J. D. Isdale

发表

European community R&D strategy in the field of heat exchanger fouling: Projects

P. A. Pilavachi, J. D. Isdale, 1993 .

Debate on Gas-Side Fouling

J. D. Isdale, 1988 .

THE USE OF A PORTABLE PROBE TO STUDY FOULING IN EXHAUST GAS STREAMS

J. D. Isdale, A. C. Scott, G. Cartwright, 1984 .

Fouling of combustion chambers and high-temperature filters

Viriato Semiao, J. D. Isdale, M. Carvalho, 1997 .

Physical properties of sea water solutions: density

J. D. Isdale, R. Morris, R. Morris, 1972 .

Transport properties of nonelectrolyte liquid mixtures—III. Viscosity coefficients for n-octane, n-dodecane, and equimolar mixtures of n-octane + n-dodecane and n-hexane + n-dodecane from 25 to 100°C at pressures up to the freezing pressure or 500 MPa

J. D. Isdale, J. H. Dymond, J. Robertson, 1981 .

Transport properties of nonelectrolyte mixtures. IX. Viscosity coefficients for acetonitrile and for three mixtures of toluene+acetonitrile from 25 to 100°c at pressures up to 500 MPa

J. D. Isdale, J. Dymond, M. A. Awan, 1991 .

Transport properties of nonelectrolyte liquid mixtures. VIII. Viscosity coefficients for toluene and for three mixtures of toluene + hexane from 25 to 100°C at pressures up to 500 MPa

J. D. Isdale, J. Dymond, M. A. Awan, 1991 .

(p, ϱ, T) of n-heptane, toluene, and oct-1-ene in the range 298 to 373 K and 0.1 to 400 MPa and representation by the Tait equation

J. D. Isdale, J. Dymond, R. Malhotra, 1988 .

Transport properties of nonelectrolyte liquid mixtures—VII. Viscosity coefficients for isooctane and for equimolar mixtures of isooctane + n-octane and isooctane + n-dodecane from 25 to 100°C at pressures up to 500 MPa or to the freezing pressure

J. D. Isdale, J. Dymond, N. Glen, 1985 .

p, ϱ, T behaviour for n-hexane + n-hexadecane in the range 298 to 373 K and 0.1 to 500 MPa

J. D. Isdale, K. J. Young, J. Dymond, 1979 .

The rheology of liquids very near to solid boundaries

J. D. Isdale, A. Hayward, 1969 .

(p, ϱ, T) for {(1−x)C6H6 + xC6D6} and {(1−x)C6H6 + xC6F6} in the range 298 to 373 K and 0.1 to 400 MPa

J. D. Isdale, J. Robertson, J. Dymond, 1982 .

Transport properties of nonelectrolyte liquid mixtures—IV. Viscosity coefficients for benzene, perdeuterobenzene, hexafluorobenzene, and an equimolar mixture of benzene + hexafluorobenzene from 25 to 100°c at pressures up to the freezing pressure

J. D. Isdale, J. Robertson, J. Dymond, 1981 .

(P,ϱ,T) OF SOME PURE N‐ALKANES AND BINARY MIXTURES OF N‐ALKANES IN THE RANGE 298 TO 373 K AND 0.1 TO 500 MPA

J. D. Isdale, J. Robertson, J. Dymond, 1982 .

(p, ϱ, T) of {0.5C8H18+0.5(1-C8H16)}, {0.5(CH3)2CHCH2C(CH3)3+0.5(1-C8H16) or 0.5C8H18}, and {0.333C8H18+0.333(1-C8H16)+ 0.333(CH3)2CHCH2C(CH3)3}, in the range 298 to 373 K and 0.1 to 500 MPa

J. D. Isdale, J. Dymond, M. A. Awan, 1988 .

Density measurement at high pressure

J. D. Isdale, J. Dymond, N. Glen, 1985 .

Transport properties of nonelectrolyte liquid mixtures—II. Viscosity coefficients for the n-hexane + n-hexadecane system at temperatures from 25 to 100‡C at pressures up to the freezing pressure or 500 MPa

J. D. Isdale, K. J. Young, J. Dymond, 1980 .

Shear viscosity of methanol and methanol + water mixtures under pressure

J. D. Isdale, A. J. Easteal, L. Woolf, 1985 .

The viscosity of liquid toluene at elevated pressures

J. D. Isdale, J. Dymond, M. Pyda, 1995 .

PRESSURE, DENSITY, TEMPERATURE RELATIONS FOR ((1-X)BENZENE + X(HEXADEUTEROBENZENE)) AND ((1-X)BENZENE + X(HEXAFLUOROBENZENE)) IN THE RANGE 298 TO 373 K AND 0.1 TO 400 MPA

J. D. Isdale, J. Robertson, J. Dymond, 1983 .

Generic Studies for Industrial Heat Exchanger Fouling

J. D. Isdale, 1993 .

Integrated modelling of process heat transfer with combustion and fouling

J. D. Isdale, J. Gomatam, A. Mulholland, 1997 .