EP0158641A1

EP0158641A1 - Improved outlet for cyclone separators

Info

Publication number: EP0158641A1
Application number: EP84903160A
Authority: EP
Inventors: Noel Carroll
Original assignee: Individual
Current assignee: Individual
Priority date: 1983-09-01
Filing date: 1984-08-29
Publication date: 1985-10-23
Also published as: OA08005A; GB2158372A; GB2158372B; WO1985000990A1; BR8407045A; DK195785A; NL8420224A; JPS61500009A; GB8510248D0; DK195785D0

Abstract

Séparateur cyclone (10) possèdant une chambre de séparation s'étendant axialement (25) avec des sections successivement voisines (12, 14, 16) de diamètre décroissant progressivement et des tuyaux d'alimentation (26, 28) pour l'entrée tangentielle du mélange liquide à séparer à l'extrémité de la chambre de séparation dont le diamètre est le plus grand. La chambre de séparation (25) comporte un tuyau de sortie de trop plein (34) à son extrémité dont le diamètre est le plus grand et une sortie de fond (23) à son extrémité dont le diamètre est le plus petit. La sortie de trop plein a un diamètre do, près de la chambre de séparation, de l'ordre de 0,0035 <= do/d1 < 1 où d1 est le diamètre de la section de la chambre de séparation possèdant le plus grand diamètre. Le liquide à séparere est mélangé, dans un mode de réalisation de la présente invention avec un interrupteur d'émulsion afin de faciliter la séparation des composants liquides du mélange à séparer.Cyclone separator (10) having an axially extending separation chamber (25) with successively adjacent sections (12, 14, 16) of progressively decreasing diameter and supply pipes (26, 28) for the tangential entry of the liquid mixture to be separated at the end of the separation chamber with the largest diameter. The separation chamber (25) has an overflow outlet pipe (34) at its end with the largest diameter and a bottom outlet (23) at its end with the smallest diameter. The overflow outlet has a diameter do, near the separation chamber, of the order of 0.0035 <= do / d1 <1 where d1 is the diameter of the section of the separation chamber having the largest diameter . The liquid to be separated is mixed, in one embodiment of the present invention with an emulsion switch in order to facilitate the separation of the liquid components from the mixture to be separated.

Description

"IMPROVED OUTLET FOR CYCLONE SEPARATORS"

This invention relates to a cyclone separator.

United States Patent 4,237,006 (Coleman et al) describes a cyclone separator having a separating chamber having first, second and third contiguous cylindrical portions arranged in that order, the first cylindrical portion being of greater diameter than the second cylindrical portion and the third cylindrical portion being of lesser diameter than the second cylindrical portion, the first cylindrical portion having an overflow outlet at the end thereof opposite to said second cylindrical portion and a tangentially directed feed inlet, the separator being adapted to separate liquids one from the other in a mixture when infed into said separating chamber via said feed inlet, one said liquid emerging from said overflow outlet and the other passing through said third cylindrical portion in the direction away from said second cylindrical portion to emerge from an underflow outlet of the separator at the end of said separating chamber remote from said first cylindrical portion. The above separator is intended specifically, but not exclusively, for separating oil from water, the oil in use emerging from the overflow outlet and the water from said third cylindrical portion.

The aforementioned cylindrical portions may not be truly cylindrical, in the sense that they do not need in all cases to present a side surface which is linear in cross-section and parallel to the axis thereof. For example. United States Patent 4,237,006 describes arrangements wherein the first cylindrical portion has a frustoconical section adjacent the second cylindrical portion and which provides a taper between the largest diameter of the first cylindrical portion and the diameter of the second cylindrical portion where this meets the first cylindrical portion. Likewise, the aforementioned patent specification describes arrangements wherein a similar section of frustoconical form is provided to cause a tapering in the diameter of the second cylindrical portion from a largest diameter of the second cylindrical portion to the diameter of the third cylindrical portion. There is also described an arrangement wherein the second cylindrical portion exhibits a constant taper over its whole length.

In the specification of my Australia Patent Application 12421/83 various modifications of cyclone separators of the above kind are described, and these modifications may be incorporated into separators formed in accordance with this invention In United States Patent 4,237,006, the described cyclone separator is said to comply with a number of dimensional restrictions insofar as the relative proportions of various components thereof are concerned. These constraints are:

10 ≤ 1₂/d₂ ≤ 25

0.04 ≤ 4A_i/ πd₁ ² ≤ 0.10

0.1 ≤ d₀/d₂ ≤ 0.25

d₁ > d₂

d₂ > d₃

wherein d₀ is the internal diameter of said overflow outlet, d₁ is the diameter of the first portion, d₂ is the diameter of the second portion and d₃ is the diameter of the third portion, 1₂ is the length of the second portion, A₁ is the total cross-sectional area of all the feed inlets measured at the points of entry into the separating chamber normal to the inlet flow.

It has been found that, generally speaking, the dimensional constrains therein mentioned are applicable with advantage to cyclone separators constructed in accordance with this invention except that it has not been found necessary to comply with the constraint concerning the ratio of the overflow outlet diameter to the diameter of the second cylindrical portion. Neither has it been found necessary to adhere to the maximum limit of 25 for the ratio 1₂/d₂, since greater values of this ratio may be employed.

Again, in the arrangement of United States patent specification 4,237,006, there are two feed inlets but it has not been found necessary to adhere to this. Arrangements with one inlet or with more than two inlets are workable.

It has been found in accordance with this invention to facilitate operation if the overflow outlet has a diameter d₀, adjacent the separating chamber, in the range 0.0035 ≤ d₀/d₁ < 1. More particularly, the overflow outlet may present a stepped bore with a first bore portion adjacent the first cylindrical portion being of greater diameter than a second bore portion thereof further from the first cylindrical portion. In this case the first bore portion may have a diameter d₀ in the range 0.0035 < d₀/d₁ ≤ 1 and the second bore portion may have a diameter d₅ in the range 0.0035 ≤ d₅/d₁ < d₀/d₁.

The invention provides an improved cyclone separator of the first above described kind wherein said overflow outlet presents the above mentioned stepped bore and wherein the stepped bore is characterised by the provision of a passageway leading from the said first bore portion to the exterior of the separator. The bore portions are conveniently of circular cross section but may have any convenient cross section. Preferably, valve means is provided selectively operable to permit flow from said passageway. Means may be provided sensitive to flow through the separator to control said valve means to permit said flow from said passageway on occurrence of flow through said second bore portion falling below a pre-selected rate. The flow may be measured by means positioned to be sensitive to flow in or from the second bore portion or by means positioned to be sensitive to flow in or through the first bore portion. The valve means may also be controlled to be operated by means responsive to the ratio of quantities of the liquid components in the liquid mixture to be separated whereby to open said valve means and permit flow from said passageway under the condition where the ratio exceeds a predetermined magnitude. In particular, when separating oil and water, the said valve may be opened under the condition where the oil content in emitted oil-water mixture exceeds, say, one-half percent.

Preferably too, means is provided operable to connect said passageway for flow of liquid thereinto and back into the separating chamber via said first bore portion, to facilitate clearing of blockages in the overflow outlet. The invention is further described by way of example only with reference to the accompanying drawing in which:

Figure 1 is a cutaway perspective view of a cyclone separator constructed in accordance with the present invention;

Figure 2 is an enlarged axial cross-sectional view of the overflow outlet of the separator of Figure 1; and

Figure 3 is an enlarged fragmentary cross-sectional view of the overflow outlet of the separator of Figure 1.

The separator 10 shown in Figure 1 has a separating chamber 25 having first, second and third cylindrical portions 12, 14 and 16 coaxially arranged in that order. These cylindrical portions are generally similar to the corresponding first, second and third cylindrical portions of the separating chamber of the cyclone separator described in the aforementioned United States patent 4,237,006, the disclosures of which are hereby incorporated into the present specification to form part thereof. Most particularly, the first cylindrical portion 12 has two feect pipes 26, 28 associated therewith, these being arranged to feed tangentially into the cylindrical portion 12 via respective inlet apertures of which only one aperture, namely aperture 30 associated with pipe 26, is visible in the drawing. The two feed inlet apertures are diametrically arranged one relative to the other and positioned close to the end of portion 12 remote from portion 14. The end of portion 12 remote from portion 14 also has a circular outlet opening 32 which leads to an overflow outlet pipe 34.

A tapered part 12a of the separating chamber is positioned between the first and second portions 12, 14 towards the second cylindrical portion 14. As explained in United States Patent 4,237,006 however, such tapered section is not essential.

The second cylindrical portion 14 exhibits a taper over its length, tapering from a diameter at the end adjacent part 12a equal to the diameter of part 12a at the junction between the two portions to a somewhat lesser dimension at its opposite end. Cylindrical portion 16 is a constant diameter equal to the minimum diameter of portion 14.

In the drawing, the length 1. of portion 12, its diameter d₁, the taper angle "α" of the tapered part 12a, the internal diameter d₀ of the outlet pipe 34 at its greatest diameter end, the length and diameter 1₂, d₂ of the second portion 14, the taper angle "β" of the second portion 14 and the length 1₃ and diameter d₃ of the third cylindrical portion, as well as the total area A_i of the two feed inlet apertures 30 may all be selected in accordance with the parameters mentioned in United States patent 4,237,006 although the outlet diameter d₀ need not constrained to be within limits as described therein, nor need the length 1₂ be selected to not exceed the maximum limit of 25 for the ratio 1₂/ d₂.

As described in ray Australian Application No. 12421/83, portion may be added to the separating chamber 25, this portion being designated by reference numeral 18 in the figure. Portion 18 has a part 18a adjacent portion 16 which is of frustocpnical configuration, tapering from a maximum diameter equal to d₃ at its end closest to and adjoining to the outlet end of cylindrical portion 16, to a diameter d. at its outlet end. At the outlet end of part 18a, fourth portion 18 includes an outlet pipe 18b which is of internal diameter d₄, this leading to an underflow outlet 23.

Preferably, the angle "γ" being the conicity or half-angle of the frustoconical surface of part 18a is about 45°, although angles in the range 30 to 60 are generally satisfactory. In any event, it is preferred that the ratio d₄/d₃ be in the range 1:3 to 2:3. The length of part 18a is not critical to the invention and in any event is normally fixed by the selection of the aforementioned ratio of diameters d₄ to d₃. Likewise, the length of the pipe 18b has not been found to be important to the operation of the invention. Although part 18a is shown as having a truly frustoconical cross-sectional form (that is to say it is shown as having a side surface which exhibits a linear sloping configuration relative to the axis of the portion when viewed in section) this is not essential. The part 18 may have a conicity angle which varies along the length thereof such as either increasing or decreasing the direction from the greater diameter end to the lesser diameter end thereof. In any event, it is preferred that the length of the part 18 be roughly the same as the maximum diameter thereof.

In use, liquid to be separated is admitted tangentially to the interior of cylindrical portion 12 via feed pipes 26, 28, the denser component of the liquid then travelling lengthwise through the separator to emerge from outlet 23 of pipe 18b, whilst the lighter component emerges from pipe 34.

In practical arrangements constructed in accordance with the invention, the portions 12, 14, and 16 may for example be of lengths 1₁ = 116mm, 1₂ = 1250mm, and 1₃ = approximately 1000mm. The tapered part 12a may be of length about 160mm. The first, second and third cylindrical portions may also in such a case have diameters as follows: first cylindrical portion, diameter d₁, 116mm, second cylindrical portion 14; diameter 58mm at diameter d₂ tapering to 27mm at diameter d₃, cylindrical portion 16, diameter d₃, 27mm. The feed inlets 30 may have diameters of 20mm with the overflow outlet 32 being of diameter 2.5mm.

Figure 2 shows outlet pipe 34 in more detail. The pipe has a stepped interior bore leading from outlet opening 32. More particularly, the bore has a first portion 34' adjacent outlet 32 of diameter equal to the diameter of outlet 32 and a second portion 34" away from outlet 32 of lesser diameter than bore portion 34'. Bore portion 34' may be of diameter d in the range 0.125 to 0.625 preferably 0.17 to 0.47 times the diameter d. of portion 12 of the separating chamber 25. Bore portion 34" may be of diameter d₅ 0.015 to 0.05 preferably 0.025 to 0.035 times the diameter d₁ of portion 12 of the separating chamber 25. However, in principle, the first bore portion may have a diameter d₀ anywhere in the range 0.0035 < d₀/d₁ ≤ 1 and the second bore portion may have a diameter d₅ in the range 0.0035 ≤ d₅/d₁ < d₀/d₁.

The length of the bore portion 34" is not important. It has been determined that the efficiency tends to decrease slightly as the length L, of the bore portion 34' is increased. With increasing length L, a point is eventually reached where the operation of the cyclone becomes unstable. It has also been found that the smaller the diameter d₀, the larger can be the length L before unstable operation occurs. Generally the ratio L/d₀ may be up to 10 at least for ratios d₀/d₂ ≥ 0.31. Example

Tests were conducted on a separator having diameters d₂, d₀, d₅ as follows:

d₁ = 116mm

d₂ = 58mm

d₀ = 18mm

d₅ = 3.2mm

was operated to separate oil from a mixture with water. The length L of outlet pipe at its larger diameter portion was varied and the separating efficiency E measured for each variation. Separate tests were undertaken when the separator was operated with a split ratio F equal to 1.5% and equal to 1.0%. The split ratio F, is defined as the ratio

F = Volume of removed oil from outlet pipe 34

Volume of mixture supplied to the separator per unit time

The efficiency was determined by measuring the concentration C₁ of oil in the inlet mixture and the concentration of oil C₂ in the water delivered from the underflow outlet of the separator so that efficiency E is defined as the ratio

These tests undertaken at volumetric flow of 200

L/minute gave results as shown in tables 1 and 2, where M is the ratio L/d₀.

In the embodiment shown in figure 3, outlet pipe 34 also has a passageway 51 formed through the side wall thereof and providing communication between the bore portion 34' and the exterior of the outlet pipe 34. This passageway may for example have a diameter in the range 0.05 to 0.10 of the diameter d₁. Passageway 51 provides communication, via an exterior pipe 55 to a valve 53. Under normal operating conditions, valve 53 may be closed so that overflow passes from the outlet 32 through the bore portion 34' and thence through the bore portion 34". However, under the condition where blockage of the pipe 34 occurs liquid may be admitted into the bore portion 34' via the pipe 55 and passageway 51 by connecting the outlet of the valve 53 to suitable high pressure liquid supply to permit liquid flow back through the passageway 34' through the outlet 32 and into the separating chamber of the separator. This has been found to facilitate clearing of blockages, even where the blockage occurs in the bore portion 34". The supply of high pressure liquid may be the supply of liquid to be separated which may, for example, be temporarily diverted from inflow into the inlet pipes 26, 28 during the time of admission of the liquid through the passageway 51 into the outlet pipe 34. It is possible, in an alternative embodiment of the invention (not shown), to provide

flow sensing means operable to sense the flow from the outlet pipe 34 and to automatically operate the valve 53 to divert the incoming liquid flow which is normally passed to the inlet pipes 26,28 to flow through passageway 51 to the bore portion 34' for blockage clearing.

It has been found that whilst, in general, the provision of the narrow bore portion 34" provides very satisfactory separation, it is necessary or desirable under some conditions to have a wider outlet from the separator than is provided by the bore portion 34". Under this condition, then, it is possible to open the valve 53 whereby outflow of the desired separated component through the pipe 34 occurs through the passageway 51, pipe 55 and valve 53. Such an arrangement is desirable, when separating oil and water from an oil-water mixture where the quantity of. oil in the mixture to be separated is relatively great. In particular, it is possible to provide means for continuously monitoring the oil content of water being admitted to the inlet pipes 26, 28 and connected to operate the valve 53 so as to permit outflow from the passageway 51 and pipe 55 and valve 53 under the circumstance where detected oil content exceeds a predetermined value, such as one-half percent.

An experimental separator constructed in accordance with this invention was found to perform satisfactorily for separating oil and water where the separator had the following dimensions: diameter d₀ of the outlet bore portion 34' = 19mm diameter d₅ of the outlet bore portion 34" = 3mm diameter d₆ of the passageway 51 = 9mm diameter d₁ =116mm

The invention is not confined to arrangements where there is a single passageway 51. For example two or more such passageways of various diameters may be provided. These may be selectively operable in accordance with the measured oil content or, for example, one may be used for diverting outflow under the high oil content condition and another used for clearance of blockages.

Operation of the separator of the invention, particularly oil and water, may be facilitated by arranging for entrainment of a suitable emulsion breaker into the incoming water-oil mixture.

The entrainment may be effected by use of known dosing techniques such as injecting an emulsion breaker into the incoming liquid prior to feeding to the feed pipes 26, 28.

Commercially available emulsion breakers have been found quite satisfactory. The emulsion breaker "Nalco 7723" marketed by Catoleum Pty Ltd Botany N.S.W. Australia was found effective when injected in concentrations in the range 5 to 8 p.p.m.

Emulsion breakers, or surfactants, are thought to be effective in facilitating separation of oily water because the oil is naturally present in the form of droplets which, by surface tension effects, are resistant to separating movement under centrifugal action in the separator. However, emulsion breakers act to reduce such surface tension effects to render the droplets more mobile under centrifugal forces.

Depending on the particular breaker used the concentration of added emulsion breaker may be selected to be in the range 2 to 100 p.p.m. Generally, the effectiveness of the emulsion breaker is dependent on the extent of kinetic mixing which occurs and the residence time in the mixture prior to admission to the separator. Good mixing and adequate residence time are necessary for best results. Generally, however, the described method of injection into the incoming liquid has been found satisfactory.

If greater residence time is found necessary this may be accomplished by passing the mixture and added emulsion breaker to a holding tank prior to passing to the separator.

EXAMPLE 1

Water containing 350 p.p.m. oil was admitted to a cyclone separator of form similar to that shown in

Figure 1, and of diameter d₂ = 35mm, at a flow rate of 200 litre/minute. The exit concentration of oil in separated water, at the underflow outlet, was found to be 50 p.p.m.

EXAMPLE 2

Example 1 was repeated but with the injection into the oil-water mixture prior to admission to the separator of 30 p.p.m. of a commercial emulsion breaker type sold under the name Applied Chemicals type 8980. Injection was made into a pipe leading to the separator inlet by use of a piston pump from a reservoir of the emulsion breaker. The separated water at the underflow outlet of the separator was found to have a concentration of 14 p.p.m. oil.

These and many modifications may be made without departing from the spirit and scope of the invention as defined in the appended claims.

Claims

THE CLAIMS DEFINING THE INVENTION ARE AS FOLLOWS:

1. A cyclone separator having a separating chamber having first, second and third contiguous cylindrical portions arranged in that order, the first cylindrical portion being of greater diameter than the second cylindrical portion and the third cylindrical portion being of lesser diameter than the second cylindrical portion, the first cylindrical portion having an overflow outlet at the end thereof opposite to said second cylindrical portion and a tangentially directed feed inlet, the separator being adapted to separate liquids one from the other in a mixture when infed into said separating chamber via said feed inlet, one said liquid emerging from said overflow outlet and the other passing through said third cylindrical portion in the direction away from said second cylindrical portion to emerge from an underflow outlet of the separator at the end of said separating chamber remote from said first cylindrical portion; wherein said overflow outlet has a diameter d₀, adjacent the separating chamber, in the range 0.0035 ≤ d₀/d₁ < 1 where d₁ is the diameter of the first cylindrical portion.

2. A cyclone separator as claimed in claim 1 wherein said overflow outlet presents a stepped bore with a first bore portion adjacent the first cylindrical portion being of greater diameter than a second bore portion thereof further from the first cylindrical portion.

3. A cyclone separator as claimed in claim 2 wherein said first bore portion has a diameter d in the range 0.0035 < d₀/d₁ ≤ 1 and the second bore portion a diameter d₅ in the range 0.0035 ≤ d₅/d₁ < d₀/d₁.

4. A cyclone separator as claimed in claim 1, claim 2 or claim 3 wherein the length L of said first bore portion is in the range 0 < L/d₀ < 10

5. A cyclone separator as claimed in claim 4 wherein the diameter d₀ is not substantially more than 0.31 of the diameter d₂ of the second cylindrical portion.

6. A cyclone separator as claimed in any one of the preceding claim where 0.04 ≤ 4A_i/π d₁ ² ≤ 0.10 where A_i is the total area of all the feed inlets to the separating chamber.

7. A cyclone separator as claimed in any one of the preceding claims wherein the length 1₂ of the second cylindrical portion is at least ten times the diameter d₂ of the second cylindrical portion.

8. A cyclone separator as claimed in claim 2 wherein the stepped bore is characterised by the provision of a passageway leading from the said first bore portion to the exterior of the separator.

9. A cyclone separator as claimed in claim 8 wherein valve means is provided selectively operable to permit flow from said passageway.

10. A cyclone separator as claimed in claim 9 wherein means is provided sensitive to flow through the separator to control said valve means to permit said flow from said passageway on occurrence of flow through said second bore portion falling below a pre-selected rate.

11. A cyclone separator as claimed in claim 10 wherein said means is positioned to be sensitive to flow in or from the second bore portion or is positioned to be sensitive to flow in or through the first bore portion.

12. A cyclone separator as claimed in any one of claims 8 to 11 wherein the valve means is controlled to be operated by means responsive to the ratio of quantities of the liquid components in the liquid mixture to be separated whereby to open said valve means and permit flow from said passageway under the condition where the ratio exceeds a predetermined magnitude.

13. A cyclone separator as claimed in any one of claims 8 to 12 wherein means is provided operable to connect said passageway for flow of liquid thereinto and back into the separating chamber via said first bore portion, to facilitate clearing of blockages in the overflow outlet.

14. A method of operating a cyclone separator of the kind having a separating chamber having first, second and third contiguous cylindrical portions arranged in that order, the first cylindrical portion being of greater diameter than the second cylindrical portion and the third cylindrical portion being of lesser diameter than the second cylindrical portion, the first cylindrical portion having an overflow outlet at the end thereof opposite to said second cylindrical portion and a tangentially directed feed inlet, the separator being adapted to separate liquids one from the other in a mixture when infed into said separating chamber via said feed inlet, one said liquid emerging from said overflow outlet and the other passing through said third cylindrical portion in the direction away from said second cylindrical portion to emerge from an underflow outlet of the separator at the end of said separating chamber remote from said first cylindrical portion; wherein an emulsion breaker is added to the liquid mixture to be separated, prior to feeding the mixture to the separator.

15. A cyclone separator having a separating chamber having first, second and third contiguous cylindrical portions arranged in that order, the first cylindrical portion being of greater diameter than the second cylindrical.portion and the third cylindrical portion being of lesser diameter than the second cylindrical portion, the first cylindrical portion having an overflow outlet at the end thereof opposite to said second cylindrical portion and a tangentially directed feed inlet, the separator being adapted to separate liquids one from the other in a mixture when infed into said separating chamber via said feed inlet, one said liquid emerging from said overflow outlet and the other passing through said third cylindrical portion in the direction away from said second cylindrical portion to emerge from an underflow outlet of the separator at the end of said separating chamber remote from said first cylindrical portion; including means for admission of an emulsion breaker to the liquid mixture prior to admission to the separating chamber.