CA1078683A - Steam boilers - Google Patents
Steam boilersInfo
- Publication number
- CA1078683A CA1078683A CA279,302A CA279302A CA1078683A CA 1078683 A CA1078683 A CA 1078683A CA 279302 A CA279302 A CA 279302A CA 1078683 A CA1078683 A CA 1078683A
- Authority
- CA
- Canada
- Prior art keywords
- tube bank
- pass
- burning furnace
- flow
- clean 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.)
- Expired
Links
Abstract
STEAM BOILERS
ABSTRACT OF THE DISCLOSURE
There is always a danger of slagging on and/or corro-sion of the tubes of the highest temperature superheater bank and, if present, reheater bank when burning heavy bunker fuel oil. Therefore a clean fuel burning furnace is provided which is separate from the heavy bunker fuel oil burning furnace and only the combustion gases from burning the clean fuel are used to heat the highest temperature superheater bank and, if present, reheater bank. The clean fuel is preferably provided by a gasi-fier in which a portion of the heavy bunker fuel oil is pre-combusted to give a clean combustible fuel gas.
ABSTRACT OF THE DISCLOSURE
There is always a danger of slagging on and/or corro-sion of the tubes of the highest temperature superheater bank and, if present, reheater bank when burning heavy bunker fuel oil. Therefore a clean fuel burning furnace is provided which is separate from the heavy bunker fuel oil burning furnace and only the combustion gases from burning the clean fuel are used to heat the highest temperature superheater bank and, if present, reheater bank. The clean fuel is preferably provided by a gasi-fier in which a portion of the heavy bunker fuel oil is pre-combusted to give a clean combustible fuel gas.
Description
f"
~'7~83 STEAM BOILERS
This inven~ion relates to steam boilers and in parti-cular marine steam boilers used to supply steam to the steam turbines powering a s'nip.
B~CKGRO~ND TO THE INVENTION
In marine steam boilers providing high temperature and pressure superheat and reheat steam there is a danger of slagging and/or corrosion o the tubes forming at least the 'nighest temperature superheater and reheater bank when burning heavy bunker fuel oil which has a high ash and sulphur content.
It is therefore an object of this invention to reduce this slagging and/or corrosion in such steam boilers.
BRIEF SUMMARY OF THE INVENTION
According to the invention there is provided a steam boiler having a heavy oil burning furnace and a separate clean fuel burning furnace, and a number of tube banks providing one or more stages of superheated steam and optionally one or more stages of reheated steam, the tube banks being arranged so that the tubes of the highest temperature superheater tube bank and of the highest temper~ture reheater tube bank if provided are heated by the combustion p~oducts from the clean fuel burning furnace.
In such a boiler the slagging on and/or corrosion of the tubes of the highest temperature superheater t~e bank and reheater tube bank is largely avoided because those tubes are contacted solely by the clean combustion gases from tlle clean fuel burning furnace. The other tubes of any lower temperature superheater and reheater tube banks can be swept by the combustion gases from the heavy fuel oil burning furnace 30 but for these tubes which operate at lower temperatures the risks of slagging and/or corrosion are less.
. . ~
37~ 33 The clean fuel for the clean fuel burning furnace can be provided by the pre-combustion of heavy fuel in a gasifier which can provide a supply of clean product gas for burning whilst retaining the impurities in the heavy fuel. These gasifiers are known and can take the form of a fluidized bed gasifier.
Under no-sleam flow conditions in the reheater, cooling air must be passed over the tubes of the reheater tube bank or banks. This can be achieved by positioning the bank or banks in gas passes whose outlets under such conditions can be closed by dampers and cooling air can then be fed in reverse flow through the pass or passes directly from an air supply fan such as the forced draught fan for the combustion air.
Separate forced draught fans and air pre-heaters can be provided for each furnace if r~quired to provide air for the furnaces and/or the gasifier. This may serve to avoid the back-feeA of contaminants from the air preheating system for the clean fuel burning furnace by the air supply to the heavy oil burning furnace so as to ensure that the combustion products from the clean fuel burning furnace remain clean.
BRIEF SUMMARY OF TH~ DRAWINGS
An example of a marine steam boiler according to the invention will now be described with reference to the accom~
panying drawing which is a sectional diagram of the boiler.
DESCRIPTION OF THE PREFERRED EMBODIMENT
The boiler 10 shown in the drawng has a heavy fuel oil burning furnace 12 and a separate clean fuel gas burning furnace 14. The combustion gases from the furnace 12 pass up through two parallel passes 16 and 18 while the combustion gases from the furnace 14 pass up through a pàss 20. The flow ,~, . . . . ' - , ~IU78~33 of gases through the passes. 16, 18, and 20 are controlled by dampers 22, 24 and 26, respectively. The gases Erom all three passes are thereafter combined in a common flue 28 containing an economiser tube bank 30. The walls of the furnaces 12 and 14 and passes 16, 18 and 20 are defined by conventional water tube walls which are not shown in detail.
The furnace 12 is f~red by heavy fuel oil from a supply 32. The heavy fuel oil is burned by burners 34 and com-bustion air is supplied from a windbox 36. Air for this wind-box is supplied from a common duct 38 and its rate of supply is controlled by a damper 40.
The furnace 14 is fired by clean gas from a gasifier 44. This gasi.fier receives heavy fuel oil from the supply 32 and air from the common duct 38 via a passage 45 at a rate determined by a damper 46 and converts the oil to a clean com-bustible gas which is fed to a burner 48 in the furnace 14 via a duct 50. Combustion air for the furnace 14 is supplied to a windbox 52 from the common duct 38 and the rate of supply is controlled by a damper 54.
The air supply to the common duc-t 38 is made from a forced draught ~an 56, the air being preheated in a regenera-tive air heater 58 heated by the combined combustion gases in ~.
the flue 28.
The pass 16 contains a first or low temperature superheater 60 and a first or low temperature reheater 62 while the pass 18 contains a second or intermediate superheater 64 serially connected with superheater 60 and a by-pass economiser 66. Dirty combustion gases from the furnace 12 flow over these ~- :
items. The pass 20 contains a thi.rd or final superheater 68 : 30. serially connected with superheater 64 and a second or final reheater 70 serially connected with reheater 62, this superheater.
~68 and rehea~er 70 being the hïghest temperature superheater and . -4-.. . .
, ~,~, .
.
' ' ~ ' '. ' , - ~7!36~3 reheater passes, respect;vely. Clean combustion gases from the furnace 14 pass over these items and to ensure this the damper 26 associa~ed with the pass 20 is controlled to maintain a slight positive pressure differential between that pass and pass 18 at the level of intermediate open screens 80 and 82 provided respectively between the passes 16 and 18 and passes 18 and 20.
- These screens 80 and 82 are provided so that the com-bustion gases can deviate from one pass to another after flow over the first, second or third superheater in dependence upon the positioning of the dampers 22, 24 and 26, the damper 26 being arranged as noted above to ensure that dirty combustion gases do not flow from the pass 18 to the pass 20.
Under no-steam flow conditions through the first and second reheaters 62 and 70, these have to be cooled. There-fore cooling air ducts 90 and 92 lead from the fan 56 to the tops of the passes 16 and 20, respectively. The passage of the ' cooling air through its ducts 90 and 92 is controlled by dampers ; 94 and 96, respectively. Thus to prevent flow of hot combustion gases over the reheaters 62 and 70 when they contain no steam, the dampers 22 and 26 are closed, all of the combustion gases then passing over the economiser 66, and cooling air is allowed to flow down over the reheaters 62 and 70 by opening the dampers 94 and 96 and this cooling air then passes through the open screens 80 and 82 to join the combustion products.
If desired a separate forced draught fan can be ~ro-vided to supply air to the furnace 14 and gasifier 44 and dirt - picked up by such air from any air preheater can be fed back into the combustion air for the furnace 12 so as to keep the combustion gases from the furnace 14 clean.
3~ The operation of the boiler 10 should be clear from ', '' ''. ' ' ~ ". . .: ' , " ' '" ' - . . ..
~ 37~ 3 the above description.
As will be appreciated, the final or third superheater 68 and the final or second reheater 70 both operate at the highest temperatures and 50 are most liable to be affected by slag and corrosion problems. However, both can only receive clean combustion gases and so problems of slagging and corrosion are reduced as compared with a situaton in which they receive combustion gases from the furnace 12.
Although the words water and steam have been used herein those woeds are to be construed as including any liquid and its vapour unless the context specifically requires other-wise.
A latitude of modification, change and substitution is intended in the foregoing disclosure and in some instances some features of the invention will be employed without a corres-ponding ase of other features. Accordingly it is appropriate ~hat the appended claims be construed broadly and in a manner consistent with the spirit and scope of the invention herein.
20 ~
'' ~ .
'': ' ~ ' . .
,,
~'7~83 STEAM BOILERS
This inven~ion relates to steam boilers and in parti-cular marine steam boilers used to supply steam to the steam turbines powering a s'nip.
B~CKGRO~ND TO THE INVENTION
In marine steam boilers providing high temperature and pressure superheat and reheat steam there is a danger of slagging and/or corrosion o the tubes forming at least the 'nighest temperature superheater and reheater bank when burning heavy bunker fuel oil which has a high ash and sulphur content.
It is therefore an object of this invention to reduce this slagging and/or corrosion in such steam boilers.
BRIEF SUMMARY OF THE INVENTION
According to the invention there is provided a steam boiler having a heavy oil burning furnace and a separate clean fuel burning furnace, and a number of tube banks providing one or more stages of superheated steam and optionally one or more stages of reheated steam, the tube banks being arranged so that the tubes of the highest temperature superheater tube bank and of the highest temper~ture reheater tube bank if provided are heated by the combustion p~oducts from the clean fuel burning furnace.
In such a boiler the slagging on and/or corrosion of the tubes of the highest temperature superheater t~e bank and reheater tube bank is largely avoided because those tubes are contacted solely by the clean combustion gases from tlle clean fuel burning furnace. The other tubes of any lower temperature superheater and reheater tube banks can be swept by the combustion gases from the heavy fuel oil burning furnace 30 but for these tubes which operate at lower temperatures the risks of slagging and/or corrosion are less.
. . ~
37~ 33 The clean fuel for the clean fuel burning furnace can be provided by the pre-combustion of heavy fuel in a gasifier which can provide a supply of clean product gas for burning whilst retaining the impurities in the heavy fuel. These gasifiers are known and can take the form of a fluidized bed gasifier.
Under no-sleam flow conditions in the reheater, cooling air must be passed over the tubes of the reheater tube bank or banks. This can be achieved by positioning the bank or banks in gas passes whose outlets under such conditions can be closed by dampers and cooling air can then be fed in reverse flow through the pass or passes directly from an air supply fan such as the forced draught fan for the combustion air.
Separate forced draught fans and air pre-heaters can be provided for each furnace if r~quired to provide air for the furnaces and/or the gasifier. This may serve to avoid the back-feeA of contaminants from the air preheating system for the clean fuel burning furnace by the air supply to the heavy oil burning furnace so as to ensure that the combustion products from the clean fuel burning furnace remain clean.
BRIEF SUMMARY OF TH~ DRAWINGS
An example of a marine steam boiler according to the invention will now be described with reference to the accom~
panying drawing which is a sectional diagram of the boiler.
DESCRIPTION OF THE PREFERRED EMBODIMENT
The boiler 10 shown in the drawng has a heavy fuel oil burning furnace 12 and a separate clean fuel gas burning furnace 14. The combustion gases from the furnace 12 pass up through two parallel passes 16 and 18 while the combustion gases from the furnace 14 pass up through a pàss 20. The flow ,~, . . . . ' - , ~IU78~33 of gases through the passes. 16, 18, and 20 are controlled by dampers 22, 24 and 26, respectively. The gases Erom all three passes are thereafter combined in a common flue 28 containing an economiser tube bank 30. The walls of the furnaces 12 and 14 and passes 16, 18 and 20 are defined by conventional water tube walls which are not shown in detail.
The furnace 12 is f~red by heavy fuel oil from a supply 32. The heavy fuel oil is burned by burners 34 and com-bustion air is supplied from a windbox 36. Air for this wind-box is supplied from a common duct 38 and its rate of supply is controlled by a damper 40.
The furnace 14 is fired by clean gas from a gasifier 44. This gasi.fier receives heavy fuel oil from the supply 32 and air from the common duct 38 via a passage 45 at a rate determined by a damper 46 and converts the oil to a clean com-bustible gas which is fed to a burner 48 in the furnace 14 via a duct 50. Combustion air for the furnace 14 is supplied to a windbox 52 from the common duct 38 and the rate of supply is controlled by a damper 54.
The air supply to the common duc-t 38 is made from a forced draught ~an 56, the air being preheated in a regenera-tive air heater 58 heated by the combined combustion gases in ~.
the flue 28.
The pass 16 contains a first or low temperature superheater 60 and a first or low temperature reheater 62 while the pass 18 contains a second or intermediate superheater 64 serially connected with superheater 60 and a by-pass economiser 66. Dirty combustion gases from the furnace 12 flow over these ~- :
items. The pass 20 contains a thi.rd or final superheater 68 : 30. serially connected with superheater 64 and a second or final reheater 70 serially connected with reheater 62, this superheater.
~68 and rehea~er 70 being the hïghest temperature superheater and . -4-.. . .
, ~,~, .
.
' ' ~ ' '. ' , - ~7!36~3 reheater passes, respect;vely. Clean combustion gases from the furnace 14 pass over these items and to ensure this the damper 26 associa~ed with the pass 20 is controlled to maintain a slight positive pressure differential between that pass and pass 18 at the level of intermediate open screens 80 and 82 provided respectively between the passes 16 and 18 and passes 18 and 20.
- These screens 80 and 82 are provided so that the com-bustion gases can deviate from one pass to another after flow over the first, second or third superheater in dependence upon the positioning of the dampers 22, 24 and 26, the damper 26 being arranged as noted above to ensure that dirty combustion gases do not flow from the pass 18 to the pass 20.
Under no-steam flow conditions through the first and second reheaters 62 and 70, these have to be cooled. There-fore cooling air ducts 90 and 92 lead from the fan 56 to the tops of the passes 16 and 20, respectively. The passage of the ' cooling air through its ducts 90 and 92 is controlled by dampers ; 94 and 96, respectively. Thus to prevent flow of hot combustion gases over the reheaters 62 and 70 when they contain no steam, the dampers 22 and 26 are closed, all of the combustion gases then passing over the economiser 66, and cooling air is allowed to flow down over the reheaters 62 and 70 by opening the dampers 94 and 96 and this cooling air then passes through the open screens 80 and 82 to join the combustion products.
If desired a separate forced draught fan can be ~ro-vided to supply air to the furnace 14 and gasifier 44 and dirt - picked up by such air from any air preheater can be fed back into the combustion air for the furnace 12 so as to keep the combustion gases from the furnace 14 clean.
3~ The operation of the boiler 10 should be clear from ', '' ''. ' ' ~ ". . .: ' , " ' '" ' - . . ..
~ 37~ 3 the above description.
As will be appreciated, the final or third superheater 68 and the final or second reheater 70 both operate at the highest temperatures and 50 are most liable to be affected by slag and corrosion problems. However, both can only receive clean combustion gases and so problems of slagging and corrosion are reduced as compared with a situaton in which they receive combustion gases from the furnace 12.
Although the words water and steam have been used herein those woeds are to be construed as including any liquid and its vapour unless the context specifically requires other-wise.
A latitude of modification, change and substitution is intended in the foregoing disclosure and in some instances some features of the invention will be employed without a corres-ponding ase of other features. Accordingly it is appropriate ~hat the appended claims be construed broadly and in a manner consistent with the spirit and scope of the invention herein.
20 ~
'' ~ .
'': ' ~ ' . .
,,
Claims (10)
1. A steam boiler comprising:
a heavy oil burning furnace, a separate clean fuel burning furnace, a common flue, a first pass through which combustion gases from said heavy oil burning furnace travel, said pass disposed between said\heavy oil burning furnace and said common flue, a second pass through which combustion gases from said clean fuel burning furnace travell said second 20 pass disposed between said separate clean fuel burning furnace and said common flue, and a superheater tube bank, chosen from a single superheater tube bank and a finishing or highest temperature super-heater tube bank, positioned in said second pass and swept by combustion gases from said clean fuel burning furnace.
a heavy oil burning furnace, a separate clean fuel burning furnace, a common flue, a first pass through which combustion gases from said heavy oil burning furnace travel, said pass disposed between said\heavy oil burning furnace and said common flue, a second pass through which combustion gases from said clean fuel burning furnace travell said second 20 pass disposed between said separate clean fuel burning furnace and said common flue, and a superheater tube bank, chosen from a single superheater tube bank and a finishing or highest temperature super-heater tube bank, positioned in said second pass and swept by combustion gases from said clean fuel burning furnace.
2. A steam boiler according to claim 1 further comprising a gasifier in which heavy oil can be pre-combusted to provide a product gas, and means for conveying said product gas to said clean fuel furnace.
3. A steam boiler according to claim 2 in which said gasifier is a fluidized bed gasifier.
4. A steam boiler according to claim 1 further com-prising dampers positioned at the outlets from said first and second passes.
5. A steam boiler according to claim 4 further com-prising communicating ports provided between said first and second passes at intermediate positions along their length, and means for controlling said damper controlling the flow of gases along said second pass to ensure that there is no flow into that pass from the first pass.
6. A steam boiler comprising:
a heavy oil burning furnace, a separate clean fuel burning furnace, a common flue, a first pass through which combustion gases from said heavy oil burning furnace travel to said flue, a second pass through which combustion gases from said clean fuel burning furnace travel to said flue, a superheater tube bank chosen from a single super-heater tube bank and a finishing or highest tempera-ture superheater tube bank, positioned in said second pass, a reheater tube bank, chosen from a single reheater tube bank and a finishing or highest temperature reheater tube bank, positioned in said second pass following said superheater tube bank and also swept by combustion gases from said clean fuel burning furnace, and heating elements optionally including at least one lower temperature superheater tube bank and at least one lower temperature reheater tube bank positioned in said first pass and swept by combustion gases from said heavy oil burning furnace.
a heavy oil burning furnace, a separate clean fuel burning furnace, a common flue, a first pass through which combustion gases from said heavy oil burning furnace travel to said flue, a second pass through which combustion gases from said clean fuel burning furnace travel to said flue, a superheater tube bank chosen from a single super-heater tube bank and a finishing or highest tempera-ture superheater tube bank, positioned in said second pass, a reheater tube bank, chosen from a single reheater tube bank and a finishing or highest temperature reheater tube bank, positioned in said second pass following said superheater tube bank and also swept by combustion gases from said clean fuel burning furnace, and heating elements optionally including at least one lower temperature superheater tube bank and at least one lower temperature reheater tube bank positioned in said first pass and swept by combustion gases from said heavy oil burning furnace.
7. A steam boiler as claimed in Claim 6 in which said first pass consists of a pair of parallel passes.
8. A steam boiler according to Claim 6 further com-prising means for passing a flow of cooling air over each re-heater tube bank when there is no steam flow through the tubes of the reheater.
9. A steam boiler according to Claim 8 in which the flow of cooling air is derived from the combustion air flow and the cooling air is passed in reverse flow over said reheater tube bank to the direction of flow of combustion products.
10. A steam boiler comprising:
a heavy oil burning furnace, a separate clean fuel burning furnace, a common flue, a gas pass for combustion products from said clean fuel burning furnace leading to said common flue, a high temperature superheater tube bank in said gas pass, a high temperature reheater tube bank following said high temperature superheater tube bank in said gas pass, a pair of parallel gas passes for combustion pro-ducts from said heavy oil burning furnace, at least one lower temperature superheater tube bank posi-tioned in one of said parallel gas passes, at least one lower temperature reheater tube bank positioned in one of said pair of parallel gas passes, an economiser tube bank positioned in one of said pair of parallel gas passes, communication ports between said passes at inter-mediate positions along their lengths, and means for supplying a flow of cooling air over each re-heater tube bank when there is no steam flow through the reheater tubes, all of the combustion gases and the cooling air then being directed to flow over said economiser tube bank.
a heavy oil burning furnace, a separate clean fuel burning furnace, a common flue, a gas pass for combustion products from said clean fuel burning furnace leading to said common flue, a high temperature superheater tube bank in said gas pass, a high temperature reheater tube bank following said high temperature superheater tube bank in said gas pass, a pair of parallel gas passes for combustion pro-ducts from said heavy oil burning furnace, at least one lower temperature superheater tube bank posi-tioned in one of said parallel gas passes, at least one lower temperature reheater tube bank positioned in one of said pair of parallel gas passes, an economiser tube bank positioned in one of said pair of parallel gas passes, communication ports between said passes at inter-mediate positions along their lengths, and means for supplying a flow of cooling air over each re-heater tube bank when there is no steam flow through the reheater tubes, all of the combustion gases and the cooling air then being directed to flow over said economiser tube bank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA279,302A CA1078683A (en) | 1977-05-27 | 1977-05-27 | Steam boilers |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA279,302A CA1078683A (en) | 1977-05-27 | 1977-05-27 | Steam boilers |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1078683A true CA1078683A (en) | 1980-06-03 |
Family
ID=4108745
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA279,302A Expired CA1078683A (en) | 1977-05-27 | 1977-05-27 | Steam boilers |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA1078683A (en) |
-
1977
- 1977-05-27 CA CA279,302A patent/CA1078683A/en not_active Expired
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3048131A (en) | Method for burning fuel | |
| US3948223A (en) | Serially fired steam generator | |
| US2511647A (en) | Combustion air heater for furnaces arranged to minimize corrosion by flue gases | |
| GB523871A (en) | Improvements in or relating to steam or other vapour generators having associated therewith independently fired reheaters or/and superheaters | |
| US4109613A (en) | Steam boilers | |
| CA1078683A (en) | Steam boilers | |
| US4465021A (en) | Steam generator with a main boiler and a fluidized bed furnace | |
| US2968288A (en) | Method of burning slag forming fuel in furnaces | |
| GB798786A (en) | Improvements in or relating to steam generators | |
| US2863424A (en) | Steam generating, superheating and reheating unit with dual furnaces and parallel gas passes | |
| US2673553A (en) | Multiple furnace fluid heating unit | |
| US2415123A (en) | Boiler | |
| US2396102A (en) | Auxiliary air heater | |
| SU1545023A1 (en) | Steam boiler | |
| GB983641A (en) | Improvements in vapour generating units adapted for firing by solid and gaseous fuels | |
| CN211822363U (en) | High-temperature high-pressure gas boiler | |
| GB802032A (en) | A steam generator and method of operating the same | |
| US1229320A (en) | Furnace. | |
| US3146762A (en) | Steam generating unit | |
| US3033178A (en) | Vapor generating and superheating unit with recirculated gas introduction along furnace floor | |
| GB974863A (en) | Improvements relating to industrial furnaces | |
| US1924877A (en) | Boiler | |
| US1544905A (en) | Heat economizer | |
| US2953124A (en) | Open pass vapor generating and superheating unit with gas recirculation to open pass | |
| US2980084A (en) | System for burning low volatile fuels |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MKEX | Expiry |