EP3866945A1 - Rotary pressure filter module - Google Patents
Rotary pressure filter moduleInfo
- Publication number
- EP3866945A1 EP3866945A1 EP19723051.9A EP19723051A EP3866945A1 EP 3866945 A1 EP3866945 A1 EP 3866945A1 EP 19723051 A EP19723051 A EP 19723051A EP 3866945 A1 EP3866945 A1 EP 3866945A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- rotary pressure
- pressure filter
- sensor
- filter module
- assigned
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/06—Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/80—Accessories
- B01D33/804—Accessories integrally combined with devices for controlling the filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/06—Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums
- B01D33/073—Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums arranged for inward flow filtration
- B01D33/09—Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums arranged for inward flow filtration with surface cells independently connected to pressure distributors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/44—Regenerating the filter material in the filter
- B01D33/46—Regenerating the filter material in the filter by scrapers, brushes nozzles or the like acting on the cake-side of the filtering element
- B01D33/463—Regenerating the filter material in the filter by scrapers, brushes nozzles or the like acting on the cake-side of the filtering element nozzles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/44—Regenerating the filter material in the filter
- B01D33/46—Regenerating the filter material in the filter by scrapers, brushes nozzles or the like acting on the cake-side of the filtering element
- B01D33/466—Regenerating the filter material in the filter by scrapers, brushes nozzles or the like acting on the cake-side of the filtering element scrapers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/58—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element
- B01D33/60—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for washing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/58—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element
- B01D33/62—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying
- B01D33/66—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying by gases or by heating
- B01D33/663—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying by gases or by heating by direct contact with a fluid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/80—Accessories
- B01D33/801—Driving means, shaft packing systems or the like
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D37/00—Processes of filtration
- B01D37/04—Controlling the filtration
Definitions
- the invention relates to a rotary pressure filter module according to the preamble of claim 1.
- a rotary pressure filter comprises a filter housing in which a filter drum, which rotates about an axis of rotation by means of a rotary drive, is mounted. On its outer peripheral surface, the filter drum has a plurality of filter cells which are open towards the filter housing. At its axial ends, the filter drum is sealed off from the filter housing by glands.
- separating elements running parallel to the axis of rotation are provided in the filter housing, which divides the rotary pressure filter in the circumferential direction into a plurality of segment zones which are separated from one another in a pressure-tight manner and which perform different functions, in particular filtration, filter cake washing, filter cake drying, and filter cake discharge and filter cell preparation.
- the usual working pressure of such a rotary pressure filter is about 3 bar, for high-performance filters up to about 7 bar.
- the suspension to be filtered, the washing medium and the drying medium are supplied via corresponding supply lines which open into the filter housing, while the mother filtrate, the
- Washing filtrate and the drying medium takes place via discharge lines that start from the bottom of the filter cells.
- a first section of the discharge lines rotates with the filter drum and ends in a control head of the pressure rotary filter, where it merges into a second section fixed to the housing.
- the filter cake is usually discharged radially outward at ambient pressure through an opening in the filter housing, optionally supported by a scraper. Then the filter cloth, which depending on the application can be formed from a plastic or metal mesh, rinsed and pressed against the support grid of the filter cell.
- the filter cake can be washed in one or more stages.
- the segment zone assigned to the filter cake washing can be divided into one or more sub-zones.
- one or more feed lines for one or more washing media for example washing liquid, steam or the like, can be provided.
- the filter cake washing can also be preceded by pre-dehumidification.
- the rotary pressure filter of the rotary pressure filter module according to the invention also has this structure.
- Rotary pressure filters of the type described above are usually used as part of a superordinate production plant, in particular in the field of large chemicals, fine chemicals, pharmaceuticals and the food industry.
- Known rotary pressure filters have operating panels with display units for displaying the values of the process parameters monitored by the sensor devices, as well as input units for entering setpoints for the actuating devices influencing these process parameters.
- an operating panel does not form a “control device” in the sense of present invention, since it only forwards commands entered by an operator to the respective actuating devices.
- this central control device forms the process control level of the production system and determines the target values of the process parameters required for the operation of the rotary pressure filter module from the process parameters specified for the entire production system, transmits these to the associated actuating devices of the rotary pressure filter module and monitors their setting on the basis of the process parameters detected by the sensor devices.
- a rotary pressure filter module of the type mentioned at the outset in which the decentralized control device assigned to the rotary pressure filter is arranged on the rotary pressure filter or in its immediate vicinity and has a signal input via which it is associated with a rotary pressure filter module that is not part of the rotary pressure filter module central control device of a higher-level production system can be brought into a data exchange connection.
- the control device is arranged on the rotary pressure filter
- the control device is arranged within a hypothetical cuboid of minimal volume , in which the rotary pressure filter including its drive unit can still be accommodated, the main direction of which extends parallel to the axis of rotation of the filter drum, and the surface of which extends parallel to the surface on which the rotary pressure filter stands.
- the control device is arranged in the immediate vicinity of the rotary pressure filter
- the distance between the geometric center of the rotary pressure filter including its drive unit and the geometric center of the decentralized control device is at most equal to the length of the longest space diagonals of the hypothetical minimum cuboid mentioned above.
- a sensor device is “assigned” to a supply or discharge line, this does not necessarily mean that the sensor device is arranged in this line. Rather, it can also be arranged in a section of the rotary pressure filter into which this line opens or from which this line starts.
- the rotary pressure filter module is equipped with its own control device which, based on the entire production system, forms a decentralized control device which is designed and designed to relieve the central control device of the entire production system of control tasks relating to the rotary pressure filter.
- the central control device of the production system of the decentralized control device of the rotary pressure filter module only has to transmit an operating start signal in the simplest case, ie to switch on the rotary pressure filter module.
- the central control device of the production system can transmit further information to the decentralized control device of the rotary pressure filter module in addition to the operating start signal, for example information about the production specifications, in particular the type of suspension to be filtered, what amount of filter cake output and in what quality is expected from it as part of the entire production process and whether continuous operation or batch operation is expected from it.
- the decentralized control device can comprise an input unit which is designed to receive messages from the central control device in a data format containing this information.
- the data exchange connection can advantageously be a standardized data exchange connection, for example a data exchange connection as provided by an MTP (Module Type Package).
- MTP Module Type Package
- the decentralized control device determines the manipulated variables for the actuating devices on the basis of the data provided by the sensor devices, possibly taking into account the at least one information received from the central control unit.
- the decentralized control device can comprise a manipulated variable determination unit.
- the manipulated variable determination unit for transmitting the manipulated variables in the form of control signals to the actuating devices is connected to these actuating devices.
- the manipulated variable determination unit is designed to do that of to transmit the actuating variables determined to a monitoring unit, which forwards them to the actuating devices and is also designed to monitor compliance with the actuating variables determined on the basis of the detection signals received from the sensor devices and to output corrective control signals to the actuating devices if necessary.
- the manipulated variable determination unit can also be designed to determine the manipulated variables for the actuating devices not only in response to the operating start signal, but also during the ongoing operation of the rotary pressure filter module, and the determined manipulated variables continuously forward to the monitoring unit.
- the decentralized control device can also comprise an output unit which is designed to transmit information about the operation of the rotary pressure filter module to the central control device of the entire production system.
- the output unit can be connected to the manipulated variable determination unit and / or the monitoring unit. For example, if the manipulated variable determination unit should determine that the production specifications cannot be met or can only be met if the filter cake quality is limited, a corresponding warning message can be sent to the central control device of the production system.
- the sensor signals of the sensor devices do not need to be transmitted to the central control device of the production system, and the latter does not need to determine the control signals for the actuating devices and to transmit them to the actuating devices.
- the decentralized control device on the rotary pressure filter or in its immediate vicinity on a large number of data lines between the rotary pressure filter and the central central control device of the production plant can be dispensed with, and the central control device of the production plant can be relieved of a large number of tasks.
- the provision of a decentralized control device according to the invention makes it easier to integrate the rotary pressure filter into an existing production system.
- control program for the rotary pressure filter does not need to be integrated into the control program of the central control device of the production system, since the rotary pressure filter controls itself with the aid of its decentralized control device.
- the rotary pressure filter module according to the invention can also be integrated in production systems with a low-performance central control device, into which the rotary pressure filter has so far been impossible or difficult to integrate.
- the manipulated variable determination unit can be designed to determine the manipulated variables using a predetermined determination program.
- This determination program can comprise a plurality of subroutines, each of which is assigned to a predetermined suspension to be filtered and determines the manipulated variables as a function of the detection signals provided by the various sensor devices, not only the sensor devices already mentioned above, but also those below sensor devices to be discussed.
- the determination program can be structured in the manner of a predetermined decision tree.
- the determination program it is also possible for the determination program to access at least one multidimensional value table to determine the manipulated variables.
- Mixed forms are also conceivable.
- a decision tree could be used to determine which value table or which value tables should be accessed.
- the manipulated variable determining unit is preferably designed as a manipulated variable determining unit equipped with artificial intelligence, wherein the artificial intelligence can include, for example, at least one adaptive decision tree and / or at least one neural network, which are generated on the basis of training data.
- Adaptive decision trees have the advantage of requiring less training data than neural networks.
- Neural networks on the other hand, have the advantage of greater precision in determining the manipulated variables.
- decision trees can be combined with those of neural networks.
- one or more weak decision branches of a decision tree can be replaced by a neural network.
- the precision of decision trees can be increased by providing a decision forest, ie a plurality of, preferably randomly generated, decision trees that decide according to the majority principle.
- the decentralized control device can be equipped with artificial intelligence, it is possible to design the rotary pressure filter module as an autonomously operating unit that controls itself faster and more safely than a human being could.
- the artificial intelligence is able to take into account a much larger number of parameters, in particular acquisition data supplied by the sensor devices, for the control, to relate them to one another and to draw conclusions for the control of the pressure rotary filter, and this with additional consideration of production specifications through the central control device of the entire production plant. For example, fluctuating operating states, such as fluctuations in throughput and / or pressure and / or temperature and / or solids content and / or viscosity and / or particle size distribution, as well as the state of the rotary pressure filter, in particular its state of wear, can be taken into account.
- the artificial intelligence can generate “smart data” from the “big data” provided by the large number of sensor devices in order to enable optimized and safe operation of the rotary pressure filter.
- unforeseen downtimes or failures of the rotary pressure filter due to overstressing and / or slow, or even incorrect reactions to changes, such as those that occur particularly during the night shift can be reduced and the overall availability of the rotary pressure filter can be increased and maintenance costs can be reduced at the same time.
- the artificial intelligence can be designed as a static intelligence, which no longer adapts once it has been trained.
- artificial intelligence can preferably be used as adaptive artificial
- the decentralized control device can comprise a storage unit which is intended to store a parameter data set corresponding to the respective operating constellation at predetermined time intervals. It is also conceivable to store at least one parameter data set, preferably a plurality of such parameter data sets, which occurred on one or more structurally identical pressure rotary filter modules, in the memory unit already at the start of the startup of the pressure rotary filter module under consideration. As soon as the entire memory location of the memory unit is occupied with parameter data records, newly added parameter data records can overwrite already stored parameter data records, older parameter data records preferably being overwritten first.
- parameter data records stored in the memory unit it is possible to use artificial intelligence at predetermined time intervals, at to train once a day, for example.
- control unit comprises a communication unit which is designed to transmit parameter data sets, preferably in the context of an Internet-based application and / or by telecommunications, to a service center and there in a suitable database , for example a NoSQL database, in particular a document-oriented NoSQL database, such as a Mongo database, for example in csv data format.
- a suitable database for example a NoSQL database, in particular a document-oriented NoSQL database, such as a Mongo database, for example in csv data format.
- the service center can provide various services for the operator of the rotary pressure filter module as part of a customer portal:
- a copy of the artificial intelligence of the manipulated variable determination unit can be stored in a computer of the service center, which can be stored on the basis of the transmitted parameter data records, if desired Consideration of experiences made with other pressure rotary filters can be trained, so that the newly trained form of artificial intelligence only has to be fed back to the actuating variable determination unit of the pressure rotary filter.
- the ongoing operation of the rotary pressure filter does not have to be interrupted. Rather, only the updating of the manipulated variables monitored by the monitoring unit needs to be suspended by the manipulated variable determination unit during the time of the replay.
- the service center can evaluate the parameter data records in various ways. For example, key figures and correlations of certain process parameters can be determined, displayed with the aid of visualization tools, such as Tableau®, and made available to the operator of the rotary pressure filter module, preferably via an Internet-based customer portal, and, if desired, in a dashboard display are displayed.
- visualization tools such as Tableau®
- the operator of the rotary pressure filter module not only to monitor the productivity of the rotary pressure filter, but also to predict and thus flexibly plan maintenance intervals.
- the operator of the rotary pressure filter module can also be provided with information about the relationship between productivity and the length of the maintenance intervals.
- the operator of the rotary pressure filter module can also be informed of the effects on the consumption of operating media, such as washing and drying media.
- the parameter data records can be analyzed in the service center to determine whether a problem has occurred with the rotary pressure filter or is in the process of being initiated. This makes it possible, in particular, to make the maintenance intervals more flexible, for example to refill or replace lubricants and to replace wear parts, for example sealing elements, individually to the operation of the respective rotary pressure filter.
- the sensor devices and actuating devices of the rotary pressure filter can have a very wide variety of structures and functions. At this point it should be pointed out that the designation "First”, “second”, “third” etc. serve only to differentiate between the sensor devices and actuating devices and are due to the order in which they are named in the claims, but are not intended to indicate a hierarchy or any other arrangement of these devices. If the order of the names is changed, they could also be chosen differently.
- the first sensor device assigned to the first supply line for supplying the suspension to be filtered can have a flow rate sensor, for example a mass flow sensor and / and a volume flow sensor, or / and a pressure sensor or / and a temperature sensor and / and a solids content sensor and / and a density sensor or / and one Viscosity sensor and / or include a particle size distribution sensor.
- the fourth sensor device assigned to the first discharge line for discharging mother filtrate can comprise a conductivity sensor and / or a turbidity sensor and / or a pH value sensor.
- the second sensor device assigned to the second supply line for supplying washing medium can comprise a flow rate sensor, for example a mass flow sensor and / or a volume flow sensor, or / and a pressure sensor and / or a temperature sensor.
- a flow rate sensor for example a mass flow sensor and / or a volume flow sensor, or / and a pressure sensor and / or a temperature sensor.
- the fifth sensor device assigned to the second discharge line for discharging washing filtrate can comprise a conductivity sensor and / or a turbidity sensor and / or a pH value sensor.
- the third sensor device assigned to the third supply line for supplying drying medium can comprise a flow rate sensor, for example a mass flow sensor and / or a volume flow sensor, and / or a pressure sensor and / or a temperature sensor.
- the rotary pressure filter can comprise a cake thickness sensor in its drying zone. As can easily be seen, the thickness of the filter cake for a given rotational speed of the filter drum is a measure of the amount of filter cake produced.
- the cake thickness sensor can, for example depending on the material of the filter cake, be an optically and / or mechanically and / or capacitively operating sensor, for example a cake thickness sensor as described in the applicant's German patent application 10 2018 205 236.0, the latter of which the entire disclosure is hereby incorporated by reference.
- the rotary pressure filter can have a fourth discharge line for discharging the drying medium, to which a seventh sensor device can be assigned, for example a pressure sensor.
- this fourth discharge line can be connected to a separating device, which can be designed to separate the drying medium from a residual filtrate discharged from the filter cells.
- the sixth sensor device assigned to the third discharge line for removing filter cakes can comprise a residual moisture sensor.
- the residual moisture of the filter cake is a criterion for the quality of the filtration process. The lower the residual moisture of the filter cake, the better the previous filtration process.
- a scraper can also be arranged, which can be actuated by the supply of pressure medium, for example compressed gas, in particular compressed air.
- the pressure medium can be fed to the actuating device of the scraper via a fourth feed line, to which an eighth sensor device can be assigned, which can comprise, for example, a pressure sensor.
- the rotary pressure filter can comprise a fourth supply line for supplying blow-back medium, for example blow-back gas, in particular blow-back air, which is connected to the bottom of the filter cells.
- An eighth sensor device can be assigned to the supply line for supplying the blow-back medium, which can comprise a pressure sensor, for example.
- the rotary pressure filter can comprise a fifth supply line for supplying cloth rinsing medium, for example cloth rinsing liquid, which can be sprayed onto the filter cloth, for example, by means of a spray nozzle in order to detach any filter cake residues still adhering to it.
- a ninth sensor device can also be assigned to the supply line for supplying cloth rinsing medium, which can comprise, for example, a pressure sensor and / or a pressure flow quantity sensor, in particular a mass flow sensor and / or a volume flow sensor.
- the rotary pressure filter can comprise a sixth supply line for supplying blow-back medium, for example blow-back gas, in particular blow-back air, which is connected to the bottom of the filter cells.
- a tenth sensor device can be assigned to the supply line for supplying the blow-back medium, which can comprise a pressure sensor, for example.
- the rotary pressure filter can contain a seventh supply line for supplying contact medium, for example contact gas, in particular contact air, which is connected to the filter housing.
- An eleventh sensor device which may include a pressure sensor, for example, can be assigned to the supply line for supplying pressure medium.
- a pressure sensor for detecting the pressure prevailing in the filter cells can be provided in at least one segment zone of the rotary pressure filter.
- a twelfth sensor device can be assigned to the drive device of the rotary pressure filter, regardless of its exact structure, which can include, for example, a speed sensor and / or a drive power sensor and / and a torque sensor and / or a sensor for the current consumption by the drive device.
- respective adjusting devices can also be assigned to the fourth to seventh feed lines.
- All actuators can be a flow adjusting valve and / or one
- Supply adjustable pump can be formed.
- the sensor elements arranged between the filter drum and the filter housing can be assigned further sensor devices, which can each include a wear sensor, for example.
- the axial ends of the filter drum can be sealed off from the filter housing by sealing elements running in the circumferential direction.
- a sealing element running in the circumferential direction can be provided by a stuffing box, as is known, for example, from DE 101 57 297 A1 and DE 10 2007 002 931 A1 of the applicant, and / or from a slide and hose ring combination, as is known, for example DE 100 05 796 A1 is known to the applicant.
- an adjusting device can be assigned to such a sealing element.
- this readjusting device can be remotely operable by means of at least one power device and can comprise a sensor device which, for example, detects the actuating path by which the readjusting device has been adjusted by means of the at least one power device, and / or the contact pressure of the readjusting device.
- the pressure sensors can be arranged at different positions, for example on the innermost packing ring towards the packing shoulder and / or on the outside diameter of the packing space and / or at the contact point from the packing gland to the stuffing box packing.
- the wear of the separating elements extending parallel to the axis of rotation of the filter drum can be measured by means of an inductively operating sensor device, for example a wear sensor as described in the applicant's German patent application 10 2018 205 237.9, the disclosure of which in this regard is hereby incorporated by reference in its entirety.
- Further sensor devices can be assigned, for example, to the rotary bearing of the filter drum, which are usually designed as deep groove ball bearings or spherical roller bearings.
- a level sensor can be provided on the lubricant container of the rotary bearing. It is also conceivable to monitor the condition of the lubricant in the rotary bearing, in particular its moisture content, by means of a sensor based on infrared spectroscopy.
- the decentralized control device can be provided in a control cabinet arranged in the immediate vicinity of the rotary pressure filter. This has the advantage of better accessibility to the decentralized control device. It should also be added that the completeness of the ejection of the filter cake can also be recorded. This can be done, for example, directly, for example by means of an image evaluation of the filter cloth after the filter cake has been ejected, or indirectly, for example by detecting the degree of turbidity of the cloth rinsing medium.
- Figure 1 is a rough schematic representation of an inventive
- FIG. 2 shows a sectional view, taken orthogonal to the axis of rotation of its filter drum, of a rotary pressure filter as can be used in the rotary pressure filter module according to the invention
- Figure 4 is a schematic representation of the structure of a decentralized
- a pressure rotary filter module is generally designated 100 in FIG.
- the rotary pressure filter module 100 comprises a rotary pressure filter 200, which is also shown in FIGS. 2 and 3, and a control device 400, the schematic structure of which is shown in FIG. 4.
- the rotary pressure filter 200 comprises a filter housing 210 and a filter drum 212 rotating in the filter housing 210 about an axis of rotation A.
- the filter housing 210 comprises a housing jacket unit 214 with end rings 216.
- the housing jacket unit 214 is supported on a foundation (not shown) by means of a filter housing support 218 attached to the end rings 216.
- Bearing plates 220 which include rotor bearings 222, are fastened to the filter housing 210.
- the filter drum 212 is rotatably supported in the rotor bearings 222 by means of two end sections 224 and 226.
- the filter drum 212 comprises a rotor jacket unit 228.
- the rotor jacket unit 228 and the housing jacket unit 214 form an intermediate space 230 between them.
- This intermediate space 230 is divided by zone separating means 232 into intermediate zone zones Z1, Z2, Z3, Z4, also called segment zones, but in the following simply as “ Zone ”.
- the gap 230 is sealed at its axially spaced ends by sealing assemblies 234.
- the outside of the rotor shell unit 228 facing the intermediate space 230 is designed as a cell structure.
- This cell structure comprises filter cells 236 and 237.
- a filter means 238 is arranged in each filter cell 236, 237 and covers a discharge opening 240.
- the discharge openings 240 of a pair of filter cells 236, 237 are connected by a discharge line 242 running around the filter drum 212 to the core 244 of a control head 246 which also runs around the filter drum 212.
- the rotating core 244 is arranged on the end section 224 of the filter drum 212 in a rotationally fixed manner.
- the control head 246 also includes a stator 248, which is supported on the filter housing 210 against rotation and surrounds the core 244.
- Ring segment chambers 250 are formed in the stator 248, each of the ring segment chambers 250 corresponding in their circumferential length to the circumferential length of one of the zones Z1 to Z4. From the ring segment chambers 250 assigned to the zones Z1 to Z3, a stationary discharge line 252 leads to a respective collecting space (not shown), while the ring segment chamber 250 assigned to the zone Z4 can, as will be explained in more detail below, be connected to a supply line for blowback air.
- the filter drum 212 is driven by a gear unit 254.
- the gear unit 254 comprises a large gear 256 and a drive pinion 258.
- the drive pinion 258 is driven by an electric motor 260.
- the speed of the electric motor 260 is translated into slow speed by the gear unit 254, so that the filter drum 212 rotates at a speed of the order of 0.5 to 4 revolutions per minute.
- the direction of rotation is indicated by an arrow U in FIG.
- the zones Z1 to Z4 are shown roughly schematically as rectangles. The left side of these rectangles in FIG. 1 corresponds to the outer peripheral surface of the filter drum 212, while the right side in FIG. 1 corresponds to the radially inner side of the filter drum 212 connected to the discharge lines 242.
- the rotary pressure filter 200 described above works, for example, as follows:
- a feed fitting A1 of the rotary pressure filter 200 is connected to a feed line 302 for filtered material FG.
- the filter material FG can be, for example
- the filter material FG enters the filtering zone Z1 through the feed fitting A1 and spreads out there. How much filtering material FG reaches the filtering zone Z1 per unit of time is determined via a metering valve 304, which receives its control commands via a control signal line 402 from the decentralized control device 400.
- the feed line 302 can also be assigned further sensors which detect further properties of the filter material FG, for example a temperature sensor and / or a solid proportion sensor and / or a density sensor and / or a viscosity sensor and / and a particle size distribution sensor. These further sensors are represented in FIG. 1 by a sensor 310 and three points. Finally, the pressure arising in the filtering zone Z1 can also be detected via a pressure sensor 312.
- the liquid component of the filter material FG is pressed through the filter medium 238 of the cells 236, 237, so that the solids content in the feed spaces 266 accumulates radially outside the filter medium 238 as filter cake FK, and reaches the filter medium through the discharge openings 240 into the Discharge lines 242.
- the flow of filtrate is indicated in FIG. 3 by the arrows PM. If one imagines FIG.
- the circulating discharge lines 242 located in the filtering zone Z1 form a first section of a discharge line 314 assigned to the filtering zone Z1 (see FIG. 1), while the stationary discharge line 252 forms a second section of this discharge line 314.
- Various sensors can also be assigned to the discharge line 314, for example a conductivity sensor and / or a turbidity sensor and / or a pH value sensor, which are represented in FIG. 1 by the sensor 316 and three points.
- the cell group 236/237 passes from the filter zone as it passes the zone separating means 232 Z1 separated and comes in connection with the washing zone Z2, in which the filter cake FK is cleaned.
- a feed fitting A2 of the rotary pressure filter 200 is connected to a feed line 318 for washing medium WM, for example a washing liquid.
- the washing medium WM reaches the washing zone Z2 through the supply fitting A2 and spreads out there.
- How much washing medium WM reaches the washing zone Z2 per unit of time is determined via a metering valve 320.
- a pressure sensor 322 and a flow rate sensor 324 are also assigned to the feed line 318.
- the washing medium WM penetrates the filter cake FK and the filter medium 238 in order to then pass through the respective discharge opening 240 into the respective discharge line 242.
- the discharge lines 242 of all filter cells 236, 237 which are currently connected to the zone Z2 in the snapshot according to FIG. 2, are connected to a (not shown) stationary discharge line by a ring segment chamber (not shown) with a stationary discharge line (also not shown).
- Washer fluid collection container supplied which can be followed by a separation stage in order to separate the washed-out liquid constituents from the cake from the washing liquid and to be able to use the washing liquid for a new washing process.
- the circumferential discharge lines 242 each located in the washing zone Z2 form a first section of a discharge line 326 assigned to the washing zone Z2, while the stationary discharge line (not shown) forms a second section of this discharge line 326.
- Various sensors can also be assigned to the discharge line 326, for example a conductivity sensor and / or a turbidity sensor and / or a pH value sensor, which are represented in FIG. 1 by the sensor 328 and three points.
- the cell group 236/237 is separated from the washing zone Z2 as it passes the zone separating means 232 and comes into connection with the drying zone Z3, which serves to dry the filter cake FK washed in the washing zone Z2.
- a supply fitting A3 of the rotary pressure filter 200 is connected to a supply line 330 for drying medium TM, for example drying air.
- the drying medium TM enters the drying zone Z3 through the feed fitting A3 and spreads out there.
- a metering valve 332 determines how much drying medium TM reaches the drying zone Z3 per unit of time.
- a pressure sensor 334 and a flow rate sensor 336 are also assigned to the feed line 330.
- the drying medium TM passes through the filter cake FK and the filter medium 238 and can in turn reach the control head 246 through the respective discharge opening 240 and the associated discharge line 242.
- drying medium TM is fed to a further (not shown) ring segment chamber of the stator 248 and can escape from it into the atmosphere through a stationary discharge line (also not shown), which together form a discharge line 338, or can be fed to a separating device 340, in which the liquid components discharged from the drying medium TM from the filter cake FK can be separated.
- At least one further sensor 344 for example an oxygen partial pressure sensor, can also be assigned to the discharge line 338 and / or the separating device 340.
- a cake thickness sensor 346 can also be provided in the drying zone Z3.
- the filter cake FK can be ejected via a discharge line 348, preferably designed as an ejection chute.
- the discharge chute 348 is at least one quality sensor
- a possible quality sensor 349 can be designed, for example, as a residual moisture sensor.
- the ejection of the filter cake FK can be facilitated by an ejection scraper 262 which can be inserted into the filter cells 236, 237 by means of a fluidic, preferably pneumatic, force device (not shown) and later withdrawn from the latter.
- a fluidic, preferably pneumatic, force device (not shown) and later withdrawn from the latter.
- the supply line for actuating fluid leading to this power device is shown in FIG.
- blow-back gas preferably blow-back air
- the blow-back gas can be supplied via a feed line 356, which is at least partially formed by the lines 242 arranged in the ejection zone Z4.
- a feed valve 358 and a pressure sensor 360 are in turn assigned to the feed line 356.
- a washing nozzle 268 can also be provided in the ejection zone Z4, by means of which any filter cake residues in the cells 236, 237 can be washed out of the latter.
- the washing nozzle 268 can be connected to a supply line 362 for filter cloth rinsing medium, which in turn can be assigned a metering valve 364, a pressure sensor 366 and a flow rate sensor 368.
- the filter cloth cleaning can also be supported by blow-back gas.
- the blow-back gas can be supplied via a feed line 370 which is at least partially formed by the lines 242 arranged in the ejection zone Z4.
- the feed line 370 are in turn assigned a metering valve 372 and a pressure sensor 374.
- a turbidity sensor 271 can also be assigned to the discharge line 270 for filter cloth rinsing medium, the degree of turbidity being used as a measure of the completeness of the discharge of the filter cake FK.
- the filter medium 238, for example the filter cloth is placed against the bottom of the respective filter cell or a support grid (not shown) provided there by a gas surge.
- the gas for this gas surge can be supplied via a supply line 376, which in turn can be assigned a metering valve 378 and a pressure sensor 380.
- At least one further sensor can also be assigned to the drive motor 260, for example a speed sensor and / and a drive power sensor and / and a torque sensor and / or a sensor for the current consumption by the drive device 260.
- the at least one further sensor is in FIG. 1 by the sensor 382 and three points are shown.
- sensors for example wear sensors, can be assigned to the sealing devices of the rotary pressure filter 200, that is to say the sealing assemblies 234 formed by stuffing box packings and the zone separating elements 232.
- a sensor can be provided which detects the fill level in a storage container for lubricant, for example lubricant for the rotor bearings 222, and / or a sensor for detecting the moisture content of the lubricant. All of these sensors are indicated in FIG. 1 by sensor 384.
- a metering pump can be provided instead of one or more of the metering valves.
- the decentralized control device 400 comprises a monitoring unit 406, which is connected via an input unit 408 and an output unit 410 to a central control device (not shown), which is part of a higher-level production system in which the rotary pressure filter module 100 is integrated .
- the monitoring unit 406 serves to monitor the compliance with manipulated variables that have been transmitted to it by a manipulated variable determination unit 412. It does this by outputting corresponding control signals via the signal line 402 to the metering valves 304, 320, 332, 352, 356, 364, 372 and 378 (hereinafter referred to collectively as “metering valves 414” for the sake of simplicity) and the reaction to this which you from the sensors 306, 308, 310, 316, 322, 324, 328, 334, 336, 342, 344, 346, 349, 354, 360, 366, 368, 374, 380, 382 and 384 (hereinafter the For the sake of simplicity, collectively transmitted detection signals referred to as “sensors 416”) are monitored.
- the manipulated variable determination unit 412 determines the manipulated variables on the basis of the production specifications received from the central control device of the production plant via the input unit 408, taking into account the detection signals received from the sensors 416, which have been forwarded to them by the monitoring unit 406.
- the production process For example, information about the type of material FG to be filtered, the amount of filter cake FK to be ejected per unit of time, the quality of the filter cake FK to be ejected and the like may be included.
- the manipulated variable determination unit 412 can determine the manipulated variables using artificial intelligence, preferably a continuously learning artificial intelligence.
- the artificial intelligence can advantageously comprise at least one adaptive decision tree and / or at least one neural network which can be generated on the basis of training data which are stored in a storage unit 418.
- the training data stored in the storage unit 418 may already have been stored there when the rotary pressure filter module 100 was first put into operation and, for example, may have been recorded on other rotary pressure filter modules of identical construction. However, it is also possible to record training data 100 during operation of the rotary filter arrangement and to store it in the storage unit 418. In this case, artificial intelligence learns from the experiences it has made. When storing new training data, it may be necessary to overwrite older training data.
- the continuity of learning does not have to be permanent or stepless continuity. Rather, it is also possible to train the artificial intelligence again and again only at predetermined time intervals. In addition, the training of artificial intelligence need not be taken over by the decentralized control device 400 itself. Rather, it is also conceivable to transmit all the data required for the training to a remote service center by means of a transmission unit 420, in which the artificial intelligence of the control variable determination unit 412 is mirrored, to carry out the training and the trained system on this “mirror system” play back to the decentralized control device 400.
- the decentralized control device 400 can, for example, take on the following further tasks: Should the decentralized control device 400 determine, on the basis of the detection signals from the sensors 416 and the setting options of the metering valves 414, that the production specifications made by the central control device of the production system do not or Only if the ejected filter cake FK is reduced in quality or quantity, or if an increased, in particular an economically unacceptably high, consumption of operating resources, for example washing medium WM, can be met, can it issue a corresponding warning message to and from the central control device of the production system Request corrected production specifications.
- the decentralized control device 400 makes suggestions to the central control device of the production plant as to which production specifications could be met, taking into account a predetermined cost-benefit efficiency.
- the decentralized control device 400 makes a prediction based on the detection signals transmitted by the wear sensors 384 based on a locking model, which can also be based, for example, on artificial intelligence, when the next maintenance should be carried out at the latest, for example lubricant refilled or seals should be replaced.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtration Of Liquid (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102018218907.2A DE102018218907A1 (en) | 2018-11-06 | 2018-11-06 | Rotary pressure filter module |
PCT/EP2019/061345 WO2020094262A1 (en) | 2018-11-06 | 2019-05-03 | Rotary pressure filter module |
Publications (1)
Publication Number | Publication Date |
---|---|
EP3866945A1 true EP3866945A1 (en) | 2021-08-25 |
Family
ID=66476611
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19723051.9A Withdrawn EP3866945A1 (en) | 2018-11-06 | 2019-05-03 | Rotary pressure filter module |
Country Status (7)
Country | Link |
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US (1) | US20210387116A1 (en) |
EP (1) | EP3866945A1 (en) |
JP (1) | JP2022504113A (en) |
KR (1) | KR20210083277A (en) |
CN (1) | CN112996582B (en) |
DE (1) | DE102018218907A1 (en) |
WO (1) | WO2020094262A1 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE542326C2 (en) * | 2018-06-21 | 2020-04-14 | Valmet Oy | Vacuum filter |
CN113599867B (en) * | 2021-08-25 | 2022-08-12 | 北京科技大学 | Micro-fine particle viscous material filter-pressing dehydration process detection control device and method |
CN114405156B (en) * | 2022-01-26 | 2023-04-28 | 中国神华能源股份有限公司哈尔乌素露天煤矿 | Control method and control system of coal slime water pressure filter |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
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US3839203A (en) * | 1973-06-18 | 1974-10-01 | C Jackson | Demonstration filter liquid control circuit |
US5096611A (en) * | 1989-05-25 | 1992-03-17 | Globe-Union Inc. | Process for the production of battery paste |
WO1999015255A1 (en) * | 1997-09-19 | 1999-04-01 | Baker Hughes Incorporated | Method and apparatus for monitoring, controlling and operating rotary drum filters |
DE10005796B4 (en) | 2000-02-10 | 2011-02-17 | Bhs-Sonthofen Gmbh | Rotary filter system |
US6800197B1 (en) * | 2000-10-12 | 2004-10-05 | Genencor International, Inc. | Continuously operable rotating drum pressure differential filter, method and systems |
US20050051473A1 (en) * | 2001-06-12 | 2005-03-10 | Wolfgang Suss | Rotating filter system |
DE10157297A1 (en) | 2001-11-22 | 2003-06-05 | Bhs Sonthofen Maschinen & Anlagenbau Gmbh | Sealing cord, a sealing packing comprising a plurality of such sealing cords |
JP2006192343A (en) * | 2005-01-12 | 2006-07-27 | Mitsubishi Heavy Industries Food & Packaging Machinery Co Ltd | Operation method of filter apparatus for bottle-washing machine, and filter apparatus for bottle-washing machine |
DE102007002931A1 (en) | 2007-01-19 | 2008-07-24 | Bhs-Sonthofen Gmbh | Sealing arrangement and sealing device, in particular as an accessory and / or spare part for such a seal arrangement |
DE102009045198A1 (en) * | 2009-09-30 | 2011-04-21 | Bhs-Sonthofen Gmbh | Rotary filter arrangement with mechanical cake compaction |
CN201534023U (en) * | 2009-10-17 | 2010-07-28 | 兰州瑞德干燥技术有限公司 | Filtering, washing and drying integrated continuous pressure filter |
EP2520348A1 (en) * | 2011-05-02 | 2012-11-07 | Siemens Aktiengesellschaft | Filter device, method for its operation and usage |
EP2522414A1 (en) * | 2011-05-11 | 2012-11-14 | Siemens Aktiengesellschaft | Filter device, method for its operation and usage |
US10866028B2 (en) * | 2017-11-08 | 2020-12-15 | Anderson Industries, Llc | Telematics system for rotary vacuum drum drying system |
DE102017221088A1 (en) | 2017-11-24 | 2019-05-29 | Bhs-Sonthofen Gmbh | Device for tensioning a stuffing box packing |
DE102018205237A1 (en) | 2018-04-06 | 2019-10-10 | Bhs-Sonthofen Gmbh | Apparatus and method for detecting wear of a separator |
DE102018205236A1 (en) | 2018-04-06 | 2019-10-10 | Bhs-Sonthofen Gmbh | Apparatus and method for measuring a filter cake thickness |
-
2018
- 2018-11-06 DE DE102018218907.2A patent/DE102018218907A1/en not_active Withdrawn
-
2019
- 2019-05-03 US US17/290,952 patent/US20210387116A1/en not_active Abandoned
- 2019-05-03 EP EP19723051.9A patent/EP3866945A1/en not_active Withdrawn
- 2019-05-03 CN CN201980072849.0A patent/CN112996582B/en not_active Expired - Fee Related
- 2019-05-03 WO PCT/EP2019/061345 patent/WO2020094262A1/en unknown
- 2019-05-03 KR KR1020217013333A patent/KR20210083277A/en not_active Application Discontinuation
- 2019-05-03 JP JP2021518145A patent/JP2022504113A/en not_active Withdrawn
Also Published As
Publication number | Publication date |
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JP2022504113A (en) | 2022-01-13 |
WO2020094262A1 (en) | 2020-05-14 |
CN112996582A (en) | 2021-06-18 |
DE102018218907A1 (en) | 2020-05-07 |
CN112996582B (en) | 2022-04-26 |
US20210387116A1 (en) | 2021-12-16 |
KR20210083277A (en) | 2021-07-06 |
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