Method and furnace for incinerating organic matter derived from the treatment of industrial or agricultural waste or wastewater, such as sludge

Patent metadata

Field	Value
Publication number	US-12467626-B2
Application number	US-202017641082-A
Country	US
Kind code	B2
Filing date	Sep 11, 2020
Priority date	Sep 13, 2019
Publication date	Nov 11, 2025
Grant date	Nov 11, 2025

Abstract

A method for incinerating organic matter derived from the treatment of wastewater, or of industrial or agricultural waste, such as sludge and notably treatment plant sludge, is in a fluidized-bed incineration furnace, the furnace including a chamber in the lower part of which there is a bed of particles, preferentially sand, constituting a fluidization zone, in which fluidization zone the organic matter is introduced as fuel whilst air is injected as oxidizer into the bed of sand from a wind box through a fluidization dome surmounting the box. The air passes through passages made in the fluidization dome, and the furnace is configured to treat a nominal value of volume of organic matter to be treated. The method includes a step of adjusting the volume of the fluidization zone as a function of the volume of organic matter to be treated in which, when the volume of organic matter to be treated is lower than the nominal value, the volume of the fluidization zone is reduced from an initial volume to a reduced volume, and the incoming air flow is reduced by closing air passages so only the passages opening into the thus reduced fluidization zone are left active.

First claim

The invention claimed is:

1 . A method for incinerating organic matter trapped in a mineral and/or liquid matrix issued from the treatment of waste water, industrial or agricultural waste, in a fluidised bed incineration furnace configured to treat a volume of the organic matter equal to a nominal value, the furnace including an enclosure in a lower part thereof, the enclosure including a particle bed constituting a fluidisation zone, the method comprising:
introducing the organic matter as fuel into the fluidisation zone while injecting air as an oxidant into the particle bed from a wind box through a fluidisation dome on top of the wind box, the air passing through passages provided in the fluidisation dome; and adjusting a volume of the fluidisation zone and a flow rate of the air coming into the fluidisation zone as a function of a volume of the organic matter to be treated, in which, when the volume of the organic matter to be treated is lower than the nominal value, reducing the volume of the fluidisation zone from an initial volume to a reduced volume, and reducing the flow rate of the air by sealing a portion of the passages so as to leave active only the passages opening into the thus reduced volume fluidisation zone, wherein adjusting the volume of the fluidisation zone comprises installing an insert in the form of a sleeve having a shape complementary to the portion of the enclosure delimiting the fluidisation zone and extending against the portion of the enclosure delimiting the fluidisation zone from the fluidisation dome over a height lower than or equal to a height of the fluidisation zone.

2 . The method according to claim 1 , wherein the adjustment of the volume of the fluidisation zone is a temporary volume reduction.

3 . The method according to claim 2 , further comprising:
a complementary volume adjustment step in which, as soon as the volume of the organic matter to be treated approaches or reaches the nominal value, restoring the volume of the fluidization zone to the initial volume and restoring the flow rate of the air to an initial flow rate by freeing the portion of the passages that were sealed.

4 . The method according to claim 1 , wherein the enclosure at the fluidisation zone has a frustoconical shape with a side extending at an angle of between 0° and 45° with respect to a vertical, the sleeve having a frustoconical shape with:
(a) an external diameter Dext at a given height above the fluidisation dome equal to a diameter of the frustoconical shape of the enclosure at the given height, and
(b) an internal diameter Dint at a given height above the fluidisation dome equal to an external diameter of the added cone frustum frustoconical shape of the enclosure at the given height minus two times a thickness A of the sleeve.

5 . The method according to claim 4 , wherein a height of the sleeve is equal to the sum of a height of the particle bed at rest and a projection height of particles in the particle bed when fluidised, and wherein the height of the particle bed is between 0.3 m and 1.5 m and the projection height of particles is between 0 and 2 m.

6 . The method according to claim 1 , further comprising:
installing the sleeve in the furnace such that the sleeve masks a portion of the passages in the fluidisation dome at a periphery thereof under a thickness of the sleeve.

7 . The method according to claim 1 , further comprising:
dismantling the insert such that the volume of the fluidisation zone is restored to the initial volume; and treating in the furnace a volume of the organic matter equal to the nominal value, wherein the initial volume of the fluidisation zone is the volume of the fluidisation zone suitable for treating a volume of the organic matter equal to the nominal value.

8 . A method for incinerating organic matter trapped in a mineral and/or liquid matrix issued from the treatment of waste water, industrial or agricultural waste, in a fluidised bed incineration furnace configured to treat a volume of the organic matter equal to a nominal value, the furnace including an enclosure in a lower part thereof, the enclosure including a particle bed constituting a fluidisation zone, the method comprising:
introducing the organic matter as fuel into the fluidisation zone while injecting air as an oxidant into the particle bed from a wind box through a fluidisation dome on top of the wind box, the air passing through passages provided in the fluidisation dome; adjusting a volume of the fluidisation zone and a flow rate of the air coming into the fluidisation zone as a function of a volume of the organic matter to be treated, in which, when the volume of the organic matter to be treated is lower than the nominal value, reducing the volume of the fluidisation zone from an initial volume to a reduced volume, and reducing the flow rate of the air by sealing a portion of the passages so as to leave active only the passages opening into the thus reduced volume fluidisation zone; and reducing the volume of the enclosure of the furnace above the fluidisation zone by installing an insert extending over an entire height of the furnace.

9 . A furnace for incinerating organic matter from treatment of waste water, industrial or agricultural waste, the furnace being configured to treat a volume of the organic matter equal to a nominal value and comprising an enclosure in a lower part thereof in which there is a fluidised particle bed, the furnace further comprising, at least from bottom to top:
a wind box having an upper part which supports a fluidisation dome having passages through which air coming from the wind box is distributed into a fluidisation zone corresponding to the fluidised particle bed; at least one organic matter feed and at least a supplemental fuel injector configured to feed supplemental fuel to the fluidisation zone; an expansion and post-combustion zone above the fluidisation zone; an upper vault on top of the expansion and post-combustion zone, the upper vault including a discharge pipe for combustion products; and when a volume of the organic matter to be treated is lower than the nominal value, an insert in the form of a sleeve having a shape complementary to a portion of the enclosure delimiting the fluidisation zone and extending from the fluidisation dome against the portion of the enclosure delimiting the fluidisation zone such that a volume of the fluidisation zone is reduced from an initial volume to a reduced volume and a portion of the passages in the fluidisation dome are sealed leaving active only the passages opening into the reduced volume fluidisation zone and a flow rate of the air through the passages is reduced.

10 . The furnace according to claim 9 , wherein a thickness A of the insert is chosen to define the volume of the reduced volume fluidisation zone and a reduced cross-sectional area of the fluidisation dome, the thickness A of the insert being proportional to the reduction in the flow rate of the air through the passages.

11 . The furnace according to claim 10 , wherein a desired flow rate of the air through the passages is defined according to the following formulas (1) and (2):
(1) Φv′=Φb′×S×MV×Coef1×Coef2, where:
Φv′: a fluidisation air flow rate in kg/h,
Φb′: an organic matter flow rate in kg/h,
S: a fraction of dry matter in the organic matter in %,
MV: a fraction of the organic matter in the dry fraction in %,
Coef1: a stoichiometric ratio corresponding to an amount of the air in kg/h to combust 1 kg of the organic matter, ranging from 5 to 10 depending on the type of the organic matter,
Coef2: excess air desired to ensure complete combustion of the organic matter between 1.01 and 1

Assignees

• Suez Int

Inventors

• Bourdais Jean-Louis

Classifications

• F23G2203/50

  Fluidised bed furnace · CPC title

• F23G7/10

  of field or garden waste {or biomasses} · CPC title

• F23G7/001

  for sludges or waste products from water treatment installations (F23G5/008 takes precedence) · CPC title

• Y02W10/40

  Valorisation of by-products of wastewater, sewage or sludge processing · CPC title

• F23G2209/12

  Sludge, slurries or mixtures of liquids · CPC title