B01D21/2405

Continuous Dewatering Recirculation System with Integral Coal Combustion Residual High Flow Plate Separator

The system for a continuous dewatering recirculating for removing particulate such as coal combustion residue from a water stream. The system includes multiple dewatering and recirculation containers, each having a submerged flight conveyor and lamella settlings plate located therein, at least one dewatering and recirculation container receives ash water stream overflow.

SETTLING TANK AND METHODS FOR GUIDING PARTIAL FLOWS IN THE INFLOW AREA OF SETTLING TANKS
20200054969 · 2020-02-20 ·

A settling or sedimentation tank including inlet structures arranged, through whose inlet opening the suspension to be separated flows to the tanks, the height of which can be variably adjusted. In addition to the height variability of the inlet opening, the volumetric flow flowing out of the inlet structure can, depending on the actual load, be directed by forming a horizontally flow-through inlet opening or a vertically flow-through inlet opening and can optionally be divided into horizontal and vertical partial flows Q.sub.I and Q.sub.II. As a result of the horizontal inflow, the capacity of the sedimentation tank increases at high loads, and as a result of the vertical inflow, the volume flow through the sedimentation chamber and the turbulent energy in the sedimentation chamber decrease at low loads, so that the retention of fine suspension in the sedimentation tank is increased and thus the effluent quality is improved.

BOTTOM SECTION FOR BEING CONNECTED TO AN ASSEMBLY WITH PLATE SETTLER, AND ASSEMBLY WITH PLATE SETTLER

This disclosure relates to a bottom section for being connected to an assembly for separating a solid component from a fluid. The assembly includes an inclined plate settler with at least one sedimentation channel for letting a solid component to be separated settle, said plate settler comprising a lower portion and an upper portion, wherein said at least one sedimentation channel extends from the lower portion to the upper portion. The bottom section is configured to be connected to the lower portion of the inclined plate settler. The bottom section comprises at least one inlet channel for feeding a fluid comprising the solid component to be separated to the plate settler, and at least one collection channel for collecting a settled solid component descending from the at least one sedimentation channel. Said at least one inlet channel and said at least one collection channel are fluidly separated from each other, said inlet channel and said collection channel being connectable to said at least one sedimentation channel, to form fluid connections between said at least one inlet channel and said at least one sedimentation channel and between said at least one collection channel and said at least one sedimentation channel, respectively.

Density Phase Separation Device

A mechanical separator for separating a fluid sample into first and second phases within a collection container is disclosed. The mechanical separator may have a separator body having a through-hole defined therein, with the through-hole adapted for allowing fluid to pass therethrough. The separator body includes a float, having a first density, and a ballast, having a second density greater than the first density. A portion of the float is connected to a portion of the ballast. Optionally, the float may include a first extended tab adjacent a first opening of the through-hole and a second extended tab adjacent the second opening of the through-hole. In certain configurations, the separator body also includes an extended tab band disposed about an outer surface of the float. The separator body may also include an engagement band circumferentially disposed about at least a portion of the separator body.

DE-SANDING A DIGESTER
20200009479 · 2020-01-09 ·

Provided is a method and system for separating components of a solid and liquid mixture. In an embodiment, the method includes de-sanding a treatment system. Digesters, clarifiers, wastewater apparatuses, self-contained processing tanks, process tanks, and the like, accumulate sand and other undesired inorganic components that ultimately prevent filtering, cleaning, and processing of the solid and liquid mixtures therein. The mixture in the treatment system may initially include sand, water, and biosolids. The mixture may be routed into a pressurized tank to separate the inorganic solids and liquid components based on their density and buoyancy. A de-sanded mixture may then proceed through the remaining cleaning process.

SYSTEMS AND METHODS USEFUL FOR EFFICIENT FLUID RUN-OFF SEPARATION OF LIQUID AND SOLID CONTAMINANTS
20200009474 · 2020-01-09 ·

A system useful for cleaning solid and liquid contaminants from fluid run-off under varying flow rate conditions has an inlet enclosure; a main separation enclosure comprising an intake, an outlet, and an interior wall; and a foil attached to the interior wall of the main separation enclosure, the foil configured to smooth laminar flow of fluid in the main separation enclosure.

System and method for static mixing in an enhanced primary waste water treatment system using a fluid containment assembly

A method for static mixing in a waste water settling tank to increase recovery of entrained solids and solvated materials, the method comprising delivering an influent stream at a substantially constant flow rate to a settling tank; discharging a first portion of said influent stream toward a fluid deflector and a second portion of the influent stream into a fluid containment assembly to distribute the influent into contact with previously introduced waste water to create mixing zones and cause coalescence of the entrained solids.

System and method for static mixing in a EPT using a fluid containment assembly

A system and method for static mixing in a waste water settling tank to increase recovery of first entrained solids and solvated materials, comprising a settling tank having a recirculation ring and a hopper bottom defining a sludge hopper having a flat bottom portion, a fluid containment assembly, and a fluid deflector assembly with an optional fluid dispersion assembly. The system further comprises an inlet pipe for introduction of waste water containing second entrained solids and solvated materials into the settling tank and a discharge outlet in proximity to the underside of the fluid deflector assembly with nozzle facing downward. Influent waste water is directed both downward into the fluid containment assembly and upward into the center of the fluid deflector assembly and an optional fluid dispersion assembly to distribute the influent into contact with previously introduced waste water to cause coalescence of the first and second entrained solids.

SEPARATION APPARATUS

A separation apparatus includes: a partitioning member inside a separation tank, includes erect and transverse portions, and partitions the tank into inflow and outflow regions of a liquid; an inlet of which a lower level is set to be lower than an upper end of the erect portion and an upper level is set to be higher; a screen in the erect portion along a flow direction of the liquid; a swirling inducing member in the erect portion intersecting with the flow direction of the liquid; a screen in the transverse portion; a dividing member dividing the liquid flowing in from the inlet into flows along side walls of the separation tank; a retaining member at a downstream side in the flow direction and retains the substance having the specific gravity less than that of the liquid; and an outlet through which the liquid flows out from the outflow region.

Process and installation for producing alumina trihydrate by alkaline digestion of bauxite ore

A process for producing alumina trihydrate includes a digestion step, a separation step, and a precipitation step the separation step including: b1) pretreating a slurry from the digestion step by adding a flocculant to said slurry and mixing the flocculant and the slurry, b2) settling the resulting flocculated slurry in a gravity settler vessel, b3) determining a measured value representative of the concentration of solid particles in the resulting clarified liquor, b4) comparing the measured value with a predetermined threshold, b5) feeding said clarified liquor directly to the precipitation step, while the measured value is less than said predetermined threshold, and b6) redirecting said clarified liquor to the pre-treatment step b1), when the measured value is more than said predetermined threshold. An installation may be configured for operating said process.