CN106996552A - Membrane wall list drum marine boiler - Google Patents

Membrane wall list drum marine boiler Download PDF

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Publication number
CN106996552A
CN106996552A CN201710311334.4A CN201710311334A CN106996552A CN 106996552 A CN106996552 A CN 106996552A CN 201710311334 A CN201710311334 A CN 201710311334A CN 106996552 A CN106996552 A CN 106996552A
Authority
CN
China
Prior art keywords
membrane wall
economizer
temperature
drum
box
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
CN201710311334.4A
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Chinese (zh)
Inventor
茅新东
赵柏年
王金阳
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.)
Zhangjiagang Greens Shazhou Boiler Co Ltd
Original Assignee
Zhangjiagang Greens Shazhou 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 Zhangjiagang Greens Shazhou Boiler Co Ltd filed Critical Zhangjiagang Greens Shazhou Boiler Co Ltd
Priority to CN201710311334.4A priority Critical patent/CN106996552A/en
Publication of CN106996552A publication Critical patent/CN106996552A/en
Pending legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00Methods of steam generation characterised by form of heating method
    • F22B1/22Methods of steam generation characterised by form of heating method using combustion under pressure substantially exceeding atmospheric pressure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B31/00Modifications of boiler construction, or of tube systems, dependent on installation of combustion apparatus; Arrangements of dispositions of combustion apparatus
    • F22B31/08Installation of heat-exchange apparatus or of means in boilers for heating air supplied for combustion
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22GSUPERHEATING OF STEAM
    • F22G1/00Steam superheating characterised by heating method
    • F22G1/02Steam superheating characterised by heating method with heat supply by hot flue gases from the furnace of the steam boiler
    • F22G1/04Steam superheating characterised by heating method with heat supply by hot flue gases from the furnace of the steam boiler by diverting flow or hot flue gases to separate superheaters operating in reheating cycle, e.g. for reheating steam between a high-pressure turbine stage and an intermediate turbine stage

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Air Supply (AREA)

Abstract

The invention discloses a kind of membrane wall list drum marine boiler, including:Membrane wall burner hearth, membrane wall convection current smoke-box and drum, drum is arranged on the top of membrane wall burner hearth, the top of membrane wall burner hearth sets burner, the bottom of membrane wall burner hearth is connected with the bottom of membrane wall convection current smoke-box, high temperature superheater is disposed with from the bottom to top in membrane wall convection current smoke-box, low temperature superheater, high-temperature economizer, middle temperature economizer, low-level (stack-gas) economizer, flue gas discharge opening is provided with the top of membrane wall convection current smoke-box, the high-temperature flue gas entered in membrane wall convection current smoke-box successively with high temperature superheater, low temperature superheater, high-temperature economizer, middle temperature economizer, discharged after low-level (stack-gas) economizer heat exchange from flue gas discharge opening.It is an advantage of the invention that:The installing space of whole boiler plant can be greatly reduced, so as to effectively solve the nervous technical problem of ship installing space, and the heat energy of high-temperature flue gas can be made further to be made full use of.

Description

Membrane wall list drum marine boiler
Technical field
The present invention relates to marine boiler field, more particularly to membrane wall list drum marine boiler.
Background technology
Traditional membrane wall list drum marine boiler, its structure includes:Burner hearth, convection current smoke-box and drum, burner hearth and convection current Smoke-box horizontal direction arranges and is connected that the side of burner hearth is provided with burner, and drum is arranged on the top of burner hearth, convection current smoke-box The interior horizontally disposed crude oil having in high-temperature economizer, middle temperature economizer, low-level (stack-gas) economizer, burner hearth, gas are produced through burner combustion High-temperature flue gas enter in convection current smoke-box, the high-temperature flue gas horizontal motion in convection current smoke-box successively with high-temperature economizer, After middle temperature economizer, low-level (stack-gas) economizer heat exchange, then discharged out of convection current smoke-box.
There is following defect in traditional membrane wall list drum marine boiler:First, required installing space is big, and this is to ship pole Very high requirement is proposed for limited space.2nd, heat utilization rate is low.
The content of the invention
The purpose of the present invention is:Offer is a kind of to greatly improve the film of heat utilization rate and the effectively save installing space of energy Formula wall list drum marine boiler.
To achieve the above object, the technical solution adopted by the present invention is:Membrane wall list drum marine boiler, including:Membrane type Fireplace thorax, membrane wall convection current smoke-box and drum, drum are arranged on the top of membrane wall burner hearth, and the top of membrane wall burner hearth is set Burner, the bottom of membrane wall burner hearth is connected with the bottom of membrane wall convection current smoke-box, in membrane wall convection current smoke-box from the bottom to top It is disposed with high temperature superheater, low temperature superheater, high-temperature economizer, middle temperature economizer, low-level (stack-gas) economizer, membrane wall convection current cigarette Flue gas discharge opening is provided with the top of room, the high-temperature flue gas entered in membrane wall convection current smoke-box successively with high temperature superheater, low Discharged after warm superheater, high-temperature economizer, middle temperature economizer, low-level (stack-gas) economizer heat exchange from flue gas discharge opening.
Further, foregoing membrane wall list drum marine boiler, wherein, low-level (stack-gas) economizer, middle temperature economizer, high temperature are saved Coal device be sequentially connected it is logical, outside feedwater to low-level (stack-gas) economizer, high-temperature economizer feeds water to drum.
Further, foregoing membrane wall list drum marine boiler, wherein, low temperature superheater is connected with high temperature superheater Logical, the saturated vapor of drum output is supplied to low temperature superheater, and high temperature superheater outwards exports superheated steam.
Further, foregoing membrane wall list drum marine boiler, wherein, the flue gas row at the top of membrane wall convection current smoke-box Export for connecting chimney.
It is an advantage of the invention that:First, burner is arranged in the top of membrane wall burner hearth and membrane wall convection current smoke-box High temperature superheater, low temperature superheater, high-temperature economizer, middle temperature economizer, low-level (stack-gas) economizer arrange from bottom to top successively, this structure The installing space of whole boiler plant can be greatly reduced, so as to effectively solve the nervous technical problem of ship installing space.2nd, Due to being provided with low temperature superheater and high temperature superheater in membrane wall convection current smoke-box, this causes membrane wall stove chamber inner combustion to produce The heat energy of high-temperature flue gas further made full use of.
Brief description of the drawings
Fig. 1 is the structural representation of membrane wall list drum marine boiler of the present invention.
Embodiment
The present invention is described in further detail with preferred embodiment below in conjunction with the accompanying drawings.
As shown in figure 1, membrane wall list drum marine boiler, including:Membrane wall burner hearth 1, membrane wall convection current smoke-box 2 and pot Cylinder 3, drum 3 is arranged on the top of membrane wall burner hearth 1, and the top of membrane wall burner hearth 1 sets burner 4, the bottom of membrane wall burner hearth 1 Portion is connected with the bottom of membrane wall convection current smoke-box 2, and high temperature superheater is disposed with from the bottom to top in membrane wall convection current smoke-box 2 5th, low temperature superheater 6, high-temperature economizer 7, middle temperature economizer 8, low-level (stack-gas) economizer 9, the top of membrane wall convection current smoke-box 2 is provided with Flue gas discharge opening 10, flue gas discharge opening 10 is used to connect chimney.The high-temperature flue gas entered in membrane wall convection current smoke-box 2 successively with Discharged after high temperature superheater 5, low temperature superheater 6, high-temperature economizer 7, middle temperature economizer 8, the heat exchange of low-level (stack-gas) economizer 9 from flue gas Mouth 10 is discharged.In the present embodiment, low-level (stack-gas) economizer 9, middle temperature economizer 8, high-temperature economizer 7 be sequentially connected it is logical, outside feedwater extremely Low-level (stack-gas) economizer 9, high-temperature economizer 7 feeds water to drum 3, and low temperature superheater 6 is connected with high temperature superheater 5, what drum 3 was exported Saturated vapor is supplied to low temperature superheater 6, and high temperature superheater 5 outwards exports superheated steam.
The flue gas flow of membrane wall list drum marine boiler is as follows:After burner 4 is lighted a fire, the crude oil in membrane wall burner hearth 1 The high-temperature flue gas that gas burning is produced is entered in membrane wall convection current smoke-box 2.The high-temperature flue gas entered in membrane wall convection current smoke-box 2 During flowing up successively with high temperature superheater 5, low temperature superheater 6, high-temperature economizer 7, middle temperature economizer 8, low temperature Economizer 9 carries out heat exchange, completes the flue gas after heat exchange and is discharged by the flue gas discharge opening 10 at the top of membrane wall convection current smoke-box 2 To chimney, then discharged by chimney.
The carbonated drink flow of membrane wall list drum marine boiler is as follows:Feed water to low-level (stack-gas) economizer 9, low-level (stack-gas) economizer 9 outside In water sequentially enter middle temperature economizer 8, high-temperature economizer 7, this process reclaimed water is constantly absorbed after the heat of high-temperature flue gas constantly Saturated vapor in heating, hot water supply in high-temperature economizer 7 to drum 3, drum 3 is supplied to low temperature superheater 6, low temperature mistake Steam in hot device 6 is entered back into high temperature superheater 5, and saturated vapor constantly absorbs the heat in high-temperature flue gas and shape during this Into superheated steam, high temperature superheater 5 outwards exports superheated steam.
The advantage of the invention is that:First, burner 4 is arranged on top and the membrane wall convection current smoke-box of membrane wall burner hearth 1 High temperature superheater 5, low temperature superheater 6, high-temperature economizer 7, middle temperature economizer 8, low-level (stack-gas) economizer 9 in 2 are successively from bottom to top Arrangement, this structure can greatly reduce the installing space of whole boiler plant, so as to effectively solve ship installing space anxiety Technical problem.2nd, it is full in low temperature superheater 6 and high temperature superheater 5, drum 3 due to being provided with membrane wall convection current smoke-box 2 With steam through low temperature superheater 6 and the formation superheated steam of high temperature superheater 5, this causes the height that burning is produced in membrane wall burner hearth 1 The heat energy of warm flue gas is further made full use of.

Claims (4)

1. membrane wall list drum marine boiler, including:Membrane wall burner hearth, membrane wall convection current smoke-box and drum, drum are arranged on The top of membrane wall burner hearth, it is characterised in that:The top of membrane wall burner hearth sets burner, the bottom of membrane wall burner hearth and membrane type The bottom of wall convection current smoke-box is connected, and high temperature superheater, cryogenic overheating are disposed with from the bottom to top in membrane wall convection current smoke-box Flue gas discharge opening is provided with the top of device, high-temperature economizer, middle temperature economizer, low-level (stack-gas) economizer, membrane wall convection current smoke-box, is entered High-temperature flue gas in membrane wall convection current smoke-box saves coal with high temperature superheater, low temperature superheater, high-temperature economizer, Zhong Wen successively Discharged after device, low-level (stack-gas) economizer heat exchange from flue gas discharge opening.
2. membrane wall list drum marine boiler according to claim 1, it is characterised in that:Low-level (stack-gas) economizer, Zhong Wen save coal Device, high-temperature economizer be sequentially connected it is logical, outside feedwater to low-level (stack-gas) economizer, high-temperature economizer feeds water to drum.
3. membrane wall list drum marine boiler according to claim 2, it is characterised in that:Low temperature superheater and hyperthermia and superheating Device is connected, and the saturated vapor of drum output is supplied to low temperature superheater, and high temperature superheater outwards exports superheated steam.
4. membrane wall list drum marine boiler according to claim 2, it is characterised in that:At the top of membrane wall convection current smoke-box Flue gas discharge opening is used to connect chimney.
CN201710311334.4A 2017-05-05 2017-05-05 Membrane wall list drum marine boiler Pending CN106996552A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710311334.4A CN106996552A (en) 2017-05-05 2017-05-05 Membrane wall list drum marine boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710311334.4A CN106996552A (en) 2017-05-05 2017-05-05 Membrane wall list drum marine boiler

Publications (1)

Publication Number Publication Date
CN106996552A true CN106996552A (en) 2017-08-01

Family

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Family Applications (1)

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CN201710311334.4A Pending CN106996552A (en) 2017-05-05 2017-05-05 Membrane wall list drum marine boiler

Country Status (1)

Country Link
CN (1) CN106996552A (en)

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1153550A (en) * 1994-06-30 1997-07-02 阿尔博格船用锅炉股份有限公司(阿尔博格工业股份有限公司) Marine boiler
CN1989387A (en) * 2004-04-01 2007-06-27 奥尔堡工业有限公司 Heat exchanger and boiler comprising the heat exchanger
CN101067489A (en) * 2007-06-07 2007-11-07 江苏双良锅炉有限公司 Film type wall sealing dry coke quenching waste heat boiler
CN201237336Y (en) * 2008-07-03 2009-05-13 河南华阳装备制造有限公司 Top-blowing type oil-burning boiler
CN102182996A (en) * 2011-03-29 2011-09-14 张家港格林沙洲锅炉有限公司 Top spraying type fuel oil and waste gas combined boiler
CN104390200A (en) * 2014-11-21 2015-03-04 张家港格林沙洲锅炉有限公司 Marine exhaust gas waste heat boiler
CN105042556A (en) * 2015-05-27 2015-11-11 西安交通大学 Burner-overhead vertical U-structured oil and gas boiler
CN206739252U (en) * 2017-05-05 2017-12-12 张家港格林沙洲锅炉有限公司 Membrane wall list drum marine boiler

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1153550A (en) * 1994-06-30 1997-07-02 阿尔博格船用锅炉股份有限公司(阿尔博格工业股份有限公司) Marine boiler
CN1989387A (en) * 2004-04-01 2007-06-27 奥尔堡工业有限公司 Heat exchanger and boiler comprising the heat exchanger
CN101067489A (en) * 2007-06-07 2007-11-07 江苏双良锅炉有限公司 Film type wall sealing dry coke quenching waste heat boiler
CN201237336Y (en) * 2008-07-03 2009-05-13 河南华阳装备制造有限公司 Top-blowing type oil-burning boiler
CN102182996A (en) * 2011-03-29 2011-09-14 张家港格林沙洲锅炉有限公司 Top spraying type fuel oil and waste gas combined boiler
CN104390200A (en) * 2014-11-21 2015-03-04 张家港格林沙洲锅炉有限公司 Marine exhaust gas waste heat boiler
CN105042556A (en) * 2015-05-27 2015-11-11 西安交通大学 Burner-overhead vertical U-structured oil and gas boiler
CN206739252U (en) * 2017-05-05 2017-12-12 张家港格林沙洲锅炉有限公司 Membrane wall list drum marine boiler

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Application publication date: 20170801