Continuous process mixing of pulverized solids and liquids and mixing apparatus

Claim 2

A continuous process for mixing pulverized solids and liquids such as plaster powder and water characterized in that it comprises: continuously introducing the liquid in a mixing container at a selected flow rate, continuously introducing the pulverized solid in said container at a selected flow rate, said flow rates being selected to provide a desired proportion of solid and liquid, rotating the solid and liquid in the container in order to create a vortex thereof, withdrawing the thus mixed solid and liquid from the container and controlling the rate of withdrawing such that a desired level of the mixture in the container is maintained, the mean stay time for the mixture in the mixing container being determined by the said level of the mixture in the container.

Claim 3

A continuous process for mixing pulverized solids and liquids such as plaster powder and water characterized in that it comprises: continuously introducing the liquid in a mixing container at a selected flow rate, continuously introducing the pulverized solid in said container at a selected flow rate, said flow rates being selected to provide a desired proportion of solid and liquid, rotating the solid and liquid in the container in order to create a vortex thereof, and withdrawing the thus mixed solid and liquid from the container at a rate such that the desired level of the mixture in the container is maintained, said process being further characterized in that its starting period includes the following steps: introducing the liquid and solid into the mixing container in a weight ratio selected beforehand until a selected filling level of said mixing container is reached, rotating the liquid and solid in the container and maintaining the rotating motion for a selected time, and then, at the same time continuously introducing into the container liquid and solid at flow rates such that weight ratio of the mixture is maintained, and continuously withdrawing the mixture from the container at a flow rate that will maintain the filling level.

Claim 4

A continuous process for mixing pulverized solids and liquids such as plaster powder and water characterized in that it comprises: continuously introducing the liquid in a mixing container at a selected flow rate, continuously introducing the pulverized solid in said container at a selected flow rate, said flow rates being selected to provide a desired proportion of solid and liquid, rotating the solid and liquid in the container in order to create a vortex thereof, and withdrawing the thus mixed solid and liquid from the container at a rate such that the desired level of the mixture in the container is maintained, said process being further characterized in that its starting period includes the following steps: introducing the liquid and solid into the mixing container in a weight ratio selected beforehand until a selected filling level of said mixing container is reached, rotating the liquid and solid in the container and maintaining the rotating motion for a selected time, and then, at the same time continuously introducing into the container liquid and solid at flow rates such that weight ratio of the mixture is maintained, and continuously withdrawing the mixture from the container at a flow rate that will maintain the filling level.

Claim 5

A process according to claim 2 characterized in that the ratio of pulverized solid to water is 100 to 80 by weight.

Claim 6

A process according to claim 2 characterized in that the means stay time for products to be mixed in the mixing container is determined by said container filling level.

Claim 7

A process according to claim 1 characterized in that the mean stay time for products to be mixed in the mixing container is at least equal to 3 seconds and preferably from 15 to 30 seconds.

Claim 8

A process according to claims 1, 2, 3, or 4 characterized by the fact that mixture is passed into an ejection device and is discharged at the periphery of the ejection device.

Claim 9

A process according to claim 6 characterized in that the pulverized solid is plaster and the liquid is water.

Claim 10

A process according to any of claims 1-3, 4 and 5 characterized in that the withdrawing is done through the bottom of the mixing container.

Claim 11

A process according to claim 8 characterized in that the pulverized solid is plaster and the liquid is water.

Claim 12

A process according to any of claims 1-3, 4 and 5 characterized by the fact that at least a portion of the liquid is introduced along the interior of the mixing container wall in order to create a continuous sheet of liquid around said wall and by the fact that the withdrawing is done through the bottom of the mixing container.

Claim 13

A process according to claim 10 characterized in that the pulverized solid is plaster and the liquid is water.

Claim 14

A process according to any of claims 1-3, 4 and 5 characterized in that the pulverized solid is introduced into the center of the vortex, at least a portion of the liquid is introduced along the interior of the mixing container wall in order to create a continuous sheet of liquid aroung said wall, and the withdrawing is done through the bottom of the mixing container.

Claim 15

A process according to claim 12 characterized in that the pulverized solid is plaster and the liquid is water.

Claim 16

A process according to any of claims 1-3, 4 and 5 characterized in that solid or liquid additives are introduced in the liquid.

Claim 17

A process according to claim 14 characterized in that the pulverized solid is plaster and the liquid is water.

Claim 18

A process according to claim 14 characterized in that the solid additives are introduced in solid phase.

Claim 19

A process according to claim 16 characterized in that the pulverized solid is plaster and the liquid is water.

Claim 20

A process according to any of claims 1-3, 4 and 5 characterized in that solid or liquid additives are introduced into the mixer.

Claim 21

A process according to claim 18 characterized in that the solid additives are introduced in solid phase.

Claim 22

A process according to claim 19 characterized in that the pulverized solid is plaster and the liquid is water.

Claim 23

A process according to claim 18 characterized in that the pulverized solid is plaster and the liquid is water.

Claim 24

A process in accordance with any of claims 1-3, 4 and 5 characterized in that the pulverized solid is plaster and the liquid is water.

Claim 25

A vertical mixer, for pulverized solids and liquids characterized in that it comprises: a container formed by a hollow solid of revolution and equipped in its lower end with a run-off opening, run-off flow rate regulation means in communication with said run-off opening, said container having an intermediate bottom spaced from the interior of the side wall of the container, a turbine mounted inside of the container above the intermediate bottom and revolving around a vertical axis on the container's axis, means for continuously supplying a liquid in the container and means for continuously supplying a pulverized solid to the container.

Claim 26

A vertical mixer, for pulverized solids and liquids characterized in that it comprises: a container formed by a hollow solid of revolution and equipped in its lower end with a run-off opening, run-off flow rate regulation means in communication with said run-off opening, said container having an intermediate bottom spaced from the interior of the side wall of the container, a turbine mounted inside of the container above the intermediate bottom and revolving around a vertical axis on the container's axis, means for continuously supplying a liquid in the container and means for continuously supplying a pulverized solid to the container.

Claim 27

A mixer according to claim 23 characterized in that the intermediate bottom offers a top surface whose shape assumes corresponding top mixing zone flow lines.

Claim 28

A mixer according to claim 23 characterized in that the intermediate bottom offers a flat top surface which is perpendicular to the container's axis and is placed in the immediate vicinity of the turbine.

Claim 29

A mixer according to claim 23 characterized in that the intermediate bottom has a depending circular wall centered on the container's axis and with a diameter smaller than said container inner diameter.

Claim 30

A mixer according to claim 23 characterized in that the container has the form of a vertical cylinder with a downward extension which tapers toward the run-off opening.

Claim 31

A mixer according to claim 27 characterized in that the intermediate bottom is located at the level where the cylinder and tapered extension of the container are joined.

Claim 32

A mixer according to claim 20 characterized in that the intermediate bottom is constituted by the top surface of a downward tapered solid of revolution core placed inside of the container's tapered extension and centered on said container's axis, said core having a section smaller than the container's extension in order to provide for a ring shaped space in cross-section between it and said container's inner wall.

Claim 33

A mixer according to claim 29 characterized in that the core placed inside the container's extension is a straight cone positioned with its tip down and whose flat base constitutes the intermediate bottom, the container's tapered extension also being conical.

Claim 34

A mixer according to claim 29 characterized in that the run-off valve flow regulation means is an elastic sleeve valve which is placed downstream of an ejection device in communication with the container run-off opening, said ejection device receiving the mixture discharging from the container and transforming its flow into a full stream for entry into the valve.

Claim 35

A mixer according to claim 31 characterized in that the ejection device is shaped like an inverted cyclone having a conical casing placed with its tip upward with an inlet at the tip of the cone and has a flat base, and a collector pipe comes out of the ejection pipe flush with said base and tangentially to the comical casing in the direction of rotation of the turbine.

Claim 36

A mixer according to claim 31 characterized in that the ejection device is an impact crown formed by a vertical can with a bottom and a lateral discharge pipe.

Claim 37

A mixer according to claim 23 characterized in that the run-off flow regulation means is an elastic sleeve valve.

Claim 38

A mixer according to claim 23 characterized in that the pluverized solid supply means comprises: a supply hopper for a pulverized solid, trap means for regulating flow from the hopper, a constant weight weight-sensitive conveyor belt upon which pulverized solid from the hopper is poured and whose unbalance results in a change of trap means position, and a flow rate regulating means for receiving pulverized solid carried by the weight-sensitive conveyor belt comprising a vibrating spout.

Claim 39

A mixer according to claim 23 characterized in that the liquid supply means comprises: a ring-shaped pouring spout adjacent the top of the container and distributing liquid along the inside of the container's side wall, a tube directed toward the shaft of the turbine to discharge liquid thereon, and valve means for regulating the rate of flow.

Claim 40

A mixer according to claim 23 characterized in that the turbine is placed in the immediate vicinity of the intermediate bottom top surface.

Claim 41

A vertical mixer for pulverized solids and liquids comprising: a container in the form of a vertical cylinder with a downward extension which tapers toward its lower end which has a run-off opening, a downwardly tapered core in the downward extension of the container providing for a ring-shaped space in cross-section between it and the container's inner wall and its top providing an intermediate bottom at the level of the junction of the cylinder portion and tapered extension of the container, a turbine mounted inside of the container immediately above the intermediate bottom formed by the core, an ejection device in communication with the run-off opening for transforming the discharge from the run-off opening into a full stream, an elastic sleeve valve in communication with the ejection device and downstream thereof for run-off flow rate regulation, means for continuously supplying a liquid to the container including a ring-shaped pouring spout adjacent the top of the container and distributing liquid along the inside of the container's side wall, a tube directed toward the shaft of the turbine to discharge liquid thereon, and valve means for regulating the rate of flow, and means for continuously supplying a pulverized solid to the container including a supply hopper for a pulverized solid, trap means for regulating flow from the hopper, a constant weight weight-sensitive conveyor belt upon which pulverized solid from the hopper is poured and whose unbalance results in a change of trap means position, and a flow rate regulating means for receiving pulverized solid carried by the weight-sensitive conveyor belt comprising a vibrating spout.

Claim 42

A vertical mixer for pulverized solids and liquids comprising: a container in the form of a vertical cylinder with a downward extension which tapers toward its lower end which has a run-off opening, a downwardly tapered core in the downward extension of the container providing for a ring-shaped space in cross-section between it and the container's inner wall and its top providing an intermediate bottom at the level of the junction of the cylinder portion and tapered extension of the container, a turbine mounted inside of the container immediately above the intermediate bottom formed by the core, an ejection device in communication with the run-off opening for transforming the discharge from the run-off opening into a full stream, an elastic sleeve valve in communication with the ejection device and downstream thereof for run-off flow rate regulation, means for continuously supplying a liquid to the container including a ring-shaped pouring spout adjacent the top of the container and distributing liquid along the inside of the container's side wall, a tube directed toward the shaft of the turbine to discharge liquid thereon, and valve means for regulating the rate of flow, and means for continuously supplying a pulverized solid to the container including a supply hopper for a pulverized solid, trap means for regulating flow from the hopper, a constant weight weight-sensitive conveyor belt upon which pulverized solid from the hopper is poured and whose unbalance results in a change of trap means position, and a flow rate regulating means for receiving pulverized solid carried by the weight-sensitive conveyor belt comprising a vibrating spout.

Claim 43

A continuous process for mixing pulverized solids and liquids such as plaster powder and water characterized in that it comprises continuously introducing liquid into a mixing container at a selected flow rate, continuously introducing pulverized solids into said container at a selected flow rate, said flow rates being selected to provide a desired proportion of solid and liquid, rotating the solids and liquid in the container to create a vortex thereof and a mixture of the solids and liquid, rotating the mixture through a ring-shaped space in the container in a spiral descent into a discharge opening, and continuously passing the mixture through the discharge opening.

Claim 44

A continuous process for mixing pulverized solids and liquids such as plaster powder and water characterized in that it comprises continuously introducing liquid into a mixing container at a selected flow rate, continuously introducing pulverized solids into said container at a selected flow rate, said flow rates being selected to provide a desired proportion of solid and liquid, rotating the solids and liquid in the container to create a vortex thereof and a mixture of the solids and liquid, rotating the mixture through a ring-shaped space in the container in a spiral descent into a discharge opening, and continuously passing the mixture through the discharge opening.

Claim 45

The continuous process of claim 39, said ring-shaped space tapering toward the discharge opening, and rotating the mixture downwardly through the tapered space in ever decreasing circles in its spiral descent.

Claim 46

The continuous process of claim 39, the speed of the mixture being rotated through the ring-shaped space being at least 30 cm per second to prevent premature deposits and mass setting of the mixture.

Claim 47

The continuous process of claim 39, the speed of the mixture being rotated through the ring-shaped space being about 1 meter per second to prevent premature deposits and mass setting of the mixture.

Claim 48

The continuous process of claim 39, the mean time of the solids and liquids in the container being about 15 to 20 seconds.

Claim 49

The continuous process of claim 39, the time of the solids and liquids in the container being about 3 seconds.

Claim 50

The continuous process of claim 39, including introducing at least a portion of the liquid along the interior of the mixing container wall in order to create a continuous sheet of liquid on said interior wall.

Claim 51

The continuous process of claim 39, including regulating the output flow of the mixture.

Claim 52

A continuous process for mixing pulverized solids and liquids such as plaster powder and water characterized in that it comprises continuously introducing liquid into a mixing container at a selected flow rate, continuously introducing pulverized solids into said container at a selected flow rate, said flow rates being selected to provide a desired proportion of solid and liquid, rotating the solids and liquid in the container to create a vortex thereof and a mixture of the solids and liquid, rotating the mixture through a ring-shaped space in the container in a spiral descent into a discharge opening, and continuously passing the mixture through the discharge opening, said process including passing the mixture from the discharge opening into an ejection zone and rotating the mixture in the ejection zone, and discharging the mixture tangentially from the ejection zone into a collector pipe

Claim 53

A continuous process for mixing pulverized solids and liquids such as plaster powder and water characterized in that it comprises continuously introducing liquid into a mixing container at a selected flow rate, continuously introducing pulverized solids into said container at a selected flow rate, said flow rates being selected to provide a desired proportion of solid and liquid, rotating the solids and liquid in the container to create a vortex thereof and a mixture of the solids and liquid, rotating the mixture through a ring-shaped space in the container in a spiral descent into a discharge opening, and continuously passing the mixture through the discharge opening, said process including passing the mixture from the discharge opening into an ejection zone and rotating the mixture in the ejection zone, and discharging the mixture tangentially from the ejection zone into a collector pipe

Claim 54

A continuous process for mixing pulverized solids and liquids such as plaster powder and water characterized in that it comprises continuously introducing liquid into a mixing container at a selected flow rate, continuously introducing pulverized solids into said container at a selected flow rate, said flow rates being selected to provide a desired proportion of solid and liquid, rotating the solids and liquid in the container to create a vortex thereof and a mixture of the solids and liquid, rotating the mixture through a ring-shaped space in the container in a spiral descent into a discharge opening, and continuously passing the mixture through the discharge opening, said process including said ejection zone having an inverted cone shape, and revolving the mixture in ever widening circles in the ejection zone in a spiral descent to the discharge opening so that no uncontrolled vortex is likely to create a motionless zone where mass setting could occur.

Claim 55

A continuous process for mixing pulverized solids and liquids such as plaster powder and water characterized in that it comprises continuously introducing liquid into a mixing container at a selected flow rate, continuously introducing pulverized solids into said container at a selected flow rate, said flow rates being selected to provide a desired proportion of solid and liquid, rotating the solids and liquid in the container to create a vortex thereof and a mixture of the solids and liquid, rotating the mixture through a ring-shaped space in the container in a spiral descent into a discharge opening, and continuously passing the mixture through the discharge opening, said process including said ejection zone having an inverted cone shape, and revolving the mixture in ever widening circles in the ejection zone in a spiral descent to the discharge opening so that no uncontrolled vortex is likely to create a motionless zone where mass setting could occur.