IFS AND GRIT BOX FOR WATER CLARIFICATION SYSTEMS
A grit box to separate particulate matter from an influent stream. The grit box has an upper portion and a lower portion with a deflection plate separating the upper portion from the lower portion. It includes a hopper for accumulation of particulate matter settled from the influent stream. The hopper has a drainage pipe and a valve therebetween to control passage of material from the grit box into the drainage pipe. A mechanism delivers the influent stream at a predetermined and substantially constant flow rate. The influent stream is separated into two or more streams which are recombined under pressure in the grit box in a turbulent mixing zone. The fluid rise rate in the grit box is lower than the settling rate of the particulate matter to be separated from the influent stream.
1 . A grit box for receiving particulate matter derived from an influent, comprising:
a) an upper portion, a lower portion, and a hopper,
wherein said lower portion includes a bottom and side walls circumscribing an outer region of said lower portion, and
wherein said upper portion includes one or more side walls in common with said lower portion, said upper portion being in fluid communication with said lower portion,
b) a deflection plate positioned between said upper portion and said lower portion;
c) a mechanism configured to deliver a stream of said influent into said grit box at a predetermined and substantially constant flow rate, said influent stream being divided into two or more streams which are then recombined from substantially opposing directions in said lower portion, resulting in a first fluid rise rate in said lower portion and a second fluid rise rate in said upper portion,
wherein said first fluid rise rate is less than a settling rate of said particulate matter in said influent in said lower portion.
2 . The grit box of claim 1 wherein said second fluid rise rate is less than a settling rate of said particulate matter in said influent in said upper portion.
3 . The grit box of claim 1 wherein said influent delivery mechanism is selected from the group consisting of a pump and a holding tower.
4 . The grit box of claim 1 wherein said recombination of two or more divided influent streams causes formation of a turbulent mixing zone.
5 . The grit box of claim 1 , wherein said upper portion further includes a fluid discharge mechanism, and wherein said hopper is coupled to a drainage pipe via a valve to control passage of materials from said grit box into said drainage pipe.
6 . The grit box of claim 4 , wherein three or more divided influent streams being recombined in said turbulent mixing zone are directed substantially toward each other from three or more opposing feed pipes that extend from a manifold in said fluid delivery mechanism at about an equal angular spacing.
7 . The grit box of claim 6 , wherein said opposing feed pipes extend from said manifold at about a 120 degree angular spacing.
8 . The grit box of claim 6 , wherein four opposing feed pipes extend from said manifold at about a 90 degree angular spacing.
9 . The grit box of claim 6 , wherein each of said opposing feed pipes comprises a first substantially 90 degree bend about where each of said pipes is coupled to said manifold and a second substantially 90 degree bend wherein said first and second 90 degree bends cause said divided influent streams to be directed substantially towards each other.
10 . The grit box of claim 6 , comprising four opposing feed pipes that extend from said manifold at about a 90 degree spacing,
wherein each of said opposing feed pipes includes a first bend of about 90 degrees where each pipe is coupled to said manifold,
wherein each of a first two opposing feed pipes of said four opposing feed pipes includes a second bend of 90 degrees or more, such that divided influent streams exiting said first two opposing feed pipes are directed upward and toward each other, and
wherein each of a second two opposing feed pipes of said four opposing pipes includes a second bend of 90 degrees or less, such that divided influent streams exiting said second two opposing feed pipes are directed downward and toward each other and toward said divided influent streams exiting from said first two opposing feed pipes.
11 . A method to remove particulate matter from an influent, comprising the steps of:
a) providing a grit box having an upper portion, a lower portion, a deflection plate disposed between said upper portion and said lower portion, a hopper, and a mechanism for delivering said influent to said grit box, wherein said lower portion includes a bottom and side walls circumscribing an outer region, and wherein said upper portion includes one or more side walls in common with said lower portion, said upper portion being in fluid communication with said lower portion;
b) delivering a stream of influent to said grit box at a predetermined and substantially constant flow rate;
c) separating said stream of influent into two or more influent streams in said grit box, and
d) recombining said two or more influent streams from substantially opposing directions in said lower portion, wherein a first fluid rise rate of said influent in said lower portion of said grit box is less than a settling rate of said particulate matter from said influent in said lower portion.
12 . The method of claim 11 wherein a second fluid rise rate in said upper portion is less than a settling rate of said particulate matter from said influent in said upper portion.
13 . The method of claim 11 wherein said delivering step includes the step of pumping said stream of influent.
14 . The method of claim 11 wherein said delivering step includes gravity flow.
15 . The method of claim 11 , wherein said recombining step of said two or more influent streams creates a turbulent mixing zone.
16 . The method of claim 11 further comprising the step of accumulating said particulate matter in said hopper.
17 . The method of claim 16 further comprising the step of removing accumulated particulate matter from said hopper.