CN102278743A - Recirculating fluidized bed boiler - Google Patents

Recirculating fluidized bed boiler Download PDF

Info

Publication number
CN102278743A
CN102278743A CN2011102338235A CN201110233823A CN102278743A CN 102278743 A CN102278743 A CN 102278743A CN 2011102338235 A CN2011102338235 A CN 2011102338235A CN 201110233823 A CN201110233823 A CN 201110233823A CN 102278743 A CN102278743 A CN 102278743A
Authority
CN
China
Prior art keywords
flue
heating surface
boiler
economizer
superheater
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.)
Pending
Application number
CN2011102338235A
Other languages
Chinese (zh)
Inventor
孙建涛
潘宇峰
陈弘
田忠权
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.)
Jiangsu Taihu Boiler Co Ltd
Original Assignee
Jiangsu Taihu Boiler Co Ltd
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 Jiangsu Taihu Boiler Co Ltd filed Critical Jiangsu Taihu Boiler Co Ltd
Priority to CN2011102338235A priority Critical patent/CN102278743A/en
Publication of CN102278743A publication Critical patent/CN102278743A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Air Supply (AREA)

Abstract

The invention provides a recirculating fluidized bed boiler which can enable the rear pat of the boiler to have less deposited dust, and ensure the normal use of the boiler. The technical scheme is as follows: the boiler comprises a boiler cylinder, a hearth, an evaporation heating surface, a superheater, an economizer, an air preheater and a tail part gas flue; the boiler cylinder is installed above the hearth; the superheater, the evaporation heating surface, the economizer, the air preheater and the tail part gas flue are sequentially installed in the flue gas flow direction of the hearth; the boiler is characterized in that after the flue gas of the hearth rises, the flue gas sequentially flows into a horizontal flue and a turn flue and then is leaded to a vertical flue at the tail part; a cyclone separator is arranged below the horizontal flue; the suction inlet of the cyclone separator faces to the horizontal flue; an exhaust opening at the lower part of the cyclone separator is connected with a returning charge channel; the returning charge channel is communicated with the bottom of the hearth; the cross section of the evaporation heating surface is of a W-shaped structure; and the superheater, the evaporation heating surface of the W-shaped structure, the economizer and the air preheater are sequentially connected and sequentially arranged in the vertical flue at the tail part.

Description

CFBB
Technical field
The present invention relates to the technical field of structures of boiler, be specially CFBB.
Background technology
Along with China rises steadily to the raising and the burned coal price of environmental requirement, and the continuous development of industrial economy, in a large number at the low-pressure low-temperature low capacity boiler of usefulness because of not adapting to reasons such as environmental requirement, the thermal efficiency be low, face the superseded situation of stopping transport.CFBB has the advantage of many uniquenesses, and is wide as efficiency of combustion height, fuel tolerance, can carry out desulfuration in furnace, can effectively control the discharging of NOx etc.
But after the process burner hearth burning of existing fuel, its fly ash content height, and contain not by clean-burning material particles, existing structure can't effectively be handled, and makes that boiler rear portion dust stratification is serious, just needs deashing in very short time, has influenced the normal use of boiler.
Summary of the invention
At the problems referred to above, the invention provides CFBB, it can make that boiler rear portion dust stratification is few, guarantees the normal use of boiler.
CFBB, its technical scheme is such: it comprises drum, burner hearth, evaporating heating surface, superheater, economizer, air preheater, back-end ductwork, the top of described burner hearth is equipped with described drum, the flue gas flow direction direction of described burner hearth is equipped with described superheater successively, evaporating heating surface, economizer, air preheater, back-end ductwork, it is characterized in that: the flue gas of described burner hearth flows into horizontal flue after rising successively, lead to tail vertical well gas flue behind the turning flue, the below of described horizontal flue is provided with cyclone separator, described cyclone separator suction inlet is towards described horizontal flue, the below outlet of described cyclone separator connects the returning charge passage, described returning charge passage leads to the bottom of described burner hearth, described evaporating heating surface is specially the evaporating heating surface that the cross section is a W shape structure, described superheater, the evaporating heating surface of W shape structure, economizer, air preheater connects in turn and is arranged in turn in the described tail vertical well gas flue.
After adopting structure of the present invention, material forms flue gas after the burner hearth internal combustion, after flue gas flow into horizontal flue, flying dust in the flue gas, do not sucked by cyclone separator by clean-burning material particles, and flow to burner hearth bottom by the returning charge passage, flying dust is discharged from slag notch, is not fully burnt by clean-burning material particles, and it can make that boiler rear portion dust stratification is few, guarantees the normal use of boiler; In addition, the evaporating heating surface of W shape structure makes flue gas fully to contact, and makes the energy utilization rate height.
Description of drawings
Fig. 1 is a front view structural representation of the present invention.
The specific embodiment
See Fig. 1, it comprises drum 1, burner hearth 2, evaporating heating surface 10, superheater 8, economizer 11, air preheater 12, back-end ductwork 14, the top of described burner hearth 2 is equipped with described drum 1, the flue gas flow direction direction of described burner hearth 2 is equipped with described superheater 8 successively, evaporating heating surface 10, economizer 11, air preheater 12, back-end ductwork 14, the flue gas of burner hearth 2 flows into horizontal flue 15 after rising successively, lead to tail vertical well gas flue 17 behind the turning flue 7, the below of described horizontal flue 15 is provided with cyclone separator 9, described cyclone separator 9 suction inlets are towards described horizontal flue 15, the below outlet of described cyclone separator 9 connects returning charge passage 3, described returning charge passage 3 leads to the bottom of described burner hearth 2, described evaporating heating surface 10 is specially the evaporating heating surface that the cross section is a W shape structure, described superheater 8, evaporating heating surface 10, economizer 11, air preheater 12 connects in turn and is arranged in turn in the tail vertical well gas flue 17.Charging aperture 4 leads to the bottom of burner hearth 2, and the below, bottom of burner hearth 2 is provided with water cooled wind chamber 6, slag notch 16, and the bottom sidewall of burner hearth 2 is provided with secondary air channel 5.

Claims (1)

1. CFBB, it comprises drum, burner hearth, evaporating heating surface, superheater, economizer, air preheater, back-end ductwork, the top of described burner hearth is equipped with described drum, the flue gas flow direction direction of described burner hearth is equipped with described superheater successively, evaporating heating surface, economizer, air preheater, back-end ductwork, it is characterized in that: the flue gas of described burner hearth flows into horizontal flue after rising successively, lead to tail vertical well gas flue behind the turning flue, the below of described horizontal flue is provided with cyclone separator, described cyclone separator suction inlet is towards described horizontal flue, the below outlet of described cyclone separator connects the returning charge passage, described returning charge passage leads to the bottom of described burner hearth, described evaporating heating surface is specially the evaporating heating surface that the cross section is a W shape structure, described superheater, the evaporating heating surface of W shape structure, economizer, air preheater connects in turn and is arranged in turn in the described tail vertical well gas flue.
CN2011102338235A 2011-08-16 2011-08-16 Recirculating fluidized bed boiler Pending CN102278743A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011102338235A CN102278743A (en) 2011-08-16 2011-08-16 Recirculating fluidized bed boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011102338235A CN102278743A (en) 2011-08-16 2011-08-16 Recirculating fluidized bed boiler

Publications (1)

Publication Number Publication Date
CN102278743A true CN102278743A (en) 2011-12-14

Family

ID=45104348

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011102338235A Pending CN102278743A (en) 2011-08-16 2011-08-16 Recirculating fluidized bed boiler

Country Status (1)

Country Link
CN (1) CN102278743A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106016226A (en) * 2016-07-14 2016-10-12 无锡华光锅炉股份有限公司 Gas-fired boiler
CN109185892A (en) * 2018-10-11 2019-01-11 无锡华光锅炉股份有限公司 A kind of recirculating fluidized bed garbage fired boiler structure

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0851173A2 (en) * 1996-12-30 1998-07-01 Combustion Engineering, Inc. A method of controlling nitrous oxide in circulating fluidized bed steam generators
US20030202913A1 (en) * 2002-04-30 2003-10-30 Mikhail Maryamchik Compact footprint CFB with mechanical dust collector
CN201526942U (en) * 2009-09-30 2010-07-14 哈尔滨锅炉厂有限责任公司 High-efficient energy-saving residual-heat utilization device
CN201582805U (en) * 2010-01-05 2010-09-15 太原锅炉集团有限公司 Biomass-energy circulating fluidized bed boiler with low energy consumption
CN102012097A (en) * 2010-04-28 2011-04-13 山东圣威新能源有限公司 Fluidized bed oil and water dual-medium circulation boiler
CN201811432U (en) * 2010-09-29 2011-04-27 河北艺能锅炉有限责任公司 Heat-conduction oil boiler of recirculating fluidized bed
CN202267056U (en) * 2011-08-16 2012-06-06 江苏太湖锅炉股份有限公司 Circulating fluidized bed boiler

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0851173A2 (en) * 1996-12-30 1998-07-01 Combustion Engineering, Inc. A method of controlling nitrous oxide in circulating fluidized bed steam generators
US20030202913A1 (en) * 2002-04-30 2003-10-30 Mikhail Maryamchik Compact footprint CFB with mechanical dust collector
CN201526942U (en) * 2009-09-30 2010-07-14 哈尔滨锅炉厂有限责任公司 High-efficient energy-saving residual-heat utilization device
CN201582805U (en) * 2010-01-05 2010-09-15 太原锅炉集团有限公司 Biomass-energy circulating fluidized bed boiler with low energy consumption
CN102012097A (en) * 2010-04-28 2011-04-13 山东圣威新能源有限公司 Fluidized bed oil and water dual-medium circulation boiler
CN201811432U (en) * 2010-09-29 2011-04-27 河北艺能锅炉有限责任公司 Heat-conduction oil boiler of recirculating fluidized bed
CN202267056U (en) * 2011-08-16 2012-06-06 江苏太湖锅炉股份有限公司 Circulating fluidized bed boiler

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106016226A (en) * 2016-07-14 2016-10-12 无锡华光锅炉股份有限公司 Gas-fired boiler
CN106016226B (en) * 2016-07-14 2018-10-16 无锡华光锅炉股份有限公司 A kind of gas fired-boiler
CN109185892A (en) * 2018-10-11 2019-01-11 无锡华光锅炉股份有限公司 A kind of recirculating fluidized bed garbage fired boiler structure

Similar Documents

Publication Publication Date Title
CN102588959B (en) Gas-solid separator of recirculating fluidized bed boiler and boiler comprising same
CN101949535A (en) Low-ratio biomass circulating fluidized bed boiler and combustion method thereof
CN201964387U (en) High-efficiency biomass-combusting electricity generating boiler
CN203718760U (en) Boiling furnace
CN201463253U (en) Double-furnace horizontal type industrial pulverized coal fired boiler
CN202141027U (en) Environment-friendly energy-saving biomass hot pipe boiler
CN203731392U (en) U-shaped flame boiler with overhead straight-through pulverized coal burner
CN102278743A (en) Recirculating fluidized bed boiler
CN202267056U (en) Circulating fluidized bed boiler
CN202101217U (en) Biomass steam boiler with horizontal water and fire tubes
CN101963350A (en) Material separator for circulating fluidized bed boiler
CN103322676A (en) Biomass fuel hot blast device
CN106287680A (en) Small-sized biomass shaped fuel recirculating fluidized bed steam boiler
CN102095254B (en) Organic heat carrier boiler of fluidized bed, with low cost, environment protection, energy saving and emission reduction
CN101576317B (en) Horizontal type double-flue industrial coal powder boiler
CN205090372U (en) Meniscus formula flying dust circulation separator structure
CN201521950U (en) Circulating fluidized bed boiler provided with internal cyclone upper-exhausting high-temperature separator
CN100478612C (en) Circulating fluidized bed combustion device and its combustion method
CN103388820A (en) Clean pulverized coal combustion industrial boiler device
CN102563627B (en) Efficient pulverized coal industrial boiler with low-pollution emission characteristic
CN203336814U (en) Horizontal hot water boiler
CN202709088U (en) High-efficiency coal powder burning device for molten salt furnace
CN201166360Y (en) Affiliated combustion apparatus for anthracite powder to replace lump coal
CN202813348U (en) Layer-burning boiler with internal two-stage dust collector
CN202024473U (en) Environment-friendly, energy-saving and emission-reduction fluidized bed organic heat carrier boiler with low cost

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C12 Rejection of a patent application after its publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20111214