chemical physics of discharges - Argonne National Laboratory

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' 112 axial diffusion through the discharge one, axial diffusion through the reactor zone, production, recombination on the end plate, recombination in the discharge zone, and recombination in the reactor zone. Thus, the interaction between the rate of production and the other rate processes can be conveniently characterized by seven dimensionless groups: 11 - U2 = RI n 2- RIL - rate of atom production in the discharge zone = 'e2 rate of radial diffusion to the wall D12 rate of atom production in the discharge zone p M or &R rate of atom recombination within the discharge zone k: YVl rate of atom production in the discharge zone P !Go,%&! rate of atom recombination within the reactor zone kl yV1 rate of atom production in the discharge zone - W R rate of atom recombination on the end plate - Y'F1 rate of atom production in the discharge zone E k& rate of axial convection VZ rate of atom production in the discharge zone -kdRM rate of axial diffusion through the discharge zone D12 rate of atom production .in the discharge zone *L I rate of axial diffusion through the reactor zone. D12 These dimensionless groups can be further condensed to,yield just two groups relating the overall rates of atom production, transport, and loss: = rate of atom production = U' loss rate of atom loss 115' + 116Iz + l/p - ( 124 I @loss - rate of atom loss - l/k' + 1/612 + 1/u2 r - Otransport - R/L + RIM + $ + 1 In a steady-state experiment, there must be a competition between two rate processes -- a source and a sink. If the source and sink are spatially separated, then a transport process may further complicate the results. In the present case, the rate of atom production can be measured only if rod 1, for if the source is much greater than the sink, no concentration @loss gradient can exist. 2. Significance of k& For purposes of discussion, assume that the rate parameter Id represents the rate of production of atomic hydrogen(c;) via the following ion-electron recombination reaction, H$ + e' A H + H (125) ! f
I I 1 I I I \ Thus, kA(c - c;) = 2 = 2kr(H:)(e') defines the parameter k6. If atomic hydrogen is also produced when water is present via an ion-molecule reaction, H20+ + H2 k; changes to kim > H,O+ + H It is clear from the above that kt, is a composite parameter which rarely can be subdivided into its component parameters from discharge product measurements alone. Furthermore, as shown in Sec. 11. B., the ion and electron concentrations are not uni'form throughout the discharge zone, so an average value, -1 k,, is observed, Thus, the measurement of absolute yields of discharge products is not a fruitful technique for studying discharge-zone kinetics. An exception to this statement occurs when the discharge is initially well characterized and per- turbations are made on this initial state. For example, in the absence and pre- sence of water, the ratio of the above rate parameters becomes + The quantity kim(H20 )AV can be determined provided that the ratio of is measurable and the other quantities are known. 3. Interaction Between Discharge and Reactor Zones values The activity of the reactor-zone walls and the location of the catalytic end plate have a measurable influence upon the atom concentration within the discharge zone and at the discharge-zone boundary. This phenomenon can be used to advantage for the measurement of absolute or relative values of the rate constant of atom production k;. In the absence of reactor-zone sinks, Eqs. (27) and (45) apply, The atom.production rate constant k: can be determined from Eq. (130) provided that (a) the amount o f atom recombination on the discharge-zone walls is known, (b) it remains constant during the measurement process, and (c) it is the dominant atom loss process. . In an electrode discharge, metal sputtering on
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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
Page 63 and 64: \ 0.9 0.8 0.7 06 0.5 0.4 0.3 0.2 01
Page 65 and 66: 65 ' cause of the reduction in the
Page 67 and 68: INTRODUCTION I' Attachment of polar
Page 69 and 70: I 69 EXPERIMENTAL The mass spectrom
Page 71 and 72: + Figure 1 Mixed water and methanol
Page 73 and 74: 73 ' , radius might be expected bec
Page 75 and 76: 75 Negative Ion Mass Spectra of Som
Page 77 and 78: 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 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 130 and 131: {;I . - . .. . - .., . . .. _- .. .
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
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Fig. 1 Process Apparatus -__l.ll__
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v) t- at- InIo Io0 t-Q) loo lcua O
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This study is only an approximation
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Mole Reaction Material ratio time e
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\ i (4) Effect of System Pressure T
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173 Pressure. Since pressure is a c
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175 Table VI X-RAY DATA OF DEPOSIT
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177 Another source of weakness is t
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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
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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
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. .. 386 9 * - r. Y 2 .' d a f' r.
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.) .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
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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
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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. (
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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
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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
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Biphenyl Fraction 448 The low molec
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LUd The actual structural definitio
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I I I I I In m 9 In 2 , I: r- In m
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’. 454 Mechanism I The available
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456 , , . The relatively low yield
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458 h/lethylacetylene, allene and b
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Introduction VAPOR PHASE DECOMPOSIT
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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
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476 Instead a hydrogen deficient fi
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i 478
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480 FATTY ACIDS AND n-ALKANES IN GR
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482 TA5L,E 2. - Carbon number distr
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6. 7. a. 9. 484 Lawlor, D. L., and
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' I ' Sample No. 6 ' 12 IO 8 6 z 4
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. 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
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- '-'. . ' . . values are listed in
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500 (1;) Ten, T. 17.: a;1d,Dic;
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- ~ Resistivity Czlculation 2: 1 j:
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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
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The line broadening at 79OK of the
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13. 14. 15. 16. 17. 18. 19. 20. 21.
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W L, Z 6 m (1: 0 6 d j o 2 ' 1 0.0
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Coals 522 Studies of the 1600 cm-l
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L in ole i c a c id - 0' Two sample
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526 Table 1.- Ultimate analyses of
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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
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534 in the vapor increases with inc
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NH3 NH3 NH3 NH3 Pyridine Pyridine P
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Mole Ratio of Test No. Quinoline to
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IXPROFJCTION D; M. Mason Institute
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-4:c~rciiny to recent studies o ;i4
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544 Table 1. LIGHT EMISSION OF Y"TR
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emission in a few cases may be by d
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LITERATUR2 CITED i. C. -. .' * il.
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co, CH,,OR 1 - OTHER ADDITIVE FRITT
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FRIT 'TED CO, CH,.OR 4 ___ OTHER AD
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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
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__- ._ 562 Table I THERMAL AND PHYS
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ln 4 I 0 4J v \ 1.0 0.8 0.6 L - 0.4
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