System for pollution suppression

• US 4,045,347 A
• Filed: 05/04/1976
• Issued: 08/30/1977
• Est. Priority Date: 04/23/1964
• Status: Expired due to Term

• Current Assignee: Edward T. Armstrong
• Original Assignee: TII Corporation
• Inventors: Armstrong, Edward T.
• Primary Examiner(s): Wyse, Thomas G.
• Assistant Examiner(s): Spitzer, Robert H.
• Application Number:
  US05/682,962
• Time in Patent Office: 483 Days
• Field of Search: 210/7, 210/14, 210/15, 210/62, 210/63 R, 210/64, 210/195 S, 210/220, 210/221 R, 210/199, 261/76, 261/77, 261/123, 261/DIG. 75
• US Class Current: 210/199
• CPC Class Codes: B01D 21/00 Separation of suspended solid particles from liquids by sedimentation separation of ores or the like by sedimentation B03B5/48 - B03B5/60 ; differential sedimentation B03D3/00; purification of water, waste water, sewage or sludge C02F, e.g. devices for separating or removing fatty or oily substances or similar floating material from water, waste water or sewage C02F1/40
• CPC Class Codes: B01D 21/0084 Enhancing liquid-particle separation using the flotation principle flotation in general B03D1/00
• CPC Class Codes: B01D 21/01 using flocculating agents for purifying water C02F1/52; for liquid radioactive waste G21F9/10
• CPC Class Codes: B01D 21/14 with rotating scrapers
• CPC Class Codes: B01D 21/24 Feed or discharge mechanisms for settling tanks
• CPC Class Codes: B01D 21/34 Controlling the feed distribution; Controlling the liquid level ; Control of process parameters
• CPC Class Codes: C01B 13/10 Preparation of ozone
• CPC Class Codes: C01B 2201/66 Pretreatment of the feed
• CPC Class Codes: C02F 1/76 with halogens or compounds of halogens C02F1/4674 takes precedence
• CPC Class Codes: C02F 1/78 with ozone C02F1/4672 takes precedence
• CPC Class Codes: C02F 3/043 Devices for distributing water over trickle filters
• CPC Class Codes: C02F 3/302 Nitrification and denitrification treatment C02F3/308 takes precedence
• CPC Class Codes: C02F 9/00 Multistage treatment of water, waste water or sewage
• CPC Class Codes: F16L 55/02 Energy absorbers; Noise absorbers in valves F16K47/00
• CPC Class Codes: F16L 55/045 specially adapted to prevent or minimise the effects of water hammer
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

A surge suppression system for dampening surge pressures or pipe hammer by introducing a gas into a flow conduit in such an amount that the introduced gas is in excess of that required to saturate the liquid. Preferably, the gases are those which are relatively inert or not unduly reactive and which possess relatively low saturation levels with respect to the liquid. Desirably, the gas is added through a member to the flow conduit in a vicinity of high turbulence. The surge suppression system can be utilized in generally any liquid system and particularly in a liquid transmission system.

Another embodiment pertains to a scrubber or washer for generally purifying gases and may contain one or two stages to efficiently remove impurities as through the use of high solubility fluids, fluids which decompose contaminants or which contain or provide (i.e. heating stage) catalysts to decompose contaminants, oxidizing agents, or reducing agents. The scrubber contains a packed bed and the packing may be characterized as one where the inside hydraulic radius equals the hydraulic radius of the external flow channels. The washer or scrubber type apparatus is particularly suitable for treating (purifying) materials such as ozone utilized in a deodorizing or disinfecting system.

Another embodiment pertains to the purification of a gas by treatment with a fluid in a flow conduit having a plug flow at its entrance containing an injection-mixing device coacting with a first high turbulence causing device and a downstream or second high turbulence causing device. The treating fluid is preferably added at the vena contracta of the first high turbulence causing device.

Claims

1. A disinfectant mixing system for an influent treatment system utilizing a contact tank which comprises

an influent inlet port into the contact tank,

a manifold fed by the inlet port,

a pipe bundle fed by said manifold,

a flat plate orifice high momentum exchange mixing member in each pipe in said bundle,

means for injecting a disinfecting fluid into each pipe at the point of highest momentum exchange,

an influent well,

means to effect influent flow from the influent well to the contact tank,

an effluent well,

means to effect flow from the contact tank to the effluent well, and

a hyperbolic transformed diffuser to deliver the influent from the pipe bundle to the influent well.

2. A system according to claim 1 where each pipe of the pipe bundle is between 120 to 150 diameters in length from the point of disinfectant fluid injection, and includes at least two flat plate orifices downstream from the point of disinfectant fluid injection at a minimum of 40 diameters separation.

3. A system according to claim 2 where the diffuser is positioned adjacent a vertical wall in the influent tank so as to project a hyperbolic sheet of influent onto such wall to mix with the fluid in the influent tank.

4. A system according to claim 3 where the diffuser is formed as a transformed hyperbolic section so as to decelerate fluid flow therefrom.

5. A system according to claim 4, wherein the diffuser is a 90°

elbow that diverges no more than 7°

in cross-sectional configuration.

6. A system according to claim 1, wherein each pipe has at least two flat plate orifices downstream from said point of disinfectant fluid injection at a minimum of 40 diameters separation.

7. A system according to claim 6, wherein said pipe bundle has a larger overall total flow area than said manifold.

8. A system according to claim 7, wherein said flat plate orifice diameter ranges from about 0.7 to about 0.9 of said pipe diameter in said bundle.

9. A system according to claim 8, wherein said injecting means is a small pipe, said pipe existing in the vena contracta of said flat plate orifice, said small pipe having a tip, said tip extending from about 0.25 to about 0.5 pipe diameters downstream from said flat plate orifice.

10. A system according to claim 9 wherein said small tip extends from about 0.3 to about 0.39 pipe diameters downstream of said flat plate orifice.

11. A system according to claim 8, wherein said point of highest momentum exchange is in the vena contracta of said flat plate orifice.

12. A system according to claim 11, wherein said pipe bundle is a plurality of pipes, each said pipe having a diameter smaller than said manifold.

13. A system according to claim 7, wherein said high momentum exchange mixing member is a 90°

elbow.

14. A system according to claim 13, wherein said injecting means is a small pipe.

15. A system according to claim 14, wherein said small pipe has a tip, said tip extending from about 0.25 to about 0.5 pipe diameters downstream of said flat plate orifice, and said flat plate orifice has a diameter of from about 0.7 to about 0.9 of said pipe diameter.

16. A system according to claim 15, wherein said small pipe tip extends from about 0.3 to about 0.39 diameters downstream from said pipe.

17. A system according to claim 15, including means for injecting a deoxygenation compound to said effluent well, said deoxygenation compound selected from the group consisting of sulfur dioxide and thiosulfate.

18. A system according to claim 1, including means for injecting a deoxygenation compound to said effluent well, said deoxygenation compound selected from the group consisting of sulfur dioxide and thiosulfate.