USRE24275E - Multicell - Google Patents

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USRE24275E
USRE24275E US24275DE USRE24275E US RE24275 E USRE24275 E US RE24275E US 24275D E US24275D E US 24275DE US RE24275 E USRE24275 E US RE24275E
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water
filter
cells
pipe
flow
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D24/00Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
    • B01D24/46Regenerating the filtering material in the filter
    • B01D24/4631Counter-current flushing, e.g. by air
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D24/00Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
    • B01D24/002Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with multiple filtering elements in parallel connection
    • B01D24/005Filters being divided into a plurality of cells or compartments
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D24/00Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
    • B01D24/02Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration
    • B01D24/10Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration the filtering material being held in a closed container
    • B01D24/14Downward filtration, the container having distribution or collection headers or pervious conduits

Definitions

  • This invention relates to multicell filter-r apparatus.
  • the invention is particularly useful in connection withasingle large horizontal filter employing partitions for forming compartments therein.
  • An object of this invention is to meet the above need and to provide a structure in which a very limited amount of water fiow may be employed eifectively in backwashing a selected cell or cells of the filter.
  • a further object is to provide a structure in which all the advantages of a large horizontal compartmented filter may be enjoyed while permitting a very small flow to be employed for backwashing through the selected. washing of indi- Re. 24,275 Reissued Feb. 12, 1957 vidual cells.
  • a still further object is to provide insuch a filter structure an: underdrain system in which it is impossible to produce a damaging difierence in pressure across. the partitions.
  • Yet another object is to provide in such a multicell' horizontal filter structure anunderdrain plate which is common to all of: the cells and in which the only pressure differential that can be developed across the partitions-is that head loss produced by flow through the filter bed during service and through the underdrain plate during backwash.
  • FIG. 1 is a side view in elevation of filter apparatus embodying my invention
  • Fig. 2 an enlarged longitudinal sectional view of the compartmented filter
  • Big, 3. a transverse sectional view
  • Fig. 4 an enlargeddetail sectional view showing the baffle plate structure employed with the underdrain plate.
  • 10 designates a largehori- Zontal filter vessel or tank supported upon standards 11. Extending transversely of the filter vessel. are spaced I beams 12, as shown more clearly in Fig. 2.
  • the filter is provided with outwardly-dished'ends 13'. Supported'upon.
  • the I beams i2 is an underdrain plate 1'4 which divides the interior of the vessel into an upper. filter. space 115. and. a lower drain or inlet chamber 16;
  • the drain plate. 14 is provided throughout with spaced openings 17 es.- tablishing cornmunicationbetween the lower drain chamber 16' and the upper chamber 15; I prefer to employ with eachv of the openings 17 a lower plate 18. and an upper baffle plate 19 which permits the water.
  • any suitable means may be provided for. the inflow and outflow of water.
  • the chamber 16 below the plate 14. is provided with an outlet fitting 27' to which is connected at. valve-controlled pipe 28, as shown more clearly in Fig. 1..
  • I provide a pipe 29 leading from apump. 3t) and connected with pipe 31 adapted to feed. water. to the compartment 26; pipe 3.2. adapted to. feed water to the compartment 25, pipe. 33 adapted to feed. water to the compartment 24, andv pipe. 34 adapted. to. feed. Water to the compartment 23.
  • the line 29 may come from any suitable source of supply, and the pump 30 is herein set out. merely as illustrative ot a. source.
  • Each of the pipes. 31,, 32,. 33. and 34 is provided with a control valve 35 and is connected by a T fitting 36 to a pipe 37 leading into the interior of the compartment.
  • the T fitting 36 also connects pipe 31 to a valve-controlled discharge pipe 38 leading the water to a drain. 39 from which water drains away through the. channel. 40,. as shown more. clearly in Fig. l.
  • drain pipe 38 is indicated by the numeral 41.
  • the pipe 37 leading into each. of the compartments preferably joins a longitudinally-extending spray pipe 42 having spaced overflow ports 43.
  • the pipe. 42 in each compartment is supported by brackets 44 and suspension straps 45 carried thereby.
  • the partitions 20, 21 and 22 are preferably braced by vertical members 46, as shown more clearly in Figs. 2 and 3. It will be understood that the structure may be varied widely with respect to the fabrication of the compartments and the supporting means for the partitions, drain plate, etc.
  • the filter structure resulting from the use of the parts hereinbefore described, there are provided four separate compartments 23, 24, 25 and 26, with the walls thereof imperforate except with respect to the bottom wall which is formed by the drain plate 14.
  • the drain plate is provided throughout with a large number of spaced openings 17 which thus provide free flow between the several compartments and the unitary or unobstructed chamber or passage 16 therebelow.
  • the passage 16 thus provides a common chamber communicating with each of the compartments.
  • the backwash is with treated water under pressure from the system storage, for example, where the filter is treating a municipal supply and there is an elevated tank close enough to supply water at a rate sufi'icient to backwash one cell at a time without lowering the pressure in the system.
  • the backwash is with treated water supplied from a pump from a storage reservoir.
  • a pump from a storage reservoir.
  • An example would be where the filter water is being discharged into a reservoir at an elevation too low to give sufficient pressure for backwashing.
  • a separate storage reservoir is provided at the plant for the express purpose of supplying backwash water.
  • each cell is backwashed with filtered water from the other cells.
  • This method would be in the operation of a multicell filter for filtration of swimming pool water. Here the only water available for backwashing is supplied by the recirculating pump. Enough cells must be provided to get the area down to the point Where the recirculating pump will supply adequate flow to backwash each cell. This system is also used in industries where space will not allow construction of storage tanks large enough for the backwash supply.
  • This method would be a combination of methods (1) and (3), and it is used where it is determined that there is not enough water available from storage and it is necessary to provide additional water from the source of supply.
  • the water is pumped through pipe 29 through, for example, pipes 31, 33 and 34, so as to filter through the filter beds in compartments 23, 24 and 26.
  • the valve 41 of the drain pipe 38 leading from these cells or compartments is closed.
  • the valve 35 of pipe 32 is closed and the valve 41 or drain pipe 38 therebelow is opened.
  • valve 28 in the withdrawal pipe 27 is closed. The incoming water passing through the compartments 23, 24 and 26 fills the chamber 16 and then passes upward-1y through the openings 17 in the underdrain plate 14 into the filter bed 19a in compartment 25 and backwashes the filter.
  • an extremely large single horizontal filter with any desired number of compartments may be employed for effective service filtration while at the same time permitting selective backwashing of one or more cells at a time while employing all of the water flow for this purpose. It is not necessary to have all the flow required for backwashing all of the cells at one time, but instead, backwashing may be limited to a single cell and the entire available flow may be utilized for the backwashing of this selected cell or cells.
  • baffle plates By employing the baffle plates to provide free upward flow of the water under the baffle plate, there it no tendency for the system to clog and the multicell operation is effective. There is no clogging and no backwash pressures which will bulge the plates, etc.
  • a horizontally-elongated tank partitions arranged within said tank to provide a plurality of separate, horizontally-spaced, vertically-extending filter cells within said tank, said cells being adapted to receive separate beds of filtering material, a raw water supply pipe, separate pipes connecting the upper portion of each of said cells with said raw water supply pipe,
  • shut-01f valve in each of said cell connecting pipes separate drain pipes extending from said cell connecting pipes on the cell side of each of said shut-off valves, separate shut-oft valves in each of said drain pipes, and a common water collection means extending across the bottom portion of said tank and providing a passage therein in open communication with the lower portion of each of said cells, whereby any one of said cells can be automatically backwashed with filtered water during normal filtration operations by simply closing the shut-oil? valve in the connecting pipe to said cell and opening the shut-off valve in the drain pipe from the same connecting pipe.
  • said water collecting means includes an underdrain plate extending beneath each of said cells for the length of said tank and being spaced upwardly from the bottom of said tank to provide said passage therebetween, said underdraiu plate being provided with a plurality of laterally and longitudinally distributed openings therethrough, said openings providing for open communication between the lower portion of each of said cells and said passage therebeneath.
  • a horizontally-elongated tank partitions arranged within said tank to provide a plurality of separate, horizontally-spaced, vertically-extending filter cells within said tank, said cells being adapted to receive separate beds of filtering material, a raw water supply pipe, separate pipes connecting the upper portion of each of said cells with said raw water supply pipe, a separate shat-0 9 valve in each of said cell connecting pipes, separate drain.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Filtration Of Liquid (AREA)

Description

Feb. 12,195! J. P. LAWLOR) MULTICELL FILTER APPARATUS Original Filed June 27, v1952 United States Patent O MULTICELL FILTER APPARATUS Joseph P. Lawlor, Ames, Iowa, assignorto General Filter Company, Ames, Iowa,.a corporation of-Iowa Original No. 2,754,971, dated July 17, 1956, Serial No.
296,008, June 27, 1952. Application for reissue November 15, 1956, Serial No. 623,275
3 Claims. (Cl. 210-144) Matter enclosed in heavy brackets appears in the original patent but forms no part of this. reissue specification; matter printed in italics indicates the additions made by reissue.
This invention relates to multicell filter-r apparatus. The invention is particularly useful in connection withasingle large horizontal filter employing partitions for forming compartments therein.
This application is a. reissue of Patent No. 2,754,971, which issued July 17, 1956, for "Multicell Filter Apparatus.
For many pressure filtering applications, asinglelarge horizontal filteris an ideal solution from the standpoint of simplicity and low initial cost. Suchfilters, however, have a definite drawback in the very large flow required for backwashing.
When it is impractical or impossible to. obtain or dis? pose of enough water to-backwash. such a large single filter, the practice has been to providethe: required filter areas. in the; form of several smaller units, each of the units being av complete; filter in itself.
It has long been desired to have a single large horizontal filter divided into a number of. cells, each of which can be backwashed adequately with. the water flow available for the purpose, and various methods of cornpartmentinghorizontal filters have been tried by filter manufacturers. Complete isolationof the cells by means of partitions. constructed of standard dished. heads has proved to be satisfactory in so far as withstanding the pressure is concerned. This method, however, has a disadvantage in that the filter bed against the convex side of the partition does not, operate well due to the shape of the partition. Further, the fabrication is. difiicult and there is little or no saving in cost over the use of an equal number of individual filters.
Another system has been employedwhichpermits the use of fiat plate partitions by providing for pressure equalization between the cells. This is accomplished. by providing an opening at the top center of the. partition large enough to pass the full flow of water available at very low head loss across the opening; In: spite of this design, care is required to insure that there; will be no great pressure differential. across the partition. Further, the backwash water moves through the openings from the cell being backwashed, and deposits material on the cells that have been cleaned.
There has long been a need for a multicell horizontal filter in which backwashing can be effected readily through selected cells by employing a limited flow of water.
An object of this invention is to meet the above need and to provide a structure in which a very limited amount of water fiow may be employed eifectively in backwashing a selected cell or cells of the filter. A further object is to provide a structure in which all the advantages of a large horizontal compartmented filter may be enjoyed while permitting a very small flow to be employed for backwashing through the selected. washing of indi- Re. 24,275 Reissued Feb. 12, 1957 vidual cells. A still further object is to provide insuch a filter structure an: underdrain system in which it is impossible to produce a damaging difierence in pressure across. the partitions. Yet another object is to provide in such a multicell' horizontal filter structure anunderdrain plate which is common to all of: the cells and in which the only pressure differential that can be developed across the partitions-is that head loss produced by flow through the filter bed during service and through the underdrain plate during backwash. Other specific objects and advantages will appear as the specification proceeds.
The invention is shown in an illustrative embodiment by the accompanying drawing, in which- Figure 1 is a side view in elevation of filter apparatus embodying my invention; Fig. 2, an enlarged longitudinal sectional view of the compartmented filter; Big, 3., a transverse sectional view; and Fig. 4, an enlargeddetail sectional view showing the baffle plate structure employed with the underdrain plate.
In the illustration given, 10 designates a largehori- Zontal filter vessel or tank supported upon standards 11. Extending transversely of the filter vessel. are spaced I beams 12, as shown more clearly in Fig. 2. The filter is provided with outwardly-dished'ends 13'. Supported'upon. the I beams i2 is an underdrain plate 1'4 which divides the interior of the vessel into an upper. filter. space 115. and. a lower drain or inlet chamber 16; The drain plate. 14 is provided throughout with spaced openings 17 es.- tablishing cornmunicationbetween the lower drain chamber 16' and the upper chamber 15; I prefer to employ with eachv of the openings 17 a lower plate 18. and an upper baffle plate 19 which permits the water. to flow upwardly and then laterally under the filter bed 1921,. as shown more clearly in Fig. 4. Theunderdrain. plate and the baffle plate structures therefor are showni'n greater. detail in my. Patent 2,594,568, dated April. 29,, 19.5.2.
Extendingupwardly from the dnainplate 114 at. spaced. intervals are three partition walls 20, 21 and 22. It will be understood that any number of partition. walls. may,- be employed, and that theuse of. three. partitions herein is merely illustrative of the invention. By the use ofj'the partition walls 20, 2-1 and 22. and the dished ends 13. of thefilter, I provide four compartments, as indicated by thenumerals 23, 2.4, 25' and 26.
Any suitable means may be provided for. the inflow and outflow of water. In the illustration. given, the chamber 16 below the plate 14. is provided with an outlet fitting 27' to which is connected at. valve-controlled pipe 28, as shown more clearly in Fig. 1.. For the. in.- flow of water, I provide a pipe 29 leading from apump. 3t) and connected with pipe 31 adapted to feed. water. to the compartment 26; pipe 3.2. adapted to. feed water to the compartment 25, pipe. 33 adapted to feed. water to the compartment 24, andv pipe. 34 adapted. to. feed. Water to the compartment 23. It will be understood that. the water supplied through, the line 29 may come from any suitable source of supply, and the pump 30 is herein set out. merely as illustrative ot a. source.
Each of the pipes. 31,, 32,. 33. and 34 is provided with a control valve 35 and is connected by a T fitting 36 to a pipe 37 leading into the interior of the compartment. The T fitting 36 also connects pipe 31 to a valve-controlled discharge pipe 38 leading the water to a drain. 39 from which water drains away through the. channel. 40,. as shown more. clearly in Fig. l. The valve. controlling. the.
drain pipe 38 is indicated by the numeral 41.
The pipe 37 leading into each. of the compartments preferably joins a longitudinally-extending spray pipe 42 having spaced overflow ports 43. The pipe. 42 in each compartment is supported by brackets 44 and suspension straps 45 carried thereby.
The partitions 20, 21 and 22 are preferably braced by vertical members 46, as shown more clearly in Figs. 2 and 3. It will be understood that the structure may be varied widely with respect to the fabrication of the compartments and the supporting means for the partitions, drain plate, etc.
In the filter structure resulting from the use of the parts hereinbefore described, there are provided four separate compartments 23, 24, 25 and 26, with the walls thereof imperforate except with respect to the bottom wall which is formed by the drain plate 14. The drain plate is provided throughout with a large number of spaced openings 17 which thus provide free flow between the several compartments and the unitary or unobstructed chamber or passage 16 therebelow. The passage 16 thus provides a common chamber communicating with each of the compartments.
Operation In the operation of the apparatus for service, water is passed through the line 29 into the several compartments and it flows through the filter bed, underdrain plate 14, and thence is discharged through the outlet pipes 27 and 28 to its desired destination. Since the operation of the filter for service is well understood and involves no special problems, it is believed unnecessary to describe further the filtering operation.
The main problem, as stated above, has had to do with the backwashing of the cells or compartments in the filter, and this problem centers about the fact that the required flow of water is limited. It is desired to wash the large compartmented filter with as little :1 water flow requirement as possible. Various methods for handling the backwash through the multicell filter shown may be employed. For example, the following four methods may be described and the particular method used will depend upon the design requirements of the plant in question:
(1) (In this method the backwash is with treated water under pressure from the system storage, for example, where the filter is treating a municipal supply and there is an elevated tank close enough to supply water at a rate sufi'icient to backwash one cell at a time without lowering the pressure in the system.
(2) In this method, the backwash is with treated water supplied from a pump from a storage reservoir. An example would be where the filter water is being discharged into a reservoir at an elevation too low to give sufficient pressure for backwashing. Occasionally, a separate storage reservoir is provided at the plant for the express purpose of supplying backwash water.
(3) In this method each cell is backwashed with filtered water from the other cells. One example of this method would be in the operation of a multicell filter for filtration of swimming pool water. Here the only water available for backwashing is supplied by the recirculating pump. Enough cells must be provided to get the area down to the point Where the recirculating pump will supply adequate flow to backwash each cell. This system is also used in industries where space will not allow construction of storage tanks large enough for the backwash supply.
(4) This method would be a combination of methods (1) and (3), and it is used where it is determined that there is not enough water available from storage and it is necessary to provide additional water from the source of supply.
In the specific example where it is desired to backwash cells separately, as, for example, using filtered water such as water sent to a swimming pool, the water is pumped through pipe 29 through, for example, pipes 31, 33 and 34, so as to filter through the filter beds in compartments 23, 24 and 26. In each instance, the valve 41 of the drain pipe 38 leading from these cells or compartments is closed. In the case of cell or compartment 25, the valve 35 of pipe 32 is closed and the valve 41 or drain pipe 38 therebelow is opened. Also, valve 28 in the withdrawal pipe 27 is closed. The incoming water passing through the compartments 23, 24 and 26 fills the chamber 16 and then passes upward-1y through the openings 17 in the underdrain plate 14 into the filter bed 19a in compartment 25 and backwashes the filter. The water level rises upwardly through the filter and above the pipe 42 and then passes outwardly through pipe 42 and the pipe 37 leading from compartment 25 and thence downward through the pipe 38 to the drain 39. Thus, with a relatively small flow of water, the filter in compartment 25 is backwashed. By manipulating the valves 35 and 41 for the difierent compartments, it is thus possible to backwash each of the filters one at a time while employing the entire water flow forelfecting such backwashing.
From the foregoing it will be noted that an extremely large single horizontal filter with any desired number of compartments may be employed for effective service filtration while at the same time permitting selective backwashing of one or more cells at a time while employing all of the water flow for this purpose. It is not necessary to have all the flow required for backwashing all of the cells at one time, but instead, backwashing may be limited to a single cell and the entire available flow may be utilized for the backwashing of this selected cell or cells.
In the operation described, the use of the non-clogging and non-restrictive uuderdrain pipe and the common passage 16 therebelow accounts for much of the successful operation. If an underdrain plate is employed which can clog and cause flow to be restricted, it will be possible to produce a damaging pressure differential across the cell partitions. Obviously, separate underdrains for the individual cells would cause the worse condition. In those systems where small nozzles are provided and in which header lateral systems are used, the small nozzles and the laterals become clogged with scale or debris from the mains, and as soon as the clogging occurs the backwash operation produces large difierentials.
By employing the baffle plates to provide free upward flow of the water under the baffle plate, there it no tendency for the system to clog and the multicell operation is effective. There is no clogging and no backwash pressures which will bulge the plates, etc.
While in the foregoing specification I have shown a specific structure in considerable detail for the purpose of illustrating the invention, it will be understood that such details of structure may be varied widely by those skilled in the art without departing from the spirit of my invention.
I claim:
1. In a water filtration apparatus, a horizontally-elongated tank, partitions arranged within said tank to provide a plurality of separate, horizontally-spaced, vertically-extending filter cells within said tank, said cells being adapted to receive separate beds of filtering material, a raw water supply pipe, separate pipes connecting the upper portion of each of said cells with said raw water supply pipe,
a separate shut-01f valve in each of said cell connecting pipes, separate drain pipes extending from said cell connecting pipes on the cell side of each of said shut-off valves, separate shut-oft valves in each of said drain pipes, and a common water collection means extending across the bottom portion of said tank and providing a passage therein in open communication with the lower portion of each of said cells, whereby any one of said cells can be automatically backwashed with filtered water during normal filtration operations by simply closing the shut-oil? valve in the connecting pipe to said cell and opening the shut-off valve in the drain pipe from the same connecting pipe.
2. The apparatus of claim 1 wherein said water collecting means includes an underdrain plate extending beneath each of said cells for the length of said tank and being spaced upwardly from the bottom of said tank to provide said passage therebetween, said underdraiu plate being provided with a plurality of laterally and longitudinally distributed openings therethrough, said openings providing for open communication between the lower portion of each of said cells and said passage therebeneath.
3. In a water filtration apparatus, a horizontally-elongated tank, partitions arranged within said tank to provide a plurality of separate, horizontally-spaced, vertically-extending filter cells within said tank, said cells being adapted to receive separate beds of filtering material, a raw water supply pipe, separate pipes connecting the upper portion of each of said cells with said raw water supply pipe, a separate shat-0 9 valve in each of said cell connecting pipes, separate drain. pipes communicating with the upper portions of each of said cells, separate shut-017 valves in each of said drain pipes, and a common water collection means extending across the bottom portion of said tank and providing a passage therein in open communication with the lower portion of each of said cells, whereby any one of said cells can be automatically backwashed with filtered water during normal filtration operations by simply closing the shat-017 valve in the connecting pipe to said cell and opening the shat-ofi valve in the drain pipe from the same cell.
References Cited in the file of this patent or the original patent UNITED STATES PATENTS
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2935195A (en) * 1956-11-13 1960-05-03 Nat Tank Co Water filters
US3286842A (en) * 1962-07-03 1966-11-22 Jong George E De Filter apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2935195A (en) * 1956-11-13 1960-05-03 Nat Tank Co Water filters
US3286842A (en) * 1962-07-03 1966-11-22 Jong George E De Filter apparatus

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