CA2760072A1 - A burner - Google Patents

A burner Download PDF

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Publication number
CA2760072A1
CA2760072A1 CA2760072A CA2760072A CA2760072A1 CA 2760072 A1 CA2760072 A1 CA 2760072A1 CA 2760072 A CA2760072 A CA 2760072A CA 2760072 A CA2760072 A CA 2760072A CA 2760072 A1 CA2760072 A1 CA 2760072A1
Authority
CA
Canada
Prior art keywords
burner
duct
introduction
fuel
solid fuel
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.)
Abandoned
Application number
CA2760072A
Other languages
French (fr)
Inventor
Ib Ohlsen
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.)
FLSmidth AS
Original Assignee
FLSmidth 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 FLSmidth AS filed Critical FLSmidth AS
Publication of CA2760072A1 publication Critical patent/CA2760072A1/en
Abandoned legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D1/00Burners for combustion of pulverulent fuel
    • F23D1/04Burners producing cylindrical flames without centrifugal action
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D2201/00Burners adapted for particulate solid or pulverulent fuels
    • F23D2201/10Nozzle tips
    • F23D2201/101Nozzle tips tiltable

Abstract

This is a description of a burner for introducing solid particulate fuel to a burning zone of a kiln such as a rotary kiln for manufacturing cement clinker or similar, said burner comprising a centrally located duct (1) for conducting solid fuel to an inlet opening (16) and at least one duct (3, 4) for conducting primary air to one or more annular nozzles (17) surrounding the inlet opening (16) of the centrally located duct (1). The particular aspect of the burner is the fact that the centrally located duct (1) for conducting solid fuel is arranged so that the direction (5) of introduction of the fuel relative to the longitudinal axis (6) of the burner and consequently the direction of introduction of the primary air may be adjusted continuously during operation of the burner. Hereby is obtained a burner with which different types of solid particulate fuels and mixtures thereof may be introduced via one and the same duct to the burning zone of a kiln so that the quantity of transport air and the cost of the burner are reduced.
This is because the direction of introduction of the solid fuel relative to the longitudinal axis of the burner and consequently the direction of introduction of the primary air may be adjusted to the optimal direction for the solid fuels introduced at any time notwithstanding the type or mixing ratio of these so as to avoid burnout of the burner lining and at the same time achieving a longer introduction path for the fuel.

Description

Description Title of Invention: A BURNER
[1] The present invention relates to a burner for introducing solid particulate fuel to a burning zone of a kiln such as a rotary kiln for manufacturing cement clinker or similar, said burner comprising a centrally located duct for conducting solid fuel to an inlet opening and at least one duct for conducting primary air to one or more annular nozzles surrounding the inlet opening of the centrally located duct.
[2] Burners of the aforementioned kind are well-known. Normally, the central duct for conveying solid fuel in these known burners is configured as one single piece of a long pipe, the extent of which typically runs parallel and concentric to the longitudinal axis of the burner so that the fuel is introduced to the burning zone in a direction parallel to the longitudinal axis of the burner and consequently also to the surrounding primary air. Experiments conducted by the applicant of this patent application with different types of solid fuel with different particle sizes, forms and densities proved that the optimum fuel burnout will not always take place when using parallel introduction.
Thus it transpired that fine-grained fuels such as coal meal achieve the best burnout when introduced parallel to the longitudinal axis of the burner, whilst coarse-grained fuels such as various types of alternative fuel, including e.g. plastics, paper, rubber and wood chips, achieve the best burnout when entered at an upward angle to the lon-gitudinal axis of the burner. Attempts have been made to meet the various re-quirements of the range of solid fuels as regards i.a. the direction of introduction by configuring the burner with more ducts for the introduction of various solid fuel types, see e.g. WO 2008-065554 owned by the applicant of this patent application, the content of which patent is hereby claimed to be included herein. The disadvantage of a burner with several ducts for the introduction of solid fuels is the fact that the quantity of transport air is increased as the number of ducts increase, and the quantity of transport air is therefore relatively large, which is undesirable as it increases both fuel requirements and the cost of the burner as the number of ducts increase.
Therefore none of the known burners are configured optimally as regards the operational as well as the financial aspects when they are intended for the introduction of various types of solid particulate fuels.
[3] It is the objective of the present invention to provide a burner by means of which the aforementioned disadvantages are reduced.
[4] According to the invention, this is achieved by a burner of the kind mentioned in the introduction and characterized in that the centrally located duct for conducting solid fuel is arranged so that the direction of introduction of the fuel relative to the lon-gitudinal axis of the burner and consequently the direction of introduction of the primary air may be adjusted continuously during operation of the burner.
[5] Hereby is obtained a burner with which different types of solid particulate fuels and mixtures thereof may be introduced via one and the same duct to the burning zone of a kiln so that the quantity of transport air and the cost of the burner are reduced. This is because the direction of introduction of the solid fuel relative to the longitudinal axis of the burner and consequently the direction of introduction of the primary air may be adjusted to the optimal direction for the solid fuels introduced at any time notwith-standing the type or mixing ratio of these so as to avoid burnout of the burner lining and at the same time achieving a longer introduction path for the fuel.
[6] In principle, the centrally located duct for conducting solid fuels may be designed in any way which enables the continuous adjustment of the direction of introduction of the fuel relative to the longitudinal axis of the burner during its operation.
E.g. the duct may be configured as a long pipe which at a point along its length is pivotally suspended from a hinge, and which is connected to a mechanism for rotating the pipe suspended from the hinge up and down in a vertical plane. As mentioned in the in-troduction, the solid fuel duct or pipe is surrounded by at least one annular duct, the inner pipe of which defines a pressurised chamber, which by at least one plate is blanked off at the inlet end of the burner, said plate being provided with an opening for the leading through of the solid fuel duct. For the purposes of limiting the size of the opening and thus the gap between the solid fuel duct and the opening as much as possible, it is preferred that the solid fuel duct is pivotally suspended from a hinge, which is placed immediately next to the opening. If necessary, the gap may be sealed using appropriate flexible sealants. In a variation of the burner according to the invention, the pressurised chamber mentioned above is not demarcated from the inner duct for the injection of primary air, but forms a part thereof.
[7] Burners of the aforementioned type are usually approximately ten metres long, and the achievable change to the direction of introduction of the solid fuel would therefore be limited to a very narrow interval if the solid fuel duct consists of a long, non-flexible pipe. It is therefore preferred that the solid fuel duct is configured of at least two parts being connected to each other by means of a flexible connection, such as a resilient hose made of, for instance, reinforced rubber, a ball joint or similar. The connection between the two parts of the duct does not need to be air-tight as it is preferred to maintain the pressure outside the duct at a higher level than the pressure in the solid fuel duct. The shorter the part of the duct closest to the inlet end of the burner is, the greater is the achievable change to the direction of introduction of the solid fuel, which should be possible to be varied within a range between 0 to 30 , preferably between 0 and 15 and most preferably between 0 and 10 relative to the longitudinal axis of the burner.
[8] Alternatively, the duct may be formed in full or in part of a flexible hose, such as a reinforced rubber hose, which may be moved using a suitable mechanism between the two extreme positions as regards adjustment of the direction of fuel introduction.
[9] According to the invention, the burner may include additional ducts for the in-troduction of other types of fuel, such as oil and gas.
[10] The invention will now be described in further details with reference to the drawing, being diagrammatical, and where [11] Figure la shows a cross-section of the inlet end of a burner according to the invention, which is set for the introduction of coarse-grained solid fuel, and [12] Figure lb shows the same burner set for the introduction of fine-grained solid fuel.
[13] Figures la and lb depict a burner meant for the introduction of various types of solid particulate fuels to the burning zone of a kiln. The burner comprises a centrally located duct 1 for conducting solid fuel to an inlet opening 16 and two annular, concentric ducts 3, 4 for conducting primary air to an annular nozzle 17, which ducts 3, 4 and nozzle 17 surround the central fuel duct 1 and the inlet opening 16 respectively. The solid fuel duct 1 is surrounded by the annular duct 3, the inner pipe 2 of which defines a pressurised chamber 15, which at the inlet end of the burner is blanked off by two plates 13, which are provided with an opening 14 for the leading through of the solid fuel duct 1.
[14] In order to be able to introduce various types of solid fuels with different particle sizes, forms and densities as well as combinations thereof in an optimum manner via one and the same duct 1 to the burning zone of a kiln so that the quantity of transport air and the cost of the burner may be reduced, the duct 1 for conducting solid fuels is arranged so that the direction 5 of introduction of the fuel relative to the longitudinal axis 6 of the burner and consequently the direction of introduction of the primary air may be adjusted continuously during operation of the burner.
[15] Thus the burner may be set to take into account the fact that fine-grained fuels, such as coal meal, achieve the best burnout when introduced parallel to the longitudinal axis of the burner, as shown in Figure lb, whilst coarse-grained fuels, such as various types of alternative fuel, including i.a. plastics, paper, rubber and wood chips, achieve the best burnout when introduced at an upward angle to the longitudinal axis of the burner, as shown in Figure Ia. In other words, the direction 5 of introduction of the solid fuel relative to the longitudinal axis 6 of the burner and consequently the direction 7 of in-troduction of the primary air may be adjusted to the optimum direction for the solid fuels introduced at any time notwithstanding the type or mixing ratio of these.
[16] In the illustrated burner, the solid fuel duct 1 comprises two duct parts 8 and 9 which are connected to each other by means of a suitable connection 10, such as a flexible hose or a ball joint. The duct part 9 is pivotally suspended from a hinge 11 placed im-mediately next to the opening 14 and may be rotated vertically up and down via a mechanism 12 connected to the duct part 8 in the current version, consequently altering the direction 5 of introduction of the fuel. The shorter the duct part 9 closest to the inlet end of the burner is, the greater is the achievable change to the direction 5 of in-troduction of the solid fuel, which should preferably range between 0 and 10 relative to the longitudinal axis of the burner.

Claims (6)

  1. [Claim 1] 1. Burner for introducing solid particulate fuel to a burning zone of a kiln, such as a rotary kiln for manufacturing cement clinker or similar, said burner comprising a centrally located duct (1) for conducting solid fuel to an inlet opening (16) and at least one duct (3, 4) for conducting primary air to one or more annular nozzles (17) surrounding the inlet opening (16) of the centrally located duct (1) characterised in that the centrally located duct (1) for conducting solid fuel is arranged so that the direction (5) of introduction of the fuel relative to the longitudinal axis (6) of the burner and consequently the direction of introduction of the primary air may be adjusted continuously during operation of the burner.
  2. [Claim 2] 2. Burner according to claim 1 characterised in that the solid fuel duct (1) is pivotally suspended from a hinge (11) which is placed immediately next to an opening (14) at the inlet end of the burner and being connected to a mechanism (12) for rotating the duct (1) up and down in a vertical plane.
  3. [Claim 3] 3. Burner according to claims 1 or 2 characterised in that the solid fuel duct (1) is configured of at least two parts (8, 9) being connected to each other by means of a suitable connection (10).
  4. [Claim 4] 4. Burner according to claim 3 characterised in that the duct part (9) is pivotally suspended from a hinge (11) placed immediately next to an opening (14) at the inlet end of the burner and comprises a mechanism (12) for rotating the duct part (9) up and down in a vertical plane.
  5. [Claim 5] 5. Burner according to any of the aforementioned claims char-acterised in that the direction of introduction of the solid fuel can be varied within an interval of 0° and 30°, preferably between 0°
    and 15° and most preferably between 0° and 10° relative to the longitudinal axis (6) of the burner.
  6. [Claim 6] 6. Burner according to claim 1 characterised in that the solid fuel duct (1) fully or partly consists of a flexible hose, such as a reinforced rubber hose.
CA2760072A 2009-04-24 2010-04-23 A burner Abandoned CA2760072A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DKPA200900528 2009-04-24
DKPA200900528 2009-04-24
PCT/IB2010/051800 WO2010122529A1 (en) 2009-04-24 2010-04-23 A burner

Publications (1)

Publication Number Publication Date
CA2760072A1 true CA2760072A1 (en) 2010-10-28

Family

ID=42237360

Family Applications (1)

Application Number Title Priority Date Filing Date
CA2760072A Abandoned CA2760072A1 (en) 2009-04-24 2010-04-23 A burner

Country Status (12)

Country Link
US (1) US20120037054A1 (en)
EP (1) EP2422134A1 (en)
JP (1) JP2012527594A (en)
CN (1) CN102803849A (en)
AU (1) AU2010240471B2 (en)
BR (1) BRPI1013568A2 (en)
CA (1) CA2760072A1 (en)
MX (1) MX2011011221A (en)
RU (1) RU2011147503A (en)
UA (1) UA99576C2 (en)
WO (1) WO2010122529A1 (en)
ZA (1) ZA201108419B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013055286A1 (en) 2011-10-12 2013-04-18 Ecomb Ab (Publ) Combustion chamber supply device and method thereof

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DE102010061496A1 (en) 2010-12-22 2012-06-28 Thyssenkrupp Polysius Ag A tubular burner and method of operating a tubular burner
EP2703339A1 (en) * 2012-09-04 2014-03-05 Casale Chemicals S.A. Burner for the production of synthesis gas
US20150292737A1 (en) * 2012-10-11 2015-10-15 Ecomb Ab (Publ) Supply device for a combustion chamber

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* Cited by examiner, † Cited by third party
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WO2013055286A1 (en) 2011-10-12 2013-04-18 Ecomb Ab (Publ) Combustion chamber supply device and method thereof
CN104011465A (en) * 2011-10-12 2014-08-27 伊科姆股份公司 Combustion chamber supply device and method thereof
EP2766663A4 (en) * 2011-10-12 2015-07-01 Ecomb Ab Publ Combustion chamber supply device and method thereof

Also Published As

Publication number Publication date
AU2010240471A1 (en) 2011-11-10
BRPI1013568A2 (en) 2019-09-24
JP2012527594A (en) 2012-11-08
AU2010240471B2 (en) 2012-11-22
UA99576C2 (en) 2012-08-27
MX2011011221A (en) 2011-11-18
ZA201108419B (en) 2012-07-25
US20120037054A1 (en) 2012-02-16
RU2011147503A (en) 2013-05-27
EP2422134A1 (en) 2012-02-29
WO2010122529A1 (en) 2010-10-28
CN102803849A (en) 2012-11-28

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Legal Events

Date Code Title Description
EEER Examination request
FZDE Discontinued

Effective date: 20140805