Method and apparatus for mixing pulverous material with liquid
View Patent ↗Liquid is supplied within a substantially vertical mixing chamber in a substantially tangential manner from a chamber top section, such that the liquid is deflected for rotatory motion against a chamber wall while advancing, in response to a pressure difference, downwards in the direction of a chamber longitudinal axis. Pulverous material is supplied by compressed air into the chamber ( 3 ) from the top section and into an air core (A) established by the liquid in rotatory motion, such that the pulverous material containing little air, and by being heavier than the air contained in the pulverous material and/or used for carrying the same, is driven in response to a centrifugal force into the liquid in rotatory motion, and the air separates towards the eddy center, and that the liquid containing pulverous material and the air supplied into the chamber, are discharged through an open bottom section of the chamber ( 3 ).
1. A method for mixing pulverous material with liquid in a substantially vertical mixing chamber comprising the steps of:
setting a liquid in rotatory motion within the substantially vertical mixing chamber, by supplying the liquid in a substantially tangential manner from a top section of the mixing chamber, such that the liquid is deflected into rotatory motion against a wall of the mixing chamber;
advancing the liquid downwards in a downward longitudinal direction along a longitudinal axis of the mixing chamber, in response to a pressure difference in the downward longitudinal direction; and
supplying the pulverous material and air contained in the pulverous material by use of compressed air into the mixing chamber from the top section of the mixing chamber into an air core established by the liquid in rotatory motion within the mixing chamber, wherein the pulverous material is driven in response to a centrifugal force into the liquid in rotatory motion within the mixing chamber forming a liquid containing pulverous material, and the air contained in the pulverous material and the air used for carrying the pulverous material is separated towards an eddy center defined by the air core, and wherein the liquid containing pulverous material, and the air contained in the pulverous material and the air used for carrying the pulverous material, are discharged through an at least mainly open bottom section of the mixing chamber.
2. The method of claim 1 wherein the liquid is fed into the supply chamber at a rate which is higher than 10 m/s.
3. The method of claim 2 , wherein the liquid containing pulverous material is fed from the mixing chamber to a mixing tank.
4. The method of claim 3 , wherein the liquid containing pulverous material is injected directly to a mixer present in the mixing tank.
5. The method of claim 1 wherein the liquid is fed into the supply chamber at a rate which is between about 12 and about 18 m/s.
6. The method of claim 1 wherein the substantially vertical mixing chamber is a cylindrical pipe having a top, the top having a means for introducing liquid and pulverous material into the cylindrical pipe, the cylindrical pipe having a bottom section which is open, the open bottom section dispersing the liquid containing pulverous material forming a film, which exits unimpeded from the mixing chamber without disturbance, in such a way that the liquid containing pulverous material travels along the chamber wall and the air core extends through the open bottom section.
7. The method of claim 1 , wherein the liquid supplied into the mixing chamber is coating material used for coating paper or other web material, or pigment slurry used for making coating material.
8. The method of claim 1 wherein the liquid supplied into the mixing chamber is a component for a coating material used for coating paper or other such web material or of a mixture thereof.
9. A method for mixing pulverous material with liquid comprising the steps of:
supplying the liquid in a substantially tangential manner to atop section of a mixing chamber having a substantially cylindrical wall, to cause the liquid to rotate against the substantially cylindrical wall of the mixing chamber;
advancing the liquid downwards in a downward longitudinal direction along a longitudinal axis defined by the cylindrical wall of the mixing chamber, in response to a pressure difference in the downward longitudinal direction; and
supplying pulverous material carried by air into the mixing chamber from the top section of the mixing chamber into an air core established by the liquid in rotatory motion within the mixing chamber, wherein the pulverous material is driven in response to a centrifugal force into the liquid in rotatory motion within the mixing chamber, and wherein the liquid now containing the pulverous material, and the air supplied into the mixing chamber, are discharged through an at least mainly open bottom section of the mixing chamber.
10. The method of claim 9 wherein the liquid is fed into the supply chamber at a rate which is higher than 10 m/s.
11. The method of claim 9 wherein the mixing chamber is a cylindrical pipe having a top, forming the top section, the cylindrical pipe having a bottom section which is open, the open bottom section dispersing the liquid containing the pulverous material as a film, which exits unimpeded from the mixing chamber without disturbance, in such a way that the liquid containing the pulverous material travels along the chamber wall and the air core extends through the open bottom section.