B01D21/0009

MAGNETIC FILTER WITH DRAIN AND REMOVABLE EXTERNAL MAGNETIC ELEMENT
20190308200 · 2019-10-10 ·

A magnetic filter 10 for a central heating system is disclosed, the filter 10 including a connection assembly 12, a canister 14, and a magnetic element 16, the connection assembly 12 including an inlet 24 and an outlet 26 for connection to a central heating circuit; the canister 14 having an interior separation chamber which is fluidly connected with the inlet 24 and outlet 26 for allowing fluid to flow into the inlet 24, through the separation chamber, and out of the outlet 26; and the magnetic element 16 being removably positionable on the outside of the canister 14, the canister 14 and the connection assembly 12 forming a sealed flow path comprising the inlet 24, the interior separation chamber and the outlet 26, and the connection assembly 12 further including a closable drain outlet 28b for draining fluid and magnetic particles from within the canister 14, internally of the magnetic element 16.

Magnetic filter for a central heating system

A magnetic filter 10 includes first and second separation chambers 10, 12. The separation chambers 10, 12 each have an inlet and an outlet, and the separation chambers 10, 12 are joined together such that the inlets of the first and second chambers are adjacent, and the outlets of the first and second chambers are adjacent. An inlet port arrangement 28 connects both inlets to a single inlet pipe, and an outlet port arrangement 30 connects both outlets to a single outlet pipe.

Liquid refinement
10343088 · 2019-07-09 · ·

Embodiments disclosed herein relate to an apparatus for refining a liquid stream which includes a liquid carrier with a heavier waste and a lighter waste. The apparatus includes a first flow chamber, a second flow chamber, and plates. The first flow chamber is a cone structure and directs the liquid stream downwards in a first direction at a first velocity. The first velocity is greater than a settling velocity of a heavier waste in the liquid carrier. The second flow chamber directs the liquid carrier upwards in a second direction at a second velocity less than the settling velocity. The plates are in the second flow chamber and at a transition between the first and second flow chambers. The plates have an inclined geometry to cause laminar flow in the liquid stream to separate the heavier waste to a lower collection chamber and lighter waste to an upper collection reservoir.

Liquid refinement
10343089 · 2019-07-09 · ·

Embodiments disclosed herein relate to an apparatus for refining a liquid stream. The apparatus includes a first flow chamber, an inclined plate region, and a second flow chamber. The first flow chamber forms a first portion of an hourglass double cone structure and directs the liquid stream in a first direction at a first velocity. The inclined plate region includes inclined plates radiating outward from the hourglass double cone structure in a helical pattern. The inclined plate region directs the liquid carrier in a second direction opposite the first direction at a second velocity less than the first velocity forming a laminar flow condition in the liquid stream to separate heavy waste and light waste from the liquid stream. The second flow chamber forms a second portion of the hourglass double cone structure and directs the liquid stream to a liquid stream outlet.

Method for recovering target materials from source materials

A single-heating stage method for reclaiming or recovering metals like nickel and vanadium from a petroleum waste byproduct has three steps: melting the petroleum waste byproduct in a reducing atmosphere, generating agglomerated metal in the melted byproduct, and lifting the agglomerated metal to an exposed surface of the melted byproduct. The metal precipitates out of the molten byproduct, agglomerates into a separate portion, and rises to an exposed surface of the melted petroleum waste byproduct even though the metal may have greater density than the molten petroleum waste byproduct. The original petroleum waste byproduct stratifies into a byproduct remnant and the agglomerated metal disk. The agglomerated metal disk is separable from the byproduct remnant and may be additionally separated into constituent metals in those embodiments with multiple metals in the disk.

Passive gravity filter cell and methods of use thereof

A passive filter cell having a basin with a floor and two or more vertical or upright sidewalls forming chute or container having first or left sidewall, second or right sidewall, and third or back sidewall, and fourth or front downwardly curved sidewall, an inlet positioned proximate a top of the fourth or front sidewall and an outlet positioned proximate the top of the third or back sidewall, wherein the floor is configured angled from the fourth or front sidewall to the third or back sidewall, discharge pipe positioned proximate junction between the floor and the third or back sidewall, and lip configured to extend from the top of the third or back sidewall into an interior of the basin.

PLANT AND PROCESS FOR REMOVING SUSPENDED SOLIDS, OILS AND GREASES FROM COOLING WATER IN THE STEEL AND METALLURGICAL SECTOR
20240181373 · 2024-06-06 ·

The invention relates to a water treatment line and a process for removing suspended solids, such as ferrous scale, and in particular also oils and greases, from cooling waters of metallurgical or steel processing. A sedimentation tank is included in which there is a lamellar pack filter with inclined sedimentation surfaces comprising a plurality of adjacent, essentially parallel and inclined tubular profiles, in particular with an angle of inclination with respect to the bottom of said tank of 50-65?. The application of the laminar packs in the tank which separate suspended solids, in particular ferrous scale, by sedimentation avoids the use of sand filters or the like.

Combination of carrier-magnetic-separation and a further separation for mineral processing

A process for concentrating desired particles containing a carrier-magnetic-separation with the following steps, providing a feedstock which contains the desired particles; adding hydrophobic magnetic particles to the feedstock which results in a loaded feedstock containing agglomerates of the magnetic particles and the desired particles or of the magnetic particles and the undesired material; separating the agglomerates from the loaded feedstock by a separation method which results in isolated agglomerates, breaking up the isolated agglomerates to obtain a suspension having magnetic particles in de-agglomerated form; and separating the magnetic particles from the suspension obtained in step d) by a separation method and provided that at least one separation method is a magnetic separation, and where the process has at least one further separation and where the further separation is s sorting, electric separation, screening, classification, gravity concentration, and flotation.

REMEDIATION AND RECYCLING OF FRAC WATER AND FLOW BACK WATER
20190144315 · 2019-05-16 · ·

A method and device for treating contaminated water where the device is portable. The method includes the steps of moving contaminated water into a first tank to settle out large solids such as cuttings and metallic particles while adding a pH modifier, a coagulant, and gaseous ozone. Moving the contaminated water into a second tank where the pre-treated water is subjected to an electro-coalescing process that subjects the water to a strong DC current as the water passes between several bi-metallic plates. After the electro-coalescing process the water may be filtered to remove the remaining solids resulting from the pre-treatment and the electro-coalescing process or the solids may be allowed to settle. The resulting water may then be re-used in the fracturing or drilling processes.

ACCELERATED METHOD FOR PREPARING PLATELET RICH PLASMA
20190134293 · 2019-05-09 ·

Provided is an accelerated method for preparing platelet rich plasma (PrP) without centrifugation or filtration. The method comprises contacting a sample of whole blood with an anti-coagulant and an inducer of Rouleaux formation; allowing the mixture to stand thereby depleting the sample of RBCs, and collecting the platelet-rich plasma fraction. The PrP volume obtained by the present method is about 10-60% of the volume of the starting whole blood sample, and contains less than 200,000 RBCs and at least 100,000 platelets per microliter.