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JPS6365818B2 - - Google Patents
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JPS6365818B2 - - Google Patents

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Publication number
JPS6365818B2
JPS6365818B2 JP58237889A JP23788983A JPS6365818B2 JP S6365818 B2 JPS6365818 B2 JP S6365818B2 JP 58237889 A JP58237889 A JP 58237889A JP 23788983 A JP23788983 A JP 23788983A JP S6365818 B2 JPS6365818 B2 JP S6365818B2
Authority
JP
Japan
Prior art keywords
boiler
heating section
temperature heating
preheater
temperature
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
Application number
JP58237889A
Other languages
Japanese (ja)
Other versions
JPS60132055A (en
Inventor
Sadahiko Maeda
Shinjiro Yokota
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.)
Ube Corp
Original Assignee
Ube Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP58237889A priority Critical patent/JPS60132055A/en
Publication of JPS60132055A publication Critical patent/JPS60132055A/en
Publication of JPS6365818B2 publication Critical patent/JPS6365818B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02GHOT GAS OR COMBUSTION-PRODUCT POSITIVE-DISPLACEMENT ENGINE PLANTS; USE OF WASTE HEAT OF COMBUSTION ENGINES; NOT OTHERWISE PROVIDED FOR
    • F02G5/00Profiting from waste heat of combustion engines, not otherwise provided for
    • F02G5/02Profiting from waste heat of exhaust gases
    • 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
    • Y02E20/14Combined heat and power generation [CHP]
    • 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
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Supercharger (AREA)

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は、たとえば船舶用機関などとして用い
られるデイーゼル機関の排熱回収装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to an exhaust heat recovery device for a diesel engine used, for example, as a marine engine.

〔従来技術〕[Prior art]

近年、度重なる石油価格の高騰によつて各方面
において省エネルギ化を図ることが求められてお
り、これは重油等を燃料とするデイーゼル機関も
例外ではなく、その高効率化を図るべく各種の改
善が進められ、またこれに合わせて従来無駄に廃
棄されていた排ガスのもつ熱エネルギをも効率よ
く回収してその再利用化を図ることが望まれてい
る。特に、後者のように排熱を回収しこれを他の
機器、装置のエネルギ源として利用することは、
余分なエネルギの浪費をなくし、その節減化を図
るうえでその効果は大きいものである。
In recent years, due to the repeated rises in oil prices, there has been a demand for energy conservation in various fields, and diesel engines that use heavy oil as fuel are no exception, and various efforts are being made to improve their efficiency. As improvements are being made, there is a desire to efficiently recover and reuse the thermal energy of exhaust gas, which was previously wasted. In particular, recovering waste heat and using it as an energy source for other equipment and devices, as in the latter case,
This is highly effective in eliminating excess energy waste and reducing energy consumption.

そして、この種の排熱回収装置として、比較的
高温域にある排熱を回収して再利用するようにし
たものについては従来から種々提案されている
が、効率面からまだまだ改善の余地が残されてお
り、また中、低温域にある排熱をも合わせて効率
よく回収してその再利用化を図ることができ得る
ものは未だ提案されておらず、何らかの対策を講
じることが必要とされている。
Various proposals have been made for this type of waste heat recovery device that recovers and reuses waste heat in a relatively high temperature range, but there is still room for improvement in terms of efficiency. Furthermore, no method has yet been proposed that can efficiently recover and reuse waste heat in medium to low temperature ranges, and it is necessary to take some measures. ing.

これを第1図に示す従来例を用いて簡単に説明
すると、図中符号1は、デイーゼル機関、2,3
は、それぞれその吸、排気管で、これら吸、排気
管2,3にまたがつて排気タービン式の過給機4
が設けられている。この過給機4は排気管3内の
排ガスにより吸気管2内の吸入空気を加圧するた
めのもので、これにより排ガスのもつ熱エネルギ
の一部が吸入空気加圧用として、回収利用され
る。
To briefly explain this using a conventional example shown in FIG. 1, reference numeral 1 in the figure indicates a diesel engine,
are the intake and exhaust pipes respectively, and an exhaust turbine type supercharger 4 is installed astride these intake and exhaust pipes 2 and 3.
is provided. The supercharger 4 is used to pressurize the intake air in the intake pipe 2 using the exhaust gas in the exhaust pipe 3, so that a part of the thermal energy of the exhaust gas is recovered and used for pressurizing the intake air.

5は過給機4を通過した排ガスが導入されるこ
とによりその熱エネルギを回収する排熱回収ボイ
ラで、このボイラ5内には排熱回収サイクル系6
を構成する蒸発部7、給水予熱部8が設けられて
いる。そして、これら蒸発部7および給水予熱部
8にて水タンク9から給水ポンプ10により供給
される水が排ガスのもつ熱エネルギを回収して順
次蒸発し、そお熱水が蒸発部7および給水予熱部
8の下流側に設けられた気水分離器11にて分離
されて蒸気として取出される。この取出された蒸
気は、たとえば発電機を駆動する蒸気タービン等
の熱利用機器12のエネルギ源として使用される
ほか、その一部は燃料油ストレージタンク13の
加熱用などに利用されている。そして、この熱利
用された蒸気は復水されて戻り凝縮水としてタン
ク9に戻り、再びボイラ5側に給水されるもので
ある。なお、前記気水分離器11は、ボイラ5の
給水予熱部8の出口側に接続されるとともに、こ
の給水予熱部8から導入された熱水が蒸発部7に
接続された循環路14を循環ポンプ14aにて順
次流れることにより加熱されて気水分離が行なわ
れるものである。また、図中15はデイーゼル機
関1の各部を冷却する冷却水循環路で、海水等に
より熱せられた冷却水を冷却するクーラ15a
と、その循環用のポンプ15bとを備えている。
Reference numeral 5 denotes an exhaust heat recovery boiler that recovers thermal energy by introducing exhaust gas that has passed through the supercharger 4. Inside this boiler 5, an exhaust heat recovery cycle system 6 is installed.
An evaporating section 7 and a water supply preheating section 8 are provided. The water supplied from the water tank 9 by the water pump 10 in the evaporator 7 and the water supply preheating section 8 recovers the thermal energy of the exhaust gas and evaporates in sequence. It is separated in a steam separator 11 provided on the downstream side of 8 and taken out as steam. This extracted steam is used as an energy source for a heat utilization device 12 such as a steam turbine that drives a generator, and a portion of it is also used for heating a fuel oil storage tank 13 and the like. This heat-utilized steam is then condensed and returned to the tank 9 as return condensed water, and is again supplied to the boiler 5 side. The steam-water separator 11 is connected to the outlet side of the feed water preheating section 8 of the boiler 5, and the hot water introduced from the feed water preheating section 8 is circulated through a circulation path 14 connected to the evaporation section 7. The water is heated by sequentially flowing through the pump 14a, and water and steam are separated. In addition, 15 in the figure is a cooling water circulation path that cools each part of the diesel engine 1, and a cooler 15a that cools the cooling water heated by seawater or the like.
and a pump 15b for circulation.

ところで、上述したように過給機4を用いたデ
イーゼル機関1にあつては、吸気管2を流れる吸
入空気が過給機4にて断熱圧縮されるため発熱
し、その温度が約160℃程度まで上昇してしまう
ものであつた。そして、このままでは空気の容積
が増えすぎ、その吸入空気密度が低下するため、
吸気管2の途中に空気冷却器16を設け、空気温
度を約60℃程度まで低下させて所望の機関出力が
得られるようにすることが従来から行なわれてい
る。ここで、図中17はこの空気冷却器16の冷
却水循環路で、ポンプ17aと海水等による、間
接的な冷却を行なうクーラ17bとが設けられて
いる。
By the way, as mentioned above, in the case of the diesel engine 1 using the supercharger 4, the intake air flowing through the intake pipe 2 is adiabatically compressed by the supercharger 4, which generates heat, and the temperature is about 160°C. It was something that would rise to . If this continues, the volume of air will increase too much and the density of the intake air will decrease.
Conventionally, an air cooler 16 is provided in the middle of the intake pipe 2 to lower the air temperature to about 60° C. so that a desired engine output can be obtained. Here, 17 in the figure is a cooling water circulation path of this air cooler 16, and is provided with a pump 17a and a cooler 17b that performs indirect cooling using seawater or the like.

しかしながら、このような構成では、せつかく
排ガスを利用して加圧した吸入空気のもつ熱エネ
ルギを単に空気冷却器16にて冷却して廃棄して
いるだけであり、無駄であるばかりでなく、空気
冷却器16としてもある程度の容量をもつものが
必要で、省エネルギ対策上からその改善が求めら
れている。
However, in such a configuration, the thermal energy of the pressurized intake air using exhaust gas is simply cooled and disposed of in the air cooler 16, which is not only wasteful, but also wasteful. The air cooler 16 also needs to have a certain capacity, and its improvement is required from the viewpoint of energy saving.

また、上述した構成において、ボイラ5の入口
側排ガス温度は約320℃程度で、一方出口側温度
は約171℃程度であり、より一層回収効率を高め
ることが望まれており、さらに回収した熱エネル
ギの再利用化にあたつてもその多様化を図ること
が要求されている。
In addition, in the above configuration, the temperature of the exhaust gas on the inlet side of the boiler 5 is about 320°C, while the temperature on the outlet side is about 171°C. There is a need to diversify energy when it comes to reusing energy.

しかし、その一方において、注意すべきこと
は、排ガス中に含まれるイオウ(S)分の酸化に
よる、無水硫酸(SO3)が水分と化合し硫酸
(H2SO4)となつてボイラ5等の伝熱管壁に結露
することがないようにその管壁温度を酸露点(約
135℃)以上に保つことである。すなわち、上述
したようなSO3分の結露がボイラ5の伝熱管の管
壁などに付着すると、その部分が腐蝕して損傷し
てしまうもので、このような点を考慮することが
必要とされている。
However, on the other hand, it should be noted that due to the oxidation of the sulfur (S) contained in the exhaust gas, sulfuric anhydride (SO 3 ) combines with moisture and becomes sulfuric acid (H 2 SO 4 ), which is released into boilers 5, etc. To prevent condensation on the heat transfer tube walls, the temperature of the tube walls should be adjusted to the acid dew point (approximately
temperature (135℃) or higher. In other words, if the condensation of SO 3 as mentioned above adheres to the tube wall of the heat exchanger tube of the boiler 5, that part will corrode and be damaged, so it is necessary to take this point into consideration. ing.

〔発明の概要〕[Summary of the invention]

本発明はこのような事情に鑑みてなされたもの
であり、デイーゼル機関の吸気管で過給機よりも
下流側に排熱回収サイクル系の戻り凝縮水路が接
続された予熱器を設け、この予熱器を排熱回収ボ
イラの低温加熱部を介してその高温加熱部の入口
側に接続するとともに、この予熱器よりも上流側
から分岐した戻り凝縮水のバイパス路を前記ボイ
ラの高温加熱部の入口側に接続し、かつこの高温
加熱部の出口側にフラツシユタンクを設けるとい
う簡単な構成によつて、従来無駄に捨てられてい
た吸入空気の熱エネルギを効率よく回収し、その
再利用化を図るとともに、ボイラ伝熱管壁での温
度をSO3分の酸露点以上に保ち、その腐蝕防止を
図ることができ、またボイラでの回収効率をも向
上させ、さらにフラツシユタンクにて蒸気および
熱水を得てその再利用化にあたつての多様化を図
ることが可能となるデイーゼル機関の排熱回収装
置を提供するものである。
The present invention has been made in view of these circumstances, and includes a preheater connected to a return condensation waterway of an exhaust heat recovery cycle system on the downstream side of the supercharger in the intake pipe of a diesel engine. The boiler is connected to the inlet side of the high temperature heating section of the waste heat recovery boiler via the low temperature heating section, and the return condensed water bypass path branched from the upstream side of the preheater is connected to the inlet of the high temperature heating section of the boiler. With a simple structure that connects to the side and provides a flash tank on the outlet side of this high-temperature heating section, the thermal energy of the intake air, which was previously wasted, can be efficiently recovered and reused. At the same time, it is possible to maintain the temperature on the boiler heat exchanger tube wall above the acid dew point of SO 3 minutes, preventing corrosion, and improving the recovery efficiency in the boiler. The present invention provides an exhaust heat recovery device for a diesel engine that makes it possible to obtain hot water and diversify its reuse.

〔実施例〕〔Example〕

以下、本発明を図面に示した実施例を用いて詳
細に説明する。
Hereinafter, the present invention will be explained in detail using embodiments shown in the drawings.

第2図は本発明に係るデイーゼル機関の排熱回
収装置の一実施例を示すものであり、同図におい
て第1図と同一または相当する部分には同一番号
を付してその説明は省略する。
Fig. 2 shows an embodiment of the exhaust heat recovery device for a diesel engine according to the present invention, and in the figure, the same or corresponding parts as in Fig. 1 are given the same numbers and their explanations are omitted. .

さて、本発明によれば、機関吸気管2の過給機
4下流側に、排熱回収サイクル系6を構成する予
熱器20を設け、この予熱器20に熱利用機器1
2(12A,12B,12C)や燃料油ストレー
ジタンク13からの戻り凝縮水の循環路21を接
続することにより、過給機4にて昇温された吸入
空気からの熱エネルギを効率よく回収してその再
利用化を図れるように構成している。そして、こ
の予熱器20は循環路22を介してボイラ5の低
温加熱部19に接続されるとともに、この低温加
熱部19の出口側は高温加熱部18の入口側に接
続され、前記予熱器20にて予熱された熱水を排
ガスにより加熱して昇温させるように構成されて
いる。また、前記予熱器20の上流側の循環路2
1途中には、戻り凝縮水の一部が導びかれるバイ
パス路23が分岐して設けられており、このバイ
パス路23は前記ボイラ5の高温加熱部18の入
口側に接続されている。したがつて、このような
構成によれば、循環路21内の戻り凝縮水は、前
記予熱器20とボイラ5の低温加熱部19とで熱
せられたものと、バイパス路23を通つて導びか
れたものとが、ボイラ5の高温加熱部18の入口
側で合流されてボイラ5内に導入され、排ガスに
より加熱されることになる。
Now, according to the present invention, the preheater 20 constituting the exhaust heat recovery cycle system 6 is provided downstream of the supercharger 4 in the engine intake pipe 2, and the heat utilization equipment 1 is connected to the preheater 20.
2 (12A, 12B, 12C) and the return condensed water circulation path 21 from the fuel oil storage tank 13, the thermal energy from the intake air heated by the supercharger 4 can be efficiently recovered. The structure is designed so that it can be reused. The preheater 20 is connected to the low temperature heating section 19 of the boiler 5 via the circulation path 22, and the outlet side of the low temperature heating section 19 is connected to the inlet side of the high temperature heating section 18. The system is configured to heat the hot water preheated by the exhaust gas to raise its temperature. Further, the circulation path 2 on the upstream side of the preheater 20
1, a bypass passage 23 is branched in the middle, through which a portion of the return condensed water is guided, and this bypass passage 23 is connected to the inlet side of the high-temperature heating section 18 of the boiler 5. Therefore, according to such a configuration, the return condensed water in the circulation path 21 is heated by the preheater 20 and the low-temperature heating section 19 of the boiler 5, and is guided through the bypass path 23. These are combined at the inlet side of the high-temperature heating section 18 of the boiler 5, introduced into the boiler 5, and heated by the exhaust gas.

このような構成を採用した理由は、ボイラ5内
で特に低温域にある伝熱管管壁の温度を、排ガス
中に含まれるSO3分の酸露点以上に保ち、この管
壁などへの結露による腐蝕を防止するためであ
る。すなわち、熱利用機器12(12A,12
B,12C)からの戻り凝縮水の温度が約70℃程
度である場合において、その流量が多いとき、こ
れを全量予熱器20を通すと、ボイラ5の低温加
熱部19の入口側温度が上述した酸露点以下とな
ることがある。このため、本発明は上述した予熱
器20への供給量をその一部をバイパスすること
により調整し、ボイラ5の入口側での温度が酸露
点、約135℃以上に維持できるように構成すると
ともに、バイパスされた低温水(約70℃)を、ボ
イラ5の低温加熱部19にて加熱された高温水
(約163℃)に合流させて全体の温度を酸露点以上
の約140℃程度としてボイラ5内に導入するよう
に構成している。
The reason for adopting this configuration is to maintain the temperature of the heat exchanger tube wall, which is in a particularly low temperature region in the boiler 5 , above the acid dew point of SO contained in the exhaust gas, and to prevent dew condensation on the tube wall. This is to prevent corrosion. That is, the heat utilization equipment 12 (12A, 12
When the temperature of the return condensed water from (B, 12C) is about 70°C and the flow rate is large, if the entire amount is passed through the preheater 20, the temperature on the inlet side of the low temperature heating section 19 of the boiler 5 will rise to the above level. The acid dew point may drop below the specified acid dew point. For this reason, the present invention adjusts the amount of supply to the preheater 20 described above by bypassing a part of it, so that the temperature at the inlet side of the boiler 5 can be maintained at the acid dew point, about 135° C. or higher. At the same time, the bypassed low-temperature water (approximately 70°C) is merged with the high-temperature water (approximately 163°C) heated in the low-temperature heating section 19 of the boiler 5 to bring the overall temperature to approximately 140°C, which is above the acid dew point. It is configured to be introduced into the boiler 5.

なお、前記吸気管2内の吸入空気温度は、前記
予熱器20を設けることにより約160℃から約85
℃まで低減されるもので、これを約60℃程度の機
関導入温度まで空気冷却器16にて冷却したとし
ても廃棄される熱量は少なく、省エネルギ化を、
図るうえで効果的なものであり、しかもこの空気
冷却器16での負荷が小さいことからその小型化
を図れるといつた利点もある。勿論、上述した吸
入空気を予熱器20にて必要とされる温度まで低
減できる場合には空気冷却器16を省略すること
も可能である。さらに、本実施例によれば、ボイ
ラ5での排ガスの入口側が約320℃程度であると
き、その出口側を約155℃程度とすることができ
るもので、従来に比べ排熱回収効率を高めること
も可能である。
The intake air temperature in the intake pipe 2 can be reduced from about 160°C to about 85°C by providing the preheater 20.
℃, and even if this is cooled down to the engine introduction temperature of approximately 60℃ using the air cooler 16, the amount of heat discarded is small, resulting in energy savings.
Moreover, since the load on the air cooler 16 is small, it also has the advantage of being able to be made smaller. Of course, if the above-mentioned intake air can be reduced to the required temperature by the preheater 20, the air cooler 16 can be omitted. Furthermore, according to this embodiment, when the temperature at the inlet side of the exhaust gas in the boiler 5 is about 320°C, the temperature at the outlet side can be set at about 155°C, which improves the efficiency of exhaust heat recovery compared to the conventional method. It is also possible.

また、本発明によれば、上述したボイラ5にて
得られる約233℃程度の熱水を、多段フラツシヤ
タンク24(本実施例では二段)を用いて二種類
の低圧蒸気と約120℃程度の熱水とを生じさせ、
これらの蒸気および熱水を、各種の熱利用機器1
2などにより再利用し得るようにし、その多様化
を図つている。蒸気の適用例としてはたとえばタ
ービンを回して動力あるいは発電機を介して電力
として取出すほか、種々の用途が考えられる。ま
た、熱水は図示されるように燃料油ストレージタ
ンク加熱用や冷、暖房用などに適用し得るもの
で、このような120℃の温水をも利用することに
より全体としてのシステム効率が大幅に向上す
る。
Further, according to the present invention, the hot water of about 233°C obtained in the boiler 5 described above is converted into two types of low-pressure steam and heated water of about 120°C using the multi-stage flush tank 24 (two stages in this embodiment). generate hot water,
These steam and hot water are used in various heat utilization equipment 1
2, etc., in order to make it reusable and diversify its use. Examples of the applications of steam include, for example, generating power by turning a turbine or generating electric power through a generator, as well as various other uses. In addition, as shown in the diagram, hot water can be used for heating, cooling, and space heating of fuel oil storage tanks, and by using such 120°C hot water, the overall system efficiency can be greatly increased. improves.

なお、本発明は上述した実施例構造に限定され
ず、各部の形状、構造等を適宜変形、変更するこ
とは自由で、またデイーゼル機関としても船舶用
に限定されず、種々のものに適用できるものであ
る。
It should be noted that the present invention is not limited to the structure of the embodiments described above, and the shape and structure of each part may be modified and changed as appropriate, and the present invention is not limited to use in ships as a diesel engine, and can be applied to various types of engines. It is something.

〔発明の効果〕〔Effect of the invention〕

以上説明したように、本発明に係るデイーゼル
機関の排熱回収装置によれば、吸気管の過給機下
流側に排熱回収サイクルの戻り凝縮水が流れる予
熱器を設け、この予熱器を排熱回収ボイラの低温
加熱部を介してその高温加熱部の入口側に接続す
る一方、前記予熱器の上流側から分岐された戻り
凝縮水のバイパス路もこの高温加熱部の入口側に
接続し、かつこの高温加熱部の出口側にフラツシ
ヤタンクを設けて蒸気および熱水が得られるよう
にしたので、簡単な構成にもかかわらず、従来無
駄に捨てられていた吸入空気の熱エネルギを効率
よく回収し、その有効利用化を図るとともに、ボ
イラ伝熱管壁での温度をSO3分の酸露点以上に保
ち、その腐蝕防止を図ることができ、しかもこ
の、ボイラでの回収効率をも向上させ、またフラ
ツシヤタンクにて得られる蒸気および熱水にてそ
の熱エネルギの再利用化を図るうえでその多様化
を図ることができる等の種々優れた効果がある。
As explained above, according to the exhaust heat recovery device for a diesel engine according to the present invention, a preheater is provided downstream of the supercharger in the intake pipe through which the return condensed water of the exhaust heat recovery cycle flows, and the preheater is While connected to the inlet side of the high temperature heating section of the heat recovery boiler via the low temperature heating section, a bypass path of return condensed water branched from the upstream side of the preheater is also connected to the inlet side of the high temperature heating section, In addition, a flusher tank is installed on the outlet side of this high-temperature heating section so that steam and hot water can be obtained, so despite the simple configuration, the thermal energy of the intake air, which was previously wasted, can be efficiently recovered. In addition to making effective use of SO, it is possible to maintain the temperature at the boiler heat exchanger tube wall above the acid dew point of SO 3 minutes, preventing corrosion, and improving the recovery efficiency in the boiler. In addition, there are various excellent effects such as being able to diversify the reuse of thermal energy from the steam and hot water obtained in the flasher tank.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は従来装置の概略を示す系統図、第2図
は本発明に係るデイーゼル機関の排熱回収装置の
一実施例を示す系統図である。 1……デイーゼル機関、2,3……吸、排気
管、4……過給機、5……排熱回収ボイラ、6…
…排熱回収サイクル系、12(12A,12B,
12C)……熱利用機器、13……燃料油ストレ
ージタンク、16……空気冷却器、18……高温
加熱部、19……低温加熱部、20……予熱器、
21,22……循環路、23……バイパス路、2
4……フラツシユタンク。
FIG. 1 is a system diagram showing an outline of a conventional device, and FIG. 2 is a system diagram showing an embodiment of the exhaust heat recovery device for a diesel engine according to the present invention. 1... Diesel engine, 2, 3... Suction and exhaust pipes, 4... Supercharger, 5... Exhaust heat recovery boiler, 6...
...Exhaust heat recovery cycle system, 12 (12A, 12B,
12C) ... heat utilization equipment, 13 ... fuel oil storage tank, 16 ... air cooler, 18 ... high temperature heating section, 19 ... low temperature heating section, 20 ... preheater,
21, 22...Circulation path, 23...Bypass path, 2
4...Flush tank.

Claims (1)

【特許請求の範囲】[Claims] 1 デイーゼル機関からの排ガスにより吸気管内
の吸入空気を加圧する過給機と、この過給機を通
過した排ガスが導入されその熱エネルギを回収す
る高温加熱部および低温加熱部を有する排熱回収
ボイラと、このボイラの高温加熱部出口側に接続
され蒸気および熱水を得てこれらを熱利用機器に
供給するフラツシユタンクとを備え、前記吸気管
の過給機下流側には前記熱利用機器からの戻り凝
縮水を加熱する予熱器が設けられ、かつこの予熱
器が前記ボイラの低温加熱部を経てその高温加熱
部の入口側に接続されるとともに、前記予熱器の
上流側から分岐されたバイパス路が前記ボイラの
高温加熱部の入口側に接続されていることを特徴
とするデイーゼル機関の排熱回収装置。
1 An exhaust heat recovery boiler that has a supercharger that pressurizes the intake air in the intake pipe with exhaust gas from a diesel engine, and a high-temperature heating section and a low-temperature heating section that introduce the exhaust gas that has passed through the supercharger and recover its thermal energy. and a flash tank connected to the outlet side of the high-temperature heating section of the boiler to obtain steam and hot water and supply them to the heat utilization equipment; A preheater for heating return condensed water from the boiler is provided, and this preheater is connected to the inlet side of the high temperature heating section of the boiler via the low temperature heating section, and is branched from the upstream side of the preheater. An exhaust heat recovery device for a diesel engine, characterized in that a bypass path is connected to an inlet side of a high-temperature heating section of the boiler.
JP58237889A 1983-12-19 1983-12-19 Waste-heat recovering apparatus for diesel engine Granted JPS60132055A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58237889A JPS60132055A (en) 1983-12-19 1983-12-19 Waste-heat recovering apparatus for diesel engine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58237889A JPS60132055A (en) 1983-12-19 1983-12-19 Waste-heat recovering apparatus for diesel engine

Publications (2)

Publication Number Publication Date
JPS60132055A JPS60132055A (en) 1985-07-13
JPS6365818B2 true JPS6365818B2 (en) 1988-12-16

Family

ID=17021921

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58237889A Granted JPS60132055A (en) 1983-12-19 1983-12-19 Waste-heat recovering apparatus for diesel engine

Country Status (1)

Country Link
JP (1) JPS60132055A (en)

Also Published As

Publication number Publication date
JPS60132055A (en) 1985-07-13

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