Estimating the air emissions of chemicals from hazardous waste landfills

1981 ◽  
Vol 4 (3) ◽  
pp. 235-244 ◽  
Author(s):  
L.J. Thibodeaux
1985 ◽  
Vol 19 (10) ◽  
pp. 986-991 ◽  
Author(s):  
Robert G. Lewis ◽  
Barry E. Martin ◽  
Donald L. Sgontz ◽  
James E. Howes

1990 ◽  
Vol 6 (5) ◽  
pp. 23-51 ◽  
Author(s):  
E. Timothy Oppelt

In the United States over the last ten years, concern over important disposal practices of the past has manifested itself in the passage of a series of federal and state-level hazardous waste cleanup and control statutes of unprecedented scope. The impact of these various statutes will be a significant modification of waste management practices. The more traditional and lowest cost methods of direct landfilling, storage in surface impoundments and deep-well injection will be replaced, in large measure, by waste minimization at the source of generation, waste reuse, physical/chemical/biological treatment, incinceration and chemical stabilization/solidification methods. Of all of the “terminal” treatment technologies, properly-designed incineration systems are capable of the highest overall degree of destruction and control for the broadest range of hazardous waste streams. Substantial design and operational experience exists and a wide variety of commercial systems are available. Consequently, significant growth is anticipated in the use of incineration and other thermal destruction methods. The objective of this paper is to examine the current state of knowledge regarding air emissions from hazardous waste incineration in an effort to put the associated technological and environmental issues into perspective.


1996 ◽  
Vol 34 (7-8) ◽  
pp. 437-444 ◽  
Author(s):  
J. Dollerer ◽  
P. A. Wilderer

Bench-scale experiments with two different types of fixed bed reactor have been conducted in order to investigate the potential of SBBr technology (Sequencing Batch Biofilm Reactor) for treatment of leachates from different hazardous waste landfills. Reactor A was equipped with a membrane oxygenatition system for bubble free transfer of oxygen into the bulk liquid. In constract, reactor B was bubble aerated. The process was found to be remarkably stable. An average DOC removal rate of 68% was achieved with a 12-hour cycle. The emission of biodegradable volatile organic substances was observed to be significantly reduced by using bubble free aeration system.


Epidemiology ◽  
2003 ◽  
Vol 14 (Supplement) ◽  
pp. S103
Author(s):  
S Tarkowski ◽  
A Buczyñska ◽  
Z Murowaniecki ◽  
R Rolecki

2016 ◽  
Vol 58 (6) ◽  
pp. 1046-1058
Author(s):  
Yu Yang ◽  
Yong-Hai Jiang ◽  
Xin-Ying lian ◽  
Bei-Dou Xi ◽  
Zhi-fei Ma ◽  
...  

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