TH64909B - Separation systems including vortex valves - Google Patents

Abstract

DC60 (12/05/53) The invention involved a separation system consisting of an inrush channel (16), a system for separating a vortex flap valve (100), managed to receive and Controls the flux of the fluid flow through the inlet channel (16) and to form a vortex flow, with a vortex flow around the core (11). The system for further decoupling. The separation chamber (40) is positioned relative to the vortex flap (100) to receive the vortex flow from the vortex flap (100), where the separation chamber. (40) consists of first and second outflow channels (41,42). The first (41) outflow channels are positioned to receive the inner part of the vortex and outlet port. The second (42) has been positioned to accept the outer portion of the spiral flow. The invention involved a separation system consisting of an inrush channel (16), a separating system with a vortex valve (100), managed to receive and Controls the flux of the fluid flow through the inlet channel (16) and to form a vortex flow, with a vortex flow around the core (11). The system for further decoupling. Also, the proportional chamber (40) is positioned relative to the endpoint with the vortex valve (100) to receive the vortex flow from the vortex flap (100), where the chamber for the Separate (40) consists of first and second (41,42) outflow channels.The first (41) outflow channels are positioned to receive the inner part of the vortex and the channel. The second outlet (42) has been positioned to accept the outer portion of the spiral flow.

Claims (8)

Disclaimer (all) which will not appear on the advertisement page: Revised 15/5/2017 1. Separation system consisting of an inflow channel, where a system for separation It is equipped with a vortex valve, managed to obtain and control the flux of the Fluid through the inlet channel And to form a vortex flow, with a vortex flow around the core, where the decoupling system is further integrated. The separation chamber is placed in The relative endpoint position with the vortex valve receives the vortex flow from the vortex valve, where for the separation it is assembled with the first and second outlet channels, where the outlet channels at One is positioned to accept the inner portion of the spiral flow. And the second outlet is positioned to accept the outer portion of the vortex flow, further integrating the fortress chamber positioned between the vortex valve and the separation chamber, to Receive a swirling flow from the swirling valve, the pan-out chamber in It is directed towards the destination side along the core to produce a flared vortex flow and to deliver a flared vortex flow into the separation chamber (formerly modified). Inflow (16), where the system for disassembly is combined With a rotating valve (100), it is managed to obtain and measure the flux of the fluid flow. Through the inrush channel (16) and to form a vortex flow, with a spiral flow around the core (11), where the separation system is further assembled. (40) which is positioned relative to the end of the vortex valve (100) to obtain the vortex flow from Spiral flute valve (100), where the separation chamber (40) is assembled with an outlet channel. The first and second (41,42), where the first (41) outflow channels are positioned to receive The inner portion of the vortex flow and the second (42) outlet channel are positioned to Receive the outer portion of the vortex flow 2. The separation system according to claim 1 is further incorporated by the fortress chamber (30) positioned between the vortex flap valve (100) and the chamber. For separation (40), to receive a vortex flow from the vortex valve (100), the fortress chamber (30) flared in the direction of At the destination side along the core (11) to produce a flared vortex flow and deliver a flared vortex flow into the separation chamber (40) 3. System for separation according to the hand held Any of the previous rights Continue to include The conical medial body (15), which was positioned in a significant co-axial position (11) in the vortex valve (100), with a gradual increase in the cross-sectional area. In the direction of 4. A system for separation according to claim 3 where the center cone (15) consists of a central outlet (17) through which the flow can be imported as a Center flow 5. A system for separating one of the previous claims. Where the spiral flaps (100) are the flanges that are assembled with the body (1), the torso (2), which are handled properly. Movable in the housing (1) to control the flux of the fluid flow passing through the fluid inlet (16) in such a way that the fluid flow is expanded and cooled. And the way Through the eddy current (3), which transmits the eddy current into the flow of Flow around the main flow axis 6. A system for separating one of the previous claims Where the first (41) outflow channel is centrally positioned within the second outflow channel (42) relative to the core (11). 7. System for separation of claims. One of the previous Where the system for separation It consists of injection material (60,70) comprising an injection outlet (61,71), positioned to inject fluid at the additional inlet into the cyclonic flow. For the separation according to claim 7, where the injection device (60) includes Injection tube (62), injection tube (62), consists of injection outlet port (61), administered injection outlet port (61) to inject fluid at additional inlet direction. that It consists of radial outward components and source-based components. The axial direction from the position where it meets the core (11) is significant 9. The separation system according to claim 7, where the injection device (70) is included. Circumference injection ring (72), injection outlet (71) managed to inject fluid for injection in a direction consisting of components that are inward along the line. Rasmee and axial source components 1 0. Systems for processing, for fluid processing, systems for processing. Carry out a composite process with at least one separation system (SS, SS1, SS2) in accordance with Any of the preceding claims 1 1. A system for executing claim 10, where a system for processing Is a system for processing gas and combining with - Managed pre-cooling (PU) unit to receive gas flow (701) and produce pre-cooled gas flow (702) - Managed First Separation (SS1) system It is intended to receive the pre-cooled gas flow (702) from the pre-cooling unit (PU) and to produce the first output flow (703) through the first outflow channel (41 ) And the second output flow (704) through the second (42) outflow channel - the first separator container (V1, HG) managed to get the second output flow (704 ) And to produce the flow at the top (705) and the bottom flow (706) - the second separation system (SS2) managed to receive the flow at the bottom (706) of the separator container. First (V1, HG) and to produce an additional first output flow (713) through the first (41) outflow channel and an additional output flow (714) through the second outflow channel. Additional (42) 1 2. System for processing under claim 11, where the system for processing Continue to include - Second separation vessel (V2) managed to obtain the additional output flow (714) of the separation system (SS2) 1 3. System for processing according to the previous claim. One of these Where the container The separator is a liquid-gas separator. (V1), any type of hydrate-gas separator (HG) 1 4. System for processing according to claim 10, where the system for processing A schematic diagram for oil processing, a system for a combined process - a system for separating (SS) managed to receive the high pressure oil flow (802) and to produce the output flow. The first (803) through the first (41) outflow channel and the second (804) outflow through the second (42) outflow channel - managed separation vessels (V3, V4). Set it to get one output flow (803) and one second output flow (804). And managed to produce the top-top flow (805, 815) and bottom flow (806,816) 1 5. System for processing claim 14 where the separation vessel (V3) at Hold it to get the second output flow (804) and the top (805) flow of the separation (V3) flow to be mixed with the first output flow. (803), Systems for Operations The assembly process is further combined with a gas compressor (COM) managed to get the first output flow (803) and the top flow (805) combined of the separation vessel ( V3) 1 6. System for the implementation of claim 14, where the separation vessel (V4) managed to receive the first output flow (803) and the bottom flow (816). ) Of the separation tube (V4) will be mixed with the second output flow. (804), Systems for Operations The assembly process is further included with the gas compressor (COM) managed to obtain the flow at the top (815) of the separation vessel (V4) 1 7.System for processing according to claim 15. To any one of the above 16 Where is the system for Further assembly operations include a preheating unit (PH) and a gas compressor (COM) managed to produce a compression flow (802), which is then introduced into the unit. For preheating (PH) for preheating of high pressure oil flow (802) 1 8. System for processing one of Claims 14 to 17 where the vessel for the process of heating is required. Separated (V3) manipulated to produce lateral flow (807), breech flow. Which is a liquid type Akias significantly And the flow on the hydrocarbon flank side Significantly 1 9. Methods for separating fluid flow, Method for assembly. - Receiving the fluid flow in the vortex valve (100), thus causing the The vortex flow, with the eddy current around the central axis (11) - the separation of the inner part of the vortex flow from the outer part from the vortex flow. The spiral chamber for the separation chamber (40), the separation chamber (40) consists of the first (41) outflow channel and the second (42) outflow channel, managed to receive the side part. In and outside, respectively 2. 0. Method under claim 19, where the assembly method is included. - The expansion and cooling of the spiral flow before separation, hence the formation A new cycle is formed at or at the end of the eddy current valve (100) by condensation 2. 1. Method for any of Clause 19 to 20. Where the assembly method continues to be included - The injection of fluid at the additional inlet into the vortex flow prior to separation 2. 2. Methods for fluid processing, assembly methods are also included. - Generation of output flow (703,713,803) through the first (41) flow channel and the second output flow. (704,714,804) through the second (42) outflow channel of the separation system (SS, SS1, SS2) in accordance with Clause 19 to 21, any of them 2. 3. Method according to claim 22, where method is a method for processing gas and Included - pre-cooling of the gas flow (701) to produce a processed gas flow Pre-cooling (702) in the pre-cooling unit (PU) - pre-cooled separation of gas flow (702) in the first separation system (SS1) to produce the output flow. The first (703) through the first (41) outflow channel and the second (704) through the second output flow (42) - the second flow output separation (704). ) In the first separator container (V1, HG) to produce topmost flow (705) and bottom flow (706) - bottom flow (706) in the separation system at Two (SS2) to produce flow One additional output (713) through an additional first outflow channel (41) and an additional first output flow (714) through an additional second outlet (42) 2 4. Method according to claim 23, where the method of assembly is also included. - Separation of the additional output flow (714) of the system for the second separation (SS2) in the secondary separation vessel (V2) 2. 5. Method according to claim 22 where method is method for liquid processing, compound method. - Separation of high pressure liquid flow (802) in the system for separation (SS) to produce the first (803) output flow through the first (41) outflow channel and the output flow. The second (804) through the second output flow (42) - the first output flow separation (803) and one second output flow (804) in the separation vessel ( V3, V4) to produce flow at the top (805,815) and flow on the bottom (806,816) 2. 6. Method according to claim 25, where the separation container (V3) may be handled to receive The second output flow (804) and the assembly method continue to combine. - Combination of the top flow (805) of the separation vessel (V3) with the first output flow (803) - compression, the first (803) output flow, and The flow at the top (805) that has been mixed. Combination of the separation vessel (V3) in the gas compressor (COM) 2. 7. Method according to claim 26, where the separation vessel (V4) managed to receive the flow. The first output (803) and the method may be assembled further. - Combination of the bottom flow (816) of the separation container (V4) with the second output flow (804) - Compression at the top (815) of the separation container. (V4) in a gas compressor (COM) 2 8. Procedures in accordance with Claim 26 through 27, any one Where the gas compressor (COM) managed To produce flow, compression (820) and assembly methods to continue as well. - Pre-heating of high pressure oil flow (802) in the unit for providing Pre-heating (PH) using compression flow (820)