• Non ci sono risultati.

Downhole water-oil separation

N/A
N/A
Protected

Academic year: 2021

Condividi "Downhole water-oil separation"

Copied!
4
0
0

Testo completo

(1)

87

iP. Andreussi, L. Antico, M. Bonuccelli, “Stato dell’arte dei modelli e delle tecnologie relative alla separazione downhole” ,TEA DOC No. 01-079 Rev. 0;

iiP. Andreussi, L. Antico “DOWS. Downhole water-oil separation” , DOC.NO.TEA.03.048;

iii K.E.Arnold, P.J. Koszela, “Droplets settling vs. Retention-Time Theories for sizing Oil/Water Separator” SPE Production Engineering, February 1990;

ivB.Hafskjold, H.K. Celius, O.M. Aamo, “A New Mathematical Model for Oil/Water Separation in Pipes and Tanks” SPE Production Engineering, February 1999;

v A. Loginov, C.Shaw, “Completetion Design for Downhole Water and Oil Separation and invert Coning” SPE Production engineering, October 1997 ;

vi B. Zemel, R.W. Bowman, “Residence Time Distribution in Gravity Oil-Water Separation” Jurnal of Petroleum Technology, February 1978;

vii G.B. Wallis “One dimensional Two-Phase Flow “, McGraw-Hill, 1969 ;

viii D. Butterworth, F. Hewitt, “Two-phase Flow and Heat Transfer”, Oxford University Press 1977 ;

ix H.A. Asheim, “Natural downhole separation and its Impact on Production Performance”, SPE Journal, December 1999 ;

x www.pttc.org/solutions/202.htm

xi www.all-llc.com/DOWS/documents.htm

xii www.spe.org

xiii “Applications system downhole for high volume” JTP online” Marzo 2004

(2)

88

xiv B.W. Watson (Halliburton Energy Service Inc., Dallas, Tex), “Method and

Apparatus for Downhole Oil-Water Separation Pumping operations”, US6173768 B1 January 2001

xv M.R. Berry, H.L.McKinizie, L.A. Stuebinger (Texaco, Inc., N.Y.), “Downhole oil and Water Separation System and Method”, US 6092599 July 2000

xvi S.C. Kennedy, L.C. Lee, M.E. Nodine, R.B.Kroeber (Camco International, Inc., Huston,Tex), “Downhole Fluid Separation System”, US 6017456 January 2000

xvii C.Shaw (Baker Hughes Incorporated, Huston, Tex.), “Method and Apparatus for Downhole Fluid separation and Control of Water Production”, US 6131655 October 2000

xviii www.energyconnect.com

xix www.pttc.org/solutions/202.htm

xx John A. Veil “Downhole water-oil separation technology “ Argonne national laboratory may 2000

xxi P. Andreussi, A. Soldati “Fluidodinamica di processo”. Forum editrice universitaria Udinese srl, 196 ;

xxii Bird, R.B. , Stewart W.E and Lightfoot, “Trasport Phenomena”. John Wileh&sons, New York, E.N. 1966 ;

xxiii R.H. Perry :”Perry’s Chemical Engineers’ Handbook” 6th edition

xxiv S.A. Haheim, “Oil-Water slip in inclined pipes and application to downhole separation”, ABB Corporate Research, Norway 2001

xxv www.panamenv.com/api-theory.html

(3)

89

xxvi

digilander.libero.it/nerowolfe/testi%20sito/Il%20disoleatore%20delle%20acque%20di

%20prima%20pioggia.htm

xxvii R.T.Morrison, R.N.Boyd "Chimica Organica", 5a ed. 1991, Casa Editrice Ambrosiana

xxviii S.Longhini, "Il libro della chimica", 1961 Garzanti

xxix M.Nardelli "Introduzione alla chimica Moderna", 2a ed. 1991, Casa Editrice Ambrosiana

xxx www.omacpompe.com

(4)

90

1 A.J. Karabelas “Droplet Size Spectra Generated in Turbolent Pipe Flow of Dilute Liquid-Liquid Dispersion” Westhollow Research Center

2 Mario Graziadio “L’atomizzazione dei combustibili nelle generazione termica” ENEL Produzione-Ricerca

3 P. Andreussi, L. Antico, “Studio di fattibilità del separatore downhole per gravità”

,TEA DOC No. 02-153 Rev. 0

4 Andreussi, L. Antico, “Analisi computazionale del sistema di separazione” ,TEA DOC No. 01-153 Rev. 0

5 S.B.Collins and J.G.Knudsen “Drop-Size Distributions Produced by Turbolent Pipe Flow of Immiscible Liquids” Oregon State University

6 Flores, J. G., Chen,X.T.Sarcia,C.Brill ” Characterization of oil water Flow Patterns in Vertical and deviated Wells”,SPE prod& Facilities14 (2) may 1999

xxxii www.axioma99.it/cromatos.htm

Riferimenti

Documenti correlati

Our drinking water high density polyethylene tanks are designed and manufactured to store foodstuffs, drinking water and to collect rain water or waste water.. Made in

The water mole fraction profile satisfactorily in the simulations, which leads to the conclusion that the EMSO software may well be used for the simulation of a process of separation

In this paper, Aspen Plus simulator is used to simulate extractive distillation and pressure-swing distillation process for separation of mixture of THF-water.. Economic analysis is

FB gasification of coal-oil in water emulsion slurry (COWS) prepared from the Polish coal and containing 47 mass % of coal, 40 mass % of water and 12 mass % of vegetable oil by CO

Combined gases from D-2050 & D-2010 are divided into two parts, the first part flow to the high pressure scrubber D-2280 where the separated gases are directed to the

Lutzu G.A., Dunford N.T., 2019, Algal treatment of wastewater generated during oil and gas production using hydraulic fracturing technology, Environmental Technology, 40,

Unlike the wax formation in the displacement of waxy crude oil, the stationary residual oil layers of Newtonian water- oil displacement are resulted from the balance between

That suggests that low salinity injection water, which may cause a shift in produced water towards lower salinity, can increase the needed residence times of oil/water separators