A centrifuge separator for different specific gravity fluid separation. Gas enriched influent is then fed into a rotary impeller, where rotational energy of the impeller is transferred to the incoming fluid creating a forced vortex. Centripetal force exerted on the fluid particles help to separate t
A centrifuge separator for different specific gravity fluid separation. Gas enriched influent is then fed into a rotary impeller, where rotational energy of the impeller is transferred to the incoming fluid creating a forced vortex. Centripetal force exerted on the fluid particles help to separate the fluid/solids to rotate at different radius. Solids are moved towards a periphery of the tube where a cone collector facilitates to collect the solids. The conical shape allows the solids to slide into an annulus. The lighter specific gravity fluids are forced to segregate into two different rotating vortexes by virtue of the rotary motion of the impeller. The gas bubbles mixed with the influent help to accelerate the separation of two different specific gravity fluids.
대표청구항▼
1. A centrifuge separator, comprising: a main inlet pipe having an inlet opening for receiving an Untreated Fluid;an inline impeller assembly in fluid communication with the main inlet pipe,a first conical chamber positioned above said inline rotor assembly and in fluid communication with said inlin
1. A centrifuge separator, comprising: a main inlet pipe having an inlet opening for receiving an Untreated Fluid;an inline impeller assembly in fluid communication with the main inlet pipe,a first conical chamber positioned above said inline rotor assembly and in fluid communication with said inline impeller assembly, said first conical chamber having a first side outlet, said first conical chamber having a first outer annulus ring and a first ramp portion positioned below the first outer annulus ring, said first ramp portion extending outwards and upwards to expand the Untreated Fluid, said first side outlet in communication with an internal area of said first conical chamber through a first side opening extending through a portion of the first outer annulus ring;a pipe member in fluid communication with the first chamber, said pipe member disposed above said first chamber;a second conical chamber positioned at a top end of said pipe member and in fluid communication with said pipe member; said second conical chamber having a second side outlet, said second conical chamber having a second outer annulus ring and a second ramp portion positioned below the second outer annulus ring, said second ramp portion extending outwards and upwards to expand a remaining portion the Untreated Fluid, said second side outlet in communication with an internal area of said second conical chamber through a second side opening extending through a portion of the second outer annulus ring;a collection pipe at least substantially centrally located with respect to said second conical chamber and said pipe member, said collection pipe in fluid communication with said pipe member;a gas inlet member in communication with an internal area of the main inlet pipe; anda static mixer disposed with said main inlet pipe for mixing gas received through said gas inlet member with the Untreated Fluid, said gas inlet member in communication with the internal area of said main inlet pipe intermediate of said static mixer and said inlet opening of said main inlet pipe. 2. The centrifuge separator of claim 1 wherein a first inlet end of said collection pipe terminates within said second conical chamber below the second ramp portion. 3. The centrifuge separator of claim 1 wherein said inline impeller assembly comprising: an internally located impeller in fluid communication with a lower end of said first conical chamber;a drive shaft operatively associated with said impeller;a gear box operatively associated with said drive shaft; anda motor operatively associated with said gear box. 4. The centrifuge separator of claim 1 wherein operation of said inline impeller assembly causes the Untreated Fluid passing by said impeller to spin which in turn causes particles with a higher specific gravity from the Untreated Fluid to spin to an outside where the higher specific gravity particles are diverted by the first ramp portion for collection within the first outer annulus ring of the first conical chamber and radially exited out through said first side outlet. 5. The centrifuge separator of claim 4 wherein after passing through the first conical chamber, a remaining portion of the Untreated Fluid continues to spin through operation of said impeller assembly and travel upwards through said pipe member with higher specific gravity fluids of the remaining portion spinning to an outside position where the higher specific gravity particles of the remaining portion are diverted by the second ramp portion for collection within the first outer annulus ring of the second conical chamber and radially exited out through said second side outlet. 6. The centrifuge separator of claim 5 wherein lower specific gravity fluids of the remaining portion travel within the collection pipe by entering the collection pipe at its first inlet end and are exited out through a second end of the collection pipe. 7. The centrifuge separator of claim 1 a further comprising a supply of gas or gases injected into the internal area of the main inlet pipe through said gas inlet member; wherein the supply of gas or gases is selected from the following gases: oxygen, ozone, air, CO2, nitrogen or methane. 8. The centrifuge separator of claim 1 wherein said first annulus ring having a radius ranging from about 1″ to about 3″ and said second annulus ring having a radius ranging from about 3″ to about 24″. 9. The centrifuge separator of claim 1 further comprising a second pipe member having a first end and a second end, said first end of the second pipe member positioned adjacent to and above the inline impeller assembly and the second end of the second pipe member positioned adjacent to and below the first ramp portion of the first conical chamber, wherein the Untreated Fluid is spun by and above the inline impeller assembly prior to separation of solids contained in the Untreated Fluid within the first conical chamber. 10. The centrifuge separator of claim 1 wherein said first ramp portion being disposed at an angle ranging anywhere from about 30 degrees to about 80 degrees. 11. The centrifuge separator of claim 1 wherein said first conical chamber is spaced from said second conical chamber at a distance ranging from about 24″ to about 60″. 12. The centrifuge separator of claim 1 wherein said first outlet is positioned substantially perpendicular to the first annulus ring and said second outlet is positioned substantially perpendicular to the second annulus ring. 13. A substantially vertically oriented centrifuge separator for separating solids from liquids contained in an Untreated Fluid, comprising: a main inlet pipe having an inlet opening for receiving an Untreated Fluid;a gas inlet member in communication with an internal area of the main inlet pipe for injecting gas into the Untreated Fluid;a static mixer disposed with said main inlet pipe for mixing gas received through said gas inlet member with the Untreated Fluid in order to breakdown gas bubbles from the injected gas into smaller size bubbles, said gas inlet member in communication with the internal area of said main inlet pipe intermediate of said static mixer and said inlet opening of said main inlet pipe;a single inline impeller assembly in fluid communication with the main inlet pipe;a first conical chamber positioned above said inline impeller assembly and in fluid communication with said inline impeller assembly, said first conical chamber having a first outer annulus ring defining a first collection area for primarily collecting solids contained in the Untreated Fluid, a first ramp portion positioned below the first outer annulus ring, said first ramp portion extending outwards and upwards to expand the Untreated Fluid, and a first tangential side outlet in communication with the first collection area of said first conical chamber through a first side opening extending through a portion of the first outer annulus ring;a substantially vertically oriented pipe member in fluid communication with the first conical chamber;a second conical chamber positioned at a top end of said pipe member and in fluid communication with said pipe member; said second conical chamber having a second outer annulus ring defining a second collection area, a second ramp portion positioned below the second outer annulus ring, said second ramp portion extending outwards and upwards to expand a remaining portion of the Untreated Fluid, and a second tangential side outlet in communication with the second collection area of said second conical chamber through a second side opening extending through a portion of the second outer annulus ring; anda collection pipe at least substantially centrally located with respect to said second conical chamber and said pipe member, said collection pipe in fluid communication with said pipe member;wherein said single inline impeller assembly spinning the Untreated Fluid entering the first conical chamber and also spinning the remaining portion of the Untreated Fluid that exits out of the first conical chamber through the substantially vertically oriented pipe member. 14. The centrifuge separator of claim 13 wherein a first inlet end of said collection pipe terminates within said second conical chamber below the second ramp portion. 15. The centrifuge separator of claim 13 wherein said inline impeller assembly comprising: an internally located impeller in fluid communication with a lower end of said first conical chamber;a drive shaft operatively associated with said impeller;a gear box operatively associated with said drive shaft; anda motor operatively associated with said gear box. 16. The centrifuge separator of claim 13 wherein operation of said inline impeller assembly causes the Untreated Fluid passing by said impeller to spin which in turn causes particles with a higher specific gravity from the Untreated Fluid to spin to an outside position where the higher specific gravity particles are diverted by the first ramp portion for collection within the first collection area defined by the first annulus ring of the first conical chamber and radially exited out through said first side outlet; wherein after passing through the first chamber, a remaining portion of the Untreated Fluid continues to spin through operation of said impeller and travel upwards through said pipe member with higher specific gravity fluids of the remaining portion spinning to an outside position where the higher specific gravity particles of the remaining portion are diverted by the second ramp portion for collection within the second collection area defined by the second annulus ring of the second conical chamber and radially exited out through said second side outlet; wherein lower specific gravity fluids of the remaining portion travel within the collection pipe by entering the collection pipe at its first inlet end and are exited out through a second end of the collection pipe. 17. The centrifuge separator of claim 13 further comprising a supply of gas or gases injected into the internal area of the main inlet pipe through said gas inlet member; wherein the supply of gas or gases is selected from the following gases: oxygen, ozone, air, CO2, nitrogen or methane. 18. The centrifuge separator of claim 13 wherein said first ramp portion being disposed at angle ranging anywhere from about 30 degrees to about 80 degrees.
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이 특허에 인용된 특허 (6)
Gomez,Rodolfo Antonio M, Advanced liquid vortex separation system.
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