WO2001061247A1 - A full-scale automated system for the destruction of air pollutants originating from wastewater treatment plants - Google Patents
A full-scale automated system for the destruction of air pollutants originating from wastewater treatment plants Download PDFInfo
- Publication number
- WO2001061247A1 WO2001061247A1 PCT/GR2001/000010 GR0100010W WO0161247A1 WO 2001061247 A1 WO2001061247 A1 WO 2001061247A1 GR 0100010 W GR0100010 W GR 0100010W WO 0161247 A1 WO0161247 A1 WO 0161247A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- gas
- collector
- incinerator
- gases
- flame
- Prior art date
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/061—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
- F23G7/065—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/006—General arrangement of incineration plant, e.g. flow sheets
Definitions
- the proposed system is a full-scale automated system for the destruction of air pollutants originating from wastewater treatment plants.
- the system consists of one or more ventilators, depending on the application system (with or no recycling), a gas collector with convex surface-usually dome, tubes, compressor, sensors, specially modified incinerator, chimney, flow rate of LPG or another fuel.
- the biomass consumes about 1 kg O 2 /m 3 waste. As a result it requires a sufficient quantity of air for biomass growth and compound degaradion.
- the air (oxygen) enters the tank, partly through the bottom, via a compressor with a system of thin tubes and partly from the surface due to armospheric oxygen. Brush aerators will be used in order to transfer atmospheric oxygen to the waste.
- a ventilator which absorbs the mal-odorous gases and routes them to the incinerator (with a pressure sensor in the dome) through tubes with two one-direction safety valves.
- the mixture of air and mal-odorous gases is originated from the waste degradation, the compressor air bubbles and the inlet fresh air from vent-holes (one direction from outlet to inlet) on the base of dome external perimeter.
- the gas collector with convex surface is fitted air-tightly on the wastewater treatment tanks, in order to avoid gas leakage. It is manufactured by a light but resistant material.
- the automated system of polluted gases purification includes the following units: 1 ) A gas collector with convex surface, by light and resistant material, which is suited tightly on the wastewater treatment tanks
- Tubes which route the exhaust gases from the exhauster outlet to the specially modified incinerator, founded with one direction valves, sensors etc, as well as a tube from the dome outlet to the compressor inlet if recycling is implemented.
- a specially modified incinerator LPG fuel enters the flame of the incinerator in order to achieve the combustion of the mal-odorous gases.
- the gases have passed through a heat exchanger (Labyrinth) for preheating, in order to achieve reduction of required combustion gas, LPG or natural gas or coal oil.
- the incinerator and boiler consist of: a)"Labyrinth" The mal-odorous gases pass in counter-flow direction and are preheated. They also maintain the outer surface of the incinerator at low temperature. b)"Turbulent mixer” It enhances the turbulence and, as a result, the gas mixing. In this way, more effective gas incineration is achieved. c)"Flame splitter” A non-aerodynamic cone that makes the flame flow in a turbulent way and operates as if tearing the flame in order to make it spread in a longer radial. d) "Catalyst" A catalyst could be optionally used to achieve better temperature conditions. This, however, would raise the cost of the project.
- Heaters which are the necessary stabilizers of the relative humidity in the inner curved surface to prevent problems in the operation of the gas exhauster or the ventilator
- the whole construction is to be equipped with sensors and fully automated.
- the construction is very economical and necessary for the protection of the environment and the maintenance of the ecological balance, with the benefits from the production of the thermal energy.
- FIG. 1 Collector Figure 2 Collector + Gas Exhauster Figure 3 Collector + Gas Exhauster + one-direction Valves Figure 4 Collector + Gas Exhauster + Ventilator + one-direction Valves + Compressor and the suitable tubing if recycling is implemented Figure 5 : Collector + Gas Exhauster + Ventilator + 95 one-direction Valves + Compressor and the suitable tubing if recycling is implemented + tubing from the dome outlet to the incinerator Figure 6 : Collector + Gas Exhauster + Ventilator + one-direction Valves + Compressor 100 and the suitable tubing if recycling is implemented + tubing from the dome outlet to the incinerator + Incinerator and Boiler Figure 7 : Collector + Gas Exhauster + Ventilator + one-direction Valves + Compressor 105 and the suitable tubing if recycling is implemented + tubing from the dome outlet to the incinerator + Incinerator and Boiler + Fuel tank + Chimney
- the Figure 8 shows the incinerator and boiler parts: Figure 8.
- A Labyr
- composition of air pollutants from these wastewater treatments plants typically 120 include:
- the dome (a convex surface which is fitted air-tightly on the wastewater treatment tanks) will be constructed out of iron sheet 6 mm, in order to avoid leakage due to the welding of the iron sheets.
- the biomass consumes 1 kg O /m waste and about 670 'm air/day (28 m /h) are required. Based on this consideration, a dimensioning of the construction will be
- the required quantity of air is the sum of 280m" Pa and the air of 150 compressor (m 3 /h) that is necessary for biomass oxygenation.
- the air (oxygen) will be bubbled with a system of thin tubes at the bottom of the plant.
- the dimensioning of the incinerator will be based on the gas-mixture velocity 155 (mal-odorous gases + LPG) from the turbulent mixer in order to avoid flame extinction.
- a catalyst could be used to achieve conversion at lower temperatures.
- the system will include portable analytical equipment for monitoring of all 160 the polluting gases and and the flow rate of the LPG can be regulated in order to achieve almost perfect combustion.
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP01904231A EP1409924B1 (en) | 2000-02-15 | 2001-02-15 | A full-scale automated system for the destruction of air pollutants originating from wastewater treatment plants |
AU2001232142A AU2001232142A1 (en) | 2000-02-15 | 2001-02-15 | A full-scale automated system for the destruction of air pollutants originating from wastewater treatment plants |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GR20000100045A GR1003543B (en) | 2000-02-15 | 2000-02-15 | Automatic industrial system for sucking gas pollutants in biological sewage treatment plants |
GR20000100045 | 2000-02-15 | ||
GR20000100358A GR1003829B (en) | 2000-10-19 | 2000-10-19 | A full-scale automated system for the destruction of air pollutants originating from wastewater treatment plants |
GR20000100358 | 2000-10-19 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2001061247A1 true WO2001061247A1 (en) | 2001-08-23 |
Family
ID=26316691
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/GR2001/000010 WO2001061247A1 (en) | 2000-02-15 | 2001-02-15 | A full-scale automated system for the destruction of air pollutants originating from wastewater treatment plants |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP1409924B1 (en) |
AU (1) | AU2001232142A1 (en) |
CY (1) | CY1106953T1 (en) |
ES (1) | ES2291292T3 (en) |
PT (1) | PT1409924E (en) |
WO (1) | WO2001061247A1 (en) |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1349123A (en) * | 1972-09-01 | 1974-03-27 | Olesen L F | Smoke control apparatus |
FR2366517A1 (en) * | 1976-09-29 | 1978-04-28 | Kleinewefers Ind Co Gmbh | Burner for combustion of effluent gases - using an auxiliary fuel and extra air, providing a swirling motion |
US4311593A (en) * | 1980-09-15 | 1982-01-19 | Bacardi Corporation | Process for treatment of waste water |
US4486310A (en) * | 1983-03-07 | 1984-12-04 | Thornton Marvin L | Wastewater trickling filter air recirculation process |
JPS63186920A (en) * | 1987-01-29 | 1988-08-02 | Ookura Sangyo Kk | Power generator |
DE3738141A1 (en) * | 1987-11-10 | 1989-05-24 | Hermann Morawetz | Burner, in particular gas burner |
JPH02302510A (en) * | 1989-05-18 | 1990-12-14 | Nakano Tomio | Deodorizer for aspirator of night solid collecting tanker vehicle |
WO1994014008A1 (en) * | 1992-12-17 | 1994-06-23 | Thermatrix Inc. | Method and apparatus for control of fugitive voc emissions |
-
2001
- 2001-02-15 ES ES01904231T patent/ES2291292T3/en not_active Expired - Lifetime
- 2001-02-15 EP EP01904231A patent/EP1409924B1/en not_active Expired - Lifetime
- 2001-02-15 PT PT01904231T patent/PT1409924E/en unknown
- 2001-02-15 AU AU2001232142A patent/AU2001232142A1/en not_active Abandoned
- 2001-02-15 WO PCT/GR2001/000010 patent/WO2001061247A1/en active IP Right Grant
-
2007
- 2007-10-22 CY CY20071101363T patent/CY1106953T1/en unknown
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1349123A (en) * | 1972-09-01 | 1974-03-27 | Olesen L F | Smoke control apparatus |
FR2366517A1 (en) * | 1976-09-29 | 1978-04-28 | Kleinewefers Ind Co Gmbh | Burner for combustion of effluent gases - using an auxiliary fuel and extra air, providing a swirling motion |
US4311593A (en) * | 1980-09-15 | 1982-01-19 | Bacardi Corporation | Process for treatment of waste water |
US4486310A (en) * | 1983-03-07 | 1984-12-04 | Thornton Marvin L | Wastewater trickling filter air recirculation process |
JPS63186920A (en) * | 1987-01-29 | 1988-08-02 | Ookura Sangyo Kk | Power generator |
DE3738141A1 (en) * | 1987-11-10 | 1989-05-24 | Hermann Morawetz | Burner, in particular gas burner |
JPH02302510A (en) * | 1989-05-18 | 1990-12-14 | Nakano Tomio | Deodorizer for aspirator of night solid collecting tanker vehicle |
WO1994014008A1 (en) * | 1992-12-17 | 1994-06-23 | Thermatrix Inc. | Method and apparatus for control of fugitive voc emissions |
Non-Patent Citations (2)
Title |
---|
PATENT ABSTRACTS OF JAPAN vol. 012, no. 459 (M - 770) 2 December 1988 (1988-12-02) * |
PATENT ABSTRACTS OF JAPAN vol. 015, no. 081 (M - 1086) 25 February 1991 (1991-02-25) * |
Also Published As
Publication number | Publication date |
---|---|
CY1106953T1 (en) | 2012-09-26 |
PT1409924E (en) | 2007-12-07 |
EP1409924B1 (en) | 2007-08-29 |
AU2001232142A1 (en) | 2001-08-27 |
EP1409924A1 (en) | 2004-04-21 |
ES2291292T3 (en) | 2008-03-01 |
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