Method of treating foul water

• US 5,744,037 A
• Filed: 11/27/1996
• Issued: 04/28/1998
• Est. Priority Date: 11/28/1995
• Status: Expired due to Term

• Current Assignee: Ebara Corporation
• Original Assignee: Ebara Corporation
• Inventors: Ichiki, Yoshiyuki, Suzuki, Takayuki, Yamada, Norio, Fujimura, Hiroyuki
• Primary Examiner(s): POPOVICS, ROBERT J
• Application Number:
  US08/758,249
• Time in Patent Office: 517 Days
• Field of Search: 210/768, 210/769, 210/609, 210/605, 210/612, 210/613, 210/903, 210/620, 210/630, 110/235, 110/243, 110/244, 110/245, 110/346
• US Class Current: 210/620
• CPC Class Codes: C02F 11/06 by oxidation incinerators for burning waste liquors, e.g. sulfite liquor from paper-making plant F23G7/04
• CPC Class Codes: C02F 3/12 Activated sludge processes
• CPC Class Codes: C02F 3/28 Anaerobic digestion processes
• CPC Class Codes: C02F 3/2846 using upflow anaerobic sludge blanket [UASB] reactors
• CPC Class Codes: C02F 3/286 including two or more steps
• CPC Class Codes: F23G 7/001 for sludges or waste products from water treatment installations F23G5/008 takes precedence
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage
• CPC Class Codes: Y02W 10/37 using solar energy
• CPC Class Codes: Y02W 10/40 Valorisation of by-products of wastewater, sewage or sludge processing
• CPC Class Codes: Y10S 210/903 Nitrogenous

Abstract

In an improved method of treating foul water, the solids that are produced during the process of treatment of foul water such as wastewater or liquid sludges are treated with a heat treatment apparatus and the resulting thermal energy and/or gas is utilized in the treatment of said foul water. The foul water may be subjected, directly and/or after a treatment, to a filtration step using a filter packed with nonflammable particulate matter such as sand, and the trapped solids are fed into a fluidized-bed heat treatment apparatus such as a fluidized-bed incinerator or gasification furnace and, thereafter, the nonflammable particulate matter in the heat treatment apparatus is returned to the filtration step. The foul water can be treated with effective utilization of the energy of the organic matter in the foul water or the solids that are produced during the process of its treatment.

Claims

1. A method of treating foul water comprising at least one of night soil, septic sludge and sewage, which comprises:

(a) feeding the foul water into a first chamber, where it is detained to remove sand and gravel;

(b) holding effluent from said first chamber temporarily in a receiving tank and forcing it through a pretreatment screen, whereby the effluent is separated into a solid portion and a liquid portion;

(c) sending the solid portion to a dewatering apparatus, from which dewatered screenings emerge;

(d) introducing separated water into an anaerobic digestion treatment apparatus, or biological denitrification treatment apparatus, or activated sludge treatment apparatus, whereby treatment is conducted to produce digested sludge or excess sludge;

(e) introducing the digested sludge or excess sludge into a sand filtration tank having a sand layer and an underlying gravel layer;

(f) combining sludge trapped with sand of said sand layer, sand removed by detention in the first chamber, dewatered screenings from a screenings dewatering apparatus, waste materials comprising scrap tires and domestic organic wastes to form a mixture, fluidizing the mixture to form a fluidized layer, and burning the mixture in a fluidized-bed heat treatment apparatus;

(g) after burning the sludge in the fluidized-bed heat treatment apparatus, feeding sand from the fluidized layer into a separator to separate said sand, and recycling the resultant separated sand to said sand filtration tank.

2. A method according to claim 1, wherein the anaerobic digestion apparatus comprises a first digestion tank under agitation and a second digestions tank in the absence of agitation, wherein said separated water is first introduced into said first digestion tank and then into said second digestion tank.

3. A method according to claim 1, wherein a gaseous mixture evolved in the fluidized-bed gasification furnace which contains hydrogen, carbon monoxide, water vapor, tar and carbides is introduced into a gasification melting furnace, where it is subjected to rapid oxidation with air, thereby evolving a hot gas and ash in the gaseous mixture said ash is melted and discharged as slag.

4. A method according to claim 3, wherein ammonia is separated in the process of foul water treatment and utilized in the denitrification and desulfurization of the emission gas from said heat treatment apparatus and in the production of a nitrogen fertilizer.

5. A method according to claim 1, wherein the gas produced by gasification or combined gasification and combustion in said heat treatment apparatus is converted to a reducing agent such as methanol and used in biological denitrification of the foul water.

6. A method according to claim 2, wherein the energy produced in said heat treatment apparatus is supplied into an ozonizer and the ozone produced is used in the process of treatment of said foul water to control the production of excess sludge in a biological treatment step.

7. A method according to claim 1, wherein said fluidized-bed heat treatment apparatus is a fluidized-bed incinerator or a gasification furnace, and wherein the mixture is fed to said fluidized-bed incinerator or said gasification furnace where said burning is carried out.

8. A method of treating foul water comprising at least one of night soil, septic sludge and sewage, which comprises:

removing solids from the foul water to provide a solid portion and separated water;

introducing said separated water into an anaerobic digestion treatment apparatus, or biological denitrification treatment apparatus, or activated sludge treatment apparatus, whereby treatment is conducted to produce digested sludge or excess sludge;

introducing the digested sludge or excess sludge into a sand filtration tank having a sand layer and an underlying gravel layer;

combining sludge trapped with sand of said sand layer, said solid portion, and waste materials comprising scrap tires and domestic organic wastes to form a mixture, fluidizing the mixture to form a fluidized layer, and burning the mixture in a fluidized-bed heat treatment apparatus;

after burning the sludge in the fluidized-bed heat treatment apparatus, feeding sand from the fluidized layer into a separator to separate said sand, and recycling the resultant separated sand to said sand filtration tank.

9. A method according to claim 8, wherein the anaerobic digestion apparatus comprises a first digestion tank under agitation and a second digestions tank in the absence of agitation, wherein said separated water is first introduced into said first digestion tank and then into said second digestion tank.

10. A method according to claim 8 wherein a gaseous mixture evolved in the fluidized-bed gasification furnace which contains hydrogen, carbon monoxide, water vapor, tar and carbides is introduced into a gasification melting furnace, where it is subjected to rapid oxidation with air, thereby evolving a hot gas and ash in the gaseous mixture said ash is melted and discharged as slag.

11. A method according to claim 10, wherein ammonia is separated in the process of foul water treatment and utilized in the denitrification and desulfurization of the emission gas from said heat treatment apparatus and in the production of a nitrogen fertilizer.

12. A method according to claim 8, wherein the gas produced by gasification or combined gasification and combustion in said heat treatment apparatus is converted to a reducing agent such as methanol and used in biological denitrification of the foul water.

13. A method according to claim 9, wherein the energy produced in said heat treatment apparatus is supplied into an ozonizer and the ozone produced is used in the process of treatment of said foul water to control the production of excess sludge in a biological treatment step.

14. A method according to claim 8, wherein said fluidized-bed heat treatment apparatus is a fluidized-bed incinerator or a gasification furnace, and wherein the mixture is fed to said fluidized-bed incinerator or said gasification furnace where said burning is carried out.