Inertial gas-liquid separator with variable flow actuator

Claim 2

An inertial gas-liquid separator for removing liquid particles from a gas-liquid stream, comprising a housing having an inlet for receiving a gas-liquid stream, and an outlet for discharging a gas stream, nozzle structure in said housing having a plurality of nozzles receiving said gas-liquid stream from said inlet and accelerating said gas-liquid stream through said nozzles, an inertial impactor collector in said housing in the path of said accelerated gas-liquid stream and causing liquid particle separation from said gas-liquid stream, a variable flow actuator movable to vary flow through at least one of said nozzles, wherein said inertial impactor collector is downstream of and spaced from said variable flow actuator.

Claim 3

The inertial gas-liquid separator according to claim 1 wherein said variable flow actuator is responsive to pressure of said gas-liquid stream.

Claim 4

The inertial gas-liquid separator according to claim 2 wherein said variable flow actuator responds to increasing said pressure by moving to increase flow, and responds to decreasing said pressure to decrease flow, such that a substantially constant pressure drop is maintained across said inertial gas-liquid separator between said inlet and said outlet notwithstanding changing flow conditions of said gas-liquid stream therethrough.

Claim 5

The inertial gas-liquid separator according to claim 1 wherein the distance between said nozzles and said inertial impactor collector is constant and unchanged by movement of said variable flow actuator.

Claim 6

The inertial gas-liquid separator according to claim 1 , wherein said variable flow actuator comprises a piston axially slidable along a cylinder extending along an axis, said cylinder having a cylinder wall with a plurality of apertures therethrough providing said plurality of nozzles, said apertures being covered and uncovered by said piston during sliding of said piston along said cylinder to respectively close and open said nozzles.

Claim 7

The inertial gas-liquid separator according to claim 5 wherein: said inertial impactor collector is spaced radially outward of said cylinder by an annular acceleration gap therebetween; said apertures extend radially through said cylinder wall; said gas-liquid stream flows axially within said cylinder and then radially outwardly through said apertures uncovered by said piston and is accelerated into said annular acceleration gap and impacts said inertial impactor collector causing liquid particle separation from said gas-liquid stream.

Claim 8

The inertial gas-liquid separator according to claim 6 wherein: said gas-liquid stream flows in a given axial direction within said cylinder; and after said separation said gas stream flows in the same said given axial direction along the exterior of said cylinder.

Claim 9

The inertial gas-liquid separator according to claim 7 wherein: said gas-liquid stream flows through said inlet in said given axial direction; and said gas stream flows through said outlet in said given axial direction.

Claim 10

The inertial gas-liquid separator according to claim 5 wherein said piston has a leading surface facing the incoming flow of said gas-liquid stream thereagainst, said leading surface being configured to directionally guide and direct flow to said apertures in said cylinder wall.

Claim 11

The inertial gas-liquid separator according to claim 5 wherein said piston is a gravimetric piston relying on the weight of said piston to regulate flow, said axis being vertical, said piston having a bottom face facing downwardly and receiving the incoming flow of said gas-liquid stream thereagainst, said piston sliding upwardly in said cylinder in response to increasing pressure of said gas-liquid stream to open up more of said apertures, said piston sliding downwardly in said cylinder in response to decreasing pressure of said gas-liquid stream to close off more of said apertures.

Claim 12

The inertial gas-liquid separator according to claim 5 comprising a biasing member biasing said piston against the incoming flow of said gas-liquid stream thereagainst, said piston sliding in a first axial direction against the bias of said biasing member in response to increasing pressure of said gas-liquid stream to open up more of said apertures, said piston sliding in a second opposite axial direction as biased by said biasing member in response to decreasing pressure of said gas-liquid stream to close off more of said apertures.

Claim 13

The inertial gas-liquid separator according to claim 1 wherein said housing has a wall facing said inertial impactor collector and separated therefrom by an acceleration gap therebetween, said wall having a plurality of apertures therethrough providing said nozzles, and said variable flow actuator comprises a rolling diaphragm having a resilient flexible region covering and uncovering said apertures in a flexing motion to respectively close and open said nozzles.

Claim 14

The inertial gas-liquid separator according to claim 12 wherein said diaphragm has a first side communicating with said inlet and exposed to the incoming flow of said gas-liquid stream, and said diaphragm has a second opposite side communicating with said outlet, said first side of said diaphragm having a changing effective area, said effective area being defined as the area exposed to said incoming flow.

Claim 15

The inertial gas-liquid separator according to claim 13 wherein: said effective area of said diaphragm increases in response to increasing pressure of said gas-liquid stream, and said diaphragm uncovers and opens up more of said apertures; said effective area of said diaphragm decreases in response to decreasing pressure of said gas-liquid stream, and said diaphragm covers and closes off more of said apertures.

Claim 16

The inertial gas-liquid separator according to claim 14 wherein said wall is a cylinder wall of a cylinder in said housing and extending axially along an axis, said apertures extend radially through said cylinder wall, said diaphragm has an outer portion extending axially along the interior of said cylinder wall and flexible radially away therefrom to uncover and open up more of said apertures.

Claim 17

The inertial gas-liquid separator according to claim 15 wherein said diaphragm has a central portion spanning radially inwardly from said outer portion and movable in a first axial direction to flex said outer portion of said diaphragm radially inwardly away from said apertures and out of engagement with said cylinder wall to uncover and open up more of said apertures, said central portion being movable in a second opposite axial direction to flex said outer portion of said diaphragm radially outwardly toward said apertures and into engagement with said cylinder wall to cover and close off more of said apertures.

Claim 18

The inertial gas-liquid separator according to claim 16 comprising a biasing member biasing said central portion of said diaphragm in said second axial direction and against the incoming flow of said gas-liquid stream.

Claim 19

The inertial gas-liquid separator according to claim 14 wherein said wall comprises a plate having an incoming flow opening therethrough communicating with said inlet and receiving the incoming flow of said gas-liquid stream, said incoming flow flowing axially through said opening, said plate extending laterally outwardly from said opening, said plurality of apertures extending axially through said plate and being laterally outward of said opening, said diaphragm having an outer portion extending laterally along said plate and flexible axially away therefrom to uncover and open up more of said apertures.

Claim 20

The inertial gas-liquid separator according to claim 18 wherein said diaphragm has a central portion spanning laterally inwardly from said outer portion and movable in a first axial direction to flex said outer portion of said diaphragm axially away from said apertures and out of engagement with said plate to uncover and open up more of said apertures, said central portion being movable in a second opposite axial direction to flex said outer portion of said diaphragm axially toward said apertures and into engagement with said plate to cover and close off more of said apertures.

Claim 21

The inertial gas-liquid separator according to claim 19 comprising a biasing member biasing said central portion of said diaphragm in said second opposite axial direction and against the incoming flow of said gas-liquid stream.

Claim 22

The inertial gas-liquid separator according to claim 19 wherein said gas-liquid stream flows through said opening in said first axial direction and flows through said apertures in said second opposite axial direction, and wherein said gas stream flows from said acceleration gap to said outlet in said first axial direction.

Claim 23

An inertial gas-liquid impactor separator for removing liquid particles from a gas-liquid stream, comprising a housing having an inlet for receiving a gas-liquid stream, and an outlet for discharging a gas stream, nozzle structure in said housing having one or more nozzles receiving said gas-liquid stream from said inlet and accelerating said gas-liquid stream therethrough, said one or more nozzles providing a cumulative flow therethrough, an inertial impactor collector in said housing in the path of said accelerated gas-liquid stream and causing liquid particle separation from said gas-liquid stream, said path of said accelerated gas-liquid stream extending along a given acceleration direction, a variable flow actuator varying said cumulative flow through said one or more nozzles, said actuator being movable along a given actuation direction transverse to said given acceleration direction, wherein: said gas-liquid stream has an incoming flow direction directed against and striking said actuator; said incoming flow direction is parallel to said given actuation direction; and said actuator is upstream of and spaced from said inertial impactor collector.

Claim 24

An inertial gas-liquid impactor separator for removing liquid particles from a gas-liquid stream, comprising a housing having an inlet for receiving a gas-liquid stream, and an outlet for discharging a gas stream, nozzle structure in said housing having one or more nozzles receiving said gas-liquid stream from said inlet and accelerating said gas-liquid stream therethrough, said one or more nozzles providing a cumulative flow therethrough, an inertial impactor collector in said housing in the path of said accelerated gas-liquid stream and causing liquid particle separation from said gas-liquid stream, said path of said accelerated gas-liquid stream extending along a given acceleration direction, a variable flow actuator varying said cumulative flow through said one or more nozzles, said actuator being movable along a given actuation direction transverse to said given acceleration direction, wherein: said gas-liquid stream has an incoming flow direction directed against and striking said actuator; said incoming flow direction is parallel to said given actuation direction; and said actuator is upstream of and spaced from said inertial impactor collector.

Claim 25

The inertial gas-liquid impactor separator according to claim 22 wherein said gas-liquid stream flows along said given acceleration direction in said housing through said one or more nozzles and then is separated at an impaction turn at said inertial impactor collector, at least one of said gas and said liquid particles flowing along a post-impaction direction which is the same as said actuation direction.

Claim 26

The inertial gas-liquid impactor separator according to claim 23 wherein said actuator is movable along first and second opposite actuation directions, said first actuation direction of said actuator increasing said cumulative flow through said one or more nozzles, said second actuation direction of said actuator decreasing said cumulative flow through said one or more nozzles, said post-impaction direction being said second actuation direction.

Claim 27

The inertial gas-liquid impactor separator according to claim 24 wherein said housing has a drain port draining said liquid particles, and a post-impaction downstream turn between said inertial impactor collector and said drain port, at least one of said gas and said liquid particles turning at said downstream turn, said drain port being gravitationally below said downstream turn and said actuator, said outlet being gravitationally above said downstream turn.

Claim 28

The inertial gas-liquid impactor separator according to claim 25 wherein said outlet is gravitationally above said actuator.

Claim 29

The inertial gas-liquid impactor separator according to claim 25 wherein each of said gas and said liquid particles turns at said downstream turn.

Claim 30

The inertial gas-liquid impactor separator according to claim 22 wherein said gas-liquid stream flows along a first direction in said housing and then turns and flows along a second direction in said housing through said one or more nozzles, said second direction being said acceleration direction, said first direction being said actuation direction.

Claim 31

The inertial gas-liquid impactor separator according to claim 22 wherein said housing defines first, second, and third flow path segments serially coupled through first and second turns, one of said segments being an acceleration segment through said one or more nozzles, one of said turns being at said inertial impactor collector.

Claim 32

The inertial gas-liquid impactor separator according to claim 29 wherein said first, second, and third flow path segments are serially coupled upstream to downstream in said housing such that flow traverses said first flow path segment and then turns at said first turn and traverses said second flow path segment and then turns at said second turn and traverses said third flow path segment, said actuator being upstream of said third flow path segment and upstream of said second turn.

Claim 33

The inertial gas-liquid impactor separator according to claim 30 wherein said actuator is located along said first flow path segment.

Claim 34

The inertial gas-liquid impactor separator according to claim 31 wherein said variable actuator is upstream of said first turn.

Claim 35

The inertial gas-liquid impactor separator according to claim 32 wherein said first turn is at said inertial impactor collector.

Claim 36

The inertial gas-liquid impactor separator according to claim 30 wherein said first turn is at said actuator.

Claim 37

The inertial gas-liquid impactor separator according to claim 34 wherein said second turn is at said inertial impactor collector, and said actuator is upstream of said second turn.

Claim 38

The inertial gas-liquid impactor separator according to claim 31 wherein said actuator is located along said first and second flow path segments at the junction thereof at said first turn.

Claim 39

The inertial gas-liquid impactor separator according to claim 30 wherein said actuator varies said cumulative flow by varying the cross-sectional area of one of said flow paths.

Claim 40

The inertial gas-liquid impactor separator according to claim 37 wherein said first flow path segment is said acceleration segment, and said actuator varies said cumulative flow by varying the cross-sectional area of said first flow path segment.

Claim 41

The inertial gas-liquid impactor separator according to claim 37 wherein said second flow path segment is said acceleration segment, and said actuator varies said cumulative flow by varying the cross-sectional area of said second flow path segment.

Claim 42

An inertial gas-liquid impactor separator for removing liquid particles from a gas-liquid stream, comprising a housing having an inlet for receiving a gas-liquid stream, and an outlet for discharging a gas stream, nozzle structure in said housing having one or more nozzles receiving said gas-liquid stream from said inlet and accelerating said gas-liquid stream therethrough, said one or more nozzles providing a cumulative flow therethrough, an inertial impactor collector in said housing in the path of said accelerated gas-liquid stream and causing liquid particle separation from said gas-liquid stream, said path of said accelerated gas-liquid stream extending along a given acceleration direction, a variable flow actuator varying said cumulative flow through said one or more nozzles, said actuator being movable along a given actuation direction, said housing defining first, second and third flow path segments serially coupled though first and second turns, one of said segments being an acceleration segment through said one or more nozzles, one of said turns being at said inertial impactor collector, said housing comprising a first annular wall surrounded by a second annular wall, said second annular wall being spaced from said first annular wall by an annular gap, said first annular wall having a hollow interior defining a first plenum, said annular gap defining a second plenum, said first flow path segment traversing along said first plenum, said second flow path segment traversing across said first annular wall between said first and second plenums, said third flow path segment traversing along said second plenum, said actuator variably constricting and expanding said second flow path segment during traversal of said second flow path segment from said first plenum to said second plenum, wherein: said inertial impactor collector is downstream of and spaced from said actuator by an annular acceleration gap therebetween; said inertial impactor collector concentrically surrounds said acceleration gap; and said acceleration gap concentrically surrounds said actuator.

Claim 43

An inertial gas-liquid impactor separator for removing liquid particles from a gas-liquid stream, comprising a housing having an inlet for receiving a gas-liquid stream, and an outlet for discharging a gas stream, nozzle structure in said housing having one or more nozzles receiving said gas-liquid stream from said inlet and accelerating said gas-liquid stream therethrough, said one or more nozzles providing a cumulative flow therethrough, an inertial impactor collector in said housing in the path of said accelerated gas-liquid stream and causing liquid particle separation from said gas-liquid stream, said path of said accelerated gas-liquid stream extending along a given acceleration direction, a variable flow actuator varying said cumulative flow through said one or more nozzles, said actuator being movable along a given actuation direction, said housing defining first, second and third flow path segments serially coupled though first and second turns, one of said segments being an acceleration segment through said one or more nozzles, one of said turns being at said inertial impactor collector, said housing comprising a first annular wall surrounded by a second annular wall, said second annular wall being spaced from said first annular wall by an annular gap, said first annular wall having a hollow interior defining a first plenum, said annular gap defining a second plenum, said first flow path segment traversing along said first plenum, said second flow path segment traversing across said first annular wall between said first and second plenums, said third flow path segment traversing along said second plenum, said actuator variably constricting and expanding said second flow path segment during traversal of said second flow path segment from said first plenum to said second plenum, wherein: said inertial impactor collector is downstream of and spaced from said actuator by an annular acceleration gap therebetween; said inertial impactor collector concentrically surrounds said acceleration gap; and said acceleration gap concentrically surrounds said actuator.

Claim 44

The inertial gas-liquid impactor separator according to claim 40 wherein said second flow path segment is said acceleration segment, and said first annular wall comprises an acceleration portion spaced from said actuator by an acceleration gap which varies during movement of said variable actuator, said one or more nozzles comprising said acceleration portion providing said acceleration gap.

Claim 45

The inertial gas-liquid impactor separator according to claim 41 wherein said acceleration portion comprises one or more orifices through said first annular wall.

Claim 46

The inertial gas-liquid impactor separator according to claim 41 wherein said actuation direction is transverse to said acceleration direction.

Claim 47

An inertial gas-liquid impactor separator for removing liquid particles from a gas-liquid stream, comprising a housing having an inlet for receiving a gas-liquid stream, and an outlet for discharging a gas stream, nozzle structure in said housing comprising a first set of one or more nozzles receiving said gas-liquid stream from said inlet and accelerating said gas-liquid stream therethrough, and a second set of one or more nozzles receiving said gas-liquid stream from said inlet and accelerating said gas-liquid stream therethrough, said first set of one or more nozzles providing a first cumulative flow therethrough, said second set of one or more nozzles providing a second cumulative flow therethrough, one or more inertial impactor collectors in said housing in the respective paths of said accelerated gas-liquid streams and causing liquid particle separation from said gas-liquid streams, said paths of said accelerated gas-liquid streams extending along given respective acceleration directions, a variable flow actuator movable along a given actuation direction and varying at least one of said first and second cumulative flows through the respective set of one or more nozzles, wherein: said gas-liquid stream has an incoming flow direction directed against and striking said actuator; said incoming flow direction is parallel to said given actuation direction; said actuator is upstream of and spaced from said inertial impactor collector; said inertial impactor collector is downstream of and spaced from said actuator by an annular acceleration gap therebetween; said inertial impactor collector concentrically surrounds said acceleration gap; and said acceleration gap concentrically surrounds said actuator.

Claim 48

An inertial gas-liquid impactor separator for removing liquid particles from a gas-liquid stream, comprising a housing having an inlet for receiving a gas-liquid stream, and an outlet for discharging a gas stream, nozzle structure in said housing comprising a first set of one or more nozzles receiving said gas-liquid stream from said inlet and accelerating said gas-liquid stream therethrough, and a second set of one or more nozzles receiving said gas-liquid stream from said inlet and accelerating said gas-liquid stream therethrough, said first set of one or more nozzles providing a first cumulative flow therethrough, said second set of one or more nozzles providing a second cumulative flow therethrough, one or more inertial impactor collectors in said housing in the respective paths of said accelerated gas-liquid streams and causing liquid particle separation from said gas-liquid streams, said paths of said accelerated gas-liquid streams extending along given respective acceleration directions, a variable flow actuator movable along a given actuation direction and varying at least one of said first and second cumulative flows through the respective set of one or more nozzles, wherein: said gas-liquid stream has an incoming flow direction directed against and striking said actuator; said incoming flow direction is parallel to said given actuation direction; said actuator is upstream of and spaced from said inertial impactor collector; said inertial impactor collector is downstream of and spaced from said actuator by an annular acceleration gap therebetween; said inertial impactor collector concentrically surrounds said acceleration gap; and said acceleration gap concentrically surrounds said actuator.

Claim 49

The inertial gas-liquid impactor separator according to claim 44 wherein said actuation direction is transverse to said acceleration direction.

Claim 50

The inertial gas-liquid impactor separator according to claim 45 wherein movement of said actuator along said actuation direction varies only said second cumulative flow through said second set of one or more nozzles.