Process for the treatment of hazardous waste water

• US 5,558,775 A
• Filed: 11/01/1994
• Issued: 09/24/1996
• Est. Priority Date: 11/01/1994
• Status: Expired due to Fees

• Current Assignee: Joseph Busch Jr, Joseph Busch Sr
• Original Assignee: Joseph Busch Jr, Joseph Busch Sr
• Inventors: Busch, Joseph B. Jr.
• Primary Examiner(s): Hruskoci, Peter A.
• Application Number:
  US08/332,660
• Time in Patent Office: 693 Days
• Field of Search: 210/638, 210/639, 210/641, 210/650, 210/651, 210/652, 210/663, 210/666, 210/694, 210/712, 210/721, 210/722, 210/724, 210/725, 210/727, 210/748, 210/758, 210/759, 210/787 , 210/806, 210/900, 210/909, 210/912
• US Class Current: 210/638
• CPC Class Codes: B01D 2311/04 Specific process operations in the feed stream; Feed pretreatment
• CPC Class Codes: B01D 2311/12 Addition of chemical agents
• CPC Class Codes: B01D 2311/2619 UV-irradiation
• CPC Class Codes: B01D 61/025 Reverse osmosis; Hyperfiltration
• CPC Class Codes: B01D 61/04 Feed pretreatment
• CPC Class Codes: B01D 61/145 Ultrafiltration
• CPC Class Codes: C02F 1/283 using coal, charred products, or inorganic mixtures containing them
• CPC Class Codes: C02F 1/32 with ultraviolet light
• CPC Class Codes: C02F 1/38 by centrifugal separation
• CPC Class Codes: C02F 1/441 by reverse osmosis
• CPC Class Codes: C02F 1/444 by ultrafiltration or microfiltration
• CPC Class Codes: C02F 1/5236 using inorganic agents
• CPC Class Codes: C02F 1/62 Heavy metal compounds
• CPC Class Codes: C02F 1/722 Oxidation by peroxides
• CPC Class Codes: C02F 1/78 with ozone C02F1/4672 takes precedence
• CPC Class Codes: C02F 2101/301 Detergents, surfactants
• CPC Class Codes: C02F 2101/32 Hydrocarbons, e.g. oil
• CPC Class Codes: C02F 2101/36 containing halogen
• CPC Class Codes: C02F 2101/363 PCB's; PCP's
• CPC Class Codes: C02F 2201/008 Mobile apparatus and plants, e.g. mounted on a vehicle for biological treatment C02F2203/008
• CPC Class Codes: C02F 9/00 : Multistage treatment of water, waste water or sewage
• CPC Class Codes: Y10S 210/90 : Ultra pure water, e.g. conductivity water
• CPC Class Codes: Y10S 210/909 : Aromatic compound, e.g. pcb, phenol
• CPC Class Codes: Y10S 210/912 : Heavy metal

Abstract

There is disclosed a portable assembly for treating hazardous waste water having a plurality of paired filter units having filter mediums and operated at high filter rates to minimize solids build up wherein solids are caused to be smashed and broken by shear forces and wherein chemicals are sequentially added to facilitate solids reduction, to oxidize organic compounds and to precipitate dissolved solids and wherein the process stream is subjected to ultraviolet light to reduce organic loading and downstream ultra filtration units to further reduce solids followed by reverse osmosis and/or ionization treatment.

Claims

1. A process for treating hazardous waste water containing organic components, suspended solids, and colloidal matter to produce recyclable water, which comprises the steps of:

a) introducing said hazardous waste water stream;

b) contacting said stream with an oxidizing agent to oxidize said organic components in said said stream;

c) passing a stream resulting from step b) through a separation zone to remove solids having a specific gravity greater than 1.0 to form a liquid stream;

d) contacting said liquid stream of step c) with a polymer to facilitate suspended solids reduction and introducing same into a separation zone to remove suspended solids;

e) contacting a liquid stream from step d) with a caustic solution and introducing same into a separation zone to remove particulates of less than about 10 microns.

f) contacting a liquid stream from step e) with an alkali-metal precipitant if said hazardous waste water being treated contains a heavy metal compound and introducing same into a separation zone to remove solids of a particle size down to about 10 microns;

g) passing a liquid stream from step f) through an ultraviolet zone to reduce organic loading;

h) passing a liquid stream from step g) through a separation zone to reduce colloidal matter to less than about 10%;

i) passing a liquid stream from step h) through a carbon filter zone to further reduce organic components; and

j) passing a liquid stream from step i) through a micron filter zone to produce recyclable water.

2. The process for treating hazardous waste water as defined in claim 1 and further including the step of passing said recyclable water of step j) through a reverse osmosis zone to further remove dissolved solids and inorganics, when said hazardous waste water contains heavy metal ions.

3. The process for treating hazardous waste water as defined in claim 1 wherein step c) is effected in a cyclone separator at pressure losses of from about 4.0 to 8.0 psig whereby about 98% of suspended solids greater than about 75 microns are removed from said stream.

4. The process for treating hazardous waste water as defined in claim 1 wherein said separation zone of step d) is performed at a flow rate of from 70 to 105 gallons per minute at a filter rate of about 7.0 gallons per minute per ft.² to remove solids of a particle size greater than 10 microns.

5. The process for treating hazardous waste water as defined in claim 1 wherein said caustic solution of step e) is introduced in an amount to raise pH above about 8.5.

6. The process for treating hazardous waste water as defined in claim 5 wherein caustic solution is added at a rate of from 50 to 140 ppm as a function of carbon dioxide loading.

7. The process for treating hazardous waste water as defined in claim 5 wherein said separation zone of step d) is performed at a flow rate of from 70 to 105 gallons per minute at a filter rate of about 7.0 gallons per minute per ft.² to remove solids of a particle size greater than 10 microns.

8. The process for treating hazardous waste water as defined in claim 1 wherein said alkali-metal precipitant of step f) is added at a rate of from 2 to 15 ppm per ppm of ions of said heavy metal compound.