A deep cone thickener with an underflow concentration rapid auto-adjustment pertains to the technical field of mining tailing disposal. The thickener includes a shell body, a dilution flocculation system, a shearing dewatering system, an underflow circulatory system, and an auto-control system. The shell body includes a thickener pool wall, a cone body, and a collection cylinder. The dilution flocculation system includes a feed pipe, a flocculant charging pipe, and a central feed well. The shearing dewatering system includes a drive motor, a drive shaft, and a rake. The underflow circulatory system includes discharging valves, underflow pumps, circulatory pipes, and a concentration meter. The auto-control system includes a PLC control system. During the underground paste filling, the dilution flocculation system and shearing dewatering system can form a paste slurry. When there is no need for underground backfill, the underflow circulatory system is used to lower the underflow concentration rapidly.

A deep cone thickener with an underflow concentration rapid auto-adjustment pertains to the technical field of mining tailing disposal. The thickener includes a shell body, a dilution flocculation system, a shearing dewatering system, an underflow circulatory system, and an auto-control system. The shell body includes a thickener pool wall, a cone body, and a collection cylinder. The dilution flocculation system includes a feed pipe, a flocculant charging pipe, and a central feed well. The shearing dewatering system includes a drive motor, a drive shaft, and a rake. The underflow circulatory system includes discharging valves, underflow pumps, circulatory pipes, and a concentration meter. The auto-control system includes a PLC control system. During the underground paste filling, the dilution flocculation system and shearing dewatering system can form a paste slurry. When there is no need for underground backfill, the underflow circulatory system is used to lower the underflow concentration rapidly.

The invention relates to a water treatment plant which comprises means (38) for supplying the water to be treated, means (31) for supplying coagulant reagent (21), a flocculation-decantation device (1) which has means (32) for dispensing the flocculant reagent, means (33) for distributing ballast, means (39d) for extracting decantation sludge and means (9) for discharging water that has been treated, a line (8) for supplying coagulated water to the flocculation-decantation device (1), means (24) for separating the ballast contained in the ballasted sludge followed by means (36) for recycling the ballast back into said flocculation-decantation device (1), characterised in that said device (1) comprises an outer tank (2) that has a first hopper (4), and at least one inner tank (3) that has a second hopper (5) and is arranged inside said outer tank (2); the inner tank (3) receiving the flocculant and the ballast and comprising stirring means (10), wherein a peripheral space is disposed between the inner tank (3) and the outer tank (2); the second hopper (5) having an opening (6) which opens into the first hopper (4); and said first hopper (4) having an outlet that communicates with the means (34) for discharging ballasted sludge, wherein the means (9) for discharging water that has been treated are disposed in the upper portion of said outer tank (2). The invention also relates to a method for implementing a plant of this types.

There is provided a material treatment apparatus. The material treatment apparatus includes a first compartment. The first compartment includes an inlet for receiving supply of slurry material, and a first material conduction space for conducting flow of the supplied slurry material in a downwardly direction. A second compartment is also provided including a second material conduction space for receiving a first intermediate material of the supplied slurry material and conducting the first intermediate material in an upwardly direction. A baffle is provided for interfering with conducting of the supplied slurry material from the first material conduction space to the second material conduction space. A turbulent flow mitigation device is disposed within the first compartment and configured to, upon interaction with the supplied slurry material, to effect adjustment to the flow characteristics of the supplied slurry material to generate a downwardly flowing flow characteristic-adjusted slurry material, wherein the flow characteristics of the supplied slurry material are transformed from turbulent flow to laminar flow. The turbulent flow mitigation device is disposed, relative to the baffle, such that the baffle directs the downwardly flowing flow characteristic-adjusted slurry material to a space below the first baffle. The first material conducting space is fluidly coupled, below the baffle, to the second material conduction space, such that the first intermediate material fraction of the downwardly flowing flow characteristic-adjusted slurry material is conducted to the second material conduction space from below the baffle. A collection region is disposed below the first and second compartments for collecting a separated solids-comprising fraction that has separated, by gravity settling, from the supplied slurry material.

A separation system for the removal of suspended solids from raw fluid. Raw fluid is placed in a non-pressurized settling tank and allowed to partially settle before injection into a pressurized clarification vessel. Following a dwell period clarified fluid is discharged at the top of the clarification vessel and settled waste is removed at the bottom thereof. Constant vessel pressure is maintained during injection of raw fluid or the discharge of clarified fluid or settled waste. The system is simpler to manufacture and more efficacious in its use than prior art methods.

A separation system for the removal of suspended solids from raw fluid. Raw fluid is placed in a non-pressurized settling tank and allowed to partially settle before injection into a pressurized clarification vessel. Following a dwell period clarified fluid is discharged at the top of the clarification vessel and settled waste is removed at the bottom thereof. Constant vessel pressure is maintained during injection of raw fluid or the discharge of clarified fluid or settled waste. The system is simpler to manufacture and more efficacious in its use than prior art methods.