Pollution Control by Locational Change and Technological Abatement

In recent years, there has been a downward trend in sulfur dioxide concentrations in downtown St. Louis. This paper examines the contribution to this trend from locational changes of polluting sources and from technological abatement. A simple diffusion model is used to relate annual average concentrations to annual emission data. The results suggest that, had there been no abatement activity, the changes in location of sources that occurred between 1963 and 1970 have more or less offset a 40% increase in annual emissions over that period. However, the abatement activity, essentially the consequence of air pollution regulations, may possibly be credited with a decline of 35% in the annual average concentration.     

Evaluation of Kraft Process Pollution Abatement Strategies by Time Series Analysis of Makeup Records

A historical record of monthly chemical makeups for a North American pulp mill has been analyzed by time series methods. The analysis yields estimates for the reduction in sulfur makeup resulting from each of three separate pollution abatement moves: black liquor oxidation, blow heat recovery, and cooking liquor sulfidity reduction. Further analysis yields estimates of sulfurous emissions and of the substantially lower emissions which could have been achieved if sulfidity management had been incorporated in the program.     

Microwave Process for Volatile Organic Compound Abatement

ABSTRACT

The CHA Corporation has completed the U.S. Air Force Phase II Small Business Innovation Research program to investigate the feasibility of using a novel microwave-based process for the removal and destruction of volatile organic compounds (VOCs) in effluents from noncombustion sources, such as paint booth ventilation streams. Removal of solvents by adsorption, followed by the regeneration of saturated granular activated carbon (GAC) by microwave energy, was achieved in a single fixed-bed reactor. Microwave regeneration of the fixed-bed-saturated carbon restored the original GAC adsorption capacity. After 20 adsorption/regeneration cycles, the adsorption capacity dropped from 13.5 g methyl ethyl ketone (MEK)/100 g GAC to 12.5 g MEK/100 g GAC. During microwave regeneration of the GAC fixed bed, the concentrated desorbed paint solvent was oxidized by passing the solvent mixture through a fixed bed of an oxidation catalyst mixed with silicon carbide in a microwave reactor. A 98% oxidation efficiency was consistently achieved from the oxidation of VOCs in the microwave catalytic reactor.     

Air Pollution Abatement in the Ceramic Industry

Air pollution abatement has been a constant concern for the ceramic indudry over the last four decades. The multiplicity of materials involved, numbering in the hundreds of fluxes and refractories for the manufacture of many different types of glasses, results in gaseous as well as particulate reaction products. Methods of abatement through various means have been developed and are in use in the United States and world-wide today.     

Air Pollution Abatement Facilities at Soybean Processing Plants

Soybean processing plants are typical of facilities in which solvent extraction is the major unit operation employed. Hexane solvent is used to treat soybeans, producing both a vegetable oil and a residue meal product. The hexane solvent is separated from the oil and the meal, recycled and used again in a closed loop fashion. At several points in the process vent streams are produced resulting in the atmospheric discharge of hexane vapor. This represents an air pollution problem and facilities are required to eliminate the problem. An economic analysis of pollution abatement requirements for soybean plants indicates that thermal incineration is the optimum system that can be used. However, at high levels of hexane content in the vent streams, a combination of activated carbon adsorption of the smaller stream plus thermal incineration of the larger stream should prove the most desirable form of pollution abatement. The analysis given in this report can be used to determine which pollution abatement system should be used, depending upon the hexane content of the vent streams.     

Federal Air Pollution Prevention and Abatement Responsibilities and Operations

The direct federal role in air pollution control was expanded and intensified by the 89th Congress to include authority for: (1) abatement of international pollution; (2) promulgation and enforcement of regulations regarding emissions from new motor vehicles and engines; and (8) the conduct cf conferences and formulation of advisory recommendations concerning potential air pollution of substantial significance. Experiences under interstate abatement authorities of the Clean Air Act and plans for future activities under the new authorities are discussed.     

Pollution Abatement Energy Usage of Gas Treating and Processing Plants

The body of information presented in this paper is directed to individuals dealing with energy distribution and environmental issues. Production of natural gas demands energy for abatement of air pollutants. Perspective of energy requirements for natural gas production is presented by analysis of a survey of about 20% of the operating gas plants in Texas. The variation of fuel requirements for production is determined for inlet gas streams with increasing concentrations of toxic contaminants. Then the energy requirements of specific abatement devices is presented and the resultant cost of preparing natural gas for distribution is outlined. The average abatement energy requirement is 1.5% of the total energy requirement for gas processing or consumption of less than 0.1 % of the marketed production of natural gas.     

Industrial Planning for Air Pollution Control

Seven general planning concepts for air pollution control are presented for industry’s consideration in this text of a speech delivered at the Air Pollution Control Workshop, New England Conference on Urban Planning for Environmental Health, Tufts University, Medford, Massachusetts, September 9, 1965.     

Industrial Pollution Prevention

The 1992 A&WMA Critical Review was authored by Harry Freeman and members of his staff at the Pollution Prevention Research Branch, Risk Reduction Engineering Laboratory, U.S. Environmental Protection Agency in Cincinnati, Ohio. Mr. Freeman presented the paper "Industrial Pollution Prevention," at the Critical Review session held during the 85th Air & Waste Management Association Annual Meeting in Kansas City, Missouri. Prepared discussions and invited comments presented during the session are published here, as well as closing remarks by Mr. Freeman.     

Industrial Ovens Designed for Air Pollution Control

Abstract

A sample preparation method has been developed in which a powder may be aerosolized and collected onto filter media in the form of a uniform layer of participate matter similar to the EPA Total Suspended Particulate (TSP) aerodynamic diameter. Samples of dusts and powders as small as 100 mg may be prepared for metals analysis by XRF with this method. The method is also applicable to the preparation of samples such as ores, soils, sediments, etc., which may be ground to pass through a #400 Tyler equivalent sieve (37 um geometric diameter) prior to aerosolization. Samples prepared in this manner present a representative aliquot with minimal matrix interferences to the XRF instrument for elements with atomic number as low as 13 (aluminum). This method is equivalent to EPA's Method 3050A digestion and subsequent analysis by either ICP or GFAA for many analytes, while other species (notably Cr) are not as favorable in comparison.     

The Opportunities for the Industrial Scientist-Engineer in Air Pollution Research

The industrial scientist-engineer is characterized by a high level of interest in solving problems, with the honest expectation that a novel solution to a problem will be rewarded by society with attendant economic benefits to his employer and to himself. Markets for new and improved emission control equipment and techniques are being created by the ever increasing public awareness of the consequences of continuing air pollution and suggest that new emission-free processes and manufacturing techniques and products will similarly find ready acceptance if not outright demand.     

Industrial Pollution Prevention! A Critical Review

Abstract

Pyrolytic product distribution rates and pyrolysis behavior of tire-derived fuels (TDF) were investigated using thermogravimetric analyzer (TGA) techniques. A TGA was designed and built to investigate the behavior and products of pyrolysis of typical TDF specimens. The fundamental knowledge of TGA analysis and principal fuel analysis are applied in this study. Thermogravimetry of the degradation temperature of the TDF confirms the overall decomposition rate of the volatile products during the depolymerization reaction. The principal fuel analysis (proximate and ultimate analysis) of the pyrolytic char products show the correlation of volatilization into the gas and liquid phases and the existence of fixed carbon and other compounds that remain as a solid char. The kinetic parameters were calculated using least square with minimizing sum of error square technique. The results show that the average kinetic parameters of TDF are the activation energy, E = 1322 ± 244 kJ/mol, a pre-exponential constant of A = 2.06 ± 3.47 × 10¹⁰ min^?1, and a reaction order n = 1.62 ± 0.31. The model-predicted rate equations agree with the experimental data. The overall TDF weight conversion represents the carbon weight conversion in the sample.     

Abatement of Sulfur Hexafluoride Emissions from the Semiconductor Manufacturing Process by Atmospheric-Pressure Plasmas

Abstract

Sulfur hexafluoride (SF₆) is an important gas for plasma etching processes in the semiconductor industry. SF₆ intensely absorbs infrared radiation and, consequently, aggravates global warming. This study investigates SF₆ abatement by nonthermal plasma technologies under atmospheric pressure. Two kinds of nonthermal plasma processes—dielectric barrier discharge (DBD) and combined plasma catalysis (CPC)—were employed and evaluated. Experimental results indicated that as much as 91% of SF₆ was removed with DBDs at 20 kV of applied voltage and 150 Hz of discharge frequency for the gas stream containing 300 ppm SF₆, 12% oxygen (O₂), and 40% argon (Ar), with nitrogen (N₂) as the carrier gas. Four additives, including Ar, O₂, ethylene (C₂H₄), and H₂O_(g), are effective in enhancing SF₆ abatement in the range of conditions studied. DBD achieves a higher SF₆ removal efficiency than does CPC at the same operation condition. But CPC achieves a higher electrical energy utilization compared with DBD. However, poisoning of catalysts by sulfur (S)-containing species needs further investigation. SF₆ is mainly converted to SOF₂,SO₂F₄, sulfur dioxide (SO₂), oxygen difluoride (OF₂), and fluoride (F₂). They do not cause global warming and can be captured by either wet scrubbing or adsorption. This study indicates that DBD and CPC are feasible control technologies for reducing SF₆ emissions.     

A System for Abatement Control Strategy Evaluation

The Air Quality Control Program of the Commonwealth of Massachusetts has developed an implementation plan for the Metropolitan Boston Intrastate Air Quality Control Region as required by PL 90-148. An essential part of the plan was a set of control regulations designed to achieve and maintain an air quality compatible with adopted standards. Control strategy modeling was used as a tool in selecting the most appropriate regulations to achieve this goal. The body of information presented in this paper is directed to those state and county air pollution control officials concerned with the formulation and evaluation of regulations.

The paper details the procedures developed and presents a case history of their use in the region. The system is a synthesis of generally-available software and newly-developed computer programs to provide ahighly automated computational structure. It permits rapid simulation of the emissions resulting from the application of various control regulations. Predictions on the changes expected in ambient air quality levels are then made by the use of the Air Quality Display Model (AQDM).

The initial step in the application was a calibration of the system using predicted and measured annual concentrations. This step yielded correlation coefficients of 0.92 for sulfur dioxide and 0.85 for particulates. Subsequently, the system was used to evaluate the baseline case of uncontrolled sulfur in fuel use. Alternative sulfur control strategies were tested for compatibility with air quality standards. The principal strategies tested were: (a) 1% sulfur uniformly throughout the region; (6) 1% sulfur in core area of region, 2.2% sulfur elsewhere; (c) 0.5% sulfur in core area of region, 2.2% sulfur elsewhere; (d) 0.5% sulfur in core area of region, 1.0% sulfur elsewhere.

Strategies (b) and (d) were implemented into a time phased set of control regulations for the region.

Experience with the system has shown it to be a convenient and rapid method for simulating the effects of control regulations. Furthermore, the utility of this initial model warrants expansion of its application to the other air quality control regions in the Commonwealth.     

The Lead Dioxide Estimation Of Sulfur Dioxide Pollution

A new system of measuring sulfation is presented. Because of its simplicity, operation of large sulfation networks can be accomplished at extremely nominal costs. Because of increased sensitivity, present 1 -month sampling time intervals may be shortened to approximately 1 day. Use of this system will permit more definitive investigations of the relationship of sulfation to sulfur dioxide concentration.     

Interaction of Population Growth,Industrial Growth and Pollution Control

A model is developed which predicts the level of pollution as a function of time given the rate of waste production and the persistence of the pollutant. In general, waste production is a function of the population density and the degree of industrialization of a society. With pollution control programs it is possible to reduce the per capita waste production for a given degree of industrialization. The model demonstrates that in a growth economy such as that of the United States, pollution control programs by themselves only delay the inevitable increase in pollution levels. In the long run population and industrial growth are incompatible with pollution control.     

Process Modifications for Air Pollution Control in Neutral Sulfite Semi-Chemical Mills

The body of information presented in this paper is directed to those individuals concerned with the air pollution control problems of the pulp and paper industry operation. Process modifications introduced at two Company mills, at Big Island, Va. and Tomahawk, Wis., where neutral sulfite semichemical pulping of hardwoods is performed at rates of 550 and 630 tons per day, respectively, are discussed. The methodology and concepts used to minimize total reduced sulfur and total sulfur oxide emissions from the recovery furnace of one of the operations are explained. In another major improvement already implemented in the Big Island Mill conventional hydrogen sulfide emissions from the sulfiting tower, on the order of 8–10 lb as sulfur per ton of pulp, have been completely eliminated by a process modification technique. Other aspects of the operations are described, and a forecast of possible emission levels for mills with a newer technology is made.