AU615689B2 - Creación de Inventos y Patentes con Inteligencia Artificial

AU615689B2 – Hydrocyclone overflow transport
– Google Patents

AU615689B2 – Hydrocyclone overflow transport
– Google Patents
Hydrocyclone overflow transport

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Publication number
AU615689B2

AU615689B2
AU25213/88A
AU2521388A
AU615689B2
AU 615689 B2
AU615689 B2
AU 615689B2
AU 25213/88 A
AU25213/88 A
AU 25213/88A
AU 2521388 A
AU2521388 A
AU 2521388A
AU 615689 B2
AU615689 B2
AU 615689B2
Authority
AU
Australia
Prior art keywords
overflow
cyclone
support plate
vessel
cavity
Prior art date
1987-09-15
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
AU25213/88A
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AU2521388A
(en

Inventor
Gavan James Joseph Prendergast
David Andrew Webb
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.)

Merpro Montassa Ltd

Original Assignee
Delawood Pty 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.)
1987-09-15
Filing date
1988-09-15
Publication date
1991-10-10

1988-09-15
Application filed by Delawood Pty Ltd
filed
Critical
Delawood Pty Ltd

1989-04-17
Publication of AU2521388A
publication
Critical
patent/AU2521388A/en

1991-10-10
Application granted
granted
Critical

1991-10-10
Publication of AU615689B2
publication
Critical
patent/AU615689B2/en

1992-01-23
Assigned to MERPRO MONTASSA LIMITED
reassignment
MERPRO MONTASSA LIMITED
Alteration of Name(s) of Applicant(s) under S113
Assignors: DELAWOOD PTY. LTD.

2008-09-15
Anticipated expiration
legal-status
Critical

Status
Ceased
legal-status
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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

B01D19/0052—Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused

B01D19/0057—Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused the centrifugal movement being caused by a vortex, e.g. using a cyclone, or by a tangential inlet

B—PERFORMING OPERATIONS; TRANSPORTING

B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES

B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES

B04C11/00—Accessories, e.g. safety or control devices, not otherwise provided for, e.g. regulators, valves in inlet or overflow ducting

B—PERFORMING OPERATIONS; TRANSPORTING

B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES

B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES

B04C5/00—Apparatus in which the axial direction of the vortex is reversed

B04C5/12—Construction of the overflow ducting, e.g. diffusing or spiral exits

B—PERFORMING OPERATIONS; TRANSPORTING

B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES

B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES

B04C5/00—Apparatus in which the axial direction of the vortex is reversed

B04C5/24—Multiple arrangement thereof

B04C5/28—Multiple arrangement thereof for parallel flow

Description

AU-AI-25213/88 6 PCT WORLD INTELLECTUAL PROPERTY PCT International Bureau INTERNATIONAL APPLICATION PUBLISHED UNDER THE PATENT COOPERATION TREATY (PCT) (51) International Patent Classification 4 (11) International Publication Number: WO 89/ 02312 B04C 5/12, 5/28 Al (43) International Publication Date: 23 March 1989 (23.03.89) (21) Iniernatinal Application Number: PCT/AU88/00359 (74) Agent: MACAULEY, Colin, Douglas; Callinans, 48 Bridge Road, Richmond, VIC 3121 (AU), (22) International Filing Date: 15 September 1988 (15.09.88) (81) Designated States: AT (European patent), AU, BB, BE (31) Priority Application Number: PX 4357 (European patent), BG, BJ (OAPI patent), BR, CF (GAPI patent), CG (OAPI patent), CH (European pa- (32) Priority Date: 15 September 1987 (15.09.87) tent), CM (OAPI patent), DE (European patent), DK, FI, FR (European patent), GA (OAPI patent), GB, (33) Priority Country: AU GB (European patent), HU, IT (European patent), JP, KP, KR, LK, LU (European patent), MG, ML (OAPI patent), MR (OAPI patent), MW, NL (Euro- (71) Applicant (for a! designated States except US), DELA- pean patent), NO, RO, SD, SE (European patent), WOOD PTY. LTD. [AU/AU]; 89 Orrng Crescent, SN (OAPI patent), SU, TD (OAPI patent), TG (OAPI Caulfield North, Vic 3161 patent), US, (72) Inventors; and Inventors/Applicants (for US only) PRENDERGAST, Published Gavan, James, Joseph [AU/AU]; 3 Seaton Court, With international search report.
Mount Waverley, VIC 3149 WEBB, David, An- Before the expiration of the time limit for amenditg the drew [AU/AU]; 108 Jenkins Street, Northcote, VIC claims and to be republished in the event of the receipt 3070 of amendments, 1 25 MAY 1989 (54) Title: HYDROCYCLONE OVERFLOW TRANSPORT (57) Abstract Fluid separator apparatus comprising at least one cyclone (16A) for separating a fraction of less dense compoent(s) from predominantly fluid mixtures having at least one predo inantly liquid component, said cyclone/s being provided with means defining at least one feed inlet means defining at least one overflow outlet (72) for discharge of overflow comprising predominantly less dense component(s) of fluid m’ tures, means defining at least one underflow outlet (66) for discharge of underflow comprising predominantly denser component(s) of said fluid mixtures, overflow conduit means (74) to receive and conduct 6A said overflow away from said cyclone, said overflow conduit means 16 AT 7.
(74) being connected securably to said overflow outlet means (72) of s ‘said cyclone (16A), support means (54) for supporting said cyclone/s in 7 s the form of a plate of pre.selected dimensions adapted to securably but 78 releasably receive the body/bodies of said cyclone/s (16A) and receiv- so ing and transport means (78) to receive and transport said overflow away from said overflow conduit means (74) said receiving and transport means (78) being connected securably but releasably to said overflow conduit ieans, Additionally, said support means may form part of or be located on or within a pressure retaining vessel enclosing at least part of said cyclone/s.
AUSTRAUAN
17 APR i989 PATENT OFFICE 77 -1- HYDROCYCLONE OVERFLOW TRANSPORT This invention relates to cyclone separators (hereinafter called «cyclones») for separating two or more fluids, to the transport of overflow after said overflow has been discharged from one or more cyclones, to means for effecting said transport, and to means for structural support for one or more cyclones. For the purposes of this specification, and unless a contrary intention should appear, «cyclone» includes a cyclone as described in the specification accompanying International Patent Application Number PCT/AU87/00398.
PRIOR ART It is known that a cyclone for separating two or more fluids may have inlet means for introducing the fluid mixture to be separated, outlet means for fluid having substantial concentration of less dense component (said fluid hereinafter called «overflow») and outlet means for fluid having substantial concentration of more dense component (said fluid hereinafter called «underflow»).
Many means have been devised for supporting and mounting a plurality of cyclones, at least partially inside a containing vessel. This is often important in the case of cyclones designed for the treatment of mixtures of fluid such as oil and water, since the source of the feed mixtures is often at high pressure, for example 10,000 kPa, and the design of single units may become complex. One such multi-cyclone apparatus is disclosed in Australian Patent Specification 33,119/84. This specification describes a liquid separator apparatus where one or more cyclones are enclosed in a pressure retaining shell. In another Sform of this application cyclones are connected in series within the same pressure 25 retaining shell, wherein in use the underflow from one cyclone is fed into the next cyclone in the series via the feed inlet of said next cyclone.
An alternative form of apparatus is descibed in PCT/AIJ86/00111. In his embodiment a plurality of cyclones are combined together inside a pressure retaining shell. One feature of this apparatus is that the cyclone overflow outlets S are combined into one stream and exit the vessel via one outlet. The overflow outlets are combined in a series of galleries and ports as part of the cyclone body, Other forms of apparatus are described in «The Hydrocyclone» by D.
Bradley (Pergamon Press, 1965). In particular, Fig 86 in that text shows a number of cyclones mounted in a tube sheet or support plate which is wafered between two flanges surrounded by a preasure retaining shell.
(7 -2- Other patent specifications which describe multiple cyclone apparatus include:- US 4,148,721, US 4,211,643, US 3,261,467 and AU-33,952/78. In addition the literature emanating from various cyclone manufacturers shows various forms of apparatus consisting of numbers of cyclones contained in vessels.
BACKGROUND TO THIS INVENTION As described in the prior art, to avoid the complexity of numerous interconnections when a plurality of cyclones are required, to treat a mixture, said cyclones are often grouped together inside pressure retaining vessels. However, a number of difficulties exist in applying the prior art to, for example, the crude oil and gas production and process industry. A typical feed mixture might include fluid mixtures of two or more components or phases of differing densities with at least one predominant liquid component. For example, the feed mixture might consist of oil and water with a small amount of gas and solids.
Problems often encountered include:- 1. Cyclones are often assembled with a plurality of cyclones combined together as a permanent fixture. This means that it is often difficult to inspect, maintain, replace and service individual cyclone units.
Furthermore, these cyclone assemblies are often very heavy; 2. Pressure retaining vessels are often manufactured and assembled using specially fabricated non-standard components. This increases the cost i and complexity of designs; 3. Prior art arrangements can result in difficulty in readily removing and accessing the cyclones. Equipment serviceability and maintenance .’25 downtime are very important factors in, for example, offshore oil and S’ as production platforms; S 4. |Trior art arrangements do not, in general, allow ready inspection and deaning of the small overflow outlet parts.
DESCRIPTION OF THIS INVENTION «30 It is an object of this invention to alleviate substantially the problems of the prior art in particular, though not exclusively, when applying cyclones to S* the treatment of fluid mixtures in the crude oil and gas production and processing industries. A typical feed mixture might consist of fluid mixtures containing at least a predominant liquid component which is more dense than the other components.
According to the present invention in one aspect there is provided an tik, apparatus for separating, into lighter overflow and heavier underflow fractions, a l^- 1 r -3fluid mixture of a higher density liquid component and a lower density component; the apparatus comprising a pressure-retaining vessel having an opening with a removable closure, a first high pressure cavity adjacent to the closure, a second low pressure cavity, inlet means for admitting the mixture into the first cavity and underflow outlet means for exit of the heavier fraction from the second cavity; and, within the vessel, a plurality of cyclones each having a body, which extends through a respective aperture in, and which is releasably secured by respective securing means to, a support plate, the securing means being accessible from the opening through the first cavity, whereby after removal of the closure, each cyclone body can, upon releasing the respective securing means, be individually released from, and withdrawn through, the support plate and out of the vessel opening for replacement; each cyclone having at least one feed inlet in communication with the first cavity, at least one underflow outlet in communication the second cavity, and at least one overflow outlet securely connected to overflow conduit means for exit of the lighter fraction, the overflow conduit means being securely but releasably connected to receiving and overflow transport means.
The support plate need not be of constant cross section. For use with particularly high pressure it may be advantageous to use a support plate of varying cross-section, Such a support plate primarily intended to support cyclones and perhaps divide a pressure retaining vessel into high pressure (or feed) and low pressure (or underflow) portions must be sufficiently thick to withstand this pressure differential. For reasons of economy it is advantageous to make the support plate as thin as possible. It is preferred that said support plate should ’25 contain a minimum number of holes. Necessary holes should be small. Holes which are parallel to the main faces of the support plate generally should be avoided. However, in certain situations it may be advantageous to incorporate said receiving and transport means within said support plate. Thus in one form of the invention there is provided an apparatus as aforesaid wherein said receiving and transport means comprise gallery means provided at least partly to the support plate.
l Said support means and said receiving and transport means may be at least partially securely but releasably combined as an assembly of plates. The said plate assembly preferably comprises a support plate as aforesaid and a separate removable plate (hereinafter described as «the cover plate»), that face of the cover plate coming into contact with the opposing face of the support plate being so -4adapted as to define, in conjunction with the opposing face of said support plate, means adapted to collect and combine the overflow from said cyclones. Such means (hereinafter described as «channel means») may take the form of grooves or channels incised, engraved, moulded, milled or otherwise provided in the face of the cover plate that comes into contact with the opposing face of the osupport plate. Alternatively, or additionally, grooves, channels or the like ramy be incised, moulded, engraved, milled or otherwise provided in said opposing face of the support plate. Conduit means may be connected to said receiving and transport means provided in said plate assembly to convey overflow away from said plate assembly.
Each cyclone body may be bolted to the support plate, the drawing up of the securing bolts automatically creating a seal between aligned parts of the cyclone overflow conduit means of that cyclone and the gallery means.
Where a plurality of cyclones emit said overflow to a plate assembly, a plurality of channel means may be interconnected within said plate assembly.
The cover plate may be removably attached to the support plate by bolts, nuts and bolts, screws or similar attachment means. This cover plate device may contain galleries and channel means. These channel means are preferably in the form of grooves milled into the face of the cover plate facing the support plate.
However, overflow may also be received and transported within the cover plate via a combination of inter-corntected galleries. It is preferred that galleries open to channel means on that face of the cover plate facing the support plate to .0 facilitate cleaning and inspection.
Where more than one cyclone body is attached to said plate assembly 25 within a pressure retaining vessel, all cyclone bodies may transmit said overflow to galleries and channels provided in said plate assembly and said galleries and channels may be interconnected so that at least a major proportion of said overflow may exit the pressure retaining vessel preferably at a single outlet. The exit of said :6 ;overflow may be via any part of the pressure retaining vessel in communication S»i 30 with outside parts, for example via the structural support plate and pressure vessel wall. Tubes, holes, malaifolds and galleries may be used to connect the combined S overflow in the plate assembly to that part or parts of the pressure retaining vessel providing said exit.
It is envisaged that the said support plate may be attached to or engaged with a pressure retaining vessel by: 1. Clamping said support plate between flanged faces of said pressure retaining vessel; 2. Welding said support plate to said pressure retaining vessel; 3. Bolting said support plate to said pressure retaining vessel; 4. Screwing said support plate to said pressure retaining vessel; A combination of any one or more of the above; or 6. Other conventional means.
According to another aspect of this invention, three or more cyclone bodies may be attached to said support means preferably in the form of a support plate with the longitudinal axes of cyclones being parallel or at least approximately parallel and also with the said cyclone bodies being arranged side by side or in a triangular matrix layout. A triangular matrix layout is preferred because it allows for more dense packing of cyclones, to maximise utilization of available space.
According to yet another aspect of this invention the cyclone body/bodies may be disengaged or removed from said support means as integral units, ie, without the need to disassemble the cyclone body/bodies whilst mounted in support means. This is believed to be advantageous in that it permits of relatively quick replacement of defective cyclone/s in the apparatus.
In addition to the possibility of having outlet means fo, overflow said support plate may be provided with:- 1. Outlet means and associated gallery means for taking samples of inlet fluid mixture; 9*: taking samples of overflow; or taking samples of underfow: 2. Gallery means and connection means to connect instrumentation e.g.
instrumentation for inlet fluid pressure measurements, overflow fluid 30 pressure measurements and undertow fluid pressure measurements; f *or 03. Other fluid flow transport means.
J Pressure limiting means may be used to limit the maximum pressure difference between inlet fluid mixture and underfow so as to limit the maximum pressure force exerted on said support plate. Said pressure limiting means may take the form of one or more pressure relief valves, burst plates, or similar devices.
-6- In another form of this invention said cyclones may be packaged from both ends into a pressure retaining vessel there being a plurality of support plates provided within said vessel.
In order that the present invention may be more clearly understood, reference is made to the accompanying non-limitative drawings, which illustrates the invention by reference to embodiments. In the drawings: Fig. 1 is a longitudinal section through two cyclone bodies and a plate assembly; Fig. 2 is a longitudinal section through a pressure retaining vessel containing a cyclone body and a combined support plate and receiving and transport means; Fig. 3 is a partial longitudinal section in the region of the inlet ends of two cyclone bodies and a plate assembly; Fig. 4 is a schematic plan view of an arrangement of cyclone bodies; Fig 5 is a longitudinal section through a pressure retaining vessel containing a number of cyclones and a plurality of plate assemblies.
In Fig. 1 cyclone bodies (16) and (18) are mounted in support means in the form of a plate assembly comprising support plate (12) and a removable cover plate Cyclone of cyclone body (16) has longitudinal axis (32) and cyclone of cyclone body (18) has longitudinal axis Axis (32) and axis (34) are at least 6*~approximately parallel, preferably parallel. Internal diameter (36) is substantially greater near cyclone inlet means (42) than the internal liameter (38) at a point adjacent to plate assembly The plate assembly (10) is situated at a preselected distance (40) along the cyclone body (16) from inlet means (42) in a direction taken parallel to longitudinal axis (32).
In use overflow leaves the cyclone of cyclone body (16) by overflow exit means then flows through a conduit means (22) provided in cyclone body The &e overflow then enters channel (24) provided within plate assembly Gallery (24) S unites with a similar channel (26) at location (28) within said plate assembly. The «30 combined overflow exits plate assembly (10) via channel and exit means (not shown).
Si46 In a typical case, internal diameter (36) is 70 mm, internal diameter (18) is 46 mm and distance (40) is 80 mm. Because diameter (38) is relatively small compared to diameter the diameter of the mounting hole (44) in plate assembly (10) in which cyclone body (16) is mounted is relatively small allowing the distance (46) between mounting hole (44) and equivalent mounting hole (48) .>rvi for cyclone body (18) to be substantil thereby substantially maintaining acceptable r -7structural strength. A relatively large distance (40) is believed to permit relatively close cyclone spacing (50) and/or relatively small plate thickness If available space for installing cyclones is small, e.g. on an oil production platfoi.:m, it may be advantageous to have cyclone spacing (50) small.
In Fig. 2, support means, in the form of a plate and a cyclone body (16A), are enclosed within a pressure vessel In this embodiment, with a single cyclone, it is not necessary for the support means and receiving and transport means to comprise a separate cover plate and a separate support plate and the cyclone body is mounted securably but releasably in a support plate provided with receiving and transport means. It is believed that this approach is not readily feasible with multiple cyclones. Inlet fluid mixture enters upper cavity (58) in said pressure vessel through pressure vessel inlet means said upper cavity (58) being defined by upper wall or walls and upper closure (62) of pressure vessel that part of cyclone body (16A) being above the plane of upper face of plate and upper face of plate Fluid in upper cavity (58) may enter the interior of cyclone body (16A) via cyclone inlet means Underflow leaves the cyclone body (16A) at underflow exit means (66) and enters lower cavity (68) defined by lower wall or walls and lower closure (69) of pressure vessel lower part of cyclone body (16A) and lower face of plate Underflow may exit lower cavity (68) via pressure vessel underflow exit means Overflow exits the cyclone at overflow exit means (72) and then flows through conduit (74) to gallery (76) provided within plate (54) and exits plate (54) at plate overflow exit means Plate (54) is clamped or otherwise secured, optionally releasably, betv.’een flanges (80) of said pressure retaining vessel Upper closure (62) may be removable to allow personnel to gain access to cyclone body (16A).
Bolts (82) may be used to hold cyclone body (16A) securely to plate In this example, cyclone body (16A) is not attached to any other support means.
However, other support means besides p!Wte (54) may be used. Said bolts (82) may be removed to allow said cyclone body (16A) to be withdrawn as a single unit from plate (54) in the direction shown by arrow (84).
As previously stated, cyclone body (16A) may be removed from support means formed by plate In this circumstance the mounting hole (86) in plate (54) into which cyclone body (16A) may be fitted, may be plugged to prevent any significant fluid flow through said hole (86) from upper cavity (58) to lower cavity Where a support means such as a plate is designed to accept more than one cyclone body, said plate may have at least one cyclone body missing and plug i 5 S S r i* f S. S S
S.
S
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r -8means inserted into the mounting hole/s not occupied by cyclone bodies to prevent significant fluid flows directly between upper cavity containing inlet fluid to be separated, lower cavity containing underflow and galleries containing overflow.
In Fig. 3 cyclone body (16B) and cyclone body (16C) are attached to a plate assembly (88) using bolts (90) (not all shown). Plate assembly consists of support plate (94) and cover plate Preferably the cyclones bodies are bolted to the cover plate. However it is also possible to bolt the cyclones directly to the support plate It is advantageous to securably but releasably fix cover plate (92) to support plate Sealing means, optionally in the form of an ring (104), are provided between said cyclone body (16C) and cover plate (92) to prevent significant fluid flow of underflow entering channel (102) via the outside of cyclone body (16C) from lower cavity (106). Sealing means (108) is provided to prevent significant fluid flow of inlet fluid mixture entering channel (102) between said cyclone body (16C) and plate assembly (88) from (high pressure area) upper cavity (110).
Overflow exits interior of cyclone body (16C) at overflow exit means (96) and flows into conduit (98) and (100) in cyclone body (16C), thence into a channel (102) defined by a groove provided in cover plate (92) and the opposing face of support plate Overflow may flow through channel (102) into a gallery (112) provided within plate assembly (88) via a channel (not shown). Analogously, overflow from interior of said cyclone body (16B) flows through similar conduit and gallery and channel means. Overflow from gallery (112) flows into gallery means (114) passing through support plate (94).
Said gallery means (114) are connected with tubing means (116) which i are connected with manifold means (118). One or more such tubing means may S»connect with said manifold means (118) to carry overflow from other cyclones not shown. Fluid in said manifold means (118) flows into gallery means (120) which connects with nozzle means (122) for exit from the apparatus. Said tubing means (116) and said manifold means (118) may form part of plate (94) or may be attached 30 to plate (94) in a conventional manner.
6 Tubing means (116) and said manifold means (118) are preferably constructed without sharp bends so as to allow cleaning means including flexible rod means wire) to be inserted into gallery means (120) and pushed through manifold means (118), tubing means (116), and gallery means (114) to allow clearing of blockages. Cyclone body (16C) may be fitted with cap or plug (124) which may be removed to allow a rod to be inserted into overflow exit means (96) to dislodge i blockage material.
K=rsI -9- Alternatively,fluid under high pressure may be introduced through nozzle means (122) to purge any total or partial blockages in support plate gallery means, tubing means, manifold means or other regions where overflow may flow.
Flow paths for overflow in said cyclone body (16C) including overflow exit means (96) may also be purged of any partial or total blockages by the same means.
During normal operation, inlet fluid mixture in upper cavity (110) generally will be at a higher pressure than underflow fluid in lower cavity (106) and overflow fluids in interior of cyclone body (16C) and plate assembly This is believed to cause a net force to act on cyclone body (16C) in a direction from upper cavity (110) towards lower cavity (106) forcing cyclone body (16C) against plate assembly This force may assist bolts (90) to hold cyclone body (16C) securely against plate assembly (88) and may assist the sealing action of sealing means (104) and (108).
Overflow flu,id will normally be at a pressure lower than that of the inlet fluid mixture and that of the underflow fluid and thus any fluid leaking past said sealing means (104) or (108) will normally flow into overflow gallery means, tubing means, manifold means and other overflow flow paths, thereby contaminating the overflow fluid.
In Fig. 4 seven cyclones with parallel longitudinal axes (126) are arranged in a triangular matrix layout. In this example, diameter (128) is the diameter of the cyclone body near the cyclone inlet and is the largest external diameter of the cyclone body. The cyclones are arranged with minimal gaps between the cyclone bodies as defined in external diameters (128).
The packaging of cyclones from both ends into pressure retaining vessels may exhibit advantages of reducing space, weight and cost of manufacture and maintenance.
In Fig. 5, cyclone bodies (16D) are attached to plate assemblies (130) and (132) which are secured within a pressure retaining vessel (134). Inlet fluid mixture to be separated enters pressure retaining vessel (134) via inlet means (136) and (138). Underflow exits said pressure retaining vessel (134) via pressure retaining vessel underflow exit means (140). Overflow exits plate assembly (130) at exit support means (142) and plate assembly (132) at exit support means (144).
In another form of this invention central cavity (146) of pressure retaining vessel (134) containing underflow may be used to separate gas from liquid. For example if the longitudinal axis of pressure retaining vessel (134) were vertical, gas in central cavity (146) may migrate toward plate assembly (130). Said r’ gas may exit pressure retaining vessel (134) from central cavity (146) by means (not .9 9r 9 5~
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10 shown) adjacent to plate assembly (1,30) or alternatively by gallery means (not shown) within plate assembly (130). In another aspect of the invention where upper cavity (148) contains a volume of fluid mixture to be separated mixed with chemicals the volume of cavity (148) may be sufficiently large to allow sufficient residence time so that the said fluid mixture and chemicals can react to a desired extent.
0 *o *0 oo0 0* 0 e g

Claims (1)

11- CLAIMS: 1. Apparatus for separating, into lighter overflow and heavier underflow fractions, a fluid mixture of a higher density liquid component and a lower density component; the apparatus comprising a pressure-retaining vessel having an opening with a removable closure, a first high pressure cavity adjacent to the closure, a second low pressure cavity, inlet means for admitting the mixture into the first cavity and underflow outlet means for exit of the heavier fraction from the second cavity; and, within the vessel, a plurality of cyclones each having a body, which extends through a respective aperture in, and which is releasably secured by respective securing means to, a support plate, the securing means being accessible from the opening through the first cavity, whereby after removal of the closure, each cyclone body can, upon releasing the respective securing means, be individually released from, and withdrawn through, the support plate and out of the vessel opening for replacement; each cyclone having at least one feed inlet in communication with the first cavity, at least one underflow outlet in communication with the second cavity, and at least one overflow outlet securely connected to overflow conduit means for exit of the lighter fraction, the overflow conduit means being securely but releasably connected to receiving and overflow transport means. 2. Apparatus according to claim 1, wherein the receiving and overflow transport means comprises gallery means provided at least partly to the support plate. 3. Apparatus according to claim 2, wherein the gallery means is at least «partly provided between opposing faces of the support plate and of a cover plate, one of the opposed faces being formed with channels. 4, Apparatus according to claim 2 or claim 3, wherein the securing means are bolts by means of which each cyclone body is bolted to the support plate, drawing up of the bolts automatically creating a seal between aligned Vif. o the cyclone overflow conduit means of that cyclone and the gallery means, 5. Apparatus according to any one of claims 2 to 4, wherein the overflow conduit means of a plurality of the cyclones communicate with a common gallery i*o. means., 6. Apparatus according to any one of the pr~eding claims, wherein the cyclones have their axes parallel to one another and defining a longitudinal direction of the vessel, the opening which is provided with the closure being an end opening of the vessel and the inlet means lending through a side wall of the Svessel, Vf 2 i ‘a -12- 7. Apparatus according to any one of the preceding claims, wherein the support plate divides the interior of the vessel into the first and second cavities. 8. Apparatus as claimed in any one of Claim 1 to 7, substantially as hereinbefore described with reference to the accompanying drawings. DATED this day of r7 1991 DELAWOOD PTY LTD By its Patent Attorneys CALLINAN LAWRIE 0c 0 I loo 0 *I S 0 I L I 0 SI 0

AU25213/88A
1987-09-15
1988-09-15
Hydrocyclone overflow transport

Ceased

AU615689B2
(en)

Applications Claiming Priority (2)

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AUPI4357

1987-09-15

AUPI435787

1987-09-15

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AU2521388A

AU2521388A
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1989-04-17

AU615689B2
true

AU615689B2
(en)

1991-10-10

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Priority Date
Filing Date

AU25213/88A
Ceased

AU615689B2
(en)

1987-09-15
1988-09-15
Hydrocyclone overflow transport

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US
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US5154826A
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EP
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EP0395647B1
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JP
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JPH03500143A
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AU
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AU615689B2
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CA
(1)

CA1329371C
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DE
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DE3885106D1
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MX
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MX171001B
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MY
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MY104329A
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NO
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NO175292C
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WO
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WO1989002312A1
(en)

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1990-01-17
1990-03-14
Statefocus Ltd
Separating apparatus

GB9101673D0
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1991-01-25
1991-03-06
Statefocus Ltd
Separating apparatus

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1991-08-01
1993-03-16
Conoco Specialty Products Inc.
Three chamber vessel for hydrocyclone separator

US5456837A
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1994-04-13
1995-10-10
Centre For Frontier Engineering Research Institute
Multiple cyclone apparatus for downhole cyclone oil/water separation

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1996-03-11
2000-06-27
Baker Hughes Limited
Downhole cyclonic separator assembly

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2000-06-09
2002-10-01
Wood Group Esp, Inc.
Water separation system with encapsulated electric submersible pumping device

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2000-06-14
2002-10-01
Wood Group Esp, Inc.
Clean water injection system

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2000-06-14
2003-04-15
Wood Group Esp, Inc.
Downhole rotary water separation system

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2000-07-11
2003-02-11
Vermeer Manufacturing Company
Continuous flow liquids/solids slurry cleaning, recycling and mixing system

US20030221558A1
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2002-03-26
2003-12-04
Lister Roy D.
Apparatus and method for separation of gases

US6800208B2
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2003-01-10
2004-10-05
United States Filter Corporation
Hydrocyclone bundle

GB2490346A
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2011-04-27
2012-10-31
Dps Bristol Holdings Ltd
Cyclonic separator having a tapered core element

JP2016093763A
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2014-11-12
2016-05-26
株式会社日進製作所
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1953-05-11
1956-10-09

Stamicarbon

Multiple hydrocyclone

GB1090978A
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1964-03-31
1967-11-15

Dorr Oliver Inc

Multiple hydrocyclone unit and system incorporating the same

GB2136327A
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1983-03-17
1984-09-19

Ohishi Engineering Limited Com

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1960-09-22
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1978-02-22
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DOUBLE-COATED HYDROCYCLONE SEPARATOR WITH LEAK INDICATORS

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1982-06-22
1988-05-18
LEVIN, Harry
Apparatus and process for making solar grade silicon

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Schoeffler William N
Controllable downhole directional drilling tool and method

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1987-02-05
Josef Kuehlmann

Egg transport device

1987

1987-09-15
US
US07/490,693
patent/US5154826A/en
not_active
Expired – Fee Related

1988

1988-09-14
CA
CA000577365A
patent/CA1329371C/en
not_active
Expired – Fee Related

1988-09-14
MY
MYPI88001029A
patent/MY104329A/en
unknown

1988-09-15
MX
MX013045A
patent/MX171001B/en
unknown

1988-09-15
JP
JP63507821A
patent/JPH03500143A/en
active
Pending

1988-09-15
EP
EP88908107A
patent/EP0395647B1/en
not_active
Expired – Lifetime

1988-09-15
AU
AU25213/88A
patent/AU615689B2/en
not_active
Ceased

1988-09-15
WO
PCT/AU1988/000359
patent/WO1989002312A1/en
active
IP Right Grant

1988-09-15
DE
DE88908107T
patent/DE3885106D1/en
not_active
Expired – Lifetime

1990

1990-03-14
NO
NO901205A
patent/NO175292C/en
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Assignee
Title

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(en)

1953-05-11
1956-10-09
Stamicarbon
Multiple hydrocyclone

GB1090978A
(en)

1964-03-31
1967-11-15
Dorr Oliver Inc
Multiple hydrocyclone unit and system incorporating the same

GB2136327A
(en)

1983-03-17
1984-09-19
Ohishi Engineering Limited Com
Multiple Hydrocyclone Apparatus

Also Published As

Publication number
Publication date

MX171001B
(en)

1993-09-24

NO901205L
(en)

1990-03-14

EP0395647A4
(en)

1991-03-13

EP0395647B1
(en)

1993-10-20

MY104329A
(en)

1994-03-31

WO1989002312A1
(en)

1989-03-23

AU2521388A
(en)

1989-04-17

JPH03500143A
(en)

1991-01-17

EP0395647A1
(en)

1990-11-07

US5154826A
(en)

1992-10-13

NO175292B
(en)

1994-06-20

DE3885106D1
(en)

1993-11-25

NO175292C
(en)

1994-09-28

CA1329371C
(en)

1994-05-10

NO901205D0
(en)

1990-03-14

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