EP0966635A1 - Plant and method for incineration of industrial and household waste and sludge - Google Patents

Plant and method for incineration of industrial and household waste and sludge

Info

Publication number
EP0966635A1
EP0966635A1 EP98900534A EP98900534A EP0966635A1 EP 0966635 A1 EP0966635 A1 EP 0966635A1 EP 98900534 A EP98900534 A EP 98900534A EP 98900534 A EP98900534 A EP 98900534A EP 0966635 A1 EP0966635 A1 EP 0966635A1
Authority
EP
European Patent Office
Prior art keywords
waste
sludge
infeed
chute
accordance
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.)
Granted
Application number
EP98900534A
Other languages
German (de)
French (fr)
Other versions
EP0966635B1 (en
Inventor
Siegfried Binner
Gunnar Baltsen
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Babcock and Wilcox Volund AS
Original Assignee
Ansaldo Volund AS
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Ansaldo Volund AS filed Critical Ansaldo Volund AS
Publication of EP0966635A1 publication Critical patent/EP0966635A1/en
Application granted granted Critical
Publication of EP0966635B1 publication Critical patent/EP0966635B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • 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
    • F23G5/44—Details; Accessories
    • F23G5/442—Waste feed arrangements
    • F23G5/444—Waste feed arrangements for solid waste
    • 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
    • F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/001—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals for sludges or waste products from water treatment installations
    • 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
    • F23G2209/00—Specific waste
    • F23G2209/12—Sludge, slurries or mixtures of liquids

Definitions

  • the present invention relates to a plant and method for incineration of industrial and household waste and sludge, comprising a generally vertically directed waste infeed chute, a waste infeed means at the bottom of the chute for advancing the waste in a generally horizontal direction, possibly an infeed sluice and a downstream located combustion chamber, comprising a movable grate system at the bottom, for advancing, drying, igniting, burning, and outburning the waste in the combustion chamber before the slag is conveyed out of the combustion chamber down into the slag chute.
  • the waste infeed chute is generally directed vertically in order that the waste can slide downwards through the chute by gravity, while the waste infeed means in the bottom of the chute removes, advances and feeds the waste lying at the bottom into the combustion chamber, possibly through an infeed sluice.
  • Known waste infeed means at the bottom of the waste infeed chute are e.g. one or more hydraulic pistons, apron feeders, moving grates or actual combustion grates, known e.g. from US patent No. 4,494,469 and DK patent No. 170,493.
  • Characteristic for the known waste infeed means is e.g. that complete filled waste bags and waste of similar bulk size easily and undivided can be fed into the combustion chamber, potentially via an infeed sluice, after having passed down through the waste infeed chute, in which the waste functions as a relatively dense plug, securing only small amounts of combustion air following the waste into the combustion chamber, avoiding propagation of the combustion back into the waste infeed chute.
  • the combustion takes place in the oven chamber at a pressure lower than ambient pressure, e.g. secured by placing an induced draft fan for the flue gas immediately in front of the chimney of the incineration plant.
  • Sludge from waste water cleaning facilities has previously to a great extent been disposed of by spreading on fields as a fertilizer, but stricter environmental rules lead to a demand that sludge of this kind, like many other liquid waste materials, is disposed of by other means, e.g. by combustion.
  • Special sludge ovens for combustion of waste water sludge are known, but will normally require supply of supplementary fuel, e.g. in the form of oil or gas.
  • the sludge When feeding the sludge through the ceiling as well as through the wall of the oven, directly into the waste combustion chamber, the sludge falls through a flue gas stream at a temperature of approximately 1000°C, drying out and carrying away many of the fine-grained sludge particles, so that the content of dust in the flue gas is raised remarkably, which is unconvenient, the boiler after the combustion oven being further smudged and the flue gas cleaning demand being increased.
  • an incineration plant as mentioned in the introduction, by providing the waste infeed chute or sluice with at least one infeed tube for adding sludge to the waste in the chute or sluice, and at least one pressure-feed applicance for feeding the sludge through the at least one infeed tube into the waste.
  • the sludge is fed into the waste infeed chute or infeed sluice, at a position in which there exists a pressure lower than ambient pressure, when the plant is working so that unhygienic dust is sucked into the cold waste and the odour materials are sucked into the combustion chamber, whereby they are burned and removed.
  • the sludge is fed into the combustion chamber in such a way that the development of dust during the combustion process is minimized and the infeed of waste is still performed optimally with respect to combustion, as normally, without any cumbersome, expensive and unhygienic comminution of the waste.
  • the infeed is performed close to the bottom part of the waste infeed chute or in the infeed sluice, so that generally all of the time waste is present in the infeed chute or infeed sluice at the level of the mouth of the infeed tube.
  • the sludge By providing the infeed tube for sludge in the wall of the waste infeed chute facing the combustion chamber or in the ceiling of the infeed sluice, the sludge will always be positioned on top of the waste being fed into the waste combustion chamber and thus being dried out immediately when entering the combustion chamber.
  • the infeed tube or tubes are preferably connected to a pipeline for the supply of sludge from a pressure-feed applicance upstream connected to a silo for temporary storage of sludge.
  • the infeed of sludge can be performed almost hermetically closed with respect to the surroundings.
  • the pipeline for supply of sludge may be provided with one or more ring nozzles, for lubricating the inner wall of the pipeline with e.g. a polymer for reduction of the sliding friction between sludge and pipeline.
  • the sludge to be incinerated in the plant in accordance with the invention may be selected from the group consisting of sludge from waste water cleaning, crude oil sludge, petrochemical waste products, animal sludge, liquid waste, slurry and liquid manure or mixtures thereof, possibly with admixture of materials selected from the group consisting of grate screanings, boiler ash, filter ash, flue gas cleaning products, other waste products from waste incineration plants, shredded waste, plastic waste, car fluff, and stabilizers reducing dust and/or vapour generation and/or unwanted chemical reactions in the combustion chamber.
  • the sludge is supplied to the incineration plant via a hermetically closed supply system.
  • the infeed quantity of the sludge can be used as one parameter for controlling the burning of waste in the combustion chamber.
  • the method preferably comprises pressure-feeding of sludge of varying composition, possibly with admixture of further material to be disposed of or material providing stabilization of the sludge mixture.
  • Fig. 1 shows an incineration plant comprising infeed tubes for adding sludge to the waste in accordance with the present invention
  • Fig. 2 shows an arrangement comprising four infeed tubes, via a manifold connected to a pipeline for supply of sludge, and
  • Fig. 3 shows a rough outline of a plant comprising a waste incineration plant and corresponding pipeline for sludge and a pressure-feed appliance provided to transport the sludge and a silo for temporary storage of sludge.
  • the incineration plant shown in Fig. 1 comprises a waste infeed chute 1 for industrial and household waste and a grate system 2 for advancing the waste through the inlet to the combustion chamber and for advancing the waste in the combustion chamber 3, positioned downstream of the chute 1.
  • the waste infeed chute 1 comprises an infeed tube 4 for supply of sludge.
  • the infeed tube is placed close to the bottom part of the waste infeed chute 1 and in the wall in the waste infeed chute 1 facing the combustion chamber 3.
  • the infeed tube 4 for supply of sludge is, as shown in the drawing, positioned to debouch in a downwardly slanted angle into the waste infeed chute 1.
  • Fig. 2 shows how four infeed tubes 4 are connected to a pipeline 5 for supply of sludge via a manifold 6, intended to provide a uniform distribution of the added sludge across the four infeed tubes 4, the sludge being equally distributed across the feeding direction for the grate system 2 in the waste combustion chamber 3.
  • Fig. 3 shows how sludge can be supplied from a storage silo 7 for temporary storage of the sludge, forward to the infeed tube 4 in a hermetically closed system.
  • a pressure-feed appliance 8 is provided close to the silo 7, and a pipeline 5 is connected between the pressure-feed appliance 8 and the infeed tube 4, the pipeline 5 potentially comprising a ring nozzle 9, for lubricating the inner wall of the pipeline 5 with e.g. a polymer for reduction of the sliding friction between sludge and pipeline 5.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Incineration Of Waste (AREA)

Abstract

In an incineration plant for industrial and household waste and sludge, comprising a generally vertically directed waste infeed chute (1), a waste infeed means at the bottom of the chute (1) for advancing the waste in a generally horizontal direction, possibly an infeed sluice and a downstream located combustion chamber (3), the waste infeed chute (1) or sluice is provided with at least one infeed tube (4) for adding sludge to the waste in the chute (1) or sluice and at least one pressure-feed appliance (8) for feeding the sludge through the at least one infeed tube (4). The sludge is preferably supplied to the plant via a hermetically closed supply system. The invention provides a reduction of odour problems and optimization of hygienic working conditions.

Description

PLANT AND METHOD FOR INCINERATION OF INDUSTRIAL AND HOUSEHOLD WASTE AND SLUDGE
The present invention relates to a plant and method for incineration of industrial and household waste and sludge, comprising a generally vertically directed waste infeed chute, a waste infeed means at the bottom of the chute for advancing the waste in a generally horizontal direction, possibly an infeed sluice and a downstream located combustion chamber, comprising a movable grate system at the bottom, for advancing, drying, igniting, burning, and outburning the waste in the combustion chamber before the slag is conveyed out of the combustion chamber down into the slag chute.
The waste infeed chute is generally directed vertically in order that the waste can slide downwards through the chute by gravity, while the waste infeed means in the bottom of the chute removes, advances and feeds the waste lying at the bottom into the combustion chamber, possibly through an infeed sluice.
Known waste infeed means at the bottom of the waste infeed chute are e.g. one or more hydraulic pistons, apron feeders, moving grates or actual combustion grates, known e.g. from US patent No. 4,494,469 and DK patent No. 170,493. Characteristic for the known waste infeed means is e.g. that complete filled waste bags and waste of similar bulk size easily and undivided can be fed into the combustion chamber, potentially via an infeed sluice, after having passed down through the waste infeed chute, in which the waste functions as a relatively dense plug, securing only small amounts of combustion air following the waste into the combustion chamber, avoiding propagation of the combustion back into the waste infeed chute.
In the oven system, to which the invention relates, the combustion takes place in the oven chamber at a pressure lower than ambient pressure, e.g. secured by placing an induced draft fan for the flue gas immediately in front of the chimney of the incineration plant. Sludge from waste water cleaning facilities has previously to a great extent been disposed of by spreading on fields as a fertilizer, but stricter environmental rules lead to a demand that sludge of this kind, like many other liquid waste materials, is disposed of by other means, e.g. by combustion.
Special sludge ovens for combustion of waste water sludge are known, but will normally require supply of supplementary fuel, e.g. in the form of oil or gas.
Combustion of waste water sludge in combination with other types of waste in a waste incineration plant is known, in which the sludge has continuously been fed in directly in the hot combustion chamber through the ceiling thereof, or by infeeding via the waste infeed chute on top of the chute. The former of these infeed methods is relatively cumbersome due to infeed sluices, flaps or nozzles in the very hot ceiling of the oven, and both infeed methods will inevitably lead to odour problems and unhygienic working conditions in connection with the infeed of the sludge.
From US-patent No. 4,724,776 it is known to forcedly feed waste and sludge through the wall of the oven directly into the hot combustion chamber using a motorized charging screw or a motorized conveyor, so that waste and sludge falls down on a combustion grate placed at the bottom or higher up in the combustion chamber. The object is stated to be the burning of waste and sludge by a method, which aims at a concurrent good gas combustion before the flue gas is delivered to the chimney. Nothing is mentioned about seeking to eliminate the odour and hygienic problems and the complete oven system described is furthermore an overpressure system, not only giving odour and hygienic problems but also dust and escape of poorly combusted flue gases to the surroundings or the working environment in which the personnnel of the plant is working. Furthermore, the infeed screw means that the waste has to be subjected to a cumbersome, expensive and unhygienic disintegration before feeding to the combustion chamber.
When feeding the sludge through the ceiling as well as through the wall of the oven, directly into the waste combustion chamber, the sludge falls through a flue gas stream at a temperature of approximately 1000°C, drying out and carrying away many of the fine-grained sludge particles, so that the content of dust in the flue gas is raised remarkably, which is unconvenient, the boiler after the combustion oven being further smudged and the flue gas cleaning demand being increased.
It is the object of the present invention to provide a waste incineration plant as mentioned in the introduction, in which the above-mentioned odour problems are minimized and the hygienic working conditions are optimized.
This is achieved by an incineration plant as mentioned in the introduction, by providing the waste infeed chute or sluice with at least one infeed tube for adding sludge to the waste in the chute or sluice, and at least one pressure-feed applicance for feeding the sludge through the at least one infeed tube into the waste.
Hereby it is achieved that the sludge is fed into the waste infeed chute or infeed sluice, at a position in which there exists a pressure lower than ambient pressure, when the plant is working so that unhygienic dust is sucked into the cold waste and the odour materials are sucked into the combustion chamber, whereby they are burned and removed. At the same time the sludge is fed into the combustion chamber in such a way that the development of dust during the combustion process is minimized and the infeed of waste is still performed optimally with respect to combustion, as normally, without any cumbersome, expensive and unhygienic comminution of the waste.
Preferably the infeed is performed close to the bottom part of the waste infeed chute or in the infeed sluice, so that generally all of the time waste is present in the infeed chute or infeed sluice at the level of the mouth of the infeed tube.
By providing the infeed tube for sludge in the wall of the waste infeed chute facing the combustion chamber or in the ceiling of the infeed sluice, the sludge will always be positioned on top of the waste being fed into the waste combustion chamber and thus being dried out immediately when entering the combustion chamber. Preferably, there are several infeed tubes evenly distributed over the width of the waste infeed chute or sluice, respectively, whereby the sludge can be distributed evenly over the waste.
By having the infeed tube or tubes debouching in a downwardly slanted angle into the waste infeed chute or forwardly slanted into the sluice, respectively, the sludge will be dragged with the waste onwards through the chute or sluice, whereby possible clogging problems at the mouth of the infeed tube or tubes are avoided.
In order to avoid odour problems the infeed tube or tubes are preferably connected to a pipeline for the supply of sludge from a pressure-feed applicance upstream connected to a silo for temporary storage of sludge. Thus, the infeed of sludge can be performed almost hermetically closed with respect to the surroundings.
In order to make it possible to transport sludge over greater distances in connection with sludge with a relatively high content of dry matter, e.g. 30-40%, the pipeline for supply of sludge may be provided with one or more ring nozzles, for lubricating the inner wall of the pipeline with e.g. a polymer for reduction of the sliding friction between sludge and pipeline.
The sludge to be incinerated in the plant in accordance with the invention may be selected from the group consisting of sludge from waste water cleaning, crude oil sludge, petrochemical waste products, animal sludge, liquid waste, slurry and liquid manure or mixtures thereof, possibly with admixture of materials selected from the group consisting of grate screanings, boiler ash, filter ash, flue gas cleaning products, other waste products from waste incineration plants, shredded waste, plastic waste, car fluff, and stabilizers reducing dust and/or vapour generation and/or unwanted chemical reactions in the combustion chamber.
As can be seen, many different waste products can be disposed of in this way. By a suitable composition of the sludge and the admixed materials, it is possible to achieve a stabilization with respect to dust, vapour, chemical reactivity, viscosity of the mixture, etc. By providing several separate pressure-feed appliances and pipelines for supply of different mixtures of sludge etc., the pipelines debouching in separate infeed tubes or in common infeed tubes via a manifold, it is possible to control the infeed speed for the different mixtures, thereby controlling the combustion in the combustion chamber. The control can be relatively fast reacting as the infeed of the sludge is placed very close to the combustion process in the combustion chamber.
It is a further object of the invention to provide a method for incinerating industrial and household waste and sludge in an incineration plant of the above-mentioned type, in which the above-mentioned odour problems are minimized and the hygienic working conditions are optimized.
This is achieved by a method comprising pressure-feeding the sludge into the waste immediately in front of the infeed means.
Preferably the sludge is supplied to the incineration plant via a hermetically closed supply system.
The infeed quantity of the sludge can be used as one parameter for controlling the burning of waste in the combustion chamber. The method preferably comprises pressure-feeding of sludge of varying composition, possibly with admixture of further material to be disposed of or material providing stabilization of the sludge mixture.
The advantages of the method in accordance with the invention correspond to the advantages described above in connection with the incineration plant in accordance with the invention.
In the following detailed portion of the present description, the present invention will be explained in more detail with reference to the exemplary embodiments of an incineration plant according to the invention shown in the drawings, in which
Fig. 1 shows an incineration plant comprising infeed tubes for adding sludge to the waste in accordance with the present invention, Fig. 2 shows an arrangement comprising four infeed tubes, via a manifold connected to a pipeline for supply of sludge, and
Fig. 3 shows a rough outline of a plant comprising a waste incineration plant and corresponding pipeline for sludge and a pressure-feed appliance provided to transport the sludge and a silo for temporary storage of sludge.
The incineration plant shown in Fig. 1 comprises a waste infeed chute 1 for industrial and household waste and a grate system 2 for advancing the waste through the inlet to the combustion chamber and for advancing the waste in the combustion chamber 3, positioned downstream of the chute 1. The waste infeed chute 1 comprises an infeed tube 4 for supply of sludge. In the embodiment shown, the infeed tube is placed close to the bottom part of the waste infeed chute 1 and in the wall in the waste infeed chute 1 facing the combustion chamber 3.
Thus, sludge being supplied to the shown waste incineration plant through the infeed tube 4 will end up lying on top of the industrial and household waste on the grate system 2 in the combustion chamber 3.
In order to avoid possible clogging problems at the infeed of sludge into the waste infeed chute 1 , the infeed tube 4 for supply of sludge is, as shown in the drawing, positioned to debouch in a downwardly slanted angle into the waste infeed chute 1.
Fig. 2 shows how four infeed tubes 4 are connected to a pipeline 5 for supply of sludge via a manifold 6, intended to provide a uniform distribution of the added sludge across the four infeed tubes 4, the sludge being equally distributed across the feeding direction for the grate system 2 in the waste combustion chamber 3.
Fig. 3 shows how sludge can be supplied from a storage silo 7 for temporary storage of the sludge, forward to the infeed tube 4 in a hermetically closed system. Between the silo 7 and the infeed tube 4, a pressure-feed appliance 8 is provided close to the silo 7, and a pipeline 5 is connected between the pressure-feed appliance 8 and the infeed tube 4, the pipeline 5 potentially comprising a ring nozzle 9, for lubricating the inner wall of the pipeline 5 with e.g. a polymer for reduction of the sliding friction between sludge and pipeline 5.

Claims

PATENT CLAIMS
1. An incineration plant for industrial and household waste and sludge, comprising a generally vertically directed waste infeed chute (1), a waste infeed means at the bottom of the chute (1) for advancing the waste in a generally horizontal direction, possibly an infeed sluice and a downstream located combustion chamber (3), comprising a movable grate system at the bottom, for advancing, drying, igniting, burning, and outburning the waste in the combustion chamber (3), characterized by the waste infeed chute (1) or sluice being provided with at least one infeed tube (4) for adding sludge to the waste in the chute (1) or sluice and at least one pressure-feed appliance (8) for feeding the sludge through the at least one infeed tube (4).
2. Incineration plant in accordance with claim 1, characterized by the at least one infeed tube (4) being provided close to the bottom part of the waste infeed chute (1) or in the infeed sluice.
3. Incineration plant in accordance with claim 1or2, characterized by the at least one infeed tube (4) being provided in the wall of the waste infeed chute (1) facing the combustion chamber (3) or in the ceiling of the infeed sluice.
4. Incineration plant in accordance with any of the preceding claims, characterized by comprising several infeed tubes (4) evenly distributed over the width of the waste infeed chute (1) or sluice, respectively.
5. Incineration plant in accordance with any of the preceding claims, ch a racterized by the infeed tube or tubes (4) debouching in a downwardly slanted angle into the waste infeed chute (1) or forwardly slanted into the sluice, respectively.
6. Incineration plant in accordance with any of the preceding claims, characterized by the infeed tube or tubes (4) being connected to a pipeline (5) for the supply of sludge from a pressure-feed appliance (8), upstream connected to a silo (7) for temporary storage of sludge.
7. Incineration plant in accordance with claim 6, characterized by the pipeline (5) for the supply of sludge comprising one or more ring nozzles (9), for lubricating the inner wall of the pipeline (5) with e.g. a polymer for reduction of the sliding friction between sludge and pipeline (5).
8. Incineration plant in accordance with any of the preceding claims, ch a racterized by the sludge being selected from the group consisting of sludge from waste water cleaning, crude oil sludge, petrochemical waste products, animal sludge, liquid waste, slurry, and liquid manure, or mixtures thereof, possibly with admixture of materials selected from the group consisting of grate screenings, boiler ash, filter ash, flue gas cleaning products, other waste products from waste incineration plants, shredded waste, plastic waste, car fluff, and stabilizers, reducing dust and/or vapour generation and/or unwanted chemical reactions in the combustion chamber (3).
9. Incineration plant in accordance with claim 8, ch a ra cte rize d by comprising several separate pressure-feed appliances (8) and pipelines (5) for supply of different mixtures of sludge etc., the pipelines (5) debouching in separate infeed tubes (4) or in common infeed tubes (4) via a manifold.
10. Method of incinerating industrial and household waste and sludge in an incineration plant in accordance with the preamble of claim 1, c h a ra ct e ri zed by comprising pressure-feeding the sludge into the waste immediately in front of the infeed means.
11. Method in accordance with claim 10, characterized by supplying the sludge to the plant via a hermetically closed supply system.
12. Method in accordance with claim 10 or 11, characterized by using the infeed quantity of the sludge as one parameter for controlling the burning of waste in the combustion chamber (3).
13. Method in accordance with any of the claims 10-12, characterized by comprising pressure-feeding of sludge of varying composition possibly with admixture of further material to be disposed of or material providing stabilization of the sludge mixture.
AMENDED CLAIMS
[received by the International Bureau on 20 July 1998 (20.07.98); original claims 1-4 amended; emaining claims unchanged (2 pages)]
1. Method of incinerating industrial and household waste and sludge in an incineration plant comprising a) feeding the industrial and household waste through a generally vertical directed waste infeed chute (1), comprising means at the bottom of the chute
(1) for advancing the waste in a generally horizontal direction, possibly an infeed sluice, and a downstream located combustion chamber (3), comprising a movable grate system at the bottom, for advancing, drying, igniting, burning and outburning the waste in the combustion chamber (3), b) adding the sludge to be incinerated through at least one infeed tube (4), debouching into the infeed chute (1) or sluice, the infeed tube or tubes (4) being connected to a pipeline (5) for the supply of sludge from a pressure feed appliance (8) upstream connected to a silo for temporary storage of sludge, characterized by further comprising: c) before adding the sludge, further materials to be disposed of is added to the sludge.
2. Method in accordance with claim 1, c h a ra c t e r i z e d by admixed materials being selected from the group consisting of: grate screenings, boiler ash, filter ash, flue gas cleaning products, other waste products from waste incineration plants, shredded waste, plastic waste, car fluff, and stabilizers reducing dust and/or vapour generation and/or unwanted chemical reactions in the combustion chamber (3), or mixtures thereof.
3. Method in accordance with any of the preceding claims, c h a ra ct e rized by the sludge being selected from the group consisting of: sludge from waste water cleaning,
AMENDED SHEET (ARTICLE 19] crude oil sludge, petrochemical waste products, animal sludge, liquid waste, slurry, and liquid manure, or mixtures thereof.
4. Method in accordance with any of the preceding claims, c h a r a c t e r- i z e d by d) lubricating the inner wall of the pipeline (5) for the supply of sludge using one or more ring nozzles (8) for adding the lubricating medium, e.g. a polymer, for reduction of the sliding friction between sludge and pipeline (5).
EP98900534A 1997-03-19 1998-01-27 Plant and method for incineration of industrial and household waste and sludge Expired - Lifetime EP0966635B1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DK199700311A DK31197A (en) 1997-03-19 1997-03-19 Waste incineration plant for industrial and household waste and sewage sludge
DK31197 1997-03-19
PCT/DK1998/000028 WO1998041795A1 (en) 1997-03-19 1998-01-27 Plant and method for incineration of industrial and household waste and sludge

Publications (2)

Publication Number Publication Date
EP0966635A1 true EP0966635A1 (en) 1999-12-29
EP0966635B1 EP0966635B1 (en) 2001-09-26

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Family Applications (1)

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EP98900534A Expired - Lifetime EP0966635B1 (en) 1997-03-19 1998-01-27 Plant and method for incineration of industrial and household waste and sludge

Country Status (8)

Country Link
EP (1) EP0966635B1 (en)
JP (1) JP2001516435A (en)
KR (1) KR100527243B1 (en)
AU (1) AU5550198A (en)
DE (1) DE69801812T2 (en)
DK (2) DK31197A (en)
HK (1) HK1024736A1 (en)
WO (1) WO1998041795A1 (en)

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JP4509695B2 (en) * 2004-07-28 2010-07-21 月島環境エンジニアリング株式会社 Waste liquid incineration treatment method
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CN106439843B (en) * 2016-09-08 2019-03-12 南京中特化工动力设备有限公司 Petrochemical industry not recovering discarded material harmless treatment process
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KR100527243B1 (en) 2005-11-09
HK1024736A1 (en) 2000-10-20
EP0966635B1 (en) 2001-09-26
JP2001516435A (en) 2001-09-25
AU5550198A (en) 1998-10-12
WO1998041795A1 (en) 1998-09-24
KR20000076315A (en) 2000-12-26
DK0966635T3 (en) 2002-01-28
DK31197A (en) 1998-09-20
DE69801812D1 (en) 2001-10-31
DE69801812T2 (en) 2002-04-11

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