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H.I. Milde
Pulse corona discharge in ESP
H.H. Petersen
An energy conserving pulse energization system
P.L. Feldman, P.J. Aa, L.C. Thanh
Present status of Research‐Cottrell pulse energization technology
L. Salasoo, J. Nelson, R. Schwabe, R. Snaddon (1987)
Estimation of particulate charging and migration for pulsed precipitator applicationsJournal of Electrostatics, 19
M. Abdel-Salam (1991)
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S. Masuda, S. Hosokawa, N. Tachibana, T. Ando, Y. Matsumoto (1987)
Fundamental Behavior of Direct-Coupled Submicrosecond Pulse Energization in Electrostatic PrecipitatorsIEEE Transactions on Industry Applications, IA-23
H.B. Lungen, W. Theobald
Environmental measures in European sinter plants and blast furnaces
P. Lausen
Application of pulse energization on ESP for various processes
B. Rajanikanth, B. Prabhakar (1994)
Modeling of prebreakdown VI characteristics of a wire-plate electrostatic precipitator operating under combined dc-pulse energizationIEEE Transactions on Dielectrics and Electrical Insulation, 1
P.A. Lawless, L. Sparks
Factors leading to electrical breakdown of resistive dust layers and sustained back corona
T.W. Lugar, J.M. Friday
Full scale demonstration results of ESP pulse energization
S. Masuda, S. Hosokawa, N. Tachibana, T. Ando, Y. Matsumoto
Fundamental behaviour of direct‐coupled submicrosecond pulse energization in ESP
R.C. Carr, W. Puille, V.H. Belba, F.A. Horney
Economic and technical comparison of fabric filters and ESP
James Turner, Phil Lawless, Toshiaki Yamamoto, David Coy, Gary Greiner, John McKenna, W. Vatavuk (1988)
Sizing and Costing of Electrostatic Precipitators, 38
Z. Weiming, M. Qingyan, P. Elholm
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H.H. Petersen
New trends in electrostatic precipitation
S. Matts, P.O. Ohnfeldt
Efficient gas cleaning with SF electrostatic precipitators
I. Gallimberti (1988)
Impulse corona simulation for flue gas treatmentPure and Applied Chemistry, 60
P.A. Lawless, L. Sparks
A mathematical model for calculating effects of back corona in wire duct ESP
N. Tachibana, Y. Matsumoto (1990)
Intermittent energization on electrostatic precipitatorsJournal of Electrostatics, 25
H. Milde (1982)
Pulse Corona Discgarge in Electrostatic PrecipitatorsIEEE Transactions on Electrical Insulation, EI-17
N.W. Frisch
Electrostatic precipitators sizing methodologies ‐ a review
J.H Turner
et al
N. Tachibana, Y. Matsumoto
Intermittent energization on ESP
F. Thümmler, W. Thomma (1967)
The sintering processInternational Materials Reviews, 12
E. Landham, J. Dubard, W. Piulle (1990)
The effect of high-voltage waveforms on ESP current density distributionsIEEE Transactions on Industry Applications, 26
H. White (1963)
Industrial Electrostatic Precipitation
O.D. Sinhuber
Improvement of ESP performance with pulse energization
J. Nelson, L. Salasoo (1987)
The Impact of Pulse Enereization on Electrostatic Precipitation PeformanceIEEE Transactions on Electrical Insulation, EI-22
H. Hall (1990)
History of pulse energization in electrostatic precipitationJournal of Electrostatics, 25
G. Dinelli, M. Rea (1990)
Pulse power electrostatic technologies for the control of flue gas emissionsJournal of Electrostatics, 25
P. Lawless, L. Sparks (1980)
A mathematical model for calculating effects of back corona in wire‐duct electrostatic precipitatorsJournal of Applied Physics, 51
H. Petersen (1981)
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J.K. Nelson, L. Salasoo
The impact of pulse energization on ESP performances
P. Lausen (1990)
Application of pulse energisation on electrostatic precipitators for various processesJournal of Electrostatics, 25
W. Puille, J. Dubard, E. Landham, L. Sparks (1984)
Estimate ESP efficiency gains from pulse energization
B.S. Rajanikanth, B.R. Prabhakar
Modeling of prebreakdown VI characteristics of a wire plate ESP operating under combined dc‐pulsed energization
K.J. McLean
Electrostatic precipitators
Investigates the application of the up‐flow anaerobic sludge bed (UASB) reactor for the anaerobic treatment of sewage sludge containing high concentrations of soluble and insoluble sulphides. Assesses the reactor’s performance in terms of volatile organic matter (VOM) and biogas production rate. The average percentage removal of VOM, total sulphide and biogas for the reactor operation without sulphide was 67 per cent, 65mgS/L and 1 L/day, respectively. The corresponding average percentage removal of VOM, total sulphide and biogas production rate for the experiment with 800mgS/L soluble sulphide was 45 per cent, 450mgS/L and 0.7L/day. Equilibrium concentrations of soluble sulphide up to 200mgS/L exert insignificant toxic effects, but toxicity increases as the concentration of soluble sulphide increases. A concentration of soluble sulphide of 1,200mgS/L produces severe toxic effects and the complete termination of gas production. An inhibitory concentration of sulphides affects gas production first, while significant volatile acid accumulation takes place much slower, and only after gas production has been severely retarded. Insoluble sulphide has an insignificant effect on the UASB up to a concentration of at least 800mgS/L. The addition of iron as ferric chloride prevents the toxicity of soluble sulphides as indicated by the minor effect on gas production. Therefore, the use of iron to precipitate sulphide could be used on a continuous basis to reduce sulphide toxicity.
Environmental Management and Health – Emerald Publishing
Published: Dec 1, 1996
Keywords: Anaerobic treatment; Performance monitoring; Sewage; Toxicity
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