GB2188562A - Combustion gas depurator mechanism - Google Patents

Combustion gas depurator mechanism Download PDF

Info

Publication number
GB2188562A
GB2188562A GB08701973A GB8701973A GB2188562A GB 2188562 A GB2188562 A GB 2188562A GB 08701973 A GB08701973 A GB 08701973A GB 8701973 A GB8701973 A GB 8701973A GB 2188562 A GB2188562 A GB 2188562A
Authority
GB
United Kingdom
Prior art keywords
liquid
container
depurator
expansion chamber
acombustion
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.)
Withdrawn
Application number
GB08701973A
Other versions
GB8701973D0 (en
Inventor
Nieto Domingo Diez
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.)
DEPURATOR SA
Original Assignee
DEPURATOR SA
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 DEPURATOR SA filed Critical DEPURATOR SA
Publication of GB8701973D0 publication Critical patent/GB8701973D0/en
Publication of GB2188562A publication Critical patent/GB2188562A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/48Sulfur compounds
    • B01D53/50Sulfur oxides

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Treating Waste Gases (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Chimneys And Flues (AREA)

Abstract

The depurator 4 is arranged at the fume release chimney exit, after a known solid particle release mechanism 2, and has the purpose of removing sulphurous anhydride from the combustion gases. The fumes, already free from solid particles, enter an expansion chamber provided with atomizers 5 which eject under pressure a liquid wherein the sulphurous anhydride is fixed, the liquid being aspired from a container 7 through an electropump group 6. Under gravity, the liquid falls from the expansion chamber in order to be re-used. Inside the container 7 a stirrer 10 homogenizes the mixture. After neutralization the liquid is drained to the sewer through a drainage 11. The electropump group 6 may function automatically with a boiler burner. <IMAGE>

Description

SPECIFICATION Combustion gas depurator mechanism The present invention, as stated in the title of these specifications, comprises a combustion gas depurator mechanism.
Among the atmospheric contaminants produced bythe combustion not only of carbons, but also of petroleum derivatives (gas-oil and fuel-oil), which are used in thermic central heating, factories, etc., one of the most harmful, if not the most dangerous among them, is the sulphurous anhydride.
Considering the fact that solid and liquid fuels contain different proportions of sulphur, in the burning thereof the production of the already mentioned sulphurous anhydride can not be avoided.
The danger of this colourless gas is not the dirt which the different solid particles suspended in the fumes may produce, but the causticity thereof, which attacks metals and principally, this being most serious, the respiratory tract, since when itcontacts humidity, it is transformed into sulphurous acid, which is highly caustic.
According to this invention, a combustion gas depurator mechanism has being conceived to obtain the complete release of the produced sulphurous anhydride.
The complete release of every solid particle being produced in any fuel combustion, is performed in a known mechanism, by means of which thefumes coming out the chimney enter an expansion chamber, colliding in the vertical thereof with an inverted cone which makes the fumes distribute by its lateral portions and due to gravity the solid particles settle atthe lower portion of this solid particle depurator. The fumes continue ascending and pass along invertedtruncatedconestoreach another similar one wherein the total release of said solid particles is completed.Above these elements, there is a water circuit provided with pulverizers for the under-pressure wash of all the elements, the water emerging through a drainage provided atthe lower portion of the depuratortowards a hydraulic siphon for the coming out into the sewer.
According to the invention, the fumes, which are already free from solid particles, enter an expansion chamberwherein two pulverizers are provided, said pulverizers ejecting under pressure the sulphurous gas fixing liquid, which, at close contact with the combustion gases, release the 802 orsulphurous anhydride.
The liquid is aspired from a container wherein a small stirrer is provided, so that the liquid is perfectly mixed due to the differences in density, sincethe liquid flowing along the pulverizers is conducted into this containerforthe re-use thereof. The aspiration is performed by a small electropump group, which impells it towards the pulverization chamber, wherein it is closely mixed with the combustion gases, returning to the container due to the gravity.
The electropump group functions automatically with the heating boiler, thermic central, etc. burner, since, as it is known, in every heating system the burner does notworkcontinuously,saidworking stopping for a third of the time approximately.
Once the liquid has been neutralized, this one is conducted towards the sewer through a drainage provided atthe bottom ofthe container.
The mixture of the catalytic liquid used is related to the sulphide rate of burned products and due to this, the maximal authorized sulphur contents, legaly established, must be taken into account.
Forthe help of a better understanding ofthese specifications and as a part thereof, a drawing sheet is attached, in the single drawing of which it has been represented, with an illustrative but non-limitative character, a section in vertical position of the combustion gas depurator mechanism, object of this invention, arranged to the exit conduct of a mechanism known in itself, wherein the solid particles produced in any fuel combustion are released.
Referring to the numeration indicated in this figure, it can be seen howthe chimneyforthe release ofthefumes produced by fuel combustion, in general referred to with No. 1 and partially representedinthefigure, has a mechanism arranged, which, also is in general referred to with No. 2, wherein the solid particles produced bythe combustion are released, said mechanism being used nowadays and wherein only said solid particles are pulled by the water flowing through pulverizers provided at the upper portion thereof.
At the exit ofthe depurator 2 of solid particles, a conduction 3 is arranged for the exit of combustion fumes, already free from solid particles and in the opening of which the mechanism object of this application, in general referred to with No. 4, is arranged.
The depurator mechanism 4 presented in the invention, is arranged in orderto releasethe combustion gases, specifically the sulphurous anhydride produced, which, as said hereinabove, is the most dangerous and contaminant, since it damages the airways and when it contacts humidity itistransformed intosulphurousacid,whichis highly caustic.
The depurator mechanism 4 comprises a container wherein the fumes, already free from solid particles, expand and closely mix with the liquid being ejected under pressure by the pulverizers 5.
The sulphurous gas fixing liquid is aspired by the electro-pump group 6 from a container 7, and it is conducted from the depurator 4 bottom 8 again through the pipe 9 towards the very container 7, to be re-used again.
On the basis of density differences of the pure liquid which is contained in the container 7 and of that one which enters said container through the conduct 9, which constitutes the catalyzing liquid, a small stirrer loins provided inside the container 7, with which the mixture becomes homogeneous.
Once the liquid contained in the container7 has been completely neutralized, it is drained towards the sewerthrough the drainage 11.

Claims (3)

1. Acombustion gas depurator arranged ata fume release chimney exit, after a solid particle removal device, and having the purpose of removing sulphurous anhydride from combustion gases, characterised in that the fumes, already free from solid particles, enter an expansion chamber provided with pulverizers which eject under pressure liquid wherein the sulphurous anhydride is fixed, the liquid being aspired from the bottom region of a containerthrough an electropump group up to the expansion chamber, wherein it falls due to gravity in orderto be re-used; inside the container there being optionally a stirrer so as to homogenize the mixture,which, after neutralization, is drained through a drainage provided atthe container bottom.
2. Acombustion gas depurator as claimed in claim 1, in which the electropump group functions automaticallywith a boiler burner.
3. Acombustion gas depurator mechanism substantially as described with reference to, and as shown in, the accompanying drawing.
GB08701973A 1986-03-03 1987-01-29 Combustion gas depurator mechanism Withdrawn GB2188562A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
ES1986292673U ES292673Y (en) 1986-03-03 1986-03-03 COMBUSTION GAS TREATMENT DEVICE

Publications (2)

Publication Number Publication Date
GB8701973D0 GB8701973D0 (en) 1987-03-04
GB2188562A true GB2188562A (en) 1987-10-07

Family

ID=8440068

Family Applications (1)

Application Number Title Priority Date Filing Date
GB08701973A Withdrawn GB2188562A (en) 1986-03-03 1987-01-29 Combustion gas depurator mechanism

Country Status (6)

Country Link
JP (1) JPS62210034A (en)
DE (1) DE3705685A1 (en)
ES (1) ES292673Y (en)
FR (1) FR2595055A1 (en)
GB (1) GB2188562A (en)
IT (1) IT1203490B (en)

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB794060A (en) * 1954-11-09 1958-04-30 Bayer Ag Method of and apparatus for scrubbing gases
GB920203A (en) * 1958-04-10 1963-03-06 Ruhrchemie Ag Method and apparatus for contacting gas with a liquid
US3907523A (en) * 1972-12-26 1975-09-23 Krebs Engineers Method for removing SO{HD 2 {B from gases
US3928005A (en) * 1974-02-19 1975-12-23 Fuller Co Method and apparatus for treating gaseous pollutants in a gas stream
US4040803A (en) * 1975-02-11 1977-08-09 Mitsubishi Jukogyo Kabushiki Kaisha Wet waste flue gas desulfurizing process using lime as absorbent
EP0017348A1 (en) * 1979-03-06 1980-10-15 Peabody Process Systems, Inc. Flue gas scrubbing process using fly ash alkali
EP0024551A2 (en) * 1979-07-27 1981-03-11 The M. W. Kellogg Company Process and apparatus for removing sulfur dioxide from industrial waste gas
US4323371A (en) * 1979-06-15 1982-04-06 Oy Wartsila Ab Method and arrangement for treating gaseous combustion products

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2755252A1 (en) * 1977-12-12 1979-07-05 Babcock Bsh Ag METHOD OF REMOVING SULFUR DIOXIDE FROM EXHAUST GASES TO CREATE PLASTER

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB794060A (en) * 1954-11-09 1958-04-30 Bayer Ag Method of and apparatus for scrubbing gases
GB920203A (en) * 1958-04-10 1963-03-06 Ruhrchemie Ag Method and apparatus for contacting gas with a liquid
US3907523A (en) * 1972-12-26 1975-09-23 Krebs Engineers Method for removing SO{HD 2 {B from gases
US3928005A (en) * 1974-02-19 1975-12-23 Fuller Co Method and apparatus for treating gaseous pollutants in a gas stream
US4040803A (en) * 1975-02-11 1977-08-09 Mitsubishi Jukogyo Kabushiki Kaisha Wet waste flue gas desulfurizing process using lime as absorbent
EP0017348A1 (en) * 1979-03-06 1980-10-15 Peabody Process Systems, Inc. Flue gas scrubbing process using fly ash alkali
US4323371A (en) * 1979-06-15 1982-04-06 Oy Wartsila Ab Method and arrangement for treating gaseous combustion products
EP0024551A2 (en) * 1979-07-27 1981-03-11 The M. W. Kellogg Company Process and apparatus for removing sulfur dioxide from industrial waste gas

Also Published As

Publication number Publication date
DE3705685A1 (en) 1987-09-10
ES292673Y (en) 1987-03-01
GB8701973D0 (en) 1987-03-04
IT1203490B (en) 1989-02-15
IT8719416A0 (en) 1987-02-18
FR2595055A1 (en) 1987-09-04
JPS62210034A (en) 1987-09-16
ES292673U (en) 1986-06-16

Similar Documents

Publication Publication Date Title
JP2657896B2 (en) Fluid bed reactor and combustion method
KR101417233B1 (en) Method for incinerating waste by two-stage swirling flow fluidized bed incinerator
KR830009431A (en) Incinerator with two shredding stages and heat recovery unit
CN102489280A (en) Silica gel regenerator and regeneration method
US3974021A (en) Process and cyclone reactor for fire decontamination of industrial waste water containing organic and refractory mineral impurities
GB2188562A (en) Combustion gas depurator mechanism
CS9002651A2 (en) Method of solid combustible residues combustion from chemical workshops and device for this method realization
KR101492379B1 (en) System for purifying gas and vapor exhausted from tenter
JP2015034691A (en) Waste matter incineration processing method through two-stage swirl fluidized bed type incineration and its facility
JPH06213409A (en) Method of processing outflow substance which contains organic pollution or inorganic compound
JP3842948B2 (en) Waste decomposition equipment
JPH02263009A (en) Method and equipment for reducing production of dyoxine and furan during incineration of refuse
JPH1194223A (en) Exhaust smoke cleaning unit for garbage incinerator
JP2003042424A (en) Fluidized bed furnace, and supply method for solid incinerated substance with low specific gravity to the fluidized bed furnace
WO2016099245A1 (en) Device for cleaning combustion fumes
DE69211464T2 (en) Heat exchanger heated with a flame
JP2001012714A (en) Re-combustion furnace and recombustion equipment
JP4056233B2 (en) A combustion method that suppresses the synthesis of dioxins in combustion gas generated by a two-stage swirling fluidized bed incinerator.
JPS6130026Y2 (en)
JP3374020B2 (en) Waste pyrolysis melting system
SU1513315A1 (en) Plant for neutralizing waste water
SU875183A1 (en) Apparatus for fire neutralizing of liquid combustible wastes
JPS59164803A (en) Combustion device
SU1597497A1 (en) Apparatus for flame neutralization of flooded waste
SU1730504A1 (en) Arrangement for neutralizing industrial wastes

Legal Events

Date Code Title Description
WAP Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1)