EP0888158A1 - Separateur - Google Patents

Separateur

Info

Publication number
EP0888158A1
EP0888158A1 EP97945985A EP97945985A EP0888158A1 EP 0888158 A1 EP0888158 A1 EP 0888158A1 EP 97945985 A EP97945985 A EP 97945985A EP 97945985 A EP97945985 A EP 97945985A EP 0888158 A1 EP0888158 A1 EP 0888158A1
Authority
EP
European Patent Office
Prior art keywords
baffle
tank
free area
separator according
separator
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.)
Ceased
Application number
EP97945985A
Other languages
German (de)
English (en)
Inventor
Neville Paul Chamberlain
Alison Colvin Stewart
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.)
Kvaerner Process Systems Ltd
Original Assignee
Kvaerner Paladon Ltd
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 Kvaerner Paladon Ltd filed Critical Kvaerner Paladon Ltd
Publication of EP0888158A1 publication Critical patent/EP0888158A1/fr
Ceased legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D19/00—Degasification of liquids
    • B01D19/0042—Degasification of liquids modifying the liquid flow
    • 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
    • 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
    • B01D17/0208—Separation of non-miscible liquids by sedimentation
    • B01D17/0211—Separation of non-miscible liquids by sedimentation with baffles

Definitions

  • This invention relates to a separator and, more particularly, to a separator for separating a mixture of relatively high and low density liquids into its separate high and low density constituent parts.
  • the invention is particularly applicable to a 3- phase separator for separating a mixture of high and low density liquids and gas into its separate gaseous, high density and low density constituent parts. It should be appreciated, however, that the invention is of more general applicability and may be used in 2-phase sepaiators intended to separate high and low density liquids and in 2-phase separators intended to separate gas from liquid.
  • 3 -phase separators are commonly used in the oil and gas industry for separating a stream which comprises an aqueous liquid, a hydrocarbon liquid, and a gas into its separate aqueous liquid, hydrocarbon liquid and gas constituent parts.
  • the initial stream may consist of a gas flow in which liquid droplets or foam are entrained, or a substantially liquid flow in which gas bubbles are entrained.
  • the exact design of the separator depends to an extent on the nature of the expected input flow, but in essence the function of the 3 -phase separator is to separate the three constituent parts of the input flow into three separate outputs, one consisting of substantially only aqueous liquid, one consisting of substantially only hydrocarbon liquid, and a third consisting of substantially only gas.
  • a typical 3-phase separator comprises an elongate tank arranged with its axis substantially horizontal.
  • the inlet flow is delivered to one end of the tank and outlets for gas, aqueous liquid and hydrocarbon liquid are provided at the opposite end of the tank.
  • gas, aqueous liquid and hydrocarbon liquid are provided at the opposite end of the tank.
  • the gaseous component migrates to the top of the tank for removal through the gas outlet and the aqueous component settles to the bottom of the tank for removal through an aqueous liquid outlet.
  • the hydrocarbon liquid forms a central zone of the tank between the gaseous component and the aqueous component and, near the outlet of the tank, flows over a weir to a hydrocarbon liquid outlet.
  • a 3 -phase separator may include at least one perforated baffle along its length for controlling the flow of liquid along the tank to allow separation of the aqueous and hydrocarbon fractions of the liquid, and to allow any gas bubbles in the liquid to migrate to the surface thereof to join the gas flow above the liquid phases.
  • more than one perforated baffle may be provided along the length of the tank. Traditionally, the percentage of the baffle area which is open for fluid flow has been substantially constant over the entire height of each baffle.
  • certain 2-phase separators of the prior art have included perforated baffles, the percentage of baffle area which is open being substantially constant over the entire height of each baffle.
  • baffle as used herein means a generally wall-like structure which extends across the fluid flow direction in a tank and which pennits the restricted flow of fluid therethrough.
  • a baffle may be a self-supporting structure which is mounted in a tank or may be fonned by a plurality of separate members which are secured to an appropriate support structure in the tank to form the baffle.
  • the detail of the baffle design will depend on the expected nature of the input flow and, in particular, on the expected ratio of the component parts thereof, the viscosity and surface tension thereof, and on other operating conditions such as temperature, flow rate, and required degree of separation. Also, the detail of the design of the baffle will depend on whether the in-flow of fluid to be separated is at the top or at the bottom of the inlet zone of the separator. However, it would appear to be generally true that operation of a separator can be improved if the variation in baffle free area in accordance with the invention is observed.
  • one aspect of the present invention provides a separator for separating a mixture of high and low density components into its constituent high and low density parts, the separator comprising: an elongate tank with an inlet for receiving an inlet mixture of high and low density components and outlets, spaced from the inlet, for separated high and low density components respectively; and at least one baffle in the tank between the inlet and the outlets thereof, the baffle having a different proportion of free area in a zone adjacent the bottom of the tank than it has in a zone further up the tank.
  • the baffle in which the inlet for fluid to be separated is close to the top of the tank the baffle has several zones of progressively decreasing free area from the bottom thereof towards the upper edge thereof.
  • the baffle may have a continuously decreasing free area from the bottom thereof upwardly.
  • the baffle has several zones of progressively decreasing free area from the upper edge thereof towards the bottom thereof.
  • the baffle may have a continuously decreasing free area from the top thereof downwardly.
  • the upper edge of the baffle is located spaced from the top of the tank to provide a completely open area above the upper edge of the baffle.
  • the upper edge zone of the baffle itself is imperforate.
  • the baffle may include a perforated zone at the top of the tank to assist in gas distribution and foam retention, and an imperforate region immediately below the upper perforate region followed, in the downward direction, by one or more perforate regions for controlling liquid flow.
  • the upper edge of the baffle is spaced from the top of the tank and is imperforate, and the region between the imperforate upper edge of the baffle and the lower edge thereof includes four horizontal bands of progressively increasing free area from the uppermost of said bands to the lowermost thereof.
  • the free area of the uppe ⁇ nost band may be about 7% of the total surface area and the free area of the lowermost band may be about 30% of the total surface area.
  • the free area of the baffle is provided by rectangular perforations.
  • the desired increase in free area towards the bottom of the baffle may be obtained by increasing the density and/or the size of the perforations.
  • the perforations adjacent the imperforate upper edge of the baffle are rectangular openings measuring 10mm x 25mm and the perforations adjacent the bottom of the baffle are square holes 25mm x 25mm.
  • the present invention is not limited to the use of rectangular perforations and, indeed, perforations of other shapes may prove desirable in certain circumstances.
  • the holes may be fonned by perforating and defonning regions of the plate to produce funnel-like openings.
  • the baffle may be formed with a multiplicity of long thin holes extending either vertically or horizontally.
  • Such an anangement can be produced by perforating a solid plate or by fabricating a baffle from a series of strips, bars, angles or other profiles which are spaced apart to provide the required holes.
  • the baffle may, in fact, be fabricated from any combination of plate, strips, bars, angles or other profiles to have particular flow characteristics. If the baffle extends into the gas flow region of the separator the openings may be designed to improve coalescence of droplets, e.g. by selection of an appropriate aspect ratio for the holes.
  • each baffle may exhibit the prefened increasing free area towards the bottom thereof in accordance with the present invention.
  • one or more of the baffles may have other specific designs to improve separation or through-put which do not exhibit the prefened variation in free area in accordance with the invention.
  • the baffle according to the invention is believed to be particularly effective when used at an upstream region of the tank immediately downstream of the inlet thereof.
  • the prefened embodiment of the present invention will offer less total resistance to flow than that of typical prior art baffles and accordingly when used at the inlet end of a separator it may be possible to use a single baffle plate according to the present invention where, in the prior art, a double baffle plate anangement has been necessary.
  • the prefened embodiment of the present invention controls channelling of flow and the fonnation of a plug flow along the vessel. Accordingly, the invention is especially useful in the context of heavy oils with high viscosities and high drag characteristics.
  • the invention is generally applicable to a wide range of separators, and in particular may be applied to separators of the type of which the inlet flow is in the upper part of the separator (in which case the proportion of perforated area will in general be higher adjacent the bottom of the battle) and the separators of the type in which the inlet flow is in the lower part of the separator (in which case the baffle will in general have a larger area of perforation adjacent the upper edge thereof).
  • the illustrated 3 -phase separator 1 comprises an elongate tank 2 which is mounted, in use, with the longitudinal axis 3 thereof substantially horizontal.
  • An inlet 4 is provided adjacent one end of the tank for receiving a mixture of aqueous liquid, hydrocarbon liquid and gas.
  • the mixture received at the inlet 4 is delivered via a vane pack 5 to an inlet zone 6 located adjacent one end of the tank.
  • vane pack 5 located adjacent one end of the tank.
  • From the inlet zone 6 the mixture flows along the tank towards the outlet end 7 thereof. During the course of passage along the tank gas contained in the inlet mixture rises to the top of the tank and eventually leaves the tank via a gas outlet 8.
  • the aqueous liquid sinks to the bottom of the tank and eventually leaves the tank via an aqueous liquid outlet 9.
  • the hydrocarbon liquid forms a layer between the aqueous liquid and the gas and eventually flows over a weir 10 into an outlet zone 11 from which it leaves the tank via a hydrocarbon liquid outlet 12.
  • baffles 13,14 are provided within the tank.
  • the number of baffles used will depend to an extent on the size of the installation, the expected flow rate, and the degree of separation required. In all installations, however, at least one baffle will be provided.
  • at least one of the baffles has a free area adjacent the lower edge thereof which is greater than the free area in a zone of the baffle further up the tank.
  • the variation in free area is applied to the upstream baffle 13 adjacent the inlet zone 6.
  • the variation in baffle free area may also be applied to the baffle 14.
  • this baffle may be designed with other operating characteristics in mind which will dictate other free area anangements.
  • the baffle 13 is divided vertically into five zones or bands.
  • the uppennost zone adjacent the upper edge 15 of the baffle is imperforate.
  • the exact depth of the uppennost zone will depend on operating conditions and on the size of the installation, but for a typical installation in which the tank 2 has a diameter of approximately 3000mm the uppermost imperforate zone may typically have a vertical extent of 100mm.
  • the portions of the baffle 13 located below the uppermost imperforate zone may be divided into four zones or bands of approximately equal vertical extent.
  • the free area of the zones progressively increases from the uppennost zone to the lowennost zone, hi one embodiment of the invention the uppennost zone may have a free area of approximately 7%, the next zone down may have a free area of approximately 12%, the next zone down may have a free area of approximately 25% and the bottom zone may have a free area of approximately 30%. It must be stressed that the actual free areas, the relative size of the different zones of free area and the ratio of the free area of the largest zone to the smallest zone will be selected depending on the particular operating characteristics expected for the particular installation in question. The present invention is not limited to any particular values or combinations of values.
  • the baffle 13 is in the form of a steel plate and the free areas are provided by way of substantially rectangular perforations through the plate.
  • the size and/or density of perforations may be increased relative to those adjacent the upper end of the plate.
  • the portion of the plate having a free area of 7% is fonned with rectangular perforations 10mm x 25mm at appropriate spacings.
  • the zone having a free area of 12% is provided with perforations 10mm x 25mm at a greater density than those of the 7% free area zone.
  • the zone having a free area of 25% is provided with holes 25mm x 25mm and the zone having the free area of 30% is provided with holes 25mm x 25mm at a greater density than in the zone having a free area of 25%.
  • the upstream baffles 13 (generally known as the distribution baffle) has been formed by a particularly robust structure constmcted by securing two baffle plates to appropriate support members. It is believed that in the case of the present invention the need for such a double baffle plate anangement is removed in many installations and a single baffle plate only is required. It should be noted, however, that under certain circumstances it may be desirable for two baffles of variable pitch, in accordance with the present invention, to be located closely adjacent to each other so as to produce a combined effect on the flow pattern through the separator.
  • the present invention is primarily concerned with the design of baffles to improve the flow characteristics of material through an essentially static separator
  • the invention is also applicable to the design of separators for use on floating platforms and barges where the baffle, in addition to controlling the flow of material through the separator, is used to control surging of the liquid within the separator due to platform or barge movement.
  • the present invention is primarily concerned with separators in which the tank extends substantially horizontally, it should be appreciated that the invention is also applicable to separators in which the tank extends substantially vertically and the baffle separates a lower region of the tank into inlet and outlet zones.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Separating Particles In Gases By Inertia (AREA)

Abstract

L'invention concerne un séparateur, par exemple un séparateur à trois phases, comprenant une entrée (4) et des sorties (8, 9 et 12) pour les matières séparées. Une ou plusieurs cloisons (13, 14), placées entre l'entrée (4) et les sorties (8, 9, 12), régulent l'écoulement des fluides. Les cloisons sont perforées et présentent, sur leurs différentes surfaces verticales, un espace libre de taille variable. Afin de créer des conditions de séparation optimales, l'écoulement à l'intérieur du séparateur peut être contrôlé en choisissant la forme et la taille des perforations ainsi que le pourcentage de surface perforée.
EP97945985A 1996-11-29 1997-11-28 Separateur Ceased EP0888158A1 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GBGB9624867.9A GB9624867D0 (en) 1996-11-29 1996-11-29 Separator
GB9624867 1996-11-29
PCT/GB1997/003295 WO1998023351A1 (fr) 1996-11-29 1997-11-28 Separateur

Publications (1)

Publication Number Publication Date
EP0888158A1 true EP0888158A1 (fr) 1999-01-07

Family

ID=10803689

Family Applications (1)

Application Number Title Priority Date Filing Date
EP97945985A Ceased EP0888158A1 (fr) 1996-11-29 1997-11-28 Separateur

Country Status (4)

Country Link
EP (1) EP0888158A1 (fr)
GB (1) GB9624867D0 (fr)
NO (1) NO983473L (fr)
WO (1) WO1998023351A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107965970A (zh) * 2017-10-17 2018-04-27 海盐派特普科技有限公司 一种简易天然气凝液回收系统

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BR0008743B1 (pt) 1999-03-05 2010-02-09 separador de trÊs fases, e, processo para separar uma mistura de gÁs, àleo e Água nos constituintes gÁs, àleo e Água.
DE602004012420T2 (de) 2003-09-09 2008-06-19 Shell Internationale Research Maatschappij B.V. Gas/flüssigkeits-abscheider
AR059164A1 (es) 2006-01-25 2008-03-12 Shell Int Research Integracion de calor
AU2007260016A1 (en) 2006-06-13 2007-12-21 Shell Internationale Research Maatschappij B.V. Glycol separation and purification
DE102007024029A1 (de) * 2007-05-22 2008-11-27 Evonik Degussa Gmbh Mehrphasen-Reaktorsumpf
CN102728087A (zh) * 2012-07-19 2012-10-17 成都德美工程技术有限公司 用于脱硫富液的闪蒸脱烃罐
CN107388652A (zh) * 2017-08-25 2017-11-24 天津商业大学 一种卧式气液分离器
WO2020047214A1 (fr) * 2018-08-29 2020-03-05 Bechtel Oil, Gas And Chemicals, Inc. Distributeur d'admission à dérivation de flux
US11560326B2 (en) 2021-03-08 2023-01-24 Synergy Watercare Solutions Inc. Fluid treatment system and process

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4157969A (en) * 1977-12-29 1979-06-12 Texaco Inc. Settling tank structure

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR576908A (fr) * 1923-12-29 1924-08-28 Dispositif d'épuration des eaux d'égouts par le procédé à l'eau fraîche
FR2487926B2 (fr) * 1980-07-31 1986-04-25 Verbiese Perfectionnement au dispositif permettant l'etablissement d'une loi de repartition determinee du debit dans une veine liquide
FR2713507B1 (fr) * 1993-12-09 1996-01-26 Degremont Perfectionnements apportés aux décanteurs.

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4157969A (en) * 1977-12-29 1979-06-12 Texaco Inc. Settling tank structure

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107965970A (zh) * 2017-10-17 2018-04-27 海盐派特普科技有限公司 一种简易天然气凝液回收系统

Also Published As

Publication number Publication date
NO983473L (no) 1998-09-17
GB9624867D0 (en) 1997-01-15
NO983473D0 (no) 1998-07-28
WO1998023351A1 (fr) 1998-06-04

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