WO2018049703A1 - Ethanol dehydration steam heating device - Google Patents

Ethanol dehydration steam heating device Download PDF

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Publication number
WO2018049703A1
WO2018049703A1 PCT/CN2016/101440 CN2016101440W WO2018049703A1 WO 2018049703 A1 WO2018049703 A1 WO 2018049703A1 CN 2016101440 W CN2016101440 W CN 2016101440W WO 2018049703 A1 WO2018049703 A1 WO 2018049703A1
Authority
WO
WIPO (PCT)
Prior art keywords
combustion chamber
steam
disposed
flue
chamber
Prior art date
Application number
PCT/CN2016/101440
Other languages
French (fr)
Chinese (zh)
Inventor
孙明华
王建平
王兆民
Original Assignee
江苏金牛环保工程设备有限公司
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 江苏金牛环保工程设备有限公司 filed Critical 江苏金牛环保工程设备有限公司
Publication of WO2018049703A1 publication Critical patent/WO2018049703A1/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/04Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste liquors, e.g. sulfite liquors
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22GSUPERHEATING OF STEAM
    • F22G1/00Steam superheating characterised by heating method
    • F22G1/16Steam superheating characterised by heating method by using a separate heat source independent from heat supply of the steam boiler, e.g. by electricity, by auxiliary combustion of fuel oil
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22GSUPERHEATING OF STEAM
    • F22G7/00Steam superheaters characterised by location, arrangement, or disposition
    • F22G7/12Steam superheaters characterised by location, arrangement, or disposition in flues
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J13/00Fittings for chimneys or flues 
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00Arrangements of devices for treating smoke or fumes
    • F23J15/06Arrangements of devices for treating smoke or fumes of coolers
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/30Technologies for a more efficient combustion or heat usage

Definitions

  • the present invention relates to an incineration heating furnace in an ethylene oxide plant.
  • the prior art heating furnace basically adopts the structural form of a tubular heating furnace.
  • the furnace has a low temperature surface of the furnace tube, the incineration of organic matter is incomplete, the convection heat exchange efficiency is low, the exhaust temperature of the heating furnace is high, and the heat efficiency is low.
  • An alcohol dehydration steam heating device comprising a horizontal furnace body, characterized in that the furnace body is sequentially divided into a front stage combustion chamber, a middle stage radiant heating chamber, and a rear stage convection heating chamber, and the combustion chamber and the radiant heating chamber
  • the porous heat storage wall is separated, the radiant heating chamber is provided with a radiant heater, the radiant heater is provided with steam inlet and outlet, and the convection heating chamber is provided with a vertical upward flue at the top of the convection heating chamber, and a plurality of heat exchangers are arranged at intervals above and below the flue.
  • a plurality of heat exchangers are sequentially connected in series by a steam pipe, and the bottom heat exchanger is connected to the radiant heater through a steam pipe, a burner inlet is arranged at the front end of the combustion chamber, and a waste liquid gun inlet is arranged at a front end of the combustion chamber side wall.
  • the waste steam inlet and the circulating air supply device, the circulating air supply device comprises a hot air circulation pipe which is connected and connected to the side wall of the combustion chamber, and a hot air intake pipe which is arranged tangentially to the hot air circulation pipe, and is located on the combustion chamber side in the hot air circulation pipe An air hole is arranged around the center of the wall, and the air supply hole is connected to the combustion chamber.
  • the porous heat storage wall increases the radiant heat of the furnace to increase the temperature of the steam outlet of the radiant section, and also avoids the direct contact of the burner flame with the U-shaped tube of the radiant section, and prolongs the service life of the U-shaped tube of the radiant section. In short, energy efficient recycling of heat energy.
  • the waste steam inlet is provided with a waste steam mixing distributor, and the waste steam mixing distributor comprises a vertical cylinder, a hot air inlet tangentially connected to the vertical cylinder, and waste steam disposed at the center of the vertical cylinder
  • the waste steam inlet pipe extends into the near bottom end of the vertical cylinder, and the waste steam inlet pipe is evenly distributed around the center of the pipe. Fan-shaped guide piece.
  • the improvement of the circulation air supply device can help the waste steam to be tangentially entered by the waste steam mixing distributor to produce better swirl mixing and full combustion.
  • the air-filling hole is inclined, and is inclined at an angle of 15 degrees with respect to the vertical direction and rotates along the center of the combustion chamber.
  • the fan-shaped guide piece has a spread angle of 60 degrees, and each of the sector-shaped guide pieces is rotated by 26 degrees with the needle.
  • the combustion chamber material is cast from an outer metal casing and an inner steel jade, and the combustion chamber is provided with at least one convex ring at a rear end thereof to form a zoom structure at the rear end of the combustion chamber.
  • the radiant heater adopts a U-tube heat exchanger
  • the U-tube heat exchanger comprises a U-shaped tube bundle in the radiant heating chamber and a top tube box communicating with the U-shaped tube bundle, and the steam inlet is arranged on the tube box And the steam outlet, the steam inlet is connected to the bottom heat exchanger.
  • a baffle plate through which the flue gas passes between the U-shaped tube bundles is disposed below the U-shaped tube bundle.
  • the bottom end of the convection heating chamber is provided with an inclined flow path baffle.
  • the flue is formed by splicing several layers, and a heater is disposed on each of the flue.
  • a flue connecting pipe is disposed between the upper and lower flue pipes, and the flue connecting pipe comprises a cylindrical body, preferably a cylindrical portion, an expansion joint, a lining plate on the inner side of the expansion joint, and a ceramic fiber lining.
  • the invention effectively utilizes thermal energy, saves natural gas and fuel, and burns fully, and achieves harmless discharge.
  • 1 is a plan view of the present invention.
  • FIG. 2 is a cross-sectional view taken along line A-A of FIG. 1.
  • FIG. 3 is a cross-sectional view taken along line B-B of FIG. 1.
  • FIG. 4 is a left side view of FIG. 2.
  • FIG. 5 is a front elevational view of the exhaust gas mixer of FIG. 2.
  • FIG. 6 is a plan view of FIG. 5.
  • 8 is a schematic view of the sector guide piece of FIG. 5.
  • FIG. 9 is a partial enlarged view of FIG. 5.
  • FIG. 10 is a schematic view of a flue connecting pipe.
  • FIG. 11 is a schematic view of the steam pipe of FIG. 2.
  • Embodiment 1 An alcohol dehydration steam heating device, comprising a horizontal furnace body 1, the furnace body 1 is sequentially divided into a front stage combustion chamber 1.1, a middle stage radiant heating chamber 1.2, and a rear stage convection heating chamber 1.3, burning Room 1.1 is a horizontal round straight cylinder.
  • the material of the combustion chamber 1.1 is made of metal shell of external Q235B and internal steel jade.
  • the radiant heating chamber 1.2 and the convection heating chamber 1.3 are made of external Q235B metal shell and internal ceramic fiber cotton lump. Made.
  • the proximal end of the combustion chamber 1.1 is provided with two convex rings 1.1.1, and the convex ring 1.1.1 is made of refractory material, so that the rear end of the combustion chamber 1.1 forms a scaled structure.
  • the combustion chamber 1.1 and the radiant heating chamber 1.2 are separated by a ceramic porous heat storage wall 1.4, the radiant heating chamber 1.2 is provided with a radiant heater 2, the radiant heater 2 is a U-tube heat exchanger, and the U-tube heat exchanger includes radiation.
  • the upper portion of the tube box 2.2 is provided with a steam inlet 2.2.1 and a steam outlet 2.2.2, and the top of the convection heating chamber 1.3 is vertically disposed.
  • the flue 3 is formed by splicing eight, B, C, D, and four layers, and a heat exchanger 4 is disposed on each of the flues 3.
  • the heat exchanger 4 material 304 is provided with a flue connecting pipe 5 between the upper and lower flue pipes 3, and the flue connecting pipe 5 includes the cylindrical body 5.1, the expansion joint 5.2 on the cylindrical body 5.1, the inner liner 5.3 of the expansion joint 5.2, and the ceramic. Fiber lining 5.4.
  • the four heat exchangers 4 are connected in series by a steam line 6, and the steam inlet 2.2.1 of the tank 2.2 is connected to the bottommost heat exchanger 4.
  • the front end of the combustion chamber 1.1 is provided with a burner inlet 1.1.2, and the side wall of the combustion chamber 1.1 is provided with a waste liquid gun inlet, a waste steam inlet 1.1.3, a flame observation port, a meter insertion port (a temperature detection port, a negative pressure detection port).
  • the circulating air supply device 7 is distributed at a position 1500 mm backward of the front end of the combustion chamber 1.1, and the circulating air supply device 7 includes a hot air circulation pipe 7.1 surrounding the side wall of the combustion chamber 1.1 and sealingly connected thereto, and the hot air Circulating pipe 7.1 tangentially set hot air intake pipe 7.2, located on the side wall of the combustion chamber 1.1 in the hot air circulation pipe 7.1, around the center of the circle, there is a venting hole 7.3, the venting hole 7.3 is inclined, and the inclination angle is 15 degrees from the vertical direction. And rotates 62.5 degrees along the center of the combustion chamber 1.1, and the air supply hole 7.3 communicates with the combustion chamber 1.1.
  • the rear side of the device 7 is provided with a waste steam mixing distributor 8 comprising a vertical cylinder 8.1, a hot air inlet 8.2 tangentially connected to the vertical cylinder 8.1, and a center of the vertical cylinder 8.1
  • the waste steam inlet pipe 8.3, the waste steam inlet pipe 8.3 extends into the near bottom end of the vertical cylinder 8.1, and the waste steam inlet pipe 8.3 end is evenly distributed with eight sector-shaped guide pieces 8.4 around the center of the circle.
  • the fan-shaped guide piece 8.4 has an angle of 60 degrees, and each of the sector-shaped guide pieces 8.1 is mounted with a 26-degree rotation of the needle.
  • a deflector baffle 9 for passing the flue gas from between the U-shaped tube bundles 2.1.
  • the bottom end of the convection heating chamber 1.3 is provided with a flow path baffle 1.3.1 inclined at 35°.
  • the steam pipe 6 is a bent pipe structure, and an expansion joint 6.1 is disposed on the pipe body.
  • the material of the A, B, C and D flue 3 is Q235B/ceramic fiber lump, which is made of hanging fiber cotton lump, sealed as a looper flange and gland, including each layer of flue 3 shell There is a 35° deflector 3.1 to change the direction of the flue gas, so that the heat exchanger 4 and the flue gas fully exchange heat.
  • Process steam (pipe layer), perforated tube sheet, finned tube, head, etc., its material is selected according to the flue gas temperature in each layer of flue (A material 316, B material 321, C material 3 04, D material 304)
  • Each layer of flue 3 has a spring bracket 3.2 outside the shell, and the spring bracket 3.2 is symmetrically arranged, which reduces the thermal deformation of the equipment and the high temperature steam pipe, greatly improves the heat transfer efficiency of the convection section, and the top of the D layer flue 3
  • the soft water heater is provided, and the heating structure of the pressure vessel of the soft water heater is changed to the structure of the high-pressure pipeline in the outer finned tube of the tube, which simplifies the structure and manufacturing difficulty of the soft water heater, and the above furnace body and heater The structure and combination increase the heating efficiency of the incinerator and reduce fuel consumption.
  • the combustion chamber in the front stage, the radiant heating chamber in the middle stage, and the convection heating chamber in the rear stage are an integral structure or a segmented splicing structure.
  • the entire apparatus of the present invention operates under negative pressure (-lOOpa).

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Combustion Of Fluid Fuel (AREA)
  • Drying Of Solid Materials (AREA)

Abstract

An ethanol dehydration steam heating device comprises a horizontal furnace (1), comprising, in order, a combustion chamber (1.1) at a front section, a radiant heating chamber (1.2) at a middle section, and a convection heating chamber (1.3) at a rear section. The combustion chamber (1.1) is separated from the radiant heating chamber (1.2) by a porous heat storage wall (1.4). A radiant heater (2) is disposed in the radiant heating chamber (1.2). A steam inlet (2.2.1) and a steam outlet (2.2.2) are disposed on the radiant heater (2). A vertical flue (3) is disposed at the top of the convection heating chamber (1.3). Heat exchangers (4) are disposed along the flue (3) and vertically spaced apart. The heat exchangers (4) are concatenated in order by a steam pipeline (6). The lowest heat exchanger (4) is connected to the radiant heater (2) by the steam pipeline (6). A front end of the combustion chamber (1.1) is provided with a burner inlet (1.1.2). A waste liquid gun inlet, a waste steam inlet (1.1.3), and a circulating air supplementation device (7) are disposed on a sidewall close to the front end of the combustion chamber (1.1). The circulating air supplementation device (7) comprises a hot air circulation pipeline (7.1) surrounding the sidewall of the combustion chamber (1.1) and connected thereto in a sealed manner and a hot air inlet pipe (7.2) disposed to be tangential to the hot air circulation pipeline (7.1). Air supplementation holes (7.3) surrounding the center of a circle are disposed on the sidewall of the combustion chamber (1.1) in the hot air circulation pipeline (7.1). The air supplementation holes (7.3) communicate with the combustion chamber (1.1).

Description

一种酒精脱水蒸汽加热装置  Alcohol dehydration steam heating device
技术领域  Technical field
[0001] 本发明涉及环氧乙烷装置中的焚烧加热炉。  [0001] The present invention relates to an incineration heating furnace in an ethylene oxide plant.
背景技术  Background technique
[0002] 现有技术的加热炉基本采用管式加热炉的结构形式。  [0002] The prior art heating furnace basically adopts the structural form of a tubular heating furnace.
技术问题  technical problem
[0003] 炉内存在炉管低温面, 有机物焚烧不完全, 对流换热效率底, 加热炉排烟温度 高, 热效率低。 问题的解决方案  [0003] The furnace has a low temperature surface of the furnace tube, the incineration of organic matter is incomplete, the convection heat exchange efficiency is low, the exhaust temperature of the heating furnace is high, and the heat efficiency is low. Problem solution
技术解决方案  Technical solution
[0004] 一种酒精脱水蒸汽加热装置, 包括卧式炉体, 其特征在于炉体依次分为前段的 燃烧室、 中段的辐射加热室以及后段的对流加热室, 燃烧室与辐射加热室以多 孔蓄热墙分隔, 辐射加热室内设置有辐射加热器, 辐射加热器上置有蒸汽进、 出口, 对流加热室顶端设置有竖直向上的烟道, 烟道上下间隔设置有若干个换 热器, 若干个换热器通过蒸汽管道顺次串接, 最底端的换热器通过蒸汽管道连 接辐射加热器, 燃烧室前端设置有燃烧机进口, 燃烧室侧壁近前端设置有废液 枪进口、 废蒸汽进口以及循环补风装置, 循环补风装置包括围绕燃烧室侧壁并 与之密封连接的热风循环管道、 与热风循环管道切向设置的热风进气管, 位于 热风循环管道内的燃烧室侧壁上围绕圆心幵设有补气孔, 补气孔与燃烧室连通  [0004] An alcohol dehydration steam heating device, comprising a horizontal furnace body, characterized in that the furnace body is sequentially divided into a front stage combustion chamber, a middle stage radiant heating chamber, and a rear stage convection heating chamber, and the combustion chamber and the radiant heating chamber The porous heat storage wall is separated, the radiant heating chamber is provided with a radiant heater, the radiant heater is provided with steam inlet and outlet, and the convection heating chamber is provided with a vertical upward flue at the top of the convection heating chamber, and a plurality of heat exchangers are arranged at intervals above and below the flue. a plurality of heat exchangers are sequentially connected in series by a steam pipe, and the bottom heat exchanger is connected to the radiant heater through a steam pipe, a burner inlet is arranged at the front end of the combustion chamber, and a waste liquid gun inlet is arranged at a front end of the combustion chamber side wall. The waste steam inlet and the circulating air supply device, the circulating air supply device comprises a hot air circulation pipe which is connected and connected to the side wall of the combustion chamber, and a hot air intake pipe which is arranged tangentially to the hot air circulation pipe, and is located on the combustion chamber side in the hot air circulation pipe An air hole is arranged around the center of the wall, and the air supply hole is connected to the combustion chamber.
[0005] 多孔蓄热墙是增加了炉膛的辐射热量, 以提高辐射段蒸汽出口温度, 也为了避 免燃烧器火焰直接接触到辐射段 U型管, 延长辐射段 U型管的使用寿命。 总之节 能高效热能循环回收。 [0005] The porous heat storage wall increases the radiant heat of the furnace to increase the temperature of the steam outlet of the radiant section, and also avoids the direct contact of the burner flame with the U-shaped tube of the radiant section, and prolongs the service life of the U-shaped tube of the radiant section. In short, energy efficient recycling of heat energy.
[0006] 作为优选, 废蒸汽进口设置有废蒸汽混合分布器, 废蒸汽混合分布器包括竖直 筒体、 与竖直筒体切向连接的热风进口、 设置于竖直筒体中心的废蒸汽进管, 废蒸汽进管伸入竖直筒体近底端, 废蒸汽进管末端围绕圆心均匀布设有若干块 扇形导向片。 [0006] Preferably, the waste steam inlet is provided with a waste steam mixing distributor, and the waste steam mixing distributor comprises a vertical cylinder, a hot air inlet tangentially connected to the vertical cylinder, and waste steam disposed at the center of the vertical cylinder In the inlet pipe, the waste steam inlet pipe extends into the near bottom end of the vertical cylinder, and the waste steam inlet pipe is evenly distributed around the center of the pipe. Fan-shaped guide piece.
[0007] 通过循环补风装置的改进, 可帮助废蒸汽由废蒸汽混合分布器切向进入后产生 更好的旋流混合, 充分燃烧。  [0007] The improvement of the circulation air supply device can help the waste steam to be tangentially entered by the waste steam mixing distributor to produce better swirl mixing and full combustion.
[0008] 作为优选, 补气孔倾斜幵设, 与竖直方向倾斜角度为 15度并沿燃烧室圆心旋转[0008] Preferably, the air-filling hole is inclined, and is inclined at an angle of 15 degrees with respect to the vertical direction and rotates along the center of the combustion chamber.
62.5度。 62.5 degrees.
[0009] 作为优选, 扇形导向片的展幵角度为 60度, 每块扇形导向片均顺吋针旋转 26度 安装。  [0009] Preferably, the fan-shaped guide piece has a spread angle of 60 degrees, and each of the sector-shaped guide pieces is rotated by 26 degrees with the needle.
[0010] 作为优选, 燃烧室材质由外部金属外壳以及内部钢玉料浇注而成, 燃烧室近后 端设置有至少一个凸环, 使燃烧室后端形成缩放式结构。  [0010] Preferably, the combustion chamber material is cast from an outer metal casing and an inner steel jade, and the combustion chamber is provided with at least one convex ring at a rear end thereof to form a zoom structure at the rear end of the combustion chamber.
[0011] 作为优选, 辐射加热器采用 U型管换热器, U型管换热器包括辐射加热室内的 U 型管束以及与 U型管束连通的顶端管箱, 管箱上幵设有蒸汽进口和蒸汽出口, 蒸 汽进口与最底端的换热器连接。  [0011] Preferably, the radiant heater adopts a U-tube heat exchanger, and the U-tube heat exchanger comprises a U-shaped tube bundle in the radiant heating chamber and a top tube box communicating with the U-shaped tube bundle, and the steam inlet is arranged on the tube box And the steam outlet, the steam inlet is connected to the bottom heat exchanger.
[0012] 作为优选, U型管束下方设置有使烟气从 U型管束间穿过的导流档板。  [0012] Preferably, a baffle plate through which the flue gas passes between the U-shaped tube bundles is disposed below the U-shaped tube bundle.
[0013] 作为优选, 对流加热室末端底部设置有倾斜流道挡板。  [0013] Preferably, the bottom end of the convection heating chamber is provided with an inclined flow path baffle.
[0014] 作为优选, 烟道由若干层拼接而成, 每层烟道上设置有一加热器。  [0014] Preferably, the flue is formed by splicing several layers, and a heater is disposed on each of the flue.
[0015] 作为优选, 上下两层烟道间设置有烟道连接管, 烟道连接管包括筒体、 筒体上 的作为优选, 膨胀节、 膨胀节内侧的衬板以及陶瓷纤维内衬。  [0015] Preferably, a flue connecting pipe is disposed between the upper and lower flue pipes, and the flue connecting pipe comprises a cylindrical body, preferably a cylindrical portion, an expansion joint, a lining plate on the inner side of the expansion joint, and a ceramic fiber lining.
发明的有益效果  Advantageous effects of the invention
有益效果  Beneficial effect
[0016] 本发明有效利用热能, 节约天然气和燃料, 燃烧充分, 达到无害化达标排放。  [0016] The invention effectively utilizes thermal energy, saves natural gas and fuel, and burns fully, and achieves harmless discharge.
对附图的简要说明  Brief description of the drawing
附图说明  DRAWINGS
[0017] 图 1为本发明俯视图。  1 is a plan view of the present invention.
[0018] 图 2为图 1的 A-A剖视图。  2 is a cross-sectional view taken along line A-A of FIG. 1.
[0019] 图 3为图 1的 B-B剖视图。  3 is a cross-sectional view taken along line B-B of FIG. 1.
[0020] 图 4为图 2的左视图。  4 is a left side view of FIG. 2.
[0021] 图 5为图 2中废气混合器主视图。  [0021] FIG. 5 is a front elevational view of the exhaust gas mixer of FIG. 2.
[0022] 图 6为图 5的俯视图。 [0023] 图 8为图 5的扇形导向片示意图。 6 is a plan view of FIG. 5. 8 is a schematic view of the sector guide piece of FIG. 5.
[0024] 图 9为图 5的局部放大图。  9 is a partial enlarged view of FIG. 5.
[0025] 图 10为烟道连接管示意图。  [0025] FIG. 10 is a schematic view of a flue connecting pipe.
[0026] 图 11为图 2中蒸汽管道示意图。  11 is a schematic view of the steam pipe of FIG. 2.
实施该发明的最佳实施例  BEST MODE FOR CARRYING OUT THE INVENTION
本发明的最佳实施方式  BEST MODE FOR CARRYING OUT THE INVENTION
[0027] 实施例 1 : 一种酒精脱水蒸汽加热装置, 包括卧式炉体 1, 炉体 1依次分为前段 的燃烧室 1.1、 中段的辐射加热室 1.2以及后段的对流加热室 1.3, 燃烧室 1.1为卧 式圆形直筒, 燃烧室 1.1材质由外部 Q235B的金属外壳以及内部钢玉料浇注而成 , 辐射加热室 1.2以及对流加热室 1.3材质由外部 Q235B金属外壳以及内部陶瓷纤 维棉块组合而成。 燃烧室 1.1近后端设置有两个凸环 1.1.1, 凸环 1.1.1为耐火材料 制成, 使燃烧室 1.1后端形成缩放式结构。 燃烧室 1.1与辐射加热室 1.2以陶瓷料多 孔蓄热墙 1.4分隔, 辐射加热室 1.2内设置有辐射加热器 2, 辐射加热器 2采用 U型 管换热器, U型管换热器包括辐射加热室 1.2内的 U型管束 2.1以及与 U型管束 2.1连 通的顶端管箱 2.2, 管箱 2.2上幵设有蒸汽进口 2.2.1和蒸汽出口 2.2.2, 对流加热室 1.3顶端设置有竖直向上的烟道 3, 烟道 3由八、 B、 C、 D, 4层拼接而成, 每层烟 道 3上设置有一换热器 4。 A层烟道 3上的换热器 4材质 316、 B层烟道 3上的换热器 4 材质 321、 C层烟道 3上的换热器 4材质 304、 D层烟道 3上的换热器 4材质 304, 上下 两层烟道 3间设置有烟道连接管 5, 烟道连接管 5包括筒体 5.1、 筒体 5.1上的膨胀 节 5.2、 膨胀节 5.2内侧的衬板 5.3以及陶瓷纤维内衬 5.4。 4个换热器 4通过蒸汽管 道 6顺次串接, 管箱 2.2的蒸汽进口 2.2.1与最底端的换热器 4连接。 燃烧室 1.1前端 设置有燃烧机进口 1.1.2, 燃烧室 1.1侧壁近前端设置有废液枪进口、 废蒸汽进口 1 .1.3、 火焰观察口、 仪表插入口 (温度检测口、 负压检测口) 以及循环补风装置 7, 循环补风装置 7分布在燃烧室 1.1前端向后 1500mm的位置, 循环补风装置 7包 括围绕燃烧室 1.1侧壁并与之密封连接的热风循环管道 7.1、 与热风循环管道 7.1切 向设置的热风进气管 7.2, 位于热风循环管道 7.1内的燃烧室 1.1侧壁上围绕圆心幵 设有补气孔 7.3, 补气孔 7.3倾斜幵设, 与竖直方向倾斜角度为 15度并沿燃烧室 1.1 圆心旋转 62.5度, 补气孔 7.3与燃烧室 1.1连通。 废蒸汽进口 1.1.3设置于循环补风 装置 7后侧并设置有废蒸汽混合分布器 8, 废蒸汽混合分布器 8包括竖直筒体 8.1、 与竖直筒体 8.1切向连接的热风进口 8.2、 设置于竖直筒体 8.1中心的废蒸汽进管 8. 3, 废蒸汽进管 8.3伸入竖直筒体 8.1近底端, 废蒸汽进管 8.3末端围绕圆心均匀布 设有 8块扇形导向片 8.4。 扇形导向片 8.4的展幵角度为 60度, 每块扇形导向片 8.1 均顺吋针旋转 26度安装。 U型管束 2.1下方设置有使烟气从 U型管束 2.1间穿过的导 流档板 9。 对流加热室 1.3末端底部设置有倾斜 35°的流道挡板 1.3.1。 蒸汽管道 6为 弯管结构, 管体上设置有膨胀节 6.1。 [0027] Embodiment 1: An alcohol dehydration steam heating device, comprising a horizontal furnace body 1, the furnace body 1 is sequentially divided into a front stage combustion chamber 1.1, a middle stage radiant heating chamber 1.2, and a rear stage convection heating chamber 1.3, burning Room 1.1 is a horizontal round straight cylinder. The material of the combustion chamber 1.1 is made of metal shell of external Q235B and internal steel jade. The radiant heating chamber 1.2 and the convection heating chamber 1.3 are made of external Q235B metal shell and internal ceramic fiber cotton lump. Made. The proximal end of the combustion chamber 1.1 is provided with two convex rings 1.1.1, and the convex ring 1.1.1 is made of refractory material, so that the rear end of the combustion chamber 1.1 forms a scaled structure. The combustion chamber 1.1 and the radiant heating chamber 1.2 are separated by a ceramic porous heat storage wall 1.4, the radiant heating chamber 1.2 is provided with a radiant heater 2, the radiant heater 2 is a U-tube heat exchanger, and the U-tube heat exchanger includes radiation. a U-shaped tube bundle 2.1 in the heating chamber 1.2 and a top tube box 2.2 communicating with the U-shaped tube bundle 2.1. The upper portion of the tube box 2.2 is provided with a steam inlet 2.2.1 and a steam outlet 2.2.2, and the top of the convection heating chamber 1.3 is vertically disposed. In the upward flue 3, the flue 3 is formed by splicing eight, B, C, D, and four layers, and a heat exchanger 4 is disposed on each of the flues 3. Heat exchanger 4 material 316 on layer A flue 3, heat exchanger 4 on layer B flue 3 material 321 , heat exchanger 4 material on layer C flue 3 material 304, change on D layer flue 3 The heat exchanger 4 material 304 is provided with a flue connecting pipe 5 between the upper and lower flue pipes 3, and the flue connecting pipe 5 includes the cylindrical body 5.1, the expansion joint 5.2 on the cylindrical body 5.1, the inner liner 5.3 of the expansion joint 5.2, and the ceramic. Fiber lining 5.4. The four heat exchangers 4 are connected in series by a steam line 6, and the steam inlet 2.2.1 of the tank 2.2 is connected to the bottommost heat exchanger 4. The front end of the combustion chamber 1.1 is provided with a burner inlet 1.1.2, and the side wall of the combustion chamber 1.1 is provided with a waste liquid gun inlet, a waste steam inlet 1.1.3, a flame observation port, a meter insertion port (a temperature detection port, a negative pressure detection port). And the circulating air supply device 7, the circulating air supply device 7 is distributed at a position 1500 mm backward of the front end of the combustion chamber 1.1, and the circulating air supply device 7 includes a hot air circulation pipe 7.1 surrounding the side wall of the combustion chamber 1.1 and sealingly connected thereto, and the hot air Circulating pipe 7.1 tangentially set hot air intake pipe 7.2, located on the side wall of the combustion chamber 1.1 in the hot air circulation pipe 7.1, around the center of the circle, there is a venting hole 7.3, the venting hole 7.3 is inclined, and the inclination angle is 15 degrees from the vertical direction. And rotates 62.5 degrees along the center of the combustion chamber 1.1, and the air supply hole 7.3 communicates with the combustion chamber 1.1. Waste steam import 1.1.3 set in the circulation of wind The rear side of the device 7 is provided with a waste steam mixing distributor 8 comprising a vertical cylinder 8.1, a hot air inlet 8.2 tangentially connected to the vertical cylinder 8.1, and a center of the vertical cylinder 8.1 The waste steam inlet pipe 8.3, the waste steam inlet pipe 8.3 extends into the near bottom end of the vertical cylinder 8.1, and the waste steam inlet pipe 8.3 end is evenly distributed with eight sector-shaped guide pieces 8.4 around the center of the circle. The fan-shaped guide piece 8.4 has an angle of 60 degrees, and each of the sector-shaped guide pieces 8.1 is mounted with a 26-degree rotation of the needle. Below the U-shaped tube bundle 2.1 is provided a deflector baffle 9 for passing the flue gas from between the U-shaped tube bundles 2.1. The bottom end of the convection heating chamber 1.3 is provided with a flow path baffle 1.3.1 inclined at 35°. The steam pipe 6 is a bent pipe structure, and an expansion joint 6.1 is disposed on the pipe body.
[0028] A、 B、 C、 D层烟道 3材质为 Q235B/陶瓷纤维棉块, 采用挂吊纤维棉块、 密封 为活套法兰及压盖形式, 包括每层烟道 3壳层设有 35°导流板 3.1, 以改变烟气走 向, 使换热器 4与烟气充分换热。 工艺蒸汽 (管层) , 多孔管板、 翅片管、 封头 等, 它的材质根据每层烟道内的烟气温度选材 (A材质 316、 B材质 321、 C材质 3 04、 D材质 304) 加热器, 每层烟道 3壳层外设有弹簧支架 3.2, 弹簧支架 3.2对称 设置, 减除了设备及高温蒸汽管道的热变形, 大大地提高了对流段的传热效率 , D层烟道 3顶端设置有软水加热器, 将软水加热器的压力容器的加热结构改为 管外围翅片管内可以承受高压力管道的结构, 简化了软水加热器的结构和制造 难度, 以上的炉体及加热器的结构和组合提高了焚烧加热炉的加热效率, 减少 了燃料的消耗。 [0028] The material of the A, B, C and D flue 3 is Q235B/ceramic fiber lump, which is made of hanging fiber cotton lump, sealed as a looper flange and gland, including each layer of flue 3 shell There is a 35° deflector 3.1 to change the direction of the flue gas, so that the heat exchanger 4 and the flue gas fully exchange heat. Process steam (pipe layer), perforated tube sheet, finned tube, head, etc., its material is selected according to the flue gas temperature in each layer of flue (A material 316, B material 321, C material 3 04, D material 304) Each layer of flue 3 has a spring bracket 3.2 outside the shell, and the spring bracket 3.2 is symmetrically arranged, which reduces the thermal deformation of the equipment and the high temperature steam pipe, greatly improves the heat transfer efficiency of the convection section, and the top of the D layer flue 3 The soft water heater is provided, and the heating structure of the pressure vessel of the soft water heater is changed to the structure of the high-pressure pipeline in the outer finned tube of the tube, which simplifies the structure and manufacturing difficulty of the soft water heater, and the above furnace body and heater The structure and combination increase the heating efficiency of the incinerator and reduce fuel consumption.
[0029] 前段的燃烧室、 中段的辐射加热室以及后段的对流加热室为一体式结构或分段 拼接式结构。  [0029] The combustion chamber in the front stage, the radiant heating chamber in the middle stage, and the convection heating chamber in the rear stage are an integral structure or a segmented splicing structure.
[0030] 本发明整个装置为负压运行 (-lOOpa) 。  [0030] The entire apparatus of the present invention operates under negative pressure (-lOOpa).

Claims

权利要求书 Claim
[权利要求 1] 一种酒精脱水蒸汽加热装置, 包括卧式炉体, 其特征在于炉体依次分 为前段的燃烧室、 中段的辐射加热室以及后段的对流加热室, 燃烧室 与辐射加热室以多孔蓄热墙分隔, 辐射加热室内设置有辐射加热器, 辐射加热器上置有蒸汽进、 出口, 对流加热室顶端设置有竖直向上的 烟道, 烟道上下间隔设置有若干个换热器, 若干个换热器通过蒸汽管 道顺次串接, 最底端的换热器通过蒸汽管道连接辐射加热器, 燃烧室 前端设置有燃烧机进口, 燃烧室侧壁近前端设置有废液枪进口、 废蒸 汽进口以及循环补风装置, 循环补风装置包括围绕燃烧室侧壁并与之 密封连接的热风循环管道、 与热风循环管道切向设置的热风进气管, 位于热风循环管道内的燃烧室侧壁上围绕圆心幵设有补气孔, 补气孔 与燃烧室连通。  [Attach 1] An alcohol dehydration steam heating device, comprising a horizontal furnace body, characterized in that the furnace body is sequentially divided into a front stage combustion chamber, a middle stage radiant heating chamber, and a rear stage convection heating chamber, a combustion chamber and radiant heating The chamber is separated by a porous heat storage wall. The radiant heating chamber is provided with a radiant heater. The radiant heater is provided with steam inlet and outlet. The top of the convection heating chamber is provided with a vertical upward flue, and the flue is arranged at intervals above and below. The heat exchanger, a plurality of heat exchangers are sequentially connected in series by a steam pipe, the bottom heat exchanger is connected to the radiant heater through a steam pipe, the burner inlet is provided at the front end of the combustion chamber, and the waste liquid gun is disposed at the front end of the combustion chamber side wall Imported, waste steam inlet and circulating air supply device, the circulating air supply device comprises a hot air circulation pipe which is connected around the side wall of the combustion chamber and is connected with the hot air circulation pipe which is tangentially arranged with the hot air circulation pipe, and is located in the hot air circulation pipe. An air supply hole is arranged around the center of the chamber on the side wall, and the air supply hole is connected to the combustion chamber.
[权利要求 2] 根据权利要求 1所述的一种酒精脱水蒸汽加热装置, 其特征在于废蒸 汽进口设置有废蒸汽混合分布器, 废蒸汽混合分布器包括竖直筒体、 与竖直筒体切向连接的热风进口、 设置于竖直筒体中心的废蒸汽进管 , 废蒸汽进管伸入竖直筒体近底端, 废蒸汽进管末端围绕圆心均匀布 设有若干块扇形导向片。  [Claim 2] The alcohol dehydration steam heating device according to claim 1, wherein the waste steam inlet is provided with a waste steam mixing distributor, and the waste steam mixing distributor comprises a vertical cylinder and a vertical cylinder The tangentially connected hot air inlet, the waste steam inlet pipe disposed at the center of the vertical cylinder body, the waste steam inlet pipe extends into the near bottom end of the vertical cylinder body, and a plurality of fan-shaped guide pieces are evenly distributed around the center of the waste steam inlet pipe.
[权利要求 3] 根据权利要求 1所述的一种酒精脱水蒸汽加热装置, 其特征在于补气 孔倾斜幵设, 与竖直方向倾斜角度为 15度并沿燃烧室圆心旋转 62.5度  [Attaction 3] An alcohol dehydration steam heating apparatus according to claim 1, wherein the air supply hole is inclined and inclined at an angle of 15 degrees with respect to the vertical direction and rotated by 62.5 degrees along the center of the combustion chamber.
[权利要求 4] 根据权利要求 2所述的一种酒精脱水蒸汽加热装置, 其特征在于扇形 导向片的展幵角度为 60度, 每块扇形导向片均顺吋针旋转 26度安装。 [Claim 4] An alcohol dehydration steam heating apparatus according to claim 2, wherein the fan-shaped guide piece has a spread angle of 60 degrees, and each of the sector-shaped guide pieces is rotated by 26 degrees with the needle.
[权利要求 5] 根据权利要求 1所述的一种酒精脱水蒸汽加热装置, 其特征在于燃烧 室材质由外部金属外壳以及内部钢玉料浇注而成, 燃烧室近后端设置 有至少一个凸环, 使燃烧室后端形成缩放式结构。  [Claim 5] The alcohol dehydration steam heating device according to claim 1, wherein the combustion chamber material is cast from an outer metal casing and an inner steel jade, and at least one convex ring is disposed near the rear end of the combustion chamber. , to form a zoom structure at the rear end of the combustion chamber.
[权利要求 6] 根据权利要求 1所述的一种酒精脱水蒸汽加热装置, 其特征在于辐射 加热器采用 U型管换热器, U型管换热器包括辐射加热室内的 U型管 束以及与 U型管束连通的顶端管箱, 管箱上幵设有蒸汽进口和蒸汽出 口, 蒸汽进口与最底端的换热器连接。 [Claim 6] An alcohol dehydration steam heating apparatus according to claim 1, wherein the radiant heater adopts a U-tube heat exchanger, and the U-tube heat exchanger includes a U-shaped tube bundle in the radiant heating chamber and U-shaped tube bundle connected to the top tube box, the tube box is provided with steam inlet and steam outlet The steam inlet is connected to the bottom heat exchanger.
[权利要求 7] 根据权利要求 7所述的一种酒精脱水蒸汽加热装置, 其特征在于 U型 管束下方设置有使烟气从 U型管束间穿过的导流档板。 [Claim 7] An alcohol dehydration steam heating apparatus according to claim 7, wherein a flow guide plate through which the flue gas passes between the U-shaped tube bundles is disposed under the U-shaped tube bundle.
[权利要求 8] 根据权利要求 1所述的一种酒精脱水蒸汽加热装置, 其特征在于对流 加热室末端底部设置有倾斜流道挡板。 [Claim 8] An alcohol dehydration steam heating apparatus according to claim 1, wherein an inclined flow path baffle is provided at the bottom end of the convection heating chamber.
[权利要求 9] 根据权利要求 1所述的一种酒精脱水蒸汽加热装置, 其特征在于烟道 由若干层拼接而成, 每层烟道上设置有一加热器。 [Claim 9] An alcohol dehydration steam heating apparatus according to claim 1, wherein the flue is formed by splicing a plurality of layers, and a heater is disposed on each of the flue.
[权利要求 10] 根据权利要求 1所述的一种酒精脱水蒸汽加热装置, 其特征在于上下 两层烟道间设置有烟道连接管, 烟道连接管包括筒体、 筒体上的膨胀 节、 膨胀节内侧的衬板以及陶瓷纤维内衬。 [Claim 10] The alcohol dehydration steam heating device according to claim 1, wherein a flue connecting pipe is disposed between the upper and lower flue pipes, and the flue connecting pipe includes a cylinder body and an expansion joint on the cylinder body. , the inner liner of the expansion joint and the ceramic fiber lining.
PCT/CN2016/101440 2016-09-18 2016-10-07 Ethanol dehydration steam heating device WO2018049703A1 (en)

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