperature for various values



of  the critical energy  (activation energy  at 0°K).  Frequencies in the



molecule were  selected  to  give  total entropies at 300°K, in agreement



with experimental  data or  results obtained by group additivity.  The



experimental  rate  constants  (ky^) over a  range of temperatures and the



predicted curves appear in the  figures.  The frequencies for the complex



 found  in Table III were actually selected  to give a model transition



 state  which would, in turn,  have a value of AS* (i.e., A-factor) which



would  fit the  VLPP data when the choice of critical energy was confined



 to  a value such  that  the activation  energy at 298°K was identical  with



 the known value  of AE(298°K) for the reaction  (Table IV).





     The Arrhenius parameters which  best describe the VLPP data are



 shown  in Figures  I and 2 and in Table V.   These parameters combined with



 the known entropy  change  for the reaction  allow the calculation of the



 rate constants for the reverse  processes,  the combination of the  requisite



 alkoxy radicals  with  NO and N02.  These rate constants are also given  in



 Table  V.
                                     12

-------
TABLE II. Decomposition of dimethyl peroxide in the presence of nitrogen dioxide.
T°C
121



121


121



121




1^1




163




163





163


163





P°(torr)
Me,°2
30.5



10.0


10.5



10.0




10.0




7.0




1.6





4.8


13.5





N02
58



44.5


13.0



5.0




5.0




55.0




21.4





3.2


188.5





Other
i"*.-



—


740
torr
air

745
torr
N
1

745
torr
°z






















"a
ka + kb
0.72
0.63
0.62
0.67
0.74
0.56
0.81
0.4
0.96
1.0
1.1
0.4
0.7
0.9

0.9
0.3
0.7
0.7
0.7
0.7
0.56
0.64
0.59
0.55
0.54
0.38
0.42
0.44
0.48
0.54
0.42
0.41
0.44
0.38
0.89
0.95
0.76
0.71
0.67
0.61
Time
(min.)
14
30
45
60
40
64
105
30
51
70
90
30
50
70

90
30
50
70
90
110
3.6
11.6
28
42
55
3
6.8
15
25
33
59
17
30
101
3.1
6.6
19
32
42
51
                                       13

-------
TABLE III. Molecular parameters used for RRKM calculations; molecular parameters

                         for n-PrONO2 and fc

Frequencies, cm"1
with degeneracy











n-PrONO,
Molecule
30OO (7)
1600 (1)
1450 (4)
1350 (4)
1200 (1)
1000 (2)
1150 (4)
750 (3)
350 (4)
^50 (3)
100 (1)
50 (2)
Complex 1
3000 (7)
1600 (1)
1450 (4)
1350 (4)
1150 (5)
1000 (2)
720 (2)

125 (6)
50 (3)


Complex 2








260 (6)



tert-BuONO
Molecule
3000 (9)
16OO (1)
1400(15)
1200 (1)
1000 (3)
800 (1)
200 (3)
410 (5)
100 (4)



Complex 1
3000 (9)
1600 (1)
1400(15)
1200 (1)
1000 (2)
800 (1)
200 (3)
350 (3)
100 (6)



Complex 2







350 (2)
100 (7)



RO-NOX, A             1.46       2.46









1040 I   /(gm cm")    - -        6.10
      red



log [A(300°K)/sec-1 ]  - -       16.5
                                           14.7
                                                     1.46       3.60      	




                                                     2.93 x 10T 1.53 x 108




                                                                1.00




                                                    - -        15.8     16.3
                                     14

-------
                      TABLE IV. Thermochemical quantities.
Species
n-PrONO^
n-PrO
NO,
t-BuONO
t-BuO
NO
a
AH?
I ,2 98
- 41.6
- 9.0
7.9
- 41.0
- 22.7
21.6
Ref
c
h,e
f
g
d
f
b
oO
S298
91.1
74.0
57.3
89.6
75.0
50.3
Ref.
d
e
f
d
e
f
   0 kcal/mole.
   6 cal/mole • deg.
   c Reference (11).
   d See  "Thermochemistry" section.
   •Reference [10].
   ' Reference [12].
   • Reference [3].
   * We have chosen the value of —9.0 rather than the —9-7 listed in [103] because it is
more consistent with a large number of measurements of alkoxy compounds as well as with
a uniform RO-H bond strength of 104.0 ± 1.0 kcal/mole.
                            TABLE V.  Rate constants.
                               n-PrONO,
                                      I2  ~  n-PrO + NO2
                               t-BuONO   -  t-BuO + NO
               ^H°oo/kcal "ole-1

               as500/cal mole-1 dec-1

               log k*  -/sec-1 [VLPP]
                                    lnR*T)
                              2.3 R
               log k+00/sec-1 [Ref. 3]
     (1)

    40.5

    40.2

16.5 - 40.0/6


     6.95



     9.5
      (2)

     39.9

     35.7

15.8 - 39.3/8


      5.97



      9.8

16.3 - 40.3/6
                                       15

-------
     The combination rates given in Table V are ~ 102  higher than values



currently accepted.  The rate for t-BuO + NO is in good agreement with



the results by Batt et al.3  Phillips and Shaw,11  and  Baker and Shaw12



reported relative rates for recombination of NO and N02 with RO (R = Me,



Et, t-Bu) between 1.7 and 2.7.  The ratio k-^k^  = 10°'3 ^ 2 is in the



center of this range.





     The results from the methyl peroxide-NO2 study are in  good agreement



with those of Baker and Shaw12 who obtained ka/(k& + kb)  =  0.90 at 130°C .



Extrapolation of the data shows that the combination at 760 torr is in



its high-pressure limit, and hence that combination of larger RO radicals



with NO2 will also be pressure independent.






      The decomposition of n-propyl nitrate appears to be a uniform process



 at various temperatures, collision  numbers, and flow rates.  The rate



 constant reported here for nPrON02 decomposition was  chosen so that the



 activation energy at 298°K was Ea98 = AH298 —0.6.  Thus we find a best fit



 RRKM value of log k /sec'1 = 16.5 — 40.0/9.  There is a value reported in



 reference 2a of log k^/sec-1 =14.7 - 36.9/9.  if we  change frequencies in



 the transition state to produce an A-factor of log A/sec-1 = 14.7, we find



 that E  = 37.7 kcal/mole (Figure 1).  Thus we cannot really distinguish



 between these values from the VLPP data alone, but require the values of



 AHt from other sources, as well as the increasing evidence that the combin-



 ation of alkoxy radical with NO2 would have to be higher than the value of



 log k-j/M-1 sec-1 =7.7 which would follow from the lower A-f actor.





      The rate constant for tBuONO decomposition was evaluated in the same



 way as  above.  The data could be equally well fitted by the parameters of



 reference 3 (Figure 2), and since the value of AH298  is uncertain by at



 least ± 1 kcal/mole, no distinction is possible.
                                    16

-------
   The scattered points in the VLPP plot for tert-butyl nitrite at the low


temperature end, as well as the isobutene formation in that temperature range,


indicate that a surface-catalyzed process is operative that produces nitrous


acid and isobutene.  In an earlier study of 1- and 2-nitropropane pyrolysis13


it was found that nitrous acid decomposed under VLPP conditions,  even though


it could not have occurred in a homogeneous manner.  We suggest that tert-butyl


nitrite decomposition is autocatalytic in the low-temperature range, in that


acid produced in the P-scission is absorbed onto the walls, where it both


decomposes and catalyzes elimination  of more HONO.  Surface effects for


RONO have been described by Batt  et al.3 and the decomposition of tert-


butanol in our system to give isobutene must be a catalyzed process,


because the homogeneous rate is prohibitively slow.  The origin of tert-


butanol from tert-butyl nitrite is not clear.  It could arise from H-


abstraction from walls or HONO by tert-butoxy, or by a surface-catalyzed


hydrolysis of the nitrite by water in equilibrium with nitrous  acid.



     The decomposition of methyl nitrite was not studied extensively.  The


NO and HNO may arise by homogeneous or multistep mechanisms; the  falloff


for this small molecule [o.3, assuming log (k /sec'1)  = 15.6 -  41.1/9],


                                    r
                             CH3ONO  -  CH20 + HNO


                                     ^  CH30 + NO

                                    t
                         CH30 + HNO  -  CH3OH + NO


                          CH30 + NO  ^  CH2O + HNO




is much less than predicted (10~5) , and the process is probably wall catalyzed.


Methanol can arise by two mechanisms as discussed for t-BuONO above.
                                17

-------
     In a relative rate study, Wiebe  et al. 20 have concluded that for

the reactions:

                                     3
                          CH30 + 02  -  CH20 + H02                   (3)
                                     4
                          CH30 + NO  -*  CH3ONO                       (4)


                              k3/k4  =  5.5 x 10-5 at 25°C


If we take k4 to be the same  as  k_2  proposed in  this work  (i.e.,  k4  =  109 •8

M-1 sec-1) , then k3 = 1.7 x 10s M-1 sec"1 .  Heicklen has estimated k3 as

1Q7.6-6/6 M_i sec-i _ io3>* at 25°C.  The importance of measuring k3 is

underscored.  Demerjian  et al.x pointed out that a ratio of k3/k5 = 4.9 x 10~5

is compatible with CH3ONO2 formation in smog chamber studies:

                                     5
                         CH30 + N02  -  CH3ON02                      (5)



If k5 is taken as ~ k_j of this study (i.e., k5 = 109*5 M'1 sec'1), this

would also make k3 ~ 105 M"1 sec-1 .
                                 18

-------
Thermochemi stry





     Entropy of nPrONO2;






     The value  used,  91.1 cal/mole-deg was computed from group additivity14



by assigning  the value 72.3 cal/mole-deg to CH3ONO2,  in agreement with Stull



et al.,15 and adding twice the value of the group C-(C).,(H)2 which is 9.42



cal/mole-deg  [i.e., C-(C)(0)(H)2 = C-(C)2(H)2].






     Entropy  of tBuONO:




     The entropy of tBuONO may be calculated from group additivity if a value



for the group 0-(C)(N=O)  can be found.  This, in turn, is found from the



entropy of CH3ONO whose value is in some dispute.15   The value16 S°98(CH3ONO) =



69.7 cal/mole-deg has been chosen.  This leads to S°98(tBuONO)  = 90.4



cal/mole-deg.





     The entropy of tBuONO can also be calculated from the entropy of 2,2-



dimethylpentene-1 by correcting for the difference between CH3ONO and butene-1.



This yields a value of 88.7 cal/mole-deg, and we have chosen 89.6 cal/mole-deg



as the  best choice.







     Heat  of Formation of  tBuO:



     The value AHf  oo(tBuO) = 21.6 kcal/mole found  in most recent references3'10
                 •*- 9 '^ ™ 8


comes from the activation energy of the decomposition of ditertiary butyl



peroxide,17 and the heat  of formation of the same compound.16  The value in



Reference 18  of AHf    (t-C4H90)^  = -81.5 kcal/mole  is only correct if the
                   I 2 9 8


heat of vaporization used therein is also correct. Two values  exist19 for



AHvap,  and the second value gives AHf(t-C4H90)2  = -83.4 kcal/mole which yields



AHf(tDuO)  =-22.7 kcal/mole.
                                  19

-------
B .   THE DECOMPOSITION OF DIMETHYL PEROXIDE AND THE RATE CONSTANT
     FOR CH30 + 02 - CH20 + H02
      The  methoxy radical  (MeO)  is  a  ubiquitous  species  present in the
 atmosphere  as  well  as  in  flames and  combustion  processes  where it is
 potentially active  as  a chain-carrier and  propagator.   A  reaction of
 particular  importance  is  that of methoxy radicals  with  molecular oxygen.
 In the polluted troposphere that reaction  plays an important role in
 the oxidation  of nitric oxide according to the  following  sequence of
 reactions:21
                           CH4  +  OH -  CH3  +  H20
                           CH3  + 02      CH302
                         CH302  + NO -  CH30 + N02

                          CH30  + 02 -»  H02  + CH20                     (17)
                           H02  + NO  -«  OH + NO2
                                   etc.
       Not included in this sequence are two reactions  which can compete
  with reaction (l?) under certain circumstances:

                          CH30 + NO  "  CH3ONO                      (14a)
                                     M
                         CH30 + N02  -•  CH3ON02                     (12a)

  It is desirable that absolute rate constants for reactions (17), (14a),
  and Cl2a)be obtained by direct observation.  Unfortunately,  the detection
  of MeO is difficult, necessitating the use of indirect techniques  which
  can give the rate constants with as little attendant  uncertainty as
  possible.  Since relative measurements are necessary  it is advantageous
                                    20

-------
 to  choose  either  reaction  (14a) or (12a) as  the  reference reaction,  since
 these  reactions are  also of importance in  the  troposphere.
     The reverse  of  reaction (14a) was  the  subject of a recent and
 thorough study by Batt  and coworkers3  who  obtained Arrhenius parameters
 for the unimolecular decomposition of  methyl nitrite.   Using the ex-
 perimental parameters and  the equilibrium  constant for the  reaction, they
 then deduced  the  absolute  rate  constant  for the  forward direction  of
 reaction  (14a) .
     Reaction (12a) has  been studied by a number  of investigators3°>11> l*
 who have obtained rate  constant ratios kl2a/ki4a Although the experimental
 values do  not agree  exactly,  the net uncertainty in log k.    is only
 about ± 0.3.  This point will be discussed in  more detail later.
     The rate constant  for reaction (17) has never been measured di-
 rectly, and the rate constant ratio k17/k14 has  been obtained only at
 room temperature.20  For our study,  we  decided  to measure the ratio
k7/k14  as a  function of temperature in  order  to obtain the Arrhenius
 parameters for the reaction.  We chose reaction  (I2a)because N02 is
 stable in  an  oxygen  atmosphere,  and because the  activation  energy  of
 reaction (I2a) is  about  zero.2   Since there can also be uncertainties due
 to  an assumed mechanism, we have made  a  considerable effort to  understand
 the reaction  system  as  thoroughly as possible  in order to reduce conse-
 quent uncertainties  in  the resulting rate  constant.
     Dimethyl peroxide  (DMP)  was chosen  as the precursor for producing
 MeO since  it  decomposes cleanly  and at  relatively low temperatures
 and it has been well  studied  before.22!23.5  To  understand the chemistry
 as  thoroughly as  possible,  numerous experiments  and analyses were  carried
 out in three  stages:  decomposition of  pure DMP,  decomposition of DMP
 in  the presence of N02, and decomposition  of DMP in the presence
                                   21

-------
of added NO2 and 02.  The results we have obtained are entirely con-



sistent with those from earlier studies of DMP decomposition, and differ



only slightly from earlier investigations of DMP decomposing in the



presence of added N02.2a>11,12 As a result, we feel that the value we



obtain for k17  is relatively free of errors arising from an



erroneous reaction mechanism.




     In the next section, the experimental techniques are described,



followed by a section on Results and Discussion that is divided into



three parts: 1) Pure DMP, 2) DMP + NO2, and 3) DMP + N02 + 02.
                                  22

-------
Experimental





      A schematic diagram of the experimental  apparatus is shown in



 Figure 3.   The apparatus was changed from one configuration to another,



 depending  on the information needed.  Thus,  pressure measurements were



 always made, but gas chromatography was carried out only for some ex-



 periments  with DMP + N02, and in situ spectrophotometric observations



 of NO2 were made principally in the experiments with DMP + NO2 + O2.





      The experimental apparatus consisted of  a reaction vessel sur-



 rounded by an oven whose temperature was regulated to within ± 0.2°C



 by a ProportioNull temperature regulator.  The reaction vessel was



 connected  to a Validyne (Model 7D)  pressure transducer so that the



 pressure of the reaction mixture could be recorded continuously on a



 strip-chart recorder.  Also connected to this reaction vessel was an



 F & M (Model 720)  gas chromatograph fitted with a 10 ft. by 0.25 in.



 column of  20$ di-(2 ethyl hexyl)sebacate on 60-80 mesh chromasorb




 at 40°C for product analysis.  A standard vacuum line was used for mixture



 preparation and gas handling.





      For all experiments except for the In situ spectrophotometric runs,



 the reaction vessel, RV, consisted  of a double-walled pyrex vessel of



 about 200  cc.  The outer jacket of  RV could be used as the reference



 side of the pressure tranducer to reduce the  effect of minor temperature



 fluctuations, but this procedure was not really necessary and the gas-filled



 outer jacket simply served to eliminate "hot  spots" on the inner walls.



 The temperature of RV was measured  by either  a copper-constantan or



 Chromel-Alumel thermocouple.





      For the in situ measurement of NO2,  a conventional quartz cell



 (~ 500 cc) fitted  with windows and  an optical path of ~ 15 cm was  employed.







                                  23

-------
         VACUUM LINE
                 AND
       CHROMATOGRAPH
- /



OVEN
M
:\
\
i\
i CELL 1
Os
*V



n
I
i
i
i
i
I
1
1
1
1
i
^
Qv


r

TRANSDUCER


                              	J
                      /       1
LIGHT BEAM
SPECTROPHOTOMETER
                                                          SA-2554-32
        FIGURE 3  SCHEMATIC DIAGRAM OF APPARATUS
                              24

-------
 A special  oven,  incorporating a window and a mirror,  was used to house

 the cell,24  and  a Gary 15 spectrophotometer was employed to continuously
                                 o
 monitor the absorbance (at 4200 A)  due to NO2.


      Dimethyl  peroxide was prepared according to Hanst and Calvert. 5

(One explosion  occurred during preparation of DMP when the concentrated

 base was added too rapidly to the hydrogen peroxide-dimethyl sulfate

 mixture.)  The  DMP was conveniently  purified by passage through a trap

 cooled to —78°C.  This procedure gave DMP with only a trace (< 1% by

 gas chromatography)  of a single unknown impurity.  Occasionally, CH3ONO

 was present in the apparatus after  many runs had been performed.  It

 was found that the vapor pressure of DMP at —78°C (~  2 torr) was a useful

 indicator of higher-volatility impurities.


      Nitrogen  dioxide was obtained  from Matheson Gas  products, Inc.

 and purified by  bulb-to-bulb distillation.  Oxygen gas  was  also

 obtained from  Matheson.
                                  25

-------
Results and Discussion





     In the next sections, we will discuss our results in the light of



other work on dimethyl peroxide decomposition.  Since our primary ob-



jective was to evaluate rate constant k18,  we have attempted to make



a self-consistent interpretation of our data, even though our inter-



pretation differs in small ways from those in the literature.  In



some cases, the differences disappear when further considerations are



made, but in others, we feel that our results are the most consistent.







     Dimethyl Peroxide Decomposition:




     The decomposition of DMP has been studied by three different groups,



Takezaki and Takeuchi23(TT) pyrolyzed DMP in the presence of excess



methanol, which acted as a radical trap, and found that log k6/s-1 =



15.61 - (36.9 ± !.!)/» (9 = 2.3 RT in kcal/mole).






                           MeOOMe  -»  2 MeO                          (6)






In a related study,25  Takezaki and coworkers concluded that the acti-



vation energy for reaction  (7) is E? ^ 5.8 kcal/mole.






                     MeO + MeOOMe  =*  MeOH + MeOOCH2                (7a)





                         MeOOCH2   •*  MeO + CH2O                    (7b)






Since the pre-exponential factor for many methoxy radical reactions is



log [A/M"1 s"1] ~ 8.5,2a reaction  (7) is expected to lead to a chain



reaction, if no radical trap is present.
                                  26

-------
     Hanst and Calvert5  (HC)  studied  the  decomposition of DMP without



a  radical trap.  They  found  that  the  stoichiometry was given by







                            2 DMP  -  3 MeOH + CO,                (A)






and reported log kg/s"1 = 15.2 - (35.3 ± 2.5)/9, giving a  rate constant



about three times larger than that reported by TT.  The larger rate



constant is consistent with a contribution from a  chain reaction, but



HC concluded that there was no chain contribution.  On the contrary,




our results (see below) explain the discrepancy as due to  a  chain



reaction.





     In a recent study, Batt and McCullochB2(BM) studied the decomposition



of DMP using isobutane as a radical trap.  They found log  kg/s"1 =



(15.5 ± 0.5) — (37.0 ± 0.2)/9; in close agreement  with the value reported



by TT.  They also found that DMP is a "clean" thermal source of MeO



and wall reactions are not important.





     Our own experiments are best described in terms of a mechanism



consisting of reactions (6) and (7) followed by a  series of termination



reactions:





                        MeO + MeO  -*  MeOH + CH2O                  (8)





                       MeO + CH20  -  CHO + MeOH                   (9)





                        MeO + CHO  -*  MeOH + CO                   (10)





                        CHO + CHO  -  CH2O + CO                   (11)






This mechanism is consistent with the stoichiometry found by HC and



is consistent with our results, as well.





     In our experiments, we added pure DMP to the  reaction vessel and



simply observed the pressure as a function of time as shown in Figure 4

-------
                                                                 Tt
                                                                 in
                                                                 in
                                                                 (N
                                                                           00
                                                                       {H  CO  CO
                                                                       O  -H
                                                                       OT
d/dV
        28

-------
for four runs.  Typically, the rate of pressure increase, dP/dt,

is greater initially, and gradually decreases to a constant value as the

experiment progresses.  In general terms, this is due to the chain reaction

being gradually inhibited by one or more of the reaction products, i.e.,

formaldehyde.  Since the rate of reaction (9) is much greater than that

of reaction  (7) , the MeO preferentially attacks the formaldehyde to

produce the relatively inactive CHO radicals, thus partially quenching

the chain.


     We carried out a series of runs at different temperatures and

obtained data similar to that presented in Figure 4.  From the data,

we deduced k    = P   * (dP/dt)at run times greater than about 180
            obs    DMP
seconds, when the rates approach a constant value.  Despite some scatter

in the results, we found our data (Figure 5) to be very well fitted by

the expression obtained by HC: log k = 15.2 — 35.3/9.  This good agreement

confirms the consistency between pressure measurements and the spectro-

photometric measurements of HC.


     To test the proposed mechanism in detail, numerical calculations

were performed using the Gear computer program for integrating coupled

sets of stiff differential equations,2*  Reasonable estimates for the

rate constants were made (Table VI) for all reactions except for ky, which

was used as an adjustable parameter.  We experienced no difficulty in

fitting the experimental results, which indicates that the proposed

mechanism is consistent with the data.  The particular rate constants

we chose may be somewhat in error, thus the rate constant k? can

also be slightly in error.  Nonetheless, the best fits were obtained for
           4  -i -i
k7^5xlO  M  s  ,  which can be compared to that for similar reactions.

                                                                 8.5 i 0.5
     Typical A-factors for methoxy radical reactions are about 10
 -i -i                                                  -i
M  s  , giving an activation energy E7 = 7 ± 1 Kcal  mole  '  in good agree-
                                -i
ment with the E, £ 5.8 Kcal mole   deduced in Reference 25.   These values

                                  29

-------
                        (0
                                              *  §
                                               d  -P
                                               rt  x
                                                  o
                                              .M  -P
                                              •P  h

                                                  O




                                               h  (Q
30

-------
              Table VI .  Rate constants for computer calculation.

6
7
8
9
10
1 1
i2a
I2b

13
i4a
15
16

MeOOMe
MeO + OMP
MeO + MeO
MeO + CH,O
MeO + CHO
CHO + CHO
MeO + NO,
MeO + N02

HONO "
MeO + NO
MeO + NO
N02 + CHO
Reaction
•» 2 MeO
- MeO + CH4O + CH3OH
-• MeOH + CH,0
- MeOH + CHO
-• MeOH + CO
- CH20 + CO
" MeONO,
-• HONO + CH,0
mil * * '
i -; NO + f NO, + -J H20
- MeONO
- HNO + CH,0
•• HONO + CO
log ka
15.7 - 37.1/9
Adjusted
10
8 - 3/«
10
10
9.8
9.3

0.05
10.1
9.4
9
Ref
This Work
—
(b)
10
(b)
(b)
See Text
This Work

28, (b)
3
3 2O
(b)
   ' Units are as follows: unimolecular: sec-'; bimolecular: M-'-sec"1; wall reaction: sec ';
activation energies: kcal/mol.
   6 Many of these rate constants are estimates, since the computer calculations are only
meant to be used as a test of the steady-state assumptions and not a definitive simulation of the
mechanism.
              Table VII.    Dimethyl peroxide rate constants."
T (°K)
391
404
411
414
432
log (kjj /a"1)
log (k, /s->)
*<•
8.99
3.52
8.90
1.06
7.39
= (15.6 ± 0.5)e -
= (15.7 ± 0.5)8 -
,-)"
(-6)d
(-5)
(-5)
(-^4)
(-4)
(37.1 ± 0.9)e/9
(37.1 db 0.9)6/*
kg (8""1)
1.06 <-5)d
4.15 (-5)
1.05 (-4)
1.25 (-4)
8.72 (-4)

    • Uncertainties are estimated to be ± 10%.
    6 See text for definition of kt/.
    'k^=  1.18 kN.
    d Notation: 1.00(-5) =  1.00 X  10-'.
    • Uncertainties are one standard  deviation.
                                         31

-------
may be compared to log 1^ = 9.3 — 10/9 estimated by O'Neal and Richardson,27


which is about a factor of seven too low at 400°K.  Thus, we have  repro-


duced the results of HC and can explain them in terms of a reasonable


chain mechanism.






      Dimethyl Peroxide with Added NO2:



      Nitrogen dioxide is an effective radical trap and effectively


quenches the chain reaction in the pyrolysis of DMP.  As long as suffi-


cient N02 is present, the mechanism for DMP decomposition consists of


reaction (6) followed by



                                   M
                        MeO + N02  -• MeON02                        (12a)



                                   -• HONO + CH2O                   (12b)



                             HONO  - 1 NO + i N02 + 1 H20          (13)

                                     22       2


                                   M
                         MeO + NO  -• MeONO                         (14a)



                                   - CH20 + HNO                    (14b)



                        HNO + NO2  -• HONO + NO                     (15)



                       MeO + CH20  -» CHO + MeOH                    ( 9)



                        NO2 + CHO  -* HONO + CO                     (16)




      This  reaction mechanism is similar to those suggested by other

         345
authors.  '  '   Reaction (13) has been inferred to be wall-catalyzed and


to have rate constant ^3s* 0.01 sec"1 at room temperature; 28 at 400°K


it may well be somewhat faster.  Rate constants for all of these reactions


are presented in Table VII. It should be pointed out that the following
                                   32

-------
reactions have been omitted, even though they may be important when the



NO2 concentration is very low:






                      MeO + CH3OH  - MeOH + CH2OH





                    MeO + CH3ONO2  •-• MeOH + CH2ON02





                     MeO + CH3ONO  -• MeOH + CH2ONO






These reactions have been neglected  since their rates  are  unknown, but




they are expected to be unimportant  unless the NO2 concentration  falls




to a very low value.





     When the N02 has been consumed, the termination reactions mentioned



earlier as well as those listed above  become  important.  Note that if



k12. « k12    the stoichiometry  for the  reaction would be





                      BMP + 2 N02  -* 2 MeON02                     (B)






and a pressure decrease results.  When all of the N02 has been consumed,



the stoichiometry reverts to equation  (A) and a pressure increase results,



Thus the "titration endpoint" for N02 consumption is signaled by  the



change in sign of dP/dt at time f as shown in Figure  6.    Using  this



simple picture,  a rate constant k.^ can be defined:
                                                                 (C)
This equation was written assuming stoichiometry equation  (B) and



assuming all of the N02 has been consumed at time T.





      Typical experimental data for a single run are shown in Figure 6



These data qualitatively resemble the simple picture described in the



preceding paragraph.  The total pressure steadily decreases until nearly






                                  33
1
. 1 ,-,
r
2 [DMP]O
2 [DMP]O -[N02]0

-------
                                in
                                in
                                CM
                             Ol

                             2
                                                +» o
                                                •P  r-<
34

-------
all of the NO 2 has been  consumed and  then starts  to  increase.   In most
runs, the titration endpoint at T  is  very sharp and  easily  recognized.
Typical uncertainties  in T are of  the order of a  few seconds.

     Gas chromatographic analyses  for MeONO and MeON02 and  spectropho-
tometric analyses for  N02 were carried out to test the proposed mechanism
for consistency.  The  gas chromatography was slightly hampered  by the
tendency of the DMP and  MeON02 to decompose suddenly at the chromatograph
inlet.  On several occasions, the DMP decomposed  completely during gas
chromatography.  The experimental data are presented in Figure  7.  The
co-ordinates are reduced variables: the ordinate  is  the ratio of the
component concentration  to the concentration of NO2  initially present,
and the abscissa is the  reduced time, t/r.  Despite  the experimental
scatter, virtually all of the original N02 shows  up  later as MeON02 and
MeONO.  Only small quantities of MeONO were observed (~0.1 - 0.3 times
[MeON02]), but the reproducibility was poor and that  detected may have
been due to residual amounts in the inlet lines.  In any event, the ob-
served products are consistent with the proposed mechanism.  Note that
[NO2] /[NO2]0 » 0.06 for this series of runs; for another series of runs,
[N02] / N02]0 = 0.08 ± 0.03.  The relative constancy of this value may
be due to the competition of reaction (k,0^) for MeO vs reactions of MeO
                                       A A Si         • ' —
with products such as  those due to the reactions  listed above that were
omitted from the mechanism.

     According to the  simple stoichiometry equation  (B), one NO2 molecule
is consumed for each MeO radical generated.  In actual fact, however,
k  -is not greatly smaller than kl2a, and more than one methoxy  radical
is necessary to consume  each N02, implying k« > k6 by some amount due
to the effects of k^^.  Moreover, in  the simple picture, it was assumed
that [N02]  = 0, an assumption not borne out by the  data.  Thus, less
N02 has been consumed  by time T than was assumed, implying that k-, < k6
Since these effects tend to cancel, kjj ~ kg to a  first approximation
                                   35

-------
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36

-------
(below, we find kN = 0.85 kx ) .   The data are presented in Table VI,

and log kj, is plotted vs. 1/T in Figure 5, along with data from the

literature.  A more quantitative estimate of kG  can be obtained if the

effects of k12b are taken into account.

     The most obvious effect due to k12b  is that the relative slope

[DMP]"1 (dP/dt) is not equal to unity (Figures), but is ~ 0.4.  This de-

monstrates qualitatively that(l2b) is an  important reaction.  Baker and

Shaw12made measurements on the DMP + NO2  reaction system and came to the

conclusion that k12t)/k1   =0.1.   This value, however, is not consistent

with our results.

     We analyzed our data by carrying out a pseudo-steady state cal-

culation, assuming that the following species are in steady-state:

MeO, HONO, NO, and HNO.  The formaldehyde was assumed to be immune from

attack in the early and intermediate stages of the reaction.  Using these

assumptions, the rate of pressure change can be written


                    «p = _k  [DMP]kl2a"3Xkl2b                 o»
                    dt
where X = k14a/(2k14a — k14^) .   The ratio k14b/k14a has been measured

recently by two different groups to be 0.1729  and 0.18  ± 0.02.3  Using

k14b/k14c = 0.18 gives X = 0.55.

     A series of in situ spectrophotometric runs was performed to determine

[N02]  and it was found that [ N02]  = (0.08 ± 0.03) [NO2]0.   This finding,

along with the steady-state analysis allowed us to write k™ in terms

of k
where Cs is a ratio of rate constants that depends on the assumed steady

state conditions.  Using this result and the expression for (dP/dt),  the
                                  37

-------
(JJOl)    —  —
                                                     s
                                                             s
                                                             in
                                                                   CO
                                                                   w
                                                                   13
                                                     n  a.


                                                         O
                                                                   g


                                                                   I
f
                                                                            «  us
                                                                        • • o  o    •
                                                                        «  in  m  w
                                                                       o    •    • o
                                                                        r-i  n  m  N
                                                                        05  o  IH  n
                                                                        oo  ^  ^  •<#
                                                                           O
                                                                  00
                       38

-------
following expression can be written:


                 -  —  — = T DMPl  (0-92)   k*2a " ki2b           (F)
                    dt  k            C      k+~k
                         N            s     Ki2a r Ki2b

At early and intermediate times, [DMP] = [ DMP]0 and a plot of

— (dP/dt)/k  vs. [DMP]0 is expected to give a straight line.  The ex-

perimental data obtained at five different temperatures are plotted

this way in Figure 8 and the resulting straight line has a slope of

0.40 ± 0.05.  With an appropriate value of C , the ratio k  b/k

can be determined.


     For the evaluation of C , three different sets of assumptions were
                            S
made:
     1)  Initial conditions: nothing except MeO is in steady-state
         and no products have accumulated.  This is unlikely to
         be the case except for a very short period after an experiment
         is begun.


     2)  Intermediate conditions:  MeO, HONO, NO, and HNO are in
         steady-state and formaldehyde is immune from attack.
         This is a more likely case, since N02 greatly suppresses
         the MeO concentration and thereby prevents its attack
         on CH20.  The rate of N02 attack on CH2O is very slow
         at these temperatures. 30


     3)  Final conditions: MeO, HONO, NO, HNO, CH20, and CHO are
         all at steady-state.  This may be the case near the
         titration point, but the respective concentrations
         might not be the same as those calculated by the
         steady-state expressions.
                                 39

-------
     The values of the constant C  for these three cases are,  respectively:
                                 s





               C1 = 1.0                                          (G)




                    ki2a + k     X
                    kiaa
                                   2ki4a
                                              = 0.55              (I)
The corresponding values of k^^/k^  are 0.26, 0.30, and 0.29, respectively.



Since condition 1 is felt to be unlikely, we find that k12b/kl2a = 0 .30 ± 0.05





     The result that k^  v/k,  = 0.30 +. 0.05 may be compared to the value
                      1 2 O T- 2 9.


0.1 obtained by Baker and Shaw.12 Those authors depended on the  assumption



that the attack of N02  on CH20 was very fast compared to the time scale



of their experiments ( ~ 3 hrs) carried out at 403°K.  Literature values



for the rate constant,30 however, coupled with the pressures of  NO2



used by Baker and Shaw give lifetimes for CH2O decomposition on  the



order of ~ 1 .4 to ~ 2.8  hrs.  Thus, for some of their runs, a substantial



amount of CH2O may have  remained unreacted, possibly leading them to




underestimate the ratio k12b/ki2a* Thus, their results may represent a



lower limit to the actual ratio and are compatible with the ratio



obtained above .
      Using  ki2b//ki2a  = ° *3  in  e<5uation (H)  and  in  equation (E) ,  the


 expression  for  ke becomes





                               k6   =   1.18  kN                     (J)







A properly weighted least squares  analysis  of the  data gives log



 kjj/s"1 =  (15.6 ± 0.5) - (37.1 ± 0.9)/0; thus log kg/s'1 =



 (15.7 ± 0.5) -  (37.1 ± G.9)/0, in  good agreement with values obtained by TT



and BM.  At 420°K, this rate constant  is about 1.6 times that obtained by Batt



and McCulloch22and about 1.1 times that obtained by Takezaki and Takeuchi.23




                                   40

-------
One  possible  source  of  discrepancies  among  these  three sets of data



is thermal heating of the gas in the  reaction vessel due  to the exother-



micity of the reaction  itself.31  Batt and  McCulloch took special  care



to avoid generating  thermal gradients by using  low  pressures of DMP



(~ 0.5 — 5 torr) and high pressures of isobutane  (-^ 700 torr).   In the



present experiments  and in those carried out by TT, considerably higher



pressures of DMP were employed  (~ 10-50 torr and  23 torr,  respectively)



and  thermal gradients generated by the reaction could  contribute to the



rate.  In fact, shifts  of only 2°K can account  for  all  discrepancies



between the present  results and those of TT and BM.  In light  of these



considerations, we feel that the data of BM are probably  the best  ob-



tained so far for DMP decomposition.





     Aside from slight  differences in A-factors,  the present data  and



those of TT agree well  with those obtained  by BM; the  activation energies



are  37.1 ± 0.9, 36.8 ±  1.1, and 37.0 ± 0.2  Kcal mole"1, respectively.



The  consistency of these results strongly supports  the  methoxy  radical



heat of formation deduced by BM  ( AH° (MeO) = 3.8 ± 0.2 Kcal mole"1),



and  further supports their conclusion3 that values  for  the dissociation



energy D(RO — H) derived from ICR work and  electron detachment32 are



consistently  lower  by ~ 2 Kcal mole"1.





     To test the proposed mechanism and the rate  constants deduced on



the  basis of the pseudo steady state assumption, a calculation  was



carried out using the Gear computer program26 to do the time-integration



of the coupled differential equations. The  rate constants  used  are pre-



sented in Table VII, and the results of the calculation are presented



in Figure 6 along with data from one experiment.  The calculated results




seem to be in good agreement with the experiment,  essentially con-



firming the analysis.  The computer calculation shows that  the
                                   41

-------
pseudo-steady-state concentration of MeO is attained very quickly; that



of HONO comes near the middle of the run, and those of NO, HNO, and




CH2O are attained only near t/j = 1.  Thus, the "intermediate conditions"



assumed earlier are probably the closest to actual fact, but the other



sets of assumptions are not much in error.








     Dimethyl Peroxide with Added N02  and O2 :





     The experiments with DMP + N02 + 02 were carried out by placing



BMP — NO2 mixtures in the reaction vessel,  then adding  ~700 torr of O2.



The reaction was followed in situ by spectrophotometric observation of



NO2 and by measuring the total pressure as a function of time.  Data



from a typical experiment is shown in Figure 9.  The initial disturbance



due to gas mixing soon subsides and smooth curves of pressure and [N02]



are obtained.  In all runs, the pressure curves were noticeably more



"rounded" and the amounts of N02 remaining at time T were larger than



when 02 was not present.





     Only two more reactions need be added to the mechanism when O2  is



added to N02 — DMP mixtures:





                        MeO + O2  -» HO2 + CH2O                   (17)





                       H02 + NO2  -» HONO + O2                    (18)









Reaction (17) is the reaction we have been  trying to measure.   Other



termination steps are not important as long as NO2 is present.





     An "intermediate" steady-state treatment can be defined in which



pseudo-steady-states are assumed for MeO, HONO, NO,  HNO, and H02;
                                 42

-------
                               (JJOJ)
to
o
in
d
n
d
CN
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                                                               CD
                                                               n
                                                                          in
                                                                          in
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                                                                      o
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                                                                        5
                                                                        t-
                                                                                    o
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                                                                                    00
                                                                                     - «
                                                                                     NO
                                                                                    o o
                                                                                       N
                                                                                    Q •*
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                                                                                     « h

                                                                                    Q °
                                                                                    S5 -P

                                                                                    Q to
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                                                                                       II
                                                                         Q
                                                                         <

                                                                         K
                                                                         EH'
                                                                                    >  O
                                                                                       h
                                                                                       h
                                                                                       O
                                                                                       •P
                                                                                    2;  m
                                                                                    O  H
                                                                                    M   •
                                                                                    H  to
                                                                                    IH
                                                                                    CO  II
                                                                                   8
                                                                                   §§
                                                                                   QL—J
                                                                                   O5
                                                                                   O
                                                                                   I—I
                                                                                   fe
q
pj
            q
            (N
                            (JJOl)  °Nd
                                            43

-------
formaldehyde is again assumed to be immune to attack.  The rate of

pressure change can be written
     dP
     dt -  6             ki2a[NOa] + 3  kl2b[No2] + k17  [02]  X
where X = — - - — = 0.55, just as before.  At the titration point
 , (dP/dt)  = 0 and equation (K) can be rearranged to give
          T
                                                pro.]
                                                     T
                                                [02]
                                                                  (L)
This expression is sensitive to the ratio kl2b/k12  ,  justifying the care

taken earlier to determine that quantity.


     The expression for k 17 consists of three parts: 1) a stoichiometry

factor (in curly brackets), 2) rate constant ki2a and 3) experimental

values for the ratio [NO2] /[O2],  The results obtained for the  ratio

[NO2] /[O2] at several temperatures are presented in Table VII.  These
     T
ratios are subject to experimental uncertainties of about ± 15jb , as

noted in the table.  The stoichiometry factor depends on the ratios
                       3
        (= 0.18 ± 0.02) and k/k   (= 0.30 ± 0.05) and is not subject
to a large uncertainty, barring gross errors in the reaction mechanism:


                     k     k   ^
               - _    I4b   12M   = 0.31 ± 0.05                   (M)
               3
Rate constant kiaa, on the other hand, suffers from a larger uncertainty.


     Three indirect determinations of  kl2a are  reported in the literature,

Baker and Shaw12 measured the ratio k14a/kl2& =2.7 at  403°K and Phillips

and Sha* * 1 obtained  k14a/k12b = 1.8 at  363°K. However,  Baker  and Shaw
                                  44

-------
felt that their data was better since the pressure of NO2 was  more

                                             2 o
constant in their experiments.  Wiebe, et al.  measured  k14/kl2   =1.3  at


room temperature, leading to k  /k12a = 1 .1 .  Jt is possible  that  this


ratio exhibits a temperature dependence, but that is not expected to


be the case.6  A likely explanation is that unrecognized systematic


errors influenced the experimental determinations.  On the basis  of


these data, a fair estimate seems to be k,4 /k,   =2+1.



     As mentioned earlier, Batt and coworkers3 measured  the  reverse of


reaction (14a) and on the basis of their data and thermochemical cal-


culations they concluded that log (k14a /M"1 s"1! = 10.1 ± 0.4 at 300°K;


at temperatures near 400°K, the rate constant should be about  the same.


Combining their result with the ratio k14 /k12  = 2 +_ 1 , we  find  that


log fk12a/M-1 s"1  I = 9.8 ± 0.5, where the quoted uncertainty  has been


derived by a propagation of errors analysis.  Thus, the uncertainty


associated with k^  is far greater than that due to stoichiometry or


that due to random experimental errors in the ratio [N02 ] /[02].
                                                         T


     The experimental values for [NO2] /[02] are presented in Table VIII.
                                      T

A properly weighted least squares analysis of this data gives


log J[N02] /[02]  = - (0.82 ± 1.46) - (4.0 ± 2.8)/9.   When this value


is combined with the stoichiometry factor, we obtain the expression

    [    .   ]                     (4.0 ± 2.8)
log  kl7 'k12J = — (1.33 ± 1.46) -- . The rate constant ratio
    L       T                          H

itself is not subject to as much uncertainty as the individual arrhenius


parameters.  Combining the value log (k^g/M"1 s~1) = 9'8 - °*5 with tne



expression for log Ik17/k12a|, the final result is log Ik17/M~1 s"1^
     The large uncertainty in the Arrhenius parameters mainly reflects


the relatively small temperature range of our experiments; the para-


meters themselves appear to be fairly reasonable.  Our results are



                                  45

-------
                               Table VIII


                 DATA SUMMARY FOR MeO + 02  -»  HO2 + CH2O
    T, °K              103 x [N02]r/{02]a         ID'6 x k17  (NT1 s'1)
396
409
420
442
0
1
1
1
.71 J
.34 d
.26 d
.52 d
= 0
: 0
b 0
b 0
.10
.11
.10
.19
1
2
2
3
.4
.6
.5
.0
±
±
±
±
0
0
0
0
.2
.2
.2
.4
          log k17  /M"1 s'1  =  (8.5 ± 1.5)b - (4.0 + 2.8)b/9
a
 Experimental uncertainties quoted are average error.


 Uncertainties quoted are one standard deviation.
                                  46

-------
presented in Figure 10 , along with a result  (described  below) obtained

by Wiebe  et al»20as well as a line corresponding  to log  k17 =  8.5 — 4/9.

The extrapolated line clearly agrees well with the results of Wiebe  et  al,

at room temperature.

     Wiebe  et al.  deduced k17/k14a=  (5.5 ± 1.1) x 10~5 at 300°K.  Using

k14a= 1010'1 * °'4  M"1 s"1 due to Batt and  coworkers3  log

5.84 ± 0.4 at 300°K.  The authors estimated the uncertainty  to  be ±  20$,

but did not explain how they made the estimate.  Their reaction mechanism

included about twenty reactions, and  it  is  possible that  unknown systema-

tic errors have affected their results.  Despite the chances for error

in our own data and in theirs, the results  appear  to be remarkably

consistent with one another, as well as  with recent estimate!-33  for

the rate constant.

     A number of other values for k17 have  been reported  in  the litera-

ture.  Most of these, however, were obtained by using  "third generation"

methoxy radicals and a complex reaction  mechanism.  An example  of the

production of  "third generation" methoxy radicals is  described by the

sequence of reactions:
                          !heat \
                            or ( ->  CH3                            (19)
                          light)

                    CH3 + 02 + M ->  CH302 + M                      (20)

                        2 CH302  ->  2 CH30  + 02                    (21)


     Heicklen and Johnston34 and (later) Shortridge and Heicklen35 used

the reaction sequence given above to obtain values for the ratio k.^/k.,1/2
                                                                   17  8
equal to 0.020 M"1/2 s~1/2 and 0.021 M"1/2  s""1/2,  respectively,  at 300°K.

Choosing kg «» 1010 M~J s"1 leads to the  low values  of  k17  which  Heicklen

used to estimate36the arrhenius parameters  for the  reaction.  More recent

estimates33 gave a much faster rate.

                                  47

-------
                             ID
                             in
                             (N
                             i


                             (A
                                    M  g  CO
                                        
-------
     In a similar study at 373°K, Alcock and Mile37 found k17 =


1.2 x 106 M"1 s"1, in good agreement with our results.  Their data


analysis consisted of a computer simulation of the reaction mechanism,


and they found it necessary to include the reaction




                    CH302 + CH302  -» CH3OH + CH2O + O2           (22)




where k   « ^21'  Recent data obtained by Bayes  et al.38  indicate that


reaction (23)  should be considered along with reaction (20),





                         CH3 + 02  - CH20 + OH                   (23)




complicating the picture still further since other evidence8  indicates


that reaction (23) is unimportant.  A possible alternative to reaction


(22) that would also give stable products and a lower MeO yield is:




                          2 CH302  - CH3OOCH3  + 02              (24)



                                *  M
                        CH3OOCH3   - CH3OOCH3                    (25)




                                   -* 2 MeO                       (26)

                                        39

Reaction (24) is about 43.5 Kcal mole"1   exothermic  and D(MeO-OMe)  is


about 37.6 Kcal mole~1,22making  reaction (26) possible.  The way the


reactions are now written,  the yield of MeO  will be pressure-dependent.


An  alternative would be  to  assume  that the 02 carries away much of the


excess  energy, leaving mostly stabilized DMP behind and giving an even


lower yield of MeO.



     In a recent  paper,  Heicklen and coworkers40 reported  the  results of


a study on the photo-oxidation of CD3N2CD3.   They concluded  that


reactions (21), (22), and (24) occur 43%,  50%,  and 7% of the time,


respectively, in good agreement  with the  relative rate constants  deduced
                                 49

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by Alcock and Mile,37  They also concluded that k17 = (0.5 - 1.25) x 104



M"1 s"1 at 300 K, a value that is somewhat higher than those obtained



earlier,34'35 and is not inconsistent with our results.  On the other



hand, the use of "third generation" radicals necessitates very complex



data analysis and much additional work is needed if such methods are



used to obtain unambiguous methoxy radical rate constants.
Summary





     The  present  study has demonstrated  that  the  decomposition of



dimethyl  peroxide is  now well understood.  The  value  obtained  for k  =
                                                                    6


10(i5.7+0.5)-(37 .i±o.9/6) ig  consistent with those obtained by  Takezaki




and  Takeuchi23and by  Batt and McCulloch.22 Due  to the extra care taken by



Batt and  McCulloch to eliminate  the  possibility of thermal gradients,



their  determination o-f the A-factor  of kj  is  probably the  most reliable.



The  data  obtained by  Hanst and Calvert5are explained  by  invoking a chain




reaction  mechanism, and k? <=* 5 x 104 M"1 s"1  was  obtained  near 400°K.





     By adding N02 to the decomposing DMP, a  value of the  disproportion-



ation/recombination ratio for MeO +  NO2  was obtained;  k12,/k12a = 0.30 + 0.05





     The  reaction of  MeO with 02 was measured relative to  the  reaction



of MeO +  N02,  yielding log [k17/M~1s-1]  =  (8.5  ±  1.5)  -  (4.0± 2.8)/6,



where  most  of  the uncertainty in the Arrhenius  parameters  is due to



the  limited temperature range used.   The Arrhenius parameters  are quite



reasonable   and compare well with recent estimates^ however, further



work is needed to reduce the uncertainties.
                                   50

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                              SECTION  4




                          ESTIMATION METHODS








A.   METHODS FOR THE ESTIMATION OF RATE PARAMETERS




     The thrust in modern science and technology has been increasingly



to analyze complex systems at a molecular level.  To the impatient




engineer, much of this may appear to be a narcissistic infatuation  with



unimportant detail.  For the working scientist, however, who has lived



with these complexities for some time, the exhaustive examination of



just this detail is his only guarantee that he has really understood



the phenomena involved.  More important,  it is the only reliable path



he has available to him for making any continuing progress in analyzing,



diagnosing and hopefully controlling the    systems under study.





     Almost all of the technical problems facing our society today  (and



how many are not technological)  share in  common this molecular complexity.



It is strikingly evident in the subject of our current symposium, the



kinetics of atmospheric processes involved in pollution.  Although



possibly half-a-dozen elementary reactions involving O2, O3, NO, NO2,



and O atoms dominate the diurnal chemistry of the troposphere and strato-



sphere, the secondary reactions which can affect the stationary  concen-



tration of some of these species may run  into the tens, and if we include



"pollutants", into the hundreds.  The sheer volume of kinetic information



required to analyze these systems has put a large premium on theoretical



and semi-empirical methods for obtaining  rate data.  In principle,  one



would prefer to have direct experimental  measurements of the important



reactions under the prevailing atmospheric conditions of temperature,



pressure, and composition.  Practically,  this is not always attainable.



Some reactions  involving excited atoms or free radicals are just not





                                  51

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measurable by current techniques.  Others can only be measured in temper-


ature or pressure regimes very far from atmospheric (tropo- or strato-)


and need to be extrapolated with, in some cases, great uncertainty.




     It is the purpose of the present report to examine the techniques


which have been used to generate rate data from theoretical or empirical


considerations and to attempt to place some quantitative measures on


their reliability.  The reactions to be considered will be elementary


gas-phase reactions and the emphasis will be on the ones significant in


atmospheric chemistry.  For these reasons the bulk of our attention will


be given to biomolecular processes.






Transition  State Theory




     There is at present only one kinetic model with any broad claims to


generality  which can be used quantitatively to describe elementary,


chemical rate processes.   This is the model incorporated into what has


become known as Transition State Theory,



     Transition State Theory rests on a number of independent assumptions,


The first of these is that any elementary chemical reaction can be des-


cribed in statistical mechanical terms by the passage through phase space


of a complex aggregate, containing the reactant species across an energy


maximum on the potential energy surface describing the complex.  The


second and most important assumption is that the reaction complex in the


neighborhood of this maximum (i.e., the transition state) can be consid-


ered to be in thermodynamic equilibrium with the reactant species.  This


gives rise to the familiar kinetic scheme for an elementary reaction of


any order:



                          K*'                *  V*
       A + B + C +  •  •  • <   *  [A • • -B • • -C • • •] 	*~ products
                                  52

-------
with an overall rate constant k  described by:
             Rate = k*(A)(B)(C)  =  -  ——  = V*(A•. -B••«C•••)*
                                        dt

                                 =  V*K*'(A)(B)(C)                   (27)

or                           k*  =  v*K*'                            (28)



where K ' is the equilibrium constant for formation of transition state

complex (TS) from reactants, and v*  is the probability per unit time

(first-order rate constant) for decomposition of  TS into products.


     Making use of the extreraum properties of the potential energy sur-

face and the approximation that hv  < kT we can factor K '  into a product

of a partition function for the reaction coordinate (i.e.,  passage across

the maximum), kT/hv  and a remainder K* .  Hence the well known result,

independent of v :


                              k* =  (|r)K*                          (29)


or in thermodynamic  language:
                  k*  = llT=-J|e~	                               (30)


     There is no evidence that indicates that the approximation  hv  < kT

is a source of appreciable error.  It would require a very compact potential
                                        o
energy surface with a very thin ( < 0.3 A) activation energy barrier to

invalidate this approximation and no a priori calculations have so far

indicated the existence of such surfaces.


     If we confine our discussion to thermodynamic language, Transition

State Theory is a two-parameter theory, the two parameters being AS  and

AH  .  The situation is actually more complex than this since both of these


                                 53

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are temperature dependent.  Because of this latter, it is not  easy to



relate k* to the more familiar Arrhenius form, k = A exp(—E/RT) ,  except



in a limited temperature range (T = Tm ± AT).  The relation is:*1
                       E  =  AH* + RTm                               (31)
                                                                     (12)
                       A  = I 	«u- I e" 1U" "                            v«"»/

                            \  h   /




where Tm is the center of the temperature range chosen, and AH  and



AS_ are calculated at T_.  Remember that AH* and AS*, if calculated
  mm                            *


statistically, must be calculated with the "reaction coordinate" (v*)



contribution to the TS omitted.  Its contribution has already been



counted in the (kT/h) term.




     To make use of equations(31)  or  (32) requires either a total knowledge



of the potential energy surface for the reaction or an empirical knowledge



of the surface in the neighborhood of the transition state (i.e., the



barrier).  The former alternative is probably not viable for the near



future, and so we must have recourse to the latter.  To have empirical



knowledge of the potential energy surface in the neighborhood of the TS



implies that we have reliable rate data (E and A) for one or more of a



related class of reactions from which we can extract experimental values



of AH* and AS  .  This has proven a very fruitful approach and is the one



we shall now explore.






A-factors and Entropies of Activation




     Equation (32) relates directly the Arrhenius A-factor to the entropy



of activation, AS  .  Since this latter is the difference between the



entropies of reactants and transition state, and the former can be deter-



mined directly, equation (32) gives us a method for relating A-factors to
                                    54

-------
the entropy of the transition state S .   This by itself might not be too


useful a relation were it not for the circumstance that the molar entropy



of a gas-phase species is relatively insensitive to its structure.  If  we



examine the contributions to the entropy of a gas-phase species from the



different external and internal degrees  of freedom, we find the following:43
          S° ~ S°     + S°   + S°   + S°                         (33)
                trans    rot    vib    elec






Strans = 3?'° + 2 Rln (40)  + I Rln + Rln(n)              (34)






S°   [linear molecule]  = 6.9 + Rln(I/O + Rln(T/298)
 rot





[non-linear molecule] =  11.5 + Rln [ (ABC) 1/2/J ] + - Rln(T/298)







S° t [ 1-dimensional rotor] = 4.6 + Rlnd1/2/^) +- Rln(T/298)    (35)
        t                           .





where M = molecular weight in atomic mass units (AMU) ,  I = moment of



inertia about the center of gravity, ABC = product of moments of inertia



(AMU-Ang2) , a = total symmetry number, and n is the number of optical



isomers .




     The vibrational entropy consists of contributions  from each of the



internal vibrations.  Each of these is usually small compared to the


contributions from translation and rotation, and generally only the bend-



ing motions involving atoms heavier than H or D are significant in the


range 200-400°K.  The only significant (i.e., > 0.5 e.u.)  contributions


from internal modes arise from hindered internal rotations.  These can



be in the range of 2 to 5 gibbs/mole per rotor, and hence  are comparable



to the contributions from external rotations.
                                   55

-------
     Electronic contributions generally take the form of  Rln g  ,  where



ge, the electronic partition function, is usually the electronic  degener-



acy of the ground state.  For free radicals this usually  reduces  to a



contribution of Rln2 =1.4 gibbs/mole from their spin degeneracy.  In



exceptional cases of atoms, such as O, and odd radicals such as NO and  O2 ,



the electronic partition function is more complex and changes significantly



with temperature in the range of atmospheric interest 200-300°K.




     High frequencies (v i 800 cm-1) contribute less than 0.2 gibbs/mole



to S° at 300°K.  We can thus make gross errors in guessing them (± 20$)



without incurring a significant error in S°.  A frequency of 400  cm-1



will have an entropy of 1.0 e.u. at 300°K and a 10$ error in its  value



will introduce an uncertainty of ± 0.1 e.u. in S°.  This  doubles  at 200 cm"1



and triples at 100 cm-1, but only torsional motions have  frequencies in this



range.  We thus observe that in estimating S°* the chief  structural features



of interest are the moments of inertia and barriers to internal rotation.





     The moments of inertia can be guessed from simple empirical  rules



involving bond lengths and angles39and even errors of ± 10$ in the latter



will introduce uncertainties in S° of only + 0.2 e.u.  At low temperatures



it is the uncertainty in barriers to internal rotation which constitute our



chief source of error.




     The relative intensity of molar entropy to precise structural details



and to the number of H-atoms in a species is illustrated  in the following



Tables  IX, X, and XI,  which compare the molar entropies  and heat capacities



at 300°K of some structurally similar species.43
                                    56

-------
Table  IX .   Standard entropies and heat capacities at 300°K of some structurally similar molecules.5

Molecule
A H20
NH3
CH4
BH3
B CH3CH3
NH2NH2
HOOH
CH3NH2
CH3OH
BH,BH,
C°
P300
8.0
8.5
8.5
8.7
12.7
12.2
10.3
11.9
10.5
13.9
CO "
300 (int)
46.5
48.2
49.3
48.4
60.6
58.5
58.0
59.9
59.5
58.5
a
2
3
12
6
18
2
2
3
3
4
S300
45.1
46.0
44.5
44.9
54.9
57.1
56.6
57.7
57.3
55.7

aUnits of Cp and
bSSoo (intrinsic) =
S are gibbs/mol.
S^oo + Rln a.



                                                57

-------
Table X .   Standard entropies and heat capacities of some complex, but structurally similar,
                                         molecules.

Molecule C?;
A CH3CH2CH3 17
CH3OCH3 15
CH3CH2OH 15
CH3NHCH3 16
CH3CH2NHZ 17
CH3NHNH2 17
B CHF3 12
BF3 12
NF3 12
COF2 11
FN02 11
N2F2 (cis) 11
CH2=CF2 14
3oO — CO j. J?ln
•^intrinsic " A + Kut
Table XI . Standard entropies
Molecule
A COC12
CH2=CC12
CHCfcaCHCl (cis)
B C6H6 (benzene)
C5NHK (pyridine)
B3N3H6(borozole)
B303H3(boroxine)
S30o(lnt)a
.7 70.3
.8 70.4
.7 69.7
.6 69.8
.6 69.9
.0 68.8
.2 64.2
.1 64.3
.8 64.5
.3 63.3
.9 63.6
.9 63.4
.2 64.8
a; units are gibbs/mol for CL and 5° .
and heat capacities of some complex,
molecules.
Cpaoo S°00(int) a
13.8 69.2
16.1 69.7
15.6 70.8
19.7 69.2
18.8 69.1
22.0 72.1
21.0 71.6
o
18
18
3
9
3
3
3
6
3
2
2
2
2

but structurally
0
2
2
2
12
2
6
6
oO
°300
64.6
63.7
67.5
65.4
67.7
66.6
62.0
60.7
62.3
61.9
62.2
62.0
63.4

similar,
qO
"300
67.8
68.3
69.4
64.3
67.7
68.5
68.0

aco _ co JL. Diji
"intrinsic "
a; units are gibbs/mol for C% and 5°.


                                             58

-------
For convenience, the intrinsic entropies (corrected for symmetries)  are


compared, as well as the absolute entropies.   We note that  in any of the


five series of molecules compared, we would make an error less than


+ 1.0 e.u. in choosing the average in the group to represent  any one of


them.  We could do about the same for Cp and  improve the latter by mak-


ing a correction of about 0.4 e.u. for the contributions of H atoms.


This becomes a reliable method10(± 1.0 e.u.)  for assigning  C  ° and S°


to free radicals and ions.  Extensions of these methods have  been made


with about the same success to cyclic and polycyclic compounds.



     In applying these methods for estimating entropy to transition  states,


we proceed by selecting an initial structure  which would seem reasonable in


terms of the overall structural changes in the reaction. We  then calculate


a value of AS  and an A-factor (eq. 32)  and compare it with  the experimental


data.  It generally turns out that once we have "calibrated"  our intuition,


there is not too much latitude  in varying the initial structure if  the


agreement is not good.



     The largest range in S  occurs between what has been designated a


"tight" and a "loose" transition state.  A tight transition state is one


in which the bond lengths and bond angles are within 0.3 A  and 2O°,  respec-


tively, of the values which describe stable structures.  Loose transition


states which appear to occur in simple bond fission reactions only,  are


characterized by unusually long bonds between nascent free  radical centers.


These can be as much as 2.5 to 3 times the ground bond distance.  The best


documented example is the transition state for CH3»««CH3 recombination in

                                         o                   o
which the C.. .C distance is at least 3.8 A, and possibly 4.5  A, long in


comparison to a normal C-C single bond distance of 1.54 A.
                                    59

-------
A-Factors for Metathesis Reactions
     Bimolecular reactions can be divided into three categories:
        (1)  Energy transfer processes
        (2)  Metathesis reactions (atom transfer)
        (3)  Addition reactions

     Each of these is characterized by a "strong"  collision between two
discrete species and can from this point of view be looked upon as a type
of addition reaction.  We distinguish the true addition reaction from the
others by using it to characterize those exothermic reactions in which the
adduct is more stable than the reactants,  for  example, the recombination
of radicals and addition of  atoms to  double bonds.
     The formation of the transition state in a bimolecular event can be
looked upon as involving the net transformation of translational and
rotational degrees of freedom of reactants into vibrational and torsional
degrees of the complex TS.  Because of the relative magnitudes of the
entropies associated with these degrees of freedom, &S  for the process
is always negative.  It is more negative for heavy species than for light
and becomes increasingly more negative with increasing complexity of the
colliding species.
     In the reaction of a light atom, such as H or D, with a large poly-
atomic molecule, the TS complex has about the same intrinsic entropy as
the molecule, and hence  —AS* ~ S°(H) corrected for spin and symmetry.
S£88(H) = 27.4 gibbs/mole (e.u.) or 21.0 e.u. (mole/liter standard state).
Correcting for spin, Rln 2 = 1.4 e.u., and adding R for the change in
An = —1 (bimolecular event), we find AS* ~ —17.6 e.u. per atom attacked.
Since ekT/h = io13'25 sec"1 at 300°K, this would lead to a minimum A-factor
                                   60

-------
for metathesis by H-atoms of 109*5 I/mole-sec per atom attacked.   For



attack on C2H6 ,  which has six equivalent H-atoms, we would raise  this



by a factor of 6 to 1010*3.  Observed A-factors could be a power  of



10 higher than these values if the TS complex had a structure in  which



the H*«*X«*R bonds were bent and possessed a torsional mode with low



or zero internal barrier-to-rotation of the H atom.





     The observed values for H-atom metatheses, some of which are shown



in Table XII, are in excellent agreement with these conclusions.   Moreover,



the values are sufficiently above the lower limits to suggest that the



TS complexes have an H-atom which is not co-linear with the H-R bond being



attacked.  The attack of H-atoms on 1? and I2 have A-factors even  more than



a power of ten higher than the minimum values,and only a very nonlinear



TS can account for these high A-factors.   This may, in fact, be  typical



of H-atom attacks on all group V, VI, and VII elements and thus the  inverse



reactions as well.  A simple rule of thumb for H-atom metatheses  is  that



their A-factors  are io10-5i°'5 I/mole-sec.





     It would be extremely difficult to defend,on structural grounds,



A-factors (per atom) for metathesis by H-atoms which were less than  the



minimum values calculated.  Hundreds of reported rate constants 45,46,47



support these conclusions and reported A-factors which fall below these



limits must be looked upon as suspect.





     When we consider atoms heavier than H or D, the analysis is  not so



simple.  While these heavier atoms have larger translational entropies,



their TS complexes in compensation will also have increased translational



and rotational entropies and the net result is not expected to be much




different than for H-atoms.  Table  XIII shows rate parameters for heavy atom



metathesis, and  we note that again an average value of 1010'5—°'5 I/mole-sec



will bracket most of the results.
                                   61

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Table XII.  Arrhenius Parameters  for Some Metathesis Reactions Involving
            H-Atoms.
Ref .
la
.b
2
3
4a
b
5
6
7
8
Reaction
H + D2 - HD + D
H + HOH - H2 + OH
ft + F2 - HF + F
H + HC1 - H2 + Cl
H + CH4 - H2 + CH3
H + C2H6 - H2 + C2H5
H + I2 - HI + I
H + N20 - HO + N2
Tm (°K)
900
(177-477)
(300-2500)
(300-560)
(200-500)
(500-700)
(300-600)
(300-1100)
(400-465)
(450-1487)
log A
(M-1 sec-1)
10.6
10.7
10.9
11.1
10.4
10,4
11.1
11.1
11.6
10.7 ± 0.4
E
(kcal/mole)
8.0
9.4
20.5
2.4
3.5
4.2
11.9
9.7
0
13 ± 1.5
la. G.  Boato,  et al., J. Chem. Phys.,  24, 783 (1956).
 b. A.  A. Westenberg and N. de Haas, Ibid.  47,  1393  (1967).
2.  D. L. Baulch, et al., Evaluated Data for High Temperature Reactions,
    Vol. I.,  Butterworth, London (1972).
3.  R. G. Albright, A. F. Dedonov, G. K. Lavrovskaya,  I.I. Morozov, and
    V. L. Talrose, J. Chem. Phys., 50,  3632 (1969).
4a^ A. A. Westenberg and N. deHaas, J. Chem. Phys.,  48,  4405 (1968).
 b<. S. W. Benson, F. R. Cruickshank, and R. Shaw, Int.  J. Chem. Kinetics,
    _!, 29 (1969)
5.  R. R. Baldwin, D. E. Hopkins, A. C.  Norris,  and  R. W.  Walker,
    Combustion and Flame, 15, 33 (1970).

6.  R. R. Baldwin and A. J. Melvin, J.  Chem. Soc., 1785 (1964).

7.  J. H. Sullivan,  J. Chem. Phys., 30, 1292 (1959).
8.  G. Dixon-Lewis,  Sutton and Williams, J. Chem. Soc., 5724 (1965).
                                    62

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Table XIII.   Arrhenius Parameters for Metathesis Reactions Involving Atoms
Ref .
1
2
1
1
3
4
5,6
5,6
7,
8a
1
1
9
Reaction
0 + NO2 -* O2 + NO
0 + OH -* O2 + H
O + O, - 200
0 £.
O + C2H6 -» OH + C2H5
Cl + C2H6- HC1 + C2H5
Br + C2H6- HBr + C2H5
I + CH4 - HI + CH3
I + CH3I - I2 + CHj
I + CF3I - I2 + CF3
N + NO - N2 + 0
N + O2 - NO + 0
S + OCS - S2 + CO
Tm(°K)
300
300
(220-1000)
(300-650)
300
(490-590)
560
580
(350-550)
370-450
(300-5000)
300
300
log A
(M-1 sec"1)
10.0
10.3
10.08
10.4
10.6
11.0
11.7
11.4
10.9
9.6
10.2
9.3
9.0
E
(kcal/mole)
0.
0
4.6
6.4
0
14.0
33.5
20.5
17.8
16.0
0
6.3
3.6
1.  D. Garvin and R. F.  Hampson, Editors "Chemical Kinetics Data Survey,"
    VII, NBSIR 74-430, Washington, D.C. (1974).
2.  D. L. Baulch, D. D.  Drysdale, D. G. Home, and A. C. Lloyd,  Evaluated
    Data for High Temperature Reactions. I., Buttersworth, London (1972).
3.  D. D. Davis, W. Braun,  and A. M. Bass, int. J. Chem. Kinetics, £,  101  (1970).
4.  K. D.  King, D. M. Golden, and S. W. Bmson, Trans. Faraday  Soc.,  66,
    2794 (1970).
5.  D. M. Golden, R. Walsh, and S. W. Benson,  J. Amer. Chem. Soc., 87,  4053  (1965).
6.  M. C. Flowers and S. W. Benson, J. Chem. Phys., 38, 882 (1963).
7.  Amphlett and E. Whittle, Trans. Faraday Soc., 63, 2695 (1967).
8.  (a)      Lawrence, Trans. Faraday Soc., 63, 1155 (1967).

9.  R. B. Klemm and D. D. Davis, J. Phys. Chem., 28, 1138 (1974).
                                     63

-------
     The reaction of N + O2 - NO + O has a sufficiently low A-factor



to warrant further inspection.  If we assume it has a tight transition



state (N-O-O) , we can approximate the entropy of the latter by either



the value of NO2 if it is  nonlinear  or N20 if it is linear.  Starting



with the former and correcting for symmetry and spin (TS must be doublet) ,



we find AS* > -20.5 which leads to A > 109 *2 I/mole-sec, in excellent



agreement with the data.  A linear TS (NNO model) would yield a minimum



A of about 108'4 I/mole-sec from which we can conclude that if the



observed A-factor is correct, then the TS  must be bent.





     The last result makes the much larger A-factor for N + NO -• N2 + O



of some interest.  The TS complex must be a triplet and a minimum A-factor



for a tight linear transition state is 108<0 I/mole-sec, while a bent



transition state has A £ 109'° I/mole-sec.  The observed value of 1010*2



I/mole-sec suggests that in actual fact we must have the equivalent of



a very loose TS, equivalent to those effective in radical recombination.



This would be reasonable if the N••«NO interaction were attractive up



to distances of about 3.2 A on the triplet surface.





     The other  low A-factor reported in Table XII is for the reaction



S + SCO -* S2 + CO.  If we model the TS using S°nt(COCl2) = 69.2 e.u.



and correct for spin (triplet), we find A % 109*8 I/mole-sec.  There is



no plausible structure for the TS that could account for an A-factor as



small as 109a°  I/mole-sec.





     The very important atmospheric reactions  0 + NO2 -» NO + O2 and



0 + 03 -* 202  are structurally very similar.  If we assume common non-



planar transition states for both,  or planar ones with low rotation



barriers, we can simulate TS by FNO2 (Table X) with corrections for



spin and internal free rotation.  On this basis we estimate A(O + 0) >



109'9 I/mole-sec and A(0 + N02) ^ 109'8 I/mole-sec, in excellent agreement



with the data.
                                   64

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    We observe in Table XIII  a  peculiarity unique to I atoms;  that  is,  their



abstraction reactions have unusually high A-factors , much higher  in fact



than we would calculate from minimum A-factors.  For the reaction I + CH,



in fact, we estimate A ^ 109'8 I/mole-sec at 300°K in contrast to the



observed 1011'7 I/mole-sec (based on CH3I as a model for TS).   This  suggests



an extremely loose complex since even a .nonlinear  TS would  still have an



A-factor only 10-fold higher.





     A postulate of Hammond48 proposes that for very exothermic reactions



having low activation energies the TS complex resembles reactants . This



is, in fact, the case for the reverse of the I-atom reactions, i.e.,  for



CH3 + HI and for CH3 + I2 with E  t = 1 + 1 and 0 kcal/mole,  respectively.





     Applied to the I + CH4 reaction, this suggests that the  TS looks



like a very weakly coupled CH3 • • *HI with the C"*H*"I axis  bent.  If we



assume that in this complex the CH3 is freely rotating about  the  C••«H



bond (3.6 e.u.), has two rocking modes about this bond of about 350 cm"1



each (2.4 e.u.) and the C-'-H-'-I  bend is about 200 cm"1 (2.2 e.u.), we



can account for an A-factor of about 1011*5 I/mole-sec in reasonable



agreement with the results.  A similarly loose model can account  for  the



I + CH3I - I2 + CH3 A-factor.





     A-factors for some metatheses by diatomic and polyatomic  radicals



are shown in Table XIV.  Although the table covers a range of  radicals



and atoms varying conr--t
-------
Table XIV.  Arrhenius Parameters for  Some Metathesis Reactions of Radicals.
Ref .
1
la
1
la
1
Ib
2
3
3,4
5
6
6
6a
7
6
6
6
Reaction
HO + CH4 - HOH + CH3
HO + C2H6 - HOH + C^HS
HO + CO - H -1- CO2
HO + O3 - H02 + O2
HO2 + 03 - HO + 202
H02 + NO - HO + NO2
CH3 + C2H6- CH4 + C2HS
CH3 + CH3COCH3 -
CH4 + CH2COCH3
CH3 + CC14 - CH3C1 + CC13
CF3 + C2H6 - CF3H + C2H5
CF3 + CC14 - CF3C1 + CC13
C2HS + n-C7H16 -
C2H6 + n-C7H15
n-C3F7 + acetone -
C3F7H + acetonyl

(300-500)
770
(300-500)
770
(3OO-500)
(220-450)
(225-298)
300
420
(400-500)
400
(320-450)
(400-560)
(360-510)
450
(300-600)
log A
(NT1 sec-1)
9.5
10.3 (10.9)c
10.1
10.9
8.1
8.5
8.8
7.8
>9.2 (10.3)d
8.5
8.6
10.4
8.6
8.0
8.8
9.6
8.7
8.8
E
(kcal/mole)
3.8
4.9 (6.6)c
2.5
3.5
0.2
0.6
1.9
2.5
0(?)(1.4)d
10.8
9.7
13
9.1
6.5
9.3
10.4
10.6
7.2
i.  N. R. Greiner,  J.  ^hom ,  Phys. ,  5J.,  5049  (1969).
      (a)  R.  R.  Bakor ,  K K.  Baldwin,  and R. W. Walker, Trans Faraday
           Soc.,  66,  2812 (1970) .
      (b)  W.  E.  Wilson, Jr.,  J.  Phys.  Chem., Ref. Data _1, 535 (1972).
      (c)  S.  Gordon  and W.  A. Mulac, Int. J. Chem. Kinetics, Symp. 1, 289 (1975)
      (d)  W.  Hack  and K. Hoyerman, this  symposium.

2.  J. G. Anderson  and F. Kaufman,  Chem.  Phys.  Lett.,  19, 483 (1973).

3.  Table XII], ref. 5.

4.  Activation energy not determined, estimated on the basis of
    radical recombination.

5.  A. F. Trotman-DickenscKi  and E.W.R.  Steacie, J. Chem. Phys.,  19, 329  (1951).

6.  Reference 45; (a)  J. Currie, H.  Sidebottom,  and J.  Tedder, Int. J. Chem.
    Kinetics 6, 481 (1974).

7.  Reference 46.
                                     66

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A ^ 109-3 I/mole-sec.  A similar analysis lor C2H6 + OH gives A ^ 109 "°



I/mole-sec.  A nonlinear  complex would have A-factors about a power of



10 higher for both.  The valuu of 1010 I/mole-sec would seem to be



reasonable for C2H6,  and this would suggest that the higher of the two



values listed, 1010*3, might be a better choice for CH4 + OH.





     The very important reaction CO + HO has a TS which can be modeled



by HONO.  This yields A ^ 108'6 I/mole-sec, suggesting that both listed



A-factors are probably on the low side.  All reasonable models for the



HO + 03 reaction yield A-factors in excess of 109'3 I/mole-sec, about



three-fold higher than the reported value.  The A-factor for HO2 + 03



is in much worse agreement.  The TS entropy would have to be 78.1 e.u.



at 300°K to account for the anomalously low A-factor of 107'8.  The



estimate for TS is about 84 e.u., suggesting A > 109*° I/mole-sec.





     The CH3 metathesis reaction from C2H6 can be modeled using C3H8 for TS.39



This leads to A ^ 108'° I/mole-sec.  Correcting for a larger moment of



inertia increases this to 108"3 and a further correction for a lower CH3



rotation barrier of 1.5 kcal/mole instead of 3.0 increases it further



to 10s'5.  If we assumed either a nonlinear  C «H-C structure in TS or two



weakened CH3-H'C rocking modes, this would increase to 109*° I/mole-sec.



The bulk of A-factors for CH3 abstraction45"47 suggests that the TS struc-



tures are probably nearly co-linear.





     The A-factor listed in lable XIV far CH3 + CC14 is at least a factor



of 101>8 higher than can be accounted for in terms of any reasonable TS



structure.  The new value presented by Tedder   et  al.  agrees  quite well



with TS estimates.
                                    67

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Addition Reactions





     Addition reactions in which atoms or radicals attach themselves to



vmsaturated systems usually involve small activation energies  and hence



can be considered to pass through tight transition states, not unlike



those for metathesis reactions.  This is more or less in agreement with the



much sparser data for these reactions, some of which are tabulated in Table



XV.   It should be observed that these are much more difficult reactions to



measure experimentally since the products are not themselves stable and go



on to react further.  They are usually not observed directly,  and their rates



are often inferred from the rate of disappearance of reactants with the aid



of some assumptions on chain lengths and secondary reactions.   In addition,



the adducts are energetically excited, and their stabilization will require



subsequent deactivating collisions.  In consequence, many of these reactions



show a rate dependence on total pressure which may or may not  be properly



accounted for in the published data.





     With these cautions made, we note that for H + C2H4 the simplest model



for a tight transition state give A ^ 1010>1 I/mole-sec, in excellent agree-



ment with the data.  For 0 + C.-.H4 we estimate A ^ 109 '° I/mole-sec.  This



is probably in reasonable concurrence with the data for which the reported



values are uncertain by a factor of 3.  For Cl + C2H4, a tight transition



state, using CH2=CHC1 as a model, leads to A ^ 109*1 I/mole-sec, very much



lower than the reported 1010'6.  Only a loose transition state character-



istic of radical recombinations can account for such a large A-factor.  The



zero activation energy is in agreement with such a structure and can be



rationalized in terms of a charge transfer attraction.  The ionization



potential of C2H4 is 10.5 e.u.49 while the electron affinity of Cl is 3.6



e.u.49  The difference of 6.9 e.u. is made up by coulombic attraction at



distances of 2.1 A, which is about 0.3 A larger than the C-C1 covalent bond.50
                                    68

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Table XV.  Arrhenius Parameters for Some Addition Reactions
           of Atoms  and Radicals to Pi Bonds.
Ref
1
1
2
1
3,2
4
5
6
6
React ants
H + C2H4
0 + C2H4

Cl + C2H4
OH + C2H4
OH + C3H6
0 + C2H2
CH3 + C2H4
C2H5 + C2H4
Tm(°K)
(296-540)
(223-613)

310
(210-460)
300
300
400
400
log A
(^/mole-sec)
10.4
9.9
9.5
10.6
9.7
9.5
[9.8](?)
8.5
8.3
E
(kcal/mole)
2.0
1.6
1.1
0
0.2
0 (?)
[2.8](?)
7.7
7.5
    V. N. Kondratiev, "Rate Constants of Gas  Phase  Reactions," Reference
    Book, Trans, by L. J. Holtschlag, Ed. by  R.  M.  Fristrom, NSRDS,
    U.S. Government Printing Office, Washington, D.C.  (1972).
2.  Table XIII, ref.  1.

3.  I.W.M. Smith and R.  Zellner,  J.  Chem.  Soc.,  Far.  Trans.  II, 69,  1617  (1973)
4.  J. Bradley, et al.,  Ibid., 1889  (1973).

5.  F. Stuhl and H. Niki,  J. Chem. Phys.,  55, 3954 (1971).   Authors  did not
    measure A and E,  but. reported only k300  = 107'9 -t/mole-sec; A and E are
    our choices.

6.  J. A.  Kerr and M.  J.  Parsonage, Evaluated Kinetic  Data  on Gas Phase
    Addition Reactions,  Buttersworth, London (1972).
                                    69

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Thus, unless there is some large van der Waals1  repulsion between Cl  and C2H4 ,

one could expect that their interaction would correspond closely to that of a

recombination curve.  In fact, it is expected that  halogens (atoms and molecules)

will form attractive Pi-bond complexes at van der Waals1 distances.

     One would expect all of the halogen atoms to show a similar facility in

adding to Pi systems.  The case of the OH radical is,from this aspect, very

interesting.  Its electron affinity of about 1.8 e.u. is not enough to form

an ion pair with C2H4 except at smaller distances of the order of about 1.7 A.50
                        o
This is again about 0.3 A larger than the C-0 single bond distance, and hence

would constitute tight complex for which we would calculate a minimum A-factor

(based on CH2=CHOH) of about 108'5 I/mole-sec.  The reported values, though

uncertain, are about a power of ten or more higher,  suggesting again a loose

transition state characteristic of radical recombinations.  A very loose

transition state with two rocking modes of HO relative to C2H4 of about 200

cm""1 and a weak 0«--C-C bending mode of about 200 cm'1 would raise this value

to 109'6 I/mole-sec in good agreement.

     Collision Theory which is a zero order limit of Transition State Theory

will give a similar A-factor for OH + C2H4 collisions if the collision (i.e.,
                                 o
impact) diameter is taken as 1.8 A, and it is assumed that 1/3 of the surface

surrounding the C2H4 does not permit a proper collision because of steric

repulsion of the H-atoms and an additional factor of 1/2 is used to correct

for the geometry of the OH approach, i.e., the H of OH should be pointing

away from the C2H4.

     The reactions of O atoms with acetylene gives, for a tight complex,

A ^ 109'8 I/mole-sec, suggesting that the observed rate constant (the authors

did not measure A and E), which is 107'9 I/mole-sec at 300°K, must have at
                                      70

-------
least 2.8 kcal/mole of activation energy or else is too low because of pressure


effects.  For 0 + C2H4 a tight complex has A ^ 109*° 1/mole-sec,  in reasonable


agreement with the data.  Note that in this reaction and in that  of O + C H0
                                                                         2 2

the reaction must be mechanistically complex since the initial adduct is a


triplet biradical which must eventually be transformed into a singlet species.


     The addition of alkyl radicals to olefins has activation energies suffi-


ciently high that we model the TS by tight complexes.  For CH3 +  C2H4 propylene


(C3H6) is a good model and yields A ^ 107'7 I/mole-sec.  Corrections for a


lower barrier, a slightly larger moment of inertia and a lower C-C-C bending


frequency raises this to 108'4, in excellent agreement with the reported values.



Recombination Reactions Involving Atoms


        The recombination of free radicals is an exothermic process which


produces an excited species that will redissociate into the initial fragments

unless stabilized by a de-exciting collision.  For large radicals, such as ethyl,


with many internal degrees of freedom f  into which the recombination  energy  can


be partitioned,  the lifetime of the energized adduct is sufficiently  long  and

energy transfer  is sufficiently efficient  so that  at pressures of  1-10  torr

deactivation is almost always faster than redissociation.  Consequently, in


this pressure range, radical recombination of large radicals is bimolecular and


independent of  total pressure.  With small species, such as atoms, the reverse


is true, and recombination appears to be a third-order process.51 It can be

looked upon as a succession of bimolecular events:


                                      1    *
                              A + B  52  AB
                              *      2
                            AB  + M  ^  AB + M

                                                                   *
When A  is an atom and B is a diatomic molecule, the lifetime of  AB  is so


short that AB* can be considered to be in virtual equilibrium with A and B.
                                      71

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In that case (k_j » k2),  the overall rate can be written as:
                                     = k8K1(A)(B)(H)                   (36)



and the third-order, recombination rate constant  kr is:




                                 kr  =  k2Kj                          (37)




        Since k2 is the rate constant for an energy transfer process,  we can


write it as a product Xkz, where kz is a simple hard-sphere collision  frequency


and X is the probability of deactivation of AB on collision.  For highly


energized species possessing many quanta of energy, X  is  expected to be in


the range 0.2 to l.O,52 while kz ~ 1011'3 I/mole-sec.


                                         *
        The pseudo-equilibrium constant K  can be looked upon in two


different ways.  If the recombination energy of AB is readily partitioned


among its internal degrees of freedom, then on the average there will be


equal numbers of quanta in each mode.   If the modes  are comparable in


frequency and there are n of them, each will have about  l/nl— the recombin-


ation energy, and the molecule is not expected to look very different  from


the normal unexcited molecule,  in that case we can write K  as:S3




                              RlnK*  =  -AS°B + AS^g                   (38)



where AS°  is the standard entropy change in forming  ground state AB from
        f\Jj

A + B, and AS^g is tne extra entropy that results from the high energy
content of AB .  AS.Q may be evaluated as Rlnp*, where p   is the number of

                                                  .g.
ways of distributing the energy of recombination E  among the n internal
                                    72

-------
degrees of freedom of AB .    If the geometric mean frequency of the


active degrees of freedom of AB  is v , then a reasonable approximation


to p  is:
                                                                      09)
     If we apply this to the recombination of 0 + NO -* N02 ,  we find:




              ASj^Q  =  —31.5 e.u.  (atmospheric-standard state)


                    =  —25.1 e.u.  (M/liter-standard state)


                vm  «  1200 cm-1



              E300K ^  E° +l RT = 73 kCal

                 p* ~  530/2 = 265 = 102'4



and



              kr = \kz(10-5)(102 -4)  =X(10~2'6)kz                     (40)



     If we set kz equal to 1011'4 I/mole-sec and employ a maximum value of


1 for X, this yields kr = 108*8 I/mole-sec as compared to the measured value


of 1010'3 I/mole-sec.  The discrepancy of a factor of 30 cannot  be reconciled


with any anharmonicity assignment or reasonably distorted structure  for NO*.


The inclusion of excited electronic  states simply does not help  since their


lifetime would be significantly less than that of the ground state due to

                                    •x-
their lower kinetic energy content E  (eq. 39).  We may thus conclude that


the (ONO)  that leads to recombination cannot be a simple structural  variant


of the ground state NO2 .



     Another way to examine this anomaly is to consider a trajectory  of


O + NO with impact parameter in the  range ~ 3.0 A.  The rate constant kx(NO*)


for such collisions is 1.3 x 1011 I/mole-sec.  The average relative collision
                                   73

-------
velocity vr is 7.5 x 104 cm/sec (300°K).  If we make the arbitrary, but


reasonable, assumption that the range A of potential interaction between NO
                       o
and  o extends over 1 A (1 x 10~8 cm) and that the average relative radial


velocity during this portion of the collision is 1/2 the initial velocity,


then the duration of the collision is:
                        TC Si  -—	 = — = 5.3 x 10-13 seconds
     The first-order rate constant k_t for the breakup of this collision

             \t
complex of N02 may be taken as I/TC , and hence we can write:
                                        = 7 x 10"2 1/raole


                    v.
     This value of K  is a factor of 28 larger than the value of 1Q-2 '6


computed for the tight collision complex and yields an excellent value for


kr when combined with a strong collision deactivation (\=1) .  We are thus


forced to conclude that the TS complex for 0 + NO recombination is loose,


just as it is for all other radical recombinations.  While this is not in


agreement with some shock tube results55 obtained recently, it is the only


way to explain the results of Pitts, Sharp, and Chan56 on the threshold


wavelengths for NO2 photolysis.  The usual rule of a loose transition state

                     ±                                           o
complex for (0=No<<0)  would have an N • • *0 distance of about 3.0 A.  At an

                      o
N-«»0 distance of 1.8 A, the ion-pair curve"1  would have zero energy if we


neglect ion-dipole interactions and polarization.  It is likely, however,


that polarization effects will stabilize the ion-pair curve out to even


larger distances, and this type of interaction S7 could account for the


relative ease of formation of the loose complex.  Such a loose complex could
                                     74

-------
also account for the much discussed anomaly in the fluorescence lifetime of


electronically 58excited NO,,.



     In further support of this "loose" model of the NO + O recombination


is the atom exchange data for the exchange reactions: 57»59



                 O18 + NO16  a  (018...N016)*  si  18NO + O16



It was found that the rate of complex formation which is just twice the


observed exchange rate is 199'3 I/mole-sec at 300°K.  This is about ten


times slower than the rate of formation of the loose "collision" complex

      •x-
of NO2  we have just considered, but it corresponds very closely to the


rate of formation of a semi-tight NO2 transition state in which the bending


mode at 760 cm"1 is replaced by a restricted  (~ 60°)  1-dimensional rotation.43


Such a semi-tight structure is required if the  two 0-atoms are  to become


equivalent, which is needed to allow the exchange.  A  loose TS with large


moments of  inertia will have a centrifugal barrier which v/ill prevent the


two O-atoms from becoming equivalent.



     Additional evidence comes from the findings obtained by Hippler  et al.60


where a limiting bimolecular rate constant for  0 + NO — N02 in  high pressures


of inert gases  (1000 atm) is 1.8 x 101° I/mole-sec.   This now coincides with the


rate of formation of a genuine loose TS for N02 ' and  suggests that at these


very high  pressures, every complex is  quenched  (TconiSiOn — 10~12"5 sec),


even rotationaly hot NO^  .



     The high ionization potential of  O2  (12.06 e.v.)49 will permit ion-pair


formation  only  at distances of about 1.3 A,which is practically the normal

                o
covalent  (1.28  A) bond length in 03.   Thus, no  loose  transition state can be


f ormed.
                                    75

-------
     Again, supporting data comes both from O18 + O2  exchange measurements57'59


where the rate of complex formation is 109'0 I/mole-sec,  only a factor of two


less than that found for NO,, and presumably corresponding to the rate of


formation of a semi-tight transition state.  The difference in rates corres-


ponds very closely to the differences in AS0 .  Further support is provided


by the data of Hippler et al.,60who find for the limiting bimolecular rate


constant k(0 + 02) ~ 109'*, only slightly greater than the rate of formation


of the serai-tight transition state, and indicating that no loose transition


state is possible for 03.



     One would expect that halogen atoms with their large electron affinities


would similarly form loose ion-pair complexes with NO and this is indeed


compatible with the termolecular rate constants observed for the recombination


of Cl + NO,59 all in the range of lo10'5-*0'1 l/mole-sec.  In distinct and


pardoxical contrast is the low recombination rate constant observed for


O + 02 + M - 03 + M5jl of about 108-2 lVmole2-sec at  300°K.  This is clearly


incompatible with a loose transition state complex and can instead be inter-


preted in terms of a tight transition state complex.   Using the same analysis


as for NO, we find:



                            AS°(O3)  =  —30.4 e.u.  (atmospheres)


                                     =  —24.0 e.u.  (moles/liter)


                                 VM  «  930 cm-1


                              E*     ~  26.5 kcal
                               300K

                                  P* ~ 101'7


and kr(O3) = A.kz(10-4 %8) (101 -7) = X(10-3'1)kz.  If ^  = 1 and kz = 1011 '*


I/mole-sec, then kr = 10s*3 12/mole2-sec, in excellent agreement with the


observed data.
                                     76

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Activation Energies

     The only activation energies which can be said to be reasonably well
understood are those for simple bond fission reactions.  The bulk of the data

on these reactions support the loose transition state model  for bond rupture,26

and the activation energies are simply equal to the bond dissociation energy

(DH)°-RT.  Hence the reverse recombination reactions have zero activation

energies (for standard state, of mole/liter).  This loose transition state,

originally proposed by Gorin, is compatible with a potential function which

extends out to form 2.5 to 3 times the covalent bond radius.

     The activation energies for bimolecular processes do not fall into such

a simple pattern.  If we restrict our attention to what has  been called the

intrinsic activation energy of a reversible reaction, i.e.,  the activation

energy in the exothermic direction, they are generally low, in the range

0-15 kcal/mole.  This is true both for atom metathesis reactions and for

addition reactions.  Perhaps 80 percent of measured, intrinsic E&ct fall in

the range 8 ± 3 kcal/mole, while over 90 percent are in the  range 8 ± 5

kcal/mole.  A few fall conspicuously outside of this range,  and within

homologous series of reactions there are occasionally some curious deviations

from general trends.

     A number of semi-empirical efforts at treating metathesis reactions,  such
as the bond energy-bond order model61>62  (BEBO) have succeeded in estimating

Eintrinsic to — 2 kcal/m°le-  More recently, Alfassi and Benson63  have demon-
strated that Extrinsic can be represented by simple formulas of the form:

                                  E  =  13.0 - 3.3 I                  (4i)
                        or
                                  E  =  XA + Xc                       (42)
                        or
                                  E  =  FA •  FC                      (43)
                                    77

-------
where Eintrinsic is in kcal/ra°le> I is tne SUJn of the electron affinities


of the entering (A) and leaving (C) radicals (or atoms)  in the metathesis



reaction:





                      A + BC  ^  (A • • -B • • 'C)   -  AH3 + C + energy





     In relation (42), XA and Xc are constants, characteristic of the radicals



A and C, respectively, and turn out to correlate with their ionization potentials



F  and FQ  are similar group constants.




     All three relations are capable of estimating E    for broad categories
                                                    3-Ct


of reactions to an average of + 1 kcal and a maximum deviation of about 2.6



kcal/mole.




     In a few cases larger deviations can be explained on the basis of dipole-



dipole repulsion (CF3 + HX).  In the abstraction of halogen atoms (B = halogen) ,



there must be a strong influence of the migrating atom B on the activation



energy, but this is neglected in the-correlation.  The data currently available



are not sufficient to further examine this point.




     We have already noted that addition reactions of atoms or radicals to



Pi bonds are especially sensitive to the ionization potentials and activation



energies of the reacting pair.  This is strikingly parallel to the empirical



finding for metathetical reactions and suggests that the ability to form



donor-acceptor (ion-pair) complexes plays an important role in determining



the crossing of the two potential energy surfaces represented by reactants



and products.





     There are a few examples of exceptionally high activation energies in



exothermic metathesis reactions which are worthy of further examination.
                                     78

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Two examples are: CO + O2 -*  CO2  + O (Eact — 47 kcal)  and CO + N02  -*



CO2 + NO (Eact ~ 25 kcal) which are exothermic by some 8 and 46 kcal,



respectively.





     If we examine the intermediates formed in each case, we find that  they



are very endothermic biradicals,  such that the intrinsic activation energy



is in each case only 8-10 kcal/mole above the endothermicity of the addition.64



If we neglect such exceptional cases, then we find that the intrinsic activ-



ation energies for exothermic addition reactions fall  into the same range as



for metathesis reactions, namely 8 ± 5 kcal/mole.  Data on these activation



energies is not abundant, and so empirical analyses have been made in an



effort to correlate them with simple bonding properties.
                                    79

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B.   RATE PARAMETER EVALUATION AND ESTIMATES





     Extensive  efforts are underway throughout the world to accurately



model atmospheric chemistry.  Whether the efforts are directed toward



modeling tropospheric or  stratospheric phenomena, there is a need to evaluate



existing rate constant data and to estimate unknown rate parameters in a way



that is consistent with  current knowledge for similar reactions.   We are



developing an explicit reaction mechanism to explain data obtained in smog



chambers and we are constantly faced with the fact that too few accurate



rate data for elementary reactions are available.





     Since the  kinetic data on particular families of reactions ranges from



"excellent and  extensive" to "nonexistent," a variety of methods must be



used for evaluation and/or estimation.  As a general guiding principle, it



has been found  that best results are obtained when reactions are treated as



"families" rather than as individuals,because only rarely are enough data



available for an individual reaction to make a meaningful evaluation.





     A  second guiding principle often overlooked is that an estimate



or evaluation is not useful unless accompanied by a fair assessment of its



probable accuracy.  Since A-factor and activation energy combine to give a



 single  rate constant, we have adopted the method of propagation of errors



to estimate the uncertainty in rate constants, based on the probable uncer-



tainties associated with A-factor and activation energy.  This estimate of



uncertainty is  very useful since it is a quantitative measure indicating




over what range an estimated rate constant can be varied legitimately.
                                   80

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Alkoxyl Radical Decomposition Reactions

     The decomposition reactions of alkoxyl radicals provide a good example
of a family of reactions for which an adequate number of accurate studies
have been made.  Most of the studies have been made on t-butoxyl  radicals,
but several other radicals have been studied as well.  All the studies
were determinations of relative rate constants and so we returned to the
original data and recomputed it on the basis of current values for the
reference reaction rate constants.
     Three different reference reactions have been used:

                        9'          M    ONO
                      RjCR2R3 + NO  -*  RiCRjjRg                        (44)
                  ?'
                IH
(CH3)3CH  -»  R^R-jR;,  + (CH3)3C              (45)
                         9'              9
                              + NO  -  R±CR2 + HNO                    (46)
     Values chosen for k^ were those obtained by Batt  et al.,86 and   are
in good agreement with those obtained by Golden  et al.33; the value of k4s
chosen was that determined by Berces and Trotman-Dickenson66 ; the values
chosen for k46were derived from disproportionation/combination ratios and
values of k44.34 >65 Other reported data were not used because their reference
reaction rates are not sufficiently well known.
     The recalculated data are presented in Figures n through 14,  and the
corresponding Arrhenius parameters are presented in Table XVI .  The data
                                   81

-------
                               Table XVI
             EXPERIMENTAL VALUES  FOR RO" DECOMPOSITION RATESa
Radical
EtO'
i-PrO'
s-BuO-
t-BuO*
log A
13.7
16.1
16.4
14.9
15.1
log E
22.1
20.6
18.0
15.3
16.2
ASg
33.4
37.8
37.7
41.2
log Ar
8.2
8.2
8.0
8.0
lo* Aest
13.7
14.6
14.4
15.2
E'
22.1
17.4
13.9
14.2
16.3
Ref .
67
68,69
70
65d
71-74
Units: E in kcal/mole; Ar in M-1 s"1;  A in s-1.
 for t-BuO* are the most extensive (Figure 11), covering  nearly four  orders of
 magnitude.  The individual sets of experimental data taken independently show
 a rather wide range of Arrhenius parameters and appear to be inconsistent,
 but taken together, the actual data give a reasonably good straight line
 with parameters, log k/s'1 = 15.1 - 16.2/9.  Given the entropy change of
 the reaction, As£ = 41.2 Gibbs/mole, the A-f actor for the reverse reaction
 is Ap = 107 -8 M"1 s"1 , a value very close to that for the reaction of methyl
 radicals with isobutene (log A = 8.0).75  This suggests a self -consistent
 method for evaluating and codifying the limited data available for the other
 alkoxyl radical reactions: choose an A-f actor for the reverse reaction and
 find the corresponding activation energy.  If this unified scheme is used, the
 alkoxyl decompositions can be considered together as a class, rather than
 individually.
      The decomposition of an alkoxyl radical is the reverse of the addition
 of an alkyl radical to the carbon atom of a carbonyl group, which is analogous
                                   82

-------
                                    o
                                    a
                                   6
83

-------





o
X
V
S
•f
+J
w
S t

9
CQ
n
4)
a
•H
•H
•o
«
tO
»
«H
4>
K

•

0
>
£1
                        g
84

-------
to alkyl radicals adding to the 2-position of a primary olefin.   Since data
are only available for alkyl radicals adding to the 1-position of primary
olefins, the assumption was made that the A-factors for addition to both
ends of an olefin double bond are the same and only the activation energies
differ.  Thus, A-factors for analogous alkyl radical plus olefin reactions
were chosen from the tables of Kerr and Parsonage,7& corrected for any
difference in reaction path degeneracy, and applied to the alkoxyl reactions.
     Assumed A-factors for the reverse reaction, Ap, are summarized along
with ASn, log A   , and corresponding activation energies E in Table XVI.   A
plot of E vs AH^ is presented in Figure 15 and gives a good straight line:
               E = 12.8 + 0.71 AH£                AH£ > 0             (47)
                 =12.8                           AHg < 0

This equation predicts activation energies with an uncertainty of about
±.0.5 kcal/mole.  It predicts that the reverse reaction has an activation
energy given by:

                    Er = E - AH°  + RT = 13.6 - 0.29 AH£               (48)
Although these equations apply to ~ 400 K where most of the experiments
were carried out, the estimated activation energies will be negligibly
different at ~ 300 K.
     Estimated decomposition rate constants for a number of alkoxyl radicals
at 300 K and atmospheric pressure are presented in Table XVII.   Fall-off
corrections were obtained by use of the Emanuel RRK Integral Tables.76'77
For the experimental data available, the estimated rates are accurate to
about a factor  of two, as demonstrated by comparing estimated  and observed
rate constants (Figures 11-14). The differences apparent between the estimated
                                   85

-------
   25,
   20
8

^



815
^

In
   10
                          I     I
E(400K) = 12.8 + 0.71 (AH|,)
                                               8     9    10    11    12    13
                                 AH*  / kcal mol'1
                                    n
                                                                    SA-2SS4-47R
 FIGRJRE  15  Correlation Between Activation Energy E  and Enthalpy


             of Reaction
                                   86

-------
                                      Table  XVII
                            ESTIMATED HO'  MtX'OMPOSITION RATES
Radical
C-CO-
CC-CO-
6
i
c-cc
ccc-co-
6
cc-cc
c
c-co.
6
IBC-CC

HOCCC-CO'
6
IIOCCC-COII
0
( 110) 2CCC -COI1
9
UK».,CCC-C(OII)2
6
(lK))3CCC-C(01l)a
c
i
IIOC-CO-

o o'
II 1
cc-cc
A1.JJ
12.4
9.4


7.1
8.9

2.6

4.3

6.8
(3.5)°
8 .7

-9.7

-9.6

-30.9

-24.5


11.4
(8.2)e


-5.1
^R
33.4
35.0


37.8
36.3

37.7

41.2

38 .0

36.6

39.2

39.2

37.7

37.7


37.7



40.3
log Ar
8.2
8.0


8.2
7.5

8.0

8.0

8.O

7.1

7.1

6.8

6.8

6.5


7.5



7.5
log A(s-')
13.7
13.8


14.6
13.6

14.4

15.2

14.5

13.3

13.8

13.5

13.2

12.9


13.9



14.5

21.6
19.5


17.8
19.1

14.6

15.9

17.6
(15.3)e
19.0

12.8

12.8

12.8

12.8


20.9
(18.6)e


12.8
k/U
00
O.OO3
0.6


0.5
0.8

0.7

0.5

0.8

1

1

1

1

1


0.9



0.8
kdiiln-1)
2.1 x 10^
1.7 x 10'


1.6 x 10*
2.9 x 10'

2.9 x 10s

1 .5 x 10s

2.8 x 103
(2.i!xl06)u
2.1 x 10*

2.1 x 10b

1 .0 x 10s

5.2 x 10*

2.6 x 10s


3.6 x 10°
(2.2 x 102 f


8.2 x 106
                 ?                   ?           •      L
 Notation:   IIOC-CC represents  IIOCII^CIICII, -  11OC1I., + IICCIIj ,  etc.
b
 A-liic(or for analogous alkyl  rudicul  i-  ulkene association  reaction.
CKC.S(   l^.B I 0.71  illjj (kcal/woJe) .
 K.ill-oif us I united  from RUK Tables lor  1  atm, 3«>00K.
 llasud f>n (iroii|>  Ailditivity ,     not on expcrimental Allf lor propane-1  ,2
 Rule constunls  1'or  300 K .incl  1 aim.  air.
-diol.'
      89
                                           87

-------
and experimental rate constants are due to the ±0.5 kcal/mole uncertainty


in estimating the reaction activation energy and round-off errors on the


A-factors.



     Estimates made when no experimental data are available can be appraised


by using the propagation of errors equation.  Since A-factor and activation


energy are usually estimated independently, the uncertainty in log k can be


written



                            cr2      =  a2     + a2/92                 (49)
                             log k      log A    E




where cr      , a     , and cr  are standard deviations in  log k, log A, and
       log k   log A       E

activation energy, respectively, and 6 = 2.303 RT.  Since log A is probably


uncertain by ± 0.5, and the activation energy is uncertain by about + 1


kcal/mole, the value for a      « 0.88 at 300 K, and k is uncertain by
                          log k

about a factor of eight.  This represents a relatively favorable case for


estimations, since an adequate amount of kinetic data is available, and


it is fairly consistent.  For the reactions discussed below, very little


data is available, and the reliability of the estimates is much lower.
                                   88

-------
Alkoxyl Radical Reactions with Oxygen




                                            7 o
     The only reliable Arrhenius parameters   known for this class of



reactions are:





               CH30 + 02  -.  CH3O + H02      log k/M-1 s-1 = 8.5 - 4.0/8   (50)





Rates for other members of this class can only be estimated after making



assumptions regarding variations in A-factors and activation energies.  The


concomitant  uncertainties in estimating rate constants will be relatively


large since little is known about such variations.




     The A-factors for this group of reactions are expected to be similar to


that for methoxy radicals, aside from the reaction path degeneracy (n) factor;



therefore, log A can be estimated as follows:





                  log Aegt/M-1 s-1  =  8.0 + log n                         (51)





     Estimates for activation energy variations are rather problematical,


especially when EQ is low.  Two alternative methods can be used:
                 cl



     (1)  Assume E& is constant for the entire homologous series



     (2)  Assume that an empirical relationship that holds for other

          radical reactions applies to this series  as well.





A simple empirical relationship79  that gives E  with an uncertainty of about
                                              cl

±. 3 kcal mol"1 for exothermic H, OH, and CH3 reactions is given by equation (52)





                         E& = 11.5 + 0.25 (AHjj)  ,                         (52)
                                   89

-------
where £HR is the enthalpy  of reaction.  For reaction (50) ,  equation (52)



predicts Ea = 5 kcal mol"1, about 1 kcal mol"1  too high.  Equation (52)  has



two parameters and can be modified in two different ways to give the proper



E& for reaction (44):






                        E   =  10.5 + 0.25 (AHP)                       (53)
                         a                   n



                        Ea  =  11.5 + 0.29 (AHR)                       (54)






     Rate constants for a number of alkoxyl radical reactions were estimated



by the three methods and are presented in Table XVIII.   Considering  the  large



uncertainty associated with equation (45)  and the low activation energies,



the estimates in column III of the table are highly uncertain and may well



be upper limits to the correct rate constants.   Similarly,  rate constants



in column I of the table may be near the lower  limits.




     The overall uncertainties for this family  of reactions may be estimated



as before.  Log A is probably uncertain by ±. 0.5  and the activation energy



is probably uncertain by an average of + 1.5 kcal/mole.  Thus, CT^oe jj « 1.2,



and the estimated rate constant is uncertain by about a factor of 16.  If



the activation energy is uncertain by an average of ~ ±. 2.5 kcal/mole, the



estimated rate constant is uncertain by a factor of ~ 80.
                                   90

-------
     ra

     §
     i—i
     EH
     O
3   °
t*   +
«   §
f~H

oS    ••


^   |
M
O
^— v
+ oort
•°. 2
rH
rH X
II
M
m
N
O

CO <3
o
rH X

II

q
^

u

cS
W
I-H
-P
0)
0)

I
§
•H
-P
U
01
0)
OH





^-^
H
•H
e

•*

*
j


^


^
«

g
^x



















10 CD to to in to
o o o o o o
X X X X X X

O CO CO t^ 00 d
CM rH rH CO in M
in in m to in cc
O O O O O O
X X X X X X .
O CM (N m in rH
• •••••
CM 00 00 rH CO rH

m in m «f in «
O O O O O O

rN ?N ?S rS rS rS

O CO CO t~ CO t*
• •••••
CM rH rH  1 1 1 1
o w e -H c n
                                                                          I
                                                                         m
                                                                         O
                                                                         •H
                                                                          cd
                                                                         CO

                                                                         -p
                                                                          a
                                                                          a)
                                                                         •p
                                                                          CO
                                                                          C
                                                                          O
                                                                          U

                                                                          0)
                                                                         -p
                                                                          cd
                                                                          0)
                                                                         •a
                                                                         •P
                                                                          m
                                                                         •H
                                                                         
-------
Alkoxyl Radical Isomerization Reactions




     The importance of alkoxyl radical isomerization reactions has been


inferred from smog chamber data,80 as well as from more qualitative


considerations.81  The estimation of the isomerization rates is relatively


straightforward,  but the estimates are somewhat uncertain,  as discussed below.



     A-factors for 5-membered ring (5R) and 6-membered ring  (6R) isomerizations


were estimated to be 1011'2 s"1 and 1010 '9 s"1 (per H-atom), respectively.  The


estimate for the 5R transition state was made by noting that in tying up the


methyl and ethyl internal rotations, the change in entropy is about —6.6


Gibbs/mole; subtracting another 0.3 Gibbs/mole for the reaction coordinate,


we obtain log A   =11.7 for three abstractable H-atoms.  Thus, for each
               5R

abstractable H-atom, log A5R (per-H) = 11.2.



     For the 6R transition state, a model transition state was used.  For the


decomposition of ethyl vinyl ether (EVE), log A = 11.4 at 700°K.  If log A


is about the same at 300°K and S°(EVE) = 82.6 Gibbs/mole,82  then the entropy


of the transition state is 74.3 Gibbs/mole.  In comparing the EVE transition


state and that of n-butoxyl radical, EVE has some double bond character, and


that of n-butoxyl will be looser by about 0.6 Gibbs/mole. n-Butoxyl has one


more hydrogen atom, worth about 0.2 Gibbs/mole, and has spin, contributing


1.4 Gibbs/mole.  Adding all of these corrections, gives S°  = 76.5 and


log A = 11.4 for three abstractable H-atoms; thus  log AgR(per H) = 10.9.


The uncertainties in these estimates are probably + 4 Gibbs/mole and log A


is uncertain by + 1.
                                   92

-------
     Activation energies may be estimated from the activation energies



for H-abstraction by alkoxyl radicals2a by adding a "strain" energy of



0.5 kcal/mole for 6R reactions and 5.9 kcal/mole for 5R reactions.82



These activation energies are rather uncertain, probably ±. 2 kcal/mole.



The combination of the two sources of error by the propagation of errors



formula gives an estimated uncertainty in log  k of ± 1.8 at room



temperature.  Thus, the rates are estimated to be uncertain by about a



factor of 60.





    The method for estimating these rates is summarized in Table XIX,  and



estimated rates for several alkoxyl radicals are presented in Table XX.



All reactions are assumed to be at the high-pressure limit.
                                   93

-------
                            Table XIX
        RO' ISOMERIZATION REACTIONS—ESTIMATION PROCEDURE
  E  =  E (abstraction) + E (strain)
  Hydrogen Abstracted
       RCH2-H
       RCH(OH)-H
       RC(OH)2-H
E (abstraction), kcal/mole
            7.2
            6.0
            4.1
            4.1
            4.1a
  Strain Energy
       5-membered ring
       6-membered ring
5.9 kcal/mole
0.5 kcal/mole
  A-Factor (per abstractable H)
       5-membered ring
       6-membered ring
A = 1011-2
A = 1010'9
Estimated.
                                94

-------
                                Table XX

               ESTIMATED RO'  ISOMERIZATION REACTION RATES
a
Reaction
OCCCC - HOCCCC
0 OH
CCCC - CCCC •
HOCCCCO -* HOCCCCOH
0*
HOCCCCOH -» (HO)2CCCCOH
0'
(HO)2CCCCOH - (HO)2CCCC(OH)2
0
(HO)2CCCC(OH)2 - (HO)3CCCC(OH)2
OH QH
1 .1
cccco • - CCCCOH
log A(s-1)
11.4
11.7
11.2
11.2
10.9'
10.9
11.4
E(kcal/mole)
7.7
13.1
6.5
6.5
4.6
4.6
7.7
kdnin-1)
3.7 x 107
8.6 x 103
1.9 x 10s
1 .9 x 10s
2.2 x 109
2.2 x 109
3.0 x 108
            OH
Notation:  CCCCO*
 OH                   OH
.1                    I
CCCCOH represents  CH3CHCH2CH20»
   OH
CH2CHCH2CH2OH
                                   95

-------
Reaction of NO, with HOg


     These species have long been thought to react via a radical dispropor-

tionation to give HONO and 02:


                         H02 +  N02  -  HONO + 02                       (55)


Recently, however, Niki and coworkers83  have studied the reaction and could

not detect any HONO.  They concluded that the predominant reaction is:

                                    M
                         H02 +  N02  *  HOONQ2                         (56)


This conclusion is also supported by some of Heicklen's data,84  but the

reaction was not considered explicitly,  and k13 was not determined.  Both

Heicklen85 and Cox86 found that the loss rate due to H02 + N02  is about

2-10 x 107 M"1 s-1.  This value is uncertain, however, because  they did not

consider the effect of HOON02.   Calvert and coworkers 87 have also observed

H02N02 and have attempted to obtain some kinetic  information from the chemical

system, but the system is too complicated to allow unambiguous  interpretation.

Both Niki and Calvert observed  the lifetime of HO2N02 to be ~ 6-8 minutes

and both ascribed the loss mechanism to wall reactions.  Thus,  quantitative

kinetic information on the homogeneous reaction is virtually nonexistent.

     Because H02N02 can act as  a radical reservoir or sink,  the  kinetics of

H02N02 can have far-reaching effects in photochemical smog and  in stratos-

pheric chemistry.  According to this scheme, HO2  and NO2 react  to form

H02NO2, which can "store" the reactive species until it homogeneously decomposes

at its natural unimolecular decomposition rate.   At that time,  it releases  the

HO- and NO- back into the reaction mixture to react further with the other
  &       A
species present.  Thus, it is important to estimate the rate constants for

association and decomposition.
                                   96

-------
     As a  starting point for estimating the rate constants, we can use the
 rates determined by Hendry88 for the reaction of peroxyacetylnitrate (PAN) :


        0
     CH-COONO,  -*  CH.COO + N00         log k/s'1 = 16.2 - 26.8/9     (57)
       O     £,       O        £,           *-*

 This reaction is  analogous  to  that  for HO2N02  and  its Arrhenius  parameters
 provide a  good starting point.  The major uncertainty is whether the
 [OO-NO2]   bond  dissociation energy in PAN is equal to that in H02N02 .   For
 most radical association reactions there is no activation energy.  Thus the
 A-factor for the association reaction can be derived from that of the
 decomposition step and AS^ for the reaction.  In the case of PAN  decomposition,
 AS§ for the reaction is estimated to be 42 Gibbs/mole,  giving log A_57  =8.8
 for the association.  This value is not unreasonable for radical  association
 reactions, but may be a little low.

    A detailed estimate for the entropy of H02NO2 was made based  on the
value of 72.2 e.u. for MeONO289 by adjusting for the change of internal
 rotor from a methyl to an OH and including the corresponding rotational
barrier change due to the loss  of two hydrogen atoms, and correcting for
 spin gives S^(HO2NO2)  = 71.6 e.u.  The frequency assignment for the molecule
 is given in Table XXI .  The first five frequencies listed are those actually
observed by Niki, et al.83;  the remaining frequencies are based on those for
FNO3,  H2O2, and HNO3,  with the  low frequency torsions adjusted to give
S°(HO2N02) = 71.6 e.u.  The values used are compatible  with the known
 torsion barriers for 0-OH and O-NO2.   In the transition state, the N-O  stretch
 is assumed to become the reaction coordinate,  and the N02 group is assumed
to be free rotor.  Other vibrational frequencies were lowered as  in Table XXI
 to give an entropy for the transition state that yields the desired high
 pressure A-factor.  If E56 = 0  and Iog10 AS6 = 9.0  (similar to PAN),  then
 log A_56 = 15.9.  The results of the calculations  are  given in Table XXII
                                  97

-------
                            Table XXI
                FREQUENCY ASSIGNMENT FOR H02N02
Frequency in
Molecules
(cm-1)
3540a
1728a
1304a
803a
1396a
633
500
735
125
400
880
200
Frequency in
Transition State
(cm-1)
3540
1728
1304
803
1396
Reaction coordinate
200
435
Free rotor
100
580
150
Type
OH stretch
N03
N03
N03
OH bend
NO stretch
NO2 rock
NO2 wag
O-N02 torsion
OOH bend
00 stretch
HO-0 torsion
From reference 83,
                               98

-------
                 Table XXII
RRKM CALCULATED k/k  FOR HO,NO, DECOMPOSITION
                   00       £  £

E = 23.1 kcal/mole
log A/s-1 = 15.9
E = 25.1 kcal/mole
log A/s-1 = 15.9
E = 27.1 kcal/mole
log A/s-1 = 15.9
Collision Efficiency
0.4
0.46
0.56
0.65
0.5
0.50
0.60
0.68
0.6
0.53
0.63
0.71
                     99

-------
for three high-pressure activation energies and  three  values of  Y,  the



collision efficiency.  The values of k/k  are near unity  at 1  atm and



300 K and are presented as a function of E_56 in Figure 16 for two  values



of the collision efficiency that are expected to bracket  that  of N2 or O2 .



These results show that reactions (56) and (-56) may be very important in



controlling the concentration of NO2 in smog chamber experiments.  In the



following section, the effects of this reaction  will be illustrated by



computer simulations.






     The major question here is whether HO2N02 and PAN are expected to have



the same activation energy for decomposition. Since this question  cannot be



answered with any confidence, the activation energy E_56  may be  used as  an



adjustable parameter in simulating smog chamber  data.  Although  this procedure



is not very satisfactory, it does illustrate the necessity for accurate  rate



data if this issue is to be resolved.
                                  100

-------
1.0
0.5
                                   7
          0.6
                                                    0.4
       23
   25



EM(kcal/mole)
27
                                                            SA-2554-51
   FIGURE 16  Falloff Calculated by RRKM Theory as a Function of
              Activation  Energy for the Reaction H02N02
   H0_
                                     N0
                              101

-------
Simulations of Smog Chamber Experiments






     A major use for an explicit photochemical smog mechanism is to establish



U.S. Environmental Protection Agency regulations for controlling pollutant



emissions into the troposphere.  While it is important to validate a proposed



mechanism, it is  difficult   to use real atmospheric data for this purpose



because of the wide variety of organic reactants,  the complexity of products,



and the presence of capricious transport phenomena.  Smog chambers are often



employed for carrying out experiments on relatively simple reaction mixtures



thought to represent pollutants in the real urban atmosphere;  the results



obtained are useful in testing assumed mechanisms because the effects of



transport phenomena are minimized while temperature and light intensity can



be controlled.





     Associated with smog chambers, however, are several troublesome problems.



The most obvious problem is that the pollutant concentrations are generally



higher in a smog chamber than in the real atmosphere; thus when a reaction



mechanism is applied to real atmospheric problems, there is an extrapolation



into regimes where the mechanism has not been validated.  This extrapolation



could tend to magnify errors in the chemical mechanism and thus it is important



to devise a mechanism which is as accurate as possible in relation to the



smog chamber data.  A second and most troublesome problem is that of "chamber



effects" in which chemical species interact with the walls of the chamber  or



even appear to desorb from the walls.  This manifests itself in a poor mass



balance between reactants and products, and in the sometimes observed necessity



for postulating a radical source associated with the chamber.  Although every



attempt must be made to understand the sources of such problems, there is



always the possibility that an effect ascribed to "chamber effects" is really
                                   102

-------
due to a deficiency in the postulated reaction mechanism; conversely, an



error in the reaction mechanism might conceal effects better ascribed



to the smog chamber.





     Since the postulated reaction mechanism must be tested against smog



chamber data, it is important that the data be of high quality and that



care be taken to minimize "chamber effects."  We have been using data



reported by Pitts and coworkers90 at the Statewide Air pollution Research



Center located at the University of California, Riverside, who have taken



great care in an effort to minimize chamber effects and to characterize



their experimental conditions.





     The reaction mechanism is complex and partly speculative, and therefore



not all elementary reaction steps have been individually measured, yet many



important reaction rates are now well known.91  One may hope that the effects



of the unknown rate constants will not predominate in the reaction mecha-



nism.  Calvert and coworkers,1  Pitts  et al.,21 Niki  et al.,92 and Hechl





et al.,93 have made major strides in elucidating the mechanisms of photo-



chemical smog.  Our efforts are built upon their work,  with the emphasis



placed upon systematically estimating and evaluating families of reactions,



as described in the preceding sections.  Our guiding philosophy has been to



start with a "first guess" mechanism, consisting of well-known reactions and



our own best estimates for other reactions, and then to make any refinements



necessary, within the uncertainties of the experimental data and estimated



rate constants.





     Our work thus far has been primarily concerned with the photooxidation



of propene, butane, and propene/butane mixtures.  Although we are continuing
                                  103

-------
to work on the reaction mechanisms for these species,  we feel  that the
postulated mechanisms are substantially complete,  and  that it  is  possible
to point out the areas of greatest uncertainty.

     Reactions of n-Butane
     Since n-butane is thought to be representative of the straight chain
alkanes present as pollutants in the urban atmosphere, it is used as a
model compound in smog chamber experiments.   The experiments are  performed
on air mixtures containing a few ppm of n-butane and somewhat  less NO and
N02 ; CO is often present  as well.  The initial  concentrations and relative
ratios of RH to NO  and NO to N02 have been varied somewhat in different
experiments to provide data over a range of initial conditions.90
     The major reaction pathways for carbon-containing species in the
n-butane system are depicted in Figure 17. The rate constants  shown corres-
pond to 300 K and one atmosphere of air and are  expressed in units of
min"1 and ppm"1 min"1.  For bimolecular reactions involving 02 , the concen-
tration of 02 (2.1 x 10s ppm) has been multiplied by the appropriate
bimolecular rate constant (units of ppm"1 min"1) to give an effective
first-order rate constant (units of min"1).  The rate  constants shown represent
our best estimates or the best experimental data available.
     The initial attack of OH radical on n-butane is known to  give ~ 86%
sec-butyl radical and ~ 14% n-butyl radical.91  These  radicals combine
very rapidly with O2 to give the corresponding peroxyl radicals.   As long
as NO is present, the peroxyl radicals oxidize NO to form N02  and alkoxyl
radicals, which can go on to react as described  in the preceding   sections.
                                  104

-------
                                                                 at
                                                                 -p
                                                                 3
                                                                 c
                                                                 o
                                                                 9)
                                                                 03
  g
  B"

4
            105

-------
     s-Butoxyl radicals can either react with oxygen to  give  2-butanone  and
H02 ,  or they can decompose to give acetaldehyde and ethoxyl radical;  the
major fate of ethoxyl is to react with oxygen to give acetaldehyde.   Although
acetaldehyde and 2-butanone react with OH and photolyze,  they disappear
only slowly, and the ratio of their yields gives a sensitive  measure  of  the
relative rates for loss of s-butoxyl:   decomposition versus reaction  with O2 .
Since the s-butoxyl decomposition rate is known fairly accurately, and its
reaction with 02 is rather uncertain,  the rate constant  for the  latter
reaction can be adjusted to give the proper relative value.

     n-Butoxyl radical also can react  with 02 or slowly  decompose, but it has
the additional reaction channel of isomerization.  In fact, the  estimated
isomerization rates are so fast that the other possible  reactions hardly
compete.  Examination of Figure 17 shows that about 98% of the original
n-butoxyl radical formed ends up as the polyhydroxylated aldehyde (HO)3CCH2CHO
and only a small amount appears as butanal and other products.  The fate of
(HO)3CCH2CHO is not known, but if it dehydrates, the product  HO(CO)CH2CHO
might photolyze quickly to give free radicals that can continue  the chain
mechanism.  Although only 14% of the butane reacts by the n-butoxyl reaction
pathways, n-butoxyl accounts for about 36% of the NO oxidized directly by
alkoxyl radicals.  This is directly attributable to the  isomerization reactions

     A reaction not included in our mechanism which might dramatically alter
the course of reactions is:

                        R^R2 + 02  -   R1CR2 + H02                   (58)
                          0              0
                                  106

-------
If this reaction is fast compared to simple addition of O2  to form peroxyl



radical, the isomerization steps would not have an opportunity to take place,



and the character of the n-butane reaction would be quite different from



that described above.  Reliable experimental data are needed in order to assess




the importance of reaction (58), but we would not expect it to compete effectively



with addition of 02 , which has the same A-factor and no activation energy.





     Another area of uncertainty in the mechanism that deserves mention is



the photolysis reactions of aldehydes and ketones.  Photolysis rate constants



and products for many of the carbonyl compounds are not known and must be



estimated.  Radical photolysis products serve to accelerate the overall reaction



and so are very important.  In the  absence of good data, many of the rates  have



simply been estimated by analogy with those rates that are known.  In the butane



simulations presented below, a radical influx from the chamber walls must also



be assumed in order to reproduce the observed rate of butane consumption. It



is quite possible that the assumed radical influx is merely compensating for



an underestimate of the photolysis rates of carbonyl reaction products,  or



some other reaction sequence that has been overlooked so far.  Further exper-



iments are necessary to clear up this point.





     Two computer simulations of the smog-chamber experiment on the n-butane



system are presented in Figures 18 and 19.  The first simulation (Figure 18)



represents our "first guess" mechanism, consisting of experimental rate constants,



where available, and our best estimates for unknown rate constants.  The activ-



ation energy for HO2NO2 decomposition was assumed to equal  that of PAN (26.8



kcal/mole).   Using these rates, an influx of ~ 10~3 ppm min-1 of HO2  radicals



is necessary to approximate the correct conversion rate of  n-butane.   It is



noteworthy that H02NO2 acts as a radical reservoir—storing H02 radicals from



the early period of the reaction and slowly releasing them  in the later stages.
                                  107

-------
     12

     4.1

     10

    3.90

    3.80
  O
  <
  cc
  o
  O
  o
     01

     0.3

     0.2

     0.1

      0
       »-*—.
                                          BUTANC
                                           H02N02
              45
                      90
                                                  270
                                                          315
                                                                 360
                            135     180     225
                               TIME/MINUTES
(a)   Simulation of Run EC-41 in Reference 90.  Initial Concentrations:
     Butane,  4.03 ppm; N02,  0.068 ppm; NO,  0.524 ppm.

     The points are experimental results; the lines represent the
     computed concentration  profiles for butane and peroxynitric acid.
     Radical  input is 1 x 10~3 ppm min"1 of HO,.  The rate of decom-
     position of H02NO2 has  an assumed activation energy of 26.8 kcal/mole.
                                           T
                                                         T
                                           I*'-.
                     90     135     180      225     270     315     360
(b)  Simulation of run EC-41,  as in 7(a) ,  showing the Concentrations of
     NO2 ,  NO,  and ozone.
                                FIGURE  18
                                   108

-------
                                                               PI
                                                               n
                                                               i-.
                                                               U)
                                                            UJ
                                                            I-
g,
ft
                                                                     X  to
                                                                        to
                                                                    M  CIS

                                                                     M  fi
                                                                    •H  OJ

                                                                    •P  in
ti
•H

r-l CT

g *„

3§
Oj

    O

 •  ti
O  O
O^ "H
   -P
0) -H
o  w
c  o   •
Q)  C^  Q)
rl  S  rH
Q)  O  O
«H  O  B
a>  cu  \
OJ -O  rH
       a)
d      Oj
                                                                     r-l rH   >
                                                                     3  I   -H
                                                                     s  e  -p
                                                                     -H  -H  O
                                                                     W  6  01
IAIdd/NOIlVHlN30NOO
                     109

-------
Much of the nitrogen is tied up as H02NO2,  and relatively less is present  as



N02, affecting both the PAN yield and 03  production.   It may be argued that



HO2NO2 is expected to contribute to the experimental  N02 measurement  (as does



PAN),  and thus the NO2 data may represent  the sum of  contributions from



H02N02 and N02.  This question about the correct interpretation of the exper-



imental  N02  concentration adds an extra  element of  uncertainty in comparing



the simulation to the experiment and must  be resolved by laboratory experiments,



Another feature of this first simulation is that ozone and PAN production  are



greatly underestimated as is the consumption of butane.  This is due  to the



quenching effect HO2N02 formation has on the reaction mechanism.





     If the H02N02 decomposition activation energy is less than 26.8  kcal/mole,



the influence of H02N02 formation becomes  less important.  If the activation



energy for decomposition of H02N02 is assumed to be ~ 23 kcal/mole, H02NO2



has little  effect ,    and the simulation is in much better agreement with



experiment (see Figure 19).    Moreover, an influx of  2 x 10~4 ppm min"1



of radicals must be assumed to match the observed conclusion rate of  n-butane.



Note that PAN and ozone formation are near the experimental values and HO2NO2



concentrations are too low to be shown in the figure.  Our experience with



simulations of this nature is that the activation energy for HO2NO2 decompos-



ition probably falls somewhere between 23  kcal/mole and 25 kcal/mole, but



this number is highly tentative, and we must await an  experimental determination



before this major uncertainty can be resolved.





     Once the overall mechanism has been brought into good agreement  with



experiment, various rate constants can be adjusted within their uncertainties



to bring the various product yields into agreement.  For example, our  first-



guess mechanism predicts  .018 ppm of 2-butanone and .17 ppm of acetaldehyde
                                   110

-------
after 360 minutes, but .125 ppm and .082 ppm, respectively, are observed


in the experiment.   As mentioned earlier, these  product yields depend


mainly  on the following reactions:



                             O*         0

                       CH3CH2CHCH3  -»  HCCH3  + CH3CH2                 (59)



                                          0
                                          II
                                    -*  CH3CCH2CH3 + H02               (60)




Since the rate of reaction (59) is fairly well known, and the rate of


reaction (60) is quite uncertain, the latter can be changed to 8.8 x 105


min"1,  in order to produce the correct product yields.  Unfortunately,  not


many different product species were measured in the experiments, making it


impossible to assess the estimated rate parameters for many of the reactions.




     Reactions of Propene



     The reactions of alkenes in photochemical  smog are quite different


from those of alkanes.  Not only is hydroxyl radical attack important,  but


the reactions of oxygen atoms and of ozone must also be considered (see


Figure 20).  Generally, the reactions which involve addition of these species


to the double bond are very fast and result in alkenes reacting substantially


more quickly than alkanes in the smog environment.



     Although the total rate constants for the reactions of O,  O3,  and  OH


with propene are well known,   neither the products of the reaction,  nor


specific branching ratios into the various product channels are known with


certainty for environmental conditions.  Thus, the propene mechanism relies


considerably on the products observed in the smog chamber data to  define


specific reaction channels.
                                   Ill

-------
          OH
un2=^ru^n3
CH0=CHCH,
2 «*

CH2=CHCH3
_ 0 	 ,-4 	 1 	 : 	 T — *~ nucii utiUH,
3.8 x 10* ppm-1 min-1 * \
02 /6.7xl04 NV 2.7 x 10s
V min-l\ min-1 Q
X y ^v "
HOCH2CCH3 ^ HOCH2 ' + CH3CH
°/\°S
/ CH20 + H02
/ o2 \
HOCH20' 	 >- HCOH + H02
0
0(3P) •
!,, T 	 1- TH.^H PH
1.8 x 103 min-1 J '
0
fW3pN II
0( P) » ^H.O/ + rH.ro *
1 .8 x 103 min-1 2 J ^
0
0(3p) II °2
1.8 x 103 min-1 2
0 0
03 ll II 0,
7.5 x 10-3 min-1 ' ° 2
?
7.5 x 10~3 min-1
           FIGURE 20   Reactions of Propene
                        112

-------
     Unlike the butane system, it has been found that propene reacts quickly



enough so that it is not necessary to assume a constant influx of  radicals



due to chamber effects.  Rather,  one can postulate  that HONO is present



initially (due to H2O + NO + NO2   5±  2 HONO)  and provides a  radical  source



when photolyzed.   Once the reaction has been initiated, further chamber



sources of radicals need not be postulated.  On the other hand, if a chamber



source of radicals is assumed, as in the butane system, good results are



still obtained.





     The most important reactions of propene are shown in Figure 20 . As



noted above, the overall rate constants for the reaction of  OH, O, and 03



are known, but the branching ratios were obtained by computer simulations



of the smog chamber data.  The aldehydes produced in the initial reactions



can be photolyzed to give shorter carbon skeletons  and free  radicals; peroxy-



acetyl radicals formed in the initial steps can react with N02  to  give PAN



or can oxidize NO to NO2 .





     A typical simulation of the  smog chamber data  is presented in Figure 21.



Inspection of the figure shows that product yields  are well  represented by the



assumed mechanism; while better agreement certainly would be desirable,



variation between smog chamber runs suggests that there are  also some uncer-



tainties in the reported data which contribute to lack of precision  in the fit,







     Conclusions




     There are many uncertainties associated with the complex mechanism for



degradation of hydrocarbons in photochemical smog.   In several  cases, we have



used estimation techniques to exploit the limited experimental  data  for



reactions important in these mechanisms.  However,  experimental information
                                 113

-------
                                                 n
                                                 r~
                                                 in
                                                    M E  O
                                                    a a  -H
                                                    o o.  -P
                                                    •H    0!
                                                    •P **  >
                                                    OS O  -H
                                                    fc  •  -P
                                                         o
                                                    §  .
                                                    O O
                                                    O O
                                                    O K  M

                                                    i-H ••  -H
                                                    cs e  to
                                                    •H a  a
                                                    •P ft
                                                    •H    TJ
                                                    a o  v
                                                    M rH  -P
•
o


d)
o
a
V
FH
0)

a)
B3

d
•H

rH
M
rH
1
O


rt
3
05

J
bO

0>
C
0-
lAldd/NOIlVdlN30NOD
                                                   (N
                                                   3
             114

-------
on branching ratios, chamber effects, identities and concentrations of



minor products, and laboratory data on critical reaction rate constants



are necessary to reduce the remaining uncertainties present in our updated



model mechanisms for butane and propene.   Available experimental data can



be simulated fairly well, but there is still considerable latitude in



adjusting many individual rate constants.   Although these uncertainties



do not seem severe in simulating the available data, it is currently



difficult to predict the reliability of the mechanisms when applying them



to atmospheric concentrations.
                                  115

-------
                       REFERENCES AND FOOTNOTES

 1.  K. L. Demerjian, J. A. Kerr,  and J.  G. Calvert, Adv. Environ. Sci.
    Technology, 4, 1 (1974).

 2.   (a)  P. Gray, R. Shaw, and J.C.J.  Thynne, Progress in Reaction
         Kinetics, 4, 63 (1967) ;
     (b)  S. W. Benson and H. E. O'Neal,  Kinetics Data on Gas-Phase
         Unimolecular Reactions,  NSRDS-NBS 21, U.S. Government Printing
         Office, Washington, D.C. (1970).

 3.  L. Batt, R. D. McCulloch, and R. T.  Milne, Int. J. Chem. Kinetics,
    Symposium !_, 441 (1975); L. Batt and R. T. Milne, Int. J. Chem.
    Kinetics, 6, 945 (1974).

 4.  M. Delepine, Bull. Soc., Chim. Fr.,  (3) 13_, 1044 (1895); Beilstein I,
    p. 284.  The compound is reported to detonate by shock.

 5.  P. L. Hanst and J. G. Calvert, J. Phys. Chem., 63, 104 (1959).

 6.  Procedure from J. A. Gray and D.W.G. Style, Trans. Faraday Soc., 48,
     1137 (1952) .

 7.  D. M. Golden, R. Walsh, and S. W. Benson, J. Amer. Chem. Soc., 87,
     4053 (1965) .

 8.   S. W. Benson and G. N. Spokes, J. Amer. Chem. Soc., 89, 2525 (1967);
    D. M. Golden, G. N. Spokes, and S. W. Benson, Angw. Chemie (Int'l Ed.),
     12, 534  (1973) .

 9.   G. Emanuel, Int. J. Chem. Kinetics,  4, 591 (1972).

10.   H. E. O'Neal and S. W. Benson in Free Radicals, Vol. II, Chapter 17,
     275  (1973), edited by Jay K.  Kochi,  John Wiley and Sons, Inc., New York.

11.   L. Phillips and R. Shaw, Tenth Symposium  (International) on Combustion,
     453  (1968), Williams and Williams, Baltimore, Md.

12.   G. Baker and R. Shaw, J. Chem. Soc., 6965  (1965).
                                  116

-------
13.  G. N. Spokes and S. W. Benson, J. Amer. Chem. Soc.,  89, 6030 (1967).

14.  S. W. Benson, et al. , Chem. Rev., 6J3, 279 (1969).

15.  D. R. Stall, E.  F. Westrum, Jr., and G. C. Sinke, The Chemical
     Thermodynamics of Organic Compounds,  John Wiley and Sons,  Inc.,
     New York, 1969.

16.  R. Silverwood and J. H. Thomas, Trans. Faraday Soc., 63, 2476  (1967).

17.  L. Batt and S. W. Benson, J. Chem. Phys., 36, 895 (1962).

18.  G. Baker, et al., J. Chem. Soc., 1286 (1965).

19.  (a)  W. E. Vaughn, Disc. Faraday Soc., 1£, 330 (1951).

     (b)  A. C. Egerton, W. Emele, and G. S. Minkoff, ibid. , 278 (1951).

20.  H. A. Wiebe, A.  Villa, T. M. Hellman, and J. Heicklen, J. Amer. Chem.
     Soc., 95, 7 (1973) .

21.  J. N. Pitts, Jr. and B. J. Finlayson, Angew. Chem.  (Int. Ed.), 14,
     1 (1975) and references cited therein.

22.  L. Batt and R. D. McCulloch, Int. J. Chem. Kinetics, 8, 491 (1976).

23.  Y. Takezaki.and  C. Takeuchi, J. Chem. Phys., 22, 1527 (1954).

24.  D. M. Golden, R. Walsh, and S. W. Benson, J. Amer. Chem. Soc., 87,
     4053 (1965) .

25.  Y. Takezaki, and T. Miyazaki, and N. Nakahara, J. Chem. Phys . , 25,
     536 (1956) .                                                  """

26.  C. W. Gear, The  Numerical Solution of Initial Value  Problems,
     Prentice-Hall, Englwood Cliffs, New Jersey,  1971.

27.  H. E. O'Neal and W. H. Richardson, Comprehensive Chemical Kinetics,
     Vol. 5 (C. H. Bamford and C.F.H.  Tippler, Ed., Elsevier,  Amsterdam,
     1972) .

28.  D. Gray, E. Lissi, and J. JHeicklen, J. Phys. Chem.,  7£»  I9*9 U972) .

29.  H. A. Wiebe and  J. Heicklen,  J. Amer. Chem.  Soc., 95,  1  (1973).

30.  Pollard and Wyatt, Trans. Faraday Soc., 45,  760 (1949).

                                  117

-------
31.  S. W. Benson,  Foundations of Chemical Kinetics, McGraw-Hill Book
     Co. ,  New York, 1960.

32.  K. J. Reed and J.  I. Brauman, J. Amer . Chem . Soc . ,  97, 1625 (1975).

33.  G. D. Mendenhall,  D. M. Golden, and S. W. Benson,  Int. J.  Chem.
     Kinetics, 7, 725 (1975), see Section

34.  J. Heicklen and H. S. Johnston, J. Amer. Chem. Soc., 84,  4030  (1962).

35.  R. Shortridge  and  J. Heicklen, Can. J. Chem., 5^,  2251 (1973).

36.  J. Heicklen, Advances in Chemistry Series, No. 76,  Vol. II, 23  (1968)

37.  W. G. Alcock and B. Mile, Combustion and Flame, 24, 125 (1975).

38.  K. D. Bayes and N. Washida, 12th    ternational Symposium on Free
     Radicals (January  4-9, 1976), Laguna Beach, California.

39.  S. W. Benson,  Thermochemi ca 1 Kinetics, John Wiley  and Sons, Inc.,
     New York, 1968.

40.  J. Weaver, R.  Shortridge, J. F. Meagher, and J. Heicklen,
     J. Photochem., 4,  109 (1975).
41.  Note that only for  unimolecular reactions is ^3* independent  of  the
     choice of standard  states.  For bimolecular reactions with standard
     states in units of  concentration, the Arrhenius rate constants are
     related by kc  = (RT)kp; for termolecular reactions, kc = (RT)2kp.
     Since thermochemical quantities for gases are tabulated in terms of
     atmosphere as  standard state, this requires considerable care in
     relating forward and reverse reactions (see Ref . 42).

42.  D. M. Golden,  J. Chem. Educ . , 48, 235 (1971).

43.  S. W. Benson and D. M. Golden, "Reactions in Condensed Phases,"
     Chapter II, Vol. 7, in Advanced Physical Chemistry, edited by
     H. Eyring and  D. Henderson, John Wiley and Sons, Inc., New York  (1975)

44.  H. E. O'Neal and S. W. Benson, J. Chem. and Eng . Data, 1J>, 266 (1970).

45.  A. F. Trotman-Dickenson and G. S. Milne, Tables of Bimolecular Gas
     Reactions, NSRDS-NBS9 , U.S. Government Printing Office, Washington,
     D.C. , 1967.
                                  118

-------
46.  E. Ratajczak and A. F. Trotman-Dickenson, Supplementary Tables of
     Bimolecular Gas  Reactions, OSTI, Publishing Department, UWIST,
     Cardiff,  Wales  (1969.

47.  J. A. Kerr and E. Ratajczak, Second Supplementary Tables of Bimolecular
     Gas Reactions, The University, Birmingham (1972).

48.  G. S. Hammond, J. Amer. Chem. Soc. , 77, 334 (1955).

49.  J. L. Franklin et al., lonization Potentials, Appearance, Potentials,
     and Heats of Formation of Gaseous Positive Ions, NSRDS-NBS 26,
     U.S. Government  Printing Office, Washington, B.C. (1968).

50.  The potential energy, vion» of the ion pair (separation = r A)
     relative  to the  separated neutral species of infinity is given by:
             V.    =  — ——  +  (ionization potential-electron affinity)

                                                          14 .4
     All energies in  electron volts, Vion = 0 when r =      _'	 (A) .

51.  Reference 39,  p.  110.

52.  S. C. Chan.  J. T. Bryant, L. D. Spicer, and B. S. Rabinovitch,
     J. Phys. Chem.,  74, 2058 (1970).

53.  Thermodynamically, RTln K   = - AG° = - AH° + TAS°.    For an adiabatic
     reaction with  standard state in atmosphere, AH° = - RT, and the
     energy of AB  is  just the sum of the energies of the reactants A + B.

54.  D. Garvin and  R.  F. Hampson, editors of Chemical Kinetics Data Survey
     VII, NBS IR74-430, Washington, B.C. (1974),

55.  J. Troe, Ber.  Buns. Physiki. Chem., 73, 144 (1964);  73,  906  (1969);
     H. Gaedtke,  H. Hippler, and J. Troe, Chem. Phys. Letters,  16, 177 (1972)

56.  J. N. Pitts, Jr., J. H. Sharp, and S. I. Chan, J. Chem.  Phys., 40,
     3655 (1964) .

57.  S. Jaffe and F.  S. Klein, Trans. Faraday Soc., 62, 3135  (1966).

58.  F. Kaufman in  Chemiluminescence and Bioluminescence,  edited  by
     M. J. Cormier, D. M. Hercules, and J. Lee, Plenum Publ.  Co.,
     New York, 1973,  p. 83.

59.  J. T. Herrpn and  F. S. Klein, J. Chem. Phys., 40, 2731 (1964).

                                 119

-------
60.  H. Hippler,  C.  Schippert, and J. Troe, Int. J. Chem.  Kinetics,
     Symposium !_, 27 (1975) .

61.  H. J. Johnston  and C. Parr, J. Amer. Chem. Sdc.,  85,  2544 (1963).

62.  A. A. Zavitsas, Ibid., 94, 2779 (1972).      !
                                                 )
63.  Z. B. Alfassi and S. W. Benson, Int. J. ChemJ Kinetics,  5,  879  (1973).

64.  AH°(-CO-OCr) is obtained by starting with AH^(HCOOOH)  =  - 65  kcal/mole.
     Assuming the H-C and 0-H bonds are the same as in formic acid (93
     kcal/mole)   and H202 (90 kcal/mole), respectively, we find
     AHf('CO-OOO =   14 kcal/mole and ffLT = 40 kcal/mole,  endothermic.

     In similar fashion we estimate AH°(ON-O-NO) = 22  kcal/mole;
     AH$(H-CO-ONO) = - 44 kcal/mole, and AHj('CO-ONO)  = - 3 kcal/mole.
     This yields for the reaction NO2 + CO -* -CO-ONO,  AHr = 15 kcal/mole.

65.  (a)  L. Batt, R. D. McCulloch, and R. T. Milne, Int.  J.  Chem.
          Kinetics,  6, 945  (1974).

     (b)  L. Batt, R. D. McCulloch, and R. T. Milne, Int.  J.  Chem.
          Kinetics,  Symposium No. !_, 441 (1975).

     (c)  L. Batt and R. T. Milne, Int. J. Chem. Kinetics,  8, 59 (1976).

     (d)  L. Batt and R. D. McCulloch, Int. J. Chem. Kinetics, 8,  911  (1976)

66.  T. Berces and A. F. Trotman-Dickenson, J. Chem. Soc.,  348 (1961).

67.  C. Leggett and  J.C.J. Thynne, J. Chem. Soc., (A), 1188 (1970).

68.  J. M. Ferguson  and L. Phillips, J. Chem. Soc., 4416 (1965).

69.  D. L. Cox, R. A. Livermore, and L. Phillips, J. Chem.  Soc., (B) ,
     245 (1966) .

70.  R. L. East and  L. Phillips, J. Chem. Soc., (A), 1939  (1967).

71.  P. Cadman, A. F. Trotman-Dickenson, and A. J. White,  J.  Chem. Soc.,
     (A) , 2296 (1971) .
                                                 !
72.  F. W^Bires, C. J. Danby, and C. M. Hinshelwood,  Proc. Roy. Soc.
     (London), A239, 154  (1957) .

         T    ~~                               i
73.  N. J./Quee and  J.C.J. Thynne, Trans. Faraday (Soc., 63, 2970 (1967).
                                  120

-------
74.  G. R. McMillan,  J. Amer. Chem. Soc., 82, 2422 (1960).

75.  J. A. Kerr and M. J. Parsonage, Evaluated Kinetic Data  on Gas-Phase
     Addition Reactions, CRC Press, Cleveland, Ohio (1972).

76.  G. Emanuel, Aerospace Report No. TR-0200(4240-20)-5.

77.  D. M. Golden,  R. K. Solly, and S. W.  Benson, J.  Phys.  Chem., 75,
     1333 (1971) .

78.  J. R. Barker,  S. W. Benson, and D. M. Golden, Int. J. Chem. Kinetics,
     9, 31 (1977).  See Section 4, A.

79.  "Semonov Rule,"  see K. J. Laidler, Chemical Kinetics, McGraw-Hill, Inc.,
     New York, 1965,  p. 132.

80.  W.P.L.  Carter, K. R. Darnall, A, C. Lloyd, A. M.  Winer, and J. N. Pitts,
     Jr., Chem. Phys. Letters, 42, 22 (1976).

81.  G. Z. Whitten  and H. H. Hugo, SAI Report EF76-126, Draft Final
     Report (1976) .

82.  S. W. Benson,  Thermochemical Kinetics,  2nd Ed., John Wiley and Sons,
     Inc., New York,  1976.

83.  H. Niki, P. D. Maker, C. M. Savage, and L. P. Breitenbach, Chem. Phys.
     Letters, to be published.

84.  D. Gray, E. Lissi, and J. Heicklen, J.  Phys. Chem., 76, 1919 (1972).

85.  R. Simonaitis  and J. Heicklen, J. Phys. Chem., 78,  653  (1974).

86.  R. A. Cox, Int. J. Chem. Kinetics,  Symposium No.  !_, 379 (1975);
     R. A. Cox and R. G. Derwent, J. Photochem., 4, 137  (1975).

87.  S. Z. Levine,  W. M. Uselman, W.  H. Chan,  J. G. Calvert, and J. H. Shaw,
     Chem. Phys. Letters, to be published.

88.  D. G. Hendry and R. A. Kenley, J. Amer. Chem.  Soc., 99, 0000 (1977).

89.  Reference 15;  J. D. Cox and G. Pilcher, Thermochemistry of Organic
     and Organometallic Compounds, Academic  Press,  Inc., 1970.
                                  121

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90.  J. N.  Pitts, Jr., K. R. Darnall, A.  M. Winer, and J. M. McAfee,
     Mechanisms  of Photchemical Reactions in  Urban Air, Vol. II,
     Chamber Studies, U.S. Environmental  Protection Agency, 600/3-77-014b,
     February 1977.

91.  For a  recent review, see NBS Technical Note  866  (1975) .

92.  See, for example, H. Niki, E. E. Daby, and W. Weinstock, Advan.
     Chem.  Series, 113, 16 (1972).

93.  T. A.  Hecht and J. H. Seinfeld, Environ. Sci. Technol., 6, 47 (1972);
     T. A.  Hecht, J. H. Seinfeld, and M.  C. Dodge, Environ. Sci. Technol.,
     8, 327 (1974) .
                                  122

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                              APPENDIX A
INTERNATIONAL JOURNAL OF CHEMICAL KINETICS, VOL. VII, 943-949 (1975)
          VLPP  Unimolecular Rate Theory
                            JOHN R. BARKER
Department of Thermochemistry and Chemical Kinetics, Stanford Research Institute, Menlo Park,
                                 California 94025
                                  Abstract
   The exact theory is derived for the thermal unimolecular decomposition of gas-phase
molecules activated and deactivated exclusively through heterogeneous collisions with the
walls of a spherical vessel.  This theory is appropriate for the treatment of very-low-pressure
pyrolysis (VLPP) experiments and other experiments carried out at very low pressures.
It is shown, however, that the exact theory is closely approximated by ordinary gas-phase
unimolecular rate theory and that for practical application to experiments the results of
both theories are indistinguishable.

                               Introduction

    In most gas-phase thermal unimolecular  reaction  studies,  heterogeneous
de(activation) is a complication arising at low pressures and which is best avoided.
Maloney and Rabinovitch [1]  considered such heterogeneous  effects for the case
of a  spherical reactor.  They  derived expressions  for  the heterogeneous con-
tribution by writing  down  the diffusion equation and solving  it subject to the
proper boundary conditions.   Implicit in their treatment are the usual assump-
tions of unimolecular rate theory [2, chap. 8], (1)  the lifetimes of activated mole-
cules are random, and (2) the time intervals between colisions are  random.  These
assumptions  lead to time-independent  rate constants  for decomposition and
deactivation [2, chap. 8].
    In very-low-pressure pyrolysis (VLPP) experiments [3] the  pressure is deliber-
ately maintained so low that heterogeneous (de)activation predominates, and gas-
gas collisions are a complication  to be  avoided.   This corresponds to  the low
pressure limit of the analysis  by  Maloney  and Rabinovitch  [1].  Under these
conditions, when an activated  molecule leaves the wall, it has a good chance of
drifting through  a collision-free region for a relatively long period of time, a cir-
cumstance not matched in the gas-gas collision case.   Consequently, the distribu-
tion of time intervals between collisions  (flight times) is not random, and the
gas-phase formulation of thermal  unimolecular rate theory is  not exactly correct
for these conditions.
    In the following analysis, the exact expression for the flight time distribution
(in a spherical reactor) is derived and compared to the random  distribution.  The
                                    123

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differences between the two distributions are relatively small, leading to only
small errors (<5%) if the usual gas-gas unimolecular theory is employed instead
of the exact theory.

                        General Expression for kunl
    If a particle is activated to  the energy range E to E -f- dE, the "random life-
time assumption" [2, p. 9] states that in the absence of collisions the probability
of not decomposing during the time interval (0,t)  is

(1)                         Pd(t)  = exp {-k(E)t |

where k(E) is the rate constant for decomposition of particles excited to energy E\
k(E) can be calculated  by statistical theory  [2, chap. 4—7].
    Presumably the probability  of surviving decomposition in the absence of
collisions is not correlated with Pc(t), the probability of not experienceing a colli-
sion during the same time interval.  Thus  the joint probability of surviving the
time interval (O,/) is Pc(t)Pd(t) = Pc(/)exp{ -k(E)t\.  The probability of decom-
posing during any given increment of time  (t to t  + df) is just k(E)dt.  Thus the
probability of an  activated particle decomposing in the next time increment after
having  survived the interval (0,t) is

(2)               Pd(t)Pc(t)k(E)dt  = Pc(t)k(E)cxp{-k(E)t\dt

    This probability must be integrated over all lifetimes possible during a given
experiment in order to get the total  probability of decomposition during the course
of the experiment [2, p. 10].
 (3)                   Ptot k(E)   =  /  Pd(t)Pe(t)k(E)dt
                                    Jo
    The upper limit r is the maximum lifetime possible in the experiment, that is,
 the duration of the experiment.   Since T is usually many times longer than the
 average flight time or lifetime with respect  to decomposition, little error is intro-
 duced by assuming r =w  .
   If the particles are activated at the rate Re, the steady-state rate of decomposi-
 tion is RcPtot, which may be written [2, chap. 8]
 where [A *] is the concentration of active particles of energy E.
    For collisional activation (strong collision assumption), in the absence of any
 other process, the collisional rate of activation equals the rate of collisional deacti-
 vation :

                            A + M T=± A* + M

 (5)                  Rc = *,[M][A]  = MM][A*] = «[A*J
                                    124

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where  [A] is the total concentration of species A.  Under these conditions  [A*]
is the equilibrium concentration: [A*] =  [A]Pe(E)dE for energy range E to E -f
dE, where  Pe(E) is the equilibrium distribution function.   It  follows that the
rate of activation is given  by Rc =  u[A.]Pe(E)dE, and this expression holds (for
activation),  regardless of whether other channels are open for depletion of [A*].
It should be pointed out that Rc is  the average rate of activation, regardless of
whether it takes place due to gas-gas collisions or due to gas-wall collisions.   The
collision rate w is calculated differently depending on the mode of activation, but
this fact makes no difference.  The  difference between VLPP unimolecular rate
theory and gas-gas unimolecular rate theory is due to the distribution of "flight
times" at the same  average collision rate.
    Under steady-state conditions the expression for the rate of decomposition is
                        —    =  /    —   —  dE =  £UI1i[
                        at      Jo       at
 (6)

where the unimolecular rate constant is

(7)            /tuni = u i  \   P,(E)k(E)exp{- k(E)t\Pc(t)dtdE
                       Jo  Jo
   In the  next section an  expression for Pc(t) will be derived for a spherical
reactor and VLPP conditions.  It is informative, though, to derive k^m for gas-gas
collisions.  In this case the random flight time assumption [2, chap. 8] applies and
 (8)                           Pf(0 =  exp(- co/)
Thus for gas-gas collisions,

(9)

which is the usual expression for a unimolecular rate constant.  It will be shown
below that the final  rate constant for  heterogeneous (de)activation can  be  ex-
pressed in similar form with a multiplicative factor B(E), which is always close to
unity for a spherical reactor:

(10)                 CPP  =  /   B(E)P.(E)
                                           co +

                         for Spherical VLPP Reactor
   A direct way of calculating Pc(t), the probability that the flight time equals
or exceeds /, is to first calculate the path-length distribution and then fold in the
Maxwell-Boltzman velocity distribution.
   The probability that a particle will leave the inner surface of a sphere and have
its velocity vector directed in the range of solid angle w to w + dw is assumed to be
random:

(11)                           p(w)dw =
                                    125

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If 8 is the angle between the velocity vector and the normal to the surface (that is,
the radius vector), eq. (11) can be written

(12)                   P(8)d8 =  -2r ™J * = sin 0 dB

If the sphere is of radius r, the length of the path within the sphere at angle 8 is
s' = 2r cos 0, giving the probability for a path  length s' to s' + ds'\

(13)                            p(s')ds' = |-

The probability that the path length  is greater  than or equal to s is

(I*)

If a particle is moving along a path with speed v to s + dv, the probability that
the flight time is greater than or equal to / is the joint probability that 2r > s > vt
and that the speed is  in the range v to v  + dv:
(15)
                   r     rti
p(v,t)dv = /»(») 2r
The total probability (for all speeds) that the flight time is greater than t is the
integral over speed from 0 to » .   The conditions on p(v,t) can be incorporated
into the integration limits, and the result is
                           vt~\
                         - — jfc
(16)                   Pe(t)  =

where P(v)dv is the Maxwell-Boltzman speed distribution,

(17)              PW.- <,        "V =!•(-=£.)*
and the symbols have their usual meanings.
    Equation (16) can be integrated exactly [4] to give
                                                                  - m}\
where iFi(p,q,x,) is the confluent hypergeometric function [5].
   The collision frequency co for particles with the walk of a sphere is [3]

(19)
                                  126

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Using this identity and the known transformations of the hypergeometric function
[5], the expression for Pc(t) can be put in more familiar terms:
(20)
             Pc(t) = Pe(a) = erf (a1/2) - -£= \\ - exp(-a))
                                         V« (              )
where a = 9/7r(o>/)2.  A semilog plot of this function versus ut  is presented in
Figure  1 along with Pf(f)  for comparison.  It may be observed that the pure
exponential function Pf**(t) is a good approximation to the  overall behavior of
Pe(t), but with slight deviations due to three factors: (1) the fixed geometry of the
reactor allows a considerable collision-free region not found in a homogeneous gas
(ut ^  1); (2) the boundaries of the reactor limit the flight times of particles moving
at average speeds (1 % ut  %  5); (3) the broad velocity  distribution causes a
deviation from the pure exponential after long times (ut ^5).  It is qualitatively
clear, however, that
                         P
                          is closely approximated by
                   1.0
                  10"
              ~a  1C'2
              a.
                  10"
                  10"
                                        6     8     10    12
                                           cot
                                                                14
       Figure 1. Flight-time probability distribution functions. Solid line—exact prob-
       ability for a spherical vassel; dashed line—pure exponential behavior appro-
       priate to gas-gas collisions.
                                        127

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   For the quantitative  assessment of A:^   it is  necessary to integrate  eq. (7)
with eq. (20) substituted  for Pc(t).   Before carrying out the integration, however,
it is convenient to scale the integral  by transforming to a new variable x =
[u + k(E)]t.   This substitution gives
(21)
                   I.VLPP _
1 uk(E)Pe(E)dE
   « + k(E)
               I'
               J o
                                     -^ dx
where Pe(x,z) is just Pe(t) expressed in terms of the new variable x and the para-
meter z — w/[k(E) + «], a function of energy E.  From this it is clear that the
factor B(E) in eq. (10) is just
(22)
   /'
   Jo
                         1-* dx
                         Results and Conclusions
   Equation (21) was evaluated numerically by a fifteen-term Gauss-Laguerre
integration [5, chap. 25], and the B factor is presented in Figure 2 as a function of
a/k(E).  From inspection of this figure it is clear that B never differs from unity
by more than ± 5%.  Under the usual VLPP conditions, ta <3C k(E), and  B is
very close  to unity.  Even in the worst of cases,  gas-phase unimolecular  rate
theory eq. (9) should be quite  adequate since VLPP  experimental  errors are
generally expected to exceed ± 5%.
   The interesting behavior of B(E)  is a direct consequence  of the positive  and
negative deviation of the flight time distribution relative to the random collision-
time distribution.   When k(E) » u, the distribution is hardly sampled at all and
                1.05  -
                1.00
                0.95
                0.90
                               I
                   0.01
0.10
                                                   10
                   1.0
                 cj/ME)

Figure 2. B factor dependence on a/k(E).
                                100
                                 128

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B(E)  ^ 1.  When k(E) « u, the collision-free drift region of the spherical reactor
is important, and more decomposition takes  place than  in the random collision
time distribution, leading to B(E) > \.  When k(E) <  5 in Figure 1), has a slight effect on B(E), but is far less important
than the other two effects mentioned.
    In principle, an expression for Pe(t) can be derived for any geometrical con-
figuration; most VLPP reactors are approximately cylindrical.  The factor B(E)
for other reactor geometries will probably be  of magnitude similar to that calcu-
lated here for the sphere, since the major feature of VLPP appears to be the exist-
ence of a collision-free region not present in a homogeneous gas.
    In conclusion, it was found that the exact theory for a spherical VLPP reactor
differed only slightly from the usual gas-phase unimolecular rate theory.

                             Acknowledgment

    Useful discussions with Sidney W. Benson and David M. Golden are gratefully
acknowledged, as are some helpful suggestions from the referees.
    This  work was supported  by the  U.  S.  Environmental Protection  Agency
under grant R802288.

                               Bibliography
[1]  K. M. Maloney and B. S. Rabinovitch, J. Phjs. Chan., 72, 4483 (1962).
[2]  W. Forst, "Theory of Unimolecular Reactions," Academic Press, New York, 1973.
[3]  For a review, see D. M. Golden, G. N. Spokes, and S. W. Benson, Angav. Chem., Int. Eng. Ed.,
   12, 534 (1973).
[4]  I. S. Gradshteyn and I. M. Ryzhik,  "Table of Integrals, Scries, and Products," Academic
    Press, New York, 1965.
[5]  M. Abramowitz and I. A.  Stegun, "Handbook of Mathematical Functions," Dover, New
   York, 1968, chap. 13.

Received April 8, 1975
Revised June 11, 1975
                                   129

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TECHNICAL REPORT DATA
(Please read Instructions on the reverse before completing)
1. REPORT NO.
EPA-600/3-77-110
2.
4. TITLE AND SUBTITLE
MEASUREMENT OF RATE CONSTANTS OF IMPORTANCE IN SMOG
7. AUTHOR(S)
John R. Barker, Sidney W. Benson, and David M. Golden
9. PERFORMING ORGANIZATION NAME AND ADDRESS
SRI International
333 Ravenswood Avenue
Menlo Park, California 94025
12. SPONSORING AGENCY NAME AND ADDRESS
Environmental Sciences Research Laboratory - RTP, NC
Office of Research and Development
U. S. Environmental Protection Agency
Research Triangle Park., Nnrth r.arnl-ina 27711
15. SUPPLEMENTARY NOTES
3. RECIPIENT'S ACCESSION- NO.
5. REPORT DATE
October 1977
6. PERFORMING ORGANIZATION CODE
8. PERFORMING ORGANIZATION REPORT
10. PROGRAM ELEMENT NO.
lAAfim AF-m (FY-77)
11. CONTRACT/GRANT NO. ;
R 802288
NO.

-
13. TYPE OF REPORT AND PERIOD COVERED
Final 4/73 - 7/77
14. SPONSORING AGENCY CODE
EPA/600/09


16. ABSTRACT
To provide understanding of elementary reactions of importance in smog, a
three-part investigation has been carried out: (1) experimental determinations of
certain elementary reaction rate constants, (2) development of general techniques for
estimating elementary reaction rate constants, and (3) estimation of many reactions
important in smog.
Specific estimated rate constants included the following reactions:
(1) Decomposition of alkoxy radicals
(2) Isomerization of alkoxy radicals
(3) Reactions of alkoxy radicals with oxygen
(4) The reaction H02 + N02 T H02N02
In addition, a limited number of computer simulations were carried out for the photo-
oxidation of n-butane and propene.
17.
a. DESCRIPTORS
* Air Pollution
* Smog
* Reaction kinetics
* Photochemical reactions
Ozone
Hydrocarbons
18. DISTRIBUTION STATEMENT
RELEASE TO PUBLIC
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