Cyclone separator

Claim 2

A cyclone separator for separating oil and water liquid components in a mixture thereof and having an elongate separating chamber in the form of a surface of revolution which over at least a substantial portion thereof exhibits a variation in taper, from a location towards one larger diameter end of the separating chamber to a location towards another smaller diameter end thereof, with the variation in taper thereof varying from a relatively greater angle at locations towards said one end of the separating chamber to a relatively lesser angle at locations towards said another end, the separating chamber being provided with inlet means in the form of at least one inlet disposed at or adjacent said one end of the separating chamber and arranged for inflow of the liquid to the separated into the separating chamber with a tangential component of motion, the separator having an axial overflow outlet at said one end thereof and an axial underflow outlet at said other end, said portion having a taper such that, when viewed in axial section, tangents thereto at substantially all locations along the length thereof make a taper angle in the range 11/2° to 3° to the axis of the separating chamber, and wherein the following relationships also apply: where d 1 is the diameter of the said separating chamber where flow enters, preferably in an inlet portion at said one end of said separating chamber, (but neglecting any feed channel) d ix is twice the radius at which flow enters the cyclone through the x th inlet (i.e., twice the minimum distance of the tangential component of the inlet center line from the axis) and ##EQU11## where A ix is the projection of the cross sectional area of x th inlet measured at entry to the cyclone separator in a plane parallel to the axis of the cyclone separator which is normal to the plane, also parallel to the cyclone axis which contains the tangential component of the inlet center line, and where: ##EQU12##

Claim 3

A cyclone separator for separating oil and water liquid components in a mixture thereof and having an elongate separating chamber in the form of a surface of revolution which over at least a substantial portion thereof exhibits a variation in taper, from a location towards one larger diameter end of the separating chamber to a location towards another smaller diameter end thereof, with the variation in taper thereof varying from a relatively greater angle at locations towards said one end of the separating chamber to a relatively lesser angle at locations towards said another end, the separating chamber being provided with inlet means in the form of at least one inlet disposed at or adjacent said one end of the separating chamber and arranged for inflow of the liquid to the separated into the separating chamber with a tangential component of motion, the separator having an axial overflow outlet at said one end thereof and an axial underflow outlet at said other end, said portion having a taper such that, when viewed in axial section, tangents thereto at substantially all locations along the length thereof make a taper angle in the range 11/2° to 3° to the axis of the separating chamber, and wherein the following relationships also apply: where d 1 is the diameter of the said separating chamber where flow enters, preferably in an inlet portion at said one end of said separating chamber, (but neglecting any feed channel) d ix is twice the radius at which flow enters the cyclone through the x th inlet (i.e., twice the minimum distance of the tangential component of the inlet center line from the axis) and ##EQU13## where A ix is the projection of the cross sectional area of x th inlet measured at entry to the cyclone separator in a plane parallel to the axis of the cyclone separator which is normal to the plane, also parallel to the cyclone axis which contains the tangential component of the inlet center line, and where: ##EQU14## and d 2 is the diameter of the separating chamber at the location where said portion begins.

Claim 4

A cyclone separator for separating oil and water liquid components in a mixture thereof and having an elongate separating chamber in the form of a surface of revolution which over at least a substantial portion thereof exhibits a variation in taper, from a location towards one larger diameter end of the separating chamber to a location towards another smaller diameter end thereof, with the variation in taper thereof varying from a relatively greater angle at locations towards said one end of the separating chamber to a relatively lesser angle at locations towards said another end, the separating chamber being provided with inlet means in the form of at least one inlet disposed at or adjacent said one end of the separating chamber and arranged for inflow of the liquid to the separated into the separating chamber with a tangential component of motion, the separator having an axial overflow outlet at said one end thereof and an axial underflow outlet at said other end, said portion having a taper such that, when viewed in axial section, tangents thereto at substantially all locations along the length thereof make a taper angle in the range 11/2° to 3° to the axis of the separating chamber, and wherein the following relationships also apply: where d 1 is the diameter of the said separating chamber where flow enters, preferably in an inlet portion at said one end of said separating chamber, (but neglecting any feed channel) d ix is twice the radius at which flow enters the cyclone through the x th inlet (i.e., twice the minimum distance of the tangential component of the inlet center line from the axis) and ##EQU13## where A ix is the projection of the cross sectional area of x th inlet measured at entry to the cyclone separator in a plane parallel to the axis of the cyclone separator which is normal to the plane, also parallel to the cyclone axis which contains the tangential component of the inlet center line, and where: ##EQU14## and d 2 is the diameter of the separating chamber at the location where said portion begins.

Claim 5

A cyclone separator as claimed in claim 2 wherein the separating chamber except, possibly for a part adjacent said one end which has substantially zero taper, has a part over which the taper angle varies from a value greater than 3° to a value equal to or less than 3°, d 2 is the diameter of the separating chamber measured at the point z 2 where the condition first applies that ##EQU15## for all z>z 2 where z is the distance along the cyclone separator axis downstream of the plane containing the inlet is located (or considered to be located if there is more than one inlet) and d is the diameter of the cyclone at z.

Claim 6

A cyclone separator as claimed in claim 3 wherein there are `x` inlets and the point z=0 is the axial position of the weighted areas of the inlets such that the injection of angular momentum into the cyclone separator is equally distributed axially about said axial position where z=0 and being defined by: ##EQU16## where z x is the axial position of the x th inlet.

Claim 7

A cyclone separator as claimed in any one of claims 1 and 2 wherein the tapered portion extends over substantially the whole length of the separating chamber.

Claim 8

A cyclone separator as claimed in any one of claims 1 and 2 wherein the overall length of the separator is in the range 10 to 40 times the diameter of the separating chamber at said one end.

Claim 9

A cyclone separator as claimed in claim 6 wherein the overall length of the separator is in the range 10 to 20 times the diameter of the separating chamber at said one end.

Claim 10

A cyclone separator as claimed in claim 7 wherein the overall length of the separator is substantially fourteen times said diameter at said one end.

Claim 11

A cyclone separator as claimed in one of claims 1 and 2 wherein said underflow outlet has a diameter in the range 0.05 to 0.9 times the diameter of the separating chamber at said one end.

Claim 12

A cyclone separator as claimed in claim 9 wherein said underflow outlet has a diameter in the range 1/5 th to 1/15 th times the diameter of the separating chamber at said one end.

Claim 13

A cyclone separator as claimed in any one of claims 1 and 2 wherein the overflow outlet has a diameter in the range 0.015 to 0.35 said diameter at said one end.

Claim 14

A cyclone separator as claimed in claim 11 wherein the overflow outlet has a diameter in the range 1/10 th to 1/30 th said diameter at said one end.

Claim 15

A cyclone separator as claimed in any one of claims 1 and 2 wherein said inlet portion, where provided, is of length in the range 0.5 to 1.5 times the diameter of the separating chamber at said one end.

Claim 16

A cyclone separator as claimed in any one of claims 1 and 2 wherein diameter d 1 is equal to d i .