Water treatment apparatus and method

Claim 2

A liquid treatment apparatus comprising: a single enclosure containing therein at least one reaction zone having therein sludge and at least one decanting zone, said reaction zone having a lower portion and an upper portion separated from said lower portion; means for introducing liquid to be treated into said lower portion of said reaction zone; means for turbulently mixing said liquid and sludge within a turbulent area of said lower portion of said reaction zone and withdrawing at a controlled rate the thus formed mixture of liquid and sludge from said turbulent area of said lower portion to said upper portion; means for recycling a first portion of the thus withdrawn mixture from said upper portion back into said turbulent area of said lower portion; means, separate from said recycling means, for distributing a second portion of said thus withdrawn mixture from said upper portion in a uniform manner throughout the entire area of the lower portion of said decanting zone, whereby purified liquid rises upwardly to the top of said decanting zone and sludge settles toward the bottom of said decanting zone; and means for collecting said purified liquid.

Claim 3

An apparatus as claimed in claim 1, further comprising means for returning sludge which has settled on the bottom of said decanting zone into said turbulent area of said lower portion of said reaction zone.

Claim 4

An apparatus as claimed in claim 2, wherein said decanting zone communicates along the entire width thereof through an opening with said turbulent area of said lower portion of said reaction zone, and said returning means comprises means for scraping settled sludge from the bottom of said decanting zone through said opening into said turbulent area.

Claim 5

An apparatus as claimed in claim 1, wherein said liquid introducing means comprises an inlet pipe extending into said lower portion of said reaction zone.

Claim 6

An apparatus as claimed in claim 1, wherein said upper and lower portions of said reaction zone are separated by a wall having therein a central passage, and said mixing means comprises pump means positioned within said central passage.

Claim 7

An apparatus as claimed in claim 5, wherein said pump means is a variable speed pump capable of pumping said mixture through said central passage at a desired controlled rate greater than the rate at which said liquid to be treated is introduced into said reaction zone.

Claim 8

An apparatus as claimed in claim 6, wherein said pump is capable of pumping said mixture through said central passage at a rate of three to four times the rate at which said liquid to be treated is introduced into said reaction zone.

Claim 9

An apparatus as claimed in claim 5, wherein said recycling means comprises openings in said wall on opposite sides of said central passage.

Claim 10

An apparatus as claimed in claim 8, further comprising means for adjusting the size of said openings and for thereby regulating the amount of said first portion of said mixture recycled back to said turbulent area.

Claim 11

An apparatus as claimed in claim 1, wherein said decanting zone is substantially rectangular and communicates adjacent an end thereof with said reaction zone.

Claim 12

An apparatus as claimed in claim 10, wherein said distributing means comprises ducts extending from said upper portion of said reaction zone on opposite sides of said decanting zone, exterior of said decanting zone, throughout the entire length of said decanting zone, and orifices extending from said ducts into said decanting zone, said orifices being spaced along the entire length of said decanting zone.

Claim 13

An apparatus as claimed in claim 11, further comprising means, separate from said orifices, for deflecting and aligning flow of said mixture into said decanting zone through said orifices.

Claim 14

An apparatus as claimed in claim 11, wherein said mixing means comprises pump means capable of maintaining the fluid pressure in said mixture passing through said orifices at a level sufficient to achieve a continuously uniform distribution of said mixture throughout the entire area of said decanting zone.

Claim 15

An apparatus as claimed in claim 11, further comprising parallel plates positioned within said decanting zone and spaced along the entire length thereof, said orifices being positioned to distribute said mixture uniformly into the spaces between said parallel plates.

Claim 16

An apparatus as claimed in claim 1, wherein said single enclosure has therein one reaction zone and two separate decanting zones, one each on opposite sides of said reaction zone.

Claim 17

An apparatus as claimed in claim 1, wherein said single enclosure has therein two reaction zones and four separate decanting zones, each said reaction zone having on each opposite side thereof one said decanting zone.

Claim 20

A method as claimed in claim 17, wherein the quantity of said second portion of said withdrawn mixture which is distributed to said decanting zone is greater than the quantity of said liquid supplied to said lower portion of said reaction zone.

Claim 21

A method as claimed in claim 17, further comprising returning sludge which has settled on the bottom of said decanting zone into said lower portion of said reaction zone.

Claim 22

A method as claimed in claim 17, wherein said mixture is withdrawn from said turbulent area of said lower portion of said reaction zone at a desired controlled rate greater than the rate at which said liquid to be treated is introduced into said reaction zone.

Claim 23

A method as claimed in claim 20, wherein said desired controlled rate is three to four times the rate at which said liquid to be treated is introduced into said reaction zone.

Claim 24

A method as claimed in claim 17, further comprising regulating the amount of said first portion of said mixture recycled back to said turbulent area.

Claim 25

A method as claimed in claim 17, further comprising directing, by the use of means separate from said orifices, the direction of flow of said second portion of said mixture which is distributed to said decanting zone.

Claim 26

A method as claimed in claim 17, further comprising controlling the fluid pressure of said second portion of said mixture distributed to said decanting zone.

Claim 27

A liquid treatment apparatus comprising: a single enclosure containing therein at least one reaction zone having therein sludge and at least one decanting zone, said reaction zone having therein a turbulent area defined by a wall having a central passage, and said decanting zone communicating along the entire width thereof through an opening with said turbulent area of said reaction zone; means for introducing liquid to be treated into said reaction zone; means, positioned within said central passage, for turbulently mixing said liquid and sludge within said turbulent area and for withdrawing at a controlled rate the thus formed mixture of liquid and sludge from said turbulent area through said central passage; openings provided in said wall on opposite sides of said central passage, said openings forming means for recycling a first portion of the thus withdrawn mixture back into said turbulent area; means for adjusting the size of said openings and for thereby regulating the amount of said first portion of said mixture recycled back to said turbulent area; means for distributing a second portion of said thus withdrawn mixture in a uniform manner throughout the entire area of the lower portion of said decanting zone, whereby purified liquid rises upwardly to the top of said decanting zone and sludge settles toward the bottom of said decanting zone; and means for collecting said purified liquid.

Claim 28

A liquid treatment apparatus comprising: a single enclosure containing therein at least one reaction zone having therein sludge and at least one decanting zone, said reaction zone having therein a turbulent area defined by a wall having a central passage, and said decanting zone communicating along the entire width thereof through an opening with said turbulent area of said reaction zone; means for introducing liquid to be treated into said reaction zone; means, positioned within said central passage, for turbulently mixing said liquid and sludge within said turbulent area and for withdrawing at a controlled rate the thus formed mixture of liquid and sludge from said turbulent area through said central passage; openings provided in said wall on opposite sides of said central passage, said openings forming means for recycling a first portion of the thus withdrawn mixture back into said turbulent area; means for adjusting the size of said openings and for thereby regulating the amount of said first portion of said mixture recycled back to said turbulent area; means for distributing a second portion of said thus withdrawn mixture in a uniform manner throughout the entire area of the lower portion of said decanting zone, whereby purified liquid rises upwardly to the top of said decanting zone and sludge settles toward the bottom of said decanting zone; and means for collecting said purified liquid.

Claim 29

An apparatus as claimed in claim 25, further comprising means for returning sludge which has settled on the bottom of said decanting zone into said turbulent area of said reaction zone.

Claim 30

An apparatus as claimed in claim 26, wherein said returning means comprises means for scraping settled sludge from the bottom of said decanting zone through said opening into said turbulent area.

Claim 31

An apparatus as claimed in claim 25, wherein said liquid introducing means comprises an inlet pipe extending into the bottom of said reaction zone.

Claim 32

An apparatus as claimed in claim 25, wherein said mixing means is a variable speed pump capable of pumping said mixture through said central passage at a desired controlled rate greater than the rate at which said liquid to be treated is introduced into said reaction zone.

Claim 33

An apparatus as claimed in claim 29, wherein said pump is capable of pumping said mixture through said central passage at a rate of three to four times the rate at which said liquid to be treated is introduced into said reaction zone.

Claim 34

An apparatus as claimed in claim 25, wherein said decanting zone is substantially rectangular and communicates adjacent an end thereof with said reaction zone.

Claim 35

An apparatus as claimed in claim 31, wherein said distributing means comprises ducts extending from said reaction zone on opposite sides of said decantng zone, exterior of said decanting zone, throughout the entire length of said decanting zone, and orifices extending from said ducts into said decanting zone, said orifices being spaced along the entire length of said decanting zone.

Claim 36

An apparatus as claimed in claim 32, further comprising means, separate from said orifices, for deflecting and aligning flow of said mixture into said decanting zone through said orifices.

Claim 37

An apparatus as claimed in claim 32, wherein said mixing means comprises pump means capable of maintaining the fluid pressure in said mixture passing through said orifices at a level sufficient to achieve a continuously uniform distribution of said mixture throughout the entire area of said decanting zone.

Claim 38

An apparatus as claimed in claim 32, further comprising parallel plates positioned within said decanting zone and spaced along the entire length thereof, said orifices being positioned to distribute said mixture uniformly into the spaces between said parallel plates.

Claim 39

An apparatus as claimed in claim 25, wherein said single enclosure has therein one reaction zone and two separate decanting zones, one each on opposite sides of said reaction zone.

Claim 40

An apparatus as claimed in claim 25, wherein said single enclosure has therein two reaction zones and four separate decanting zones, each said reaction zone having on each opposite side thereof one said decanting zone.

Claim 43

A method as claimed in claim 38, wherein the quantity of said second portion of said withdrawn mixture which is distributed to said decanting zone is greater than the quantity of said liquid supplied to said reaction zone.

Claim 44

A method as claimed in claim 38, further comprising returning sludge which has settled on the bottom of said decanting zone into said turbulent area of said reaction zone.

Claim 45

A method as claimed in claim 38, wherein said mixture is withdrawn from said turbulent area of said reaction zone at a desired controlled rate greater than the rate at which said liquid to be treated is introduced into said reaction zone.

Claim 46

A method as claimed in claim 41, wherein said desired controlled rate is three to four times the rate at which said liquid to be treated is introduced into said reaction zone.

Claim 47

A method as claimed in claim 38, further comprising regulating the amount of said first portion of said mixture recycled back to said turbulent area.

Claim 48

A method as claimed in claim 38, further comprising directing, by the use of means separate from said orifices, the direction of flow of said second portion of said mixture which is distributed to said decanting zone.