120

Corrigenda

Effect of Dissolved Gases on Subcooled Flow Boiling Heat Transfer

%r den Eiafluss geliister Gase auf den Wirmeiibergang beim unterkiihlten Sieden striimender Fliissigkeiten

H. MULLER-STEINHAGEN Auckland (New Zealand)

N. EPSTEIN and A. P. WATKINSON Vancouver, B.C. (Canada)

Chem. Eng. Process., 23 (1988) 115-124

T,, x, on the left-hand side of Fig. 1, p. 116, should be changed to T,, xb.

The two lines immediately below eqn. (5), p. 117, should be changed to:

If the isobaric equilibrium solubility ratio at the surface and bulk temperatures is used instead of Henry’s law. . . .

Equation (13), p. 123 should be changed to

E = i i (Tin, pred - Tn. measI/Tin. meas

The definition of X, given in the Nomenclature, p. 124, should be changed to:

mole fraction of gas dissolved in liquid at partial pressure pg and temperature T,.

(13)

Errata

Binary and Ternary Vapor-Liquid Equilibrium Calculations for Methyl Chloride, Dimethyl Ether and Methanol*

Berechnung van bioPren und terniiren Dampf-Fliissigkeits-Phasengleichgewichten van Systemen aus Methylchlorid, Dimethylether und Methanol

HERBERT WOGATZKI and BERNHARD GUTSCHEt Institut fiir Thermodynamik und Anlagentechnik, Technische Universitlit Berlin, 1000 Berlin (West) 12

Chem. Eng. Process., 24 (1988) 57-62

Page 57, footnote t: the address of Hankel KGaA is Postbox 1100, 4000 Dusseldorf 1 (F.R.G.).

Page 58, r.h. column, line 1: for ‘fraction’ read ‘number’.

Equation (6) should read

Equation ( 12) should read

0, P) rrert = _ - RT ’

Page 59, r.h. column, paragraph 3, final sentence: ‘n-monochlorohydrocarbon group’ should read ‘n-mono- chlorohydrocarbons’.

Page 60, Fig. 2, legend: (1) should read MeCl(CH,Cl).

Page 61, r.h. column, paragraph 3, last line: for ‘eithers’ read ‘ethers’.

Reference 2, first author should read H. Holldorff.

Chem. Enf. Process., 24 (1988) 120 0 Elsevier Sequoia/Printed in The Netherlands