EP2066420A2 - Procédé de séparation de fluides biphasés et système d'accélérateur associé - Google Patents

Procédé de séparation de fluides biphasés et système d'accélérateur associé

Info

Publication number
EP2066420A2
EP2066420A2 EP07805764A EP07805764A EP2066420A2 EP 2066420 A2 EP2066420 A2 EP 2066420A2 EP 07805764 A EP07805764 A EP 07805764A EP 07805764 A EP07805764 A EP 07805764A EP 2066420 A2 EP2066420 A2 EP 2066420A2
Authority
EP
European Patent Office
Prior art keywords
phase
fluids
fluid
density
separation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP07805764A
Other languages
German (de)
English (en)
Inventor
Michele Sanseverino
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Publication of EP2066420A2 publication Critical patent/EP2066420A2/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02—Separation of non-miscible liquids
    • B01D17/04—Breaking emulsions
    • B01D17/044—Breaking emulsions by changing the pressure
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02—Separation of non-miscible liquids
    • B01D17/0208—Separation of non-miscible liquids by sedimentation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02—Separation of non-miscible liquids
    • B01D17/04—Breaking emulsions
    • B01D17/045—Breaking emulsions with coalescers

Definitions

  • Forming the object of the present finding is a process for the separation of two-phase fluids and the relative accelerator unit.
  • different systems for separating two-phase fluids are known, which are based upon the following principles, used totally or in part, according to the type of unit: the principle of coalescence that indeed induces the phenomenon of coalescence in the particles of dispersed fluid, through coalescing filters or fluid channelling arrays; the principle of separation that induces a laminar flow in the two-phase fluid in order to cancel out the force vectors of a turbulent flow, as well as a natural physical separation of the two fluids, with speed proportional to their difference in density; finally, the principle of removal of the dispersed fluid that separates the fluid at lower density through use of skimmers or by overflow, still in laminar flow.
  • the great disadvantage of known systems consists of the fact that none of them is able to accelerate the separation process of the two-phase fluid.
  • the above systems have all great limitations linked to the following negative aspects:
  • the latter comprises pumping means (o forse il pi ⁇ letterale thrusting means, non Pato dal contesto, ndt) of the two-phase fluid, at least one washing tank, filtering means for the coalescence of the particles, sensors and actuators for controlling flow rate, pressure and temperature, at least one tank for collecting the fluid at a lower density (normally oil) and is characterised by an oil separator capable of generating a controlled field of hydrodynamic pressures, correlated to the density of the fluids to be treated, in order to accelerate the phenomenon of coalescence of the residual particles.
  • a field of pressures accelerates the stratification phenomenon, allowing the phase at lower density (for example oil) to be drawn off and the constant flow of the decontaminated phase (for example water) towards the outlet from the system.
  • the purpose of the finding is therefore to achieve the task of accelerating the separation of two fluids that cannot be mixed, at different density, in turbulent flow. According to a further purpose, the finding is reversible, since it allows the separation of the dispersed phase, without limitations in concentration in the continuous phase.
  • the unit in object comprises a first pumping means (1) of the two-phase fluid, at least one washing tank (2), a second pumping means of the fluid (3), filtering means for the coalescence of the particles (4), (5) with different filtering power, a phase separator (6) that constitutes the heart of the system, at least one tank for collecting the fluid at lower density (7), a system for analysing the decontamination of the residual phase (8), sensors and actuators for controlling flow rate, pressure and temperature.
  • the two-phase fluid to be separated is therefore given the mechanical energy necessary to equalise the pressure drops of the system from the pumping means (1), (3).
  • a first phenomenon of size variation of the particles is induced through forced coalescence in the filtering batteries (4), (5), in order to make the separation process easier.
  • the hydrostatic thrust acting on the particles counteracted by the force vectors induced by the Brownian motion generated by the turbulence of the fluid, allows a first separation of the two phases to be obtained.
  • the fluid is then mechanically channelled, through calibrated diffusers, capable of generating a laminar flow and simultaneously the stratification of the two phases.
  • a controlled field of hydrodynamic pressures is generated, correlated to the density of the fluids to be treated, in order to accelerate the phenomenon of coalescence of the residual particles.
  • Such a field of pressures accelerates the stratification phenomenon, allowing the phase at lower density (for example oil) to be drawn off towards the collection tank (7) and the constant flow of the decontaminated phase (for example water) towards the outlet from the system.
  • the analysis of the decontamination is possible in the system (8) and normally the level of residual pollutant is of the order of a few ppm.
  • the two-phase fluid separation accelerator is therefore the ideal system for the separation of two fluids at different density, in a vast field of application and without restrictions of any sort concerning the fluids, the flow rates, the temperatures, the flow and the characteristics of the location of use. It is recommended for applications in the following fields: mechanics, ironworking, oil, food, shipping, aeronautics, environmental protection, maritime ecology and chemistry.

Landscapes

  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

La présente invention concerne un procédé de séparation de fluides biphasés et unité d'accélérateur associée, comportant un moyen de pompage de fluide biphasé, au moins une cuve de lavage, un moyen de filtration pour la coalescence des particules, des capteurs et des actionneurs pour contrôler le débit, la pression et la température, au moins un réservoir pour recueillir le fluide à faible densité (normalement de l'huile) et est caractérisée par un séparateur d'huile dans lequel un champ contrôlé des pressions hydrodynamiques est généré, corrélé à la densité des fluides à traiter, qui accélère le phénomène de stratification, permettant le prélèvement de la phase à faible densité (par exemple, de l'huile) et l'écoulement constant de la phase décontaminée (par exemple, de l'eau) vers l'orifice de sortie hors du système.
EP07805764A 2006-08-07 2007-08-06 Procédé de séparation de fluides biphasés et système d'accélérateur associé Withdrawn EP2066420A2 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT000051A ITBA20060051A1 (it) 2006-08-07 2006-08-07 Procedimento per la separazione di fluidi bi-fase e relativo impianto acceleratore
PCT/IT2007/000571 WO2008018108A2 (fr) 2006-08-07 2007-08-06 Procédé de séparation de fluides biphasés et système d'accélérateur associé

Publications (1)

Publication Number Publication Date
EP2066420A2 true EP2066420A2 (fr) 2009-06-10

Family

ID=38907201

Family Applications (1)

Application Number Title Priority Date Filing Date
EP07805764A Withdrawn EP2066420A2 (fr) 2006-08-07 2007-08-06 Procédé de séparation de fluides biphasés et système d'accélérateur associé

Country Status (3)

Country Link
EP (1) EP2066420A2 (fr)
IT (1) ITBA20060051A1 (fr)
WO (1) WO2008018108A2 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012090077A1 (fr) 2010-12-28 2012-07-05 Michele Sanseverino Système de séparation accélérée des fluides multiphasiques

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH579939A5 (en) * 1974-06-10 1976-09-30 Hectronic Ag Liquid petroleum product separator - with visible flow resistance indicator and coalescence filters to collector cowls separately withdrawable
FR2402463A1 (fr) * 1977-09-07 1979-04-06 Creusot Loire Appareil compact pour traitement continu d'un effluent aqueux contenant des hydrocarbures emulsionnes
DE3346931A1 (de) * 1983-12-24 1985-07-04 Howaldtswerke - Deutsche Werft AG Hamburg und Kiel, 2300 Kiel Verfahren und vorrichtung zum trennen eines oel-wasser-gemisches
BE1010782A3 (nl) * 1996-12-03 1999-01-05 Atlas Copco Airpower Nv Compressorinstallatie met olie-afscheiding uit condensaat en daarbij gebruikte inrichting voor het afscheiden van olie uit condensaat.
DE59813936D1 (de) * 1998-04-29 2007-04-19 Sulzer Chemtech Ag Verfahren zum Trennen einer ersten von einer zweiten Flüssigkeit
BE1011906A3 (nl) * 1998-05-12 2000-02-01 Atlas Copco Airpower Nv Inrichting voor het scheiden van twee onmengbare vloeistoffen met verschillend soortelijk gewicht.
NO316109B1 (no) * 2001-11-07 2003-12-15 Aibel As En coalescer anordning
GB0323918D0 (en) * 2003-10-11 2003-11-12 Kvaerner Process Systems As Fluid phase distribution adjuster

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2008018108A2 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012090077A1 (fr) 2010-12-28 2012-07-05 Michele Sanseverino Système de séparation accélérée des fluides multiphasiques

Also Published As

Publication number Publication date
WO2008018108A2 (fr) 2008-02-14
ITBA20060051A1 (it) 2008-02-08
WO2008018108A3 (fr) 2008-03-20

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