EP0921352B1 - Verfahren für Verbrennung von Abfällen und Behandlung von Flugstäuben und Vorrichtung zur Durchführung des Verfahrens - Google Patents
Verfahren für Verbrennung von Abfällen und Behandlung von Flugstäuben und Vorrichtung zur Durchführung des Verfahrens Download PDFInfo
- Publication number
- EP0921352B1 EP0921352B1 EP19980403008 EP98403008A EP0921352B1 EP 0921352 B1 EP0921352 B1 EP 0921352B1 EP 19980403008 EP19980403008 EP 19980403008 EP 98403008 A EP98403008 A EP 98403008A EP 0921352 B1 EP0921352 B1 EP 0921352B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- pulp
- household
- ash
- furnace
- waste
- 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.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title claims description 54
- 239000010881 fly ash Substances 0.000 title claims description 29
- 238000004056 waste incineration Methods 0.000 title description 6
- 239000002956 ash Substances 0.000 claims description 48
- 239000010791 domestic waste Substances 0.000 claims description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- 239000002699 waste material Substances 0.000 claims description 22
- 239000002440 industrial waste Substances 0.000 claims description 21
- 238000006460 hydrolysis reaction Methods 0.000 claims description 9
- 230000007062 hydrolysis Effects 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 7
- 229910001504 inorganic chloride Inorganic materials 0.000 claims description 6
- 238000000605 extraction Methods 0.000 claims description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 2
- 239000011707 mineral Substances 0.000 claims description 2
- 239000005416 organic matter Substances 0.000 claims description 2
- 238000000746 purification Methods 0.000 claims description 2
- 238000011144 upstream manufacturing Methods 0.000 claims description 2
- 239000003546 flue gas Substances 0.000 claims 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims 5
- 239000007864 aqueous solution Substances 0.000 claims 1
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 25
- 239000003517 fume Substances 0.000 description 10
- 239000000779 smoke Substances 0.000 description 9
- 239000010882 bottom ash Substances 0.000 description 8
- 239000010802 sludge Substances 0.000 description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 4
- 150000001805 chlorine compounds Chemical class 0.000 description 4
- 229910001385 heavy metal Inorganic materials 0.000 description 4
- 238000002347 injection Methods 0.000 description 4
- 239000007924 injection Substances 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 230000006641 stabilisation Effects 0.000 description 3
- 238000011105 stabilization Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 230000009466 transformation Effects 0.000 description 3
- 238000004017 vitrification Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 239000010426 asphalt Substances 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L calcium carbonate Substances [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 230000008030 elimination Effects 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 150000004760 silicates Chemical class 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 238000001149 thermolysis Methods 0.000 description 2
- 230000001131 transforming effect Effects 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical class [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 235000010216 calcium carbonate Nutrition 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- -1 oxides Chemical class 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- CHWRSCGUEQEHOH-UHFFFAOYSA-N potassium oxide Chemical class [O-2].[K+].[K+] CHWRSCGUEQEHOH-UHFFFAOYSA-N 0.000 description 1
- 229910001950 potassium oxide Inorganic materials 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 235000002639 sodium chloride Nutrition 0.000 description 1
- 229910001948 sodium oxide Inorganic materials 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J3/00—Removing solid residues from passages or chambers beyond the fire, e.g. from flues by soot blowers
- F23J3/06—Systems for accumulating residues from different parts of furnace plant
-
- 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
- F23G5/008—Incineration of waste; Incinerator constructions; Details, accessories or control therefor adapted for burning two or more kinds, e.g. liquid and solid, of waste being fed through separate inlets
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/70—Blending
- F23G2201/702—Blending with other waste
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2202/00—Combustion
- F23G2202/10—Combustion in two or more stages
- F23G2202/106—Combustion in two or more stages with recirculation of unburned solid or gaseous matter into combustion chamber
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2209/00—Specific waste
- F23G2209/10—Liquid waste
- F23G2209/101—Waste liquor
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2209/00—Specific waste
- F23G2209/12—Sludge, slurries or mixtures of liquids
Definitions
- the invention relates to a method for processing fly ash entrained by the fumes emitted during the incineration of household and / or industrial waste, to a household waste incineration process and / or manufacturers including such a process for processing entrained fly ash, and a device for the implementation of these methods.
- fly ash are pulverulent solids made up unburnt particles, silicates and silico-aluminates calcium, inorganic chlorides in particular of heavy metals and alkaline earths such than sodium and potassium chlorides, oxides, sulfates and calcium carbonates as well as metals heavy. These fly ash are collected throughout along the smoke circuit from which they are separated, particular, by filters.
- WO-A-8,909,253 describes a reduction method acid gas emissions by reducing agents put in contact with fly ash, this process involving the disposal of said ashes by their transformation into bottom ash in the incinerator.
- the invention aims to overcome the drawbacks of the methods of the prior art by proposing a treatment method fly ash entrained by the fumes emitted during the incineration of household waste and / or industrialists by transforming these ashes into bottom ash by clinkérisation.
- the invention uses a reverse reaction to WO-A-8,909,253 allowing the elimination of inorganic chlorides and leading to the formation of hydrochloric acid.
- said supply of water is made by adding water alone.
- said contribution water is made by adding wet sludge water, organic matter and mineral matter such as sludge from stations water purification or black liquors from paper mills.
- said pulp has a dryness of between 20 and 40% by weight.
- a mixture of said pulp is produced with household and / or industrial waste before introduction of this mixture by the normal means of introducing household and / or industrial waste.
- household and / or industrial waste is introduced by normal means of waste introduction and the pulp is introduced by means of introduction separate located upstream and in the cold zone of the the incinerator.
- the pulp and household waste and / or manufacturers are introduced by separate means, the household and / or industrial waste being introduced by the normal way of introducing waste and pulp being introduced directly into the hearth of the incinerator.
- the invention also relates to an incineration process household and / or industrial waste, characterized in that that he understands the treatment of fly ash driven by the fumes emitted during this incineration by the process described above.
- said means of transport is connected to the household by the means of introduction opening into the chute located under the normal hopper for the introduction of household waste and / or industrial.
- said means of transport is connected to the household by the hopper normal introduction of household waste and / or industrial.
- said introduction means is connected directly to the fireplace, in hot zone.
- the means of transporting the pulp is a pump associated with a conduit.
- the means of transporting the pulp is consisting of bulk mechanical conveyors, with belts or bucket.
- the waste to be incinerated is introduced through the hopper 11 and the chute 9 in a combustion hearth 10 where they are cremated.
- the incinerator used in this process can be either a oven without heat recovery, in which case all ash is collected under filter 2, i.e. a furnace-boiler that is to say an oven equipped with the hearth 10 and a heat recovery means constituted by the boiler 1, in which case the ashes are recovered from a partly under the boiler 1 and partly under the filter 2.
- filter 2 i.e. a furnace-boiler that is to say an oven equipped with the hearth 10 and a heat recovery means constituted by the boiler 1, in which case the ashes are recovered from a partly under the boiler 1 and partly under the filter 2.
- the fly ash is then further processed in another device, before storage.
- the invention proposes to process the fly ash continuously and in the same installation as that planned for the treatment of waste themselves.
- the invention proposes to collect the all of the ashes, and mix them in a mixer 5 with water from an introduction means 6.
- a pulp is formed which is then injected by a means of transport 7, 8, into the hearth 10.
- This reintroduction of ashes, in the form of pulp in focus 10 can be done either directly in the hearth 10 and in the hot zone, by a device sludge injection known per se, either with waste to be incinerated, in a cold zone.
- the pulp may either be mixed with the waste to be incinerated before introduction of this pulp / waste mixture through the hopper 11, either injected by a separate introduction means, in the chute 9.
- the process for handling fly ash from the invention is therefore particularly advantageous because it transforms ash into bottom ash, which is easily recyclable and therefore recoverable.
- this process directly uses the thermal energy of the household and / or industrial waste incinerator and minimizes the thermal energy required to process ash which only affects the surface of the grains of ashes and not the whole mass of these grains, and this without addition of reagent.
- the chlorine present in these ash is removed as hydrochloric acid by hydrolysis of alkali and alkaline earth chlorides and heavy metals, this hydrochloric acid then being retained in the smoke treatment system including the incineration plant is regulated equipped. This process also removes unburnt from carbon in the form of carbon dioxide.
- Water to make an easily transportable pulp, preferably by a pump, and to hydrolyze the chlorides is supplied by either water alone or, advantageously, by the water contained in sludge wet from water treatment plant. In the latter case, we save the water that should have been used to make the pulp.
- the clinkerization of ash and incineration of sludge from water treatment plants are performed in a single operation.
- the waste is introduced through the hopper 11 and the ashes are collected under the boiler 1 and under the filter 2 and are routed by screws 3 and 4 to a mixer 5.
- the ash represents approximately a weight of 20 kg of dry matter.
- the mixer 5 is supplied with water by the means introduction 6.
- Water is dosed by a system volumetric or classical mass so as to obtain out of the mixer a pulp having a dryness, that is to say a dry matter content, which allows it to be easily pumped by a pump 7 known per se.
- the pump 7 is volumetric. She sends the pulp through the conduit 8 and the introduction means 15 located in the chute 9 in the hearth 10.
- the pulp is introduced into the hearth 10 at the same time that the waste and we will make sure to distribute the pulp on the entire width of the chute 9.
- the invention allows a continuous treatment and complete elimination of the need to dispose of fly ash.
- the mixer 5 is fed, by the introduction means 6, with wet sludge from water treatment plants.
- 150 kg of sludge at 20% by weight of materials are used dry, which gives a pulp with a dryness of 30% which is still easily transportable, for example by pumping.
- a means of transport is used here mechanical consisting of a series of mass conveyors or belt and bucket elevator.
- the pulp is mixed with the waste to be incinerated before introduction of this mixing by hopper 11.
- the pulp / waste mixture to to be cremated is then sent to hearth 10 where the fly ash undergoes hydrolysis reactions and of clinkering described above and are integrated clinker resulting from waste incineration themselves.
- Example 1 the clinkerized ashes have then the same physico-chemical characteristics as clinkers.
- Example 2 The procedure is as in Example 1, except that the pulp is directly introduced into the hearth 10. Again, the pulp will be hydrolyzed and clinkered and integrated into the clink as in examples 1 and 2.
- the ash treatment process and device flying driven by the fumes from the incineration of household and / or industrial waste according to the invention and as described above, can of course be integrated into a process and a waste incineration device, respectively industrial and / or household goods of the prior art.
- the invention also encompasses all of the household waste and / or incineration processes manufacturers that include the processing step ash entrained by the fumes from the incineration of household and / or industrial waste and which consists of collecting these ashes, transforming them into aqueous pulp and to recycle them, in the incinerator of waste, to clinkerize it and integrate it into clinkers produced in this incinerator.
- any device for the incineration of household and / or industrial waste which includes the ash treatment device entrained by fumes from the incineration of household waste and / or industrial and which includes a means of transformation, recovery and transformation of ash into pulp aqueous and a means of injection and recycling of this aqueous pulp in the incinerator is encompassed by the invention.
- the method and the device of the invention are not limited to injection means, pulp transport, obtaining pulp and recycling this pulp in the fireplace described and illustrated here, as long as these means are used to recycle the ash entrained in the gases from the incineration of household waste and / or industrial, in the form of aqueous pulp, in the incinerator itself.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
Claims (13)
- Verfahren zur Behandlung der Flugaschen, welche mit Rauchen mitgezogen werden, die bei der Verbrennung von Haushalts- und Industrieabfällen ausgestoßen wird, dadurch gekennzeichnet, dass es die Stufen umfasst von:Sammeln der Aschen entlang eines Kreislaufs der Rauche,Bildung einer Weichmasse durch Zufuhr von Wasser zu diesen Aschen,Einführung der so erhaltenen Weichmasse in den Feuerraum (10) des Abfallverbrenners (1), um die Aschen durch Hydrolyse der in den Aschen enthaltenen Chloride und Klinkerbildung zu Schlacke zu machen,Gewinnung am Ausgang des Brenners (1) der gebildeten Schlacken durch den Abzieher (12).
- Verfahren zur Behandlung nach Anspruch (1), dadurch gekennzeichnet, dass die Wasserzufuhr mittels einer einzigen Wasserzufuhr durchgeführt wird.
- Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass die Wasserzufuhr durch Zugabe von aus Wasser, organischen Materialien und mineralischen Materialien bestehenden feuchten Schlämmen, wie z.B. Schlämmen, die von Wasserverdampfungsstationen oder den schwarzen Flüssigkeiten von Papierherstellungen kommen, durchgeführt wird.
- Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass die Weichmasse eine Trockenheit zwischen 20 und 40 Gew.% hat.
- Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass man eine Mischung der Weichmasse mit den Haushalts- und Industrieabfällen vor Einführung dieser Mischung durch das Einführungsmittel (11) der Industrie- und/oder Haushaltsabfälle durchführt.
- Verfahren nach einem der Ansprüche 1 bis 4, dadurch gekennzeichnet, dass die Haushalts- und/ oder Industrieabfälle durch das normale Einführungsmittel (11) eingeführt werden und dass die Weichmasse durch ein getrenntes Einführungsmittel (15) eingeführt wird, dass stromaufwärts und in der kalten Zone des Feuerraums (10) angeordnet ist.
- Verfahren nach einem der Ansprüche 1 bis 4, dadurch gekennzeichnet, dass die Weichmasse und die Haushalts- und/oder Industrieabfälle durch getrennte Einführungsmittel eingeführt werden, wobei die Haushalts- und/oder Industrieabfälle durch das normale Einführungsmittel (11) eingeführt werden und die Weichmasse direkt in den Feuerraum (10) des Brenners (1) eingeführt wird.
- Verfahren zur Verbrennung der Haushalts- und/oder Industrieabfälle, dadurch gekennzeichnet, dass es die Behandlung der durch die Rauche mitgezogenen Flugaschen, welche bei dieser Verbrennung ausgestoßen werden, umfasst, durch ein Verfahren nach einem der Ansprüche 1 bis 7.
- Vorrichtung zur Durchführung des Verfahrens gemäß einem der vorhergehenden Ansprüche umfassend:dadurch gekennzeichnet, dass sie zusätzlich umfasst:ein Mittel (11) zur Einführung der Abfälle in den Feuerraum (10) eines Brenners (1),einen Abzieher (12), der am unteren Ausgang des Feuerraumes (10) angeordnet ist, um die so gebildeten Schlacken zu gewinnen,ein Trennmittel (2) der Flugaschen der Rauche zum Reinigen dieser Rauche,ein Mittel zur Extraktion (13) und zur Entfernung (14) der gereinigten Rauche undwenigstens ein Mittel zur Gewinnung (3, 4) der Flugaschen entlang des Kreislaufs der Rauche verbunden mit einem Knetmischer (5),ein Mittel zum Speisen einer wässrigen Lösung (6), dass mit dem Knetmischer (5) verbunden ist,ein Transportmittel (7, 8) der in dem Knetmischer (5) gebildeten Weichmasse, das den unteren Teil des Knetmischers (5) direkt oder indirekt mit dem Feuerraum (10) des Brenners (1) verbindet um die Weichmasse in den Feuerraum (10) zuzuführen, damit die Aschen zu Schlacken durch Hydrolyse der in den Aschen enthaltenen anorganischen Chloride und durch Klinkerbildung umgeformt werden.
- Vorrichtung nach Anspruch 9, dadurch gekennzeichnet, dass das Transportmittel (7, 8) mit dem Feuerraum (10) durch das Mittel zur Einführung (15) verbunden ist, welches in einer Rutsche (9) mündet, die unter dem Trichter (11) zur normalen Einführung der Haushalts- und/oder Industrieabfälle angeordnet ist.
- Vorrichtung nach Anspruch 9, dadurch gekennzeichnet, dass das Transportmittel (7, 8) mit dem Feuerraum (10) durch den Trichter (11) zur normalen Einführung der Haushalts- und/oder Industrieabfälle verbunden ist.
- Vorrichtung nach Anspruch 9, dadurch gekennzeichnet, dass das Transportmittel (7, 8) direkt mit dem Feuerraum (10) in der warmen Zone verbunden ist.
- Vorrichtung nach einem der Ansprüche 9 bis 12, dadurch gekennzeichnet, dass das Transportmittel (7, 8) eine Pumpe (7) ist, die mit einer Leitung (8) verbunden ist.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR9715419A FR2771946B1 (fr) | 1997-12-05 | 1997-12-05 | Procede d'incineration de dechets, procede de traitement des cendres volantes et dispositif pour la mise en oeuvre de ces procedes |
| FR9715419 | 1997-12-05 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP0921352A1 EP0921352A1 (de) | 1999-06-09 |
| EP0921352B1 true EP0921352B1 (de) | 2004-06-23 |
Family
ID=9514243
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP19980403008 Expired - Lifetime EP0921352B1 (de) | 1997-12-05 | 1998-12-01 | Verfahren für Verbrennung von Abfällen und Behandlung von Flugstäuben und Vorrichtung zur Durchführung des Verfahrens |
Country Status (4)
| Country | Link |
|---|---|
| EP (1) | EP0921352B1 (de) |
| ES (1) | ES2223112T3 (de) |
| FR (1) | FR2771946B1 (de) |
| PT (1) | PT921352E (de) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105910112A (zh) * | 2016-04-18 | 2016-08-31 | 娈疯 | 垃圾焚烧厂飞灰综合处理工艺 |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE1014437A3 (nl) * | 2001-10-24 | 2003-10-07 | Meyer Andru De | Methode en inrichting voor het verdikken, drogen en verbranden van vochtige massa's zoals varkensmest zonder voorafgaandelijke scheiding. |
| DE10213787C1 (de) * | 2002-03-27 | 2003-11-27 | Martin Umwelt & Energietech | Verfahren zum Minimieren der Konzentration an toxischen organischen Schadstoffen in Flugstäuben |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2169733B1 (de) * | 1972-01-31 | 1974-09-13 | Socea | |
| US4231303A (en) * | 1978-10-31 | 1980-11-04 | Showa Denki K.K. | Method for incineration of organic chlorine compound and incinerator used therefor |
| FR2579723B2 (fr) * | 1985-04-01 | 1988-06-17 | Henry Eugene | Incinerateur de boues urbaines et ordures |
| DK153888A (da) * | 1988-03-21 | 1989-09-22 | Fls Miljoe A S | Fremgangsmaade til forbraending af affald |
| FR2700605B1 (fr) * | 1993-01-19 | 1995-03-17 | Cnim | Dispositif d'injection de boues dans un incinérateur de déchets. |
-
1997
- 1997-12-05 FR FR9715419A patent/FR2771946B1/fr not_active Expired - Lifetime
-
1998
- 1998-12-01 PT PT98403008T patent/PT921352E/pt unknown
- 1998-12-01 EP EP19980403008 patent/EP0921352B1/de not_active Expired - Lifetime
- 1998-12-01 ES ES98403008T patent/ES2223112T3/es not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105910112A (zh) * | 2016-04-18 | 2016-08-31 | 娈疯 | 垃圾焚烧厂飞灰综合处理工艺 |
Also Published As
| Publication number | Publication date |
|---|---|
| FR2771946A1 (fr) | 1999-06-11 |
| ES2223112T3 (es) | 2005-02-16 |
| PT921352E (pt) | 2004-10-29 |
| EP0921352A1 (de) | 1999-06-09 |
| HK1021219A1 (en) | 2000-06-02 |
| FR2771946B1 (fr) | 2000-01-28 |
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