Aspirator pump and metering device

Claim 2

Fluid flow control apparatus comprising: an aspirator including a liquid orifice and a venturi for pumping at a low flow rate such that the Reynolds number is less than 30,000 and mixing a liquid into a diluent gas to form a vapor mixture having a substantially constant volume fraction independent of flow rates; and means for metering the flow rate of said vapor mixture; wherein said aspirator comprises said venturi and said liquid orifice having a configuration such that its venturi discharge coefficient C DV and its liquid orifice discharge coefficient C D2 forms a ratio C DV /C D2 substantially linear over flow rates below the said Reynolds number of 30,000 above which the discharge coefficients become invariant.

Claim 3

The apparatus of claim 1 wherein said aspirator comprises means for equilibrating a static pressure at said liquid orifice in relation to a pressure change imposed by said means for metering and further comprising means for controllably adjusting the flow of said liquid into said venturi.

Claim 4

The apparatus of claim 2 wherein said liquid orifice comprises a metering orifice for adjusting flow rate.

Claim 5

The apparatus of claim 2 wherein said liquid comprises SiCl 4 or TiCl 4 and said diluent gas comprises an inert gas.

Claim 6

The apparatus of claim 4 wherein said specified venturi proportions include an entrance cone angle of about 15°±3°.

Claim 7

The apparatus of claim 5 wherein said specified venturi proportions include entrance orifice area of about 0.009 in. 2 .

Claim 8

A fluid control device for controlling flow of a corrosive, volatile liquid comprising: a flow casing; a venturi insert within said flow casing, said insert selected to have specified proportions including a discharge coefficient; a liquid orifice of specified discharge, coefficient; and means for passing at a low rate of flow such that the Reynolds number is less than 30,000 said liquid by venturi suction through said liquid orifice of specified discharge coefficient and into the venturi at a position at or near the vena contracta of said venturi; wherein, C VD =the discharge coefficient for the venturi; C D2 =the discharge coefficient for the liquid orifice; and C DV /C D2 forms a substantially linear proportionality over flow rates below the said Reynolds number of 30,000 above which the discharge coefficients become invariant.

Claim 9

A fluid control device for controlling flow of a corrosive, volatile liquid comprising: a flow casing; a venturi insert within said flow casing, said insert selected to have specified proportions including a discharge coefficient; a liquid orifice of specified discharge, coefficient; and means for passing at a low rate of flow such that the Reynolds number is less than 30,000 said liquid by venturi suction through said liquid orifice of specified discharge coefficient and into the venturi at a position at or near the vena contracta of said venturi; wherein, C VD =the discharge coefficient for the venturi; C D2 =the discharge coefficient for the liquid orifice; and C DV /C D2 forms a substantially linear proportionality over flow rates below the said Reynolds number of 30,000 above which the discharge coefficients become invariant.

Claim 10

A device as set forth in claim 7 wherein said means for passing further comprises a liquid reservoir communicating with said liquid orifice and means for equalizing pressure between said reservoir and a position downstream from the vena contracta of the venturi.

Claim 11

A flow control device as set forth in claim 8 wherein said means for equalizing pressure comprises a pressure balance line communicating with said reservoir and a position downstream from the vena contracta.

Claim 12

A flow control device as set forth in claim 9 further comprising means for metering fluid flow at a position downstream from the venturi.

Claim 13

A flow control device as set forth in claim 10 wherein said metering means is adapted to controllably adjust said liquid orifice.

Claim 14

A flow control device as set forth in claim 11 wherein said entrance cone angle comprises 15°±3°.

Claim 15

In an aspirator for pumping a primary fluid employing the momentum of a secondary fluid, the improvement for measuring flow rates of said primary fluid by controllably mixing said primary and secondary fluids and metering the mixture to form a metered mixture of predetermined composition independent of flow rates, comprising: a venturi; means for passing said secondary fluid through said venturi having a discharge coefficient C DV ; a primary fluid orifice; means for pumping said primary fluid at a low flow rate such that the Reynolds number is less than 30,000 through suction by said venturi to pass through said primary fluid orifice having discharge coefficient C D2 ; wherein, C DV =the discharge coefficient for the venturi; C D2 =the discharge coefficient for the primary fluid orifice; and C DV /C D2 forms a substantially linear proportionality over flow rates below the said Reynolds number of 30,000 above which the discharge coefficients become invariant; and means for mixing and measuring said primary and secondary fluids.

Claim 16

In an aspirator for pumping a primary fluid employing the momentum of a secondary fluid, the improvement for measuring flow rates of said primary fluid by controllably mixing said primary and secondary fluids and metering the mixture to form a metered mixture of predetermined composition independent of flow rates, comprising: a venturi; means for passing said secondary fluid through said venturi having a discharge coefficient C DV ; a primary fluid orifice; means for pumping said primary fluid at a low flow rate such that the Reynolds number is less than 30,000 through suction by said venturi to pass through said primary fluid orifice having discharge coefficient C D2 ; wherein, C DV =the discharge coefficient for the venturi; C D2 =the discharge coefficient for the primary fluid orifice; and C DV /C D2 forms a substantially linear proportionality over flow rates below the said Reynolds number of 30,000 above which the discharge coefficients become invariant; and means for mixing and measuring said primary and secondary fluids.

Claim 17

An aspirator as set forth in claim 13 wherein said primary fluid orifice comprises a metering orifice for adjusting flow rate.

Claim 18

An aspirator as set forth in claim 14 wherein said secondary fluid comprises a gas and said primary fluid comprises a liquid.

Claim 19

An aspirator as set forth in claim 10 wherein said gas comprises an inert gas and said liquid comprises SiCl 4 or TiCl 4 .

Claim 20

An aspirator as set forth in claim 16 wherein said specified venturi proportions include an entrance cone angle of about 15°±3°.

Claim 21

An aspirator as set forth in claim 17 wherein said specified venturi proportions include entrance orifice area of about 0.009 in. 2 .