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. 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 an axial direction of the outlet element. 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%. When the capacity of the separator is increased, i.e. 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. the gas). One of the disadvantages of the degasser is that this type of separatorcan be operated in case of a liquid continuous flow, i.e. 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. The known deliquidiser however has a number of drawbacks. 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. FLASH TECHNOLOGIES N.V., NETHERLANDS ANTILLES, Free format text: 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. In a first type, also known in the art as a degasser, the separator separates gas from liquid. Assigned to FLASH TECHNOLOGIES N.V., FMC TECHNOLOGIES C.V. when the pressure and/or the quantity of the mixture is increased, such liquid creep will become worse. The pipe has a number of cylindrical holes situated downstream of the swirl inducing guiding vanes. The first time the direction of the gas is changed from a circumferential direction into a radial direction when the gas is entering the holes. The Carbatec In-Line Cyclone Separator instantly transforms your standard dust collector into a Cyclone! The provision of an outlet element of which the proximal part diverges from the proximal to the distal end, i.e. The conical shape may demonstrate a constant diameter increase per unit of length (also known as a straight cone, this type of cone may be manufactured relatively easily). It has surprisingly been found that removing the gas in a smoother manner has a positive effect on the separating characteristics of the separator. This allows the collector to do the job of creating the vacuum with minimal effort while retaining maximum efficiency. 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. The blocking element may for example be: a flange (plate) which can be flat or tapered. Discuss you need with our sales team, or check the website for our massive range of dust collection fittings and accessories. In a further preferred embodiment the diverging portion of the outlet element has a substantially conical shape. 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. 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. 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. A further disadvantage of the known degasser is at above a certain gas fraction the pressure drop across the gas-outlet becomes very high. A further drawback of the known degasser is that gas removal implies twice a directional change of the gas causing a relatively high pressure drop. The gas-outlet is a cylindrical open pipe, which is mounted in the flow space of the separator. The in-line separator has a large capacity collection drum and holds the majority of your shavings and dust. Collapse of the liquid film causing liquid carryover is therefore avoided. 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. 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. 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 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. 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. A cyclone separator for separating a mixture containing solid particles, liquid and/or gas into a heavy fraction and a light fraction. The anti-creep element is preferably arranged close to the upstream side of the openings. It is noted that the openings in the divergent element may have any shape, for example circular, rectangular, slot-like, etc. of which the cross-sectional area increases from its proximal to its distal end, removes the abrupt geometry change of the deliquidiser gas-outlet. The precision-engineered cyclone uses the vacuum power created by any standard dust collector to create a powerful vortex to separate dust from air. a further part connected to the outlet element. ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:LARNHOLM, PER-REIDAR;SCHOOK, ROBERT;REEL/FRAME:018154/0806;SIGNING DATES FROM 20051212 TO 20051217, Owner name: 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. 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. The separator may be used for separation of a mixture containing different liquids as well. Note: Powered dust collector or extractor not included. 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 degasser is used when the continuous phase is the liquid in case of a gas/liquid mixture. 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. Also the pressure drop across the gas-outlet is only a fraction of the pressure drop in the conventional degasser outlet. The method includes feeding the mixture through an inlet of a cyclone separator into a flow space of the cyclone separator and guiding the mixture along one or more swirl-elements of the cyclone separator for causing the mixture to rotate so as to fling the heavy fraction into a outer region adjacent the inner surface of the outer casing and so as to keep the light fraction in a central region. 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. 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. An example of an inlet cyclone is disclosed in European patent application EP 1 187 667 A2. The flange. This machine will reduce the likelihood of your filter or filter bag clogging, resulting in all-round better performance. 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. ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:FLASH TECHNOLOGIES N.V.;REEL/FRAME:021170/0883, Free format text: 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. Therefore the angled elongate openings are arranged in the outlet element so as to minimize the angle between the streamlines and the openings for ensuring a more natural, smooth flow of the gas through the openings. It is an object of the present invention to overcome the above mentioned disadvantages of the known inline degasser- and deliquidiser devices. 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. 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 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. 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. 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. In the outlet region the gas and liquid are separated at a fired streamwise position. FMC TECHNOLOGIES C.V., ILLINOIS, Owner name: 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. According to another aspect of the present invention, a method is provided for separating a mixture containing solid particles, liquid and/or gas into a heavy fraction and a light fraction. 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. 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. The separator including the following which are 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 fraction 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, the outlet element being provided with one or more elongate openings through which the light fraction can enter the inner passage, the openings extending obliquely with respect to an axial direction. It is however also conceivable to arrange the anti-creep element one or more other locations, for example more upstream. 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. 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. Device and system for separating a mixture. 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. In order to prevent the desired effects of the liquid creep one or more anti-creep elements are arranged upstream of the openings in the outlet element, which anti-creep elements deflect the liquid flow outward, so that the liquid can be carried along by the turbulence flow on the outer side of the outlet element. Conversely, a mixture flowing along a swirling blade with decreasing curvature, undergoes an increasingly slower swirling movement. 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