chemical physics of discharges - Argonne National Laboratory

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{;I . - . .. . - .., . . .. _- .. ..., ,, : .......- . .:,.: - . , : ,,; - . .. . :;:.:.:.. .:..:.:. ._.__ . ..... .- .:.. ... - :: . Flg. 1 kh.motlc dlqmm of Factors urd for hyamln E = E1octrod.r L=UqJd Inlet Q--QI Rorr S-Sllko Borrlw U=UltramlC Vlbmta 4 6 0 10 12 14 16 18 20 22 24 26 28 Pcwu h i t y KW /ccx103 FI) 2 Hydrotln. y W tor th. cwx~ol rmctor A1 wlth L without WA !
I I t I, '\ I 'a downstream from the discharge to ensure proper dispersal of spray in the electrode gap. The C-type reactor employed a pair of rectwar electrodes so set in the gas flow as to avoid reactant by-passing. "ne use of D.C. power, necessitated stabilization of the discnarge by means of a resistive load in the electrical circuit. Provision was made to admit liquid spray into the inlet gas stream using the same aerosol generator used in tile type-B reactors. Table 1. Reactor units employed. Type Reactor Flow Area Discharge Discharge Uilectic CoGe cm 2 I idth rjarr ie r cm c1n cm Tubular 81 Centrifwal A2 Fi3.m ileactor A3 A4 2.203 II II n 1.270 0.254 0.127 0.040 2.798 0.560 0.280 0.089 0.15875 II II II rubular Spray Reactor B1 62 1.089 II la270 0.254 1.383 0.277 It II Used Reactor c1 1.4U 0- 635 0.896 0 "O1Y "hicme ss gmJLTs:. Hydrazine yields for the various reactor geometries and the operating variables employed are given in Figs. 2 tm 6. From the data presented in rig 2 to 4, it is evident that the yield varies inversely as an exponential function of the *lower density at pressures under l0Umm of mercury. The effect of pressure also follows a Regative exponentid variation therefore a general equation of the form Y = a exp (-W-cv) adequately describes the results. Of course this correlation of the results does not in any sense give a complete description of the underlying pnysical chemistry involved in the synthesis. Ideally,it would have been preferable to develop separate rate equations in terms of the partial pressures of tne various components in the overall hydrazine 1 synthesis. This would have necessitated a complete product analysis and since,in the present case,these data are lacking the phenomenological approach had to be used. The constants the equation for tne various reactors acd operating conditions used were evaluated using the method of least squares (12). These are tabulated in Table 2. It should be noted in this Table tnat certLin pressure exponential values were bracketed. here the relevant data were lacking for c&cdat&n and ,therefore, the dependence of energy yield upon preesurefdeactors A2 to A4 and B2 were assumed to be the eane RS those found experimentally for Reactors Al and B1.
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)i 1 reesonably complete and accura
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3 inquire about the component of ve
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4 I I 5 To find (t2)av, we assume t
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\ vnich, it is noted can be negativ
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I 7 than or smaller than the second
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i I i I I I ) ) i L , I I . INT1:OD
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13 field per electron is and per co
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. 11. 5. CharRe-Transfer and Ion-Mo
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17 In the followin:: sections much
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above. With that EIN, an estimate o
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21 region in w!iich large, nighlv l
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i ’ understanding: 23 (a) Electro
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Obviously, the secondary ion must h
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27 (22) Franklin, J. L., Munson, M.
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Tables 1-6 present examples of rela
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Table 8 Some Ions Formed by Process
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33 velocity of the reacting partn r
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35 must be added to the Langevin cr
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37 In our laboratory a microwave di
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+ . 4 . r 39 as well as N in a cor0
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ION-MOIECULE REACTION RATES MEASUFI
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43 excitntion 2onditions so that th
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45 In 2 like manner Fig. 3, showing
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47 Absorption Spectra of Transient
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50 maximum fiela. In this manner, a
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52 3 % %- %- 5- a- 7 h W P H 0 L v)
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References I I . A.B.Callear, J.A.G
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._ . _-.. - , , . . ,. . The Pyrex
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58 0 0 0 VI J > I cv . u H a
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.... . 0 2 e I / m 0 H F4 : 1
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\ 0.9 0.8 0.7 06 0.5 0.4 0.3 0.2 01
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65 ' cause of the reduction in the
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INTRODUCTION I' Attachment of polar
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I 69 EXPERIMENTAL The mass spectrom
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+ Figure 1 Mixed water and methanol
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73 ' , radius might be expected bec
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75 Negative Ion Mass Spectra of Som
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A b 1 1 I H I I I FILAMEN T CONTINU
Page 79 and 80: 79 for positive and negative ions,
Page 81 and 82: 51 out to answer some of the questi
Page 83 and 84: 93 INTERACTIONS OF EXCITED SPECIES
Page 85 and 86: L 4 I*C z 0'2 = a, a U x I m 4 m 0
Page 87 and 88: I L I, ; > > E Fig. 3 I50 200 150 1
Page 89 and 90: I 300 r 1 - 200 i io ;' a cn I I. 0
Page 91 and 92: where DISCUSSION OF XESULTS PERTAIN
Page 93 and 94: 93 where the bar indicates values c
Page 95 and 96: 'I i 'I 0 2. 4 6 8 2 [ N]* x' I 0-2
Page 97 and 98: Fig. 14 IO 8 6 4F [NO] x IO-" (mole
Page 99 and 100: for chemiluminescent excitation in
Page 101 and 102: 101 Chemiluminescent Reactions of E
Page 103 and 104: 103 All gases were taken directly f
Page 106 and 107: 10; He: + N2 -. 2He + h': (8) whi!?
Page 108 and 109: description for both diffusion and
Page 110 and 111: B. Ions and Electrons I Consider a
Page 112 and 113: ' 112 axial diffusion through the d
Page 114 and 115: the tube walls occurs continuously
Page 116 and 117: E2R M ' $6"
Page 118 and 119: 1. 2. 3. 4. 5. 6. 7. 8. 9- 10. u. -
Page 120 and 121: 120 . Dlschorge zone Reactor zone 1
Page 122 and 123: 122 In radiation chemistry the cust
Page 124 and 125: 124 4. chemistry seem limited essen
Page 126 and 127: 126 Conversion of Mixtures into Mor
Page 128 and 129: Hydrazine Synthesis in A Silent dle
Page 132 and 133: 1 \ \ \ , \ , \ \ Pmer hnrity K.W.
Page 134 and 135: . I operating fact that the sloGe i
Page 136 and 137: _- of ' . 8. - 7 6, Residence Time
Page 138 and 139: 135 Ionic Reactions in Corona Disch
Page 140 and 141: GAS OUT GAS IN i.ho QUADRUPOLE MASS
Page 142 and 143: - + ( ~ ~ + 0 H ) ~ O ~ ( H~o)~H+ +
Page 144 and 145: 144 i I , , , , . + 1- u 3c w Inu c
Page 146 and 147: 146 SYNTHESIS OF ORGANIC COIGhTDS B
Page 148 and 149: mi5 a- dz CI n I a I n +4 - 0 -I- k
Page 150 and 151: 0 z cu I I I
Page 152: I- I - t d m a .rl Y x c, t-' d k
Page 155 and 156: , 155 This result is significant in
Page 157 and 158: Compound Bond he rgy Li I 82 UBr 10
Page 159 and 160: , ”..’ 3or 25 - 5 20 - s 3 w Y
Page 161 and 162: I 161 THE GLOW DISCHARGE DEPOSITION
Page 163 and 164: Fig. 1 Process Apparatus -__l.ll__
Page 165 and 166: v) t- at- InIo Io0 t-Q) loo lcua O
Page 167 and 168: This study is only an approximation
Page 169 and 170: Mole Reaction Material ratio time e
Page 171 and 172: \ i (4) Effect of System Pressure T
Page 173 and 174: 173 Pressure. Since pressure is a c
Page 175 and 176: 175 Table VI X-RAY DATA OF DEPOSIT
Page 177 and 178: 177 Another source of weakness is t
Page 179 and 180: 179 PLATING IN A CORONA DISCHARGE R
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\ 3 , ,\ 110 v 60 CPS MANOMETER . F
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I i , \ I i & a - P Fig. 3 Reaction
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\ \' C 0 .d * d .- C U d 0) c( 1) L
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I i I . Q) I, s w 0 v) Y 0 a w W a
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I (b) Polarized Light Fig. 6 Cross
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i m v) Y C i! u o) 23 a a- + 191 m
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i, d C .d c c W Q ) 0 0 L1Y 0 000 0
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i e 4 0 wcr -4 4 al 0 0 0 c) cr 13:
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\ E ‘ 1 TIME FOR RUN 13-1 14-1 -
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199 a red heat in this cell using d
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\ , t j \ I, v) 2 Y . C 0 u m .I C
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203 VAPOR PHASE FORMATION OF NONCRY
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BELL JAR STANC TO VACUUM SYSTEM U T
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207 of the boron oxide film, the fi
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i I, 4 I.( Y I- * 0 i f i 3 0.t I I
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211 The Reacticn 3f Oxygen with Car
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2 E, W t- a Z 9 I- a 2 X 0 I50 too
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'i' 100 50 IC 21 5 2.0 2.5 SURFACE
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I- z W 0 w a a 100 80 60 40 20 215
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s., Literature Cited Berkley, C. ,
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7 h \ F 221 600°C and 1 atmosphere
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223 e I'
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R L ' -1 9mm O.D. 5mm I.D. 45mm 0.D
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Figure 5.- Paschen's law curves. 2-
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\ '? I The water-free product gases
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N I + 0" ON i I + 0 u / 0 0 I 0 cu
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- 233 SOME PROBLEMS OF THE KINETICS
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.. . :. ,. .I , . i ? .. . , ... .
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237 Table 2 Experimental Variables
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239 Zhbie I Eerccnt Consumption of
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241 Discussion The systematic varia
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I \ 1 243 FORMATION OF HYDROCARBONS
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h z - a o m a 20 T IME, minutes . F
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I 1 I I I I 0 I 2 3 4 5 TIME, minut
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The next five coluws in table 1 sho
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\ .\ t 251 Given the existence of t
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I L 253 Epple, R. P. and C. M. Apt.
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1 ' Fig. 1 Schematic of flow discha
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5' . ' I 1 257 co, with excess H2,
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1 1 1 moo 1400 1300 c V' I IPOO I I
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i 25i The Dlssocfatior of ToIuere V
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L ! , c PRODUCTS FROM A 28 MC. DISC
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'\ J ?. , .. . : PRODUCT FORMATION
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'9 / I '\ "1 BENZYL CATION AND RADI
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a
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271 tube serve? as the high voltare
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273 ion (1L.). Zxcitei-ion by colli
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Apparatus and Procedure 275 EXPERIM
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. 277 6. A freshly prepared sam le
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observed. The polystyrene (10% solu
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i i (12) c (11) (14) I 281 LITERATU
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FLOW- METER I ADDITIVE SUPPLY * ,28
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285 TABLE 2 Effect of Haloqenated A
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ANALYTICAL RESULTS Some evidence wa
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DISCUSSION 289 The salient features
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? ~ MENBERSHIP IN THE DIVISION OF F
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292 flow of the reactant gas stream
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294 have suitable residence times i
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0 E < h( E l! d K c 0 .- Y 0 t u t
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298 yields of many chemical product
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- ;i Y . 15. Pressure lOmm 5 > 10-
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302 the best and in many practical
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GENERATION AND MEASUREMENT OF AUDIO
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. The transformer secondary and the
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Vaccum-Tube Amplifier The mobile co
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310 f = Power supply frequency in c
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FUFARCI! INSTITUTE OF TFYDLC UNIVER
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J # I / 4) I . . '8 r4 0 r( P
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317 i Cuencb svsten w.nnar;itus use
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epcrte? the noss~kil.itv of nroduct
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1' b t +
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323 ....... - . . . . . . . . . . .
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1 \ i I i , / / / 8 3 1 325 To205 +
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- .- - - . - - . . . - . 327 n + c
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' POWER PLASMA GAS l e , ' I ! I I
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331 f'ENI?AL PF'FCLCCFC Dernis, P.R
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i J 333 ; mosphere (as opposed to a
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; it raised the question, still &?z
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p .I V I .= - - HCN/C(CALC. WITH C
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1 1 339 atmospheric ressure and ach
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RESULTS 341 Composition Dependence
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0.09 0.08 0.07 9 0.06 2 U - .$ 0.05
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II \ to the Slot So that less of th
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i 4 2 HYDROCARBON-NITROGEN REACTION
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I 1 349 c M m ; a e, k M x
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1.0 I - a. I n TEMPERATURE - OK Fig
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353 the experimental results in the
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,) 355 The ceaswed conversion cf ni
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1 6 357 Freezing. 3jpotnesise thzf
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359 \ Frozen Compositior: Calcillat
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I 1 \ 361 -. ne reaction proceecis
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\ 36 3 ' h, I 26. H. Purnell, Gas C
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In experiments on the direct conver
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367 used as blnders, with different
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369 ' i 1. REFERENCES Berber, John
Page 372 and 373:
Distribution and yield rates of pro
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. . I . I 370 . . . . ., . . .. . .
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4 372 090- > E w - m c N O - 0 z :
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A-Feed tank 6-Thermocracker GReceiv
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80 \ 0 70 60 e 40 a U VI 9 30 20 10
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COAL DEASH& AND HIGH-PURITY COKE Wa
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3Pn _. -. - L -J:,J.-;~~~L, ):as se
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S ~ l ~ o n~pg:ading r is the resul
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The range ~f temperatures and gener
Page 390 and 391:
. .. 386 9 * - r. Y 2 .' d a f' r.
Page 392 and 393:
.) .L m 388 I
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TABLE 4 390 DELAYED COKING OF DEASH
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, ! I- on '---
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394 The present method is to keep t
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396 ‘c erperature, while the pres
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2, '! ! Proximate Analysis, wt $ Mo
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0 IS 0 14 LL 9 013 e \ 3 b- m *- 01
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402 HYDROGEN CYANIDE PRODUCED FROM
Page 408 and 409:
404 Before startup, the system is p
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4 OL. ' , I. . TesCs. With.Coals .o
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Table 3.- Product Gas Analyses and
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410 BIBLIOGRAPHY 1. American Public
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Figure 2. Enclosure surrounding hyd
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0 0 f v) C 0 u m I z 2 c 2 r d J w
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0. E c .4 7 .. .c . I ( - Low tempe
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418 cual. A mjor aa\;antage or' the
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420 Ir ?Y ? ? 9 9 9 pc rod n o c o
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422 Table 3. Room-texperature M'dss
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424 state, depending on the strengt
Page 430 and 431:
Table 4. Room-?;ergerature isomer s
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I' 1.3 . /o 9 IO 9 6 a 425 F F 33 I
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Brooks J.D. and Sternhell S. (1957)
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(52) Gib3 T.C. and Greenwood N.N. (
Page 438 and 439:
434 transducer vas then introduced
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436 yield is quite similar. The con
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?-!??? 0 mv, Uh\OhIe . . . . eirlrl
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4. 5. 6. 7. 8. 9. 10. 11. 12. 13. 4
Page 446 and 447:
442 CHEMICAL REACTIONS IN A CORONA
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helium 444 CORONA REACTOR SYSTEM Fi
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446 The ultraviolet spectrum. for t
Page 452 and 453:
Biphenyl Fraction 448 The low molec
Page 454 and 455:
LUd The actual structural definitio
Page 456 and 457:
I I I I I In m 9 In 2 , I: r- In m
Page 458 and 459:
’. 454 Mechanism I The available
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456 , , . The relatively low yield
Page 462 and 463:
458 h/lethylacetylene, allene and b
Page 464 and 465:
Introduction VAPOR PHASE DECOMPOSIT
Page 466 and 467:
462 more efficient hydrogenation. T
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464 place in parallel with fragment
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466 P rl 0, k 7 rnI rn al k a I hl
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458 TABLE I. COMPOSI'IION OF GASEOU
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REFERENCES 1. C. Hirayama and D. A.
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i 472 Reciprocal Arc Enthalpy ,-> F
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474 be pumped down without altering
Page 480 and 481:
476 Instead a hydrogen deficient fi
Page 482 and 483:
i 478
Page 484 and 485:
480 FATTY ACIDS AND n-ALKANES IN GR
Page 486 and 487:
482 TA5L,E 2. - Carbon number distr
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6. 7. a. 9. 484 Lawlor, D. L., and
Page 490 and 491:
' I ' Sample No. 6 ' 12 IO 8 6 z 4
Page 492 and 493:
. 488 uiolecular weight of which ca
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Xississippi (Sample GS). Stock solu
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492 found at 5.7 and 4.9& for the W
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494 mechanisms. However, the voltad
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For pure polynuclcar arom.i;ic hydr
Page 502 and 503:
- '-'. . ' . . values are listed in
Page 504 and 505:
500 (1;) Ten, T. 17.: a;1d,Dic;
Page 506 and 507:
- ~ Resistivity Czlculation 2: 1 j:
Page 508 and 509:
504 o ' C 0s 2 0 v x i 8 2 0 ! P -
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506 i
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d 601 L P LL
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I I I I I I I I m W N W N 0 (D ? 0
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514 was heated under nitrogen in a
Page 520 and 521:
The line broadening at 79OK of the
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13. 14. 15. 16. 17. 18. 19. 20. 21.
Page 524 and 525:
W L, Z 6 m (1: 0 6 d j o 2 ' 1 0.0
Page 526 and 527:
Coals 522 Studies of the 1600 cm-l
Page 528 and 529:
L in ole i c a c id - 0' Two sample
Page 530 and 531:
526 Table 1.- Ultimate analyses of
Page 532 and 533:
528 6. Friedel, R. A., and H. Retco
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egeneration. The system can be seen
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532 and can be expressed in terms o
Page 538 and 539:
534 in the vapor increases with inc
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NH3 NH3 NH3 NH3 Pyridine Pyridine P
Page 542 and 543:
Mole Ratio of Test No. Quinoline to
Page 544 and 545:
IXPROFJCTION D; M. Mason Institute
Page 546 and 547:
-4:c~rciiny to recent studies o ;i4
Page 548 and 549:
544 Table 1. LIGHT EMISSION OF Y"TR
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emission in a few cases may be by d
Page 552 and 553:
LITERATUR2 CITED i. C. -. .' * il.
Page 554 and 555:
co, CH,,OR 1 - OTHER ADDITIVE FRITT
Page 556 and 557:
FRIT 'TED CO, CH,.OR 4 ___ OTHER AD
Page 558 and 559:
340 350 300 400 4 50 500 600 700 80
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0 554 WITH COOLING (PLATE AT 40°C)
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5 56 then t = to when e = 0 2) the
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5 58 The surface heat transfer coef
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Discussion and Results 560 Three br
Page 568 and 569:
__- ._ 562 Table I THERMAL AND PHYS
Page 570:
ln 4 I 0 4J v \ 1.0 0.8 0.6 L - 0.4
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