JPS6017972B2 - steam superheating furnace - Google Patents
steam superheating furnaceInfo
- Publication number
- JPS6017972B2 JPS6017972B2 JP50022772A JP2277275A JPS6017972B2 JP S6017972 B2 JPS6017972 B2 JP S6017972B2 JP 50022772 A JP50022772 A JP 50022772A JP 2277275 A JP2277275 A JP 2277275A JP S6017972 B2 JPS6017972 B2 JP S6017972B2
- Authority
- JP
- Japan
- Prior art keywords
- steam
- furnace
- steam generator
- support beam
- flue
- 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
Description
【発明の詳細な説明】
この発明は化学プラント等で発生した蒸気を過熱する蒸
気過熱炉において上記蒸気とは別系統の蒸気発生器を同
一炉内に組み込んだ蒸気過熱炉に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a steam superheating furnace for superheating steam generated in a chemical plant or the like, in which a steam generator of a system different from the steam generator is incorporated in the same furnace.
第1図は従来の蒸気過熱健一を有するエチレンプラント
を示す図である。FIG. 1 is a diagram showing an ethylene plant having a conventional steam superheater.
この装置においては、分解炉1に原料2が供給されると
、原料2が分解炉1で高温熱分解される。この分解され
た生成ガスは急冷熱交換器3に導びかれ、急冷されて次
段の精製部門に送られる。この急冷熱交換器3において
は冷却剤として水が用いられるが、この水は上記生成ガ
スと熱交換して蒸発する。この蒸気5はドラム4を経て
外部に取出される。なお、大形エチレンプラントは通常
多数の同形の分解炉から構成されているから、上述と同
様の工程を経て蒸気6,7が取出される。これらの蒸気
5〜7は合流し、蒸気過熱法戸一8に導びかれ、独立蒸
気過熱器9でコンブレツサ駆動用蒸気タービンを作動す
るのに必要な温度まで過熱されて過熱蒸気10となる。
なお、この蒸気過熱を行なう独立蒸気過熱器9を個々の
分解炉1の対流部に設置したものもある。また、分解炉
1を出た燃焼ガスは、鰹道11を経て、他炉からの燃焼
ガス12,13と混合されガス清浄装置14により脱硝
等がなされたのち誘引通風機15により、煙突16に導
かれる。最近、上述のようなプラントにおいては、燃焼
炉に付随する公害処理機器の共通利用ならびに炉数を減
少することによるプラント全体の経済性の追求等の観点
から、蒸気過熱炉8に蒸気発生器を組み込むことが行な
われている。第2図は従釆の蒸気発生器を組み込んだ蒸
気過熱炉を示す図である。In this apparatus, when a raw material 2 is supplied to a cracking furnace 1, the raw material 2 is subjected to high-temperature pyrolysis in the cracking furnace 1. This decomposed product gas is led to the quenching heat exchanger 3, quenched, and sent to the next refining section. Water is used as a coolant in this quenching heat exchanger 3, and this water exchanges heat with the generated gas and evaporates. This steam 5 is taken out to the outside via the drum 4. Incidentally, since a large ethylene plant is usually composed of a large number of identically shaped cracking furnaces, the steams 6 and 7 are extracted through the same process as described above. These steams 5 to 7 are combined, guided to a steam superheater 18, and superheated in an independent steam superheater 9 to a temperature necessary to operate a steam turbine for driving a combustor, and become superheated steam 10.
In some cases, an independent steam superheater 9 for performing this steam superheating is installed in the convection section of each cracking furnace 1. The combustion gas leaving the cracking furnace 1 passes through the bonito pipe 11, is mixed with the combustion gases 12 and 13 from other furnaces, is denitrated by the gas purifier 14, and is then sent to the chimney 16 by the induced draft fan 15. be guided. Recently, in the above-mentioned plants, a steam generator has been installed in the steam superheating furnace 8 from the viewpoint of common use of pollution treatment equipment attached to the combustion furnace and pursuit of economic efficiency of the entire plant by reducing the number of furnaces. It is being incorporated. FIG. 2 is a diagram showing a steam superheating furnace incorporating a secondary steam generator.
この蒸気過熱炉17においては〜独立蒸気過熱器18の
後方の鰹道20中にバーナ21による燃焼熱の廃熱を回
収するために蒸気発生器22が設置され、ドラム23か
ら蒸気が取出される。なお、プラントから送られてくる
蒸気19は独立蒸気過熱器18で所定温度まで過熱され
て過熱蒸気10となる。しかし、この蒸気過熱炉では回
収できる蒸気量に限度がある。したがって、廃熱回収を
するだけでなく相当量の蒸気を積極的に得たい場合には
、第2図に示すバーナ21の焚き高を増加するか、第3
図に示すように蒸気発生器22の前の適当な位置にバー
ナ24を設け、造焚きをすることが考えられる。しかし
、前者の場合には蒸気過熱炉i7内のガス温度が高くな
るから、炉の寿命を短縮させないためには、独立蒸気過
熱器18の頚射部伝熱管18aや対流部伝熱管18bの
高温側の高価な耐熱材料をさらに高級にする必要がある
。一方「後者の場合には所要蒸気量が多くなる程、バー
ナ24が大がかりなものとなり、運転操作、保守などが
繁雑になる。また、この場合には通常煙道20を一旦地
上におろし、その鰹道201こバーナ24、蒸気発生器
22等を設置し、さらに誘引通風機25を設けて燃焼ガ
スを排出する必要がある。しかがって、独立に煙突を設
けるにしろ(場合によっては脱硝設備も必要)、多数の
分解炉からの共通煙道に継ぎ込むにしろ、設備費が多く
なるとともに、設置面積が大きくなることは免れない。
このように、従釆の蒸気発生器を組み込んだ蒸気過熱炉
においては種々の問題点があった。この発明は上述の問
題点を解決するためになされたもので、構造が簡単で、
設備面積が小さく「かつ相当量の別目的に用いられる蒸
気を得ることができる蒸気過熱炉を提供することを目的
とする。In this steam superheating furnace 17, a steam generator 22 is installed in the bonito path 20 behind the independent steam superheater 18 in order to recover waste heat of combustion heat from the burner 21, and steam is taken out from the drum 23. . Note that steam 19 sent from the plant is superheated to a predetermined temperature in an independent steam superheater 18 and becomes superheated steam 10. However, there is a limit to the amount of steam that can be recovered in this steam superheating furnace. Therefore, if you want to actively obtain a considerable amount of steam in addition to recovering waste heat, increase the firing height of the burner 21 shown in FIG.
As shown in the figure, it is conceivable to provide a burner 24 at an appropriate position in front of the steam generator 22 to create fire. However, in the former case, the gas temperature in the steam superheating furnace i7 becomes high, so in order not to shorten the life of the furnace, it is necessary to The expensive heat-resistant material on the side needs to be made even higher grade. On the other hand, in the latter case, the larger the amount of steam required, the larger the burner 24 becomes, making operation and maintenance more complicated. It is necessary to install a bonito path 201, a burner 24, a steam generator 22, etc., and an induced draft fan 25 to exhaust the combustion gas. Even if it is connected to a common flue from multiple cracking furnaces, it will inevitably increase the equipment cost and the installation area.
As described above, there have been various problems in steam superheating furnaces incorporating secondary steam generators. This invention was made to solve the above problems, and has a simple structure.
The purpose of the present invention is to provide a steam superheating furnace that has a small facility area and can obtain a considerable amount of steam that can be used for other purposes.
この目的を達成するため、この発明においては枠体と、
その枠体に水平に固定された複数の支持梁と、その支持
梁の少なくとも一部に下部が固定され、かつ下端が上記
支持梁より下方に突出した対流部煙道と、その対流部煙
道の内部に組み込まれた独立蒸気過熱器と、上記支持梁
と基礎部との間に設けられ、上記支持梁の少なくとも一
部に上部が吊下げられ、かつ蒸気管で炉墜が形成された
蒸気発生器と、上記対流部煙道の下部と上記蒸気発生器
の上部との間に設けられた可携性を有する被覆板とを設
ける。In order to achieve this purpose, the present invention includes a frame body,
A plurality of support beams horizontally fixed to the frame, a convection flue whose lower part is fixed to at least a portion of the support beams, and whose lower end protrudes downward from the support beam, and the convection flue. an independent steam superheater built into the interior of the vessel, and a steam system provided between the support beam and the foundation, the upper part of which is suspended from at least a portion of the support beam, and a furnace formed by a steam pipe. A generator and a portable cover plate disposed between a lower portion of the convection flue and an upper portion of the steam generator.
また、枠体と、その枠体に水平に固定された支持梁と、
その支持梁に下部が固定され、かつ下端が上記支持梁よ
り下方に突出した対流部煙道と、その対流都塵道の内部
に組み込まれた独立蒸気過熱器と「上記支持梁と基礎部
との間に設けられ、ボトムサポートにより下部が支持さ
れ「かつ蒸発管で炉肇が形成された蒸気発生器と、上記
対流部煙道の下部と上記蒸気発生器の上部との間に設け
られた可操性を有する被覆板とを設ける。第4図はこの
発明に係る蒸気過熱炉を示す図である。Also, a frame body, a support beam horizontally fixed to the frame body,
A convection flue whose lower part is fixed to the support beam and whose lower end protrudes below the support beam, an independent steam superheater built into the inside of the convection flue, a steam generator whose lower part is supported by a bottom support and whose furnace arm is formed by an evaporation tube; and the lower part of the convection flue and the upper part of the steam generator. FIG. 4 is a diagram showing a steam superheating furnace according to the present invention.
図において26は枠体、27は枠体26に水平に固定さ
れた複数の支持梁、28は吊りボルト29により支持梁
27に上部が吊下げられた蒸気発生器で、蒸気発生器2
8‘ま支持梁27と基礎部52との間に設けられており
、また蒸気発生器28‘ま蒸発管で炉壁が形成されてい
る。30は蒸気発生器28‘こよって形成された燃焼炉
、31は蒸気発生器28の上部管寄せ、32は蒸気発生
器28の下部管寄せ、33はドラムで、管寄せ31,3
2とドラム33とは上昇管34、降水管35によって接
続されている。In the figure, 26 is a frame, 27 is a plurality of support beams horizontally fixed to the frame 26, and 28 is a steam generator whose upper part is suspended from the support beams 27 by hanging bolts 29.
The steam generator 28' is provided between the support beam 27 and the base part 52, and the furnace wall is formed by the steam generator 28'. 30 is a combustion furnace formed by the steam generator 28'; 31 is an upper header of the steam generator 28; 32 is a lower header of the steam generator 28; 33 is a drum;
2 and the drum 33 are connected by a rising pipe 34 and a downcomer pipe 35.
また、36は蒸気発生器28の外側に取付けられた保温
材、37は蒸気発生器28に設置されたバーナ、38は
燃焼用空気の押込通風機、39はバーナ37と押込通風
機38とを接続する空気風道で、押込通風機38により
送り込まれた燃焼用空気は空気風道39を介して、バー
ナ37まで送られる。オイルまたはガス燃料は、上記燃
焼用空気と適切に配合されて、バーナ37で燃焼される
。また、4川ま下部が支持梁27に固定され、かつ下端
が支持梁27より下方に突出した対流部煙道で、燃焼炉
30の出口に位置し、レンガまたはキャスタブルによる
築炉構造とされている。41は独立蒸気過熱器で、対流
都塵道40の内部に組み込まれている。Further, 36 is a heat insulating material attached to the outside of the steam generator 28, 37 is a burner installed in the steam generator 28, 38 is a forced draft fan for combustion air, and 39 is a burner 37 and a forced draft fan 38. In the connecting air duct, the combustion air brought in by the forced draft fan 38 is sent via the air duct 39 to the burner 37 . The oil or gas fuel is suitably blended with the combustion air and combusted in the burner 37. In addition, the convection flue is fixed at the lower part to the support beam 27 and whose lower end protrudes downward from the support beam 27, and is located at the outlet of the combustion furnace 30, and has a furnace structure made of brick or castable. There is. 41 is an independent steam superheater, which is incorporated inside the convection pipe 40.
また、独立蒸気過熱器41は管内蒸気の許容圧損を小さ
く押えるため、通常は比較的大きな直径の伝熱管で構成
されているが、その選択は自由に行なうことができる。
42,43は独立蒸気過熱器41の入口管寄せ、出口管
寄せで、プラントから送られてくる蒸気19は入口管寄
せ42を経て独立蒸気過熱器41で所定温度まで過熱さ
れ、出口管寄せ43に至る。Further, the independent steam superheater 41 is normally constructed of heat exchanger tubes having a relatively large diameter in order to keep the allowable pressure drop of the steam inside the tubes small, but the choice can be made freely.
42 and 43 are an inlet header and an outlet header of the independent steam superheater 41, and the steam 19 sent from the plant passes through the inlet header 42, is superheated to a predetermined temperature in the independent steam superheater 41, and is then transferred to the outlet header 43. leading to.
なお、44,45は廃熱回収の観点から設けられた廃熱
回収部で、廃熱回収部44,45の用途は種々考えられ
るが、最も適当な用途を選択すればよい。46は煙道で
熱回収された燃焼ガスは鰹道46を経て煙突あるいは共
通煙道等に導かれる。In addition, 44 and 45 are waste heat recovery parts provided from the viewpoint of waste heat recovery, and various uses of the waste heat recovery parts 44 and 45 can be considered, but the most appropriate use may be selected. The combustion gas whose heat has been recovered in a flue 46 is led to a chimney or a common flue through a bonito pipe 46.
このように蒸気発生器28と独立蒸気過熱器41とは構
造的には分離されている。また、47は両端が蒸気発生
器28の上部と対流部煙道40の下部とに固定された可
操性を有する被覆板で、被覆板47は燃焼ガス、空気の
洩れを防止するためのものである。なお、燃焼炉30内
は、負圧とされており、燃焼ガスが外部に洩れるのが防
止されている。このように、この炉においては蒸気発生
器28にバーナ37が設置されているから、独立蒸気過
熱器41の容量とは関係なく相当量の別目的の蒸気を得
ることができる。In this way, the steam generator 28 and the independent steam superheater 41 are structurally separated. Further, 47 is a movable cover plate whose both ends are fixed to the upper part of the steam generator 28 and the lower part of the convection flue 40, and the cover plate 47 is for preventing combustion gas and air from leaking. It is. Note that the inside of the combustion furnace 30 is kept under negative pressure to prevent combustion gas from leaking to the outside. In this manner, since the burner 37 is installed in the steam generator 28 in this furnace, a considerable amount of steam for other purposes can be obtained regardless of the capacity of the independent steam superheater 41.
また、熱膨張に対しては蒸気発生器28は支持梁27に
吊下げられているから下方に自由に変形でき、対流部煙
道40は支持梁27に下部が固定され上方に自由に変形
することが可能である。また、炉の中央部近傍の支持梁
27を上下方向の熱膨張の基点としているので炉全体の
熱膨張量がみかけ上小さくなるとともに蒸気発生器28
と対流部煙道40との接合部の構造が簡単かつ安定化で
きるので燃焼ガスあるいは空気の洩れ防止を容易にして
いる。さらに、蒸気発生器28と対流部煙道40とは可
榛性を有する被覆板47で接続されているから、互いに
その構造が制約を受けることがなく、構造が簡単となり
、またこの炉は蒸気過熱器41と蒸気発生器28とが上
下に配置されており、垂直堅形であるから、煙突効果を
最大限に利用することができ、かつ設置面積が小さい。
またさらに、蒸気発生器28と対流部煙道40とは構造
的に分離されているから、蒸気発生器28の最大蒸発量
と独立蒸気過熱器41の容量とを自由に定めることがで
きる。なお、独立蒸気過熱器41を主体に運転する場合
には、バーナ37の燃焼量を調整することにより自由に
独立蒸気過熱器41の運転範囲を変えることが可能であ
る。また、第5図はこの発明に係る他の蒸気過熱炉を示
す図である。Furthermore, in response to thermal expansion, the steam generator 28 is suspended from the support beam 27 and can freely deform downward, and the convection flue 40 has its lower part fixed to the support beam 27 and can freely deform upward. Is possible. In addition, since the support beam 27 near the center of the furnace is used as the base point for vertical thermal expansion, the amount of thermal expansion of the entire furnace is apparently small, and the steam generator 28
The structure of the joint between the convection flue 40 and the convection flue 40 is simple and stable, making it easy to prevent combustion gas or air from leaking. Furthermore, since the steam generator 28 and the convection flue 40 are connected by the flexible cover plate 47, their structures are not restricted to each other, and the structure is simple. Since the superheater 41 and the steam generator 28 are arranged one above the other and are vertically rigid, the chimney effect can be utilized to the maximum and the installation area is small.
Furthermore, since the steam generator 28 and the convection flue 40 are structurally separated, the maximum evaporation amount of the steam generator 28 and the capacity of the independent steam superheater 41 can be freely determined. Note that when the independent steam superheater 41 is mainly operated, the operating range of the independent steam superheater 41 can be freely changed by adjusting the combustion amount of the burner 37. Moreover, FIG. 5 is a diagram showing another steam superheating furnace according to the present invention.
この蒸気過熱炉においては蒸気発生器28を吊りボルト
により吊さげずに、蒸気発生器28の下部をボトムサポ
ート51により支持している。以上説明したように、こ
の発明に係る蒸気過熱炉においては独立蒸気過熱器と、
別目的の蒸気発生器とが構造的に分離されているうえに
構造が簡単で、設置面積が小さく、かつ相当量の蒸気を
得ることができる。In this steam superheating furnace, the steam generator 28 is not suspended by hanging bolts, but the lower part of the steam generator 28 is supported by a bottom support 51. As explained above, the steam superheating furnace according to the present invention includes an independent steam superheater,
In addition to being structurally separated from the steam generator for other purposes, the structure is simple, the installation area is small, and a considerable amount of steam can be obtained.
このように、この発明の効果は顕著である。As described above, the effects of this invention are remarkable.
第1図は従来の蒸気過熱炉を有するエチレンプラントを
示す図、第2図、第3図はそれぞれ従来の蒸気発生器を
組み込んだ蒸気過熱炉を示す図、第4図、第5図はそれ
ぞれこの発明に係る蒸気発生器を組み込んだ蒸気過熱炉
を示す図である。
符号の説明、1・・・・・・分解炉、2・・・・・・原
料、3・・・…急冷熱交換器、4,23,33…・・・
ドラム、5〜7,19・・・・・・蒸気、8,17・・
・・・・蒸気過熱炉、9,18,41…・・・独立蒸気
過熱器、10・・・・・・過熱蒸気、21,24,37
・…・・バーナ、22,28・・・・・・蒸気発生器、
26・・・・・・枠体、27・・・・・・支持梁、29
・・・・・・吊りボルト、30・・・・・・燃焼炉、4
0・・・・・・対流部煙道、47・・・・・・被覆板。
第l図第2図
第3図
第4図
第5図Figure 1 shows an ethylene plant with a conventional steam superheating furnace, Figures 2 and 3 show steam superheating furnaces incorporating a conventional steam generator, and Figures 4 and 5 respectively. FIG. 1 is a diagram showing a steam superheating furnace incorporating a steam generator according to the present invention. Explanation of symbols: 1... Cracking furnace, 2... Raw material, 3... Quenching heat exchanger, 4, 23, 33...
Drum, 5-7, 19... Steam, 8, 17...
...Steam superheating furnace, 9,18,41...Independent steam superheater, 10...Superheated steam, 21,24,37
...Burner, 22,28...Steam generator,
26... Frame body, 27... Support beam, 29
... Hanging bolt, 30 ... Combustion furnace, 4
0... Convection flue, 47... Covering plate.
Figure l Figure 2 Figure 3 Figure 4 Figure 5
Claims (1)
と、その支持梁の少なくとも一部に下部が固定され、か
つ下端が上記支持梁より下方に突出した対流部煙道と、
その対流部煙道の内部に組み込まれた独立蒸気過熱器と
、上記支持梁と基礎部との間に設けられ、上記支持梁の
少なくとも一部に上部が吊下げられ、かつ蒸発管で炉壁
が形成された蒸気発生器と、上記対流部煙道の下部と上
記蒸気発生器の上部との間に設けられた可撓性を有する
被覆板とを具備することを特徴とする蒸気過熱炉。 2 枠体と、その枠体に水平に固定された支持梁と、そ
の支持梁に下部が固定され、かつ下端が上記支持梁より
下方に突出した対流部煙道と、その対流部煙道の内部に
組み込まれた独立蒸気過熱器と、上記支持梁と基礎部と
の間に設けられ、ボトムサポートにより下部が支持され
、かつ蒸発管で炉壁が形成された蒸気発生器と、上記対
流部煙道の下部と上記蒸気発生器の上部との間に設けら
れた可撓性を有する被覆板とを具備することを特徴とす
る蒸気過熱炉。[Scope of Claims] 1 A frame body, a plurality of support beams horizontally fixed to the frame body, and a lower part of which is fixed to at least a part of the support beams, and a lower end of which protrudes downward from the support beams. a convection flue;
An independent steam superheater built into the convection flue is provided between the support beam and the foundation, the upper part is suspended from at least a portion of the support beam, and the evaporation tube is connected to the furnace wall. 1. A steam superheating furnace comprising: a steam generator having a structure formed therein; and a flexible covering plate provided between a lower part of the convection flue and an upper part of the steam generator. 2 A frame, a support beam horizontally fixed to the frame, a convection flue whose lower part is fixed to the support beam and whose lower end protrudes below the support beam, and the convection flue. an independent steam superheater built into the interior, a steam generator provided between the support beam and the foundation part, the lower part of which is supported by a bottom support, and whose furnace wall is formed by an evaporation tube, and the convection part. A steam superheating furnace comprising a flexible cover plate provided between a lower part of the flue and an upper part of the steam generator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50022772A JPS6017972B2 (en) | 1975-02-26 | 1975-02-26 | steam superheating furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50022772A JPS6017972B2 (en) | 1975-02-26 | 1975-02-26 | steam superheating furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5198402A JPS5198402A (en) | 1976-08-30 |
| JPS6017972B2 true JPS6017972B2 (en) | 1985-05-08 |
Family
ID=12091947
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP50022772A Expired JPS6017972B2 (en) | 1975-02-26 | 1975-02-26 | steam superheating furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6017972B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63162168A (en) * | 1986-12-26 | 1988-07-05 | 旭木材工業株式会社 | Tacker |
| JPH03120383U (en) * | 1990-03-20 | 1991-12-11 |
-
1975
- 1975-02-26 JP JP50022772A patent/JPS6017972B2/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63162168A (en) * | 1986-12-26 | 1988-07-05 | 旭木材工業株式会社 | Tacker |
| JPH03120383U (en) * | 1990-03-20 | 1991-12-11 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5198402A (en) | 1976-08-30 |
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