cyclone separator dust separators collectors collector separation cs separator bsp cyclonic Besides separating a two phase mixture, the separator according to the present invention may also be used for separating a mixture having more than two phases (multi phase mixture). of which the cross-sectional area increases from its proximal to its distal end, removes the abrupt geometry change of the deliquidiser gas-outlet. One of the disadvantages of the degasser is that this type of separatorcan be operated in case of a liquid continuous flow, i.e. Numerous devices are known for separating incoming flows of various liquids (far example oil and water), gas and solid particles (dust particles), liquid and gas (for example oil and natural gas) or solid particles, liquid and gas. The pipe has a number of cylindrical holes situated downstream of the swirl inducing guiding vanes. In this arrangement the continuous phase is the gas and in practice only volumetric gas fractions of less than 10% can be handled by such devices implying that the operating range of the deliquidiser is small. It allows for a 99% dust and chip separation prior to the shavings entering your existing extractor. It has surprisingly been found that removing the gas in a smoother manner has a positive effect on the separating characteristics of the separator. The gas will accumulate upstream of the blocking element, causing the gas to be discharged through the openings in the outlet element instead of through the second passage between the outer element and the outer casing. Another type of cyclone separator is the so-called inline separator wherein the incoming mixture and at least a part of the outgoing mixture flows through a pipeline, the separator being essentially aligned with the pipeline. According to another aspect of the present invention a separator is provided for separating a mixture containing solid particles, liquid and/or gas into a heavy fraction and a light fraction, the apparatus including an outer casing defining a flow space through which the mixture is to flow and having an inlet for the incoming mixture, a first outlet for the separated light fraction and second outlet for the separated heavy fraction. Carbatec In-Line Cyclone Separator with Mobile Stand, Out of Stock - Will be placed on Backorder, Welcome to Carbatec - The home of woodworking, Planer Thicknessers & Combination Machines, Sharpening Machine, Grinders & Accessories, Spindle Moulder Cutter Blocks and Accessories, Countersink and Counterbore Bits and Sets, Carbatec Sharpening, Grinding & Polishing, CMT Spindle Moulder Cutter Blocks and Accessories, Robert Sorby Sharpening, Grinding & Polishing, Share Your Woodworking Passion and Inspire Others, Carbatec Clear Dust Extraction Ducting Kit with "Y" Fittings, Carbatec 4" Dust Collection Accessory Kit, Carbatec 3 metres of 4" Clear Hi-Flex PVC Hose, Carbatec Plastic Collection Bags - Pk of 10 - Suits drum diameters up to 510mm - 1250mm Long, Unpowered unit connects to your existing dust collector or dust system, Sits between your powered collectorand your machines, Separates the dust and shavings BEFORE they get to your powered collector, Fully frame supported cyclone cone, with mobile base and drum. For high gas loads with a volumetric gas fraction above 30% this may result in relatively large pressure drops and limited gas removal capacity. The gas-outlet is a cylindrical open pipe, which is mounted in the flow space of the separator. the cyclone separator including an outer casing defining a flow space through which, the mixture is to flow and having an inlet for an incoming mixture. Due to the density difference between the gas and the liquid and the initiated centrifugal field, the gas is forced into the center of the separator, implying a stable core of gas. 119, the benefit of priority of the filing date of May 26, 2004 of a Dutch patent application, copy attached, Serial Number 1026268, filed on the aforementioned date, the entire contents of which is incorporated herein by reference. This means that gas removal can lead to a collapse of the above mentioned gas core/liquid film which will create unstable behavior and will deteriorate the separation characteristics of the separator. Removal of the gas core is executed by a cylindrical gas-outlet pipe in the center of the cyclone. The included mobile support frame is compact and stable, with no awkward lifting to empty the drum. It is a still a further object of the present invention to provide a separator and a method of separating a mixture which is not clearly gas-continuous or liquid-continuous. The present invention also relates to a method of separating the mixture in the separator. It is noted that the openings in the divergent element may have any shape, for example circular, rectangular, slot-like, etc. A first aspect of the present invention regards a cyclone separator provided for separating a mixture containing solid particles, liquid and/or gas into a heavy fraction and a light fraction, the separator including an outer casing defining a flow space through which the mixture is to flow and having an inlet for an incoming mixture, a first outlet for the separated light fraction and second outlet for the separated heavy fraction. It is a further object of the present invention to provide a separator and a method of separating a mixture with an extended operating range compared to the existing in-line separator arrangements. Inlet cyclones are employed in gravity separation vessels wherein. The curvature of the guiding vanes can vary. According to a preferred embodiment of the present invention the elongate openings extend within an angle of 30 with respect to the local flow direction of the light fraction. ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:FLASH TECHNOLOGIES N.V.;REEL/FRAME:021170/0883, Free format text: The precision-engineered cyclone uses the vacuum power created by any standard dust collector to create a powerful vortex to separate dust from air. ABANDONED -- FAILURE TO PAY ISSUE FEE. Application filed by FMC Technologies CV, Flash Technologies NV. A cyclone separator for separating a mixture containing solid particles, liquid and/or gas into a heavy fraction and a light fraction. When the mixture is a liquid-liquid mixture, the heavy fraction mainly contains a first liquid having a relatively high density, for instance water, and the light fraction mainly contains a second liquid having a relatively low density, for instance oil. The Carbatec In-Line Cyclone Separator instantly transforms your standard dust collector into a Cyclone! an outer casing defining a flow space through which, the mixture is to flow and having an inlet for an incoming mixture, wherein the inlet is connected to the supply part; an outlet element having a central, axially extending inner passage connected to the first outlet for discharge of the light fraction and an outer surface which, together with an inner surface of the outer casing, defines an outer passage connected to the second outlet for discharge of the heavy fraction, the outlet element being provided with one or more elongated openings through which the light fraction can enter the inner passage, the one or more elongate openings extending obliquely with respect to a axial direction of the outlet element; and. When for instance the curvature of a swirling blade increases in flow direction, the mixture flowing therealong will then undergo an increasingly more rapid swirling movement. For example when the flow body and the outlet element are integrated into one structural element, the anti-creep element may be provided on different locations between the downstream end of the swirl element and the upstream end of the openings in the outlet element. In a further embodiment the length of each of the openings is about 10-50% of the circumference of the outer surface of the outlet element. This machine will reduce the likelihood of your filter or filter bag clogging, resulting in all-round better performance. The method further includes guiding the heavy fraction in the outer region through an outer passage of the cyclone separator, discharging the heavy fraction from a first outlet of the cyclone separator and guiding the light fraction in a core region of the cyclone separator through an opening in an outlet element of the cyclone separator and discharging the light fraction from a second outlet of the cyclone separator. According to both of the previously mentioned aspects of the present invention the separation characteristics are improved by having the incoming mixture follow a more natural path through the separator, either by providing angled elongate openings in the outlet element or by providing a divergent portion of the outlet element. Further advantages, features and details of the present invention will be elucidated in the light of the following description, with reference to the annexed drawings, in which: The embodiments of the separators according to the present invention shown in the drawings are especially intended for separation of a gas phase (gas phase vapor) from a liquid phase (water/oil), for example in a pipeline leading to an oil platform. Device and system for separating a mixture. The present invention also relates to a pipe for transporting said mixture, the pipe being provided with at least one of the cyclone separators. It is however also conceivable to arrange the anti-creep element one or more other locations, for example more upstream. However, the separation characteristics of the separator are further improved when the diverging shape of the outlet element is combined with the angled elongate openings or slots in the outlet element. CYCLONES, Apparatus in which the axial direction of the vortex (flow following a screw-thread type line) remains unchanged Also devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct, Construction of inlets or outlets to the vortex chamber, PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL, Separation of liquids, not provided for elsewhere, e.g. The deliquidiser separates in this case the liquid from the gas. Moreover, a relatively low pressure drop is present across the gas-outlet.

A further drawback is that the gas-outlet pipe forms a disturbance in the flow space of the separator, which may result in controllability problems due to the sudden removal of the driving phase (i.e.

In a further preferred embodiment one or more blocking elements are arranged downstream of the openings for at least partially blocking the light fraction from entering the outer passage.

at least one swirl element arranged in the outer casing and between the flow body and the outer casing for setting the mixture into a rotating movement for the purpose of separating the mixture into the heavy and light fractions. feeding the mixture through an inlet of a cyclone separator into a flow space of a cyclone; guiding the mixture along a swirl element for causing the mixture to rotate so as to fling the heavy fraction into an outer region adjacent an inner surface of an outer casing of the cyclone separator and so as to keep the light fraction in a central region of the cyclone separator; guiding the heavy fraction in the outer region through an outer passage of the cyclone separator; discharging the heavy fraction from a first outlet of the cyclone separator; guiding the light fraction in the central region through openings in the outlet element; discharging the light fraction from a second outlet of the cyclone separator. If the openings or slots are arranged with a length of about 50% of the circumference of the outer surface and the angle between the slots and the actual direction is about 45, the length of the slots will be comparable to the mean diameter of the outlet element. An example of a deliquidiser is described on WO 02/056999 A1. Due to the density difference and the created centrifugal field the liquid is forced towards the pipe-wall resulting in a table liquid film moving in a direction of the gas-outlet. Assigned to FLASH TECHNOLOGIES N.V., FMC TECHNOLOGIES C.V. This unpowered separator cannot increase the suction power of your existing system, but instead does an amazing job of keeping the dust and shavings out of your dust collector. In case of curved guiding vanes one can therefore modify the swirling speed of the heavy fraction and hence the pressure drop through a correct choice of the curvature. A further effect is that the rotating movement of the mixture remains more stable for a longer axial distance, as a result of which the liquid carry-over in the gas-outlet is minimized. By arranging a counter swirl-element in the first discharge channel to reduce swirling movement of the light fraction, the pressure drop across the inner passage is decreased, whereby the discharge of the light fraction through the inner passage is improved. a further part connected to the outlet element. Collapse of the liquid film causing liquid carryover is therefore avoided. The anti-creep element is preferably arranged close to the upstream side of the openings. In a further preferred embodiment one or more anti-creep elements are arranged in the flow space between the flow body and the openings in the outlet element. One of the known techniques for separating such mixtures is the cyclone technique, wherein the incoming mixture is caused to rotate inside a cyclone tube, the rotation causing the relatively heavyweight parts of the mixture, for example the liquid in a liquid/gas mixture or the solid particles in a gas/solid particle mixture, to flow as a result of the centrifugal forces exerted on the rotating mixture in the direction of the walls of the tube, while the relatively lightweight fraction, for example the gas in the gas/liquid mixture, remains more or less in a central region inside the tube. an outer casing defining a flow space through which the mixture is to flow and having an inlet for an incoming mixture, wherein the inlet is connected to the supply part, a first outlet for the separated light fraction and second outlet for the separated heavy fraction; wherein the outlet element is a tubular element having a substantially cylindrical downstream portion and a substantially diverging upstream portion, the diverging portion being provided with one or more openings through which the light fraction can enter the inner passage; and. The present invention relates to a cyclone separator for separating a mixture containing solid particles, liquid and/or gas into a light fraction and a heavy fraction. The second type of inline cyclone separator is a separator, also referred to as a deliquidiser, wherein a gas-continuous feed is brought into rotation by a number of swirl inducing guiding vanes. Inline cyclone separators can be subdivided in two different types. FMC TECHNOLOGIES CV, ILLINOIS, Free format text: The provision of an outlet element of which the proximal part diverges from the proximal to the distal end, i.e. The abrupt removal of the gas may moreover lead to a collapsing liquid film, which also has a negative effect on the separation characteristics, for example the separation efficiency, of the deliquidiser. Also the pressure drop across the gas-outlet is only a fraction of the pressure drop in the conventional degasser outlet. In practical situations the angle between the longitudinal direction of an opening and the axial direction (z-axis) of the outlet element is between 0 and 90, more preferable between 10 and 80 and even more preferable between 30 and 60 degrees. coil, Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces, Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces, Construction of elements by which the vortex flow is generated or degenerated, GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS, TECHNICAL SUBJECTS COVERED BY FORMER USPC, TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION, With means for separating solid material from the fluid, Korea Institute Of Geoscience And Mineral Resource. The apparatus including the following items arranged in the outer casing: a flow body along which the mixture to be separated can be carried; at least one swirl element arranged between the flow body and the outer casing for setting the mixture into a rotating movement for the purpose of separating the mixture into the heavy and light fractions; and an outlet element having a central, axially extending inner passage connected to the first outlet for discharge of the light fraction and an outer surface which, together with the inner surface of the outer casing, defines an outer passage connected to the second outlet for discharge of the heavy fraction. As the mixture that has been brought into rotation by the swirl inducing guiding vanes has a substantial axial speed component in the core region of the cyclone, liquid creep may occur along the outlet element, whereby liquid droplets from the inlet flow may enter the inner passage of the outlet element through the openings or slots provided in the outlet element. by thermal diffusion, Separation of non-miscible liquids by centrifugal force, Degasification of liquids modifying the liquid flow, Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused, 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. The 5 single inlet port with 2x4 Y fitting allow you to connect multiple machines. Shell Internationale Research Maatschappij B.V. , , Korea Institute Of Geoscience And Mineral Resources, FLASH TECHNOLOGIES N.V., NETHERLANDS ANTILLES, ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:LARNHOLM, PER-REIDAR;SCHOOK, ROBERT;REEL/FRAME:018154/0806;SIGNING DATES FROM 20051212 TO 20051217, ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:FLASH TECHNOLOGIES N.V.;REEL/FRAME:021170/0883, Distillation solids removal system and method, In-line device for gas-liquid contacting, and gas processing facility employing co-current contactors, Axial flow-type cyclone dust collection device, Apparatus for Cyclone Separation of a Fluid Flow Into a Gas Phase and a Liquid Phase and Vessel Provided with such an Apparatus, Assembly for monitoring contaminant particles in liquid flow, Pipe-integrated oil well fluid or oilfield fluid separation apparatus, and method thereof, A kind of multitube multicyclone dust collector, Centrifugal separator having frame secured within a vessel, Contacting a gas stream with a liquid stream, Separating impurities from a gas stream using a vertically oriented co-current contacting system, Separating impurities from a fluid stream using multiple co-current contactors, Separating carbon dioxide and hydrogen sulfide from a natural gas stream using co-current contacting systems, A kind of combination high-efficiency gas-liquid separator, A kind of width process multi-streaming type high efficient gas and liquid separator, Centrifugal separator having a vortex generator, Inner surface features for co-current contractors, Compact contacting systems and methods for scavenging sulfur-containing compounds, Fractionation system using compact co-current contacting systems, Integration of cold solvent and acid gas removal, Cyclone separator and methods of using same, Devices and methods for the isolation of particles, Oil separator and air conditioner including the same, Fractionation system using bundled compact co-current contacting systems, Bituminous froth inclined plate separator and hydrocarbon cyclone treatment process, System and process for concentrating hydrocarbons in a bitumen feed, Bituminous froth inline steam injection processing, Process and apparatus for treating a heavy hydrocarbon feedstock, Method and apparatus for oil sands ore mining, Method and device for separation of oil-water mixes, Assembly for separating a multiphase stream, Cyclone separator for high gas volume fraction fluids, Apparatus and method for regulating flow through a pumpbox, DEVICE FOR SEPARATING A HETEROGENEOUS MIXTURE, Method and system for fluid separation with an integrated control system, Apparatus and method for removing a contaminant from a contaminated stream, Arrangement for separating liquid mixtures, High temperature dust tail gas cyclone dust collector, Automatic vertical heterogeneous integration cyclone separation device of paraffin removal, Gas scrubber, entrainment separator and combination thereof, Device for removing impurities from gases, Device for separating liquids and/or solids from a high-pressure gas stream, Device for separating from a gas stream liquids and/or solid matters or gases having a different specific weight, Apparatus and method for processing of a mixture of gas with liquid and/or solid material, Apparatus for separation of a fluid flow, especially into a gas phase and a liquid phase, Apparatus for separating aqueous phase from a mixture of hydrocarbon & aqueous fluid, Apparatus for cyclone separation of a fluid flow into a gas phase and a liquid phase and vessel provided with such an apparatus, Device for cyclone separation of gas-liquid mixture flow into gas-phase fraction and liquid fraction, additionally equipped with special tank, Cyclone separator and method for separating a solid particles, liquid and/or gas mixture, Separator for separating a solid, liquid and/or gas mixture, Cyclone separator, liquid collecting box and pressure vessel, Multi-stage gas-water separation device and gas-water separator, Apparatus for and method of separating multi-phase fluids, Cyclonic liquid degassing separator and method for degassing a fluid mixture, System for separating an entrained immiscible liquid component from a wet gas stream. the liquid is entrained by the gas and discharged through the gas-outlet pipe.

In a first type, also known in the art as a degasser, the separator separates gas from liquid. Owner name: A first outlet for the separated light fraction and a second outlet for the separated heavy fraction and a flow body arranged in the outer casing and along which the mixture to be separated is carried. This means that in practice only volumetric gas fractions between 0% and 40% can be handled by such devices. The shape of the outlet element will provide sufficient space for the light fraction to be removed from the separator and will, in combination with the angled slots extending more or less in parallel with the streamlines, result in the earlier described low pressure drop and the non-sudden removal of the driving phase. FMC TECHNOLOGIES C.V., ILLINOIS, Owner name: In this way a fairly natural flow of the mixture can be achieved, resulting in an improved separating efficiency of the separator. This may limit the capacity of the cyclone, whereby the cyclone separator for the desired separation conditions would have to increase in size. In the degasser, the liquid-continuous flow is brought into rotation by a plurality of swirl inducing guiding vanes. The flange. When the angle between the longitudinal direction of the opening and the actual direction of the outlet element is chosen between 30 and 60, or, more preferable, about 45, a cyclone separator of an extended operating range is provided, the range being typically defined by a volumetric gas fraction of 30-95% and a volumetric liquid fraction of 5-70%. If the slots are made too long, the structural integrity of the outlet part may be jeopardized, while if the slots are too short this will result in a relatively large pressure drop across the outlet, element. By arranging the elongate openings in an oblique manner with respect to the axial direction (z-direction in the drawings) of the outlet element the circumferential movement (rotation) of the rotating mixture can be followed more easily, resulting in a more natural way of guiding the gas through the openings, with less change of the directions of the gas, and discharging the gas from the gas-outlet. Also the controllability of the separator is increased as the gas removal takes place along a larger axial distance and there is no abrupt removal of the driving force. The counter swirl-elements may include one or more guiding vanes, which may be curved or just straight blades, and which are shaped so as to reduce the rotating movement of the heavy fraction. A blocking element can be embodied for example as a flange or a hollow truncated form extending from the outer surface of the outlet element.

By arranging a counter swirl-element in the second discharge channel to reduce swirling movement of the heavy fraction, the pressure drop across the second passage is decreased, whereby the discharge of the heavier fraction through the second passage is improved. In a further preferred embodiment the diverging portion of the outlet element has a substantially conical shape. In an especially preferred embodiment the openings extend substantially parallel with the local main flow direction of the light fraction. The inlet cyclone is connected to the inlet of the gravity separation vessel and is provided with an outlet for the heavy fraction and an outlet for the light fraction, both outlets discharging into the interior of the gravity separation vessel for further separation of the mixture. It is an object of the present invention to overcome the above mentioned disadvantages of the known inline degasser- and deliquidiser devices. Apparatus and method for separating particles from a particulate suspension, Information on status: application discontinuation. Conversely, a mixture flowing along a swirling blade with decreasing curvature, undergoes an increasingly slower swirling movement. using a cyclone, or by a tangential inlet, Separation of suspended solid particles from liquids by sedimentation, Separation of sediment aided by centrifugal force or centripetal force, Separation of sediment aided by centrifugal force or centripetal force by using a vortex inducer or vortex guide, e.g. The separator may be used for separation of a mixture containing different liquids as well. Applicants claim, under 35 U.S.C. The known deliquidiser however has a number of drawbacks. May require extra fittings to connect to your collector or collection system. The design and size of the blocking element will depend on the gas/liquid or gas/solid particle ratios. some sort of pretreatment is performed on the mixture to be separated.

A further disadvantage of the known degasser is at above a certain gas fraction the pressure drop across the gas-outlet becomes very high. Assignors: SCHOOK, ROBERT, LARNHOLM, PER-REIDAR, data:image/svg+xml;base64,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, data:image/svg+xml;base64,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, CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES, APPARATUS USING FREE VORTEX FLOW, e.g.



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