US20180236386A1 - Cleaning method, control apparatus and connecting device - Google Patents
Cleaning method, control apparatus and connecting device Download PDFInfo
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- US20180236386A1 US20180236386A1 US15/522,960 US201515522960A US2018236386A1 US 20180236386 A1 US20180236386 A1 US 20180236386A1 US 201515522960 A US201515522960 A US 201515522960A US 2018236386 A1 US2018236386 A1 US 2018236386A1
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- Prior art keywords
- filter
- cleaning
- section
- connecting device
- openings
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- B01D46/002—
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
- B01D46/04—Cleaning filters
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- B01D46/0068—
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
- B01D46/58—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in parallel
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/66—Regeneration of the filtering material or filter elements inside the filter
- B01D46/70—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter
- B01D46/71—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter with pressurised gas, e.g. pulsed air
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- B01D46/0065—
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/42—Auxiliary equipment or operation thereof
- B01D46/4272—Special valve constructions adapted to filters or filter elements
Definitions
- This invention relates to a cleaning method for cleaning of a filter in sections according to the preamble of claim 1 , a control apparatus for executing a cleaning method according to the preamble of claim 14 , a connecting device for connecting a filter to a cleaning device according to the preamble of claim 15 , a cleaning device for cleaning of a filter according to the preamble of claim 34 , a filter system with a filter and a cleaning device for cleaning the filter according to the preamble of claim 42 , and an installation, in particular for coating processes, with an installation housing, a filter and a cleaning device for cleaning of the filter according to the preamble of claim 46 .
- cleaning method in this invention is defined as all methods, procedures and processes by means of which the cleaning of a filter, of a filter system and/or of an installation before, during and/or after filtration by means of the filter is planned, analyzed, implemented, coordinated and/or adjusted or controlled.
- Cleaning methods are necessary in many installations and/or filter systems in order to clean fouled or clogged filters.
- the filter sections are cleaned in cleaning processes separated from one another by fixed or constant time intervals. In doing so it can happen that the filter or one of the filter sections is being cleaned, although this is not yet necessary at the time of cleaning.
- a filter cake which forms on the filter can be cleaned off or removed too early or too late by means of the cleaning. Accordingly additional and avoidable costs are also associated with such a cleaning method.
- connecting device in this invention is preferably a structural apparatus, in particular for filter systems, cleaning devices and/or installations, for example as an adapter or intermediate piece which is preferably made to fluidically connect a filter to a cleaning device.
- a connecting device is made to direct a medium, in particular a fluid of the cleaning device, to the filter which is preferably connected to the cleaning device.
- cleaning device in this invention is defined preferably as a device which is made to clean an assigned filter, preferably pneumatically or by means of compressed air, preferably particles in or on the filter and/or a filter cake of the filter which has formed or is forming on the filter being removed partially or completely from the filter.
- cleaning devices generate a pressure pulse, in particular at least essentially against that flow direction which prevails in the filter in filtration by means of the filter. Cleaning devices are used both during continuing operation of the filter or of the filter system (online operating mode) and also when the operation of the filter or of the filter system is being interrupted (offline operating mode).
- filter system in this invention is defined preferably as a system which has at least one filter and at least one cleaning device for cleaning of the filter.
- the filter of a filter system is preferably made to remove and filter solids/particles of a fluid from the fluid within the scope of filtration.
- the separation of the particles of the fluid to be cleaned takes place by a filter medium of the filter, within the filter medium and/or by means of a filter cake which has formed or is forming on the filter medium.
- filters are especially surface filters, such as filter cartridges or filter hoses which are made in particular to separate particles of a gas or raw gas by means of cake filtration and/or filter-medium filtration.
- installation in this invention is defined in particular as industrial installations and/or process-engineering installations. In this invention they are preferably coating installations for coating of a product with a layer. In particular installations according to this definition are made to coat pharmaceutical products such as pellets. Preferably the coating takes place by means of fluidized bed processes, in particular the product to be coated being fluidized as a fluidized bed. Preferably installations according to this definition have a filter system with a filter and a cleaning device for cleaning of the filter, in particular to separate particles such as dust from a raw gas during the coating process and/or to supply them again to the coating process.
- Cleaning devices are necessary in many methods to clean fouled or clogged filters.
- Current cleaning devices, filter systems and/or installations have cleaning devices which are spaced 3-dimensionally apart from assigned filters such that during filtration the cleaned medium or the clean gas can escape from the filter, in particular from the filter outlet of the filter.
- DE 298 23 965 U1 and EP 1 507 579 B1 disclose compressed air pulse injector systems which for cleaning and regeneration of individual filter cartridges by means of compressed air are located and spaced above the filter and for cleaning purposes blow compressed air first into the space surrounding the compressed air pulse injector systems and then into the respective filter cartridge. Based on the distance between the outlet of the cleaning device and the filter cartridge to be cleaned at the time, high flow losses arise which can lead to the respective filter cartridges, in particular in the neck region, not being completely cleaned and/or having to be cleaned very often or repeatedly.
- the object of this invention is to devise a cleaning method for cleaning of a filter as well as a control apparatus for executing a cleaning method for cleaning of a filter which enables or supports improved, reliable, efficient and/or economical cleaning of the filter and/or filtration by means of the filter and/or the number of cleaning processes is minimized. Furthermore the object of this invention is to devise a connecting device in particular for connecting a filter to a cleaning device, a cleaning device, a filter system and an installation, as a result of which a compact construction and/or reliable, efficient, economical, low-maintenance and low-loss cleaning of the filter or of a filter section of the filter is enabled or supported.
- One aspect of this invention lies in that the filter sections are cleaned within one cleaning cycle in cleaning processes which are separated in time from one another and the cleaning method has at least two cleaning cycles, both one time interval between the cleaning processes within the respective cleaning cycle and also one time interval between the end of one of the cleaning cycles and the start of a following one of the cleaning cycles being changed.
- the cleaning method cleans the filter altogether more reliably, efficiently and/or economically.
- the filter has at least three filter sections, the filter sections being cleaned in cleaning processes separated by time intervals from one another and the time intervals between successive cleaning processes being changed.
- the time intervals between the cleaning processes within the respective cleaning cycle and also the time intervals between the end of one of the cleaning cycles and the start of a following one of the cleaning cycles is changed by means of feedback control.
- This enables preferably complete automation of the suggested cleaning method, in particular reliable, efficient and/or economical cleaning of the filter and/or filtration by means of the filter being achieved.
- the feedback control adjusts a differential pressure between one filter inlet and one filter outlet of the filter and/or a differential pressure between one filter inlet and one filter outlet is used as the controlled variable in the feedback control. This advantageously makes it possible to change the time intervals depending on the differential pressure by means of the feedback control.
- the differential pressure or the system deviation is filtered with a control filter, preferably with a lowpass characteristic and/or such that peaks and/or fluctuations of the differential pressure caused by one or more cleaning process are at least essentially suppressed or filtered. This ensures that the cleaning method is quiet and/or stable.
- the time intervals between the cleaning processes within one cleaning cycle are constant or are kept at a constant value. In this way the complexity of the cleaning method is reduced and the number of possible fault sources is minimized.
- One suggested control apparatus is made to execute the suggested cleaning method, preferably the control apparatus being made to determine using at least one pressure sensor a differential pressure between a filter inlet and a filter outlet of the filter, and/or to trigger a valve to initiate a cleaning process.
- the control apparatus being made to determine using at least one pressure sensor a differential pressure between a filter inlet and a filter outlet of the filter, and/or to trigger a valve to initiate a cleaning process.
- a connecting device has one side wall which borders an internal cross section which increases along one longitudinal axis of the connecting device and has openings laterally with assigned major axes, the major axes of the openings running obliquely to the side wall and pointing from outside to inside in the direction of one internal cross section which is greater than an internal cross section into which the respective opening discharges.
- the suggested connecting device enables a direct connection of the filter to the cleaning device and/or a support of the cleaning device both during the cleaning and also during the filtration.
- the medium with which the filter is being cleaned, during and/or for cleaning travels from the cleaning device via the connecting device directly to the filter, while the medium cleaned by means of the filter or the clean gas can escape from the filter through the openings of the connecting devices from the inside to the outside. Consequently it is not necessary to replace, change or three-dimensionally move the connecting device for the respective operation of the filter.
- the openings which run obliquely to the side wall preferably reduce flow losses both during cleaning and also during filtration.
- the manner of construction of the connecting device preferably and advantageously increases the mass flow and/or the pressure of the medium with which the filter is being cleaned and/or reduces the risk of possible flow detachment on the side wall of the connecting device during cleaning.
- the openings of the connecting device are oriented at one or more planes which is or are aligned orthogonally to the longitudinal axis of the connecting device. This ensures economical production of the connecting device and enables the side wall of the connecting device to be provided with as many openings as possible, in particular without the connecting device losing stability.
- the side wall has a section free of openings in the region of the greatest internal cross section.
- a suggested cleaning device for cleaning of a filter preferably has the suggested connecting device in order to connect the filter to the cleaning device. In this way the already explained advantages can be achieved.
- a suggested filter system with a filter and a cleaning device for cleaning of the filter preferably has the suggested connecting device for connection of the filter to the cleaning device.
- a suggested installation, in particular for coating processes, with an installation housing, a filter and a cleaning device for cleaning of the filter preferably has the suggested connecting device.
- the installation has an installation housing which in the interior has a storage apparatus which is made to supply the cleaning device with a medium with which the filter is being cleaned, in particular compressed air.
- a storage apparatus which is made to supply the cleaning device with a medium with which the filter is being cleaned, in particular compressed air.
- the installation housing internally has a valve for initiating a cleaning process.
- the valve preferably connects the storage apparatus to the connecting device, in particular fluidically and/or on one end facing away from the filter or end with reduced internal cross section of the connecting device.
- FIG. 1 shows a schematic section of a suggested installation with a suggested filter system, a suggested connecting device and a suggested cleaning device;
- FIG. 2 shows a perspective view of a suggested connecting device
- FIG. 3 shows a schematic section of a suggested filter system with the connecting device, a valve in the closed state and a filter shown in sections;
- FIG. 4 shows a schematic section of the filter system according to FIG. 3 with the valve in the opened state
- FIG. 5 shows a schematic plan view of the suggested filter system as well as a suggested cleaning device with a storage apparatus and several control apparatus;
- FIG. 6 shows a schematic side view of a suggested installation with a suggested filter system, a first filter section of the filter being cleaned;
- FIG. 7 shows a schematic side view of the installation according to FIG. 6 , a second filter section of the filter being cleaned
- FIG. 8 shows a schematic block diagram of a feedback control underlying a suggested cleaning method
- FIG. 9 shows a schematic of the pressure as a function of time in the suggested cleaning method according to a first version of the method.
- FIG. 10 shows a schematic of the pressure as a function of time in the suggested cleaning method according to a second version of the method.
- the installation 1 shown in FIG. 1 is preferably made to carry out coating processes.
- the installation 1 is a fluidized bed coating installation for the production of pellets (not shown) or for pelletizing within the scope of preferably pharmaceutical production.
- the installation 1 preferably has an installation housing 2 with a housing inlet 3 and a housing outlet 4 .
- the installation housing 2 is made as a reactor. Especially preferably the pelletizing or coating/production of the pellets takes place within the installation housing 2 .
- the installation housing 2 is or can be divided into an inlet air region 5 , spray region 6 , filter region 7 and dome region/clean gas region 8 .
- the housing inlet 3 is preferably fluidically connected to an inlet air system (not shown) which is made to supply the installation 1 or the installation housing 2 , in particular the inlet air region 5 , with inlet air 9 , in particular the inlet air 9 being conditioned by means of the inlet air system for the coating.
- inlet air system not shown
- the inlet air region 5 is separated from the spray region 6 by means of a perforated bottom 10 .
- inlet air 9 is directed or guided through the perforated bottom 10 from the inlet air region 5 into the spray region 6 .
- the installation 1 preferably has a suspension tank 11 which in the interior contains a suspension 12 or another fluid for the coating process.
- the suspension 12 is preferably supplied to the installation housing 2 by means of a suspension pump 13 via a suspension line 14 and/or pumped into the installation housing 2 .
- nozzles 15 which are made to atomize the suspension 12 in the installation housing 2 , in particular in the spray region 6 and/or to apply it to the pellets (not shown), preferably the pellets being fluidized within the scope of the fluidized bed coating process and/or moving as a fluidized bed in the spray region 6 .
- the nozzles 15 are each located in a pipe, in particular in a Wurster pipe 16 .
- the pellets are preferably routed past the nozzles 15 in the Wurster pipe 16 and sprayed or coated with the suspension 12 by means of the nozzles 15 .
- the pellets in the Wurster pipe 16 are routed or blown upward or against gravity by means of the inlet air 9 .
- the pellets drop preferably in the direction of the perforated bottom 10 and/or with gravity. In this way the pellets are coated along an at least essentially ellipsoidal path in the installation housing 2 .
- the illustrated embodiment is in particular a bottom spray version, preferably the nozzles 15 pointing up. But other embodiments or arrangements in the installation 1 and/or in the installation housing 2 are also possible.
- the filter system 17 preferably has a connecting device 18 which is made to connect a filter 19 assigned to the filter system 17 to a cleaning device 20 which is likewise assigned to the filter system 17 .
- the connecting device 18 can be part of the filter 19 or of the cleaning device 20 or connected hereto or can be implemented separately.
- the filter 19 preferably a particle filter, is preferably located within the installation housing 2 , in particular above the spray region 6 and/or in the filter region 7 and/or in the region of the housing outlet 4 . But other arrangements and/or designs are also possible.
- the filter 19 preferably separates the spray region 6 from the dome region 8 , in particular in a gas-permeable and/or particle-retaining manner.
- the filter 19 has several filter sections 21 and/or is and/or can be divided into several filter sections 21 .
- the filter sections 21 are spaced three-dimensionally apart from one another and/or are made as separate units of the filter 19 .
- the filter sections 21 are quite especially preferably made as elongated, tubular and/or cylindrical surface filters, in particular as filter cartridges 22 which project preferably from the dome region 8 into the filter region 7 .
- a medium to be filtered flows through the filter cartridge 22 during the filtration by means of the filter 19 from the outside to the inside, as shown in FIG. 1 .
- the surface of the filter section 21 or of the filter cartridge 22 is made as the filter inlet 24 and the inside of the filter section 21 or of the filter cartridge 22 indicated by broken lines is made as the filter outlet 25 .
- part of the suspension 12 which does not adhere to the pellets is carried preferably as dust, in particular as a suspension dust or raw gas 23 , from the spray region 6 into the filter region 7 .
- the filter 19 is made in particular to filter the dust-laden air or raw gas 23 and then to direct it as clean gas 26 —preferably by means of the connecting device 18 —into the dome region 8 and/or to the housing outlet 4 .
- the filter 19 and/or individual filter sections 21 clogs increasingly with particles, in particular the suspension dust, during filtration of the raw gas 23 .
- the cleaning device 20 is preferably made to clean the filter 19 .
- the cleaning device 20 is made to remove the dust of the suspension 12 or other particles from the filter 19 and/or from the filter surface and/or to convey it, in particular blow it, from the filter region 7 into the spray region 6 .
- the cleaning device 20 is not active or no cleaning is taking place.
- the cleaning device 20 is located at least partially or completely in the installation 1 , in particular in the installation housing 2 .
- the cleaning device 20 is located in the dome region 8 and/or on the clean gas side or above the filter 19 or individual filter sections 21 . But other arrangements are also possible.
- the cleaning device 20 preferably has one storage apparatus 28 , in particular the storage apparatus 28 being made to supply the cleaning device 2 Q with a medium, in particular compressed air.
- the storage apparatus 28 is located at least partially, preferably completely, within the installation housing 2 .
- the storage apparatus 28 is especially preferably located in the dome region 8 and/or above the filter 19 .
- the installation 1 , the filter system 17 and/or the cleaning device 20 has or have a control apparatus 29 .
- the control apparatus 29 is made in particular to control or regulate the cleaning device 20 and/or the cleaning of the filter 19 .
- control apparatus 29 is located preferably outside the installation housing 2 . But other arrangements are also possible.
- the installation 1 , the filter system 17 , the cleaning device 20 and/or the control apparatus 29 has or have at least one pressure sensor 30 , in particular the pressure sensor 30 being made to determine and/or measure a differential pressure DP.
- the differential pressure DP is preferably the difference between two static pressures, dynamic pressures, or total pressures of a fluid.
- the differential pressure DP is the difference of the preferably static pressure of the raw gas 23 and of the preferably static pressure of the clean gas 26 .
- the differential pressure DP is determined and/or measured between the filter inlet 24 and the filter outlet 25 , between the dome region 8 and one of the other regions of the installation housing 2 and/or between the housing inlet 3 and housing outlet 4 by means of the pressure sensor 30 .
- control apparatus 29 controls or regulates a valve 31 which is assigned in particular to the cleaning device 20 and/or the filter system 17 depending on the differential pressure DP and/or according to the suggested cleaning method.
- valve 31 at a time is assigned to each filter section 21 or to each filter cartridge 22 and/or one filter section 21 or one filter cartridge 22 at a time is fluidically connected to one valve 31 , especially preferably by means of the respective connecting device 18 .
- a valve 31 is fluidically connected to several filter sections 21 .
- the installation 1 , the filter system 17 , the cleaning device 20 and/or the control apparatus 29 is or are made to determine and/or measure the differential pressure DP with one or more pressure sensors 30 and/or to trigger the valve or valves 31 to clean the filter 19 .
- the installation 1 , the filter system 17 , the cleaning device 20 and/or the control apparatus 29 is or are made to carry out a suggested cleaning method which is explained later in the description.
- a dust layer in particular a filter cake 32 , forms on the surface of the filter 19 , in particular of the filter sections 21 .
- the mass or the volume, in particular the thickness, and/or the density of the filter cake 32 increases during the filtration and/or during operation of the installation 1 .
- the differential pressure DP likewise rises.
- the differential pressure DP is at least essentially a function of the mass, of the volume, and/or of the density of the filter cake 32 and/or the differential pressure DP correlates, in particular positively, with the mass, the volume and/or the density of the filter cake 32 .
- the control apparatus 29 controls or adjusts the valve or valves 31 preferably such that the valve or valves 31 open and/or compressed air or some other medium is blown or directed out of the storage apparatus 28 through the valves or valves 31 and/or through the connecting device 18 into the filter 19 and/or into one of the filter sections 21 .
- the differential pressure DP drops by and/or during the cleaning of the filter 19 and/or of one of the filter sections 21 .
- FIG. 2 shows a perspective view of the connecting device 18 .
- the connecting device 18 is made to connect the filter 19 (not shown in FIG. 2 ) to the cleaning device 20 (not shown), the connecting device 18 having one side wall 33 which borders an internal cross section Q which increases along a longitudinal axis L and has openings 34 with assigned major axes H.
- the connecting device 18 preferably has at least two, in particular at least 50, especially preferably at least 100, and/or at most 1000, especially at most 500, quite especially preferably at most 400 openings 34 .
- the connecting device 18 is or can be divided into at least two, preferably three regions or sections.
- the openings 34 are located in a first section 35 of the connecting device 18 .
- the connecting device 18 has a second section 36 free of openings.
- the second section 36 is free of openings and/or is closed laterally along the longitudinal axis L.
- the second section 36 preferably directly and/or continuously borders the first section 35 and/or forms with it an interruption-free or continuous flow wall.
- the second section 36 has the internal cross section Q which increases along the longitudinal axis L and/or the greatest internal cross section Q 1 at least in part.
- each internal cross section Q of the second section 36 is greater than one of the internal cross sections Q of the first section 35 .
- the second section 36 extends preferably to at least 10%, especially preferably to at least 20%, in particular to at least 30% and/or to at most 70%, especially preferably to at most 60%, in particular to at most 50%, of the length or height of the connecting device 18 .
- the connecting device 18 and/or the side wall 33 has or have preferably a third section 37 , preferably the third section 37 having a constant, in particular cylindrical internal cross section Q.
- the third section 37 preferably directly borders the first section 35 , preferably on one side of the first section 35 facing away from the second section 36 .
- the first section 35 , the second section 36 and/or the third section 37 are preferably tightly connected or made integral.
- the internal cross section Q of the third section 37 is smaller than the internal cross section Q of the second section 36 and/or smaller than or equal to the preferably smallest internal cross section Q 2 of the first section 35 .
- the internal cross section Q of the third section 37 is the smallest internal cross section Q 2 of the connecting device 18 .
- first section 35 and/or the third section 37 has or have the smallest internal cross section Q 2 of the connecting device 18 .
- a width or a diameter of the smallest internal cross section Q 2 is greater than 33 mm and/or smaller than 70 mm, preferably at least essentially equal to 50.8 mm (2 inches), and/or a width or a diameter of the smallest internal cross section Q 2 is more than 20%, preferably more than 30%, and/or less than 60%, preferably less than 50%, of a diameter or a width of the greatest internal cross section Q 1 of the connecting device 18 .
- the ratio of the surface of the filter section 21 assigned to the connecting device 18 or of the filter cartridge 22 assigned to the connecting device 18 at the least or to the internal cross section Q 2 of the connecting device 18 bordering the cleaning device 20 is an especially dimensionless characteristic K.
- a Filter being the surface of the filter section 21 assigned to the connecting device 18 or of the filter cartridge 22 assigned to the connecting device 18
- Q being the smallest internal cross section Q 2
- d filter being the inside or outside diameter of the filter section 21 or of the filter cartridge 22
- L Filter being the length or height of the filter section 21 or of the filter cartridge 22 and d Q being the diameter or the width of the smallest and of the internal cross section Q 2 or of the one bordering the cleaning device 20 .
- the characteristic K can be computed accordingly for different filter geometries.
- the ratio of the surface of the filter section 21 assigned to the connecting device 18 or of the filter cartridge 22 assigned to the connecting device 18 at the least or of the internal cross section Q 2 of the connecting device 18 bordering the cleaning device 20 and the characteristic K is greater than 200, in particular greater than 250, and/or less than 3000, in particular less than 2500.
- the internal cross section Q is preferably a (maximum) internal cross sectional area perpendicular to the longitudinal axis L of the connecting device 18 or a hydraulic cross section or a hydraulic cross sectional area.
- the internal cross section Q is the area enclosed or bordered by the side wall 33 of the connecting device 18 .
- the connecting device 18 has at least one connecting apparatus, in particular a flange union 38 or a clamp union 39 , in particular the connecting apparatus being made to connect the connecting device 18 to the filter 19 and/or the cleaning device 20 , the valve 31 and/or the storage apparatus 28 by form-fit, force-fit and/or by bonding.
- a connecting apparatus in particular a flange union 38 or a clamp union 39 , in particular the connecting apparatus being made to connect the connecting device 18 to the filter 19 and/or the cleaning device 20 , the valve 31 and/or the storage apparatus 28 by form-fit, force-fit and/or by bonding.
- the connecting device 18 in particular the connecting apparatus(es) of the connecting device 18 , is/are made preferably to connect the connecting device 18 to the filter 19 , the connecting device 18 to the cleaning device 20 , and/or the filter 19 to the cleaning device 20 , especially in an immovable, holding, supporting and/or rigid manner.
- the connecting device 18 on the two axial ends has one connecting apparatus each, as shown in FIG. 2 .
- the connecting apparatus(es) is/are preferably made as a flange, clamp connection and/or screwed pipe joint and/or are located on opposite axial ends of the connecting device 18 , in particular are formed integrally therewith.
- the connecting device 18 preferably on the axial end of the second section 36 —has a flange union 38 and—preferably on the axial end of the third section 37 —a clamp union 39 .
- a flange union 38 and—preferably on the axial end of the third section 37 —a clamp union 39 .
- two axial ends of the connecting device 18 have a flange union 38 or clamp union 39 as connecting apparatus.
- the connecting apparatus or connecting apparatuses can be made both as groove unions or collar unions.
- the flange union 38 is made preferably as a collar union and the clamp union 39 is made preferably as a groove union.
- the connecting apparatus has a groove 40 , preferably the groove 4 Q being made to hold a seal 41 .
- the outside diameter of the connecting apparatus is preferably larger than the outside diameter of the bordering section of the connecting device 18 .
- the outside diameter of the flange union 38 is greater than the maximum or bordering outside diameter of the second section 36 and/or the outside diameter of the clamp union 39 is greater than the maximum or bordering outside diameter of the first section 35 and/or of the third section 37 .
- the internal cross section Q of the connecting device 18 is made at least essentially circular. But other designs are also possible, in particular in which the internal cross section Q is made at least oval, rectangular or square.
- the connecting device 18 and/or the side wall 33 preferably borders the internal cross section Q with one inside 42 of the side wall 33 .
- the inside 42 runs conically along the longitudinal axis L—at least in the first section 35 and/or in the second section 36 —and/or has an at least essentially straight contour.
- the inside 42 is shaped bell-like, is bell-shaped or in the form of a diverging Laval nozzle section.
- the inside 42 of the side wall 33 is made at least essentially concave and/or convex.
- the internal cross section or the pitch of the internal cross section Q or of the inside 42 along the longitudinal axis L or an angle enclosed between the longitudinal axis L and a tangent of the side wall 33 decreases.
- the first section 35 has an internal cross section Q which increases more dramatically along the longitudinal axis L than the second section 36 .
- the connecting device 18 in particular the side wall 33 , has an outside 43 , and preferably the profile or the contour of the outside 43 can be made independent of the inside 42 .
- the outside 43 has an external cross section A which increases along the longitudinal axis L.
- the outside 43 runs along the longitudinal axis L at least essentially parallel to the inside 42 . But other approaches are also possible.
- outside 43 at least in the first section 35 and/or second section 36 —is at least essentially straight and/or the outside 43 has an at least essentially conical contour or one which is arched in the longitudinal direction or is bell-like. But other designs are also possible here.
- FIG. 3 shows a schematic section of the connecting device 18 together with the valve 31 in the closed state and with one part of one of the filter sections 21 .
- the transition between the first section 35 and second section 36 and/or between the second section 36 and third section 37 is/are preferably at least essentially continuous. Especially preferably the inside 42 at least in the first section 36 and/or in the second section 37 is made continuous.
- outside 43 at least in the first section 35 and in the second section 36 —is made straight and/or conical. But other designs are also possible here.
- the thickness of the side wall 33 and/or the difference between the internal cross section Q and the external cross section A increases along the longitudinal axis L and/or with increasing internal cross section Q.
- the internal cross section Q increases along the longitudinal axis L with a first angle W 1 which is greater than 5° and/or less than 20°, preferably at least essentially is equal to 12°, in particular an imaginary extension or tangent of the inside 42 including the first angle W 1 with the longitudinal axis L.
- the major axes H of the openings 34 run obliquely to the side wall 33 , in particular to the inside 42 of the side wall 33 .
- FIG. 3 shows only the major axis H of one opening 34 .
- the following explanations however apply preferably to the major axes H of the other openings 34 accordingly.
- the major axes H point from the outside to the inside in the direction of an internal cross section Q which is greater than an internal cross section Q into which the respective opening 34 discharges.
- the major axes H point from the outside to the inside in the direction of greatest internal cross section Q 1 and/or intersect a plane imagined through the greatest internal cross section Q 1 .
- the major axes H point from the outside to the inside in the direction of the filter 19 , as shown in FIG. 3 .
- the major axes H of the openings 34 intersect the longitudinal axis L at a second angle W 2 and/or the major axes H with the longitudinal axis L in a longitudinal sectional view of the connecting device 18 , as shown in FIG. 3 , include a second angle W 2 , preferably the second angle W 2 being less than 90°, preferably at least essentially equal to 45°.
- the inside 42 includes with the major axis H, in particular in the region of the respective mouth of the opening 34 , a third angle W 3 , in particular preferably the third angle W 3 being less than 90° and/or greater than the first angle W 1 and/or the second angle W 2 .
- the openings 34 are preferably oriented and/or located in one or more planes E, in particular the planes E being aligned at least essentially orthogonally to the longitudinal axis L of the connecting device 18 , as illustrated in FIG. 3 using two planes E.
- the planes E are each defined by at least three openings 34 .
- at least three openings 34 lie and/or discharge in one of the planes E.
- each opening 34 is or can be assigned to one of the planes E.
- the planes E along the longitudinal axis L are arranged—preferably at least essentially equidistantly—offset to one another and/or parallel to one another. But other designs or arrangements are also possible.
- the number of openings 34 per plane E increases preferably with increasing internal cross section Q along the longitudinal axis L.
- the ratio of all cross sections of the openings 34 of one plane E to the internal cross section Q into which the openings 34 of the plane E discharge remains constant at least essentially along the longitudinal axis L.
- the openings 34 at least along the internal cross section Q into which the respective openings 34 discharge, and/or in a plane E—are arranged at least essentially circularly and/or form several concentric circles along the longitudinal axis L.
- the openings 34 alternatively or additionally are arranged in a latticed manner or form a latticed structure.
- the major axes H of the openings 34 of one of the planes E preferably have one common intersection point, in particular the intersection point lying on the longitudinal axis L.
- the openings 34 are arranged uniformly distributed preferably along the longitudinal axis L—at least in the first section 35 —and/or over the respective internal cross section Q.
- the openings 34 in the respective plane E are equidistantly offset to one another and/or arranged rotationally symmetrically to one another.
- the openings 34 are made as a hole and/or have a circular cross section. But other geometries are also possible, in particular the openings 34 having an angular, in particular rectangular cross section and/or being made as a slot, cylindrical, rotationally symmetrical and/or axially symmetrical to the respective major axis H.
- the openings 34 have a diameter and/or a width which is more than 2% and/or less than 20%, preferably at least essentially equal to 10% of the diameter and/or of the width of the greatest internal cross section Q 1 .
- the openings 34 each have at least essentially the same diameter and/or the same width. But other designs are also possible, in particular in which the diameter and/or the width of the openings 34 per and/or in one plane E and/or along the longitudinal axis L varies.
- the openings 34 have a diameter and/or a width of at least 5 mm and/or at most 40 mm, in particular of at least essentially 20 mm.
- the cross section of the mouth or the cross sectional area of all openings 34 is together or cumulated preferably more than 2% or 5%, in particular more than 8% or 10%, especially preferably more than 12%, and/or less than 50% or 40%, in particular less than 30% or 20%, quite especially preferably less than 15%, of the area of the inside 42 and/or outside 43 .
- the openings 34 are preferably made elongated and/or tubular, preferably with a length which is greater than the diameter and/or the width of the openings 34 .
- the internal cross section Q tapers in the direction of the cleaning device 20 and/or of the valve 31 and/or increases in the direction of the filter 19 and/or of the filter sections 21 .
- the suggested cleaning device 20 preferably has the connecting device 18 and/or is or can be connected to it.
- the valve 31 which is preferably assigned to the cleaning device 20 and/or is an integral part of the cleaning device 20 , is fluidically connected to the connecting device 18 , as shown in FIG. 3 .
- the valve 31 is preferably made as an axial valve, as shown for example in FIG. 3 . But other designs are also possible.
- valve 31 is or can be driven pneumatically, hydraulically and/or electrically.
- valve 31 is preferably driven pneumatically, in particular by means of compressed air of the storage apparatus 28 (not shown).
- the valve 31 preferably has a piston 44 , preferably the piston 44 being movable axially and/or in the direction of the longitudinal axis L.
- valve 31 is in the closed state.
- the piston 44 is pretensioned by means of a spring 46 or some other tensioning element.
- the valve 31 preferably has a valve chamber 47 .
- the pressure of a medium in the valve chamber 47 is or can be adjusted or controlled by means of the control apparatus 29 (not shown).
- valve 31 opens when the pressure in the valve chamber 47 is greater than the pressure produced by the spring 46 .
- the filter 19 shown in FIG. 3 or one of the filter sections 21 of the filter 19 preferably has one manifold 48 with several holes 49 .
- the manifold 48 is jacketed in particular by a filter cloth 50 .
- the filter cloth 50 is preferably made to retain or filter particles of a certain size, in particular the initially described suspension dust.
- the filter cake 32 forms on the manifold 48 and/or the filter cloth 50 .
- the arrows shown in FIG. 3 schematically illustrate the preferred flow direction in the filter 19 and in the connecting device 18 during filtration by means of the filter 19 .
- the arrows illustrate only schematically the flow direction; any turbulence, eddies, detachments and/or other flow phenomena remain ignored.
- the medium to be cleaned flows through the filter section 21 at least essentially from the outside to the inside or in the radial direction to the longitudinal axis L.
- Flow through the connecting device 18 takes place during filtration by means of the filter 19 in the second section 36 preferably at least essentially axially or along the longitudinal axis L.
- the flow in the first section 35 during filtration is diverted such that it flows from the inside to the outside through the openings 34 .
- Flow through the connecting device 18 and/or the openings 34 takes place preferably at least essentially from the inside to the outside during filtration and/or the connecting device and/or openings are made for flow through them to take place from the inside to the outside during filtration.
- the suggested filter system 17 is made to direct a medium, preferably the clean gas 26 , from the inside or one side facing the filter 19 to the outside or to one side facing away from the filter 19 through the openings 34 .
- the connecting device 18 is made in particular to accelerate a medium, in particular the clean gas 26 , during filtration. Especially preferably the connecting device 18 acts as a nozzle or convergent tube during filtration.
- FIG. 4 shows a schematic section of the connecting device 18 and of the filter 19 shown by way of an extract or of one of the filter sections 21 according to FIG. 3 together with the valve 31 in the opened state.
- the installation 1 , the cleaning device 20 and/or the control apparatus 29 is or are made to at least essentially reverse the flow direction through the connecting device 18 , in particular through the openings 34 , and/or through the filter 19 , in particular through one of the filter sections 21 , preferably by means of opening and closing of the valve 31 .
- FIG. 4 shows the cleaning of one of the filter sections 21 or the partial cleaning of the filter 19 .
- the connecting device 18 and/or the cleaning device 20 is or are preferably made to retard a medium, in particular compressed air from the storage apparatus 28 (compare FIG. 1 ) during and/or for cleaning—in particular in the direction of increasing internal cross section Q—and/or to raise the static pressure of the medium, in particular of the compressed air of the storage apparatus 28 —at least in the connecting device 18 .
- the openings 34 are made to direct or suction another medium, in particular the clean gas 26 , from the outside to the inside during and/or for cleaning.
- the connecting device 18 and/or the cleaning device 20 is or are made to increase the mass flow of a medium, preferably of the compressed air of the storage apparatus 28 and/or to suction a second medium, preferably the clean gas 26 —in particular through the and/or by means of the openings 34 .
- the connecting device 18 acts preferably during and/or for cleaning as a diffusor.
- the action of the connecting device 18 depends on the flow direction through the connecting device 18 .
- flow takes place through the connecting device 18 and/or the filter 19 , in particular one of the filter sections 21 , during and/or for cleaning in one direction which is preferably opposite at least essentially the flow direction which prevails during and/or for filtration by means of the filter 19 .
- the connecting device 18 is made as a supercritical diffusor and/or the internal cross section Q increases along the longitudinal axis L with a first angle W 1 greater than 8°.
- the openings 34 are in particular made—at least during and/or for cleaning—to prevent and/or reduce flow separation, in particular at and/or on the inside 42 of the connecting device 18 .
- the connecting device 18 at least during cleaning—there is an at least essentially laminar flow and/or the connecting device 18 is made to enable a laminar flow or to support the formation of a laminar flow.
- FIG. 5 shows a schematic plan view of the suggested filter system 17 as well as of the suggested cleaning device 20 with the storage apparatus 28 as well as one or more, in particular synchronized, the control apparatus 29 which are made preferably to control the valves 31 and/or to measure one or more differential pressures DP assigned to the filter sections 21 .
- the storage apparatus 28 is preferably made to supply the cleaning device 20 with a medium, in particular compressed air. Especially preferably the storage apparatus 28 is assigned to the filter system 17 and/or to the cleaning device 20 and/or is a component of the filter system 17 and/or of the cleaning device 20 .
- the installation housing 2 has at least in part in the interior the storage apparatus 28 or the storage apparatus 28 is located at least essentially within or in the interior of the installation housing 2 .
- the storage apparatus 28 is made both in the interior of the installation housing 2 and also outside of the installation housing 2 .
- the storage apparatus 28 optionally has one or more storage units 51 , as shown in FIG. 5 , preferably the storage units 51 being located outside the installation housing 2 .
- the storage apparatus 28 can be supplied from the outside with medium or compressed air, in particular by fluid connections between the storage unit(s) 51 and/or a compressor and the interior which is formed or surrounded by the storage apparatus 28 . But it is also otherwise possible to supply compressed air or a medium to the storage apparatus 28 .
- the storage apparatus 28 has in particular a ring reservoir 52 which is located in the interior of the installation housing 2 .
- the storage apparatus 28 and/or the ring reservoir 52 is made at least essentially as a ring or is made ring-shaped.
- the storage apparatus 28 and/or the ring reservoir 52 extends in the upper region of the installation housing 2 , in particular in the dome region 8 , and/or above the filter system 17 or the filter 19 . But other designs or arrangements are also possible.
- the storage apparatus 28 is made as a gas reservoir, in particular as a reservoir for compressed air and/or as a line network, in particular as a gas line network, especially preferably as a compressed air line network.
- the storage apparatus 28 is made to uniformly distribute and/or deliver a medium, in particular compressed air, to the valves 31 and/or to the filter system 17 .
- the storage apparatus 28 is made to supply several filter sections 21 of the filter 19 with a medium, in particular compressed air, individually and/or separated in time.
- the storage apparatus 28 in particular the ring reservoir 52 , has at least two pipe segments 53 and/or is made of several pipe segments 53 .
- the pipe segments 53 are connected to one another or made integral preferably by force-fit, form-fit and/or bonding, in particular by welding.
- the pressure of the medium in the storage apparatus 28 is preferably more than 1 bar, in particular more than 2 bar, and/or less than 10 bar, in particular less than 8 bar, especially preferably less than 4 bar.
- the volume of the storage apparatus is preferably more than 50 l, in particular more than 100 l, especially preferably more than 200 l, and/or less than 1000 l, in particular less than 800 l, especially preferably less than 500 l. This has been found to be advantageous in conjunction with a compact construction and good cleaning performance.
- the storage apparatus 28 in particular the ring reservoir 52 , is fluidically connected to the valve 31 and/or the connecting device 18 .
- valve 31 is located in the interior of the installation housing 2 , in particular within the storage apparatus 28 and/or between the storage apparatus 28 and the connecting device 18 .
- the storage apparatus 28 preferably the ring reservoir 52 , is made to protect the valve 31 against an explosive atmosphere and/or to prevent direct contact of the valve 31 with an explosive atmosphere, in particular direct contact of the installation housing 2 and/or of the dome region 8 .
- the installation housing 2 , the cleaning device 20 and/or the storage apparatus 28 has or have several lines for supply of the cleaning device 20 , of the storage apparatus 28 , in particular of the ring reservoir 52 , and/or of the valve 31 with a medium, in particular compressed air.
- the storage apparatus 28 is preferably supplied by means of a compressed air line 54 and/or the valve 31 is supplied by means of a control air line 55 .
- the control air line 55 is preferably made to alternately open or close the valve 31 .
- the control apparatus 29 controls or adjusts the valve 31 by means of the control air line 55 .
- the pressure in the control air line 55 is greater than the pressure in the compressed air line 54 .
- the installation housing 2 has preferably several penetrations 56 , in particular the compressed air line 54 and/or the control air line 55 being routed through the penetration 56 from the outside to the inside into the installation housing 2 .
- control apparatus 29 is made to control the valve 31 for cleaning of the filter 19 , in particular of one of the filter sections 21 .
- the installation 1 , the filter system 17 and/or the cleaning device 20 preferably has or have several control apparatus 29 , preferably one control apparatus 29 at a time controlling or adjusting at least two valves 31 .
- the cleaning method is executed preferably by means of the installation 1 , the filter system 17 , the connecting device 18 , the cleaning device 20 and/or the control apparatus 29 .
- FIGS. 6 and 7 show the installation 1 , the filter system 17 , the connecting device 18 , the cleaning device 20 and the control apparatus 29 as the suggested cleaning method is being carried out.
- the filter system 17 or the filter 19 is cleaned in sections or partially during the cleaning method.
- the filter system 17 or the filter 19 has at least two, preferably at least three, in particular at least four, filter sections 21 , in particular filter cartridges 22 , by means of a cleaning process 57 one of the filter sections 21 or one of the filter cartridges 22 at a time being cleaned, as shown in FIGS. 6 and 7 .
- the filter sections 21 are cleaned in cleaning processes 57 which are offset to one another or separated in time from one another.
- the filter sections 21 are cleaned in cleaning processes 57 separated from one another by a time interval T 1 .
- a cleaning process 57 is completely finished or ended before a further cleaning process 57 starts.
- the cleaning method has at least two cleaning cycles 58 .
- the end of one cleaning cycle 58 is separated in time by a time interval T 2 from the start of a following cleaning cycle 58 .
- the (second) cleaning cycle 58 which follows a (first) cleaning cycle 58 is the (second) cleaning cycle 58 which directly follows the (first) cleaning cycle 58 , in particular between the end of the (first) cleaning cycle 58 and the start of the (second) cleaning cycle 58 or during the time interval T 1 and/or T 2 no cleaning process 57 being triggered or carried out.
- the filter system 17 or the filter 19 has especially preferably at least three filter sections 21 , the filter sections 21 being cleaned in cleaning processes 57 separated from one another by time intervals T 1 .
- a cleaning process 57 and/or a cleaning cycle 58 is triggered by opening the assigned valve 31 , preferably one valve 31 being assigned to one filter section 21 or filter cartridge 22 at a time or one filter section 21 at a time being cleanable by opening of the corresponding valve 31 .
- the filtration is continued during cleaning of one of the filter sections 21 by means of the other filter sections 21 .
- the method are also possible, in particular in which filtration is stopped or adjusted during the cleaning process 57 .
- FIG. 6 shows the cleaning of a first filter section 21 or a first filter cartridge 22 , in particular compressed air being directed from the storage apparatus 28 through the assigned valve 31 and the suggested connecting device 18 into the filter section 21 or the filter cartridge 22 , in particular by the valve 31 being opened.
- another medium, in particular the clean gas 26 is directed into the filter section 21 or the filter cartridge 22 , as is indicated by arrows in FIG. 6 and FIG. 7 .
- FIG. 7 shows the cleaning process 57 of another, second filter section 21 or another filter cartridge 22 .
- filter sections 21 adjacent to one another are cleaned in cleaning processes 57 offset in time from one another, as shown by means of FIG. 6 and FIG. 7 .
- the sequence in which the filter sections 21 are cleaned remains identical in each cleaning cycle 58 .
- other versions of the method are also possible, in particular in which the sequence in which the filter sections 21 are being cleaned is varied with each cleaning cycle 58 .
- one cleaning cycle 58 in one cleaning cycle 58 first those filter sections 21 are cleaned which have the greatest distance to the compressed air line 54 .
- the time interval T 1 between the cleaning processes 57 , in particular within the respective cleaning cycle 58 , and/or the time interval T 2 between the end of one of the at least two cleaning cycles 58 is or are changed.
- time intervals T 1 between successive cleaning processes 57 in the cleaning method are changed.
- the feature that “two cleaning processes 57 follow one another” should preferably be understood such that no further cleaning process 57 takes place between the two successive cleaning processes 57 .
- the filter 19 has at least three filter sections 21 , in the cleaning method the time interval T 1 between the successive cleaning process 57 of a first and a second filter section 21 and the time interval T 2 between the successive cleaning processes 57 of the second and a third filter section 21 are each changed.
- time interval T 1 and/or the time interval T 2 is or are changed by means of feedback control 59 and/or feedback control 59 is carried out in the suggested cleaning method and causes a change or variation of the time intervals T 1 and T 2 .
- FIG. 8 shows in this regard a schematic block diagram of the feedback control 59 underlying the suggested cleaning method or of the feedback control circuit of the feedback control 59 .
- the differential pressure DP between the filter inlet 24 and the filter outlet 25 is adjusted and/or used as a controlled variable 60 in the feedback control 59 .
- a rated differential pressure SP as a reference variable 61 is specified in particular exogenously to the feedback control 59 .
- the rated differential pressure SP is preferably more than 1000 Pa, in particular more than 2000 Pa, especially preferably more than 3000 Pa, and/or less than 7000 Pa, in particular less than 6000 Pa, especially preferably less than 5000 Pa. Quite especially preferably the rated differential pressure SP is at least essentially 4000 Pa.
- the rated differential pressure SP in the cleaning process is kept constant. But other versions of the method are also possible in which the rated differential pressure SP is changed.
- the difference between the rated differential pressure SP and the differential pressure DP is used as the system deviation 62 in the feedback control 59 and/or in the cleaning method.
- the feedback control 59 and/or the cleaning method uses or use preferably one controller, in particular a PID controller 63 . But it is also possible to use other controllers in the feedback control 59 and/or in the cleaning method.
- the triggering of a cleaning process 57 and/or the opening of the valve 31 or of one of the valves 31 or the length of the time interval T 1 and/or T 2 is preferably used as a manipulated variable 64 in the feedback control 59 and/or in the cleaning method.
- the controller is preferably made to determine the manipulated variable 64 by means of the system deviation 62 , in particular the system deviation 62 multiplied by a factor being integrated and/or derived over a fixed time.
- the cleaning method and/or the feedback control 59 preferably uses the filter system 17 and/or the cleaning device 20 , preferably together with the storage apparatus 28 as the controlled system 65 .
- one influencing quantity 66 acts on the cleaning method and/or the feedback control 59 , in particular on the controlled system 65 .
- possible influencing quantities 66 include the increasing clogging or fouling of the filter 19 , in particular of the filter sections 21 , and/or the formation or increase of the filter cake 32 , the degree of dust loading of the raw gas 23 , the flow velocity in the installation housing 2 , quantity and quality of the suspension 12 supplied to the installation housing 2 and/or quantity and quality of the inlet air 9 supplied to the installation housing 2 .
- the differential pressure DP and or the system deviation 62 is preferably filtered with a control filter 67 , preferably with a lowpass characteristic and/or such that peaks or fluctuations of the differential pressure DP caused by a cleaning process 57 and/or the cleaning processes 57 of one cleaning cycle 58 are at least essentially suppressed and/or filtered.
- the time interval T 1 between two successive cleaning processes 57 and/or the time interval T 2 between two successive cleaning cycles 58 with several cleaning processes 57 each is each determined by feedback control 59 which preferably has the control filter 67 .
- the control filter 67 is preferably made or designed such that both the pressure peaks which are produced by the respective cleaning process 57 , in particular by feed of compressed air, and also pressure deviations based on the differential pressure DP which has changed after the completion of a cleaning process 57 are smoothed and/or averaged.
- control filter 67 has a three-dB corner frequency or critical frequency of one preferred lowpass characteristic which is smaller than 1/(2 ⁇ time constant), the time constant preferably being greater than the minimum time interval T 1 , the minimum time interval T 2 and/or greater than 1 s, preferably greater than 2 s or 4 s, in particular greater than 5 s.
- the time constant is preferably smaller than the sum of the time intervals T 1 of the cleaning processes 57 of one cleaning cycle 58 , less than 30 s, preferably less than 25 s, especially preferably less than 20 s or 15 s.
- the control filter 67 can however have a filter characteristic other than a lowpass characteristic, its being preferred that it is made to smooth deviations of the differential pressure DP which have been caused by cleaning processes 57 .
- the differential pressure DP or the difference between the differential pressure DP and rated differential pressure SP in the sense of this invention is then regarded as smoothed when the deviations caused by or in a cleaning process 57 are reduced or damped by more than 10%, preferably more than 20%, in particular more than 30% or 40%.
- the feedback control 59 is designed such that the control filter 67 damps frequencies above 10 Hz, preferably above 5 Hz, in particular above 2 Hz or 1 Hz, by more than 50%.
- FIG. 9 shows a schematic of the pressure P as a function of the time T in the suggested cleaning method according to a first version of the method.
- the illustrated cleaning method preferably five filter sections 21 are cleaned by means of one cleaning process 57 at a time in one cleaning cycle 58 , the time intervals T 1 between the cleaning processes 57 being changed each time.
- time intervals T 1 between the cleaning processes 57 become smaller with increasing clogging or fouling of the filter sections 21 , in particular of the filter cloth 50 and/or with time.
- the time at which a cleaning process 57 is completed or takes place is less than 10 s, in particular less than 5 s, especially preferably less than 2 s. Quite especially preferably the time of one cleaning process 57 is at least essentially 1 s.
- the time for one cleaning process 57 is less than the time which cleaned particles, in particular the suspension dust and/or the filter cake 32 requires or require to travel or fall out of the immediate suction area of the respective filter section 21 during the cleaning process 57 .
- time intervals T 1 between the cleaning processes 57 are limited with a maximum value and/or a minimum value, preferably the maximum value and/or the minimum value being specified exogenously to the feedback control 59 and/or the cleaning method.
- the maximum value is less than 500 s, in particular less than 400 s, especially preferably less than 300 s, and/or the minimum value is more than 5 s, in particular more than 10 s, especially preferably more than 15 s.
- the differential pressure DP rises during filtration by means of the filter 19 , in particular when a cleaning process 57 is not taking place.
- the differential pressure DP increases preferably at least essentially linearly with the time T or the difference between the differential pressure DP and the rated differential pressure SP decreases essentially linearly with the time T. But other curve characteristics are also possible.
- a cleaning process 57 is preferably triggered when the differential pressure DP reaches the rated differential pressure SP, exceeds it and/or approaches it.
- a cleaning process 57 is triggered depending on the differential pressure DP, the system deviation 62 and/or on the preferably previous time interval T 1 and/or the time interval T 2 .
- the controller of the feedback control 59 determines the instant of triggering of a cleaning process 57 or the start of a cleaning cycle 58 .
- the differential pressure DP drops during the cleaning process 57 and/or by the cleaning process 57 .
- the difference between the differential pressure DP and the rated differential pressure SP increases during the cleaning process 57 and/or by the cleaning process 57 .
- the differential pressure DP rises again after completion of the cleaning process 57 or the difference between the differential pressure DP and the rated differential pressure SP decreases.
- the differential pressure DP after cleaning or after one cleaning process 57 rises linearly and/or at least essentially as before cleaning or a cleaning process 57 .
- other curve characteristics are also possible, in particular in which the gradient of the differential pressure DP increases with the time T and/or with the number of triggered cleaning processes 57 .
- the differential pressure DP drops in a cleaning process 57 at least essentially to the same value as in the previous cleaning process 57 or the differential pressure DP after successive cleaning processes 57 is at least essentially the same.
- the time until the differential pressure DP reaches the rated differential pressure SP, exceeds it and/or approaches the rated differential pressure SP decreases with the time T.
- the time interval T 1 between two successive cleaning processes 57 in particular between the start of two successive cleaning processes 57 and/or the end of two successive cleaning processes 57 and/or the end of one temporarily and the start of a following cleaning process 57 becomes preferably at least essentially exponentially smaller preferably during filtration by means of the filter 19 and/or with the time T.
- the time interval T 1 and/or the time interval T 2 is adjusted and/or used as a controlled variable 60 or controlled variables 60 in the feedback control 59 .
- time interval T 1 and/or the time interval T 2 is/are used as the manipulated variable 64 or manipulated variables 64 in the feedback control 59 or in the cleaning method.
- time intervals T 1 and T 2 are not directly derived from the differential pressure DP or the comparison of the differential pressure DP to the rated differential pressure SP. It is preferred that the time interval T 1 and the time interval T 2 are computed, defined or determined by the feedback control 59 , especially preferably by means of the control apparatus 29 .
- FIG. 10 shows a schematic representation of the pressure P as a function of the time T in the suggested cleaning method according to a second version of the method, in particular the time interval T 1 being at least essentially constant within one cleaning cycle 58 .
- one cleaning process 57 is triggered at the start of the respective cleaning cycle 58 when the differential pressure DP reaches the rated differential pressure SP, exceeds it and/or approaches the rated differential pressure SP.
- the time interval T 1 between successive cleaning processes 57 of one cleaning cycle 58 is changed in particular by means of the above explained feedback control 59 and/or for the entire cleaning cycle 58 is fixed at an at least essentially constant value.
- the subsequent cleaning processes 57 take place within the cleaning cycle 58 regardless of the differential pressure SP and/or the rated differential pressure SP and/or after the time interval T 1 .
- the time interval T 1 between successive cleaning processes 57 within one cleaning cycle 58 is preferably changed and/or fixed before and/or at the start of the cleaning cycle 58 , preferably by means of the feedback control 59 and/or is held constant at the previously established value during the entire cleaning cycle 58 .
- the differential pressure DP which prevails at the start of one cleaning process 57 and/or at the end of one cleaning process 57 can drop and/or rise within one cleaning cycle 58 .
- the filter 19 preferably has three filter sections 21 and/or one cleaning cycle 58 encompasses three cleaning processes 57 .
- a further following cleaning cycle 58 starts, in particular the time interval T 2 of successive cleaning cycles 58 being changed.
- another cleaning cycle 58 starts with the triggering of a cleaning process 57 .
- the time intervals T 1 in the second cleaning cycle 58 are changed compared to the first cleaning cycle 58 .
- time intervals T 1 from cleaning cycle 58 to cleaning cycle 58 and/or with the time T become smaller. But other variations are also possible.
- the differential pressure DP with time T increasingly approaches the rated differential pressure SP.
- the filter 19 is preferably completely cleaned, in particular wet, preferably the installation 1 and/or the filter system 17 being shut down and/or the filtration being adjusted by means of the filter 19 .
- time intervals T 1 are changed such that the number of cleaning processes 57 is minimized and/or the time until necessary wet cleaning of the filter 19 is maximized.
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Abstract
Description
- This invention relates to a cleaning method for cleaning of a filter in sections according to the preamble of
claim 1, a control apparatus for executing a cleaning method according to the preamble ofclaim 14, a connecting device for connecting a filter to a cleaning device according to the preamble ofclaim 15, a cleaning device for cleaning of a filter according to the preamble ofclaim 34, a filter system with a filter and a cleaning device for cleaning the filter according to the preamble ofclaim 42, and an installation, in particular for coating processes, with an installation housing, a filter and a cleaning device for cleaning of the filter according to the preamble ofclaim 46. - The term “cleaning method” in this invention is defined as all methods, procedures and processes by means of which the cleaning of a filter, of a filter system and/or of an installation before, during and/or after filtration by means of the filter is planned, analyzed, implemented, coordinated and/or adjusted or controlled.
- Cleaning methods are necessary in many installations and/or filter systems in order to clean fouled or clogged filters. In current cleaning methods for sectional cleaning of a filter which has several filter sections, in particular filter cartridges, the filter sections are cleaned in cleaning processes separated from one another by fixed or constant time intervals. In doing so it can happen that the filter or one of the filter sections is being cleaned, although this is not yet necessary at the time of cleaning. In particular in such a cleaning method a filter cake which forms on the filter can be cleaned off or removed too early or too late by means of the cleaning. Accordingly additional and avoidable costs are also associated with such a cleaning method.
- The term “connecting device” in this invention is preferably a structural apparatus, in particular for filter systems, cleaning devices and/or installations, for example as an adapter or intermediate piece which is preferably made to fluidically connect a filter to a cleaning device. In particular a connecting device is made to direct a medium, in particular a fluid of the cleaning device, to the filter which is preferably connected to the cleaning device.
- The term “cleaning device” in this invention is defined preferably as a device which is made to clean an assigned filter, preferably pneumatically or by means of compressed air, preferably particles in or on the filter and/or a filter cake of the filter which has formed or is forming on the filter being removed partially or completely from the filter.
- Especially preferably cleaning devices generate a pressure pulse, in particular at least essentially against that flow direction which prevails in the filter in filtration by means of the filter. Cleaning devices are used both during continuing operation of the filter or of the filter system (online operating mode) and also when the operation of the filter or of the filter system is being interrupted (offline operating mode).
- The term “filter system” in this invention is defined preferably as a system which has at least one filter and at least one cleaning device for cleaning of the filter. The filter of a filter system is preferably made to remove and filter solids/particles of a fluid from the fluid within the scope of filtration. In particular the separation of the particles of the fluid to be cleaned takes place by a filter medium of the filter, within the filter medium and/or by means of a filter cake which has formed or is forming on the filter medium. According to this definition filters are especially surface filters, such as filter cartridges or filter hoses which are made in particular to separate particles of a gas or raw gas by means of cake filtration and/or filter-medium filtration.
- The term “installation” in this invention is defined in particular as industrial installations and/or process-engineering installations. In this invention they are preferably coating installations for coating of a product with a layer. In particular installations according to this definition are made to coat pharmaceutical products such as pellets. Preferably the coating takes place by means of fluidized bed processes, in particular the product to be coated being fluidized as a fluidized bed. Preferably installations according to this definition have a filter system with a filter and a cleaning device for cleaning of the filter, in particular to separate particles such as dust from a raw gas during the coating process and/or to supply them again to the coating process.
- Cleaning devices are necessary in many methods to clean fouled or clogged filters. Current cleaning devices, filter systems and/or installations have cleaning devices which are spaced 3-dimensionally apart from assigned filters such that during filtration the cleaned medium or the clean gas can escape from the filter, in particular from the filter outlet of the filter. DE 298 23 965 U1 and EP 1 507 579 B1 disclose compressed air pulse injector systems which for cleaning and regeneration of individual filter cartridges by means of compressed air are located and spaced above the filter and for cleaning purposes blow compressed air first into the space surrounding the compressed air pulse injector systems and then into the respective filter cartridge. Based on the distance between the outlet of the cleaning device and the filter cartridge to be cleaned at the time, high flow losses arise which can lead to the respective filter cartridges, in particular in the neck region, not being completely cleaned and/or having to be cleaned very often or repeatedly.
- The object of this invention is to devise a cleaning method for cleaning of a filter as well as a control apparatus for executing a cleaning method for cleaning of a filter which enables or supports improved, reliable, efficient and/or economical cleaning of the filter and/or filtration by means of the filter and/or the number of cleaning processes is minimized. Furthermore the object of this invention is to devise a connecting device in particular for connecting a filter to a cleaning device, a cleaning device, a filter system and an installation, as a result of which a compact construction and/or reliable, efficient, economical, low-maintenance and low-loss cleaning of the filter or of a filter section of the filter is enabled or supported.
- This object is achieved by a cleaning method as claimed in
claim 1, a control apparatus as claimed inclaim 14, a connecting device as claimed inclaim 15, a cleaning device as claimed inclaim 34, a filter system as claimed inclaim 42, or an installation as claimed inclaim 46. Advantageous developments are the subject of the dependent claims. - One aspect of this invention lies in that the filter sections are cleaned within one cleaning cycle in cleaning processes which are separated in time from one another and the cleaning method has at least two cleaning cycles, both one time interval between the cleaning processes within the respective cleaning cycle and also one time interval between the end of one of the cleaning cycles and the start of a following one of the cleaning cycles being changed. In this way it is possible to reduce the number of necessary cleaning processes overall, to leave a filter cake as long as possible on the filter sections and or/to optimize or change the time or the time interval between the cleaning processes within the respective cleaning cycle as well as the time interval between the end of one of the cleaning cycles and the start of a following one of the cleaning cycles such that the cleaning method cleans the filter altogether more reliably, efficiently and/or economically.
- According to another independently attainable aspect of this invention the filter has at least three filter sections, the filter sections being cleaned in cleaning processes separated by time intervals from one another and the time intervals between successive cleaning processes being changed. The already explained advantages can be achieved in this way.
- Preferably the time intervals between the cleaning processes within the respective cleaning cycle and also the time intervals between the end of one of the cleaning cycles and the start of a following one of the cleaning cycles is changed by means of feedback control. This enables preferably complete automation of the suggested cleaning method, in particular reliable, efficient and/or economical cleaning of the filter and/or filtration by means of the filter being achieved.
- Especially preferably the feedback control adjusts a differential pressure between one filter inlet and one filter outlet of the filter and/or a differential pressure between one filter inlet and one filter outlet is used as the controlled variable in the feedback control. This advantageously makes it possible to change the time intervals depending on the differential pressure by means of the feedback control.
- In one especially preferred version of the suggested cleaning method the differential pressure or the system deviation is filtered with a control filter, preferably with a lowpass characteristic and/or such that peaks and/or fluctuations of the differential pressure caused by one or more cleaning process are at least essentially suppressed or filtered. This ensures that the cleaning method is quiet and/or stable.
- Especially preferably the time intervals between the cleaning processes within one cleaning cycle are constant or are kept at a constant value. In this way the complexity of the cleaning method is reduced and the number of possible fault sources is minimized.
- One suggested control apparatus is made to execute the suggested cleaning method, preferably the control apparatus being made to determine using at least one pressure sensor a differential pressure between a filter inlet and a filter outlet of the filter, and/or to trigger a valve to initiate a cleaning process. In this way the already explained advantages can likewise be achieved.
- Another also independently attainable aspect of this invention lies in that a connecting device has one side wall which borders an internal cross section which increases along one longitudinal axis of the connecting device and has openings laterally with assigned major axes, the major axes of the openings running obliquely to the side wall and pointing from outside to inside in the direction of one internal cross section which is greater than an internal cross section into which the respective opening discharges. In this way the suggested connecting device enables a direct connection of the filter to the cleaning device and/or a support of the cleaning device both during the cleaning and also during the filtration.
- In particular the medium with which the filter is being cleaned, during and/or for cleaning travels from the cleaning device via the connecting device directly to the filter, while the medium cleaned by means of the filter or the clean gas can escape from the filter through the openings of the connecting devices from the inside to the outside. Consequently it is not necessary to replace, change or three-dimensionally move the connecting device for the respective operation of the filter.
- The openings which run obliquely to the side wall preferably reduce flow losses both during cleaning and also during filtration.
- The manner of construction of the connecting device preferably and advantageously increases the mass flow and/or the pressure of the medium with which the filter is being cleaned and/or reduces the risk of possible flow detachment on the side wall of the connecting device during cleaning.
- According to another also independently attainable aspect of this invention, the openings of the connecting device are oriented at one or more planes which is or are aligned orthogonally to the longitudinal axis of the connecting device. This ensures economical production of the connecting device and enables the side wall of the connecting device to be provided with as many openings as possible, in particular without the connecting device losing stability.
- According to another also independently attainable aspect of this invention the side wall has a section free of openings in the region of the greatest internal cross section. In this way the flow losses during cleaning are reduced and/or a pressure rise by means of the connecting device is enabled during cleaning, in particular without the medium with which the filter is being cleaned flowing from the inside to the outside through the openings of the connecting devices and thus not contributing to the cleaning of the filter.
- A suggested cleaning device for cleaning of a filter preferably has the suggested connecting device in order to connect the filter to the cleaning device. In this way the already explained advantages can be achieved.
- A suggested filter system with a filter and a cleaning device for cleaning of the filter preferably has the suggested connecting device for connection of the filter to the cleaning device. In this way the already explained advantages can likewise be achieved.
- A suggested installation, in particular for coating processes, with an installation housing, a filter and a cleaning device for cleaning of the filter preferably has the suggested connecting device. In this way the already explained advantages can likewise be achieved.
- According to another also independently attainable aspect of this invention, the installation has an installation housing which in the interior has a storage apparatus which is made to supply the cleaning device with a medium with which the filter is being cleaned, in particular compressed air. This reduces the distance between the cleaning device and a storage apparatus which is located outside the installation housing. Along with this, the flow losses of the cleaning device are reduced and/or the existing construction space in the installation housing is efficiently used or a compact installation is enabled.
- According to another also independently attainable aspect of this invention the installation housing internally has a valve for initiating a cleaning process. This likewise enables optimized use of the construction space in the installation housing and prompt control or adjustment of the cleaning. The valve preferably connects the storage apparatus to the connecting device, in particular fluidically and/or on one end facing away from the filter or end with reduced internal cross section of the connecting device.
- The aforementioned aspects and other aspects and features arising from the claims and following description can be implemented independently of one another and in any combination.
- Other advantages, features, properties and aspects of this invention follow from the claims and the following description of preferred embodiments using the drawings.
-
FIG. 1 shows a schematic section of a suggested installation with a suggested filter system, a suggested connecting device and a suggested cleaning device; -
FIG. 2 shows a perspective view of a suggested connecting device; -
FIG. 3 shows a schematic section of a suggested filter system with the connecting device, a valve in the closed state and a filter shown in sections; -
FIG. 4 shows a schematic section of the filter system according toFIG. 3 with the valve in the opened state; -
FIG. 5 shows a schematic plan view of the suggested filter system as well as a suggested cleaning device with a storage apparatus and several control apparatus; -
FIG. 6 shows a schematic side view of a suggested installation with a suggested filter system, a first filter section of the filter being cleaned; -
FIG. 7 shows a schematic side view of the installation according toFIG. 6 , a second filter section of the filter being cleaned; -
FIG. 8 shows a schematic block diagram of a feedback control underlying a suggested cleaning method; -
FIG. 9 shows a schematic of the pressure as a function of time in the suggested cleaning method according to a first version of the method; and -
FIG. 10 shows a schematic of the pressure as a function of time in the suggested cleaning method according to a second version of the method. - In the only schematic figures which are partially not to scale, the same reference numbers are used for the same or similar parts, corresponding or comparable properties and advantages being attainable even if a repeated description is omitted.
- The
installation 1 shown inFIG. 1 is preferably made to carry out coating processes. In particular theinstallation 1 is a fluidized bed coating installation for the production of pellets (not shown) or for pelletizing within the scope of preferably pharmaceutical production. - The
installation 1 preferably has aninstallation housing 2 with ahousing inlet 3 and ahousing outlet 4. - Preferably the
installation housing 2 is made as a reactor. Especially preferably the pelletizing or coating/production of the pellets takes place within theinstallation housing 2. - Preferably the
installation housing 2 is or can be divided into aninlet air region 5,spray region 6, filterregion 7 and dome region/clean gas region 8. - The
housing inlet 3 is preferably fluidically connected to an inlet air system (not shown) which is made to supply theinstallation 1 or theinstallation housing 2, in particular theinlet air region 5, withinlet air 9, in particular theinlet air 9 being conditioned by means of the inlet air system for the coating. - Preferably the
inlet air region 5 is separated from thespray region 6 by means of aperforated bottom 10. - In particular the
inlet air 9 is directed or guided through the perforated bottom 10 from theinlet air region 5 into thespray region 6. - The
installation 1 preferably has asuspension tank 11 which in the interior contains asuspension 12 or another fluid for the coating process. - The
suspension 12 is preferably supplied to theinstallation housing 2 by means of asuspension pump 13 via asuspension line 14 and/or pumped into theinstallation housing 2. - Preferably in the
spray region 6 there are one ormore nozzles 15 which are made to atomize thesuspension 12 in theinstallation housing 2, in particular in thespray region 6 and/or to apply it to the pellets (not shown), preferably the pellets being fluidized within the scope of the fluidized bed coating process and/or moving as a fluidized bed in thespray region 6. - Preferably the
nozzles 15 are each located in a pipe, in particular in aWurster pipe 16. The pellets are preferably routed past thenozzles 15 in theWurster pipe 16 and sprayed or coated with thesuspension 12 by means of thenozzles 15. Preferably the pellets in theWurster pipe 16 are routed or blown upward or against gravity by means of theinlet air 9. - Outside the
Wurster pipe 16 the pellets drop preferably in the direction of the perforated bottom 10 and/or with gravity. In this way the pellets are coated along an at least essentially ellipsoidal path in theinstallation housing 2. - The illustrated embodiment is in particular a bottom spray version, preferably the
nozzles 15 pointing up. But other embodiments or arrangements in theinstallation 1 and/or in theinstallation housing 2 are also possible. - There is preferably a suggested
filter system 17 in thefilter region 7. - The
filter system 17 preferably has a connectingdevice 18 which is made to connect a filter 19 assigned to thefilter system 17 to acleaning device 20 which is likewise assigned to thefilter system 17. The connectingdevice 18 can be part of the filter 19 or of thecleaning device 20 or connected hereto or can be implemented separately. - The filter 19, preferably a particle filter, is preferably located within the
installation housing 2, in particular above thespray region 6 and/or in thefilter region 7 and/or in the region of thehousing outlet 4. But other arrangements and/or designs are also possible. - The filter 19 preferably separates the
spray region 6 from thedome region 8, in particular in a gas-permeable and/or particle-retaining manner. - Preferably the filter 19 has several filter sections 21 and/or is and/or can be divided into several filter sections 21. Especially preferably the filter sections 21 are spaced three-dimensionally apart from one another and/or are made as separate units of the filter 19.
- The filter sections 21 are quite especially preferably made as elongated, tubular and/or cylindrical surface filters, in particular as filter cartridges 22 which project preferably from the
dome region 8 into thefilter region 7. - Preferably a medium to be filtered, in particular a
raw gas 23, flows through the filter cartridge 22 during the filtration by means of the filter 19 from the outside to the inside, as shown inFIG. 1 . - In particular the surface of the filter section 21 or of the filter cartridge 22 is made as the
filter inlet 24 and the inside of the filter section 21 or of the filter cartridge 22 indicated by broken lines is made as thefilter outlet 25. - The medium, in particular a
clean gas 26, which is cleaned or filtered by means of the filter 19, is preferably routed into thedome region 8 of theinstallation housing 2 preferably by means of the connectingdevice 18 in order to subsequently leave theinstallation housing 2 via thehousing outlet 4 asexhaust air 27. - In particular that part of the
suspension 12 which does not adhere to the pellets is carried preferably as dust, in particular as a suspension dust orraw gas 23, from thespray region 6 into thefilter region 7. - The filter 19 is made in particular to filter the dust-laden air or
raw gas 23 and then to direct it asclean gas 26—preferably by means of the connectingdevice 18—into thedome region 8 and/or to thehousing outlet 4. - Preferably the filter 19 and/or individual filter sections 21 clogs increasingly with particles, in particular the suspension dust, during filtration of the
raw gas 23. - The
cleaning device 20 is preferably made to clean the filter 19. In particular thecleaning device 20 is made to remove the dust of thesuspension 12 or other particles from the filter 19 and/or from the filter surface and/or to convey it, in particular blow it, from thefilter region 7 into thespray region 6. InFIG. 1 thecleaning device 20 is not active or no cleaning is taking place. - Especially preferably the
cleaning device 20 is located at least partially or completely in theinstallation 1, in particular in theinstallation housing 2. In the illustrated arrangement thecleaning device 20 is located in thedome region 8 and/or on the clean gas side or above the filter 19 or individual filter sections 21. But other arrangements are also possible. - The
cleaning device 20 preferably has onestorage apparatus 28, in particular thestorage apparatus 28 being made to supply the cleaning device 2Q with a medium, in particular compressed air. - Preferably the
storage apparatus 28 is located at least partially, preferably completely, within theinstallation housing 2. Thestorage apparatus 28 is especially preferably located in thedome region 8 and/or above the filter 19. - Preferably the
installation 1, thefilter system 17 and/or thecleaning device 20 has or have acontrol apparatus 29. Thecontrol apparatus 29 is made in particular to control or regulate thecleaning device 20 and/or the cleaning of the filter 19. - In the illustrated embodiment the
control apparatus 29 is located preferably outside theinstallation housing 2. But other arrangements are also possible. - Preferably the
installation 1, thefilter system 17, thecleaning device 20 and/or thecontrol apparatus 29 has or have at least onepressure sensor 30, in particular thepressure sensor 30 being made to determine and/or measure a differential pressure DP. - The differential pressure DP is preferably the difference between two static pressures, dynamic pressures, or total pressures of a fluid. In particular the differential pressure DP is the difference of the preferably static pressure of the
raw gas 23 and of the preferably static pressure of theclean gas 26. - Preferably the differential pressure DP is determined and/or measured between the
filter inlet 24 and thefilter outlet 25, between thedome region 8 and one of the other regions of theinstallation housing 2 and/or between thehousing inlet 3 andhousing outlet 4 by means of thepressure sensor 30. - Preferably the
control apparatus 29 controls or regulates avalve 31 which is assigned in particular to thecleaning device 20 and/or thefilter system 17 depending on the differential pressure DP and/or according to the suggested cleaning method. - In particular one
valve 31 at a time is assigned to each filter section 21 or to each filter cartridge 22 and/or one filter section 21 or one filter cartridge 22 at a time is fluidically connected to onevalve 31, especially preferably by means of the respective connectingdevice 18. But other designs are also possible, in particular in which avalve 31 is fluidically connected to several filter sections 21. - Especially preferably the
installation 1, thefilter system 17, thecleaning device 20 and/or thecontrol apparatus 29 is or are made to determine and/or measure the differential pressure DP with one ormore pressure sensors 30 and/or to trigger the valve orvalves 31 to clean the filter 19. - Preferably the
installation 1, thefilter system 17, thecleaning device 20 and/or thecontrol apparatus 29 is or are made to carry out a suggested cleaning method which is explained later in the description. - By filtering the
raw gas 23, with time a dust layer, in particular afilter cake 32, forms on the surface of the filter 19, in particular of the filter sections 21. - Preferably the mass or the volume, in particular the thickness, and/or the density of the
filter cake 32 increases during the filtration and/or during operation of theinstallation 1. - In particular with or by the increase of the mass, of the volume, and/or of the density of the
filter cake 32 the differential pressure DP likewise rises. - Preferably the differential pressure DP is at least essentially a function of the mass, of the volume, and/or of the density of the
filter cake 32 and/or the differential pressure DP correlates, in particular positively, with the mass, the volume and/or the density of thefilter cake 32. - In particular when the differential pressure DP reaches, exceeds or approaches a given value, the
control apparatus 29 controls or adjusts the valve orvalves 31 preferably such that the valve orvalves 31 open and/or compressed air or some other medium is blown or directed out of thestorage apparatus 28 through the valves orvalves 31 and/or through the connectingdevice 18 into the filter 19 and/or into one of the filter sections 21. - Preferably the differential pressure DP drops by and/or during the cleaning of the filter 19 and/or of one of the filter sections 21.
- First of all, the suggested connecting
device 18 is shown isolated below usingFIG. 2 and then in the installed state usingFIG. 3 andFIG. 4 . -
FIG. 2 shows a perspective view of the connectingdevice 18. - Preferably the connecting
device 18 is made to connect the filter 19 (not shown inFIG. 2 ) to the cleaning device 20 (not shown), the connectingdevice 18 having oneside wall 33 which borders an internal cross section Q which increases along a longitudinal axis L and hasopenings 34 with assigned major axes H. - The connecting
device 18 preferably has at least two, in particular at least 50, especially preferably at least 100, and/or at most 1000, especially at most 500, quite especially preferably at most 400openings 34. - Preferably the connecting
device 18 is or can be divided into at least two, preferably three regions or sections. - Preferably the
openings 34 are located in afirst section 35 of the connectingdevice 18. Especially preferably the connectingdevice 18 has asecond section 36 free of openings. In particular thesecond section 36 is free of openings and/or is closed laterally along the longitudinal axis L. Thesecond section 36 preferably directly and/or continuously borders thefirst section 35 and/or forms with it an interruption-free or continuous flow wall. - In particular the
second section 36 has the internal cross section Q which increases along the longitudinal axis L and/or the greatest internal cross section Q1 at least in part. - Preferably each internal cross section Q of the
second section 36 is greater than one of the internal cross sections Q of thefirst section 35. - The
second section 36 extends preferably to at least 10%, especially preferably to at least 20%, in particular to at least 30% and/or to at most 70%, especially preferably to at most 60%, in particular to at most 50%, of the length or height of the connectingdevice 18. - The connecting
device 18 and/or theside wall 33 has or have preferably athird section 37, preferably thethird section 37 having a constant, in particular cylindrical internal cross section Q. Thethird section 37 preferably directly borders thefirst section 35, preferably on one side of thefirst section 35 facing away from thesecond section 36. - The
first section 35, thesecond section 36 and/or thethird section 37 are preferably tightly connected or made integral. - Preferably the internal cross section Q of the
third section 37 is smaller than the internal cross section Q of thesecond section 36 and/or smaller than or equal to the preferably smallest internal cross section Q2 of thefirst section 35. In particular the internal cross section Q of thethird section 37 is the smallest internal cross section Q2 of the connectingdevice 18. - In particular the
first section 35 and/or thethird section 37 has or have the smallest internal cross section Q2 of the connectingdevice 18. - Preferably a width or a diameter of the smallest internal cross section Q2 is greater than 33 mm and/or smaller than 70 mm, preferably at least essentially equal to 50.8 mm (2 inches), and/or a width or a diameter of the smallest internal cross section Q2 is more than 20%, preferably more than 30%, and/or less than 60%, preferably less than 50%, of a diameter or a width of the greatest internal cross section Q1 of the connecting
device 18. - Especially preferably the ratio of the surface of the filter section 21 assigned to the connecting
device 18 or of the filter cartridge 22 assigned to the connectingdevice 18 at the least or to the internal cross section Q2 of the connectingdevice 18 bordering thecleaning device 20 is an especially dimensionless characteristic K. - The characteristic K can preferably be computed or expressed via the following formula:
-
K=A Filter /Q=d Filter *L Filter*4/d Q 2 - preferably in the formula an at least essentially cylindrical filter section 21 being assumed, and/or AFilter being the surface of the filter section 21 assigned to the connecting
device 18 or of the filter cartridge 22 assigned to the connectingdevice 18, Q being the smallest internal cross section Q2, dfilter being the inside or outside diameter of the filter section 21 or of the filter cartridge 22, LFilter being the length or height of the filter section 21 or of the filter cartridge 22 and dQ being the diameter or the width of the smallest and of the internal cross section Q2 or of the one bordering thecleaning device 20. The characteristic K can be computed accordingly for different filter geometries. - Preferably the ratio of the surface of the filter section 21 assigned to the connecting
device 18 or of the filter cartridge 22 assigned to the connectingdevice 18 at the least or of the internal cross section Q2 of the connectingdevice 18 bordering thecleaning device 20 and the characteristic K is greater than 200, in particular greater than 250, and/or less than 3000, in particular less than 2500. - The internal cross section Q is preferably a (maximum) internal cross sectional area perpendicular to the longitudinal axis L of the connecting
device 18 or a hydraulic cross section or a hydraulic cross sectional area. In particular the internal cross section Q is the area enclosed or bordered by theside wall 33 of the connectingdevice 18. - Preferably on at least one axial end or in the opening or mouth region the connecting
device 18 has at least one connecting apparatus, in particular aflange union 38 or aclamp union 39, in particular the connecting apparatus being made to connect the connectingdevice 18 to the filter 19 and/or thecleaning device 20, thevalve 31 and/or thestorage apparatus 28 by form-fit, force-fit and/or by bonding. - The connecting
device 18, in particular the connecting apparatus(es) of the connectingdevice 18, is/are made preferably to connect the connectingdevice 18 to the filter 19, the connectingdevice 18 to thecleaning device 20, and/or the filter 19 to thecleaning device 20, especially in an immovable, holding, supporting and/or rigid manner. - Especially preferably the connecting
device 18 on the two axial ends has one connecting apparatus each, as shown inFIG. 2 . - The connecting apparatus(es) is/are preferably made as a flange, clamp connection and/or screwed pipe joint and/or are located on opposite axial ends of the connecting
device 18, in particular are formed integrally therewith. - In the embodiment shown in
FIG. 2 the connectingdevice 18—preferably on the axial end of thesecond section 36—has aflange union 38 and—preferably on the axial end of thethird section 37—aclamp union 39. However other designs are also possible, in particular in which two axial ends of the connectingdevice 18 have aflange union 38 orclamp union 39 as connecting apparatus. - The connecting apparatus or connecting apparatuses can be made both as groove unions or collar unions. In the illustrated embodiment the
flange union 38 is made preferably as a collar union and theclamp union 39 is made preferably as a groove union. - Preferably the connecting apparatus has a groove 40, preferably the groove 4Q being made to hold a seal 41.
- The outside diameter of the connecting apparatus is preferably larger than the outside diameter of the bordering section of the connecting
device 18. In particular the outside diameter of theflange union 38 is greater than the maximum or bordering outside diameter of thesecond section 36 and/or the outside diameter of theclamp union 39 is greater than the maximum or bordering outside diameter of thefirst section 35 and/or of thethird section 37. - As shown in
FIG. 2 , the internal cross section Q of the connectingdevice 18 is made at least essentially circular. But other designs are also possible, in particular in which the internal cross section Q is made at least oval, rectangular or square. - The connecting
device 18 and/or theside wall 33 preferably borders the internal cross section Q with one inside 42 of theside wall 33. - Preferably the inside 42 runs conically along the longitudinal axis L—at least in the
first section 35 and/or in thesecond section 36—and/or has an at least essentially straight contour. Alternatively or additionally the inside 42 is shaped bell-like, is bell-shaped or in the form of a diverging Laval nozzle section. Preferably the inside 42 of theside wall 33 is made at least essentially concave and/or convex. - In the illustrated embodiment the internal cross section or the pitch of the internal cross section Q or of the inside 42 along the longitudinal axis L or an angle enclosed between the longitudinal axis L and a tangent of the
side wall 33 decreases. In particular thefirst section 35 has an internal cross section Q which increases more dramatically along the longitudinal axis L than thesecond section 36. - Preferably the connecting
device 18, in particular theside wall 33, has an outside 43, and preferably the profile or the contour of the outside 43 can be made independent of the inside 42. - Preferably the outside 43 has an external cross section A which increases along the longitudinal axis L. In the illustrated embodiment the outside 43 runs along the longitudinal axis L at least essentially parallel to the inside 42. But other approaches are also possible.
- In particular the outside 43—at least in the
first section 35 and/orsecond section 36—is at least essentially straight and/or the outside 43 has an at least essentially conical contour or one which is arched in the longitudinal direction or is bell-like. But other designs are also possible here. -
FIG. 3 shows a schematic section of the connectingdevice 18 together with thevalve 31 in the closed state and with one part of one of the filter sections 21. - The transition between the
first section 35 andsecond section 36 and/or between thesecond section 36 andthird section 37 is/are preferably at least essentially continuous. Especially preferably the inside 42 at least in thefirst section 36 and/or in thesecond section 37 is made continuous. - In the illustrated embodiment the outside 43—at least in the
first section 35 and in thesecond section 36—is made straight and/or conical. But other designs are also possible here. - Preferably the thickness of the
side wall 33 and/or the difference between the internal cross section Q and the external cross section A increases along the longitudinal axis L and/or with increasing internal cross section Q. - In particular the internal cross section Q increases along the longitudinal axis L with a first angle W1 which is greater than 5° and/or less than 20°, preferably at least essentially is equal to 12°, in particular an imaginary extension or tangent of the inside 42 including the first angle W1 with the longitudinal axis L.
- As shown in
FIG. 3 , the major axes H of theopenings 34 run obliquely to theside wall 33, in particular to the inside 42 of theside wall 33. For purposes of illustrationFIG. 3 shows only the major axis H of oneopening 34. The following explanations however apply preferably to the major axes H of theother openings 34 accordingly. - Preferably the major axes H point from the outside to the inside in the direction of an internal cross section Q which is greater than an internal cross section Q into which the
respective opening 34 discharges. - Especially preferably the major axes H point from the outside to the inside in the direction of greatest internal cross section Q1 and/or intersect a plane imagined through the greatest internal cross section Q1. In particular the major axes H point from the outside to the inside in the direction of the filter 19, as shown in
FIG. 3 . - Especially preferably the major axes H of the
openings 34 intersect the longitudinal axis L at a second angle W2 and/or the major axes H with the longitudinal axis L in a longitudinal sectional view of the connectingdevice 18, as shown inFIG. 3 , include a second angle W2, preferably the second angle W2 being less than 90°, preferably at least essentially equal to 45°. - Preferably the inside 42 includes with the major axis H, in particular in the region of the respective mouth of the
opening 34, a third angle W3, in particular preferably the third angle W3 being less than 90° and/or greater than the first angle W1 and/or the second angle W2. - The
openings 34 are preferably oriented and/or located in one or more planes E, in particular the planes E being aligned at least essentially orthogonally to the longitudinal axis L of the connectingdevice 18, as illustrated inFIG. 3 using two planes E. - Preferably the planes E are each defined by at least three
openings 34. In particular at least threeopenings 34 lie and/or discharge in one of the planes E. - Especially preferably each
opening 34 is or can be assigned to one of the planes E. - As shown in
FIG. 3 , the planes E along the longitudinal axis L are arranged—preferably at least essentially equidistantly—offset to one another and/or parallel to one another. But other designs or arrangements are also possible. - The number of
openings 34 per plane E increases preferably with increasing internal cross section Q along the longitudinal axis L. - Especially preferably the ratio of all cross sections of the
openings 34 of one plane E to the internal cross section Q into which theopenings 34 of the plane E discharge remains constant at least essentially along the longitudinal axis L. - The
openings 34—at least along the internal cross section Q into which therespective openings 34 discharge, and/or in a plane E—are arranged at least essentially circularly and/or form several concentric circles along the longitudinal axis L. - In one alternative which is not shown the
openings 34 alternatively or additionally are arranged in a latticed manner or form a latticed structure. - The major axes H of the
openings 34 of one of the planes E preferably have one common intersection point, in particular the intersection point lying on the longitudinal axis L. - The
openings 34 are arranged uniformly distributed preferably along the longitudinal axis L—at least in thefirst section 35—and/or over the respective internal cross section Q. Preferably theopenings 34 in the respective plane E are equidistantly offset to one another and/or arranged rotationally symmetrically to one another. - In the embodiment shown in
FIG. 3 theopenings 34 are made as a hole and/or have a circular cross section. But other geometries are also possible, in particular theopenings 34 having an angular, in particular rectangular cross section and/or being made as a slot, cylindrical, rotationally symmetrical and/or axially symmetrical to the respective major axis H. - Preferably the
openings 34 have a diameter and/or a width which is more than 2% and/or less than 20%, preferably at least essentially equal to 10% of the diameter and/or of the width of the greatest internal cross section Q1. - In the illustrated embodiment the
openings 34 each have at least essentially the same diameter and/or the same width. But other designs are also possible, in particular in which the diameter and/or the width of theopenings 34 per and/or in one plane E and/or along the longitudinal axis L varies. - Preferably the
openings 34 have a diameter and/or a width of at least 5 mm and/or at most 40 mm, in particular of at least essentially 20 mm. - The cross section of the mouth or the cross sectional area of all
openings 34 is together or cumulated preferably more than 2% or 5%, in particular more than 8% or 10%, especially preferably more than 12%, and/or less than 50% or 40%, in particular less than 30% or 20%, quite especially preferably less than 15%, of the area of the inside 42 and/or outside 43. - The
openings 34 are preferably made elongated and/or tubular, preferably with a length which is greater than the diameter and/or the width of theopenings 34. - Preferably the internal cross section Q tapers in the direction of the
cleaning device 20 and/or of thevalve 31 and/or increases in the direction of the filter 19 and/or of the filter sections 21. - The suggested
cleaning device 20 preferably has the connectingdevice 18 and/or is or can be connected to it. In particular thevalve 31 which is preferably assigned to thecleaning device 20 and/or is an integral part of thecleaning device 20, is fluidically connected to the connectingdevice 18, as shown inFIG. 3 . - The
valve 31 is preferably made as an axial valve, as shown for example inFIG. 3 . But other designs are also possible. - Preferably the
valve 31 is or can be driven pneumatically, hydraulically and/or electrically. In the illustrated embodiment thevalve 31 is preferably driven pneumatically, in particular by means of compressed air of the storage apparatus 28 (not shown). - The
valve 31 preferably has apiston 44, preferably thepiston 44 being movable axially and/or in the direction of the longitudinal axis L. - In
FIG. 3 thevalve 31 is in the closed state. - In the closed state the
piston 44 rests or lies on acone seat 45 located in thevalve 31 such that flow through thevalve 31 is prevented. - Preferably the
piston 44 is pretensioned by means of aspring 46 or some other tensioning element. To open thevalve 31 thevalve 31 preferably has avalve chamber 47. In particular the pressure of a medium in thevalve chamber 47 is or can be adjusted or controlled by means of the control apparatus 29 (not shown). - Preferably the
valve 31 opens when the pressure in thevalve chamber 47 is greater than the pressure produced by thespring 46. - The filter 19 shown in
FIG. 3 or one of the filter sections 21 of the filter 19 preferably has onemanifold 48 withseveral holes 49. The manifold 48 is jacketed in particular by afilter cloth 50. - The
filter cloth 50 is preferably made to retain or filter particles of a certain size, in particular the initially described suspension dust. - Preferably during and/or by the filtration, as indicated in
FIG. 3 , thefilter cake 32 forms on the manifold 48 and/or thefilter cloth 50. - The arrows shown in
FIG. 3 schematically illustrate the preferred flow direction in the filter 19 and in the connectingdevice 18 during filtration by means of the filter 19. The arrows illustrate only schematically the flow direction; any turbulence, eddies, detachments and/or other flow phenomena remain ignored. - In filtration by means of the filter 19 the medium to be cleaned, in particular the
raw gas 23, flows through the filter section 21 at least essentially from the outside to the inside or in the radial direction to the longitudinal axis L. - Flow through the connecting
device 18 takes place during filtration by means of the filter 19 in thesecond section 36 preferably at least essentially axially or along the longitudinal axis L. - Subsequently or downstream the flow in the
first section 35 during filtration is diverted such that it flows from the inside to the outside through theopenings 34. - Flow through the connecting
device 18 and/or theopenings 34 takes place preferably at least essentially from the inside to the outside during filtration and/or the connecting device and/or openings are made for flow through them to take place from the inside to the outside during filtration. - In particular the suggested
filter system 17 is made to direct a medium, preferably theclean gas 26, from the inside or one side facing the filter 19 to the outside or to one side facing away from the filter 19 through theopenings 34. - The connecting
device 18 is made in particular to accelerate a medium, in particular theclean gas 26, during filtration. Especially preferably the connectingdevice 18 acts as a nozzle or convergent tube during filtration. -
FIG. 4 shows a schematic section of the connectingdevice 18 and of the filter 19 shown by way of an extract or of one of the filter sections 21 according toFIG. 3 together with thevalve 31 in the opened state. - Preferably the
installation 1, thecleaning device 20 and/or the control apparatus 29 (compareFIG. 1 ) is or are made to at least essentially reverse the flow direction through the connectingdevice 18, in particular through theopenings 34, and/or through the filter 19, in particular through one of the filter sections 21, preferably by means of opening and closing of thevalve 31. -
FIG. 4 shows the cleaning of one of the filter sections 21 or the partial cleaning of the filter 19. - The connecting
device 18 and/or thecleaning device 20 is or are preferably made to retard a medium, in particular compressed air from the storage apparatus 28 (compareFIG. 1 ) during and/or for cleaning—in particular in the direction of increasing internal cross section Q—and/or to raise the static pressure of the medium, in particular of the compressed air of thestorage apparatus 28—at least in the connectingdevice 18. - Preferably the
openings 34 are made to direct or suction another medium, in particular theclean gas 26, from the outside to the inside during and/or for cleaning. In particular the connectingdevice 18 and/or thecleaning device 20 is or are made to increase the mass flow of a medium, preferably of the compressed air of thestorage apparatus 28 and/or to suction a second medium, preferably theclean gas 26—in particular through the and/or by means of theopenings 34. - The connecting
device 18 acts preferably during and/or for cleaning as a diffusor. - Especially preferably the action of the connecting
device 18 depends on the flow direction through the connectingdevice 18. - Especially preferably flow takes place through the connecting
device 18 and/or the filter 19, in particular one of the filter sections 21, during and/or for cleaning in one direction which is preferably opposite at least essentially the flow direction which prevails during and/or for filtration by means of the filter 19. - In one especially preferred embodiment of the connecting
device 18 the connectingdevice 18 is made as a supercritical diffusor and/or the internal cross section Q increases along the longitudinal axis L with a first angle W1 greater than 8°. - The
openings 34 are in particular made—at least during and/or for cleaning—to prevent and/or reduce flow separation, in particular at and/or on the inside 42 of the connectingdevice 18. Especially preferably in the connectingdevice 18—at least during cleaning—there is an at least essentially laminar flow and/or the connectingdevice 18 is made to enable a laminar flow or to support the formation of a laminar flow. -
FIG. 5 shows a schematic plan view of the suggestedfilter system 17 as well as of the suggestedcleaning device 20 with thestorage apparatus 28 as well as one or more, in particular synchronized, thecontrol apparatus 29 which are made preferably to control thevalves 31 and/or to measure one or more differential pressures DP assigned to the filter sections 21. - The
storage apparatus 28 is preferably made to supply thecleaning device 20 with a medium, in particular compressed air. Especially preferably thestorage apparatus 28 is assigned to thefilter system 17 and/or to thecleaning device 20 and/or is a component of thefilter system 17 and/or of thecleaning device 20. - Preferably the
installation housing 2 has at least in part in the interior thestorage apparatus 28 or thestorage apparatus 28 is located at least essentially within or in the interior of theinstallation housing 2. In the embodiment shown inFIG. 5 thestorage apparatus 28 is made both in the interior of theinstallation housing 2 and also outside of theinstallation housing 2. - Preferably the
storage apparatus 28 optionally has one ormore storage units 51, as shown inFIG. 5 , preferably thestorage units 51 being located outside theinstallation housing 2. - The
storage apparatus 28 can be supplied from the outside with medium or compressed air, in particular by fluid connections between the storage unit(s) 51 and/or a compressor and the interior which is formed or surrounded by thestorage apparatus 28. But it is also otherwise possible to supply compressed air or a medium to thestorage apparatus 28. - The
storage apparatus 28 has in particular aring reservoir 52 which is located in the interior of theinstallation housing 2. - Preferably the
storage apparatus 28 and/or thering reservoir 52 is made at least essentially as a ring or is made ring-shaped. - In the illustrated embodiment the
storage apparatus 28 and/or thering reservoir 52 extends in the upper region of theinstallation housing 2, in particular in thedome region 8, and/or above thefilter system 17 or the filter 19. But other designs or arrangements are also possible. - Preferably the
storage apparatus 28 is made as a gas reservoir, in particular as a reservoir for compressed air and/or as a line network, in particular as a gas line network, especially preferably as a compressed air line network. Especially preferably thestorage apparatus 28 is made to uniformly distribute and/or deliver a medium, in particular compressed air, to thevalves 31 and/or to thefilter system 17. - In particular the
storage apparatus 28 is made to supply several filter sections 21 of the filter 19 with a medium, in particular compressed air, individually and/or separated in time. - Preferably the
storage apparatus 28, in particular thering reservoir 52, has at least twopipe segments 53 and/or is made ofseveral pipe segments 53. - The
pipe segments 53 are connected to one another or made integral preferably by force-fit, form-fit and/or bonding, in particular by welding. - The pressure of the medium in the
storage apparatus 28 is preferably more than 1 bar, in particular more than 2 bar, and/or less than 10 bar, in particular less than 8 bar, especially preferably less than 4 bar. The volume of the storage apparatus is preferably more than 50 l, in particular more than 100 l, especially preferably more than 200 l, and/or less than 1000 l, in particular less than 800 l, especially preferably less than 500 l. This has been found to be advantageous in conjunction with a compact construction and good cleaning performance. - Preferably the
storage apparatus 28, in particular thering reservoir 52, is fluidically connected to thevalve 31 and/or the connectingdevice 18. - Quite especially preferably the
valve 31 is located in the interior of theinstallation housing 2, in particular within thestorage apparatus 28 and/or between thestorage apparatus 28 and the connectingdevice 18. In particular thestorage apparatus 28, preferably thering reservoir 52, is made to protect thevalve 31 against an explosive atmosphere and/or to prevent direct contact of thevalve 31 with an explosive atmosphere, in particular direct contact of theinstallation housing 2 and/or of thedome region 8. - Preferably the
installation housing 2, thecleaning device 20 and/or thestorage apparatus 28 has or have several lines for supply of thecleaning device 20, of thestorage apparatus 28, in particular of thering reservoir 52, and/or of thevalve 31 with a medium, in particular compressed air. In the embodiment shown inFIG. 5 thestorage apparatus 28 is preferably supplied by means of acompressed air line 54 and/or thevalve 31 is supplied by means of acontrol air line 55. - The
control air line 55 is preferably made to alternately open or close thevalve 31. Especially preferably thecontrol apparatus 29 controls or adjusts thevalve 31 by means of thecontrol air line 55. Quite especially preferably the pressure in thecontrol air line 55 is greater than the pressure in thecompressed air line 54. - The
installation housing 2 has preferablyseveral penetrations 56, in particular thecompressed air line 54 and/or thecontrol air line 55 being routed through thepenetration 56 from the outside to the inside into theinstallation housing 2. - Especially preferably the
control apparatus 29 is made to control thevalve 31 for cleaning of the filter 19, in particular of one of the filter sections 21. - In the embodiment shown in
FIG. 5 theinstallation 1, thefilter system 17 and/or thecleaning device 20 preferably has or haveseveral control apparatus 29, preferably onecontrol apparatus 29 at a time controlling or adjusting at least twovalves 31. - The suggested cleaning method for sectional cleaning of the filter 19 is detailed below using
FIGS. 6 to 10 . - The cleaning method is executed preferably by means of the
installation 1, thefilter system 17, the connectingdevice 18, thecleaning device 20 and/or thecontrol apparatus 29. -
FIGS. 6 and 7 show theinstallation 1, thefilter system 17, the connectingdevice 18, thecleaning device 20 and thecontrol apparatus 29 as the suggested cleaning method is being carried out. - The
filter system 17 or the filter 19 is cleaned in sections or partially during the cleaning method. - Preferably the
filter system 17 or the filter 19 has at least two, preferably at least three, in particular at least four, filter sections 21, in particular filter cartridges 22, by means of acleaning process 57 one of the filter sections 21 or one of the filter cartridges 22 at a time being cleaned, as shown inFIGS. 6 and 7 . - Preferably in the suggested cleaning method the filter sections 21 are cleaned in cleaning processes 57 which are offset to one another or separated in time from one another. In particular the filter sections 21 are cleaned in cleaning processes 57 separated from one another by a time interval T1.
- Preferably in the cleaning method a
cleaning process 57 is completely finished or ended before afurther cleaning process 57 starts. - Especially preferably all filter sections 21 or filter cartridges 22 of the filter 19 and/or the entire filter 19 are cleaned within one
cleaning cycle 58. - In particular the cleaning method has at least two cleaning cycles 58.
- Preferably the end of one
cleaning cycle 58 is separated in time by a time interval T2 from the start of a followingcleaning cycle 58. - Preferably the (second) cleaning
cycle 58 which follows a (first) cleaningcycle 58 is the (second) cleaningcycle 58 which directly follows the (first) cleaningcycle 58, in particular between the end of the (first) cleaningcycle 58 and the start of the (second) cleaningcycle 58 or during the time interval T1 and/or T2 nocleaning process 57 being triggered or carried out. - As shown in
FIGS. 6 and 7 , thefilter system 17 or the filter 19 has especially preferably at least three filter sections 21, the filter sections 21 being cleaned in cleaning processes 57 separated from one another by time intervals T1. - Preferably a
cleaning process 57 and/or acleaning cycle 58 is triggered by opening the assignedvalve 31, preferably onevalve 31 being assigned to one filter section 21 or filter cartridge 22 at a time or one filter section 21 at a time being cleanable by opening of the correspondingvalve 31. - In particular, as already explained at the beginning, by triggering a
cleaning process 57 the flow direction of the pertinent filter section 21 or of the pertinent filter cartridge 22 is reversed. - As shown in
FIGS. 6 and 7 , preferably the filtration is continued during cleaning of one of the filter sections 21 by means of the other filter sections 21. But other versions of the method are also possible, in particular in which filtration is stopped or adjusted during thecleaning process 57. -
FIG. 6 shows the cleaning of a first filter section 21 or a first filter cartridge 22, in particular compressed air being directed from thestorage apparatus 28 through the assignedvalve 31 and the suggested connectingdevice 18 into the filter section 21 or the filter cartridge 22, in particular by thevalve 31 being opened. - Preferably during the
cleaning process 57 in addition to compressed air from thestorage apparatus 28 another medium, in particular theclean gas 26, is directed into the filter section 21 or the filter cartridge 22, as is indicated by arrows inFIG. 6 andFIG. 7 . -
FIG. 7 shows thecleaning process 57 of another, second filter section 21 or another filter cartridge 22. - Preferably, in the suggested cleaning method, filter sections 21 adjacent to one another are cleaned in cleaning processes 57 offset in time from one another, as shown by means of
FIG. 6 andFIG. 7 . Especially preferably the sequence in which the filter sections 21 are cleaned remains identical in each cleaningcycle 58. But other versions of the method are also possible, in particular in which the sequence in which the filter sections 21 are being cleaned is varied with each cleaningcycle 58. - In one quite especially preferable version of the method, in one
cleaning cycle 58 first those filter sections 21 are cleaned which have the greatest distance to thecompressed air line 54. - In the suggested cleaning method preferably the time interval T1 between the cleaning processes 57, in particular within the
respective cleaning cycle 58, and/or the time interval T2 between the end of one of the at least two cleaningcycles 58 is or are changed. - In particular the time intervals T1 between successive cleaning processes 57 in the cleaning method are changed. In the sense of this invention the feature that “two
cleaning processes 57 follow one another” should preferably be understood such that nofurther cleaning process 57 takes place between the two successive cleaning processes 57. The corresponding applies to successive cleaning cycles 58. - If the filter 19 has at least three filter sections 21, in the cleaning method the time interval T1 between the
successive cleaning process 57 of a first and a second filter section 21 and the time interval T2 between the successive cleaning processes 57 of the second and a third filter section 21 are each changed. - Preferably the time interval T1 and/or the time interval T2 is or are changed by means of
feedback control 59 and/orfeedback control 59 is carried out in the suggested cleaning method and causes a change or variation of the time intervals T1 and T2. -
FIG. 8 shows in this regard a schematic block diagram of thefeedback control 59 underlying the suggested cleaning method or of the feedback control circuit of thefeedback control 59. - Preferably in the cleaning method and/or the
feedback control 59 the differential pressure DP between thefilter inlet 24 and thefilter outlet 25 is adjusted and/or used as a controlled variable 60 in thefeedback control 59. - Preferably a rated differential pressure SP as a
reference variable 61 is specified in particular exogenously to thefeedback control 59. - The rated differential pressure SP is preferably more than 1000 Pa, in particular more than 2000 Pa, especially preferably more than 3000 Pa, and/or less than 7000 Pa, in particular less than 6000 Pa, especially preferably less than 5000 Pa. Quite especially preferably the rated differential pressure SP is at least essentially 4000 Pa.
- Preferably the rated differential pressure SP in the cleaning process is kept constant. But other versions of the method are also possible in which the rated differential pressure SP is changed.
- Preferably the difference between the rated differential pressure SP and the differential pressure DP is used as the
system deviation 62 in thefeedback control 59 and/or in the cleaning method. - The
feedback control 59 and/or the cleaning method uses or use preferably one controller, in particular aPID controller 63. But it is also possible to use other controllers in thefeedback control 59 and/or in the cleaning method. - The triggering of a
cleaning process 57 and/or the opening of thevalve 31 or of one of thevalves 31 or the length of the time interval T1 and/or T2 is preferably used as a manipulated variable 64 in thefeedback control 59 and/or in the cleaning method. - The controller is preferably made to determine the manipulated variable 64 by means of the
system deviation 62, in particular thesystem deviation 62 multiplied by a factor being integrated and/or derived over a fixed time. - The cleaning method and/or the
feedback control 59 preferably uses thefilter system 17 and/or thecleaning device 20, preferably together with thestorage apparatus 28 as the controlledsystem 65. - As shown in
FIG. 8 , optionally one influencingquantity 66 acts on the cleaning method and/or thefeedback control 59, in particular on the controlledsystem 65. In particular possible influencingquantities 66 include the increasing clogging or fouling of the filter 19, in particular of the filter sections 21, and/or the formation or increase of thefilter cake 32, the degree of dust loading of theraw gas 23, the flow velocity in theinstallation housing 2, quantity and quality of thesuspension 12 supplied to theinstallation housing 2 and/or quantity and quality of theinlet air 9 supplied to theinstallation housing 2. - In the cleaning method and/or in the
feedback control 59 the differential pressure DP and or thesystem deviation 62 is preferably filtered with acontrol filter 67, preferably with a lowpass characteristic and/or such that peaks or fluctuations of the differential pressure DP caused by acleaning process 57 and/or the cleaning processes 57 of onecleaning cycle 58 are at least essentially suppressed and/or filtered. - As already explained, the time interval T1 between two successive cleaning processes 57 and/or the time interval T2 between two successive cleaning cycles 58 with several cleaning processes 57 each is each determined by
feedback control 59 which preferably has thecontrol filter 67. - The
control filter 67 is preferably made or designed such that both the pressure peaks which are produced by therespective cleaning process 57, in particular by feed of compressed air, and also pressure deviations based on the differential pressure DP which has changed after the completion of acleaning process 57 are smoothed and/or averaged. - Preferably the
control filter 67 has a three-dB corner frequency or critical frequency of one preferred lowpass characteristic which is smaller than 1/(2×π×time constant), the time constant preferably being greater than the minimum time interval T1, the minimum time interval T2 and/or greater than 1 s, preferably greater than 2 s or 4 s, in particular greater than 5 s. Alternatively or additionally the time constant is preferably smaller than the sum of the time intervals T1 of the cleaning processes 57 of onecleaning cycle 58, less than 30 s, preferably less than 25 s, especially preferably less than 20 s or 15 s. Thecontrol filter 67 can however have a filter characteristic other than a lowpass characteristic, its being preferred that it is made to smooth deviations of the differential pressure DP which have been caused by cleaning processes 57. - The differential pressure DP or the difference between the differential pressure DP and rated differential pressure SP in the sense of this invention is then regarded as smoothed when the deviations caused by or in a
cleaning process 57 are reduced or damped by more than 10%, preferably more than 20%, in particular more than 30% or 40%. - In one especially preferably embodiment the
feedback control 59 is designed such that thecontrol filter 67 damps frequencies above 10 Hz, preferably above 5 Hz, in particular above 2 Hz or 1 Hz, by more than 50%. -
FIG. 9 shows a schematic of the pressure P as a function of the time T in the suggested cleaning method according to a first version of the method. - In the illustrated cleaning method preferably five filter sections 21 are cleaned by means of one
cleaning process 57 at a time in onecleaning cycle 58, the time intervals T1 between the cleaning processes 57 being changed each time. - In the illustrated example the time intervals T1 between the cleaning processes 57 become smaller with increasing clogging or fouling of the filter sections 21, in particular of the
filter cloth 50 and/or with time. - Preferably the time at which a
cleaning process 57 is completed or takes place is less than 10 s, in particular less than 5 s, especially preferably less than 2 s. Quite especially preferably the time of onecleaning process 57 is at least essentially 1 s. - Preferably the time for one
cleaning process 57 is less than the time which cleaned particles, in particular the suspension dust and/or thefilter cake 32 requires or require to travel or fall out of the immediate suction area of the respective filter section 21 during thecleaning process 57. - In particular during and/or after one
cleaning process 57 refiltration of particles cleaned by thecleaning process 57 is prevented, avoided or reduced. - Preferably the time intervals T1 between the cleaning processes 57 are limited with a maximum value and/or a minimum value, preferably the maximum value and/or the minimum value being specified exogenously to the
feedback control 59 and/or the cleaning method. - Especially preferably the maximum value is less than 500 s, in particular less than 400 s, especially preferably less than 300 s, and/or the minimum value is more than 5 s, in particular more than 10 s, especially preferably more than 15 s.
- Preferably the differential pressure DP rises during filtration by means of the filter 19, in particular when a
cleaning process 57 is not taking place. - In the illustrated characteristic the differential pressure DP increases preferably at least essentially linearly with the time T or the difference between the differential pressure DP and the rated differential pressure SP decreases essentially linearly with the time T. But other curve characteristics are also possible.
- A
cleaning process 57 is preferably triggered when the differential pressure DP reaches the rated differential pressure SP, exceeds it and/or approaches it. In particular acleaning process 57 is triggered depending on the differential pressure DP, thesystem deviation 62 and/or on the preferably previous time interval T1 and/or the time interval T2. Especially preferably the controller of thefeedback control 59 determines the instant of triggering of acleaning process 57 or the start of a cleaningcycle 58. - Preferably the differential pressure DP drops during the
cleaning process 57 and/or by thecleaning process 57. In particular the difference between the differential pressure DP and the rated differential pressure SP increases during thecleaning process 57 and/or by thecleaning process 57. - As shown in
FIG. 9 , the differential pressure DP rises again after completion of thecleaning process 57 or the difference between the differential pressure DP and the rated differential pressure SP decreases. - Especially preferably the differential pressure DP after cleaning or after one
cleaning process 57 rises linearly and/or at least essentially as before cleaning or acleaning process 57. But other curve characteristics are also possible, in particular in which the gradient of the differential pressure DP increases with the time T and/or with the number of triggered cleaning processes 57. - Depending on the controller of the
feedback control 59, after afirst cleaning process 57 anothercleaning process 57 is triggered, in particular when the differential pressure DP again reaches, exceeds and/or approaches the rated differential pressure SP. - Preferably the differential pressure DP drops in a
cleaning process 57 at least essentially to the same value as in theprevious cleaning process 57 or the differential pressure DP after successive cleaning processes 57 is at least essentially the same. - As
FIG. 9 illustrates, the differential pressure DP which prevails immediately after completion of acleaning process 57 increases with the time T. - In particular the time until the differential pressure DP reaches the rated differential pressure SP, exceeds it and/or approaches the rated differential pressure SP decreases with the time T.
- The time interval T1 between two successive cleaning processes 57, in particular between the start of two successive cleaning processes 57 and/or the end of two successive cleaning processes 57 and/or the end of one temporarily and the start of a following
cleaning process 57 becomes preferably at least essentially exponentially smaller preferably during filtration by means of the filter 19 and/or with the time T. - Especially preferably with the suggested cleaning method the time interval T1 and/or the time interval T2 is adjusted and/or used as a controlled variable 60 or controlled
variables 60 in thefeedback control 59. - In particular the time interval T1 and/or the time interval T2 is/are used as the manipulated variable 64 or manipulated
variables 64 in thefeedback control 59 or in the cleaning method. - Especially preferably the time intervals T1 and T2 are not directly derived from the differential pressure DP or the comparison of the differential pressure DP to the rated differential pressure SP. It is preferred that the time interval T1 and the time interval T2 are computed, defined or determined by the
feedback control 59, especially preferably by means of thecontrol apparatus 29. - In the illustrated curve characteristic all five filter sections 21 are cleaned in one
cleaning cycle 58. Preferably after the end of the illustratedcleaning cycle 58 one following cleaning cycle 58 (not shown) begins. -
FIG. 10 shows a schematic representation of the pressure P as a function of the time T in the suggested cleaning method according to a second version of the method, in particular the time interval T1 being at least essentially constant within onecleaning cycle 58. - Preferably one
cleaning process 57 is triggered at the start of therespective cleaning cycle 58 when the differential pressure DP reaches the rated differential pressure SP, exceeds it and/or approaches the rated differential pressure SP. - Preferably the time interval T1 between successive cleaning processes 57 of one
cleaning cycle 58 is changed in particular by means of the above explainedfeedback control 59 and/or for theentire cleaning cycle 58 is fixed at an at least essentially constant value. In particular the subsequent cleaning processes 57 take place within the cleaningcycle 58 regardless of the differential pressure SP and/or the rated differential pressure SP and/or after the time interval T1. - The time interval T1 between successive cleaning processes 57 within one
cleaning cycle 58 is preferably changed and/or fixed before and/or at the start of the cleaningcycle 58, preferably by means of thefeedback control 59 and/or is held constant at the previously established value during theentire cleaning cycle 58. - As
FIG. 10 shows, in this version of the method the differential pressure DP which prevails at the start of onecleaning process 57 and/or at the end of onecleaning process 57 can drop and/or rise within onecleaning cycle 58. - In the illustrated example the filter 19 preferably has three filter sections 21 and/or one
cleaning cycle 58 encompasses three cleaning processes 57. - If all filter sections 21 in one
cleaning cycle 58 are cleaned by means of the cleaning processes 57, the cleaningcycle 58 is ended. - Preferably after completion of one
cleaning cycle 58 separated in time by the time interval T2 a further following cleaningcycle 58 starts, in particular the time interval T2 of successive cleaning cycles 58 being changed. - Preferably another cleaning
cycle 58 starts with the triggering of acleaning process 57. As shown inFIG. 10 , the time intervals T1 in thesecond cleaning cycle 58 are changed compared to thefirst cleaning cycle 58. - Preferably the time intervals T1 from cleaning
cycle 58 to cleaningcycle 58 and/or with the time T become smaller. But other variations are also possible. - Preferably the differential pressure DP with time T increasingly approaches the rated differential pressure SP.
- When the differential pressure DP can no longer be adjusted by means of the cleaning method and/or the
feedback control 59, in particular when the differential pressure DP exceeds the rated differential pressure SP by a previously fixed value and/or the time interval T1 and/or the time interval T2 reaches a previously established minimum value, the filter 19 is preferably completely cleaned, in particular wet, preferably theinstallation 1 and/or thefilter system 17 being shut down and/or the filtration being adjusted by means of the filter 19. - Preferably the time intervals T1 are changed such that the number of cleaning processes 57 is minimized and/or the time until necessary wet cleaning of the filter 19 is maximized.
- Individual aspects and features of the different embodiments and versions of the method can be implemented independently of one another, but also in any combination with one another.
-
- 1 installation
- 2 installation housing
- 3 housing inlet
- 4 housing outlet
- 5 inlet air region
- 6 spray region
- 7 filter region
- 8 dome region
- 9 inlet air
- 10 perforated bottom
- 11 suspension tank
- 12 suspension
- 13 suspension pump
- 14 suspension line
- 15 nozzle
- 16 Wurster pipe
- 17 filter system
- 18 connecting device
- 19 filter
- 20 cleaning device
- 21 filter sections
- 22 filter cartridge
- 23 raw gas
- 24 filter inlet
- 25 filter outlet
- 26 clean gas
- 27 exhaust air
- 28 storage apparatus
- 29 control apparatus
- 30 pressure sensor
- 31 valve
- 32 filter cake
- 33 side wall
- 34 opening
- 35 first section (with openings)
- 36 second section (free of openings)
- 37 third section (cylindrical)
- 38 flange union
- 39 clamp union
- 40 groove
- 41 seal
- 42 inside (side wall)
- 43 outside (side wall)
- 44 piston
- 45 cone seat
- 46 spring
- 47 valve chamber
- 48 manifold
- 49 hole
- 50 filter cloth
- 51 storage unit
- 52 ring reservoir
- 53 pipe segment
- 54 compressed air line
- 55 control air line
- 56 penetration
- 57 cleaning process
- 58 cleaning cycle
- 59 feedback control
- 60 controlled variable
- 61 reference variable
- 62 system deviation
- 63 PID controller
- 64 manipulated variable
- 65 controlled system
- 66 influencing quantity
- 67 control filter
- A outside cross section
- E plane
- H major axis
- L longitudinal axis
- Q internal cross section
- Q1 largest internal cross section
- Q2 smallest internal cross section
- P pressure
- DP differential pressure
- SP rated differential pressure
- T time
- T1 time interval (cleaning process)
- T2 time interval (cleaning cycle)
- W1 first angle
- W2 second angle
- W3 third angle
Claims (28)
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
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DE202014008509 | 2014-10-28 | ||
DE202014008509.9 | 2014-10-28 | ||
EP14003655.9 | 2014-10-28 | ||
EP14003655 | 2014-10-28 | ||
PCT/EP2015/073793 WO2016066427A2 (en) | 2014-10-28 | 2015-10-14 | Cleaning method, control device and connection device |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/EP2015/073793 A-371-Of-International WO2016066427A2 (en) | 2014-10-28 | 2015-10-14 | Cleaning method, control device and connection device |
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US18/107,693 Division US20230226478A1 (en) | 2014-10-28 | 2023-02-09 | Cleaning method, control apparatus and connecting device |
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US20180236386A1 true US20180236386A1 (en) | 2018-08-23 |
Family
ID=54325540
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US15/522,960 Abandoned US20180236386A1 (en) | 2014-10-28 | 2015-10-14 | Cleaning method, control apparatus and connecting device |
US18/107,693 Pending US20230226478A1 (en) | 2014-10-28 | 2023-02-09 | Cleaning method, control apparatus and connecting device |
Family Applications After (1)
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US18/107,693 Pending US20230226478A1 (en) | 2014-10-28 | 2023-02-09 | Cleaning method, control apparatus and connecting device |
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US (2) | US20180236386A1 (en) |
EP (2) | EP3862065B1 (en) |
JP (2) | JP6728157B2 (en) |
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CN112843890A (en) * | 2020-12-22 | 2021-05-28 | 重庆纤维研究设计院股份有限公司 | Air filter for passive room |
US20210245083A1 (en) * | 2020-02-12 | 2021-08-12 | Carl Freudenberg Kg | Filter module comprising sensor and method for determining the state of a filter element |
US20220097010A1 (en) * | 2020-09-29 | 2022-03-31 | Boe Technology Group Co., Ltd. | Gas-solid separation structure, feeding device and electrochemical deposition apparatus |
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JP2019135333A (en) * | 2018-02-05 | 2019-08-15 | セイコーエプソン株式会社 | Collection device, collection method and fiber raw material regenerator |
GB2592267A (en) * | 2020-02-24 | 2021-08-25 | Altair Uk Ltd | Pulse nozzle for filter cleaning systems |
CN114288771A (en) * | 2022-01-24 | 2022-04-08 | 无锡市华天环保科技有限公司 | Filter cartridge dust remover with filter element convenient to detach and clean |
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US20210245083A1 (en) * | 2020-02-12 | 2021-08-12 | Carl Freudenberg Kg | Filter module comprising sensor and method for determining the state of a filter element |
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US20220097010A1 (en) * | 2020-09-29 | 2022-03-31 | Boe Technology Group Co., Ltd. | Gas-solid separation structure, feeding device and electrochemical deposition apparatus |
CN112342336A (en) * | 2020-11-04 | 2021-02-09 | 中国科学院力学研究所 | Converter flue gas full-dry type dust collection waste heat recovery device and method |
CN112843890A (en) * | 2020-12-22 | 2021-05-28 | 重庆纤维研究设计院股份有限公司 | Air filter for passive room |
Also Published As
Publication number | Publication date |
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US20230226478A1 (en) | 2023-07-20 |
WO2016066427A3 (en) | 2016-06-23 |
EP3862065B1 (en) | 2023-11-29 |
EP3862065A1 (en) | 2021-08-11 |
EP3212306B1 (en) | 2021-04-07 |
JP7080926B2 (en) | 2022-06-06 |
JP6728157B2 (en) | 2020-07-22 |
EP3212306A2 (en) | 2017-09-06 |
JP2020182941A (en) | 2020-11-12 |
WO2016066427A2 (en) | 2016-05-06 |
JP2017533096A (en) | 2017-11-09 |
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