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JP3971865B2 - Hot gas supply device - Google Patents
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JP3971865B2 - Hot gas supply device - Google Patents

Hot gas supply device Download PDF

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Publication number
JP3971865B2
JP3971865B2 JP14052599A JP14052599A JP3971865B2 JP 3971865 B2 JP3971865 B2 JP 3971865B2 JP 14052599 A JP14052599 A JP 14052599A JP 14052599 A JP14052599 A JP 14052599A JP 3971865 B2 JP3971865 B2 JP 3971865B2
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Japan
Prior art keywords
hot gas
groove
outer jacket
gas supply
supply device
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Expired - Fee Related
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JPH11351501A (en
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キユラ ヘルムート
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ボルジヒ ゲーエムベーハー
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/0229Double end plates; Single end plates with hollow spaces
    • 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
    • F22B1/02Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
    • F22B1/18Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
    • F22B1/1884Hot gas heating tube boilers with one or more heating tubes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00Component parts or details of steam boilers
    • F22B37/02Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
    • F22B37/06Flue or fire tubes; Accessories therefor, e.g. fire-tube inserts
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F19/00Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
    • F28F19/002Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using inserts or attachments

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)

Description

【0001】
【発明が属する技術分野】
本発明は、廃熱ボイラにおいて伝熱面管に熱ガスを給気する装置に関するものであり、ボイラの内壁、特に底部につながって且つその下端部に厚みのある外部ジャケットと、熱ガスの給気開口を形成した丸形反転領域の上方で外部ジャケットにつながり且つ、外部ジャケットにより間隔をあけて囲まれており、円錐状に狭くなる流入部分を備えた給気管と、伝熱面の管に接続した流出部分及び、外部ジャケットと給気管との間に配置され、反転キャップの近くまで延びる冷却剤誘導体とを備える。
【0002】
【従来の技術】
本出願人のパンフレット「取扱設備と器械セットの構造及びピッチ円走行」(Verfahrenstechnik Anlagen- und Apparatebau Komponenten und Teilkreislaeufe)(1986年)19頁により、前記技術による装置は既知であるが、その場合は外部ジャケットの下端部に厚みが確実に少ない。熱ガスが送り込まれる廃熱ボイラでは、熱ガスを伝熱面管に給気すると、臨界領域に達する。給気装置に約1500℃の熱ガスを送り込まれる際、例えば高圧下で炭化水素の触媒分裂が起こらないことから、給気装置が熱による相当高い負荷を負うことになる。更に管の幾何学的な(Rohrgeometrie)要因及び水充填されたボイラの高い内部圧のため、大きな負荷が生じるので、大きな熱膨張を考慮しなければならない。特に外部ジャケット及び反転領域における壁厚を増やして、壁の温度を上げるため、ガス流量としての廃熱ボイラの負荷を制限している。
【0003】
前記パンフレットによる既知の装置の別の実施形態では、充分な内部圧力を保証するため、外部ジャケットがその下端部を厚みがあるように形成している。
【0004】
【発明が解決しようとする課題】
従来発明の課題は熱ガス給気装置において、厚みがある反転領域の冷却を改善することである。
【0005】
【課題を解決するための手段】
この課題は、少なくとも外部ジャケットが、その内側に厚みのある領域で、本質的に均等に分けられ、且つ本質的に軸線方向に延びる溝を周方向に備えることで解決される。
【0006】
【本発明の実施の形態】
請求項2から4は、溝が形成可能な異なる実施形態に関している。
【0007】
加えて、溝の深所を反転領域の方向、すなわち冷却剤の流れる向きに小さくする。
【0008】
結局、溝は丸形反転領域で内部につながって、溝底部が本質的に反転領域で曲線状になっており、溝の深所を給気管の方向に連続して小さくする。その様な方法で特別効果的に反転領域が冷却される。
【0009】
【実施例】
本発明を添付図面を参照して、更に詳しく説明する。
【0010】
図1は、本発明による装置の実施例の縦断面図であり、上記で引用したパンフレットの19頁の“伝熱面管における冷却式円錐形給気領域”における図面と比較することができる。
図2は、図1のII-II線に沿った横断面図である。
図3は、図1のIII-III線に沿った縦断面図である。
【0011】
パンフレットで前述した図面において、容器の壁Wの一部分のみを示しており、図示されていない廃熱ボイラの熱伝面管において熱ガスを給気する装置1が、孔Bの領域で、溶接部S1によって接合されている。丸形反転領域4の上で互いに接合されている外部ジャケット2及び、外部ジャケット2によって囲まれた給気管3が、装置の一部を成している。図1に示された実施形態において、外部ジャケット2及び反転領域4が、お互い部分的に、溶接部分S2の上で給気管3とつながる方向転換キャップ6として形成されている。方向変換キャップ6は、給気管3のガス吸気口6aを画定している。給気管3は、図示されていないが、伝熱面管とつながれる流出部分が直円筒状になるように円錐状に狭くなる部分5を備えている。
【0012】
外部ジャケットは、容器の壁に接続された第一部分7、変形部分8及び、厚みのある部分9を備えている。
【0013】
部分9の内壁9a及び反転領域4の内壁4aには、本質的に放射状で外向きに、同間隔で配置された溝10が設けられている。溝10は、外部ジャケットの部分9に設けられ、連続してその深所の方向に大きくなる溝部分10a及び、それにつながり且つ曲線状の底部を備えた溝部分10bから構成され、溝部分10bの深所は、管部分5の方向に小さくなっている。また溝は、望ましい冷却効果を達成することができるように、別の形で分割して配置することができる。
【0014】
外部ジャケット2と給気管3の間には、冷却剤誘導体11が配置されており、その自由端は反転領域4の近く、すなわち溝の上方で終端している。溝10の間には、ウェブ12が配置している。
【0015】
孔Bの壁と冷却剤誘導体11の外面との間に流入する冷却剤Kが、部分流K1になり、本質的に冷却剤Kの流れる方向、すなわち装置の軸線方向に沿った溝10へ流れて、そして更にウェブ12の上側と冷却剤誘導体11との間の空間において部分流K2となって流れる。これらの部分流は合流して、冷却剤誘導体11と流入部分5との間の空間を上方へ流れる。溝10に入る部分流によって、外部ジャケット2の下の部分9及び反転領域4が、内側から特に良く冷却される。それによって反転キャップ4の外面温度が下がる。内側に配置したウェブ12は、熱交換面を大きくして、更に水温を250℃〜350℃にする。それによって、短い時間の範囲の剛性パラメータが設計上で確定され、その値はクリープ領域(変形領域)における値よりも本質的に高くすることができる。他方でフランジが、支持または補強作用と言った構造機械的な効果を有している。
【0016】
本発明による装置では、従来、15〜20mmであった反転領域の壁厚を、約5mm減らすことができ、それによってガス側の表面温度を約100K減らすことができる。
【0017】
装置に入る熱ガスが水素を含んでいると、ガス側の表面温度を下げることは、特に重要になる。それはガスに含まれている水素成分と関連する高い表面温度が、ネルソン図形(NELSON-Diagramm)に対応して、水素脆化を生じさせるからである。
【0018】
従って、本発明による装置において、表面温度の低下が特に装置の反転キャップ領域、すなわちガスが流入する接合管で生じる。
【図面の簡単な説明】
【図1】本発明による装置の実施例の縦断面図。
【図2】図1のII-II線に沿った横断面図。
【図3】図1のIII-III線に沿った縦断面図。
【符号の説明】
1 装置
2 外部ジャケット
3 給気管
4 反転領域
5 管部分
6 反転キャップ
6a ガス吸気口
7 第一部分
8 変形部分
9 部分
9a 内壁
10 溝
10a溝部分
10b溝部分
11 冷却剤誘導体
12 ウェブ
B 孔
K 冷却剤
K1 部分流
K2 部分流
S1 溶接部分
W 壁
[0001]
[Technical field to which the invention belongs]
The present invention relates to an apparatus for supplying hot gas to a heat transfer surface tube in a waste heat boiler, and is connected to the inner wall of the boiler, particularly to the bottom, and has a thick outer jacket at its lower end, and supply of hot gas. Connected to the outer jacket above the circular inversion region forming the air opening and surrounded by the outer jacket with a space between the air supply pipe with the inflow portion narrowing in a conical shape, and the heat transfer surface pipe A connected outflow portion and a coolant derivative disposed between the outer jacket and the air supply pipe and extending near the inversion cap.
[0002]
[Prior art]
According to the applicant's brochure “Structure of the handling equipment and instrument set and pitch travel” (Verfahrenstechnik Anlagen- und Apparatebau Komponenten und Teilkreislaeufe) (1986), page 19, the device according to the above technique is known, but in that case external The thickness is surely small at the lower end of the jacket. In a waste heat boiler to which hot gas is sent, when the hot gas is supplied to the heat transfer surface tube, the critical region is reached. When hot gas having a temperature of about 1500 ° C. is fed into the air supply device, for example, the catalytic splitting of hydrocarbons does not occur under a high pressure, so that the air supply device bears a considerably high load due to heat. Furthermore, due to the tube's geometric factors and the high internal pressure of the water-filled boiler, a large load is created, so a large thermal expansion must be taken into account. In particular, in order to increase the wall thickness by increasing the wall thickness in the outer jacket and the inversion region, the load of the waste heat boiler as a gas flow rate is limited.
[0003]
In another embodiment of the known device according to the pamphlet, an outer jacket is formed with its lower end thick so as to ensure sufficient internal pressure.
[0004]
[Problems to be solved by the invention]
An object of the conventional invention is to improve cooling of a thick inversion region in a hot gas supply device.
[0005]
[Means for Solving the Problems]
This problem is solved by providing at least the outer jacket in the circumferential direction with grooves that are essentially evenly divided and essentially axially extending in the thick area inside.
[0006]
[Embodiments of the Invention]
Claims 2 to 4 relate to different embodiments in which grooves can be formed.
[0007]
In addition, the depth of the groove is reduced in the direction of the inversion region, that is, the direction in which the coolant flows.
[0008]
Eventually, the groove is connected to the inside in the circular inversion region, and the groove bottom is essentially curved in the inversion region, and the depth of the groove is continuously reduced in the direction of the supply pipe. In such a way, the inversion region is cooled particularly effectively.
[0009]
【Example】
The present invention will be described in more detail with reference to the accompanying drawings.
[0010]
FIG. 1 is a longitudinal sectional view of an embodiment of the device according to the invention, which can be compared with the drawing in “Cooled conical air supply region in a heat transfer face tube” on page 19 of the pamphlet cited above.
FIG. 2 is a cross-sectional view taken along line II-II in FIG.
FIG. 3 is a longitudinal sectional view taken along line III-III in FIG.
[0011]
In the drawings described above in the pamphlet, only a part of the wall W of the container is shown, and the apparatus 1 for supplying hot gas in the heat transfer pipe of the waste heat boiler (not shown) Joined by S1. An outer jacket 2 joined to each other on the round inversion region 4 and an air supply pipe 3 surrounded by the outer jacket 2 form part of the apparatus. In the embodiment shown in FIG. 1, the outer jacket 2 and the inversion region 4 are partly formed as a change-over cap 6 that is connected to the supply pipe 3 on the welded part S2. The direction changing cap 6 defines a gas inlet 6 a of the supply pipe 3. Although not shown, the air supply pipe 3 includes a portion 5 that narrows in a conical shape so that an outflow portion connected to the heat transfer surface tube has a right cylindrical shape.
[0012]
The outer jacket comprises a first part 7 connected to the container wall, a deformed part 8 and a thick part 9.
[0013]
The inner wall 9a of the part 9 and the inner wall 4a of the inversion region 4 are provided with grooves 10 that are essentially radially outward and arranged at equal intervals. The groove 10 is provided in the portion 9 of the outer jacket, and is constituted by a groove portion 10a that continuously increases in the direction of the depth thereof, and a groove portion 10b that has a curved bottom connected to the groove portion 10a. The depth is reduced in the direction of the tube portion 5. Also, the grooves can be divided and arranged in different ways so that the desired cooling effect can be achieved.
[0014]
A coolant derivative 11 is arranged between the outer jacket 2 and the supply pipe 3, and its free end terminates near the inversion region 4, ie above the groove. A web 12 is disposed between the grooves 10.
[0015]
The coolant K flowing between the wall of the hole B and the outer surface of the coolant derivative 11 becomes a partial flow K1, and flows into the groove 10 along the direction of the coolant K, that is, along the axial direction of the apparatus. And further flows as a partial flow K2 in the space between the upper side of the web 12 and the coolant derivative 11. These partial flows merge and flow upward in the space between the coolant derivative 11 and the inflow portion 5. Due to the partial flow entering the groove 10, the lower part 9 of the outer jacket 2 and the inversion region 4 are cooled particularly well from the inside. Thereby, the outer surface temperature of the reversing cap 4 is lowered. The web 12 arranged on the inner side has a large heat exchange surface, and the water temperature is further set to 250 ° C to 350 ° C. Thereby, the stiffness parameter in the short time range is determined by design and its value can be essentially higher than the value in the creep region (deformation region). On the other hand, the flange has a structural mechanical effect called support or reinforcement.
[0016]
In the apparatus according to the present invention, the wall thickness of the inversion region, which was conventionally 15 to 20 mm, can be reduced by about 5 mm, thereby reducing the surface temperature on the gas side by about 100K.
[0017]
Lowering the gas side surface temperature is particularly important when the hot gas entering the apparatus contains hydrogen. This is because the high surface temperature associated with the hydrogen component contained in the gas causes hydrogen embrittlement corresponding to the Nelson figure (NELSON-Diagramm).
[0018]
Thus, in the device according to the invention, a decrease in the surface temperature occurs especially in the reversal cap region of the device, i.e. in the joining tube into which the gas flows.
[Brief description of the drawings]
1 is a longitudinal sectional view of an embodiment of an apparatus according to the invention.
2 is a cross-sectional view taken along the line II-II in FIG.
3 is a longitudinal sectional view taken along line III-III in FIG.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Apparatus 2 External jacket 3 Supply pipe 4 Inversion area 5 Pipe part 6 Inversion cap 6a Gas inlet 7 First part 8 Deformation part 9 Part 9a Inner wall 10 Groove 10a Groove part 10b Groove part 11 Coolant derivative 12 Web B Hole K Coolant K1 Partial flow K2 Partial flow S1 Welded part W Wall

Claims (6)

ボイラの内壁、特に底部につながり且つその下端部に厚みのある外部ジャケット(2)と、
熱ガスの給気開口(6a)を形成した丸形反転領域(4)の上方で外部ジャケットにつながり且つ、外部ジャケットにより間隔をあけて囲まれており、円錐状に狭くなる流入部分を備えた給気管(3)と、
伝熱面管に接続した流出部分及び、外部ジャケットと給気管との間に配置され、反転キャップの近くまで延びる冷却剤誘導体(11)とを備えた
廃熱ボイラの伝熱面管に熱ガスを給気する装置において、
少なくとも外部ジャケット(2)が、その内側(9a)に厚みのある領域(9)で、本質的に均等に分けられ、且つ本質的に軸線方向に延びる溝(10)を周方向に備えることを特徴とする熱ガス給気装置。
An outer jacket (2) connected to the inner wall of the boiler, in particular the bottom, and thick at the lower end;
An inflow portion that is connected to the outer jacket above the circular inversion region (4) in which the hot gas supply opening (6a) is formed, is surrounded by the outer jacket at an interval, and narrows in a conical shape. An air supply pipe (3);
A hot gas is supplied to the heat transfer surface tube of the waste heat boiler including the outflow portion connected to the heat transfer surface tube and the coolant derivative (11) disposed between the outer jacket and the air supply tube and extending near the reversing cap. In a device for supplying air,
At least the outer jacket (2) is provided with a groove (10) in the circumferential direction which is essentially equally divided and essentially axially elongated in the thickened region (9) on its inner side (9a). A featured hot gas supply device.
溝が外部ジャケットの内壁に設けられることを特徴とする請求項1に記載の熱ガス給気装置。The hot gas supply device according to claim 1, wherein the groove is provided in an inner wall of the outer jacket. 溝が、特に外部ジャケットの内壁に溶接されたウェブによって形成されることを特徴とする請求項1に記載の熱ガス給気装置。2. A hot gas supply device according to claim 1, characterized in that the groove is formed by a web, in particular welded to the inner wall of the outer jacket. 溝が均一の鋳物として形成されることを特徴とする請求項1に記載の熱ガス給気装置。The hot gas supply device according to claim 1, wherein the groove is formed as a uniform casting. 溝の深所が、冷却剤が流れる向きすなわち反転領域の方向に連続して小さくなることを特徴とする請求項1〜4のいずれか一項に記載の熱ガス給気装置。The hot gas supply device according to any one of claims 1 to 4, wherein the depth of the groove continuously decreases in the direction in which the coolant flows, that is, in the direction of the inversion region. 溝(10a)が丸形反転領域の内側(10b)に続き、本質的に曲線状の溝の底部が反転領域につながり、溝の深所が給気管の向きに連続して小さくなることを特徴とする請求項1〜5のいずれか一項に記載の熱ガス給気装置。The groove (10a) is connected to the inside (10b) of the round inversion region, the bottom of the essentially curved groove is connected to the inversion region, and the depth of the groove is continuously reduced in the direction of the supply pipe. The hot gas supply device according to any one of claims 1 to 5.
JP14052599A 1998-05-20 1999-05-20 Hot gas supply device Expired - Fee Related JP3971865B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE1998122546 DE19822546C1 (en) 1998-05-20 1998-05-20 Heating gas inlet for boiler
DE19822546.6 1998-05-20

Publications (2)

Publication Number Publication Date
JPH11351501A JPH11351501A (en) 1999-12-24
JP3971865B2 true JP3971865B2 (en) 2007-09-05

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JP14052599A Expired - Fee Related JP3971865B2 (en) 1998-05-20 1999-05-20 Hot gas supply device

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JP (1) JP3971865B2 (en)
DE (1) DE19822546C1 (en)
FR (1) FR2778968B1 (en)
NL (1) NL1012058C2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10138626A1 (en) 2001-08-13 2003-03-13 Alstom Power Energy Recovery Gmbh Device for the entry of hot gas into a heating surface tube of a waste heat boiler
DE102004004999B4 (en) * 2004-01-30 2007-03-08 Alstom Power Energy Recovery Gmbh Device for the entry of hot gas into a Heizflächenrohr a Abhitzkessels

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1751085C3 (en) * 1968-03-30 1974-10-24 Basf Ag Multi-part tube sheet for hot gas cooler
US4445463A (en) * 1983-04-06 1984-05-01 Syngas Company Waste heat boiler

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FR2778968A1 (en) 1999-11-26
FR2778968B1 (en) 2003-06-20
NL1012058A1 (en) 1999-11-24
JPH11351501A (en) 1999-12-24
NL1012058C2 (en) 2000-03-15
DE19822546C1 (en) 1999-06-17

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