US2787378A - Slurry type liquid treating apparatus - Google Patents

Slurry type liquid treating apparatus Download PDF

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US2787378A
US2787378A US290042A US29004252A US2787378A US 2787378 A US2787378 A US 2787378A US 290042 A US290042 A US 290042A US 29004252 A US29004252 A US 29004252A US 2787378 A US2787378 A US 2787378A
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slurry
arms
rotation
blanket
partition
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US290042A
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Everett M Battey
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5281Installations for water purification using chemical agents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0018Separation of suspended solid particles from liquids by sedimentation provided with a pump mounted in or on a settling tank
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/003Sedimentation tanks provided with a plurality of compartments separated by a partition wall
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0039Settling tanks provided with contact surfaces, e.g. baffles, particles
    • B01D21/0042Baffles or guide plates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/02Settling tanks with single outlets for the separated liquid
    • B01D21/08Settling tanks with single outlets for the separated liquid provided with flocculating compartments
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24Feed or discharge mechanisms for settling tanks
    • B01D21/2405Feed mechanisms for settling tanks
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24Feed or discharge mechanisms for settling tanks
    • B01D21/2427The feed or discharge opening located at a distant position from the side walls

Definitions

  • This invention relates to slurry type liquid treating apparatus and process. More particularly it relates to apparatus and process of this general type wherein a mixture of slurry, liquid to be treated, and reagent is discharged from a central mixing zone or chamber through rotating arms across the outer portion of the tank. in such an apparatus the distributing arms rotate below a suspended slurry blanket, or pool through which a throughput portion of the liquid discharged from the arms liows upwardly toward a treated liquid outlet, Whereas the balance of the liquid discharged from the anus flows inwardly across the bottom of the tank and returns to the mixing zone.
  • the arms. are rotated at a relatively high speed, and it, has been usual to provide discharge orifices in the arms which direct the flow vertically downwardly toward the bottom of the tank to avoid disturbance of the blanket; and to continuously sweep the bottom free of deposits.
  • the rotation of arms with downwardly discharging orifices has a. marked tendency of causing the slurry blanket above the arms to rotate in the same direction as the arms and at the same speed. This is undesirable and actually nullifies the improved distribution sought by rotation of the arms.
  • Another object is to provide means for controlling the speed and rotation of: a slurry-blanket which can be adjusted to provide any desired speed and direction of blanket rotation.
  • Another object is to provide an. improved distributing arm structure for an apparatus of'the: type mentioned.
  • Another object of the invention istoprovide a rotatable distributing arm discharging downwardly at an'angle to the vertical to provide a tangential velocity component opposite to the; direction of the arm rotation.
  • Another object is to provide a, distributing arm which is rotatable about a vertical axis and can also be rotated about its own horizontal axis.
  • the speed of rotation of the slurry blanket can be controlled, and that rotation of the slurry blanket can be entirely stopped or its direction reversed, by discharging the slurry from the arms at an angle to the vertical so that. there is a tangential velocity component opposite to the direction of arm rotation.
  • the angle of discharge may vary from about 15 to about 45, depending on whether it is desired to merely slow down the rotation of the blanket, to stop it, or to reverse its direction.
  • Figure l is a vertical cross-sectional view of an apparatus utilizing the invention.
  • Figure 2 is an enlarged vertical cross-sectional view of a distributing arm taken along line 22 of Figure .l;
  • Figure 3 is an enlarged vertical sectional view of the adjustable arm mounting of Figure 1.
  • the liquid treating apparatus shown in Figure. 1 comprises. a tank 10, which may have. any suitable shape but is shown for purposes of exemplificationas having a substantially flat bottom 11 and a cylindrical boundary wall 12. Treated liquid overflows intoa launder 13 and is withdrawn through an efiiuent conduit 1 Snitable means for withdrawing excess solids are provided and may take the form of a sludge sump 15 in the bottom 11, and a sludge blow-cit line 16 leading from the sump 15.
  • Axially mounted in the tank 10 is a partition structure 20 comprising an outer partition 21, and an inner partition 22 which may be independently supported or, as
  • the partitions 21 and 22 may have any suitable configuration, but are shown for purposes of illustration as tubular.
  • the lower edges of partitions 21 and 22 are spacedabove the bottom 11 of the tank, and the channel 24 between the partitions is closed at the lower end by a floor 25.
  • the upper edge of the outer partition 21 is above the overflow into the launder 13, and the upper edge of the inner partition is at a lower elevation, thus providing an overflow from the space within the inner partition 22 to the channel 24.
  • the lower part of the outer partition is provided with a plurality of ports 26 symmetrically spaced about the partition 21.
  • a rotor 30 is mounted within the partition structure 20, preferably just above the upper end of the inner partition 22, as shown, and can be rotated by means of a suitable motor-reducer 31.
  • the liquid to be treated and the reagent are introduced into the space Within the partition structure 20 at opposite sides of the rotor 30, as through conduits 32 and 33, respectively, or the liquid to be treated can be introduced into the space within the partition 22 below the rotor, as through a conduit 32a.
  • the latter construction is preferred when the rate of raw water supply varies considerably, as it permits to maintain a constant volume of discharge through the arms 50, and therefore a constant speed of rotation of the slurry blanket, regardless of the rate of raw water flow.
  • a plate 35 may be mounted in any suitable manner between the open lower end of the inner partition 22 and the sump 15 and shelters the sump from the turbulence set up by the return flow of slurry to the inner partition 22.
  • the outer partition 21 is rotatably supported by any suitable means, such as a channel structure 36 surrounding its upper end and riding on rollers 37 journaled in bearings 38.
  • the bearings 38 are supported from a walkway or beam 39 spanning the tank 10.
  • a plurality of guide rollers 40 are provided and are journaled in bearings 41, which also are supported by the beam 39.
  • Any suitable means can be used to rotate the partition 21.
  • an internal ring gear 42 is shown which meshes with a pinion 43 mounted on the shaft of a speed reducer 44, driven by a motor 45.
  • the motor 45 and speed reducer 44 can be mounted on the beam 39. In Figure 1 it is assumed that the partition 21 rotates clockwise.
  • a plurality of hollow distributing arms are equally spaced about the partition 21 to register with the ports 26.
  • the arms 50 extend from the outer partition 21 across the tank 10 and are in hydraulic communication with the channel 24 through the ports 26. Usually at least four arms are used, but in larger tanks six or more arms should be used for good distribution.
  • the arms 50 are provided with discharge means 51, which may be in the form of a continuous slot, as shown on the right hand arm in Figure 1, or of orifices suitably spaced along the length of the arm, as shown on the left hand arm of said figure.
  • the discharge opening or openings are located in the lower portion of the arm 50 and with their center line C at an angle to the vertical center line C of the arm 50 in the direction opposite the direction of arm rotation indicated by the arrow R.
  • I provide means for adjustably mounting the arms 50 on the partition 21.
  • the ports 26 are surrounded by couplings 55, which are welded or otherwise afiixed to the partition 21.
  • Each coupling is machined to provide a shoulder 56 which serves as a stop for the distributing arm which is inserted in the coupling 55.
  • Each coupling is tapped at two places which are apart to permit the insertion of set screws 57, which bear against the arm 50 and hold it fixedly in the selected position.
  • the arm 50 By loosening the screws 57 the arm 50 can be rotated about its axis in the coupling 55 until the slots or orifices 51 are in the correct angular position to obtain the speed and direction of rotation of the slurry blanket desired, and then can be fixed in this position by tightening the screws.
  • the angle from the vertical of the center line of the discharge opening should not be less than about 15 and not more than about 45 and will usually be within the range of from 15 to 30. The choice of the angle depends on the characteristics of the slurry, the speed of the rotor 30 which controls the velocity of the jets discharged from the arms 50, and the speed of rotation of the arms 50 which is controlled by motor-reducer 45--44.
  • a slurry type liquid treating apparatus having a tank which during normal operation contains a slurry blanket and an overlying body of clarified liquid, a central mixing chamber surrounded by a casing separating said mixing chamber from an outer space between said casing and the wall of said tank and conduits having longitudinally aligned discharging distributing openings connected to apertures in the wall of said casing adjacent the bottom of said tank and extending from said casing adjacent to but spaced from the bottom of said tank for approximately the entire distance of the outer space intermediate said tank and said casing, the improvement comprising a collar secured to said casing in registry with each of said apertures and facing the intermediate space between said casing and said tank, each of said collars being dimensioned to surround a conduit, adjustable fastening means carried by each collar for engaging a conduit to maintain it in communication with an associated aperture, each conduit secured in a collar by said adjustable fastening means to position the openings in said conduit at preselected vertical angles whereby slurry mixture conducted to said casing and discharged from said openings for distribution

Description

April 2, 1957 E. M. BATTEY 2,737,373
I SLURRY LIQUID TREATING APPARATUS Filed May 26, 1952 ITIM! SL Y TYPE LIQUID TREATING APPARATUS Everett M. liattey, Falls Church, Va., assignor, by mesne assignments, to the United States of America as represented by the Secretary of the Army Application May 26, B52, Serial No. 290,tl42
1 Claim. (Cl. 210-512) This invention relates to slurry type liquid treating apparatus and process. More particularly it relates to apparatus and process of this general type wherein a mixture of slurry, liquid to be treated, and reagent is discharged from a central mixing zone or chamber through rotating arms across the outer portion of the tank. in such an apparatus the distributing arms rotate below a suspended slurry blanket, or pool through which a throughput portion of the liquid discharged from the arms liows upwardly toward a treated liquid outlet, Whereas the balance of the liquid discharged from the anus flows inwardly across the bottom of the tank and returns to the mixing zone.
in apparatus of this type. the arms. are rotated at a relatively high speed, and it, has been usual to provide discharge orifices in the arms which direct the flow vertically downwardly toward the bottom of the tank to avoid disturbance of the blanket; and to continuously sweep the bottom free of deposits. In practice it has been found that the rotation of arms with downwardly discharging orifices has a. marked tendency of causing the slurry blanket above the arms to rotate in the same direction as the arms and at the same speed. This is undesirable and actually nullifies the improved distribution sought by rotation of the arms.
It is an object of this, invention to: provide apparatus and process for controlling the speed and. direction of rotation of a slurry blanket'overlyiug rotatable distributing arms.
Another object is to provide means for controlling the speed and rotation of: a slurry-blanket which can be adjusted to provide any desired speed and direction of blanket rotation.
Another object is to provide an. improved distributing arm structure for an apparatus of'the: type mentioned.
Another object of the invention istoprovide a rotatable distributing arm discharging downwardly at an'angle to the vertical to provide a tangential velocity component opposite to the; direction of the arm rotation.
Another object is to provide a, distributing arm which is rotatable about a vertical axis and can also be rotated about its own horizontal axis.
Other objects will become apparent upon consideration of the detailed description and of the claim.
It has been the usual opinion of those practicing slurry treatment that rotation of the slurry: blanket due to rotation of rotatable members below the. blanket. should be suppressed, or at least minimized and various. kinds of bafiling devices have been used therefor, or the rotating members were circulated. at a very low speed. However, rotation of the slurry; blanket, in and ot itself, is not only permissible but often desirable, provided the velocity and direction of blanket rotation are controlled. There should be an appreciable relative velocity between the rotation of the arms and the rotation of the blanket when the slurry blanket is rotated in the same direction as the arms. I have also found that 2,787,378 Patented Apr. 2, 1957 sometimes it is desirable that the slurry blanket rotate in the opposite direction of the arms. Such reversal has resulted in considerable improvement in the operation of the treating unit, not only with regard to distribution but particularly in avoidance of local boils in the slurry blanket.
I have discovered that the speed of rotation of the slurry blanket can be controlled, and that rotation of the slurry blanket can be entirely stopped or its direction reversed, by discharging the slurry from the arms at an angle to the vertical so that. there is a tangential velocity component opposite to the direction of arm rotation. The angle of discharge may vary from about 15 to about 45, depending on whether it is desired to merely slow down the rotation of the blanket, to stop it, or to reverse its direction.
Whether slowing down of the rotation of a slurry blanket rotating in the direction of the arms, or reversal of the direction of rotation results in the best operating conditions depends largely on the quantity and quality of the solids in the slurry, and particularly their settling characteristics, and must be decided from case to case. Other factors influencing the blanket rotation are the velocity of the jets discharged from. the arms, which depends on the speed of rotation of the rotor of the apparatus, and the velocity of rotation of the arms, which is controlled independently of the speed of rotation of the rotor. One ditficulty of controlling the slurry blanket rotation is, therefore, that the correct angle of discharge usually can be ascertained only after the apparatus has been put in operation, and that. the angle must be changed if the characteristics of the liquid under treatment change considerably. I, therefore, suggest to support the arms in such manner that they can be rotated about their horizontal axis and thus can be readily adjusted to the. angle of discharge which is found best in operation.
The invention will be more readily understood by reference to the drawing wherein:
Figure l is a vertical cross-sectional view of an apparatus utilizing the invention;
Figure 2 is an enlarged vertical cross-sectional view of a distributing arm taken along line 22 of Figure .l; and
Figure 3 is an enlarged vertical sectional view of the adjustable arm mounting of Figure 1.
The apparatus shown in Figure lfor purposes of illustrating the invention is similar to the apparatus. disclosed and claimed in the copending application of- Wal ter J. Hughes, Serial No. 212,761, filed February 26, 1951, now Patent No. 2,673,181, and no claim is made herein to this apparatus per se. The present invention is not limited: to use. in connection with this specific apparatus, but can be applied to other apparatus of the general. type where. liquid is discharged through arms rotating below a slurry blanket. The invention corrects objectionable features of such previously known apparatusand provides. for better operation.
The liquid treating apparatus shown in Figure. 1 comprises. a tank 10, which may have. any suitable shape but is shown for purposes of exemplificationas having a substantially flat bottom 11 and a cylindrical boundary wall 12. Treated liquid overflows intoa launder 13 and is withdrawn through an efiiuent conduit 1 Snitable means for withdrawing excess solids are provided and may take the form of a sludge sump 15 in the bottom 11, and a sludge blow-cit line 16 leading from the sump 15.
Axially mounted in the tank 10 is a partition structure 20 comprising an outer partition 21, and an inner partition 22 which may be independently supported or, as
shown, he supported from the outer partition 21 as by brackets 23. The partitions 21 and 22 may have any suitable configuration, but are shown for purposes of illustration as tubular. The lower edges of partitions 21 and 22 are spacedabove the bottom 11 of the tank, and the channel 24 between the partitions is closed at the lower end by a floor 25. The upper edge of the outer partition 21 is above the overflow into the launder 13, and the upper edge of the inner partition is at a lower elevation, thus providing an overflow from the space within the inner partition 22 to the channel 24. The lower part of the outer partition is provided with a plurality of ports 26 symmetrically spaced about the partition 21.
A rotor 30 is mounted within the partition structure 20, preferably just above the upper end of the inner partition 22, as shown, and can be rotated by means of a suitable motor-reducer 31. To afford mixing of the liquid to be treated with the reagent in the presence of slurry pumped upwardly through the partition 22 by the rotor 30, the liquid to be treated and the reagent are introduced into the space Within the partition structure 20 at opposite sides of the rotor 30, as through conduits 32 and 33, respectively, or the liquid to be treated can be introduced into the space within the partition 22 below the rotor, as through a conduit 32a. The latter construction is preferred when the rate of raw water supply varies considerably, as it permits to maintain a constant volume of discharge through the arms 50, and therefore a constant speed of rotation of the slurry blanket, regardless of the rate of raw water flow.
A plate 35 may be mounted in any suitable manner between the open lower end of the inner partition 22 and the sump 15 and shelters the sump from the turbulence set up by the return flow of slurry to the inner partition 22.
The outer partition 21 is rotatably supported by any suitable means, such as a channel structure 36 surrounding its upper end and riding on rollers 37 journaled in bearings 38. The bearings 38 are supported from a walkway or beam 39 spanning the tank 10. To prevent sideslipping of the channel structure 36 as it travels over the rollers 37, a plurality of guide rollers 40 are provided and are journaled in bearings 41, which also are supported by the beam 39. Any suitable means can be used to rotate the partition 21. For purposes of illustration an internal ring gear 42 is shown which meshes with a pinion 43 mounted on the shaft of a speed reducer 44, driven by a motor 45. The motor 45 and speed reducer 44 can be mounted on the beam 39. In Figure 1 it is assumed that the partition 21 rotates clockwise.
A plurality of hollow distributing arms are equally spaced about the partition 21 to register with the ports 26. The arms 50 extend from the outer partition 21 across the tank 10 and are in hydraulic communication with the channel 24 through the ports 26. Usually at least four arms are used, but in larger tanks six or more arms should be used for good distribution. The arms 50 are provided with discharge means 51, which may be in the form of a continuous slot, as shown on the right hand arm in Figure 1, or of orifices suitably spaced along the length of the arm, as shown on the left hand arm of said figure. As best shown in Figure 2, the discharge opening or openings are located in the lower portion of the arm 50 and with their center line C at an angle to the vertical center line C of the arm 50 in the direction opposite the direction of arm rotation indicated by the arrow R.
Since in practice the angle to the vertical may vary considerably, I provide means for adjustably mounting the arms 50 on the partition 21. The ports 26 are surrounded by couplings 55, which are welded or otherwise afiixed to the partition 21. Each coupling is machined to provide a shoulder 56 which serves as a stop for the distributing arm which is inserted in the coupling 55. Each coupling is tapped at two places which are apart to permit the insertion of set screws 57, which bear against the arm 50 and hold it fixedly in the selected position. By loosening the screws 57 the arm 50 can be rotated about its axis in the coupling 55 until the slots or orifices 51 are in the correct angular position to obtain the speed and direction of rotation of the slurry blanket desired, and then can be fixed in this position by tightening the screws. The angle from the vertical of the center line of the discharge opening should not be less than about 15 and not more than about 45 and will usually be within the range of from 15 to 30. The choice of the angle depends on the characteristics of the slurry, the speed of the rotor 30 which controls the velocity of the jets discharged from the arms 50, and the speed of rotation of the arms 50 which is controlled by motor-reducer 45--44.
I claim:
In a slurry type liquid treating apparatus having a tank which during normal operation contains a slurry blanket and an overlying body of clarified liquid, a central mixing chamber surrounded by a casing separating said mixing chamber from an outer space between said casing and the wall of said tank and conduits having longitudinally aligned discharging distributing openings connected to apertures in the wall of said casing adjacent the bottom of said tank and extending from said casing adjacent to but spaced from the bottom of said tank for approximately the entire distance of the outer space intermediate said tank and said casing, the improvement comprising a collar secured to said casing in registry with each of said apertures and facing the intermediate space between said casing and said tank, each of said collars being dimensioned to surround a conduit, adjustable fastening means carried by each collar for engaging a conduit to maintain it in communication with an associated aperture, each conduit secured in a collar by said adjustable fastening means to position the openings in said conduit at preselected vertical angles whereby slurry mixture conducted to said casing and discharged from said openings for distribution over the bottom of said tank upon rotation of said casing imparts a substantial tangential velocity to the slurry mixture underlying the slurry blanket in said tank and a minimum vertical velocity to slurry solids traveling upward to the slurry blanket while simultaneously controlling the rotational velocity of the slurry blanket relative to the rotational velocity of the conduits.
References Cited in the tile of this patent UNITED STATES PATENTS 806,214 Trent Dec. 5, 1905 1,678,788 Remick July 31, 1928 1,837,191 Baldwin Dec. 22, 1931 2,101,908 Joos et a1. Dec. 14, 1937 2,204,093 Mallory June 11, 1940 2,245,587 Hughes June 17, 1941 2,259,221 Darby et a1. Oct. 14, 1941 2,525,842 Thompson et a1. Oct. 17, 1950 FOREIGN PATENTS 556,447
Great Britain Oct. 5, 1943
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3025966A (en) * 1959-07-29 1962-03-20 Wayne A Kivell Liquid clarifying apparatus
US3390776A (en) * 1965-10-20 1968-07-02 Crane Co Reactor for the treating of water
US3525439A (en) * 1968-11-04 1970-08-25 Franklin K Spragins Distribution and slurrying apparatus
US4650578A (en) * 1984-05-23 1987-03-17 Stein Industrie Centrifuging mixture separator
US5246583A (en) * 1989-04-06 1993-09-21 Tetsuo Nishida Liquid treating apparatus
US5478468A (en) * 1993-09-10 1995-12-26 Sumitomo Heavy Industries, Ltd. Coagulating sedimentation processing apparatus
US6334952B1 (en) * 1999-05-31 2002-01-01 Sumitomo Heavy Industries, Ltd. Coagulating sedimentation apparatus

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US806214A (en) * 1905-06-27 1905-12-05 Lamartine C Trent Agitating and mixing apparatus.
US1678788A (en) * 1926-05-10 1928-07-31 Walter L Remick Process of and apparatus for the treatment of solid-bearing liquids
US1837191A (en) * 1930-01-22 1931-12-22 William M Baldwin Apparatus for separating solids from liquids in which said solids are suspended
US2101908A (en) * 1935-07-17 1937-12-14 Cochrane Corp Method of and apparatus for treating water
US2204093A (en) * 1938-05-18 1940-06-11 Edward B Mallory Mechanical aerator
US2245587A (en) * 1936-06-05 1941-06-17 Infilco Inc Liquid treating apparatus
US2259221A (en) * 1939-12-30 1941-10-14 Dorr Co Inc Purification of liquids
GB556447A (en) * 1942-05-28 1943-10-05 Frank Pullen Candy Improvements in connection with the purification of water in tanks
US2525842A (en) * 1947-05-27 1950-10-17 Dorr Co Liquid clarifying apparatus

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US806214A (en) * 1905-06-27 1905-12-05 Lamartine C Trent Agitating and mixing apparatus.
US1678788A (en) * 1926-05-10 1928-07-31 Walter L Remick Process of and apparatus for the treatment of solid-bearing liquids
US1837191A (en) * 1930-01-22 1931-12-22 William M Baldwin Apparatus for separating solids from liquids in which said solids are suspended
US2101908A (en) * 1935-07-17 1937-12-14 Cochrane Corp Method of and apparatus for treating water
US2245587A (en) * 1936-06-05 1941-06-17 Infilco Inc Liquid treating apparatus
US2204093A (en) * 1938-05-18 1940-06-11 Edward B Mallory Mechanical aerator
US2259221A (en) * 1939-12-30 1941-10-14 Dorr Co Inc Purification of liquids
GB556447A (en) * 1942-05-28 1943-10-05 Frank Pullen Candy Improvements in connection with the purification of water in tanks
US2525842A (en) * 1947-05-27 1950-10-17 Dorr Co Liquid clarifying apparatus

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3025966A (en) * 1959-07-29 1962-03-20 Wayne A Kivell Liquid clarifying apparatus
US3390776A (en) * 1965-10-20 1968-07-02 Crane Co Reactor for the treating of water
US3525439A (en) * 1968-11-04 1970-08-25 Franklin K Spragins Distribution and slurrying apparatus
US4650578A (en) * 1984-05-23 1987-03-17 Stein Industrie Centrifuging mixture separator
US5246583A (en) * 1989-04-06 1993-09-21 Tetsuo Nishida Liquid treating apparatus
US5478468A (en) * 1993-09-10 1995-12-26 Sumitomo Heavy Industries, Ltd. Coagulating sedimentation processing apparatus
US6334952B1 (en) * 1999-05-31 2002-01-01 Sumitomo Heavy Industries, Ltd. Coagulating sedimentation apparatus

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