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    Editorial 

    Source: Journal of Environmental Engineering:;2000:;Volume ( 126 ):;issue: 003
    Author(s): Oliver J. Hao
    Publisher: American Society of Civil Engineers
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    Factors Affecting Nitrite Buildup in Submerged Filter System 

    Source: Journal of Environmental Engineering:;1994:;Volume ( 120 ):;issue: 005
    Author(s): Oliver J. Hao; Jin M. Chen
    Publisher: American Society of Civil Engineers
    Abstract: The accumulation of the nitrification intermediate, nitrite, is undesirable because of its toxicity to fish. The elevated nitrite concentration in wastewater‐treatment processes significantly increases the amount of chlorine ...
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    Kinetics of Microbial By‐Product Formation in Chemostat Pure Cultures 

    Source: Journal of Environmental Engineering:;1988:;Volume ( 114 ):;issue: 005
    Author(s): Oliver J. Hao; Antonio O. Lau
    Publisher: American Society of Civil Engineers
    Abstract: Microbial by‐products are present in large quantities in both activated sludge (AS) systems and chemostat pure cultures. In wastewater AS systems, these by‐products impose additional organic loads on downstream processes. ...
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    Closure to “Kinetics of Manganese(II) Oxidation with Chlorine” by Oliver J. Hao, Allen P. Davis, and Peter H. Chang (May/June 1991, Vol. 117, No. 3) 

    Source: Journal of Environmental Engineering:;1993:;Volume ( 119 ):;issue: 002
    Author(s): Oliver J. Hao; Allen P. Davis
    Publisher: American Society of Civil Engineers
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    Evaluation of On‐Site Waste Disposal System for Nitrogen Reduction 

    Source: Journal of Environmental Engineering:;1989:;Volume ( 115 ):;issue: 004
    Author(s): Richard J. Piluk; Oliver J. Hao
    Publisher: American Society of Civil Engineers
    Abstract: One of the enironmental concerns associated with on‐site wastewater disposal is nitrate contamination of groundwater. The purpose of this study was to design and monitor an experimental on‐site watewater disposal system ...
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    Characterization of Activated Sludge Foams from Two Plants 

    Source: Journal of Environmental Engineering:;1990:;Volume ( 116 ):;issue: 005
    Author(s): George T. Fahmy; Oliver J. Hao
    Publisher: American Society of Civil Engineers
    Abstract: Activated sludge (AS) foams from two wastewater treatment plants are characterized. The foams contained a significant amount of substrate and lipid. Their contents varied from plant to plant and even within the same plant. ...
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    Continuous Pre‐Anoxic and Aerobic Digestion of Waste Activated Sludge 

    Source: Journal of Environmental Engineering:;1990:;Volume ( 116 ):;issue: 005
    Author(s): Oliver J. Hao; Michael H. Kim
    Publisher: American Society of Civil Engineers
    Abstract: Conventional aerobic sludge stabilization requires extensive energy input. Incorporation of endogenous nitrate respiration (ENR) into the aerobic‐digestion system offers the energy‐saving advantage. In the ENR system, ...
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    Use of pH as Control Parameter for Aerobic/Anoxic Sludge Digestion 

    Source: Journal of Environmental Engineering:;1995:;Volume ( 121 ):;issue: 003
    Author(s): Ibrahim Al-Ghusain; Oliver J. Hao
    Publisher: American Society of Civil Engineers
    Abstract: Alternating aerobic/anoxic (A/A) digestion of waste activated sludge offers many advantages over traditional (aerobic or anaerobic digestion) methods. However, one of the main concerns in A/A digestion is the development ...
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    Discussion of “Real‐Time Control of Aerobic‐Anoxic Sludge Digestion Using ORP” by David G. Wareham, Kenneth J. Hall, and Donald S. Mavinic (January/February, 1993, Vol. 119, No. 1) 

    Source: Journal of Environmental Engineering:;1994:;Volume ( 120 ):;issue: 003
    Author(s): Ibrahim AI‐Ghusain; Oliver J. Hao
    Publisher: American Society of Civil Engineers
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    Adsorption Characteristics of Fluoride onto Hydrous Alumina 

    Source: Journal of Environmental Engineering:;1986:;Volume ( 112 ):;issue: 006
    Author(s): Oliver J. Hao; C. P. Huang
    Publisher: American Society of Civil Engineers
    Abstract: Fluoride removal by activated alumina, Type F‐1, depends primarily on the pH and surface loading. The optimal pH for fluoride removal is approximately 5. However, at
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