JPH0281933A - Carbon dioxide treating device for closed circuit diesel engine - Google Patents

Carbon dioxide treating device for closed circuit diesel engine

Info

Publication number
JPH0281933A
JPH0281933A JP63232534A JP23253488A JPH0281933A JP H0281933 A JPH0281933 A JP H0281933A JP 63232534 A JP63232534 A JP 63232534A JP 23253488 A JP23253488 A JP 23253488A JP H0281933 A JPH0281933 A JP H0281933A
Authority
JP
Japan
Prior art keywords
carbon dioxide
diesel engine
working fluid
absorption liquid
unwashed
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
JP63232534A
Other languages
Japanese (ja)
Inventor
Masateru Shimozu
下津 正輝
Takashi Obara
敬史 小原
Shinichi Maeda
前田 伸一
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.)
NIPPON HAKUYO KIKI KAIHATSU KYOKAI
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
NIPPON HAKUYO KIKI KAIHATSU KYOKAI
Mitsui Engineering and Shipbuilding Co 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 NIPPON HAKUYO KIKI KAIHATSU KYOKAI, Mitsui Engineering and Shipbuilding Co Ltd filed Critical NIPPON HAKUYO KIKI KAIHATSU KYOKAI
Priority to JP63232534A priority Critical patent/JPH0281933A/en
Publication of JPH0281933A publication Critical patent/JPH0281933A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02BINTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B3/00Engines characterised by air compression and subsequent fuel addition
    • F02B3/06Engines characterised by air compression and subsequent fuel addition with compression ignition
    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Landscapes

  • Output Control And Ontrol Of Special Type Engine (AREA)
  • Treating Waste Gases (AREA)

Abstract

PURPOSE:To enable a stable driving of a diesel engine without changing the volume and flow rate of an unwashed working fluid by providing a blower and an intercooler on the upper stream side of a carbon dioxide sucking device, and to enable the temperature control of the working fluid after washed with the cooling water of the diesel engine by providing a heat exchanger for gas temperature control just in the front of an intake port of the diesel engine. CONSTITUTION:An unwashed working fluid A leaving a blower 6 and an intercooler 4a is introduced into a carbon dioxide sucking device 13. The volume and flow rate of the unwashed working fluid within the carbon dioxide sucking device is made constant even when the load of a diesel engine is changed, and the diesel engine can be stably run. Further, as a heat exchanger for gas temperature control 50 controlled by the cooling water of the diesel engine is provided just in the front of an intake port 1B of the diesel engine, an excessive reduction in temperature of the working fluid after washing is prevented, and the combustion performance of the engine can be maintained satisfactorily.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、主として水中航行等に使用されるためその全
体をコンパクトに纏める必要のあるクローズドサーキッ
トディーゼル機関に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a closed-circuit diesel engine that is mainly used for underwater navigation and the like and therefore needs to be made compact as a whole.

〔従来の技術〕[Conventional technology]

クローズドサーキットディーゼル機関においては、その
排気ガスである動作流体を冷却した後、酸素を補給し、
その機関の吸気側に供給するが、燃料の燃焼により、そ
の動作流体内に炭酸ガスが増加して、機関の燃焼を困難
にすることになる。
In a closed circuit diesel engine, after cooling the working fluid, which is the exhaust gas, oxygen is supplied,
However, combustion of the fuel increases carbon dioxide gas in the working fluid, making combustion difficult for the engine.

そこで、炭酸ガスを含む未洗浄動作流体の一部、または
全部を、吸収塔で炭酸ガス吸収用の吸収液中にその炭酸
ガスを吸収させ、例えば窒素などの動作流体の成分のみ
を再び吸気側に戻して動作流体として循環再使用してい
る。
Therefore, some or all of the uncleaned working fluid containing carbon dioxide gas is absorbed into an absorption liquid for absorbing carbon dioxide gas in an absorption tower, and only the components of the working fluid, such as nitrogen, are returned to the intake side. It is recycled and reused as a working fluid.

その場合、炭酸ガスを吸収したリッチな吸収液は、加熱
させて吸収していた炭酸ガスを放出し、その炭酸ガスを
系外に排出し、炭酸ガスを放出したリーンな吸収液は炭
酸ガス吸収用の吸収塔に送られて再使用されている。
In that case, the rich absorption liquid that has absorbed carbon dioxide gas is heated to release the absorbed carbon dioxide gas and discharged to the outside of the system, and the lean absorption liquid that has released carbon dioxide gas absorbs carbon dioxide gas. It is sent to an absorption tower for reuse.

上記炭酸ガスの吸収液は、再生塔内である程度の時間、
高温状態に保つ方が再生率が良好であることが知られて
おり、一般に背の高い再生塔が必要となり、特に水中航
行用に使用されるこの種ディーゼル機関の炭酸ガス処理
装置に必要とされるコンパクト化に反するという問題が
ある。
The above carbon dioxide absorption liquid is stored in the regeneration tower for a certain period of time.
It is known that the regeneration rate is better when kept at a high temperature, and a tall regeneration tower is generally required, especially for the carbon dioxide treatment equipment of this type of diesel engine used for underwater navigation. There is a problem that it goes against the idea of compactness.

また、上記従来の装置では、排気ガスである動作流体中
にリーンな吸収液を散布する青の高い吸収塔が使用され
ており、このような吸収塔もコンパクト化の妨げとなっ
ている。
Further, in the above-mentioned conventional apparatus, a high-blue absorption tower is used to spray a lean absorption liquid into the working fluid, which is exhaust gas, and such an absorption tower also becomes an obstacle to miniaturization.

更に、従来の装置では、吸収塔で未洗浄動作流体に炭酸
ガス吸収用のリーンな吸収液のミストをノズルで噴霧し
、その下流で吸収液のミストを動作流体から分離回収し
てリッチな吸収液として再生塔に送る際、そのミスト分
離部には従来フィルタを使用しているのが普通であった
Furthermore, in conventional equipment, a mist of a lean absorption liquid for carbon dioxide absorption is sprayed onto the unwashed working fluid in the absorption tower using a nozzle, and downstream, the absorption liquid mist is separated and collected from the working fluid to create a rich absorption stream. Conventionally, when sending the liquid as a liquid to the regeneration tower, a filter has conventionally been used in the mist separation section.

しかしながら、フィルタは元来自浄能力が弱く、しかも
液滴も含む大きなミストの粒子は顛単に除去しても、小
さなミストの粒子を除去しようとすると、そのフィルタ
に大きな差圧をつけなければならず、ミストの除去効率
をあげるためには、そのフィルタの設備コスト及びメン
テナンスコストが増加するという問題があった。
However, filters inherently have a weak self-cleaning ability, and although they can easily remove large mist particles, including droplets, a large differential pressure must be applied to the filter to remove small mist particles. However, in order to improve the mist removal efficiency, there is a problem in that the equipment cost and maintenance cost of the filter increase.

そこで、クローズドサーキットディーゼル機関の未洗浄
動作流体の炭酸ガス処理装置に、従来必要とされた再生
塔や吸収塔のごとき塔槽類を使用せずに、装置全体のコ
ンパクト化をはかると共に、リッチな吸収液をリーンな
吸収液、機関の潤滑油及び機関からの未洗浄動作流体で
加熱し、吸収液の再生の度合を高め、更にIJ−ンな吸
収液のミストを噴霧した未洗浄動作流体から、洗浄後動
作流体と炭酸ガスのリッチな吸収液とを容易に、かつ除
去効率よく分離するクローズドサーキットディーゼル機
関の炭酸ガス処理装置が第2図の系統図のごとく案出さ
れており、以下にその概要を説明する。
Therefore, in the carbon dioxide treatment equipment for the unwashed working fluid of a closed circuit diesel engine, we did not use the conventionally required towers and tanks such as regeneration towers and absorption towers, making the entire equipment more compact, and making the rich carbon dioxide gas treatment equipment more compact. The absorption liquid is heated with lean absorption liquid, engine lubricating oil, and uncleaned working fluid from the engine to increase the degree of regeneration of the absorption liquid, and then the unwashed working fluid is sprayed with a mist of IJ-lean absorption liquid. A carbon dioxide treatment device for a closed-circuit diesel engine has been devised, as shown in the system diagram in Figure 2, which separates the working fluid after cleaning and the carbon dioxide-rich absorption liquid easily and with high removal efficiency. The outline will be explained below.

即ち、クローズドサーキットのディーゼル機関lの排気
口IAから排出された排気ガスは矢印Aで示す未洗浄動
作流体として過給機のタービン2を駆動した後、炭酸ガ
ス吸収液再生装置I7を経由して、冷却水Wを散布する
排気冷却装置14及び遠心分離機5を通り、炭酸ガス吸
収装置13に入り、そこで炭酸ガス吸収用のリーンな吸
収液をノズル19により噴霧させた後、この炭酸ガス吸
収装置13の出側に設けられた遠心分離機22で洗浄後
動作流体Jと、炭酸ガスを吸収したリッチな吸収液とに
分離される。
That is, the exhaust gas discharged from the exhaust port IA of the closed-circuit diesel engine I drives the turbine 2 of the supercharger as an unwashed working fluid shown by arrow A, and then passes through the carbon dioxide absorption liquid regeneration device I7. , passes through an exhaust cooling device 14 that sprays cooling water W and a centrifugal separator 5, and enters the carbon dioxide absorption device 13, where a lean absorption liquid for carbon dioxide absorption is sprayed by a nozzle 19, and then this carbon dioxide absorption A centrifugal separator 22 provided on the outlet side of the device 13 separates the washed working fluid J into a rich absorption liquid that has absorbed carbon dioxide gas.

上記の洗浄後動作流体Jには酸素供給管7から酸素ガス
02が補給された上、過給機のブロワ−6で加圧され、
そしてインタークーラ4aで冷却水Wにより冷却された
後、ディーゼル機関1の吸気口IBに供給されると共に
、このディーゼル機関1の燃焼室には燃料供給管8から
燃料Fが供給され、一方、ディーゼル機関1には機関冷
却水流路9が設けられ、冷却水が循環するようになって
いる。
The above-mentioned cleaning working fluid J is supplied with oxygen gas 02 from the oxygen supply pipe 7, and is pressurized by the blower 6 of the supercharger.
After being cooled by the cooling water W in the intercooler 4a, the fuel F is supplied to the intake port IB of the diesel engine 1, and the fuel F is supplied to the combustion chamber of the diesel engine 1 from the fuel supply pipe 8. The engine 1 is provided with an engine cooling water passage 9 through which cooling water circulates.

また、このディーゼル機関1の潤滑油は矢印Cで示す潤
滑油流路を通り熱交換器11により炭酸ガス吸収液再生
装置17へ送られるリッチな吸収液を加熱するようにな
っている。
Further, the lubricating oil of this diesel engine 1 passes through a lubricating oil flow path shown by arrow C and heats a rich absorption liquid that is sent to a carbon dioxide absorption liquid regeneration device 17 by a heat exchanger 11.

次に、上記の遠心分離機22で分離されたリッチな吸収
液は、熱交換器3にてリーンな吸収液と熱交換すること
により熱を与えられ、更に前記熱交換器11により加熱
された後、炭酸ガス吸収液再生装置17に導入され、炭
酸ガスを放出した後、リーンな吸収液として吐出される
ようになっている。なお、図中において20で示すのは
それぞれポンプである。
Next, the rich absorption liquid separated by the centrifugal separator 22 is given heat by exchanging heat with the lean absorption liquid in the heat exchanger 3, and is further heated by the heat exchanger 11. Thereafter, it is introduced into a carbon dioxide absorption liquid regeneration device 17, and after releasing carbon dioxide gas, it is discharged as a lean absorption liquid. In addition, in the figure, the reference numeral 20 indicates a pump.

以上に説明した炭酸ガス処理装置では、以前のごとく再
生塔及び吸収塔のような塔槽類を使用しないので、全体
をコンパクトに纏められると共に、炭酸ガスを含んだリ
ッチな吸収液は、リーンな吸収液と、機関の潤滑油とで
加熱された後、未洗浄動作流体で加熱されながら炭酸ガ
スを放出するので、その吸収液の再生の度合が高まり、
更に、リーンな吸収液のミストを噴霧された未洗浄動作
流体から、洗浄後動作流体と炭酸ガスのリッチな吸収液
とに遠心分離機を介して容易に、かつ除去効率よく分離
されることになり、円滑な機関運転が保たれるという利
点がある。
The carbon dioxide treatment equipment described above does not use towers and tanks such as regeneration towers and absorption towers as in the past, so the entire structure can be made compact, and the rich absorption liquid containing carbon dioxide gas can be stored in a lean manner. After being heated by the absorption liquid and the engine's lubricating oil, carbon dioxide gas is released while being heated by the unwashed working fluid, increasing the degree of regeneration of the absorption liquid.
Furthermore, the unwashed working fluid sprayed with a mist of lean absorption liquid can be easily and efficiently separated into the washed working fluid and the carbon dioxide rich absorption liquid using a centrifugal separator. This has the advantage that smooth engine operation can be maintained.

しかしながら、上記数に案出されている炭酸ガス処理装
置では、炭酸ガス吸収装置13における未洗浄動作流体
Aの圧は常に大気圧近くに保たれるため、ディーゼル機
関1の負荷が変化すると、それに応じてこの炭酸ガス吸
収装置13内の未洗浄動作流体Aの流速が変化する。
However, in the carbon dioxide treatment device devised above, the pressure of the unwashed working fluid A in the carbon dioxide absorption device 13 is always maintained close to atmospheric pressure, so when the load of the diesel engine 1 changes, Accordingly, the flow rate of the unwashed working fluid A within the carbon dioxide absorption device 13 changes.

このことは、炭酸ガスを吸収するリーンな吸収液と未洗
浄動作流体Aとの接触時間が主機関負荷によって大幅に
変化したり、炭酸ガス吸収装置13の下流に設けられた
遠心分離機22の気液分離の効率にも変化がおこること
になり、これらの変化はディーゼル機関1の高負荷の場
合はど問題になる。
This means that the contact time between the lean absorption liquid that absorbs carbon dioxide gas and the unwashed working fluid A changes significantly depending on the main engine load, and that Changes will also occur in the efficiency of gas-liquid separation, and these changes will become a problem when the diesel engine 1 is under high load.

〔発明の目的〕[Purpose of the invention]

本発明は、前記の炭酸ガス処理装置における問題点を解
消するためになされたものであり、主機関であるディー
ゼル機関の負荷が変化しても、未洗浄動作流体の流速も
、吸収液と未洗浄動作流体との接触時間も常にほぼ一定
に保たれ、安定した運転を保持できるクローズドサーキ
ットディーゼル機関の炭酸ガス処理装置を提供すること
を目的としたものである。
The present invention has been made in order to solve the problems in the carbon dioxide treatment equipment described above, and even if the load of the main engine, the diesel engine, changes, the flow rate of the unwashed working fluid remains the same as that of the absorbing liquid. The object of the present invention is to provide a carbon dioxide treatment device for a closed-circuit diesel engine that can maintain stable operation by keeping the contact time with the cleaning working fluid almost constant.

〔発明の概要〕[Summary of the invention]

上記の目的を達成するため本発明のクローズドサーキッ
トディーゼル機関の炭酸ガス処理装置は、そのディーゼ
ル機関からの排気ガスである未洗浄動作流体の炭酸ガス
を吸収させたリッチな吸収液を、そのディーゼル機関の
潤滑油で加熱した後、その未洗浄動作流体で加熱しなが
ら炭酸ガスを放出させてリーンな吸収液に再生する炭酸
ガス吸収液再生装置と、その装置から送られるリーンな
吸収液を、上記リッチな吸収液と熱交換させた後に、そ
のディーゼル機関の過給機のブロワ−及びその下流のイ
ンタークーラを経由した未洗浄動作流体中にフラッシュ
させる炭酸ガス吸収装置と、その装置の出側に設けられ
、このディーゼル機関の吸気口にガス温度調整用熱交換
器経由送られる洗浄後動作流体とリッチな吸収液とに分
離する遠心分離機とから構成される。
In order to achieve the above object, the carbon dioxide treatment device for a closed circuit diesel engine of the present invention uses a rich absorption liquid that has absorbed carbon dioxide from an unwashed working fluid, which is exhaust gas from the diesel engine, to the diesel engine. A carbon dioxide absorption liquid regeneration device that regenerates the lean absorption liquid by heating it with lubricating oil and then releasing carbon dioxide gas while heating it with the unwashed working fluid, and the lean absorption liquid sent from the device. A carbon dioxide absorption device that flushes into the unwashed working fluid via the blower of the turbocharger of the diesel engine and the intercooler downstream thereof after exchanging heat with the rich absorption liquid, and the exit side of the device. The diesel engine is equipped with a centrifugal separator that separates the washed working fluid, which is sent to the intake port of the diesel engine via a heat exchanger for gas temperature adjustment, and a rich absorption liquid.

以上の構成からなる炭酸ガス処理装置では、前記従来の
装置とほぼ同様な機能を有しながら、ブロワ−及びイン
タークーラを炭酸ガス吸収装置の上流側に設けたことに
より、主機関であるディーゼル機関の負荷の変化によっ
ても炭酸ガス吸収装置での未洗浄動作流体の体積及び流
量は変化せず安定した運転が行なわれる。
The carbon dioxide treatment device with the above configuration has almost the same functions as the conventional device, but by providing the blower and intercooler upstream of the carbon dioxide absorption device, the main engine, the diesel engine, Even if the load changes, the volume and flow rate of the uncleaned working fluid in the carbon dioxide absorption device do not change, and stable operation is performed.

また、酸素供給管から洗浄後動作流体に酸素を供給する
場合、クローズドサーキットディーゼル機関ではその酸
素として液体酸素を蒸発したものを供給しているので通
常0℃以下の低温であるが、ディーゼル機関の吸気口の
直前にガス温度調整用熱交換器を設けて、このディーゼ
ル機関の冷却水で温度の調整をしている。
In addition, when oxygen is supplied from the oxygen supply pipe to the working fluid after cleaning, in a closed circuit diesel engine, the oxygen is supplied as evaporated liquid oxygen, so the temperature is usually below 0°C. A heat exchanger for gas temperature adjustment is installed just before the intake port, and the temperature is adjusted using cooling water from the diesel engine.

〔実施例〕〔Example〕

以下図面を参照して本発明の炭酸ガス処理装置の一実施
例について第1図の系統図で説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the carbon dioxide treatment apparatus of the present invention will be described below with reference to the drawings and the system diagram shown in FIG.

まず、この炭酸ガス処理装置は、第2図の従来の装置と
同様に主として水中航行等に使用されるクローズドサー
キットディーゼル機関に装(Ii#されるものであり、
第2図の従来例とほぼ同様な構成と機能を有するもので
あり、第1図と第2図とで同じ部品は同じ部品番号で示
しており、そのフローについても前記第2図の従来例と
重複する説明は省略し、主として第2図との相違点を説
明する。
First, like the conventional device shown in Fig. 2, this carbon dioxide treatment device is installed in a closed-circuit diesel engine mainly used for underwater navigation, etc.
It has almost the same configuration and function as the conventional example shown in Fig. 2, and the same parts are indicated by the same part numbers in Figs. 1 and 2, and its flow is also similar to the conventional example shown in Fig. 2. Duplicate explanations will be omitted, and differences from FIG. 2 will be mainly explained.

そこで、本発明の炭酸ガス処理装置では、このディーゼ
ル機関1の過給機のタービン2で回転されるブロワ−6
及びその下流のインタークーラ4aを出た未洗浄動作流
体Aを炭酸ガス吸収装置13に導入し、そこで炭酸ガス
吸収用のリーンな吸収液をノズル19により噴霧させ、
その炭酸ガス吸収装置13から出た洗浄後動作流体りを
遠心分離機22で洗浄後動作流体Jと、炭酸ガスを吸収
したリッチな吸収液とに分離している。
Therefore, in the carbon dioxide treatment device of the present invention, the blower 6 rotated by the turbine 2 of the supercharger of the diesel engine 1
And the unwashed working fluid A exiting the intercooler 4a downstream thereof is introduced into the carbon dioxide absorption device 13, where a lean absorption liquid for carbon dioxide absorption is sprayed by the nozzle 19,
The washed working fluid discharged from the carbon dioxide absorption device 13 is separated by a centrifugal separator 22 into a washed working fluid J and a rich absorption liquid that has absorbed carbon dioxide gas.

次に、ディーゼル機関1の吸気口IBの直前に、このデ
ィーゼル機関1の冷却水、即ち温水により温度が調整さ
れるガス温度調整用熱交換器50を洗浄後動作流体Jの
流路に設けている。
Next, immediately before the intake port IB of the diesel engine 1, a gas temperature adjustment heat exchanger 50 whose temperature is adjusted by the cooling water of the diesel engine 1, that is, hot water, is installed in the flow path of the cleaned working fluid J. There is.

このように温度調整を行なうのは酸素供給管7から追加
される酸素0□が液体酸素を蒸発させたもので、通常0
℃以下の低温であるからであり、これにより洗浄後動作
流体Jの温度の下がりすぎを防止することができ、機関
の燃焼性能を良好に保つことができる。
The temperature is adjusted in this way because the oxygen added from the oxygen supply pipe 7 is evaporated from liquid oxygen;
This is because the temperature is at a low temperature of .degree.

〔発明の効果〕〔Effect of the invention〕

以上に説明したように、本発明のクローズドサーキット
ディーゼル機関の炭酸ガス処理装置では、従来のごとき
再生塔及び吸収塔のような塔槽類を使用しないので、装
置全体をコンパクトに纏めうるという利点があり、特に
水中用動力源等に使用されるディーゼル機関等には本発
明を有効に適用することができる。
As explained above, the carbon dioxide treatment device for a closed circuit diesel engine of the present invention does not use towers and tanks such as conventional regeneration towers and absorption towers, so it has the advantage that the entire device can be made compact. In particular, the present invention can be effectively applied to diesel engines and the like used as underwater power sources.

また、炭酸ガスを含むリッチな吸収液の再生用熱源とし
てリーンな吸収液、そのディーゼル機関の潤滑油及び排
気ガスである未洗浄動作流体を有効に利用することによ
り、ディーゼル機関から排出されるエネルギーの有効利
用をはがりうると共に、充分に再生されたリーンな吸収
液をより多く循環させうろことになり、炭酸ガスの吸収
除去の性能向上がはかれるという利点がある。
In addition, by effectively using the lean absorption liquid, the lubricating oil of the diesel engine, and the unwashed working fluid that is the exhaust gas as a heat source for regenerating the rich absorption liquid containing carbon dioxide, we can generate energy that is emitted from the diesel engine. This has the advantage that it is possible to make more effective use of carbon dioxide, and to circulate more of the sufficiently regenerated lean absorption liquid, thereby improving the performance of absorbing and removing carbon dioxide gas.

更に、本発明の装置では、炭酸ガス吸収装置内でリーン
な吸収液を噴霧された未洗浄動作流体を、遠心分離機に
より洗浄後動作流体とリッチな吸収液とに、除去効率よ
く、しかも容易に分離でき、その結果、吸収液の回収率
を高めるという効果があり、しかも従来のフィルタに比
して安価な設備コスト及びランニングコストで有利な吸
収液の分離が行なわれる。
Furthermore, in the device of the present invention, the unwashed working fluid that has been sprayed with a lean absorption liquid in the carbon dioxide absorption device can be efficiently and easily removed by using a centrifugal separator to convert the unwashed working fluid into a washed working fluid and a rich absorption liquid. As a result, it has the effect of increasing the recovery rate of the absorbent, and moreover, the absorbent can be separated advantageously with lower equipment costs and running costs than conventional filters.

特に、本発明の炭酸ガス処理装置では、炭酸ガス吸収装
置内での未洗浄動作流体の体積流量が主機関のディーゼ
ル機関の負荷が変化しても一定であり、炭酸ガス吸収用
のリーンな吸収液と未洗浄動作流体との接触時間も主機
関の負荷にかかわらず常にほぼ一定に保たれ、このクロ
ーズドサーキットディーゼル機関の安定した運転が行わ
れるという利点がある。
In particular, in the carbon dioxide treatment device of the present invention, the volumetric flow rate of the unwashed working fluid in the carbon dioxide absorption device is constant even when the load of the main diesel engine changes, and the lean absorption for carbon dioxide gas absorption is achieved. The contact time between the liquid and the unwashed working fluid is also kept almost constant regardless of the load on the main engine, which provides the advantage of stable operation of this closed-circuit diesel engine.

また、主機関のディーゼル機関の吸込み口の直前にガス
温度調整用熱交換器を設けることで、主機関の吸気側へ
の洗浄後動作流体における液体酸素を蒸発させた酸素ガ
スの追加による温度の下がり過ぎを防止でき、機関燃焼
性能を良好に維持できるという利点もある。
In addition, by installing a gas temperature adjustment heat exchanger just before the intake port of the diesel engine of the main engine, the temperature can be increased by adding oxygen gas, which is obtained by evaporating liquid oxygen in the working fluid after cleaning, to the intake side of the main engine. Another advantage is that it prevents the fuel from dropping too low and maintains good engine combustion performance.

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

第1図は本発明の一実施例におけるクローズドサーキッ
トディーゼル機関の炭酸ガス処理装置の系統図、第2図
は従来の炭酸ガス処理装置の系統図である。 ■・・・ディーゼル機関、IB・・・吸気口、3・・・
熱交換器、4a・・・インターターラ、6・・・ブロワ
−11・・・熱交換器、13・・・炭酸ガス吸収装置、
17・・・炭酸ガス吸収液再生装置、22・・・遠心分
離機、50・・・ガス温度調整用熱交換器、A・・・未
洗浄動作流体、C・・・潤滑油路、J・・・洗浄後動作
流体。
FIG. 1 is a system diagram of a carbon dioxide treatment device for a closed circuit diesel engine according to an embodiment of the present invention, and FIG. 2 is a system diagram of a conventional carbon dioxide treatment device. ■...Diesel engine, IB...Intake port, 3...
Heat exchanger, 4a... intertellar, 6... blower 11... heat exchanger, 13... carbon dioxide absorption device,
17... Carbon dioxide absorption liquid regeneration device, 22... Centrifugal separator, 50... Heat exchanger for gas temperature adjustment, A... Unwashed working fluid, C... Lubricating oil path, J. ...Working fluid after cleaning.

Claims (1)

【特許請求の範囲】[Claims] クローズドサーキットディーゼル機関からの未洗浄動作
流体中の炭酸ガスを吸収させたリッチな吸収液を、該デ
ィーゼル機関の潤滑油で加熱した後、該未洗浄動作流体
で加熱しながら炭酸ガスを放出させてリーンな吸収液に
再生する炭酸ガス吸収液再生装置と、その装置から送ら
れるリーンな吸収液を、上記リッチな吸収液と熱交換さ
せた後に該ディーゼル機関の過給機のブロワー及びその
下流のインタークーラを経由した未洗浄動作流体中にフ
ラッシュさせる炭酸ガス吸収装置と、その装置の出側に
設けられ、該ディーゼル機関の吸気口にガス温度調整用
熱交換器経由送られる洗浄後動作流体と、リッチな吸収
液とを分離する遠心分離機とからなるクローズドサーキ
ットディーゼル機関の炭酸ガス処理装置。
A rich absorption liquid that absorbs carbon dioxide in an unwashed working fluid from a closed-circuit diesel engine is heated with the lubricating oil of the diesel engine, and then carbon dioxide is released while being heated with the unwashed working fluid. A carbon dioxide absorption liquid regeneration device regenerates into a lean absorption liquid, and after the lean absorption liquid sent from the device undergoes heat exchange with the rich absorption liquid, the blower of the turbocharger of the diesel engine and its downstream A carbon dioxide absorption device that flushes into unwashed working fluid that has passed through an intercooler, and a cleaned working fluid that is provided at the outlet side of the device and sent to the intake port of the diesel engine via a gas temperature adjustment heat exchanger. A carbon dioxide treatment device for a closed-circuit diesel engine that consists of a centrifugal separator that separates carbon dioxide from a rich absorption liquid.
JP63232534A 1988-09-19 1988-09-19 Carbon dioxide treating device for closed circuit diesel engine Pending JPH0281933A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63232534A JPH0281933A (en) 1988-09-19 1988-09-19 Carbon dioxide treating device for closed circuit diesel engine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63232534A JPH0281933A (en) 1988-09-19 1988-09-19 Carbon dioxide treating device for closed circuit diesel engine

Publications (1)

Publication Number Publication Date
JPH0281933A true JPH0281933A (en) 1990-03-22

Family

ID=16940841

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63232534A Pending JPH0281933A (en) 1988-09-19 1988-09-19 Carbon dioxide treating device for closed circuit diesel engine

Country Status (1)

Country Link
JP (1) JPH0281933A (en)

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