WO2015005766A1 - An integrated waste incinerating and purifying apparatus - Google Patents
An integrated waste incinerating and purifying apparatus Download PDFInfo
- Publication number
- WO2015005766A1 WO2015005766A1 PCT/MY2014/000209 MY2014000209W WO2015005766A1 WO 2015005766 A1 WO2015005766 A1 WO 2015005766A1 MY 2014000209 W MY2014000209 W MY 2014000209W WO 2015005766 A1 WO2015005766 A1 WO 2015005766A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- combustion chamber
- exhaust gas
- waste
- based adsorbent
- adsorbent medium
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
-
- 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
- F23G5/40—Portable or mobile incinerators
- F23G5/42—Portable or mobile incinerators of the basket type
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/04—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material using washing fluids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/30—Sulfur compounds
- B01D2257/302—Sulfur oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/40—Nitrogen compounds
- B01D2257/404—Nitrogen oxides other than dinitrogen oxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/50—Carbon oxides
- B01D2257/504—Carbon dioxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/93—Toxic compounds not provided for in groups B01D2257/00 - B01D2257/708
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
- B01D2258/0291—Flue gases from waste incineration plants
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2219/00—Treatment devices
- F23J2219/40—Sorption with wet devices, e.g. scrubbers
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B10/00—Integration of renewable energy sources in buildings
- Y02B10/30—Wind power
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/12—Heat utilisation in combustion or incineration of waste
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/32—Direct CO2 mitigation
Definitions
- the invention relates to an integrated waste incinerating and purifying apparatus.
- the invention relates to an integrated waste incinerating and purifying apparatus which is able to simultaneously decompose the waste efficiently, and to remove the toxic compounds present in the exhaust gas produced thereof using a liquid-based adsorbent medium and a solid-based adsorbent medium before being released to the atmosphere.
- Waste management is crucial in order to minimize adverse effects on health or the environment, as caused by disposal of hazardous and non-hazardous wastes. Meanwhile, it is also preferred to recover valuable resources, in form of material or energy, from the disposed waste.
- the management practices may vary for different countries, as well as for residential and industrial estates, but in general, it comprises the steps of collecting the waste materials and transferring them for disposal.
- Landfilling, incineration and recycling are commonly used as waste disposal methods.
- waste materials are preferred to be combusted or subjected to an incineration process, as the energy content contained therein can be recovered, and at the same time, ash residue produced thereof can be further processed for various industrial applications, for example, production of construction materials.
- toxic or harmful gaseous products such as dioxins, carbon dioxide, nitrogen oxides, sulphur oxides, etc. are generated and the emission of these products to the environment may harm the health of the population.
- an apparatus which can reduce the release of toxic gaseous products to the atmosphere.
- An incinerator as disclosed in U.S. Patent No. 6976439 comprises a combustion chamber and a plurality of combustion-promoting fluid blast pipes, wherein the combustion-promoting fluid blast pipes are of a triple- pipe construction, having an air-supply pipe, a steam/gas-supply pipe and a water pipe.
- the combustion-promoting fluid blast pipes are of a triple- pipe construction, having an air-supply pipe, a steam/gas-supply pipe and a water pipe.
- high-pressure, high-temperature air, steam, combustible gas, or a combination thereof is supplied to the combustion chamber via the air-supply and steam/gas-supply pipes, while the water pipe of the fluid blast pipes is used for protecting the air-supply pipe and the steam/gas-supply pipe from heat.
- the incinerator is equipped with a water jacket.
- combustion heat developed within the combustion chamber is used to heat and vaporize the combustible gas having a high vaporization temperature. Further, dioxins and other toxic
- the incinerator comprises a burning section for incinerating the raw refuse and general wastes, and a removal section for removing toxic substances produced in the burning section.
- the burning section is having an ash chamber with an ash receiving dish, a primary combustion chamber and a drying chamber, while the removing section is having an exhaust gas pipe, a secondary chamber, and a blower installed with an installed fan.
- the incineration substances are accumulated in the primary combustion chamber, and ignited from the bottom. After ignition, the incineration substances are burnt in the air induced from the holes of the partition between combustion chamber and the drying chamber.
- the combustion chamber outlet is set up in line with the removal section to remove the toxic substances. Also, negative pressure condition is produced in the burning section as generation of carbon monoxide and dioxin and other toxic substances can be minimized or avoided at such condition.
- European Patent No. 0882933 discloses a burning apparatus and method for restricting the occurrence of dioxins.
- the incineration apparatus comprises a combustion furnace for burning combustibles in air within the furnace, a chlorinated aromatic compound measuring means for measuring amount of chlorinated aromatic compounds generated, and a control means for monitoring the amount of the chlorinated aromatic compounds generated.
- operating conditions of the combustion furnace may vary such as to decrease the amount of chlorinated aromatic compound generated therein.
- the apparatus comprises a bag filter for filtering an exhaust gas from the combustion chamber, or an activated carbon supply means for supplying activated carbon in the exhaust gas.
- One of the objects of the invention is to provide an apparatus for simultaneously decomposing the waste materials thermally in excess air, and purifying exhaust gas produced thereof.
- Another object of the invention is to introduce an waste disposal apparatus which minimizes release of the toxic compounds to the atmosphere.
- a further object of the invention is to introduce an effective and practical exhaust gas purification unit to be mounted on a combustion chamber for removing the toxic compounds present therefrom.
- Still another object of the invention is to introduce an apparatus which uses a liquid- based adsorbent medium and a solid-based adsorbent medium for removing ash or toxic compounds present in the exhaust gas as produced from waste incineration.
- Yet another object of the invention is to minimize operating or running cost of the apparatus by combining a solar power generator or a wind turbine to the compressor.
- an embodiment of the invention describes an integrated waste incinerating and purifying apparatus, comprising a closeable opening for receiving the waste, a combustion chamber for thermally decomposing the received waste in excess air from which ash and exhaust gases are produced, a collector disposed within the combustion chamber for collecting the ashes and non-combusted solids, an exhaust gas purifying unit mounted on the combustion chamber; wherein the exhaust gas purifying unit includes a liquid-based adsorbent medium which adsorbs uncollected ash or toxic compounds from the exhaust gas, and a solid-based adsorbent medium for entrapping any remaining toxic compound which passes through the liquid-based adsorbent medium, and an outlet attached to the exhaust gas purifying unit for expelling the purified gases to the atmosphere.
- the apparatus comprises a closeable opening which is preferably a hinged flap, where the waste is fed to the combustion chamber.
- a hinged flap minimizes occupational risk by reducing personnel exposure to the heat and smoke when feeding the waste to an operating apparatus.
- the combustion chamber of the apparatus where the waste is decomposed in excess air, comprises a plurality of inner walls with perforations, an outer wall made of a plurality layers of materials for withstanding high temperature due to the thermal decomposition, and a space between the inner and outer walls which allows the air to flow through the perforations to the combustion chamber.
- the exhaust gas purifying unit includes a liquid-based adsorbent medium which adsorbs uncollected ash or toxic compounds from the exhaust gas, and a solid-based adsorbent medium for entrapping any remaining toxic compound which passes through the liquid-based adsorbent medium.
- the liquid-based adsorbent medium is a mineral solution, whereas the solid-based adsorbent medium can be activated carbon, volcano ash or a combination thereof.
- the invention is not limited thereof or thereto.
- the apparatus includes an outlet attached to the exhaust gas purifying unit for expelling the purified gases to the atmosphere.
- Another embodiment of the invention is an integrated waste incinerating and purifying apparatus, further comprising a grating disposed within the combustion chamber and positioned above the collector for which the waste is placed.
- Still another embodiment of the invention is an integrated waste incinerating and purifying apparatus further comprising a compressor to pressurize the air for supplying to the combustion chamber.
- the apparatus of the invention is able to simultaneously decompose the waste efficiently, and to remove the toxic compounds present in the exhaust gas before being released to the atmosphere.
- Figure 1 is a side view of an integrated waste incinerating and purifying apparatus as described by one of the preferred embodiment of the invention.
- Figure 2a is an illustrative diagram of the inner wall of the combustion chamber having perforations of uniform diameter, as described by one of the preferred embodiment of the invention.
- Figure 2b is an illustrative diagram of the inner wall of the combustion chamber having perforations of varied diameters, as described by one of the preferred embodiment of the invention.
- the invention relates to an integrated waste incinerating and purifying apparatus.
- the invention relates to an integrated waste incinerating and purifying apparatus which is able to simultaneously decompose the waste efficiently, and to remove the toxic compounds present in the exhaust gas produced thereof using a liquid-based adsorbent medium and a solid-based adsorbent medium before being released to the atmosphere.
- the apparatus (100) comprises a closeable opening (101), a combustion chamber (102), a collector (103) which is slidable, an exhaust gas purifying unit (104) mounted on the combustion chamber (102), and an outlet (105) attached to the exhaust gas purifying unit (104).
- the closeable opening (101) is preferable to be a hinged flap which is movable from position A to B.
- a grating (106) is disposed within the combustion chamber (102) for which the waste is placed.
- the exhaust gas purifying unit (104) As waste is thermally decomposed in the combustion chamber (102) to produce ash, exhaust gas and non-combusted solids, it requires an exhaust gas purifying unit (104) to be mounted on the combustion chamber (102). As shown in Figure 1, the exhaust gas purifying unit (104) is divided into two sections by a matrix of solid-based adsorbent medium (1046), which are a lower section (1041) and an upper section
- the lower section (1041) is used to contain a liquid-based adsorbent medium (1045), and it comprises an inlet (1043) which allows exhaust gas produced in the combustion chamber (102) to enter, and a tubing (1044) extending from the inlet
- a matrix of solid-based adsorbent medium (1046) is found at the bottom of the upper section (1042), where the toxic compounds in the exhaust gas will be purified and passed through.
- the upper section (1042) generally contains purifying gas before being expelled to the atmosphere via the outlet (105).
- the apparatus (100) comprises a collector (103) which is movable, for collecting the ash and non-combusted solids.
- a compressor (107) is also needed for pressurizing the air supplied to the combustion chamber (102).
- the combustion chamber (102) comprises a plurality of inner walls with perforations, an outer wall made of a plurality layers of materials for withstanding high temperature, and a space between the inner and outer walls which allows the air to flow through the perforations to the combustion chamber (102).
- the perforations of the inner walls can be of uniform diameter sizes as illustrated in Figure 2a, or of varied diameter sizes as shown in Figure 2b.
- the invention discloses an integrated waste incinerating and purifying apparatus (100) comprising a closeable opening (101) for receiving the waste, a combustion chamber (102) for thermally decomposing the received waste in excess air from which ash and exhaust gases are produced, a collector (103) disposed within the combustion chamber (102) for collecting the ash and non-combusted solids, an exhaust gas purifying unit (104) mounted on the combustion chamber (102); wherein the exhaust gas purifying unit (104) includes a liquid-based adsorbent medium (1045) which adsorbs uncollected ash or toxic compounds from the exhaust gas, and a solid-based adsorbent medium (1046) for entrapping any remaining toxic compound which passes through the liquid-based adsorbent medium (1045), and an outlet (105) attached to the exhaust gas purifying unit (104) for expelling the purified gases to the atmosphere.
- the apparatus (100) comprises a closeable opening (101) where the waste is fed to the combustion chamber (102).
- the closeable opening (101) is a hinged flap, as it improves occupational safety by minimizing personnel exposure to heat and smoke when the waste is fed into an operating apparatus.
- the hinged flap is being disposed about an axis perpendicular to the width of the upper surface, characterized in that the hinged flap is movable between a first position in which it rests against one side wall and a second position in which the flap is pivoted inwardly from the first wall.
- the hinged flap may further comprise a stopper flap, which restricts the sliding motion of the hinged flap, and consequently, prevents users or operators from being hit by the flap.
- the waste as received therefrom is thermally decomposed in the combustion chamber (102) which comprises a plurality of inner walls with perforations, an outer wall made of a plurality layers of materials for withstanding high temperature due to the thermal decomposition, and a space between the inner and outer walls which allows the air to flow through the perforations to the combustion chamber (102).
- the perforations on the inner walls are preferred to be of diameters ranging from 5 to 14 cm. Further, the perforations on the inner wall can be of uniform diameter or of varied diameter sizes, as illustrated in Figures 2a and 2b.
- the outer wall is made of a plurality layers of materials, including stainless steel and wool, for withstanding high temperature of the decomposition process.
- thermal decomposition of the waste is carried out such that a fire is first set up by lighting up a paper or other materials which can be burned easily and continues to burn or thermally decompose the waste materials.
- the decomposition of the waste results to generation of ash and toxic compounds such as dioxins, carbon dioxide, nitrogen oxides, etc.
- Non-combusted solids remain intact and fall under influence of gravity into the collector (103).
- additional fuel or energy may be required in order to assist the incineration or thermal decomposition process.
- plasma incineration may take place in the combustion chamber (102), as higher temperature can be achieved, leading to more effective waste decomposition.
- plasma is produced by a discharge in air which is a carrier gas, which promotes the generation of positive or negative ions.
- higher temperature range in the combustion chamber (102) can also be achieved.
- the thermal energy in the plasma as produced is transmitted to the waste as deposited, resulting to decomposition from which ash and exhaust gas are produced.
- the exhaust gas produced contains toxic compounds such as dioxins, carbon dioxides, carbon monoxides, nitrogen oxides, sulphur dioxides, etc.
- mineral and metal substances are non-combustible and remain as solid throughout the incineration process.
- the collector (103) is used to collect non-combusted solids and the ash as produced from the plasma incineration. Typically, the ash and non-combusted solids are dropped by gravity and accumulated on the collector (103).
- the collector (103) is preferred to be movable or slidable, allowing for recovery of ash for further processing for other industrial applications. However, some of the ash remain uncollected, as they are carried by the air entering through the perforations of the inner wall, and then discharged to the atmosphere with the exhaust gas produced from the thermal decomposition. Therefore, an exhaust gas purifying unit (104) is mounted on the combustion chamber (102) for removing ash and toxic compounds contained therein.
- the exhaust gas purifying unit (104) is a container with an inlet (1043) being disposed at a bottom surface.
- the exhaust gas purifying unit (104) can be divided into a lower section (1041) and an upper section (1042) by a matrix of solid-based adsorbent medium (1046); whereby the lower section (1041) is used to contain a liquid-based adsorbent medium (1045), while the upper section (1042) is filled with purified gas.
- the liquid-based adsorbent medium (1045) is a mineral solution
- the solid-based adsorbent medium (1046) can be activated carbon, volcano ash or a combination thereof.
- selection of the liquid- (1045) or solid-based adsorbent medium (1046) of the invention is not limited thereto or thereby.
- the lower section (1041) comprises an inlet (1043) disposed at the bottom surface where the ash and exhaust gas are received, and a tubing (1044) extending from the inlet (1043).
- the inlet (1043) and the tubing (1044) are cylindrical.
- the number of the inlet (1043) or tubing (1044) is not limited therein, depending on the waste volume subjected to incineration or the amount of exhaust gas produced therefrom.
- the length of the tubing (1044) may also be varied, but it should be greater than the depth of the liquid-based adsorbent medium (1045) contained therein, in order to prevent the liquid-based adsorbent medium (1045) from leaking or escaping through the tubing (1044).
- the cylindrical tubing (1044) is preferably 17.8 cm long, and the liquid-based adsorbent medium (1045) contained therein has a depth of 12.7 cm.
- the upper section (104) is having a bottom surface comprising a matrix of solid-based adsorbent medium (1046) which is formed by embedding the solid-based adsorbent medium (1046) on a wire mesh or a grating.
- the solid-based adsorbent medium (1046) can also be loaded and distributed uniformly across the wire mesh or the grating having a spacing smaller than the size of the solid-based adsorbent medium (1046).
- the exhaust gas produced in the combustion chamber (102) is subjected to a two-step purification process. As soon as the exhaust gas is produced, it continuously flows into the lower section (1045) of the purification unit (104) through the inlet (1043), due to pressure difference between the combustion chamber (102) and the purification unit (104), and circulates around it.
- First step of purification occurs, where ash and some of the toxic compounds contained therein are dissolved in the liquid-based adsorbent medium (1045).
- the liquid-based adsorbent medium (1045) is replenished or replaced periodically with fresh adsorbent medium, such as to retain optimum adsorption efficiency.
- Gradual increase of gas volume in the lower section (1041) of the purification unit (104) exerts a pressure on the exhaust gas to flow through the matrix of solid-based adsorbent medium (1046) on the upper section (1042) of the purification unit (104), where second step of purification occurs.
- the remaining toxic compound which does not dissolve in the liquid-based adsorbent medium (1045), is adsorbed by the solid- based adsorbent medium (1046).
- the purified gas flows through the upper section (1042) of the purification unit (104) and is to be discharged to the atmosphere via the outlet (105) attached on the purification unit (104).
- the outlet (105) is attached to a top surface of the exhaust gas purifying unit (104) for expelling the purified gases to the atmosphere.
- the outlet (105) is of a cylindrical shape, similar to that of the inlet (1043) and tubing (1044) at the lower section (1041) of the exhaust gas purification unit (104).
- Another embodiment of the invention is an integrated waste incinerating and purifying apparatus (100), further comprising a grating (106) disposed within the combustion chamber (102) for which the waste is placed.
- the grating (106) is preferably disposed within the combustion chamber (102) for placing or holding the waste as received from the closeable opening (101) at the high temperature zones where the thermal decomposition can be more effectively.
- the grating (106) is positioned above the collector (103), characterized such that the ash and non-combusted solids can be collected by gravity on the collector (103).
- Still another embodiment of the invention is an integrated waste incinerating and purifying apparatus (100), further comprising a compressor (107) to pressurize the air for supplying to the combustion chamber (102).
- the apparatus (100) comprises a compressor (107) which is used to pressurize the air from the atmosphere before supplying to the combustion chamber (102). By pressurizing, the air can be transmitted at higher speed through the space between the inner and outer walls and through the perforations of the inner walls.
- the purified gas can also be recycled and used as the carrier gas for producing plasma.
- the compressor is electrically driven, where the electrical power or energy can be generated by using a solar power generator, a wind turbine, or a combination thereof.
- the electrical power supplied to the compressor can be minimised, consequently resulting to lower running or operating cost.
- the solar power generator or the wind turbine can act as an emergency power supply to the compressor such that operation of the compressor is not affected in event of power outage or power cut.
- the apparatus (100) disclosed in the invention is able to process approximately 20 to 1000 kg waste per day, depending on type and moisture content of the materials, and weather condition when the incineration process is being carried out.
- waste with a moisture content of less than 70% is being fed to the apparatus (100) for thermal decomposition into ash and exhaust gas.
- Presence of objects such as metals or minerals does not affect the incineration or thermal decomposition process, as these materials remain solid or non-combusted, and are to be accumulated and collected at the collector (103).
- the apparatus (100) disclosed in the invention can be employed to reduce the release of toxic compounds or green house gases such as dioxins, carbon dioxides, nitrogen oxides, sulphur oxides, etc. to the atmosphere, thus minimizing environmental pollution.
- the apparatus of the invention can be used at different locations, including residential area and industrial estates, for thermally decomposing wastes such as waste papers, domestic wastes, wood, vinyl products, nylon products, urethane, fabrics, tires or a combination thereof.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- General Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
- Gasification And Melting Of Waste (AREA)
- Chimneys And Flues (AREA)
- Incineration Of Waste (AREA)
Abstract
Description
Claims
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU2014287896A AU2014287896B2 (en) | 2013-07-11 | 2014-07-10 | An integrated waste incinerating and purifying apparatus |
| PH12016500076A PH12016500076B1 (en) | 2013-07-11 | 2016-01-11 | An integrated waste incinerating and purifying apparatus |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| MYPI2013701223A MY170506A (en) | 2013-07-11 | 2013-07-11 | An integrated waste incinerating and purifying apparatus |
| MYPL2013701223 | 2013-07-11 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2015005766A1 true WO2015005766A1 (en) | 2015-01-15 |
Family
ID=52280337
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/MY2014/000209 Ceased WO2015005766A1 (en) | 2013-07-11 | 2014-07-10 | An integrated waste incinerating and purifying apparatus |
Country Status (4)
| Country | Link |
|---|---|
| AU (1) | AU2014287896B2 (en) |
| MY (1) | MY170506A (en) |
| PH (1) | PH12016500076B1 (en) |
| WO (1) | WO2015005766A1 (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106090937A (en) * | 2016-07-18 | 2016-11-09 | 河北天朗环保工程有限公司 | A kind of incinerator |
| CN106482126A (en) * | 2016-11-18 | 2017-03-08 | 广西大学 | A kind of incinerator |
| CN107575872A (en) * | 2017-08-22 | 2018-01-12 | 信和(天津)环保科技发展有限公司 | Refuse disposal installation |
| CN114777134A (en) * | 2022-04-24 | 2022-07-22 | 四川天法科技有限公司 | Integrated household garbage incineration device |
| WO2023167581A1 (en) * | 2022-03-01 | 2023-09-07 | Nano Silver Manufacturing Sdn Bhd | A thermal decomposition reactor for decomposing waste material and a thermal decomposition system |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5695726A (en) * | 1993-06-10 | 1997-12-09 | Beco Engineering Company | Removal of mercury and cadmium and their compounds from incinerator flue gases |
| US6324999B1 (en) * | 1998-09-04 | 2001-12-04 | Fumio Maejima | Incinerator for removing noxious substances |
| US20100202948A1 (en) * | 2007-07-12 | 2010-08-12 | Indigo Technologies Group Pty Ltd | Reverse Flow Reactor |
-
2013
- 2013-07-11 MY MYPI2013701223A patent/MY170506A/en unknown
-
2014
- 2014-07-10 WO PCT/MY2014/000209 patent/WO2015005766A1/en not_active Ceased
- 2014-07-10 AU AU2014287896A patent/AU2014287896B2/en active Active
-
2016
- 2016-01-11 PH PH12016500076A patent/PH12016500076B1/en unknown
Patent Citations (3)
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| US5695726A (en) * | 1993-06-10 | 1997-12-09 | Beco Engineering Company | Removal of mercury and cadmium and their compounds from incinerator flue gases |
| US6324999B1 (en) * | 1998-09-04 | 2001-12-04 | Fumio Maejima | Incinerator for removing noxious substances |
| US20100202948A1 (en) * | 2007-07-12 | 2010-08-12 | Indigo Technologies Group Pty Ltd | Reverse Flow Reactor |
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| CN106090937A (en) * | 2016-07-18 | 2016-11-09 | 河北天朗环保工程有限公司 | A kind of incinerator |
| CN106482126A (en) * | 2016-11-18 | 2017-03-08 | 广西大学 | A kind of incinerator |
| CN107575872A (en) * | 2017-08-22 | 2018-01-12 | 信和(天津)环保科技发展有限公司 | Refuse disposal installation |
| WO2023167581A1 (en) * | 2022-03-01 | 2023-09-07 | Nano Silver Manufacturing Sdn Bhd | A thermal decomposition reactor for decomposing waste material and a thermal decomposition system |
| CN114777134A (en) * | 2022-04-24 | 2022-07-22 | 四川天法科技有限公司 | Integrated household garbage incineration device |
Also Published As
| Publication number | Publication date |
|---|---|
| AU2014287896B2 (en) | 2018-09-27 |
| PH12016500076A1 (en) | 2016-04-18 |
| AU2014287896A1 (en) | 2016-02-04 |
| PH12016500076B1 (en) | 2016-04-18 |
| MY170506A (en) | 2019-08-08 |
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