| 1589 - 1590 |
Regeneration of poisoned nickel catalyst by supercritical CO2 extraction
Vradman L, Herskowitz M, Korin E, Wisniak J |
| 1591 - 1593 |
A dual catalyst bed system for the elimination of hydrogen from CO2 feed gas in urea synthesis
Hao ZP, An LD, Wang HL, Lu GQ |
| 1594 - 1601 |
Production of organic oxygenates in the partial oxidation of methane in a silent electric discharge reactor
Larkin DW, Lobban LL, Mallinson RG |
| 1602 - 1607 |
Prediction of the performance of coked and regenerated fluid catalytic cracking catalyst mixtures. Opportunities for process flexibility
den Hollander BA, Makkee M, Moulijn JK |
| 1608 - 1614 |
Hydrocarbonylation of methyl acetate using a homogeneous Rh(CO)Cl(PPh3)(2) complex as a catalyst precursor: Kinetic modeling
Kelkar AA, Jaganathan R, Chaudhari RV |
| 1615 - 1623 |
Adsorption of cesium, strontium, and cobalt ions on magnetite and a magnetite-silica composite
Ebner AD, Ritter JA, Navratil JD |
| 1624 - 1632 |
A new method of gel-coating polyethyleneimine (PEI) on organic resin beads. High capacity and fast kinetics of PEI gel-coated on polystyrene
Chanda M, Rempel GL |
| 1633 - 1640 |
Seasonal model based control of processes with recycle dynamics
Kwok KE, Chong-Ping M, Dumont GA |
| 1641 - 1649 |
Application of multivariate statistical analysis in batch processes
Zheng LL, McAvoy TJ, Huang YB, Chen G |
| 1650 - 1660 |
Transfer prices for multienterprise supply chain optimization
Gjerdrum J, Shah N, Papageorgiou LG |
| 1661 - 1672 |
Control of wafer temperature uniformity in rapid thermal processing using an optimal iterative learning control technique
Lee KS, Lee J, Chin I, Choi J, Lee JH |
| 1673 - 1685 |
Optimal design and sensitivity analysis of reactive distillation units using collocation models
Seferlis P, Grievink J |
| 1686 - 1693 |
Adsorption equilibria and kinetics of propane and propylene in silica gel
Grande CA, Rodrigues AE |
| 1694 - 1705 |
Calculation of the hydrodynamic permeability of gels and gel-filled microporous membranes
Mika AM, Childs RF |
| 1706 - 1711 |
Fractionation of edible oil model mixtures by supercritical carbon dioxide in a packed column. Part I: Experimental results
Ruivo R, Cebola MJ, Simoes PC, da Ponte MN |
| 1712 - 1719 |
Use of ultrafiltration membranes for the separation of TiO2 photocatalysts in drinking water treatment
Lee SA, Choo KH, Lee CH, Lee HI, Hyeon T, Choi W, Kwon HH |
| 1720 - 1731 |
Mathematical modeling of the pervaporative separation of methanol-methylterbutyl ether mixtures
Gonzalez BG, Uribe IO |
| 1732 - 1739 |
Solubility analysis of drug compounds in supercritical carbon dioxide using static and dynamic extraction systems
Bristow S, Shekunov BY, York P |
| 1740 - 1747 |
New group-interaction parameters of the UNIFAC model: Aromatic methoxyl binaries
Hwang SM, Lee MJ, Lin HM |
| 1748 - 1754 |
An equation of state for polymers and normal fluids using the square-well potential of variable well width
Paredes MLL, Nobrega R, Tavares FW |
| 1755 - 1772 |
Prediction of flow pattern in stirred tanks: New constitutive equation for eddy viscosity
Nere NK, Patwardhan AW, Joshi JB |
| 1773 - 1780 |
Air blowing of supercritical asphalt fractions
Vassiliev NY, Davison RR, Williamson SA, Glover CJ |
| 1781 - 1790 |
A method for estimating the normal boiling point of heavy hydrocarbons suitable for a group-contribution-based equation of state
Coniglio L, Nouviaire A |
| 1791 - 1791 |
Analysis of concentration multiplicity patterns of continuous isothermal mixed suspension-mixed product removal reactive precipitators (vol 39, pg 1438, 2001)
Yin QX, Wang JK, Xu Z, Li GZ |
| 1791 - 1791 |
Multicomponent diffusion. (vol 38, pg 2520, 2001)
Curtiss CF, Bird RB |
