Ejector
Abstract
An ejector ( 200; 300; 400; 600 ) has a primary inlet ( 40 ), a secondary inlet ( 42 ), and an outlet ( 44 ). A primary flowpath extends from the primary inlet to the outlet. A secondary flowpath extends from the secondary inlet to the outlet. A mixer convergent section ( 114 ) is downstream of the secondary inlet. A motive nozzle ( 100 ) surrounds the primary flowpath upstream of a junction with the secondary flowpath. The motive nozzle has an exit ( 110 ). A secondary inlet passageway along the secondary flowpath has a terminal portion oriented to discharge a secondary flow along the secondary flowpath at an angle of less than 75° off-parallel to a local direction of the primary flowpath.
Claims
exact text as granted — not AI-modified1 . An ejector ( 200 ; 300 ; 400 ; 600 ) comprising:
a primary inlet ( 40 ); a secondary inlet ( 42 ); an outlet ( 44 ); a primary flowpath from the primary inlet to the outlet; a secondary flowpath from the secondary inlet to the outlet; a mixer convergent section ( 114 ) downstream of the secondary inlet; and a motive nozzle ( 222 ) surrounding the primary flowpath upstream of a junction with the secondary flowpath and having an exit ( 110 );
wherein:
a secondary inlet passageway ( 218 ; 218 A, 218 B; 218 ′A, 218 ′B; 218 ″A, 218 ″B) has a terminal portion oriented to discharge a secondary flow along the secondary flowpath at an angle (θ) of 10-75° off-parallel to a local direction of the primary flowpath; and
a center of an outlet of the terminal portion is at a radius (R 1 ) from an axis ( 500 ) of the motive nozzle and axially recessed by a distance (L 1 ) relative to the exit ( 110 ) of the motive nozzle.
2 . The ejector ( 200 ; 300 ; 600 ) of claim 1 wherein:
the motive nozzle is mounted in a first bore; and
the secondary inlet passageway is at least partially defined by a fitting mounted in a second bore.
3 . The ejector ( 600 ) of claim 2 wherein:
the fitting protrudes into a chamber ( 232 ) surrounding the motive nozzle.
4 . The ejector of claim 2 wherein:
the second bore is 30-60° off perpendicular to the first bore.
5 . The ejector of claim 1 wherein:
L 1 is less than 40 mm and R 1 is less than 45 mm.
6 . The ejector of claim 1 wherein:
said angle is 35-55°.
7 . The ejector ( 300 ; 400 ; 600 ) of claim 1 wherein:
there are at least two said secondary inlet passageways ( 218 A, 218 B; 218 ′A, 218 ′B; 218 ″A, 218 ″B).
8 . The ejector of claim 1 further comprising:
a needle ( 132 ) mounted for reciprocal movement along the primary flowpath between a first position and a second position; and
a needle actuator ( 134 ) coupled to the needle to drive said movement of the needle relative to the motive nozzle.
9 . The ejector of claim 1 wherein:
an outer member comprises an end-to-end axial assembly of a plurality of sections.
10 . The ejector of claim 9 wherein the sections include:
an upstream section ( 202 ) at least partially surrounding the motive nozzle;
one or more intermediate sections ( 204 ) at least partially defining a convergent portion ( 214 ) and a mixing portion ( 216 ); and
at least one downstream section ( 206 ) at least partially defining a divergent portion ( 118 ).
11 . The ejector of claim 10 wherein:
an interface of at least two of said sections ( 204 , 206 ) comprises a boss of one section protruding into a compartment in the other section.
12 . A vapor compression system comprising:
a compressor ( 22 ); a heat rejection heat exchanger ( 30 ) coupled to the compressor to receive refrigerant compressed by the compressor; the ejector ( 200 ; 300 ; 400 ; 600 ) of claim 1 ; a heat absorption heat exchanger ( 64 ); and a separator ( 48 ) having:
an inlet ( 50 ) coupled to the outlet of the ejector to receive refrigerant from the ejector;
a gas outlet ( 54 ); and
a liquid outlet ( 52 ).
13 . A method for operating the system of claim 12 comprising:
compressing the refrigerant in the compressor;
rejecting heat from the compressed refrigerant in the heat rejection heat exchanger;
passing a flow of the refrigerant through the primary ejector inlet; and
passing a secondary flow of the refrigerant through the secondary inlet to merge with the primary flow.
14 . The method of claim 13 wherein:
the refrigerant comprises at least 50% CO 2 by weight.
15 . An ejector comprising:
a primary inlet ( 40 ); a secondary inlet ( 42 ); an outlet ( 44 ); a primary flowpath from the primary inlet to the outlet; a secondary flowpath from the secondary inlet to the outlet; a convergent section ( 114 ) downstream of the secondary inlet; a motive nozzle ( 222 ) surrounding the primary flowpath upstream of a junction with the secondary flowpath and having:
a throat ( 106 ); and
an exit ( 110 ); and
means for efficiently promoting mixing of the secondary flow into the primary flow.
16 . The ejector of claim 15 wherein:
the means comprises an off-radially directed terminal portion of of a secondary passageway from the secondary inlet.
17 . The ejector of claim 15 wherein:
a center of an outlet of the terminal portion is at a radius (R 1 ) from an axis ( 500 ) of the motive nozzle and axially recessed by a distance (L 1 ) relative to the exit ( 110 ) of the motive nozzle.
18 . The ejector of claim 17 wherein:
L 1 is at least 5 mm.
19 . The ejector of claim 1 wherein:
an axis of an outlet of the terminal portion intersects an axis of the motive nozzle at a location upstream of the exit of the motive nozzle.
20 . The ejector of claim 1 wherein:
L 1 is at least 5 mm.Cited by (0)
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