Abstract: A filter of the type including a filter drum mounted within a settling tank containing a liquid to be filtered, with filtering flow drawn through a filter media on the outer surface of the drum, in which a fluid connection to the liquid circulation system is established by interfitting of tube sections as the filter drum is lowered into the tank at installation. Guiding members are included to properly position the drum as it is lowered to insure the tube sections move together as the filter drum is lowered. A valving arrangement is disclosed in one embodiment for isolating the particular drum filter from the circulation system upon removal. In another embodiment, an arrangement is utilized for producing intermittent rotation of the drum by engagement with the flights of a drag-out conveyor.

Abstract: A manure separator arrangement is described including a flume and chain conveyor arrangement by which initially received slurry of liquids and solids is directed over a perforated flume floor. Liquid is allowed to drain through perforations in the floor as the slurry is moved along a pair of troughs formed along the flume. The entire flume is inclined so the liquids received from the perforated flume floor will drain downwardly away from the solids being carried along by the drag conveyor. Solids leaving a discharge end of the flume may lose approximately 80% of the liquid previously contained in the slurry or mixture. The manure discharged from the flume may be received by a separator press roll mechanism by which remaining moisture can be separated. The separator includes a rotated perforated drum and an oppositely rotated press roll. The press roll is yieldably urged against the rotating surface of the drum and is simultaneously rotated to press or squeeze liquid from the solids.

Abstract: There is disclosed a nutsch filter having blades fitted to a central, vertically positioned hollow shaft by a hollow arm, the blades having a plough-like cutting edge and a spatula-like bottom surface acting in the opposite movement direction. A discharge pipe, arranged concentrically to the hollow shaft, is axially displaceable. The discharge pipe is moved upwards against a cover for sealing the filter casing. The filtration or resuspension or drying of the filter cake takes place in this position. In order to discharge the compressed filter cake, the upper edge of the discharge pipe is set by the blades to the level of the paring or skimming process. Paring of the filter cake and conveying of the pared mass into the central discharge pipe opening takes place in a single operation by means of the blades. On drying, hot air or a hot fluid is passed through the cavities of the arm as well as the parts connected thereto.

Abstract: A waste digestion unit which comprises a container, a waste inlet into the container, an outlet from the container for digested waste, a gas bleed outlet from the container and a stirrer for stirring the contents of the container. The inlet, waste outlet, bleed outlet and stirrer are arranged so that the container can be mounted in position and partially filled with waste to a level defined by the waste outlet to provide a gas space above the waste. In this position of the container the bleed outlet is above the waste level and, the inlet discharges into the container below the waste level. The stirrer is capable of stirring the waste at said waste level and below said waste level.

Abstract: Thickening of paper pulp, or a like suspension, is effected prior to feeding the pulp to an apparatus utilizing stationary screens for effecting washing, bleaching, or further thickening of the pulp. The stationary screens are mounted in a top portion of a vertical-axis vessel, and a plurality of radially extending rotating hollow arms, with annular screens mounted on them, is provided in the bottom of the vessel to effect thickening of the suspension from, for example, 11/2% consistency to about 9-14% consistency. Extraction from the hollow arms is provided through conduits extending vertically through a hollow shaft for rotating the arms, and a filtrate valve is also mounted within the hollow shaft in operative communication with the filtrate conduits, and includes a valve member which is rotatable in a different direction, and at a different speed, than the hollow shaft.

Abstract: The invention is a system which separates and reclaims a gas, e.g. methane, an aqueous fluid, e.g. water, and solids, e.g. coal from a slurry mixture. One application of the invention is in the degasification operations of underground mining. The system is hermetically constructed for the safe separation, collection and reclamation of the various components of the mixture.

Abstract: An on-line and continuous sampling system for monitoring the ionic content of steam-producing water in a steam-operated electrical power plant. The monitoring system comprises a plurality of sampling lines and associated apparatus for sampling the steam-producing water at a number of different points in the power plant, an ion chromatographic subsystem for analyzing the sampled water, a calibration subsystem for calibrating the ion chromatographic subsystem, and an automatic control subsystem for operating the monitoring system of the present invention.

Abstract: An extraction device for treating liquid-solid mixtures such as sewage sludge or paper pulp to remove liquid therefrom, includes a preliminary treatment station. The preliminary treatment station comprises at least two interchangeable perforated containers located on a displaceable receiver turntable beneath which a stationary disc is coaxially located. The stationary disc is provided with an aperture eccentrically disposed thereon, the aperture having a cross-sectional area corresponding to the cross-sectional area of the lower end of the container located on the turntable and to the cross-sectional area of an inlet aperture provided in the extraction device.By rotating the receiver turntable in a timed sequence a container is always moved beneath a filler tube, filled and further rotated. The solid components drop to the bottom of the container and liquid is discharged through the perforations provided in the container and the mixture thus has liquid removed in a preliminary treatment.

Abstract: A clarifier allowing increased fluid pressure differentials across the filter septum is arranged with one face of the septum exposed to the contaminated liquid and the opposite face exposed to the suction pressure of a pump with the discharge of the pump capable of being redirected to backflush through the filter septum, such backflushing being carried out sequentially through small area segments of the septum. The return of a flight conveyor may be moved selectively into and out of scraping or wiping relation with the filter and filter wiping and backflushing may be automatically controlled.

Abstract: Method and apparatus for clarifying liquids wherein a flight conveyor in the settling tank has a forwarding run for removing sludge from the bottom of the tank and a return run which is selectively moved into and out of wiping cooperation with a filter between the settling tank and a clean-liquid tank, and a filter backwasher in the clean tank is selectively operable to progressively backwash the filter, and both the wiping and backwashing being accomplished in accordance with the clogged condition of the filter.

Abstract: A conveyor apparatus has a pair of inclined, parallel, adjacent upwardly facing semicylindrical troughs, an elongated helical flight rotatably disposed in each trough, and a drive mechanism for effecting rotation of the helical flights. The lower ends of the troughs are received in a tank having spaced side walls and having spaced baffle walls between the side walls which are parallel to the side walls and extend above at least a portion of the top edge of each side wall. These top edge portions of the side walls are each adjustable about an axis normal to the side wall to a substantially horizontal position and are releasably fixable in such position. Solids introduced between the baffle walls are conveyed by the rotating flights to the upper ends of the troughs, and liquid so introduced passes under said baffle walls and over the adjustable edge portions of the side walls.

Abstract: A slurry separator utilizes the power inherent in the pressurized slurry from the slurry pump through a reaction nozzle to drive a rotor, with the slurry distributed through the nozzle being distributed over the surface of a conical grid. The rotor structure also drives squeegee-like blades which scrape the solids downward inside the cone readying screen for the next discharge, and then sweeping them down into a cylindrical auger chamber where they are compacted downwardly against an inverted conical floor to further squeeze moisture through the sides of a housing cylinder. The conical floor of the compacting cylinder presses up against the particulates to be compacted with a resistance that is proportional to the speed of the rotor, achieved through the use of a centrifugal governor. This action makes it tolerant to variations in nozzle flow volume (pressure) and converts energy output into optimum separation.

Abstract: An improved system for removing sludge from dam reservoir comprises a suction port, a delivery pipe, a float, a tug boat, several universal joints connected in the delivery pipe, a concentration alarming indicator, a boosting pipe, an ejector and a sludge consolidating means. The water of high static pressure is led through a boosting pipe into nozzles of an ejector so as to suck the air or muddy water near the bottom of a dam reservoir through the delivery pipe so that the sludge or sand existing deeply in the reservoir will be automatically discharged outside the dam without consuming electric or oil energy as driving a conventional pump.

Abstract: A portable cleaning apparatus for removing solids and particulate material from water in the basin of a cooling tower and having a trailer with a frame supporting a platform and a plurality of wheels for enabling said trailer to be towed from place to place, a power driven pump means mounted on said platform and having a suction side adapted to be placed into communication with water contaminated with solids in the basin of a cooling tower, a filter device arranged on said platform and including a filter medium therein, an inlet for liquid influent connected to the pump outlet and an effluent outlet downstream of the filter medium, the filter medium being so constructed and arranged as to retain solid particles thereon whose diameter is in excess of 0.

Abstract: Filtering devices wherein solid particulate matter is separated by filter media from a liquid flow often contain conveying means for moving the separated solid particulate to an external point for disposition. One such conveying means usable in filtering devices includes spaced endless chain loops wherein each chain comprises alternate center links pivotally joined by pins to alternate sets of spaced side bars. In each center link is an elongated aperture which in a controlled manner holds an extension bar attached to each end of a traversely positioned flight. The spaced chain may be operatively connected to a source of rotary power to periodically advance the conveying means so that the flights may be moved over a section of the filter media to effectively remove separated particulate matter collected thereon.

Abstract: A silicic acid filter cake and suspension agent are fed to a container equipped with a stirrer having a peripheral speed of about 20-30 m/sec. The ratio of container diameter to stirrer diameter is about 3:1. The ratio of container diameter to level of filling is a maximum of about 1:2. The container contains at least about 1.5 to about 2 kg of silicic acid suspension, for each 1 kg of silicic acid filter cake which is added to the container. The contents of the container is mixed while maintaining a pH of at most about 4. A portion of the resulting silicic acid suspension is drawn off from the zone of highest turbulence in the container. An apparatus for carrying out the process is provided.

Abstract: A liquid clarification system for separating solid and/or chemical contaminants from an unclarified liquid wherein a variable influent is passed through a settling clarifier to separate a portion of the contaminants from the liquid forming a semi-solid sludge. The sludge is passed into a reservoir and delivered to a filtration system at a controlled predetermined percentage of solids material. The solids material is circulated through the filtration system to form a filter cake on the septum of filters carried in a filtration chamber and the liquid is clarified by passing through the filter cake formed thereon. Periodically when the filter cake must be reformed, the expended cake is removed from the septum and conveyed from the filtration chamber through a sludge drying system to be discharged as dry solids waste material.

Abstract: A continuous decantation clarifier, wherein liquid to be clarified flows slowly and homogeneously into the interior of the clarifier, includes a first zone through which the liquid initially passes while the liquid is subjected to homogenization and flocculation, this first zone being penetrated in a substantially vertical descending direction by a second zone where the direction of liquid flow is reversed so that the liquid moves in an ascending vertical direction through flakes and solids in suspension in the liquid. In this latter zone such flakes and solids precipitate toward the bottom of the clarifier. The latter having a third zone wherein liquid commences to flow radially in an outward substantially horizontal direction, across frustoconical surfaces or trays, in which the decantation is concluded, the clarified liquid being collected close to the outer peripheries of the trays.

Abstract: An apparatus is presented for separating loose paper pieces from a bath of caustic soda, such as is ejected from a bottle washing machine including a housing having a reservoir in its upper portion, the reservoir having finely perforated bottom walls sloping toward the center where there is an elongated opening. An elongated helical screw conveyor is provided in the housing spaced below and parallel to the elongated opening with a perforated conveyor sleeve closely surrounding the conveyor on the bottom and sides leaving an open top which communicates with the paper coming down from the upper reservoir. Two cylindrical perforated drums are mounted in the housing on axes parallel to the screw conveyor and on opposite sides of the center of the housing. These drums may be rotated from time to time as set forth. A paper-chopping apparatus is provided at the end of the conveyor which discharges paper outside of the housing.

Abstract: The present invention relates to a multi-stage, single vessel, purification system for removing solid particles from liquids.Within the central portion of the vessel is a deceleration chamber having flow control means. About and substantially coextensive with the deceleration chamber is a filtering chamber. Depending well into the filtering chamber are a plurality of septums preferably coated with filter aid. Below the deceleration and filtering chambers is a settling chamber, and beneath the vessel is an expulsion device.A contaminated liquid is fed into the deceleration chamber and decelerated. In this chamber the lighter solid particles rise to the top of the liquid where they are removed, while the heavier density particles settle downwardly. As the liquid moves downwardly from the deceleration chamber it essentially displaces liquid in the settling chamber upwardly into the filtering chamber. In so doing the change of direction of liquid movement also causes the heavier particles to settle downwardly.

Abstract: The discharge end portion of a sewage delivery tube is surrounded by the input end portion of a conveyor pipe. A long, flat strip of consumable filter material is inserted through the annular space between them and into the conveyor pipe. Prior to this insertion, however, the filter strip is shaped and fastened into the form of a closed tube. The conveyor pipe discharges into an incinerator equipped with means for breaking the sewage sludge into burnable droplets. The conveyor pipe is supported over a liquid-collecting funnel and is perforated in the portion thereof that is over the funnel. A vibrator attached to the conveyor pipe oscillates it longitudinally; and ratchet teeth inside the conveyor pipe are oriented to cooperate with the vibrator to urge the filter-encased sludge toward the incinerator.

Abstract: The hot mixture of solid slag particles and water produced by contacting water with the molten slag released from a blast furnace is introduced into a tank equipped with an overflow and a filter at the overflow which permits a portion of the water and a minor fraction of slag fines to overflow. The major fraction of larger slag particles collects at the bottom of the tank and is pumped as a slurry containing the remainder of the heated water to a remote sedimentation zone where the slag particles and the water of the slurry are separated.

Abstract: Filtration apparatus comprises in a housing an annular filtration chamber into which there is admitted a suspension under pressure and which is formed between an external filtration surface in the form of a body of revolution and an internal filtration surface which is housed therein and is in the form of a body of revolution also; the annular filtration chamber has a suspension inlet at one of the chamber ends and has at its other and a product outlet; the filtration surfaces are connected in each case to a filtrate discharge collector; a rotating mixing-agitating device is arranged in the annular filtration chamber.

Abstract: An apparatus for separating solids, such as metal cuttings, from liquids, such as machine coolant, the apparatus having an upwardly inclined elongated housing which in cross-section is U-shaped with a semi-circular bottom and parallel sides, the housing being opened at the top and covered throughout its length by a removable lid, a helix rotated in the housing and extending from the lower end to the upper end, the housing having a solids discharge chute near the upper end, a gear motor mounted on the upper end of the housing for rotation of the helix and having at the lower end an upwardly extending fluid inlet chamber, the open top serving as an inlet by which solids containing liquids is conducted into the apparatus and having an upwardly extending overflow chamber connected with the lower portion of the housing, the walls of the overflow chamber being of less height than the inlet chamber, the inlet chamber, the overflow chamber and the lower portion of the housing together forming a quiescent zone in whic

Abstract: In a dynamic solids concentrator having a rotor with radially extensive disc-like elements which rotate adjacent other stationary or rotating disc-like elements, stabilizing members are provided along radial edges of the respective elements. In the case of the rotating elements, the stabilizing members are stabilizing fingers which ride within guide members on or guide paths in the inner walls of the concentrator and, in another embodiment, T-shaped stabilizing members whose arms ride on the surfaces of adjacent disc-like elements. In the case of the non-rotating elements, the stabilizng members are stabilizing fingers which ride within the guide members on or guide paths in the concentrators's rotor shaft. The fingers, T-shaped members and their cooperating guides stabilize the relative positions of the disc-like elements within the concentrator under conditions in which pressure differentials within the concentrator or high rotor speeds would otherwise disturb their relative positions.

Abstract: A slotted pipe is rotatably supported in a drag tank and communicates with the suction line of a pump. Magnetic discs are rotatable with the pipe and serve to attract and catch magnetic particles in liquid flowing to the pipe so as to prevent such particles from entering the pump. A scraper is positioned adjacent the rotatable discs and pipe to brush the caught particles therefrom and direct the particles to the bottom of the tank.

Abstract: In a dynamic solids concentrator having a rotor with radially extensive disc-like elements which rotate adjacent other stationary or rotating disc-like elements, stabilizing members are provided along radial edges of the respective elements. In the case of the rotating elements, the stabilizing members are stabilizing fingers which ride within guide members on or guide paths in the inner walls of the concentrator and, in another embodiment, T-shaped stabilizing members whose arms ride on the surfaces of adjacent disc-like elements. In the case of the non-rotating elements, the stabilizing members are stabilizing fingers which ride within the guide members on or guide paths in the concentrator's rotor shaft. The fingers, T-shaped members and their cooperating guides stabilize the relative positions of the disc-like elements within the concentrator under conditions in which pressure differentials within the concentrator or high rotor speeds would otherwise disturb their relative positions.