AU606039B2 - Treatment of multi-phase mixtures - Google Patents

Description

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PCT

INTERNATIONAL APPLICATION PUBLISHED UNDER THE PATENT COOPERATION TREATY (PCT) (51) International Patent Classification 4 B04C 11/00

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(11) International Publication Number: Al (43) International Publication Date: WO 87/ 01968 9 April 1987 (09.04.87) (21) International Application Number: PCT/AU86/00288 (22) International Filing Date: 2 October 1986 (02.10.86) (81) Designated States: AU, DK, GB, NO, US.

Published With international sear (31) Priority Application Number: PH 2705 (32) Priority Date: 2 October 1985 (02.10.85) (33) Priority Country: Ai l 34(4)a) DIRECTION SEE FOLIO NAiE DIRECTEDCooCo SCo S C 1 c1k CJ rr C i1, k crnpA-pTnrcant (for US only) PRENDERGAST, Gavan, Joseph, James [AU/AU]; 3 Seaton Court, Mt. D Waverley, VIC 3149 (AU).

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28 MAY 1987 (74) Agents: SMEETON, Anthony, R. et al.; Davies Collison, I Little Collins Street, Melbourne, VIC 3000 (AU). AUSTRALIAN 2 4 APR 1987 PATENT OFFICE (54) Title: TREATMENT OF MULTI-PHASE MIXTURES (57) Abstract A multi-phas treatment system which comprises a mixture separation apparatus having one or more cyclone separators therein, An infeed flow line delivers the multi-phase mixture to the mixture separation apparatus and at least two output flow lines (5 and 6) discharge the mixture in at least a partially separated condition from the mixture separation apparatus The system further includes analysing means which is arranged to analyse the mixture before and/or after entry or discharge from the mixture separation apparatus A central control means (15) is provided which is responsive to information received from the analysing means to control the flow rate in on or more of the flow lines.

4. The basic application... referred to in paragraph 3 of thls claration was thf m ade in a Co nv en t io n c ry i n ct of the inventionre the first application made in a Convention country in respect of the invention t ject cf th e ap pl iati zi.c Insert place and date of signature.

Signature of declarant(s) (no attltation required) Note' Initial all alterations.

Declared at X/0 t his DAVIES OLL....SO MELBOURNE and CANBER DAVIES COLLISON, MELBOURNE and CANBERRA.

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"TREATMENT OF MULTIPHfASE MIXTURES" The present inviintion relates to a multi-phase treatment system for the treatment of the mixture discharged from an oil wel,. The mixture discharged from an oil well is primarily an oil/water mixture which may include gaseous and solid phases.

Research into the use of cyclone separators for the separation of oil/water mixtures has increased in recent years. One of the reasons for a growing interest in this area is because of the particular problems associated with off-shore platforms. One of the major problems is that of the weight of processing equipment and, as a result of this, attempts are continuously being made to try and reduce the weight of processing equipment. It is with this in mind that investigations have been conducted into the use of cyclone separators.

901 1o,dbwspc.0l8,muld JpCl WO 87/01968 PCT/AU86/00 28 8 Applicant has already devised cyclone separators of a unique type which can be used in the separation of oil/water mixtures where there is a relatively small amount of oil in the mixture (say less than Such separators are useful for cleaning the water discharging from a processing system so that it can be discharged directly into the sea without major contamination problems. Generally, separators which are used in such a manner require little if any control other than some control on the flow through the separator system.

There is another processing situation where cyclone separators could find application and that is for separating the product oil from the mixture discharged from the well.

The separators of the type mentioned above have been found not to be suitable for use in applications where larger volumes of oil have to be separated. Applicant has devised several types of unique separators which are particularly suitable for this new application.

This, however, is not the complete solution as control of these new separators has been found to be difficult particularly in practical situations.

It is therefore an object of the present invention to provide a multiphase mixture treatment system which enables satisfactory separation of the phases in that mixture.

ii mI i 2a According to the present invention there is provided a multi-phase mixture treatment system for the treatment of the mixture discharged from an oil well, the system including: means for minimising the weight of the system including at least one cyclone separator comprising elements designed, sized and arranged for separating a more dense liquid component from a less dense liquid component thereof, said separator comprising a separating chamber having a feed inlet at one end, an overflow outlet at said one end and an underflow outlet at the other end; an infeed flow line for delivering the multi-phase mixture from the oil 10 well to the feed inlet of the cyclone separator; at least two outflow lines from which the separated or partially separated S phases are discharged from the overflow and underflow outlets of the cyclone separator; and means for controlling the separation of the mixture through the cyclone separator, said means including analysing means for analysing the mixture before and/or after entry to or discharge from the cyclone separator and a central control 0 means responsive to information received from said analysing means for controlling the flow rate from one or more of said flow lines.

20 The present invention further provides a multi-phase mixture treatment system for the treatment of the mixture discharged from an oil well, the system including: means for minimising the weight of the system including at least one cyclone separator comprising elements designed, sized and arranged for separating a more dense liquid component from a less dense liquid component thereof, said separator comprising a separating chamber having a feed inlet at one end, an overflow outlet at said one end and an underflow outlet at the other end; an infeed flow line for delivering the multi-phase mixture from the oil well to the feed inlet of the cyclone separator; at least two output flow lines from which the separated or partially separated phases are discharged from the overflow and underflow outlets of the 901101,dbwspe.018,multil.pe,3

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i ii .7 -3 cyclone separator; and means for controlling the separation of the mixture through the cyclone separator, said means including analysing means for analysing the mixture discharged from the overflow outlet of the cyclone separator and central means responsive to information received from said analysing means for controlling the flow rate in one or more of said flow lines.

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901 101,dbwspc.018,multilspc,4 -3a- This control means may allow for unattended operation whilst inlet concentrations vary extensively and continuously from, for example 1% water to 40%. In addition, the separation apparatus, means of analysis, central control means and control equipment may be at remote or removed locations and may be separated by other process equipment such as pumps, vessels and other control means. The analysing means may take Sany suitable form and is preferably adapted to analyse or interpolate the various volumetric percentages of the S'particular phases making up the mixture or characteristics I reflecting phase concentrations such as density, viscosity and the like. For example in the particular-app-ieat-ien-of- .eil/water-mixtures the analysing means may be in the form of *capcitance prober; a WO87/01968 PCT/AU86/0028 8 -4- In some instances, it may be desirable to provide additional information to the controller.

For example, information relating to flow rate may be provided by means of flow indicators.

Such flow indicators may be in the form of orifice plates or turbine meters by way of example.

The central control means may be for example, a pneumatic or electric controller which is programmable and preset so that it operates in response to information received from the analysing means.

TIic flow conclrol mncais may take The rormi of valves or restrictions to flow such as choku valves and the like.

In certain instances, it may be desirable to

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reduce the amount of gas or substantially remove it from the mixture prior to the mixture being delivered to the mixture separation apparatus. To this end, means may be provided for separating gas from the mixture and such means may be in the form of a surge tank or the like.

Preferred embodiments of the invention will hereinafter be described with reference to the accompanying drawings, and in those drawings: Figures 1 to 5 are different system arrangements all in accordance with the system of the present invention; and Figure 6 is one example of a practical application of the invention.

4 Referring to Figure 1, there is shown a system generally indicated at 1 according to the present invention which includes a mixture separating apparatus generally indicated at 2 comprising a cyclone separator 3 of the type for separating WO 87/01968 PCT/AU86/0028 8 relatively large amounts of oil from water, It will be appreciated that separation may not be complete during one pass and further cyclone separators may be required. An infeed flow line 4 delivers the oil/ water mixture to the separator 3 and the water is discharged through butput flow line 5 and the oil is discharged through output flow line 6.

in this particular embodiment an analyser 9 disposed in the input feed line 4 is adapted to analyse or interpolate the various volumetric percentages of the oil/water mixture or characteristics reflecting phase concentrations such as density,viscosity or the like. In addition to this flow indicators 10 and 11 provide information concerning the flow rates of the input flow line 3 and the water output flow linte 5. The information collected by the analyser 9, and flow indicators and 11 is fed to a central controller 15. The controller 15 is adapted to open or close flow control valve 17 to provide for optimum separation of the oil/water mixture. Thus, in this particular system, the analyser 9 provides the central controller with information relating to the mixture being fed to the separation apparatus.

In Figure 2, the system includes similar equipment to that shown in Figure i, except that there are no flow indicators provided and analyser 9 is arranged to analyse the mixture in oil output flow line 6 and the controller 15 is arranged to open or close flow control valve 19 which controls the flow in oil/output flow line 6.

Figure 3 is similar to that shown in Figure 2 except that it is the water output flow line 5 which is analysed and the flow controlled by the controller 15 through flow control valve 17.

i L WO 87/01968 PCT/AU86/00288 -6- Referring to Figure 4, there is shown a system in which the flow from the oil or lighter phase output flow line 6 is analysed and controlled by central controller 15 through opening or closing of valve 19.

In the system of Figure 5, the controller controls flow from the lighter phase output flow line 6 although both the input to tie separator as well as information from that output line are fed to the controller.

Figure 6 shows a system for separation of oil/ water mixtures where the oil/water mixture is fed to the system from a number of different oil wells 51 to 56.

A pump 58 may assist in delivering the mixture to the system and a surge tank 59 may be provided to remove gas from the mixture. The mixture is fed to a bank of cyclone separators 3 arranged in parallel. An analysing device 9 and a flow meter 10 analyse the mixture prior to entry into the cyclone separators and feed this information to a controller 15. The controller also receives information as to the water output flow rate and from this information controls that flow rate through valve 17.

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Claims (14)

1. A multi-phase mixture treatment system for the treatment of the mixture discharged from an oil well, the system including: means for minimising the weight of the system including at least one cyclone separator comprising elements designed, sized and arranged for separating a more dense liquid component from a less dense liquid component thereof, said separator comprising a separating chamber having a feed inlet at one end, an overflow outlet at said one end and an underflow outlet at the other end; 10 an infeed flow line for delivering the multi-phase mixture from the oil o well to the feed inlet of the cyclone separator; 0 at least two outflow lines from which the separated or partially separated phases are discharged from the overflow and underflow outlets of the cyclone separator; and means for controlling the separation of the, mixture through the cyclone separator, said means including analysing means for analysing the mixture before and/or after entry to or discharge from the cyclone separator and a central control i means responsive to information received from said analysing means for controlling the flow rate from one or more of said flow lines.

2. The system according to claim 1 wherein said analysing means comprises one or more capacitance probes.

3. The system according to claim 2 wherein said analysing means further includes one or more flow indicators,

4. The system according to claim 1, wherein said control means comprises a pneumatic or electric controller which is programmable and preset so that it is operable in response to information received from the analysing means.

The system according to claim 4 wherein said analysing means is arranged 9011 o,dbwspx.18,multi I pe7 -8- to analyse the mixture in the infeed flow line.

6. The system according to claim 4 wherein said analysing means is arranged to analyse the mixture in one of the output flow lines.

7. The system according to claim 1 further including means for removing gas from the mixture prior to entering the mixture separation apparatus,

8, A multi-phase mixture treatment system for the treatment of the mixture S* 10 discharged from an oil well, the system including: I means for minimising the weight of the system including at least one cyclone separator comprising elements designed, sized and arranged for separating a more dense liquid component from a less dense liquid component thereof, said separator comprising a separating chamber having a feed inlet at one end, an overflow outlet at said one end and an underflow outlet at the other end; an infeed flow line for delivering the multi-phase mixture from the oil ,j well to the feed inlet of the cyclone separator; at least two output flow lines from which the separated or partially separated phases are discharged from the overflow and underflow outlets of the 20 cyclone separator; and i means for controlling the separation of the mixture through the cyclone separator, said means including anilysing means for analysing the mixture discharged from the overflow outlet of the cyclone separator aMd central means responsive to information received from said analysing means ;tur controlling the flow rate in one or more of said flow lines, U

9, The system according to claim 8 wherein said analysing means omprises one or more capacitance probes.

10. The system according to claim 9 wherein her includes one or more flow indicators, O1 101,dbwspt0j8,mut 3pO,$ ov Uo%. uiiiaigu inom me overlow and underflow outlets of the cyclone separator; and means for controlling the separation of the mixture through the cyclone separator, said means ucluding analysing means for analysing the mixture before and/or after entry to or discharge from the cyclone separator and a central control S./2 1 P F7, I i i I I, -9-

11. The system according to claim 10 whercin said control means comprises a pneumatic or electric controller which is programmable and preset so that it is operable in response to information received from the analysing means.

12. The system according to claim 2 wherein said control means comprises a pneumatic or electric controller which is programmable and preset so that it is operable in response to information received from the analysing means.

13. The system according to claim 3 wherein said control means comprises a 10 pneumatic or electric controller which is programmable and preset so that it is operable in response to information received from the analysing means,

14. A multi-phase mixture treatment system substantially as hereinbefore described with reference to the accompanying drawings. 00 *0 *s 9 0.* .0. 000 0 0 *000 0 t 0 0 *909 DATED this 1st day of November, 1990, CONOCO SPECIALTY PRODUCTS, INC. By its Patent Attorneys DAVIES COLLISON iCA 4 o- U,8 901 O1dbsptOM8MU11 pSVC,9