Separation Characteristics in a Novel Gas–Liquid Vortex Separator

2020 ◽  
Vol 59 (40) ◽  
pp. 18115-18125
Author(s):  
Wen Zhou ◽  
Chenglin E ◽  
Zixuan Li ◽  
Chunxi Lu
2012 ◽  
Vol 38 (1-3) ◽  
pp. 301-305 ◽  
Author(s):  
Koo-Ho Kwon ◽  
Si-Won Kim ◽  
Lee-Hyung Kim ◽  
Joon Ha Kim ◽  
Seungyoon Lee ◽  
...  

1997 ◽  
Vol 32 (1) ◽  
pp. 169-184 ◽  
Author(s):  
J. SCHMIDT ◽  
P. SETO ◽  
D. Averill

Abstract Combined sewer overflows (CSOs) have been recognized for many years as a pollution problem within the Great Lakes ecosystem. CSOs were identified as a source of contamination in 10 of the 17 Canadian “Areas of Concern” designated by the International Joint Commission, and were considered a major problem in Hamilton Harbour and the Metropolitan Toronto Waterfront. Satellite treatment systems (located upstream in the sewerage system) were identified as being significantly more cost effective than other CSO control options in a feasibility study conducted for Metropolitan Toronto. Consequently, a multi-agency initiative was established in 1993 to examine the treatment of CSOs at a pilot-scale facility in the City of Scarborough. The technologies evaluated during two experimental seasons in 1994 and 1995 included a vortex separator, a circular clarifier, a horizontal-flow plate clarifier and an inclined rotary drum screen. Performance of the technologies is being assessed against a draft policy proposed by the Ontario Ministry of Environment and Energy. Results to date have indicated that the vortex separator and the plate clarifier under “best conditions” were capable of 50% TSS removal and 30% BOD5 removal and should be capable of satisfying the policy.


Author(s):  
T O'Doherty ◽  
D A Egarr ◽  
M G Faram ◽  
I Guymer ◽  
N Syred

The fluid residence time characterization of a 3.4 m diameter hydrodynamic vortex separator (HDVS) has been carried out under laboratory conditions. Computational fluid dynamics (CFD) modelling has then been undertaken for the same conditions at which the experimental data were collected and validated against the experimental results, for which reasonable correspondence has been found. Using the results from the CFD modelling and batch inactivation results from the disinfection of secondary treated wastewater, it is shown that the theoretical performance of an HDVS as a contact vessel for disinfection can be determined and the practical applicability of an HDVS for disinfection is confirmed.


2011 ◽  
Author(s):  
Jorge Luis Castellanos ◽  
Victor Manuel Quijada Perez ◽  
Frank Kenyery

1995 ◽  
Vol 51 (2) ◽  
pp. 1206-1212 ◽  
Author(s):  
P. Wagner ◽  
U. Frey ◽  
F. Hillmer ◽  
H. Adrian

1971 ◽  
Vol 1971 (1) ◽  
pp. 361-368 ◽  
Author(s):  
Arthur E. Mensing ◽  
Richard C. Stoeffler

ABSTRACT The use of a continuous-flow vortex separator as a component of an oil spill clean-up system was investigated. Tangential injection of the oil-water mixture into the vortex tube produces buoyant forces which accelerate the lighter oil to the vortex axis. The cleansed water and the core containing the oil are exhausted through exit ports in opposite end walls of the vortex tube. The cleansed water would be returned to the sea and the core flow containing the oil would be stored. Tests of laboratory-scale model vortex separators were made using oil-water mixtures having inlet oil-to-total-flow ratios between 0.002 and 0.3 and for a variety of geometric and flow conditions. The tests were made using four types of oil (napthene-base crude, paraffin-base crude, diesel and No. 6 heating fuel) having viscosities between 3 and 4250 cps (measured at 75 F) and specific gravities between 0.83 and 0.97. The results showed that separator performance may be optimized by proper control of the oil exhaust flow. Under optimum conditions, approximately 90 percent of the injected oil was separated and captured, and the captured flow contained approximately 90 percent oil. Studies were also made to determine the sizes and weights of components for full-scale vortex separators, including the necessary pumps and prime movers.


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