D. K. Al-harbi

发表

Recovery of Mineral Salts and Potable Water from Desalting Plant Effluents by Evaporation. Part II. Proposed Simulation System for Salt Recovery

A. A. Shaikh, H. K. Abdel-aal, K. M. Ba-lubaid, 1990 .

Densities and excess volumes of cyclohexane + hexane between 298.15 K and 473.15 K

S. A. Beg, N. Tukur, D. K. Al-harbi, 1995 .

Chemical Separation Process for Highly Saline Water. 1. Parametric Experimental Investigation

H. Abdel-aal, M. A. Shalabi, D. K. Al-harbi, 1996 .

Chemical Separation Process for Highly Saline Water. 2. System Analysis and Modeling

H. Abdel-aal, M. A. Shalabi, D. K. Al-harbi, 1996 .

Densities and excess volumes of the benzene-cyclohexane system between 298.15 and 473.15 K

S. A. Beg, E. Hamad, N. Tukur, 1994 .

Saturated liquid densities of benzene, cyclohexane, and hexane from 298. 15 to 473. 15 K

S. A. Beg, E. Hamad, N. Tukur, 1993 .

Densities and excess volumes of benzene + hexane between 298.15 and 473.15 K

S. A. Beg, E. Hamad, N. Tukur, 1995 .

Thermal conductivity of isopentane in the temperature range 307–355 K at pressures up to 0.4 GPa

Marc J. Assael, W. Wakeham, L. Karagiannidis, 1991 .

Non-catalytic partial oxidation of sour natural gas

H. K. Abdel-Aal, H. Abdel-aal, M. A. Shalabi, 1998 .

Dual-purpose chemical desalination process

H. Abdel-aal, M. A. Shalabi, D. K. Al-harbi, 1997 .

Study of transient heat transfer in laminar flow of a non-newtonian fluid over a flat plate

S. K. Achwal, D. K. Al-harbi, D. K. Al-Harbi, 1985 .