子分类：
| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 241 | VERFAHREN ZUR STEUERUNG EINER SORTIER- UND KLASSIERVORRICHTUNG FÜR SAND UND KIES | EP97935480.0 | 1997-07-19 | EP0921860B1 | 2001-09-19 | KÖRBER, Rolf |
| A process is disclosed for controlling the composition of a product from a device for sizing and sorting mineral raw materials, in particular sand and gravel, which must keep a predetermined finest sand concentration in the sand product quantity. For that purpose, an additional sizing separation of the sand product quantity into a sand fraction (mPr) and into a finest sand fraction (mFSS) to be discharged through the overflow is carried out in the chamber above the level (hFS) of the fluidised bed contained in the chamber. In order to set a predetermined finest sand concentration (C<Prsoll) in the sand product quantity, the level (hFS) of the fluidised bed is regulated in such a way that the proportion of finest sand (m<A) in the loaded amount of raw material can be divided by the fluidised bed into a finest sand proportion permissible as a function of the predetermined concentration (C<Prsoll) to be discharged into the sand product quantity (mPr) and into a finest sand proportion (mFSS) to be discharged through the overflow. | ||||||
| 242 | VERFAHREN ZUR STEUERUNG EINER SORTIER- UND KLASSIERVORRICHTUNG FÜR SAND UND KIES | EP97935480.0 | 1997-07-19 | EP0921860A1 | 1999-06-16 | KÖRBER, Rolf |
| A process is disclosed for controlling the composition of a product from a device for sizing and sorting mineral raw materials, in particular sand and gravel, which must keep a predetermined finest sand concentration in the sand product quantity. For that purpose, an additional sizing separation of the sand product quantity into a sand fraction (mPr) and into a finest sand fraction (mFSS) to be discharged through the overflow is carried out in the chamber above the level (hFS) of the fluidised bed contained in the chamber. In order to set a predetermined finest sand concentration (C¿∫Prsoll?) in the sand product quantity, the level (hFS) of the fluidised bed is regulated in such a way that the proportion of finest sand (m∫A) in the loaded amount of raw material can be divided by the fluidised bed into a finest sand proportion permissible as a function of the predetermined concentration (C¿∫Prsoll?) to be discharged into the sand product quantity (mPr) and into a finest sand proportion (mFSS) to be discharged through the overflow. | ||||||
| 243 | VORRICHTUNG ZUM ABTRENNEN VON MIT ORGANISCHEM MATERIAL VERSCHMUTZTEM ANORGANISCHEM MATERIAL AUS EINER FLÜSSIGKEIT | EP94928796.5 | 1994-09-22 | EP0707520B1 | 1999-04-21 | GRIENBERGER, Johann |
| A device for separating organic and inorganic material in a fluid has a round container (1) having in its upper region a centrically arranged feed device (19) with a spinning chamber (22), a gravity pipe (23) and a trumpet-shaped diffuser (24) to introduce the fluid into the container (1). In the lower region (7) of the container (1) there is an extractor device (32) for the inorganic material and a device (29) to discharge the organic material and the fluid. In the lower region (7) of the container (1) there is a fluidised sand bed (14) which is kept in motion by an upward flow distributed via a perforated base (8). In addition there is a by-pass (38) to transfer part of the sand in the sand bed (14) into the extractor (32) in the lower region of the container (1). | ||||||
| 244 | WATER CLARIFIER WITH FIRST FILTRATE ISOLATION, IMPROVED BACKWASHING AND IMPROVED BUBBLE GENERATION | EP93913923.4 | 1993-05-17 | EP0641292B1 | 1998-09-09 | KROFTA, Milos |
| A two stage raw water clarifier with first stage flotation and second stage filtration divides at least the lower portion of a flotation tank into independent cells. A branched slotted conduit located in a filter medium in each cell collects clarified water. Valves control the flow of clarified water from each branched conduit either to a clarified water ring conduit or to a first filtrate/backwash ring conduit connected to a storage tank. The filter media is preferably a dual media, a layer of anthracite or activated carbon over a layer of sand. High cell walls and inclined baffles in each cell retain the filter media during backwashing. The baffles also slow the flotation process. A decompression valve for pressurized water with dissolved air has a very narrow annular slot in the flow path through the valve to create microscopic air bubbles of optimal size for the flotation. A movable member sets this annular slot at a proper value. A mechanical or pneumatic actuator moves the member periodically to open the slot and flush out trapped particles. | ||||||
| 245 | COMPACT CLARIFIER SYSTEM FOR MUNICIPAL WASTE WATER TREATMENT | EP94911642 | 1994-03-18 | EP0689521A4 | 1997-11-19 | KROFTA MILOS |
| A compact water treatment plant has at least one vertical stack of dissolved air flotation (DAF) type clarifiers. Raw water is directed first to a single stage clarifier with a shallow tank. Its output is fed to an underlying two stage clarifier, preferably one with tall, mutually isolated cells, inclined baffles over a filtration medium in each cell, a cell-by-cell backwash capability, and an arrangement for isolating the first filtrate from the clarified water. Preferably, there are two such stacks in side-by-side array to provide a peak-load capacity, redundancy, and extreme compactness. Also preferably, clarified water from the single stage clarifier flows to the two stage clarifier via a bioreactor and an associated DAF clarifier. A source of aeration defines an upper, aerobic zone in the reactor where bacteria act on organic contaminants (COD's and BOD's). Strips of a deep pile, woven textile form a biocarrier. The strips oscillate in the tank. A portion of the bioliquor and sludge from the bioreactor-dedicated clarifier recirculate through a lower, anoxic zone of the bioreactor for denitrification. | ||||||
| 246 | COMPACT CLARIFIER SYSTEM FOR MUNICIPAL WASTE WATER TREATMENT | EP94911642.0 | 1994-03-18 | EP0689521A1 | 1996-01-03 | KROFTA, Milos |
| A compact water treatment plant has at least one vertical stack of dissolved air flotation (DAF) type clarifiers. Raw water is directed first to a single stage clarifier with a shallow tank. Its output is fed to an underlying two stage clarifier, preferably one with tall, mutually isolated cells, inclined baffles over a filtration medium in each cell, a cell-by-cell backwash capability, and an arrangement for isolating the first filtrate from the clarified water. Preferably, there are two such stacks in side-by-side array to provide a peak-load capacity, redundancy, and extreme compactness. Also preferably, clarified water from the single stage clarifier flows to the two stage clarifier via a bioreactor and an associated DAF clarifier. A source of aeration defines an upper, aerobic zone in the reactor where bacteria act on organic contaminants (COD's and BOD's). Strips of a deep pile, woven textile form a biocarrier. The strips oscillate in the tank. A portion of the bioliquor and sludge from the bioreactor-dedicated clarifier recirculate through a lower, anoxic zone of the bioreactor for denitrification. | ||||||
| 247 | WATER CLARIFIER WITH FIRST FILTRATE ISOLATION, IMPROVED BACKWASHING AND IMPROVED BUBBLE GENERATION. | EP93913923 | 1993-05-17 | EP0641292A4 | 1995-06-28 | KROFTA MILOS |
| A two stage raw water clarifier with first stage flotation and second stage filtration divides at least the lower portion of a flotation tank into independent cells. A branched slotted conduit located in a filter medium in each cell collects clarified water. Valves control the flow of clarified water from each branched conduit either to a clarified water ring conduit or to a first filtrate/backwash ring conduit connected to a storage tank. The filter media is preferably a dual media, a layer of anthracite or activated carbon over a layer of sand. High cell walls and inclined baffles in each cell retain the filter media during backwashing. The baffles also slow the flotation process. A decompression valve for pressurized water with dissolved air has a very narrow annular slot in the flow path through the valve to create microscopic air bubbles of optimal size for the flotation. A movable member sets this annular slot at a proper value. A mechanical or pneumatic actuator moves the member periodically to open the slot and flush out trapped particles. | ||||||
| 248 | Verfahren und Vorrichtung zum kontinuierlichen Trennen von in einer Stoffsuspension enthaltenen erwünschten von unerwünschten Stoffen | EP94117139.9 | 1994-10-29 | EP0658648A2 | 1995-06-21 | Schultz, Hans-Joachim, Dr. |
Die Erfindung betrifft ein Verfahren zum kontinuierlichen Trennen von in einer Stoffsuspension enthaltenen erwünschten von unerwünschten Stoffen, z.B. zum kontinuierlichen Reinigen einer für die Herstellung von Papier, Pappe und dgl. auf einer Papiermaschine bestimmten Fasersuspension, bei dem ein Zulaufstrom der Fasersuspension in einen Verteilbereich geleitet und dort in eine Anzahl wenigstens annähernd gleicher Teilströme aufgeteilt wird, diese Teilströme sodann je für sich einen Reinigungsvorgang durchlaufen, wobei aus den Teilströmen durch einen auf der Ausnutzung der Fliehkraft beruhenden Trennvorgang ein die erwünschten Stoffe enthaltender Gutstoffstrom und ein die unerwünschten Stoffe enthaltender Schlechtstoffstrom ("Spuckstoff") gebildet wird und anschließend die Gutstoffströme und die Schlechtstoffströme in je einem Sammelbereich vereinigt werden. Die Erfindung ist dadurch gekennzeichnet, daß die Aufteilung des Zulaufstromes der Stoffsuspension in Teilströme für alle Teilströme gleichzeitig vorgenommen und dabei schwingungsdämpfend auf die Stoffsuspension eingewirkt wird. |
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| 249 | Verfahren zur Regelung einer Flotationsanlage | EP90102757.3 | 1990-02-13 | EP0391042B1 | 1993-08-18 | Ortner, Herbert, Dr.; Pfalzer, Lothar, Dr. |
| 250 | IMPROVED WATER CLARIFYING APPARATUS | EP90911087.0 | 1990-06-04 | EP0532494A1 | 1993-03-24 | KROFTA, Milos |
| Water clarifying apparatus has a cylindrical tank where particulate contaminants suspended in raw water are separated using flotation techniques. A set of concentric mutually spaced, conical plates are positioned in the flotation tank. The plates rotate about the tank, preferably in unison with a (i) header that distributes equal quantities of raw water to each annular zone in the tank defined by the conical plates and (ii) a scoop for removing the contaminants which form a floated sludge layer. A screw conveyor is located in a discharge pipe of the floated sludge scoop. A infrared sludge detection array in a window in the side wall of the tank senses the sludge-water interface. Air dissolving tubes operating in parallel have common feeds and discharges coupled through three way valves operated to pressurize a closed volume of water with high pressure air in one tube while reloading and discharging the other tube. | ||||||
| 251 | Device for automatically adjusting the level of a pumping tank | EP83103066.3 | 1983-04-28 | EP0091600A3 | 1989-02-08 | Brandi, Alfredo |
In an automatic control device for the level in a pumping tank for treatment plants for turbid liquids containing fine solids in suspension, for example turbid water containing argillaceous mud and sand, the device utilising the residual return liquid from the treatment, a portion of the pipe for said return liquid is disposed horizontally at a predetermined level in said tank, and comprises mechanical or hydraulic means through which the residual return liquid is made to flow into the tank when the level therein falls below the predetermined level. |
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| 252 | OVERFLOW OUTLET FOR A CYCLONE SEPARATOR. | EP84902188 | 1984-06-01 | EP0145741A4 | 1988-03-28 | CARROLL NOEL |
| PCT No. PCT/AU84/00097 Sec. 371 Date Jan. 28, 1985 Sec. 102(e) Date Jan. 28, 1985 PCT Filed Jun. 1, 1984 PCT Pub. No. WO84/04702 PCT Pub. Date Dec. 6, 1984.A cyclone separator (10) having an elongated tapered separating chamber (25) with tangential inlet pipes (26, 28) thereto, and overflow outlet pipe (34) at the larger diameter end of the separating chamber, for outflow of a less dense component of a liquid mixture to be separated, and an underflow outlet (23) at the smaller diameter end of the separating chamber, for outflow of the denser component of the liquid mixture to be separated. The overflow outlet pipe (34) has an orifice (77) which is variably obstructable by a valve member (80) movable lengthwise of the pipe (34), to vary the flow rate through the outlet pipe (34). The degree of contamination of the denser liquid component emerging from the underflow outlet (23) is monitored by a detector (118) which is connected to a control circuit (108) which controls a motor (110). Motor (110) is coupled to valve member 80 whereby to move the valve member towards and away from the orifice (77), whereby to decrease the flow through outlet pipe (34) when the contamination level drops and to increase flow when the contamination level rises. A further control circuit (140) coupled to detector (118) is effective to control valves (102, 104) whereby to recycle the denser liquid component through the separator in the event that the contamination level is determined to be above a predetermined level. | ||||||
| 253 | OVERFLOW OUTLET FOR A CYCLONE SEPARATOR | EP84902188.0 | 1984-06-01 | EP0145741A1 | 1985-06-26 | CARROLL, Noel |
| PCT No. PCT/AU84/00097 Sec. 371 Date Jan. 28, 1985 Sec. 102(e) Date Jan. 28, 1985 PCT Filed Jun. 1, 1984 PCT Pub. No. WO84/04702 PCT Pub. Date Dec. 6, 1984.A cyclone separator (10) having an elongated tapered separating chamber (25) with tangential inlet pipes (26, 28) thereto, and overflow outlet pipe (34) at the larger diameter end of the separating chamber, for outflow of a less dense component of a liquid mixture to be separated, and an underflow outlet (23) at the smaller diameter end of the separating chamber, for outflow of the denser component of the liquid mixture to be separated. The overflow outlet pipe (34) has an orifice (77) which is variably obstructable by a valve member (80) movable lengthwise of the pipe (34), to vary the flow rate through the outlet pipe (34). The degree of contamination of the denser liquid component emerging from the underflow outlet (23) is monitored by a detector (118) which is connected to a control circuit (108) which controls a motor (110). Motor (110) is coupled to valve member 80 whereby to move the valve member towards and away from the orifice (77), whereby to decrease the flow through outlet pipe (34) when the contamination level drops and to increase flow when the contamination level rises. A further control circuit (140) coupled to detector (118) is effective to control valves (102, 104) whereby to recycle the denser liquid component through the separator in the event that the contamination level is determined to be above a predetermined level. | ||||||
| 254 | Plant for reclaiming waste concrete | EP82102875 | 1982-04-03 | EP0062339A3 | 1983-08-03 | BOZENHARDT, FRIEDRICH |
| 255 | DISSIMILAR MATERIALS SORTING PROCESS, SYSTEM AND APPARATUS | PCT/US2006041753 | 2006-10-24 | WO2007136403A3 | 2009-05-14 | VALERIO THOMAS A |
| An automated system for sorting dissimilar materials, and in particular for sorting plastics from other materials and for sorting different types of plastics from one another comprises, depending upon the embodiment, combinations of a sizing mechanism, a friction separation, an air separator, a magnetic separator, a dielectric sensor sortation bed, shaker screening, a ballistic separator, an inductive sensor sortation system and a float/sink tank. The dielectric sensor sortation system may be either analog or digital, depending upon the particular implementation. One or more float/sink tanks can be used, depending upon the embodiment, each with a media of a different specific gravity. The media may be water, or water plus a compound such as calcium chloride. In addition, multiples of the same general type of module can be used for particular configurations. A heavy media system or a sand float process can be used either alternatively or additionally. | ||||||
| 256 | DYCON GRAVITY MINERAL RECOVERY APPARATUS AND PROCESS | PCT/US2007016692 | 2007-07-25 | WO2008013835A3 | 2008-10-23 | BAUMMER GEORGE P |
| A gravity mineral recovery apparatus and process (10) uses stratification to separate the relatively heavier valuable particulates from the lighter tailings in ore (O). A housing (12) holds a process chamber (14) therein, the chamber (14) capable of oscillating within the housing (12). Ore (O) is gravity fed into the process chamber (14) and falls toward the bottom with the ore (O) channeled to the outer sidewall of the process chamber (14) by a deflector (46) that creates an annular passage within the chamber (14). The oscillation of the chamber (14) causes the heavier particulate to stratify into circumferentially disposed hoppers (62) while the tailings are discharged through a central chute (58) to a tailings hopper (96). The hoppers (62) have compound sloped sidewalls (64) and have a sensor (84) for opening a discharge valve (74) within the hopper (62) once a given concentration is achieved. A series of sensors (106, 108, 1 10, 1 12, 1 14) within the tailings hopper (96) control a tailings discharge valve (102) as well as an ore feed valve (94). Water (W) constantly flows through the system (10) yet does not participate in the actual transport of the particulates. | ||||||
| 257 | SYSTEMS AND METHODS FOR SORTING, COLLECTING DATA PERTAINING TO AND CERTIFYING RECYCLABLES AT A MATERIAL RECOVERY FACILITY | PCT/US2005024681 | 2005-07-12 | WO2006017282A3 | 2007-02-22 | BOHLIG JAMES W; DUFFY SEAN P |
| Systems and methods for collecting data pertaining to glass, plastic and/or paper composition within an input stream that includes recyclable material. The data collected can pertain, for example, to the weight and/or volume of the glass, plastic and/or paper within the input stream. The data can be certified for use a third party. | ||||||
| 258 | FLOAT-SINK METHOD TO DETERMINE BENEFICIATION PROSPECTS OF MINERALS | EP10801717.9 | 2010-11-15 | EP2501479B1 | 2018-05-02 | ASHIM, Kumar, Mukherjee; B K MISHRA |
| A method for separating particles of different specific gravity from a sized ore feed, wherein the ore can be coal, metallic, non-metallic and mineral ores. The method particles from the ore are sieved to obtain size fractions of different particle size ranges, after which a load of particles of a size fraction are placed in a container and fluidized by passing a fluid flow through the load of particles. By lowering the flow velocity of the fluid through the load the particles are deposited in the container in one or more layers depending on the specific gravity of each of the particles, after which the deposited particles are separated in portions of different specific gravity. The portions represent different ore content of the particles in each portion on basis of which the theoretical yield of the ore can be determined. The invention provides an apparatus to carry out the method. | ||||||
| 259 | DISSIMILAR MATERIALS SORTING PROCESS, SYSTEM AND APPARATUS | EP06836531 | 2006-10-24 | EP1960111A4 | 2013-11-20 | VALERIO THOMAS |
| An automated system for sorting dissimilar materials, and in particular for sorting plastics from other materials and for sorting different types of plastics from one another comprises, depending upon the embodiment, combinations of a sizing mechanism, a friction separation, an air separator, a magnetic separator, a dielectric sensor sortation bed, shaker screening, a ballistic separator, an inductive sensor sortation system and a float/sink tank. The dielectric sensor sortation system may be either analog or digital, depending upon the particular implementation. One or more float/sink tanks can be used, depending upon the embodiment, each with a media of a different specific gravity. The media may be water, or water plus a compound such as calcium chloride. In addition, multiples of the same general type of module can be used for particular configurations. A heavy media system or a sand float process can be used either alternatively or additionally. | ||||||
| 260 | FLOAT- SINK METHOD AND APPARATUS TO DETERMINE BENEFICIATION PROSPECTS OF MINERALS | EP10801717.9 | 2010-11-15 | EP2501479A1 | 2012-09-26 | ASHIM, Kumar, Mukherjee; B K MISHRA |
| A method for separating particles of different specific gravity from a sized ore feed, wherein the ore can be coal, metallic, non-metallic and mineral ores. The method particles from the ore are sieved to obtain size fractions of different particle size ranges, after which a load of particles of a size fraction are placed in a container and fluidized by passing a fluid flow through the load of particles. By lowering the flow velocity of the fluid through the load the particles are deposited in the container in one or more layers depending on the specific gravity of each of the particles, after which the deposited particles are separated in portions of different specific gravity. The portions represent different ore content of the particles in each portion on basis of which the theoretical yield of the ore can be determined. The invention provides an apparatus to carry out the method. | ||||||
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