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JP2002286379A - Steam and hot water generating device - Google Patents

Steam and hot water generating device

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Publication number
JP2002286379A
JP2002286379A JP2001130357A JP2001130357A JP2002286379A JP 2002286379 A JP2002286379 A JP 2002286379A JP 2001130357 A JP2001130357 A JP 2001130357A JP 2001130357 A JP2001130357 A JP 2001130357A JP 2002286379 A JP2002286379 A JP 2002286379A
Authority
JP
Japan
Prior art keywords
heat transfer
tube
heat
exhaust
exhaust gas
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
JP2001130357A
Other languages
Japanese (ja)
Inventor
Takashi Ikeda
隆 池田
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP2001130357A priority Critical patent/JP2002286379A/en
Publication of JP2002286379A publication Critical patent/JP2002286379A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • 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
    • Y02E20/16Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Heat-Pump Type And Storage Water Heaters (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

PROBLEM TO BE SOLVED: To reduce the size of the whole of an exhaust heat boiler device and simplify the whole of the device, in a heat cycle power generating device using small capacity gas turbine device and the exhaust heat boiler device. SOLUTION: A plurality of heat transfer pipes form spiral structures having the identical pitch and different diameters. The heat transfer pipes are aligned in a multiple concentric state and contained between the outer and inner drums of an annular cylindrical exhaust drum erected in a vertical direction.

Description

【発明の詳細な説明】 【0001】 【発明の属する技術分野】本発明はガスタービン装置と
排熱ボイラ装置を用いた熱サイクル動力発生装置の排熱
ボイラ装置ならびに温水発生装置に関わる。 【0002】 【従来の技術】ガスタービン装置と排熱ボイラ装置を用
いた熱サイクル動力発生装置として、従来コンバインド
サイクル装置やチェンサイクル装置が数千kWから数十
万kWの大・中容量機として用いられてきた。かかる動
力発生装置を構成する排熱ボイラ装置の代表例を 【図2】に示す。Aはエコノマイザ伝熱管、Bは蒸気ド
ラム、Cは下降管、Dは前部蒸発器伝熱管、Eは後部蒸
発器伝熱管、Fは一次過熱器伝熱管、Gは二次過熱器伝
熱管、Hは脱硝装置、Iは排気胴である。熱交換を行う
伝熱管は基本的に直線状の形状をしている。排気ガスは
一方向に流れ、一重構造の四角断面を有する排気胴は大
気と直接に接する。かかる従来の技術を小容量の熱サイ
クル動力発生装置の排熱ボイラ装置として適用すると、
装置全体は長大となり、多数の小口径伝熱管の連結が錯
綜し、排気胴内側の壁面部が複雑な構造となる。また内
部を高温の排気ガスが流れる排気胴は熱の散逸防止、火
傷防止のために排気胴に遮熱板や保温材を取付ける必要
がある。また排気ガスに多量の蒸気成分を含む場合、管
外表面に水膜が凝縮または付着する。鉛直方向の伝熱管
においてはその一部は排気ガスの流れによって後方へ吹
き飛ばされるが、他は重力により伝熱管の管外表面に沿
って下方へ流れる。そのため鉛直方向の伝熱管構造にお
いては管外表面に多量の水膜が形成され易く、水膜が管
外の排気ガスと管内の水の熱交換特性を著しく阻害す
る。 【0003】 【発明が解決しようとする課題】本発明の目的は小容量
のガスタービン装置と排熱ボイラ装置を用いた熱サイク
ル動力発生装置において、従来の排熱ボイラ装置に関す
る技術を適用した場合に生じる前述の課題を解決する簡
素小型の排熱ボイラ装置を新たに提供することである。 【0004】 【課題を解決するための手段】本発明による蒸気発生装
置を、ガスタービン装置と排熱ボイラ装置と背圧タービ
ン装置を用いた熱サイクル動力発生装置(特願2000
−132975)に適用した場合の構造を 【図1】に示す。1は原動機、2は仝空気圧縮機、3は
仝燃焼器、4は仝ガスタービン段落、5は仝蒸気タービ
ン段落、6はポンプ段落、7は発電機、8は吸気フィル
ター、9は本発明による排熱ボイラ装置、10は仝排熱
ボイラ装置における環状円筒排気胴の外胴、11は仝内
胴、12は仝最外胴、13は仝排熱ボイラ装置における
多重螺旋状の伝熱管群を示す。原動機1と排熱ボイラ装
置9の組合せ構造の全体的な立体イメージを与える斜視
図を 【図3】に示す。また多重螺旋伝熱管群の立体イメージ
を与える斜視図を 【図4】に示す。下部よりの給水aは発電機7を冷却し
た後、タービン軸内部を通りポンプ段落6で昇圧され、
原動機1の外周に設けられたポンプ吐出ヘッダ17へ導
かれる。ヘッダで分岐された高圧水bは内胴11の内側
の各連結管18を通り、環状円筒排気胴の下部にてその
中に入り、螺旋直径の異なる各伝熱管13へ導かれる。
本発明による排熱ボイラ装置9は貫流ボイラ形式であ
る。環状円筒排気胴の上部に出口を有する各螺旋状伝熱
管13を出た蒸気cは内胴11の内側の連結管18′を
通り原動機1の外周に設けられた蒸気ヘッダ19へと導
かれる。一方、環状円筒形の排熱ボイラ装置9の内胴1
1中心部に取付けられた原動機1に下部より吸込まれた
空気dは、蒸気成分を多量に含む高温の排気ガスeとな
って原動機1より上方に排出する。排出後直ちに排気ガ
スeの流れは反転し、環状円筒の排熱ボイラ伝熱部13
へ上部より入り、下部から排出する。排気ガスfは其処
で再び反転し、外胴10と最外胴12の間を通り上部よ
り排出する。螺旋状伝熱管13の表面に凝縮した水膜は
排気ガスの流れと重力の方向が一致する下方へ容易に吹
き飛び、環状排気胴の底辺に溜まり、ドレンhとして外
へ導かれる。ここで各螺旋状伝熱管13は相互に全長が
異なり、管内の圧損が異なる。最外周の伝熱管の圧損に
合わせて、その差を極力減らす目的で他の伝熱管の入口
部において絞り14を設ける。または外周側の伝熱管口
径を大きく、内周側の伝熱管口径を小さくすることによ
っても各伝熱管の圧損の均一化を図ることが可能であ
る。本発明による排熱ボイラ装置9を、ガスタービン装
置と排熱ボイラ装置と背圧タービン装置を用いた熱サイ
クル動力発生装置に適用した場合に、排熱ボイラ装置9
からの排気ガスは未だ蒸気成分を含んでいる。その潜熱
をさらに回収するため、 【図5】に示すように、冷水kを水噴射装置21によっ
て多孔板式トレイ22を抜け出てきた排気ガスgに向け
て噴霧し、両者の直接接触熱交換によって温水1を発生
させる温水発生装置20を排熱ボイラ装置9の排気ガス
出口の先に付加することも有効である。かかる直接接触
方式の温水発生装置20を用いれば小型な装置によって
効果的な排熱回収が可能となる。なお当該直接接触熱交
換器の下部に大きな温水溜23を設け貯湯槽として兼用
することも可能である。 【0005】 【発明の実施の形態】 【図3】は本発明による排熱ボイラ装置9の実施形態の
全体的な立体イメージを示す。 【図4】は伝熱管群13の立体イメージを示すと共に、 【図6】に熱サイクル図を示す熱サイクル動力発生装置
における複圧式排熱ボイラ装置の伝熱部の実施形態を示
す。伝熱管群の間に挿入する円筒状の仕切板15によっ
て伝熱管群13は二分され、外側の伝熱管群13′に高
圧水b′を通し、内側の伝熱管群13′′に低圧水
b′′を通す。排気ガスeは軸方向の適切な位置に設け
た通路16によって分岐され( 【図3】は最上流部での分岐の場合を示す)、各々下方
へ流れる。本発明による排熱ボイラ装置9の子午断面上
での管配列は碁盤目配列、千鳥配列の何れも可能であ
り、 【図3】においては外側の高圧伝熱管群13′が千鳥配
列、内側の低圧伝熱管群13′′が碁盤目配列になって
いる。コジェネレーション用の排熱ボイラ装置9として
本発明を適用するにあたり、高温の蒸気を必要とする場
合には、ボイラ出口の伝熱管や連結管の中間、もしくは
タービン入口蒸気ヘッダ19から外へ取出す。本発明に
よる排熱ボイラ装置9を、ガスタービン装置と排熱ボイ
ラ装置と背圧タービン装置を用いた熱サイクル動力発生
装置に適用した場合に、装置の起動停止時に排熱ボイラ
装置9より出る蒸気,水が原動機をバイパスすることが
可能なように、切替弁を蒸気ヘッダの後流に設けること
はスムーズな運転のために有効である。また運転中に伝
熱管に水垢が付着し、伝熱特性が劣化するのを防止する
ために、適切な水処理された給水を用いることが望まれ
る。燃焼ガスに含まれる化学成分を一切給湯内に混入さ
せない場合には、 【図5】に示すような直接接触熱交換器に代わり、多重
螺旋伝熱管を用いた温水発生器を排熱ボイラ装置伝熱管
群の下部に直列または並列に取付けることも可能であ
る。ただし 【図5】に示す直接接触熱交換器を用いる場合に比し
て、伝熱部体積の増加は免れ難い。なお、管群の流体関
連振動が問題になる場合は、環状円筒排気胴の円周上適
当な数個所に、半径方向に向き伝熱管配列に対応する円
孔を有する支え板により振動を抑制することができる。
支え板の取付けは、螺旋形状の各伝熱管を支え板に対し
回転させながら組立てる。 【0006】 【発明の効果】本発明にもとづく合理的な伝熱管群13
によって、800(1/m)以上の伝熱面密度(伝熱面
積/体積)を有する簡素な小型熱交換器を得る。この値
はシェルアンドチューブ形式の伝熱面密度70〜120
や、プレート形式の伝熱面密度150〜300を大きく
超え、フィンアンドチューブ式やコルゲートフィン式の
複雑な構造を有するコンパクト熱交換器の値に匹敵す
る。本発明を40kW級の発電容量を有するコジェネレ
ーション装置に適用すると、その概略の外形寸法は直径
400mm、高さ400mmの円筒形状となり、同等容
量の従来機に比べ数分の一の大きさとなる。また排熱ボ
イラ装置とガスタービン装置と背圧タービン装置を用い
た熱サイクル動力発生装置に本発明を適用すると、原動
機1や発電機7を排熱ボイラ装置9の中心部に配置する
ことにより、装置の構成機器全てを容易に一体化するこ
とができる。また原動機1を排熱ボイラ装置9の中心部
に配置し、その原動機1からの放熱を排熱ボイラ装置9
が再利用する本構造は、最外胴12の内側を低温の排気
ガスfが流れる構造と相俟って、熱サイクル全体として
の放熱損失を著しく軽減する。また最外胴12の温度が
低いことは火傷防止のための遮熱板や保温部材を不要と
し、それらによる外形寸法の増大を防止する。また排熱
ボイラ装置9と同一中心軸上に組立てられる原動機1に
とっては、排熱ボイラ装置9が温度分布等に軸対象性を
有することで、外部条件の軸非対象性に基づく不均一変
形が無く、回転部と静止部の間隙を縮小できる利点を有
する。また原動機1の外周に配置する排熱ボイラ装置9
は、原動機1の回転部が万一破損した場合に破片が有す
る運動エネルギーを吸収し、破片の外部飛散を防止す
る。また排熱ボイラ装置9の構造として排気胴と伝熱管
群に接触部が無いことは、両者の熱膨張差に基づく応力
発生や排気ガスのシールに関連する支障を取除く。また
複雑なヘッダや管寄せを伝熱管群近傍に持たない本構造
は、水垢やスケールの清掃を容易にし、メインテナンス
性を向上させる。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust heat boiler and a hot water generator of a heat cycle power generator using a gas turbine and an exhaust heat boiler. 2. Description of the Related Art As a heat cycle power generation device using a gas turbine device and a waste heat boiler device, a conventional combined cycle device or chain cycle device has been used as a large / medium capacity machine of several thousand to several hundred thousand kW. Has been used. FIG. 2 shows a typical example of a waste heat boiler device constituting such a power generation device. A is an economizer heat transfer tube, B is a steam drum, C is a downcomer tube, D is a front evaporator heat transfer tube, E is a rear evaporator heat transfer tube, F is a primary superheater heat transfer tube, G is a secondary superheater heat transfer tube, H is a denitration device, and I is an exhaust cylinder. A heat transfer tube that performs heat exchange has a basically linear shape. The exhaust gas flows in one direction, and the exhaust cylinder having a single-section square cross section is in direct contact with the atmosphere. When such a conventional technique is applied as a waste heat boiler of a small-capacity heat cycle power generator,
The whole device becomes long, the connection of many small-diameter heat transfer tubes becomes complicated, and the wall surface inside the exhaust cylinder has a complicated structure. Further, it is necessary to attach a heat shield plate or a heat insulating material to the exhaust cylinder in which high-temperature exhaust gas flows inside to prevent heat dissipation and burns. If the exhaust gas contains a large amount of vapor components, a water film condenses or adheres to the outer surface of the tube. Some of the heat transfer tubes in the vertical direction are blown backward by the flow of exhaust gas, while others flow downward along the outer surface of the heat transfer tubes by gravity. For this reason, in the vertical heat transfer tube structure, a large amount of water film is easily formed on the outer surface of the tube, and the water film significantly impairs the heat exchange characteristics of the exhaust gas outside the tube and the water inside the tube. [0003] An object of the present invention is to provide a heat cycle power generation device using a small-capacity gas turbine device and a waste heat boiler device when the technology related to the conventional waste heat boiler device is applied. It is another object of the present invention to provide a simple and compact exhaust heat boiler that solves the above-mentioned problems. [0004] A steam generator according to the present invention is a heat cycle power generator using a gas turbine unit, a waste heat boiler unit, and a back pressure turbine unit (Japanese Patent Application No. 2000-2000).
FIG. 1 shows a structure in the case of applying the method to FIG. 1 is a prime mover, 2 is an air compressor, 3 is a combustor, 4 is a gas turbine stage, 5 is a steam turbine stage, 6 is a pump stage, 7 is a generator, 8 is an intake filter, and 9 is the present invention. Waste heat boiler device, 10 is {the outer cylinder of the annular cylindrical exhaust drum in the waste heat boiler device, 11} is the inner trunk, 12 is the {outermost trunk, 13} is the multi-spiral heat transfer tube group in the waste heat boiler device Is shown. FIG. 3 is a perspective view showing an overall three-dimensional image of the combined structure of the prime mover 1 and the exhaust heat boiler device 9. FIG. 4 is a perspective view showing a three-dimensional image of the multiple spiral heat transfer tube group. After cooling the generator 7, the water supply a from the lower part passes through the inside of the turbine shaft and is boosted in the pump stage 6.
It is guided to a pump discharge header 17 provided on the outer periphery of the prime mover 1. The high-pressure water b branched off by the header passes through each connecting pipe 18 inside the inner body 11, enters into the lower part of the annular cylindrical exhaust body, and is guided to each heat transfer pipe 13 having a different helical diameter.
The waste heat boiler device 9 according to the invention is of the once-through boiler type. The steam c exiting from each of the spiral heat transfer tubes 13 having an outlet at the upper portion of the annular cylindrical exhaust drum is guided to a steam header 19 provided on the outer periphery of the motor 1 through a connecting pipe 18 ′ inside the inner drum 11. On the other hand, the inner cylinder 1 of the annular cylindrical exhaust heat boiler device 9
Air d sucked from below into the prime mover 1 attached to the center of the vehicle 1 becomes high-temperature exhaust gas e containing a large amount of vapor components and is discharged above the prime mover 1. Immediately after the discharge, the flow of the exhaust gas e is reversed, and the heat transfer section 13 of the exhaust heat
Enter from above and discharge from below. The exhaust gas f is then reversed again and passes between the outer shell 10 and the outermost shell 12 and is discharged from above. The water film condensed on the surface of the helical heat transfer tube 13 easily blows down downward where the direction of gravity matches the flow of the exhaust gas, accumulates at the bottom of the annular exhaust drum, and is guided to the outside as a drain h. Here, the spiral heat transfer tubes 13 have different overall lengths and different pressure losses in the tubes. A throttle 14 is provided at the inlet of another heat transfer tube for the purpose of minimizing the difference in accordance with the pressure loss of the outermost heat transfer tube. Alternatively, the pressure loss of each heat transfer tube can be made uniform by increasing the diameter of the heat transfer tube on the outer peripheral side and decreasing the diameter of the heat transfer tube on the inner peripheral side. When the waste heat boiler device 9 according to the present invention is applied to a heat cycle power generation device using a gas turbine device, a waste heat boiler device, and a back pressure turbine device, the waste heat boiler device 9
Exhaust gas still contains vapor components. In order to further recover the latent heat, as shown in FIG. 5, cold water k is sprayed toward the exhaust gas g that has exited the perforated plate type tray 22 by the water injection device 21, and hot water is generated by direct contact heat exchange between the two. It is also effective to add a hot water generating device 20 for generating 1 to the end of the exhaust gas outlet of the exhaust heat boiler device 9. If such a direct contact type hot water generator 20 is used, effective heat recovery can be achieved with a small device. In addition, it is also possible to provide a large warm water reservoir 23 below the direct contact heat exchanger and also serve as a hot water storage tank. FIG. 3 shows an overall three-dimensional image of an embodiment of a waste heat boiler device 9 according to the present invention. FIG. 4 shows a three-dimensional image of the heat transfer tube group 13 and FIG. 6 shows an embodiment of a heat transfer portion of a double-pressure exhaust heat boiler device in a heat cycle power generation device whose heat cycle diagram is shown. The heat transfer tube group 13 is divided into two by a cylindrical partition plate 15 inserted between the heat transfer tube groups, high-pressure water b 'is passed through the outer heat transfer tube group 13', and low-pressure water b is passed through the inner heat transfer tube group 13 ''. '' Through. The exhaust gas e is branched off by a passage 16 provided at an appropriate position in the axial direction (FIG. 3 shows a case of branching at the most upstream portion), and flows downward. The pipe arrangement on the meridional section of the exhaust heat boiler device 9 according to the present invention can be any of a grid arrangement and a staggered arrangement. In FIG. The low-pressure heat transfer tube groups 13 "are arranged in a grid pattern. When applying the present invention as the waste heat boiler device 9 for cogeneration, when high temperature steam is required, the steam is taken out from the middle of the heat transfer tube or the connection tube at the boiler outlet or from the turbine inlet steam header 19. When the exhaust heat boiler device 9 according to the present invention is applied to a heat cycle power generation device using a gas turbine device, an exhaust heat boiler device, and a back pressure turbine device, steam emitted from the exhaust heat boiler device 9 at the time of starting and stopping the device. Providing a switching valve downstream of the steam header so that water can bypass the prime mover is effective for smooth operation. In addition, in order to prevent scales from adhering to the heat transfer tubes during operation and to prevent heat transfer characteristics from deteriorating, it is desired to use water that has been appropriately treated with water. In the case where no chemical components contained in the combustion gas are mixed into the hot water supply, a hot water generator using multiple spiral heat transfer tubes is used instead of a direct contact heat exchanger as shown in FIG. It is also possible to mount them in series or in parallel at the lower part of the heat tube group. However, compared with the case of using the direct contact heat exchanger shown in FIG. 5, an increase in the volume of the heat transfer section is inevitable. If fluid-related vibration of the tube group is a problem, the vibration is suppressed by a support plate having circular holes oriented in the radial direction and corresponding to the arrangement of the heat transfer tubes at appropriate locations on the circumference of the annular cylindrical exhaust drum. be able to.
The mounting of the support plate is performed while rotating each of the spiral heat transfer tubes with respect to the support plate. According to the present invention, a reasonable heat transfer tube group 13 is provided.
Thereby, a simple small heat exchanger having a heat transfer surface density (heat transfer area / volume) of 800 (1 / m) or more is obtained. This value is the shell and tube type heat transfer surface density of 70 to 120.
Also, it greatly exceeds the plate type heat transfer surface density of 150 to 300, and is comparable to the value of a compact heat exchanger having a complicated structure of a fin-and-tube type or a corrugated fin type. When the present invention is applied to a cogeneration apparatus having a power generation capacity of a 40 kW class, its general outer dimensions are a cylindrical shape having a diameter of 400 mm and a height of 400 mm, which is several times smaller than that of a conventional machine having the same capacity. When the present invention is applied to a heat cycle power generation device using a waste heat boiler device, a gas turbine device, and a back pressure turbine device, by disposing the prime mover 1 and the generator 7 at the center of the waste heat boiler device 9, All the components of the apparatus can be easily integrated. In addition, the prime mover 1 is disposed at the center of the exhaust heat boiler device 9, and heat radiation from the prime mover 1 is
This structure, which is re-used, together with the structure in which the low-temperature exhaust gas f flows inside the outermost body 12, significantly reduces the heat dissipation loss in the entire heat cycle. In addition, the low temperature of the outermost body 12 eliminates the need for a heat shield plate and a heat insulating member for preventing burns, and prevents an increase in the outer dimensions due to these. Further, for the prime mover 1 assembled on the same central axis as the exhaust heat boiler device 9, since the exhaust heat boiler device 9 has axial symmetry in temperature distribution and the like, non-uniform deformation based on axial asymmetry in external conditions is prevented. Therefore, there is an advantage that the gap between the rotating part and the stationary part can be reduced. Further, a waste heat boiler device 9 arranged on the outer periphery of the prime mover 1
Absorbs the kinetic energy of the fragments in the event that the rotating part of the motor 1 is broken, thereby preventing the fragments from scattering outside. Further, the absence of the contact portion between the exhaust body and the heat transfer tube group as the structure of the exhaust heat boiler device 9 eliminates the stress generation due to the difference in thermal expansion between the two and the trouble related to the sealing of the exhaust gas. In addition, this structure, which does not have a complicated header or header near the heat transfer tube group, facilitates cleaning of scale and scale and improves maintainability.

【図面の簡単な説明】 【図1】本発明による蒸気発生装置9を、ガスタービン
装置と排熱ボイラ装置と背圧タービン装置を用いた熱サ
イクル動力発生装置に適用した場合の構造断面図で、 【特許の請求範囲】 【請求項1】より 【請求項5】を示す。 【図2】従来の動力発生装置を構成する代表的な排熱ボ
イラ装置の構造断面図 【図3】原動機1と排熱ボイラ装置9の組合せ構造の全
体的な立体イメージを与える斜視図 【図4】多重螺旋伝熱管群13の立体イメージと複圧式
排熱ボイラ装置の細部実施形態の立体イメージを与える
斜視図 【図5】冷水を噴霧し排気ガスとの直接接触熱交換によ
って温水を発生させる装置20の原理図で、 【特許の請求範囲】 【請求項6】を示す。 【図6】複圧式の排熱ボイラ装置とガスタービン装置と
背圧タービン装置を用いた熱サイクル動力発生装置の熱
サイクル図 【符号の説明】 1は原動機、2は仝空気圧縮機、3は仝燃焼器、4は仝
ガスタービン段落、5は仝蒸気タービン段落、6はポン
プ段落、7は発電機、8は吸気フィルター、9は本発明
による排熱ボイラ装置、10は仝排熱ボイラ装置におけ
る環状円筒排気胴の外胴、11は仝内胴、12は仝最外
胴、13は仝排熱ボイラ装置における多重螺旋状の伝熱
管群、13′は高圧伝熱管、13′′は低圧伝熱管、1
4は圧損調整用の絞り機構、14′は低圧伝熱管用の絞
り機構、15は仕切板、16は仕切板に設けた分岐通
路、17はポンプ吐出ヘッダ、18はポンプ吐出ヘッダ
と伝熱管の連結管、18′は伝熱管と蒸気ヘッダの連結
管、19は蒸気ヘッダ、20は温水発生装置、21は水
噴射装置、22は多孔板トレイ、23は温水溜を示す。
aはポンプ装置への給水、b、b′はポンプ装置によっ
て昇圧された給水、b′′は絞り14′によって減圧さ
れた給水、cは排熱ボイラ装置における発生蒸気、dは
原動機の吸気、eは原動機より排出する排気ガス、fは
排熱ボイラ伝熱管部を排出する排気ガス、gは環状円筒
排熱ボイラ装置の上部出口より排出する排気ガス、hは
環状円筒排熱ボイラ装置の下部より排出するドレン、i
はガス圧縮機へ供給する燃料ガス、jは発電機で発生す
る電力、kは温水発生装置への給水、lは温水発生装置
より取出す温水を示す。Aは従来の大型排熱ボイラ装置
におけるエコノマイザ伝熱管である。同じくBは蒸気ド
ラム、Cは下降管、Dは前部蒸発器伝熱管、Eは後部蒸
発器伝熱管、Fは一次過熱器伝熱管、Gは二次過熱器伝
熱管、Hは脱硝装置、Iは排気胴である。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a structural cross-sectional view when a steam generator 9 according to the present invention is applied to a heat cycle power generator using a gas turbine device, a waste heat boiler device, and a back pressure turbine device. [Claims 1] to [Claim 5] are shown. FIG. 2 is a structural cross-sectional view of a typical exhaust heat boiler device constituting a conventional power generation device. FIG. 3 is a perspective view showing an overall three-dimensional image of a combined structure of a prime mover 1 and an exhaust heat boiler device 9. 4 is a perspective view showing a three-dimensional image of the multi-spiral heat transfer tube group 13 and a three-dimensional image of a detailed embodiment of the double-pressure exhaust heat boiler device. FIG. 5: Spraying cold water and generating hot water by direct contact heat exchange with exhaust gas. The principle of the device 20 is shown in the following claims. FIG. 6 is a heat cycle diagram of a heat cycle power generation device using a double-pressure exhaust heat boiler device, a gas turbine device, and a back pressure turbine device [Description of References] 1 is a prime mover, 2 is an air compressor, and 3 is仝 Combustor, 4 仝 Gas turbine stage, 5 仝 Steam turbine stage, 6 ポ ン プ Pump stage, 7 発 電 Generator, 8 排 Intake filter, 9 排 Waste heat boiler device according to the present invention, 仝 10 仝 Waste heat boiler device , The outer cylinder of the annular cylindrical exhaust cylinder, 11 is the inner cylinder, 12 is the outermost cylinder, 13 is the multi-spiral heat transfer tube group in the exhaust heat boiler, 13 ′ is the high pressure heat transfer tube, and 13 ″ is the low pressure Heat transfer tube, 1
4 is a throttle mechanism for adjusting pressure loss, 14 'is a throttle mechanism for a low-pressure heat transfer tube, 15 is a partition plate, 16 is a branch passage provided in the partition plate, 17 is a pump discharge header, and 18 is a pump discharge header and a heat transfer tube. A connecting pipe, 18 'is a connecting pipe between the heat transfer pipe and the steam header, 19 is a steam header, 20 is a hot water generator, 21 is a water jetting apparatus, 22 is a perforated plate tray, and 23 is a hot water reservoir.
a is the feed water to the pump device, b and b 'are the feed water pressurized by the pump device, b''is the feed water depressurized by the throttle 14', c is the steam generated in the exhaust heat boiler device, d is the intake air of the prime mover, e is exhaust gas discharged from the prime mover, f is exhaust gas discharged from the heat transfer boiler heat transfer tube, g is exhaust gas discharged from the upper outlet of the annular cylindrical heat boiler, and h is lower part of the annular cylindrical heat boiler. Drain to drain, i
Denotes fuel gas supplied to the gas compressor, j denotes electric power generated by the generator, k denotes water supply to the hot water generator, and l denotes hot water taken out from the hot water generator. A is an economizer heat transfer tube in a conventional large-sized waste heat boiler device. Similarly, B is a steam drum, C is a downcomer, D is a front evaporator heat transfer tube, E is a rear evaporator heat transfer tube, F is a primary superheater heat transfer tube, G is a secondary superheater heat transfer tube, H is a denitration device, I is an exhaust cylinder.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F22B 1/18 F22B 1/18 K 27/04 27/04 A F24H 1/00 631 F24H 1/00 631D F28C 3/08 F28C 3/08 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) F22B 1/18 F22B 1/18 K 27/04 27/04 A F24H 1/00 631 F24H 1/00 631D F28C 3/08 F28C 3/08

Claims (1)

【特許請求の範囲】 【請求項1】管外の排気ガスにより管内の水を熱し蒸気
を発生させるシェルアンドチューブ熱交換器に関し、複
数の伝熱管を螺旋直径の相互に異なる同一ピッチの螺旋
状構造とし、各々の伝熱管を多重同心円状に配列し、環
状円筒排気胴の外胴と内胴の間に収める装置 【請求項2】 【請求項1】において、内胴の内側に配置したポンプ吐
出ヘッダと各伝熱管の入口を、タービン入口の蒸気ヘッ
ダと各伝熱管の出口を直接に連結する装置 【請求項3】 【請求項2】において、各管内の圧損が同一に近づくよ
うに、伝熱管またはヘッダとの連結管にオリフィスを設
置する装置、もしくは伝熱管または連結管の局所を圧潰
し管内流れに対し絞り機能を有する装置 【請求項4】 【請求項1】において螺旋状伝熱管ならびに環状円筒排
気胴の中心軸が鉛直方向に向く装置 【請求項5】 【請求項4】において内胴の内側に配置する原動機の高
温排気ガスを当該装置の上部より取り入れ、伝熱管にお
ける熱交換を終え、下方へ排出する排気ガスを当該装置
の下方部にて反転させ、外胴と外胴のさらに外側に配置
した最外胴の間を上方に流し、排気ガスを上方から吐出
させる装置 【請求項6】 【請求項1】において熱交換を終えた排気ガス中に冷水
を噴霧し、排気ガスとの直接接触熱交換によって温水を
発生させる装置
The present invention relates to a shell and tube heat exchanger for generating steam by heating water in a tube by exhaust gas outside the tube, wherein a plurality of heat transfer tubes are formed in a spiral shape having the same pitch and different spiral diameters. A device in which the heat transfer tubes are arranged in multiple concentric circles so as to be housed between an outer cylinder and an inner cylinder of an annular cylindrical exhaust cylinder. 2. A pump arranged inside an inner cylinder in claim 1. Apparatus for directly connecting the discharge header and the inlet of each heat transfer tube to the steam header of the turbine inlet and the outlet of each heat transfer tube. 3. The apparatus according to claim 2, wherein the pressure loss in each tube approaches the same. A device for installing an orifice in a heat transfer tube or a connection tube with a header, or a device having a function of squeezing a local portion of a heat transfer tube or a connection tube and restricting a flow in the tube. And circular circle 5. A device in which the central axis of the cylinder exhaust cylinder is oriented vertically. 5. The high-temperature exhaust gas of a prime mover arranged inside the inner cylinder is taken in from the upper part of the device, and heat exchange in the heat transfer tube is completed. An apparatus for inverting exhaust gas discharged downward at a lower portion of the apparatus, flowing upward between an outer body and an outermost body disposed further outside the outer body, and discharging the exhaust gas from above. 6. An apparatus for generating cold water by spraying cold water into exhaust gas which has been subjected to heat exchange according to claim 1, and by direct contact heat exchange with the exhaust gas.
JP2001130357A 2001-03-24 2001-03-24 Steam and hot water generating device Pending JP2002286379A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001130357A JP2002286379A (en) 2001-03-24 2001-03-24 Steam and hot water generating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001130357A JP2002286379A (en) 2001-03-24 2001-03-24 Steam and hot water generating device

Publications (1)

Publication Number Publication Date
JP2002286379A true JP2002286379A (en) 2002-10-03

Family

ID=18978750

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2002286379A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20060010037A (en) * 2004-07-27 2006-02-02 장근섭 Turbine-mounted boilers and water-cooled turbine engines
JP2010002100A (en) * 2008-06-19 2010-01-07 Suntory Holdings Ltd Heating pressurization system
JP2012122379A (en) * 2010-12-07 2012-06-28 Toyota Motor Corp Gas turbine power generator
CN107262446A (en) * 2017-08-02 2017-10-20 叶政 A kind of high-efficiency modularized saturated vapor cleaning equipment
EP3303802A1 (en) * 2015-06-01 2018-04-11 Samad Power Limited Micro-chp gas fired boiler with gas turbine assembly
EP4246052A1 (en) * 2022-03-15 2023-09-20 Aic Spólka Akcyjna Cogeneration boiler

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20060010037A (en) * 2004-07-27 2006-02-02 장근섭 Turbine-mounted boilers and water-cooled turbine engines
JP2010002100A (en) * 2008-06-19 2010-01-07 Suntory Holdings Ltd Heating pressurization system
JP2012122379A (en) * 2010-12-07 2012-06-28 Toyota Motor Corp Gas turbine power generator
EP3303802A1 (en) * 2015-06-01 2018-04-11 Samad Power Limited Micro-chp gas fired boiler with gas turbine assembly
US10731555B2 (en) 2015-06-01 2020-08-04 Samad Power Limited Micro-CHP gas fired boiler with gas turbine assembly
CN107262446A (en) * 2017-08-02 2017-10-20 叶政 A kind of high-efficiency modularized saturated vapor cleaning equipment
CN107262446B (en) * 2017-08-02 2023-09-08 微一绿色环保科技(海盐)有限公司 Efficient modularized saturated steam cleaning equipment
EP4246052A1 (en) * 2022-03-15 2023-09-20 Aic Spólka Akcyjna Cogeneration boiler

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