Device for separating fluid mixtures, in particular oil/water mixtures

1. A device for separating fluid mixtures, comprising

a vacuum chamber (V),

a fluid supply (FZ) through a truncated-cone round jet nozzle (K),

a fluid outlet (FA) in the bottom area of the vacuum chamber for discharge of the dried fluid by means of a fluid pump (FP),

a gas outlet (GA) that is connected to a vacuum pump (VP),

a controllable gas entry (GE),

characterized by that the truncated-cone round jet nozzle (K) is composed of

a tube (R) with a closed end (E),

wherein the tube (R) has a tapered portion before the closed end (E),

wherein the tapered portion of the tube reduces the diameter of the tube to 90-30% of the entry diameter (R D ),

2-8 holes (L) as exit openings arranged orthogonally to the flow direction (SR) in the area of the tapered portion, wherein the holes (L) respectively have a diameter (L D ) between one twentieth and one half of the tube diameter at the taper (R J ),

a first cap nut (M 1 ) having an outer diameter of 1.25-2.5 times the tube diameter at the taper (R J ) with a shoulder-type tapered portion,

wherein the shoulder has a height of 0.1-10 mm and a width of 90-70% of the original diameter,

a second cap nut (M 2 ) having an outer diameter of 1.25-2.5 times the tube diameter at the taper (R J ), with a conical shape, wherein the height of the conical portion (K H ) is between 0.01 and 10 mm and the cone angle (φ) is between 10° and 80°,

wherein the first and the second cap nuts are arranged at the tube in such a manner that in the area of the holes, a gap (Sp) of 0.01 to 10 mm width (Sp b ) is formed.

2. The device according to claim 1 , characterized by that the tube (D) has an external thread.

3. The device according to claim 1 , characterized by that a level monitoring device for determining the fluid level is formed by means of at least one floating body (S) with an upper (S O ) and a lower (S U ) stop.

4. The device according to claim 3 , characterized by an inclination limitation device comprising a tube (R N ), in which at least one floating body is arranged, which is vertically arranged in the middle of the vacuum chamber, and which has apertures at top and bottom.

5. A method for drying oils, such as for instance hydraulic oil, lubricating oil, gearbox oil, motor oil, turbine oil and/or diesel oil, comprising passing the oil through a device according to claim 1 .

6. A method for drying fluid in power plants, industrial plants, sea and airships, vehicles or airplanes, comprising passing said fluid through a device according to claim 1 .

7. A truncated-cone round jet nozzle (K) for nebulizing fluids, comprising

a tube (R) with a closed end (E),

wherein the tube comprises a tapered portion before the closed end (E),

wherein the tapered portion of the tube reduces the diameter of the tube to 90-30% of the entry diameter (R D ),

2-8 holes (L) as exit openings arranged orthogonally to the flow direction (SR) in the area of the tapered portion, wherein the holes respectively have a diameter (L D ) between one twentieth and one half of the tube diameter at the taper (R J ),

a first cap nut (M 1 ) having an outer diameter of 1.25-2.5 times the tube diameter at the taper (R J ) with a shoulder-type tapered portion,

wherein the shoulder has a height (M 1H ) of 0.1-10 mm and a width (M 1B ) of 90-70% of the original diameter,

a second cap nut having an outer diameter of 1.25-2.5 times the tube diameter at the taper (R J ), with a conical shape, wherein the height of the conical portion (K H ) is between 0.01 and 10 mm and the cone angle (φ) is between 10° and 80°,

wherein the first and the second cap nuts are arranged at the tube in such a manner that in the area of the holes, a gap (Sp) of 0.01 to 10 mm width (Sp B ) is formed.

8. The truncated-cone round jet nozzle (K) according to claim 7 , characterized by that the tube (R) has an external thread.