Separator

Abstract: A separator for separating a relatively small volume e.g. up to 20% of a less dense liquid from a larger volume of a more dense liquid, for example for separating small volumes of crude oil from produced water from an oil-well, in the form of an elongated tube of reducing cross-sectional area. The separator has at least one tangentially­ -disposed inlet (5,105) for the mixture of liquids, adjacent the wide end of the separator, an outlet (10, 121) for the more dense compartment at the narrow end, and an axially disposed outlet (11,122) for the less dense component. A further outlet (6, 113) for the more dense component may be provided intermediate the two ends. The two outlets (10, 121 or 6, 113) for the more dense component are provided with pressure control means (85, 93) for controlling the pressure of the more dense component.

Description: This invention relates to a separator. In particular it relates to a separator for separating a relatively small volume e.g. up to 20% of a less dense liquid from a larger volume of a more dense liquid, for example separating small volumes of crude oil from production water from an oil well so that the separated water may be discharged in a virtually clean condition to the sea. W0-A-8303063 and EP-A-068809 each disclose a separator for this use in tubular form of reducing circular cross-section from a wide end to a narrow end, having at least one tangentially-disposed inlet at or adjacent the wide end for introducing at relatively high velocity the mixture of liquids to be separated into the separator, and two outlets, the first disposed on the axis of the separator at the wide end for the removal of the less dense liquid component and the second disposed at or adjacent the narrow end for the removal of the more dense liquid component. During use of such a separator the less dense component, for example oil, moves towards the axis and forms a core and this moves towards the wide end, while the more dense component, e.g. sea-water, moves towards the wall of the separator and towards the narrow end. However it has been found that in some situations not all the less dense component in the central core moves towards the wide end; some of it remains stationary and some even moves towards the narrow end where it mixes with and contaminates the more dense component. EP-A-058484 discloses an air-cored tubular separator mainly used for separating particles in a fluid. However air-cored separators are not suitable for separating two liquids such as oil and water since an unwanted emulsion is likely to be formed. US-A-4378289 discloses a tubular separator commonly used in the paper-making industry for separating unwanted contaminating particles such as sand grains which are more dense than wood fibres and water. This type of separator is not suitable for separating an unwanted less dense contaminating liquid component, e.g. oil, from the more dense liquid component, e.g. water, since the required component,i.e. wood fibre and water, moves towards the axis rather than towards the separator periphery as is the case when separating contaminating oil from water. It is an object of the present invention to provide a separator in which the above disadvantageous effects are substantially reduced or overcome. According to the present invention there is provided a separator for separating a mixture of liquids into a more dense component and a less dense component comprises an elongated tube having a circular cross-section which reduces in diameter from a wide end to a narrow end and a constant taper from a location adjacent the inlet towards the narrow end, the convergence angle of the tube being about 2°, at least one tangentially disposed inlet at or adjacent the wide end for the introduction at relatively high velocity of a mixture of liquids to be separated, an outlet for the removal of the less dense component on the axis of the separator, an outlet for the removal of the more dense component positioned in the vicinity of the narrow end of the separator, and pressure control means for controlling the pressure of the more dense component in the vicinity of the outlet for the more dense component characterised by comprising at least one other, intermediate, outlet for the more dense component at a predetermined position on the wall of the separator between the two ends, and further pressure control means for controlling the pressure of the more dense component in the vicinity of the intermediate outlet for the more dense component. The outlet for the more dense component may extend for at least substantially the whole of the circumference of the tube, or may comprise at least one tangentially disposed port of any suitable cross-sectional shape, e.g. circular, elliptical, rectangular or square in the opposite sense to the said at least one inlet. The size of the outlet may be adjustable. For example it may be in the form of a gap between the tube and an outlet unit, which may be moveable along the axis of the separator, to vary the size of the gap. The adjacent surfaces of the end of the tube and of the outlet unit defining the gap may be tapered, the cross-sectional area of a surface on either tube or outlet unit increasing from the wide end towards the narrow end of the separator. The further, intermediate, outlet for the more dense component may extend for substantially the whole of the circumference of the tube, or may comprise at least one tangentially disposed port of any suitable cross-sectional shape, e.g. circular,elliptical, rectangular or square, in the opposite sense to the said at least one inlet. The size of the intermediate outlet may be adjustable, and the outlet may, in some situations, be closed. However, no change of diameter should occur. For example in the case where it extends around the whole circumference of the tube it may comprise a gap between adjacent lengths of the tube, and the gap may be adjusted by moving one length relative to an adjacent length along the tube axis. The surfaces of the two adjacent lengths defining the gap may be tapered, the cross-sectional area of a wide surface on either length increasing in a direction from the wide end towards the narrow end of the separator. Preferably there are two diametrically opposed tangential inlets for the mixture of liquids to be separated, of any suitable cross-sectional shape, e.g. circular, oval, rectangular or square. However more than two inlets may be provided. The or each inlet may connect with a cylindrical end section of the tube. The size of either outlet for the more dense component, i.e. at the narrow end and/or between the two ends, or the inlet(s) may be controlled either manually or automatically under the influence of one or more sensors for detecting changes in various parameters such as liquid flow rate, liquid composition i.e. relative proportions of each component, or pressure at various positions. The invention will now be described in more detail with reference to the accompanying drawings of which:- Figure 1 shows a simplified longitudinal cross-section through a separator according to the invention; Figure 2 shows how the angle α is defined; Figures 3-5 show in simplified form, three alternative constructions of part of the separator shown in Figure 1; Figures 6 and 7 show, in simplified form, two alternative forms of the second body section of the separator shown in Figure 1; Figure 8 shows how the angle β is defined; Figure 9 shows, in simplified form, the construction of the separator shown in Figure 1 at the narrow end thereof; and Figure 10 shows a longitudinal cross-section through a cyclone separator in accordance with a specific embodiment of the invention. A cyclone separator in accordance with the present invention is shown in Figure 1 and comprises an elongated tube having a cylindrical inlet section 1, a first body section 2 and a second body section 3. The separator also comprises an outlet unit (see Figure 9). For convenience the separator is shown with thin walls but in practice they may be much thicker to withstand internal pressures of the liquids being separated. The inlet section 1, in the form of a short cylindrical tube, has a cross-sectional area A M , and corresponding diameter D M in the range from about 20mm to about 120mm, typically about 70mm, and a length L₁ up to about 500mm. Preferably L₁ = D M . Two diametrically opposed, tangentially disposed inlet ports 5a and 5b are provided, leading to the inlet section 1 from inlet pipes (not shown) through which a mixture of water and up to 20% crude oil may be fed at high velocity to the separator interior. The inlet section is provided with a disc-shaped end cover 7, which in this example is not provided with an axially disposed outlet for the less dense component. The inlet ports may be of any suitable cross-section, although in Figure 1 the ports have a circular cross-section of diameter D₁. The total cross-sectional area of the inlet ports A₁ may lie in the range given by the equation: 0.03A M ≦ A₁ ≦ 0.12A M Preferably 0.045A M ≦ A₁ ≦ 0.09A M The inlet section 1 is connected to the first body section 2 which as shown in Figure 1 is of constant taper to provide the interior surface 8 with a constant convergence angle α between the point A where the inlet section joins the first body section and the point B where an intermediate outlet 6 for the more dense component is provided. The convergence angle α preferably lies in the range from about 30′ to about 10° e.g. about 2°, although smaller convergence angles are possible, down to about 1′-5′, if the separator inlet diameter D M is small. A preferred value of α is 1.8°. At point B as shown in Figure 1 the diameter D₂ of the separator has reduced to a value given by the equation: with a preferred value being Other shapes of the first body section 2 are possible. For example the convergence angle may vary, either abruptly, so that the first body section 2 comprises a plurality of frusto-conical portions, the convergence angle decreasing from one portion to the next in a direction away from the inlet section 1, or gradually so that the interior surface 8 of the body section 2 is curved, the degree of curvature decreasing in a direction away from the inlet section 1, as illustrated in Figure 4. In all the different shapes overall convergence angle α from point A to point B as illustrated in Figure 2, lies within the range given above, and has the same preferred values. As shown in Figure 1 the separator is provided with an intermediate outlet 6 for the more dense component in the form of a circumferential gap between the first body section 1 and the second body section 3. Pressue conrol means for controlling the pressure of the more dense component in the vicinity of the intermediate outlet is provided but not shown in Figure 1. Such means may comprise a pressure control valve. The size of the gap may be varied by moving the sections towards or away from one another so as to alter the longitudinal dimension L₂ shown in Figure 1. Preferably the value of L₂ is defined by the equation: or, preferably In this preferred range L₂ lies between 4.0mm and 8.0mm for a D M of about 70mm. As shown in Figure 1 the second body section is cylindrical in shape and has an internal diameter D₃. The value of D₃ lies within the range given by the equation:- with a preferred value being: D₃ = 0.8 D₂ It is to be noted that if D₃ < D₂ then L₂ can be negative with the limit given by the equation:- L₂ = - D M In other words the end of the second body section 3 adjacent the gap 6 may protrude inside the interior of the first body section 2. As shown in Figures 3, 4 and 5 alternatively the intermediate outlet 6 may comprise one or more outlet ports of any suitable cross-sectional shape. Two diametrically-opposed, tangentially disposed rectangular ports 6a and 6b are shown in Figure 3, two diametrically disposed, tangentially disposed circular ports 6c and 6d are shown in Figure 4 and one tangentially disposed circular port 6e is shown in Figure 5. The second body section 3 in all constructions shown in Figures 3, 4 and 5 is a continuation of the first body section 2. The total outlet area A₃ of the outlet port 6e or both outlet ports 6a and 6b or 6c and 6d may lie in the range given by the equation:- 0.2 A₂ ≦ A₃ ≦ A₂ Preferably two outlets are used with the preferred value being:- 0.4 A₂ ≦ A₃ ≦ 0.8 A₂ A₂ is the cross-sectional area of the tube at the point B in Figure 1. and corresponds to the diameter D₂. This is the diameter immediately adjacent the intermediate outlet on the side closer to the wide end of the separator. The arrangement of the outlet ports 6a, 6b etc is in the opposite sense to the inlet ports 5a and 5b. The second body section 3, as shown in the construction in Figure 1 may be cylindrical. However, alternatively it may be formed with a frusto-conical mouth portion, as shown between points C and E in Figure 6, the remainder being cylindrical, as shown between points E and D. Alternatively it may be curved as shown in Figure 4, or of wholly frusto-conical form, as shown in Figure 7. In all instances the overall angle of convergence β between points C and D (see Figure 8) lies in the range 0° to about 5°. The overall length L₃ of the second body section 3 lies in the range given by the equation:- D M ≦ L₃ ≦ 14 D M But the values of β and L₃ must be such that: D₄ ≧ 0.07 D M and:- D₃ ≧ D₄ Preferably the second body section 3 has a cylindrical shape so that β = 0 and D₄ = D₃, and also the value of L₃ is such that it lies in the range given by the equation;- 5D M ≦ L₃ ≦ 9D M with the preferred value of L₃ = 7D M As shown in Figure 9 the outlet 10 for the more dense component at the narrow end of the separator leads into a closed chamber 12. The component is fed from the chamber 12 through a restriction or other pressure control means such as a valve 13. The pressure of the outflowing component is thereby controlled. If several separators are used in parallel, the discharges of the more dense component may be into one chamber. The outlet 10 shown in Figure 9 extends around the whole circumference of the end of the second body section 3. Preferably the outlet is characterised by the axial width L₅ of the outlet, the taper angle γ of the conical deflector 15 disposed in the chamber and the diameter D₆ of the base of the deflector. The values of these dimensions lie in the following preferred ranges:- 5° ≦ γ ≦ 90° D₅ < D₆ < 4D₄ However the maximum value of D₆ may be larger than 4D₄. The upper limit depends on the size and shape of the chamber 12 or other practical limitations. Alternatively the outlet 10 may be in the form of one or more tangentially disposed outlet ports of any suitable shape e.g. circular, rectangular or square, similar to the intermediate outlet ports 6a, 6b, 6c etc, and in the opposite sense the inlet ports 5a, 5b. The less dense component of the mixture forms as a central core within the liquid and is removed from the separator via an axially disposed outlet 11 in the form of a narrow tube 19, the end of which is preferably tapered so as to form a sharp edge 17. The tube extends towards the interior of the separator beyond the extremity 18 of the second body section 3. The tube 19 may have an enlarged diameter outwardly from the separator beyond the extremity 18 of the second body section 3. The internal diameter D₅ of the tube is selected depending on the proportions of the liquid components being separated but may be varied within the range given by the following equation:- 0.9 D₄ ≧ D₅ ≧ 0.01 D M a preferred range (for low concentrations of the less dense component) being:- 0.029 D M ≦ D₅ ≦ 0.043 D M The length L₄ the tube 19 extends within the separator may be varied within the range:- 0 ≦ L₄ ≦ L₃ a preferred value being:- One specific embodiment of the invention is shown in Figure 10 and comprises a cyclone separator in the form of an elongated tube having a cylindrical inlet section 101, a first body section 102 and a second body section 103. The separator also comprises an outlet unit 104. The inlet section 101 in the form of a short cylindrical tube having a diameter D M of 70mm and a length L₁ = 50mm is provided with two tangentially disposed inlet ports 105a and 105b of circular cross-section diametrically opposed to one another leading from inlet pipes 106a and 106b through which a mixture of water and up to 2.0% crude oil may be fed at high velocity to the separator. The inlet section is provided with an end cover 107. The inlet section 101 is connected to a tubular first body section 102 by any suitable means. The first body section 102 has a tapered interior having a frusto-conical surface 83, the convergence angle α of the surface 83 having a value of 1.8°. The length L of the first body section is 835mm. The minimum diameter D₂ of the first body section is 17.5mm. At the end of the first body section 102 remote from the inlet section 101 is positioned a tubular second body section 103 having a cylindrical interior, i.e. the diameter of the interior surface 112 is constant. The diameter D₃ (=14mm) of surface 112 of the second body section 103 is slightly less than the diameter D₂ (= 17.5mm) of frustoconical surface 83 closest to the second body section 103, a small circumferential gap 113 being provided between the first body section 102 and the second body section 103. This gap 113 provides an outlet for the more dense component which discharges into a cylindrical chamber 84 surrounding the gap 113 and thence out through a pressure controlling valve 85. The position of the second body section 103 relative to the first body section 102 is adjustable by means (not shown in Figure 1) to vary the size of the gap 113. Typically the axial length L₂ of the gap is between 1mm and 10mm. Two 0 ring seals 86, 87 are provided in grooves 88, 89 in the outer cylindrical surface of the first body section 102 allowing the first body section to slide in or out of the chamber 84 as required. As can be seen in Figure 10 the gap 113 is formed between a frusto-conical surface 114 on the end of the first body section 102 remote from the inlet section 101 and a conical surface 115 on the adjacent end of the second body section 103. The surfaces 114 and 115 are such that they diverge on a direction away from the inlet section 101 at a divergence angle W typically 30° The overall length L₃ of the second body section is 500mm. Adjacent the end 116 of the second body section 103 (i.e. at the narrow end of the separator) remote from the inlet section 101 there is positioned an outlet unit 104. This is in the form of a thick-walled tube within the bore of which is an inner tube 117 having an internal diameter in the range 2mm-3mm. This inner tube 117 is a sliding fit within the outlet unit 104, has a constant internal diameter in the range 4mm-7mm, and its axis coincident with the axis of the remaining parts of the separator. An elongation 118 of the inner tube 117 extends a short distance L₄ into the separator from the narrow end 116 thereof towards the inlet section 101, so that the inner tube mouth 122 is spaced apart from the narrow end 116. The mouth 122 of the tube is externally tapered to form a sharp edge at its extremity within the separator. The surface 119 of the second body section 103 facing the outlet unit 104 is frusto-conical and the surface 120 of the outlet unit 104 facing the second body section 103 is conical. A small circumferential gap 121 is provided between the surfaces 119 and 120 to form a second outlet for the more dense component which discharges into a cylindrical chamber 92 surrounding the gap 121 and thence out through a pressure controlling valve 93. The surfaces 119 and 120 diverge in a direction away from the inlet section 1 at a divergance angle ω typically 30°. The position of the outlet unit relative to the second body section 103 may be adjusted by means (not shown in Figure 1) to vary the size of the gap 121. Typically the axial length L₅ of the gap is 0-10mm e.g. 5mm. Two 0 ring seals 94, 95 are provided in grooves 96, 97 in the outer cylindrical surface of the outlet unit 104, allowing it to slide into or out of the chamber 92 as required. Additionally suitable means may be provided for sliding the inner tube 117 within the outlet unit 104, thus varying the axial length L₄ (typically 80mm) of the elongation 118 and hence moving the mouth 122 thereof to be positioned at any required distance from the narrow end 116 of the separator. The mouth 122 of the inner tube 117 in the outlet unit 4 provides an outlet for the removal of the less dense component i.e. oil, from the separator. This inner tube 117 may be connected to a suitable valve and/or pump as required. In use of the separator of this embodiment (as shown in Figure 10) the mixture of liquids to be separated, water and crude oil, is fed at high speed into the separator through the inlet ports 105a and 105b. By adjusting the positions of the second body section 103 and the outlet unit 104 the sizes of the gaps 113 and 121 may be varied. Fluid flow and pressure are also varied. Since the less dense component i.e. the oil, moves towards the axis of the separator this may be removed through the mouth 122 of the inner tube 117. Additionally since the more dense component i.e. water, moves towards the wall of the separator i.e. the interior surfaces 83 and 112, some is removed through the gap 113 between the first and second body sections 102 and 103 (if open), while the remainder is removed through the gap 121 between the second body section 103 and the outlet unit 104. By suitable adjustment of the pressure of water by means of valves 85 and 93, of the flow rate of oil through the outlet 122, and of the relative positions of the second body section 103, the outlet unit 104 and the mouth 122, virtually clean water may be obtained from the outlets 113 or 121. When the separator illustrated in Figure 10 was operated to separate a mixture of about 400 parts per million of light oil (less dense component) in water (more dense component), the oil having a mean droplet diameter of 37 microns, the following results were achieved :- At intermediate outlet :- 94% of inlet oil removed At outlet at narrow end :- 96% of inlet oil removed The operating conditions were :- Inlet Mixture Pressure 50 psig (= 3.45 barg) More dense component Intermediate outlet pressure 38 psig (=2.62 barg) Intermediate outlet flow 45 l/min Narrow end outlet pressure 28 psig (=1.93 barg) Narrow end outlet flow 50 l/min Less dense component Axial outlet pressure About 1 psig (=0.069 barg) Axial outlet flow About 2 to 3 l/min Both components Total throughput About 97-98 l/min It was also found that when a separator similar to that illustrated in Figure 10 but with a slightly longer first body section 102 tapering to a minimum diameter D₂ of 14 mm i.e. equal to the internal diameter D₃ of the second body section 103, was operated under similar inlet pressure conditions but with the gap 113 between the first and second body sections closed the following results were obtained :- More dense component At outlet at narrow end 94.5% of oil removed Both components Total throughput About 70 l/min

Claims: A separator for separating a mixture of liquids into a more dense component and a less dense component comprising an elongated tube (2,3;102,103) having a circular cross-section which reduces in diameter from a wide end to a narrow end and a constant taper from a location adjacent the inlet towards the narrow end, the convergence angle of the tube being about 2°, at least one tangentially disposed inlet (5;105) at or adjacent the wide end for the introduction at relatively high velocity of a mixture of liquids to be separated, an outlet (11;122) for the removal of the less dense component on the axis of the separator, an outlet (10;121) for the removal of the more dense component positioned in the vicinity of the narrow end of the separator, and pressure control means (13;93) for controlling the pressure of the more dense component in the vicinity of the outlet (10;121) for the more dense component characterised by comprising at least one other, intermediate, outlet (6;113) for the more dense component at a predetermined position on the wall of the separator between the two ends, and further pressure control means (85) for controlling the pressure of the more dense component in the vicinity of the intermediate outlet (6;113) for the more dense component. A separator according to Claim 1 characterised in that the convergence angle is 1.8°. A separator according to either of the preceding claims characterised in that the size of the outlet (10;121) for the removal of the more dense component is adjustable. A separator according to any one of the preceding claims characterised in that the outlet (10;121) for the more dense component extends for at least substantially the whole circumference of the tube (3,103). A separator according to Claim 4 characterised in that the outlet (10;121) is in the form of a gap between the tube (3,103) and an outlet unit (19,104). A separator according to Claim 5 characterised in that the outlet unit (104) is movable along the axis of the separator to vary the size of the gap. A separator according to any one of Claims 3, 4, 5 or 6 characterised in that the width of the outlet, (10;121) measured in an axial direction, lies in the range from to D m being the internal diameter of the separator immediately adjacent the inlet (11;122). A separator according to either Claim 5 or 6 characterised in that the surface (120) of the outlet unit (104) defining the gap (121) is tapered, the cross-sectional area of the surface (120) increasing from the wide end towards the narrow end of the separator. A separator according to Claim 8 characterised in that the taper angle γ lies in the range 5° to 90°. A separator according to Claim 9 characterised in that the taper angle γ is about 30°. A separator according to any one of Claims 8 to 10 characterised in that the surface (119) at the end of the tube (102,103) defining the gap is tapered, and parallel to the surface (120) of the outlet unit (104). A separator according to any one of Claims 1-3 characterised in that the outlet (10) for the more dense component comprises at least one tangentially-disposed port in the opposite sense to the inlet (5). A separator according to any one of the preceding claims characterised in that the outlet (11;122) for the removal of the less dense component comprises an axially disposed tube (19;117) which extends into the separator from the narrow end thereof. A separator according to Claim 13 characterised in that the tube (19) for the removal of the less dense component is tapered so as to have a sharp edge (17) within the separator. A separator according to any either Claim 13 or Claim 14 characterised in that the tube (19;117) for the removal of the less dense component has an enlarged internal diameter outwardly of the separator. A separator according to any one of claims 13, 14 or 15 characterised in that the internal diameter of the tube (19;117) for the removal of the less dense component lies in the range 0.9 D₄ ≧ D₅ ≧ 0.01 D M where D₄ is the internal diameter of the separator at the narrow end, D₅ is the internal diameter of the tube for the removal of the less dense component, and D M is the internal diameter of the separator immediately adjacent the inlet. A separator according to Claim 16 characterised in that the internal diameter of the tube (19;117) for the removal of the less dense component which extends into the separator lies in the range 0.029 D M ≦ D₅ ≦ 0.043 D M for low concentration of the less dense component. A separator according to any one of claims 13 to 17 characterised in that the length of the tube (19;117) for the removal of the less dense component which extends into the separator lies in the range where D M is the internal diameter of the separator immediately adjacent the inlet, and L₄ is the length of the tube for the removal of the less dense component which extends into the separator from the narrow end thereof. A separator according to any one of the preceding claims characterised in that the size of the intermediate outlet (6;113) for the removal of the more dense component is adjustable. A separator according to any one of the preceding claims characterised in that the intermediate outlet (6;113) for the more dense component extends for at least substantially the whole circumference of the tube. A separator according to Claim 19 or 20 characterised in that the intermediate outlet is in the form of a gap between adjacent lengths (2,3 or 102,103) of the tube. A separator according to Claim 21 characterised in that at least one of the lengths (2,3 or 102,103) of the tube is movable relative to the adjacent length to vary the size of the gap (6;113). A separator according to any one of the preceding claims characterised in that the width of the intermediate outlet (6;113) measured in an axial direction lies in the range where L₂ is the width of the outlet, and D M is the internal diameter of the separator immediately adjacent the inlet. A separator according to Claim 23 characterised in that the width of the intermediate outlet (6;113) lies in the range A separator according to either Claim 21 or 22 characterised in that the intermediate outlet (6;113) may be closed by bringing the two adjacent lengths (2,3 or 102,103) into contact, the internal diameter of each tube length immediately adjacent the outlet being equal. A separator according to either Claim 21 or 22 characterised in that the surfaces (114;115) of the adjacent lengths defining the gap are parallel and tapered, the cross-sectional area of each surface increasing from the wide end towards the narrow end of the separator. A separator according to Claim 26 characterised in that the taper angle ω lies in the range 5° to 90°. A separator according to Claim 26 characterised in that the taper angle ω is about 30°. A separator according to any one of claims 1 to 19 characterised in that the intermediate outlet (6) for the more dense component comprises at least one tangentially-disposed port in the opposite sense of the said at least one inlet. A separator according to any one of the preceding claims characterised in that the angle of convergence, α, independent of the shape of the tube, between the position A where the internal diameter starts to reduce and the position B immediately adjacent the intermediate outlet (6) for the more dense component closer to the wide end is about 2°. A separator according to any one of the preceding claims characterised in that the angle of convergence, α, independent of the shape of the tube, between the position A where the internal diameter starts to reduce and the position B immediately adjacent the intermediate outlet (6) for the more dense component closer to the wide end is 1.8°. A separator according to Claim 1 characterised in that the tube comprises two lengths (2,3 or 102,103), the first length (2 or 102) being tapered and positioned nearer the wide end and the second length (3 or 103) being positioned nearer the narrow end, a closeable intermediate outlet (6;113) for the removal of the more dense component being positioned between the two lengths. A separator according to Claim 32 comprising a cylindrical inlet section (1;101) immediately adjacent the inlet (5;105). A separator according to Claim 32 characterised in that the convergence angle α of the first length is about 2°. A separator according to Claim 32 characterised in that the convergence angle α of the first length is 1.8°. A separator according to any one of Claims 33 - 35 characterised in that the total cross-sectional area of the at least one inlet (5,105) lies in the range 0.03 A M ≦ A₁ ≦ 0.12 A M where A₁ is the total cross-sectional area of the at least one inlet and A M is the cross-sectional area of the separator immediately adjacent the at least one inlet. A separator according to any one of Claims 33 - 35 characterised in that the total cross-sectional area of the at least one inlet (5;105) lies in the range 0.045 A M ≦ A₁ ≦ 0.09 A M where A₁ is the total cross-sectional area of the at least one inlet and A M is the cross-sectional area of the separator immediately adjacent the at least one inlet. A separator according to any one of Claims 32- 37 characterised in that the minimum diameter of the first length (2;102) lies in the range one half to one eighth of the maximum diameter (D M ). A separator according to Claim 38 characterised in that the minimum diameter of the first length (2;102) is about one quarter of the maximum diameter. A separator according to any one of Claims 32- 39 characterised in that the internal diameter of the second length (3;103) adjacent the intermediate outlet (6;113) is substantially equal to the minimum diameter of the first length (2;102). A separator according to any one of Claims 32- 39 characterised in that the internal diameter of the second length (3;103) is constant and lies within the range where D₂ is the minimum internal diameter of the first length and, D₃ is the internal diameter of the second length. A separator according to Claim 41 characterised in that D₃ = 0.8 D₂ A separator according to any one of Claims 32- 40 characterised in that the second length (3;103) is internally tapered over at least part of its length, the maximum diameter being immediately adjacent the intermediate outlet (6;113) and the angle of taper having a value up to about 5°. A separator according to any one of Claims 32- 43 characterised in that the overall length of the second length (3;103) lies in the range D M ≦ L₃ ≦ 14 D M where D M is the maximum internal diameter of the separator and L₃ is the overall length of said second length, but the following conditions apply :- D₄ ≧ 0.07 D M and D₃ ≧ D₄ where D₃ is the internal diameter of the second length adjacent intermediate outlet and, D₄ is the internal diameter of the second length adjacent the outlet at the narrow end. A separator according to any one of Claims 32 - 43 characterised in that the overall length of the second length (3;103) lies in the range 5 D M ≦ L₃ ≦ 9 D M where L₃ is said overall length of the second length and, D M is the maximum internal diameter of the first length. A separator according to any one of Claims 32- 44 characterised in that the overall length of the said second length (3;103) equals seven times the maximum internal diameter of the first length (2;102). A separator according to any one of Claims 32- 46 characterised in that the outlet (10;113) for the more dense component at the narrow end of the separator extends around the whole circumference of the separator, the axial width of the outlet lying in the range where L₅ is the axial width and, D M is the maximum diameter of the first length. A separator according to Claim 47 characterised in that the outlet (10;113) for the more dense component at the narrow end of the separator comprises a conical deflector having a taper angle in the range from 5° to 90°. A separator according to any one of Claims 32- 48 characterised in that the outlet (10;113) for the less dense component comprises an axially disposed tube (19;117) at the narrow end of the separator which extends into the second length (3;103) for a variable distance up to the overall length of the second length. A separator according to Claim 49 characterised in that the distance the axially disposed tube (19;117) extends into the second length lies in the range where D M is the maximum internal diameter of the first length, L₄ is the said distance. A separator according to any one of the preceding claims characterised in that there is no outlet for the less dense component at the wide end of the separator (2,3;102,103). A method of separating a mixture of liquids (eg oil and water), into a more dense component (eg water) and a less dense component (eg oil) comprising feeding the mixture of liquids to be separated tangentially at relatively high velocity into a separator comprising an elongated tube having a circular cross-section which reduces in diameter from a wide end to a narrow end and a constant taper from a location adjacent the inlet towards the narrow end, the convergence angle of the tube being about 2°, the mixture being fed through an inlet located at or adjacent the wide end of the tube, removing less dense component through an outlet on the axis of the separator, and removing more dense component through an outlet positioned in the vicinity of the narrow end of the separator, the pressure of more dense component in the vicinity of the outlet for more dense component being controlled by pressure control means characterised by removing more dense component through a further, intermediate, outlet positioned at a predetermined position on the wall of the separator between the two ends and controlling the pressure of more dense component in the vicinity of the further, intermediate, outlet for more dense component by further pressure control means. A method according to Claim 52 characterised by removing the less dense component through an outlet at the narrow end of the tube. A method according to Claim 52 or 53 characterised by removing the more dense component through outlets which extend circumferentially around the tube.

Inventors: LLOYD DAVID DOUGLAD, MICHALUK PETER GREGORY, LLOYD, DAVID DOUGLAD, MICHALUK, PETER GREGORY
Applicants: SERCK BAKER LTD, SERCK BAKER LIMITED
Application year: 1988
Main classification: B04C11
IPC codes: B04C5, B04C3, B04C11, B01D17