Fluid handling – Flow affected by fluid contact – energy field or coanda effect – Means to cause rotational flow of fluid
Reexamination Certificate
2000-10-11
2002-04-23
Chambers, A. Michael (Department: 3753)
Fluid handling
Flow affected by fluid contact, energy field or coanda effect
Means to cause rotational flow of fluid
C137S810000, C137S812000, C137S315110, C417S360000
Reexamination Certificate
active
06374858
ABSTRACT:
This invention relates to vortex valve flow controls.
A vortex valve flow control is a device for controlling fluid flow by a hydraulic effect without requiring moving parts. Such devices have a vortex chamber provided with an outlet at one axial end and an inlet arranged to cause swirl in the chamber when a certain critical flow has been attained. In use, the inlet communicates with a body of water which exerts a pressure head on the liquid entering the vortex chamber. Air is entrained in the liquid drawn through the valve so that, when vortex flow has been established, a central air core exists. U.S. Pat. No. 4,206,783 discloses a vortex valve having a conical vortex chamber with a tangential inlet and an outlet disposed at the narrower end of the chamber. Also known are short vortex valves of which the cross-sectional configuration of the vortex chamber is a logarithmic spiral extending the full length of its longitudinal axis to the outlet. At low flow rates, water entering through the inlet of a vortex valve passes through the vortex chamber to the outlet with substantially no pressure drop and the valve can be considered to be open. However, at high flow rates, water enters through the inlet with enough energy to create a vortex in the vortex chamber which results in a considerable pressure drop between the inlet and the outlet and may greatly restrict flow through the outlet, or even substantially cut it off altogether. Thus the valve serves to limit the rate of flow through it automatically. Vortex valves can be used, for example, to control the flow of storm water in sewers, to ensure that equipment downstream of the valve is not overloaded during periods of heavy rainfall.
The flow characteristics of a vortex valve flow control (once a vortex has been initiated in the vortex chamber thereof) are dependent on a number of factors including the area of the outlet (A) and the head (H) of fluid upstream of the device. A reasonable approximation of the relationship between the flow (Q) through a vortex valve flow control and the area of the outlet (A) and head (H) is given by the equation:
Q=C
d
·A{square root over (()}2gH)
where C
d
is a coefficient of discharge which is dependent upon the type of vortex valve under consideration, and g is the gravity constant.
Before initiation of the vortex, the rate of flow of fluid through the device is directly dependent upon the head (H) and the area (A) of the outlet. In the “pre-initiation” zone (i.e shortly before initiation), the flow actually decreases somewhat for a small increase in head, before increasing again at initiation at a slower rate than before. This gives rise to what is termed a “pre-initiation bulge” during which the characteristics of the vortex valve are such that it permits a higher rate of flow for a given pressure head than one would expect from a direct extrapolation back towards the origin of the curve at high heads after initiation. In some circumstances, it is desirable to reduce or even eliminate the pre-initiation bulge.
The configuration and dimensions of a vortex valve determine its flow characteristics, namely its coefficient of discharge (C
d
), the extent of pre-initiation bulge and the head required to initiate the vortex.
Until the present invention, it had been the experience that an increase in the dimensions of the outlet from the vortex chamber would cause a change in the coefficient of discharge; thus, in order to maintain a constant coefficient of discharge within a range of vortex valve flow controls having the same overall general configuration, but different outlet opening dimensions, it has previously been necessary to vary other dimensions of the device, including the dimensions of the inlet and the overall dimension (typically the dimension of the longitudinal axis and the diameter) of the vortex chamber itself. As a consequence, it has been necessary for suppliers of vortex valves to manufacture and keep stocks of a wide range of sizes of vortex valve.
The present invention is based on the finding that a vortex valve can be designed with a coefficient of discharge which remains constant over a wide range of outlet dimensions, the only requirement being a corresponding adjustment in the dimensions of the inlet opening. This makes it possible for a supplier of vortex valves to manufacture and stock a single vortex valve “precursor” from which a range of vortex valve flow controls with the same (or substantially the same) coefficient of discharge, but with different outlet opening dimensions, may be constructed. This requires the supplier only to form the appropriate outlet opening and inlet opening in the end wall and peripheral wall respectively of the vortex chamber to create a suitable vortex valve flow control to meet a customer's needs. There are considerable practical as well as economic advantages associated with the ability of a supplier to be able to meet its customers requirements in this way, not least the economic advantage of not having to “customise” each vortex valve to a customer's order.
According to a first aspect of the present invention, there is provided a vortex valve flow control comprising a housing defining a vortex chamber having an inlet for introducing a liquid into the vortex chamber in a manner to promote swirl and an outlet in one axial end of the vortex chamber, characterised in that:
the peripheral wall of the vortex chamber which is situated between the two end walls and surrounds the longitudinal axis of the vortex chamber has a cylindrical cross-section; and
the distance between the end walls (as measured at the axis of the flow control) of the vortex chamber is no larger than the diameter of the vortex chamber.
In a preferred embodiment of the vortex valve in accordance with this aspect of the invention, the inlet is an inlet means in the form of an inlet conduit or pipe which is open at both ends, the end thereof which intersects the peripheral wall of the vortex chamber constituting the inlet opening into the vortex chamber.
A further preferred feature is that the intersection or junction between each end wall of the vortex chamber and the cylindrical peripheral wall should take the form of a circumferentially extending concave portion (when viewed from inside the vortex chamber) having a radius of curvature which is typically less than 25% of the diameter of the vortex chamber.
The Peripheral Wall of the Vortex Chamber
The peripheral wall of the vortex chamber which is situated between the two end walls and surrounds the longitudinal axis of the vortex chamber has a cylindrical cross-section, that is to say it should have a constant cross-section along its length.
The peripheral wall of the vortex chamber is preferably of circular cylindrical form, although other cross-sectional forms, such as oblong or elliptical forms are also contemplated
The Inlet Means
The inlet means comprises a conduit or pipe which serves to direct liquid flow to the vortex chamber in a manner to promote swirl of the liquid in the vortex chamber when a predetermined pressure head is reached. The inlet conduit preferably has a circular cross section and is preferably arranged to direct liquid flow tangentially into the vortex chamber. As a consequence of its tangential abutment to the peripheral wall of the vortex chamber, the actual inlet opening in the peripheral wall of the vortex chamber is not circular, but rather has an elliptical form which corresponds to the shape of the end of the inlet conduit at its intersection with the peripheral wall. The length of the tubular conduit is not critical, but typically will be of the order of the inlet or outlet diameter.
The End Walls of the Vortex Chamber
As stated above, the distance between the end walls (as measured at the axis of the flow control) of the vortex chamber is no larger than the diameter of the vortex chamber. Preferably, this distance is no more than 60% of the diameter of the vortex chamber. The depth of the vortex chamber, i.e. its dimension measured along its axis, is thus relatively shor
Andoh Robert Yaw Gyamfi
Hides Stephen Peter
Chambers A. Michael
Hydro International PLC
Larson & Taylor PLC
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