JP5296735B2 - Ships equipped with NOx reduction devices - Google Patents

Ships equipped with NOx reduction devices Download PDF

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JP5296735B2
JP5296735B2 JP2010077622A JP2010077622A JP5296735B2 JP 5296735 B2 JP5296735 B2 JP 5296735B2 JP 2010077622 A JP2010077622 A JP 2010077622A JP 2010077622 A JP2010077622 A JP 2010077622A JP 5296735 B2 JP5296735 B2 JP 5296735B2
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reducing agent
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寿 芳賀
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Mitsui Engineering and Shipbuilding Co Ltd
Mitsui E&S Holdings Co Ltd
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Mitsui E&S Holdings Co Ltd
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Description

本発明は、船舶搭載の内燃機関から排出される排気ガス中のNOxを浄化するための選択接触還元触媒を備えたNOx低減装置を配備した船舶に関し、より詳細には、選択接触還元触媒で使用する尿素等の還元剤の貯蔵タンクの配置に工夫をこらしたNOx低減装置を配備した船舶に関する。   The present invention relates to a ship provided with a NOx reduction device equipped with a selective catalytic reduction catalyst for purifying NOx in exhaust gas discharged from an internal combustion engine mounted on a ship, and more specifically, used in a selective catalytic reduction catalyst. The present invention relates to a ship provided with a NOx reduction device that has been devised in the arrangement of storage tanks for reducing agents such as urea.

船舶に搭載されたディーゼルエンジン等の内燃機関から排出される排気ガス中のNOx(窒素酸化物)を低減する技術として、選択接触還元触媒を備えたNOx低減装置を用いる方法がある。この方法では、アンモニア又はアンモニアを発生する尿素水等の還元剤をSCR(Selective Catalytic Reduction)触媒と呼ばれる選択接触還元触媒に供給してNOxをアンモニア(NH3)で窒素(N2)と水(H2O)に還元して浄化している。 As a technique for reducing NOx (nitrogen oxide) in exhaust gas discharged from an internal combustion engine such as a diesel engine mounted on a ship, there is a method of using a NOx reduction device equipped with a selective catalytic reduction catalyst. In this method, ammonia or a reducing agent such as urea water that generates ammonia is supplied to a selective catalytic reduction catalyst called an SCR (Selective Catalytic Reduction) catalyst, and NOx is ammonia (NH 3 ) with nitrogen (N 2 ) and water ( It is reduced to H 2 O) for purification.

このSCR方法の例として、エンジンと脱硝触媒との間にNOxの吸着剤を配置し、NOxを、排気ガス温度が低い時には吸着剤に吸着させて、高温になったときに脱離させて、排気ガスに初期から含まれているNOxと吸着剤から脱離したNOxを、選択接触還元法によって還元させる船舶排気ガスの浄化方法および浄化装置が提案されている(例えば、特許文献1参照。)。   As an example of this SCR method, an NOx adsorbent is disposed between the engine and the denitration catalyst, NOx is adsorbed by the adsorbent when the exhaust gas temperature is low, and desorbed when the temperature becomes high, A ship exhaust gas purifying method and a purifying apparatus that reduce NOx contained in the exhaust gas from the beginning and NOx desorbed from the adsorbent by a selective catalytic reduction method have been proposed (see, for example, Patent Document 1). .

また、船舶の主機関の排ガス浄化用触媒脱硝装置において、触媒脱硝装置に供給する還元剤を保管する還元剤保管タンクの改善を図るために、還元剤を供給するための還元剤保管タンクとして、海洋輸送用コンテナの規格を有するタンクコンテナを利用した舶用還元剤供給設備も提案されている(例えば、特許文献2参照。)。   Moreover, in the catalyst denitration device for exhaust gas purification of the main engine of the ship, as a reducing agent storage tank for supplying the reducing agent in order to improve the reducing agent storage tank for storing the reducing agent supplied to the catalyst denitrating device, Marine reducing agent supply equipment using a tank container having a standard for marine transport containers has also been proposed (see, for example, Patent Document 2).

近年、船舶における排気ガス規制も厳しくなる傾向にあり、航路によってはNOx排出量の低減が要求される場合があり、それに伴ってNOx低減のために多量の尿素水等の還元剤が必要とされるようになってきている。この還元剤は航路によっては少なくとも一航海分を船舶に搭載する必要がある。そのため、航路とその航路における排気ガス規制にもよるが、この選択接触還元触媒を備えたNOx低減装置を用いる方法では、一般的に使用燃料の10%程度の還元剤を消費するために、大容量の還元剤タンクの装備が必要となり、船体構造(船体付きタンク)からなる大型タンクを設ける必要が生じる。   In recent years, exhaust gas regulations in ships tend to be stricter, and there are cases where reduction of NOx emissions is required depending on the route, and a large amount of reducing agent such as urea water is required to reduce NOx. It is becoming. Depending on the route of the reducing agent, it is necessary to mount at least one voyage on the ship. Therefore, although depending on the route and the exhaust gas regulations in the route, the method using the NOx reduction device equipped with this selective catalytic reduction catalyst generally consumes about 10% of the reducing agent, so that a large amount of the reducing agent is consumed. It is necessary to equip a capacity reducing agent tank and to provide a large tank having a hull structure (tank with hull).

一方、還元剤の一つであり、使用が予測される尿素水の保管条件は、低温サイドでは、尿素がマイナス10℃付近で結晶化(尿素濃度約32%〜33%において)するために、容器内の温度はマイナス10℃以上の液温になるように保管する必要がある。また、高温サイドでは、40℃になると製品寿命が4カ月程度となり、温度上昇により大きく製品の寿命が低下するために、約30℃以下で保管する必要がある。これに対して、夏場等の外気温度や機関室の室温は、この30℃を超える場合がある。   On the other hand, the storage condition of urea water that is one of the reducing agents and is expected to be used is that, on the low temperature side, urea crystallizes around minus 10 ° C. (at a urea concentration of about 32% to 33%). It is necessary to store the container so that the temperature in the container is minus 10 ° C. or higher. On the high temperature side, when the temperature is 40 ° C., the product life is about 4 months, and the product life is greatly reduced due to the temperature rise. Therefore, it is necessary to store the product at about 30 ° C. or less. On the other hand, the outside air temperature in summer and the room temperature of the engine room may exceed 30 ° C.

また、船舶の内燃機関が配置される機関室は、船体の後部に設けられることが多く、図2及び図3に示すように、この機関室周りの水面下(喫水より下)の下部部分や、機関室より後側の船尾部分は痩せた形状をしているため還元剤タンクの配置は困難である。そのため、機関室の内部又は周辺に、比較的大容量で、かつ、温度管理が必要な還元剤タンクを配置することには工夫が必要であるという問題がある。   Further, the engine room in which the internal combustion engine of the ship is arranged is often provided at the rear part of the hull. As shown in FIGS. 2 and 3, the lower part of the water surface around the engine room (below the draft) Since the stern part behind the engine room has a thin shape, it is difficult to arrange the reducing agent tank. Therefore, there is a problem that it is necessary to devise to arrange a reducing agent tank having a relatively large capacity and requiring temperature management in or around the engine room.

特開2002−295241号公報JP 2002-295241 A 特開平10−203487号公報JP-A-10-203487

本発明は、上述の状況を鑑みてなされたものであり、その目的は、外気温度や機関室内の温度が高温になっても、還元剤タンクに保管した尿素水等の還元剤の温度を適正な保管温度の範囲内に維持できて、還元剤の寿命の低下を防ぐことができ、しかも、内燃機関の排気ガスの排出経路と還元剤タンクの間の距離を短くすることができるNOx低減装置を配備した船舶を提供することにある。   The present invention has been made in view of the above-described situation, and the purpose thereof is to appropriately set the temperature of the reducing agent such as urea water stored in the reducing agent tank even when the outside air temperature or the temperature in the engine room becomes high. NOx reduction device that can be maintained within a range of storage temperatures, can prevent a reduction in the life of the reducing agent, and can reduce the distance between the exhaust gas exhaust path of the internal combustion engine and the reducing agent tank It is to provide a ship having deployed.

上記の目的を達成するための本発明のNOx低減装置を配備した船舶は、船舶に搭載した内燃機関から排出される排気ガス中のNOxを浄化するための選択接触還元触媒を備えたNOx低減装置を配備した船舶において、前記選択接触還元触媒に供給する還元剤を貯蔵するための還元剤タンクの外側の一部又は全部にコファダムを設けて船体付タンクとして形成すると共に、前記コファダムの一部又は全部に通水できるように構成される。この通水には、コファダムに海水又は水を注水して貯めることと、注水及び排水を同時に行って海水又は水を入れ替えることを含む。   A ship equipped with the NOx reduction device of the present invention for achieving the above object is a NOx reduction device provided with a selective catalytic reduction catalyst for purifying NOx in exhaust gas discharged from an internal combustion engine mounted on the ship. In which a cofferdam is provided on a part or all of the outside of the reducing agent tank for storing the reducing agent to be supplied to the selective catalytic reduction catalyst to form a tank with a hull, and a part of the cofferdam or It is configured to allow water to flow through all. This water flow includes pouring and storing seawater or water in the cofferdam, and replacing the seawater or water by performing water pouring and draining simultaneously.

この構成によれば、外気温度や機関室内の温度が高温になってその熱が還元剤タンク内の還元剤に伝達されても、コファダム(空所)に通水する海水や河川水や湖水等の船体外部の水により還元剤タンク内の還元剤を冷却することができるので、還元剤の温度を適正な保管温度の範囲内に維持できる。つまり、コファダムにより、このコファダム側から還元剤への外部から熱伝達を少なくすると共に、このコファダムへ通水することで還元剤を冷却できるので、ポンプと制御弁と配管等の比較的簡単な構成とポンプと制御弁の制御という比較的簡単な制御で、容易に還元剤の温度管理ができるようになる。   According to this configuration, even when the outside air temperature or the temperature in the engine room becomes high and the heat is transferred to the reducing agent in the reducing agent tank, the seawater, river water, lake water, etc. Since the reducing agent in the reducing agent tank can be cooled by the water outside the hull, the temperature of the reducing agent can be maintained within an appropriate storage temperature range. In other words, the cofferdam reduces the heat transfer from the outside to the reducing agent from the cofferdam side, and the cooling agent can be cooled by passing water through the cofferdam, so a relatively simple configuration of pumps, control valves, piping, etc. The temperature of the reducing agent can be easily managed by relatively simple control of the pump and the control valve.

しかも、還元剤タンクを冷却できるので、還元剤タンクの一部又は全部を、高温の外気に曝され易い喫水線より上の部位に設けることができるようになり、容量の大きい還元剤タンクを機関室の内部、又は、機関室の周辺に配置し易くなる。その結果、内燃機関の排気ガスの排出経路と還元剤タンクの間の距離を短くすることができる。   In addition, since the reducing agent tank can be cooled, a part or all of the reducing agent tank can be provided at a location above the water line that is easily exposed to high-temperature outside air, and a large capacity reducing agent tank is provided in the engine room. It becomes easy to arrange in the inside of the engine or around the engine room. As a result, the distance between the exhaust gas exhaust path of the internal combustion engine and the reducing agent tank can be shortened.

また、還元剤タンクの周囲の一部又は全部にコファダムを設けることにより、還元剤が還元剤タンクから漏出しても、一旦コファダム内に漏出するので直接外部に漏れることを防止できる。そのうえ、通水した水を船舶外部に放出する前に検査することで還元剤の漏出を容易に監視でき、また、漏出検査及び還元剤が漏出した場合の処理も通水した水のみに対して行うだけよくなり、還元剤による海洋汚染を容易に防止できるようになる。更に還元剤タンクを船体付きタンクで形成することにより、船舶の内部のスペースを有効利用できる。   Further, by providing a cofferdam around a part or all of the periphery of the reducing agent tank, even if the reducing agent leaks from the reducing agent tank, it can be prevented from leaking directly to the outside because it once leaks into the cofferdam. In addition, the leakage of reducing agent can be easily monitored by inspecting the water before it is released to the outside of the ship, and the leakage inspection and treatment when the reducing agent leaks can be performed only for the water that has passed. The only thing that needs to be done is to easily prevent marine pollution from the reducing agent. Furthermore, the space inside the ship can be effectively used by forming the reducing agent tank with a tank with a hull.

上記のNOx低減装置を配備した船舶において、船側外板、又は、貨物艙との間に前記コファダムを設けて、前記還元剤タンクを機関室に隣接させて配設すると、内燃機関の排気ガスの排出経路と還元剤タンクの間の距離を短くすることができる。また、還元剤タンクを船側側に配置すると冷却用の水の配管を短くすることができる。   In a ship equipped with the above NOx reduction device, when the cofferdam is provided between a ship side skin or a cargo trough and the reducing agent tank is disposed adjacent to the engine room, the exhaust gas of the internal combustion engine is reduced. The distance between the discharge path and the reducing agent tank can be shortened. Moreover, if the reducing agent tank is disposed on the ship side, the piping for cooling water can be shortened.

上記のNOx低減装置を配備した船舶において、前記還元剤タンクの還元剤の温度を測定する温度センサを設け、該温度センサの検出値に基づいて、前記還元剤タンクへの通水を制御すると、簡単な制御で容易に、還元剤の温度を適正な保管温度の範囲にすることができる。   In a ship equipped with the NOx reduction device, a temperature sensor that measures the temperature of the reducing agent in the reducing agent tank is provided, and based on the detected value of the temperature sensor, the flow of water to the reducing agent tank is controlled. The temperature of the reducing agent can be set within a proper storage temperature range easily by simple control.

なお、航路や外気温度の条件にもよるが、コファダムの容量が大きい場合には、水を入れ替えずに貯めておくのみで、還元剤の温度が保管温度範囲内に収まる場合もある。   Although depending on the conditions of the channel and the outside air temperature, when the capacity of the cofferdam is large, the temperature of the reducing agent may be within the storage temperature range simply by storing the water without replacing it.

本発明のNOx低減装置を配備した船舶によれば、外気温度や機関室内の温度が高温になっても、尿素水等の還元剤の温度を適正な保管温度の範囲内に維持できて、還元剤の寿命の低下を防ぐことができ、しかも、内燃機関の排気ガスの排出経路と還元剤タンクの間の距離を短くすることができる。また、還元剤タンクが腐食した場合や、衝突や座礁等により船側外板が損傷した場合でも、還元剤タンク内の還元剤が船側外板から直接船体外部に漏出することを防止できる。   According to the ship equipped with the NOx reduction device of the present invention, even if the outside air temperature or the temperature in the engine room becomes high, the temperature of the reducing agent such as urea water can be maintained within the appropriate storage temperature range, and the reduction can be achieved. The reduction in the life of the agent can be prevented, and the distance between the exhaust gas exhaust path of the internal combustion engine and the reducing agent tank can be shortened. Further, even when the reducing agent tank is corroded, or when the ship side skin is damaged due to collision or grounding, the reducing agent in the reducing agent tank can be prevented from leaking directly from the ship side skin to the outside of the hull.

本発明に係る実施の形態のNOx低減装置を配備した船舶におけるNOx低減装置と還元剤タンクの構成を示す斜視図である。It is a perspective view which shows the structure of the NOx reduction device and the reducing agent tank in the ship which provided the NOx reduction device of embodiment which concerns on this invention. 還元剤タンクの配置を示す船舶の機関室前部における横断面図である。It is a cross-sectional view in the engine room front part of the ship which shows arrangement | positioning of a reducing agent tank. 還元剤タンクの配置を示す船舶の機関室後部における横断面図である。It is a transverse cross section in the engine room rear part of a ship showing arrangement of a reducing agent tank.

以下、図面を参照して本発明に係る実施の形態のNOx低減装置を配備した船舶について説明する。   Hereinafter, a ship provided with a NOx reduction device according to an embodiment of the present invention will be described with reference to the drawings.

図1に示すように、本発明に係る実施の形態のNOx低減装置を配備した船舶は、ディーゼルエンジン等の内燃機関2と、この内燃機関2の排気ガスGの排出経路である排気ガス通路11と、この排気ガス通路11の途中に設けられた、SCR(Selective Catalytic Reduction)触媒と呼ばれる選択接触還元触媒を備えたNOx低減装置12と、この選択接触還元触媒12に還元剤Rを供給するための還元剤供給システム20と、この還元剤タンク21の還元剤Rを冷却するための還元剤冷却システム30を備えて構成される。   As shown in FIG. 1, a ship provided with the NOx reduction device according to the embodiment of the present invention includes an internal combustion engine 2 such as a diesel engine and an exhaust gas passage 11 that is a discharge path of the exhaust gas G of the internal combustion engine 2. A NOx reduction device 12 having a selective catalytic reduction catalyst called an SCR (Selective Catalytic Reduction) catalyst provided in the middle of the exhaust gas passage 11, and for supplying the reducing agent R to the selective catalytic reduction catalyst 12. The reducing agent supply system 20 and a reducing agent cooling system 30 for cooling the reducing agent R in the reducing agent tank 21 are provided.

この還元剤供給システム20は、還元剤タンク21と還元剤噴霧ノズル24と、この両者21,24を接続する還元剤用配管22と、この還元剤用配管22に配置される還元剤用ポンプ23と、制御弁25,26とから構成される。更に、排気ガスの浄化性能を高めるために、内燃機関2の運転状態で変化する排気ガス中のNOx濃度や排気ガス量等に応じて、還元剤噴霧ノズル24から排気ガスG中に供給される還元剤Rの供給量を調整する排気ガス浄化用の制御装置を設ける。なお、通常、この排気ガス浄化用の制御装置は、内燃機関2の運転制御装置に組み込まれる。   The reducing agent supply system 20 includes a reducing agent tank 21, a reducing agent spray nozzle 24, a reducing agent pipe 22 that connects both of them 21, 24, and a reducing agent pump 23 disposed in the reducing agent pipe 22. And control valves 25 and 26. Further, in order to improve the exhaust gas purification performance, the exhaust gas G is supplied from the reducing agent spray nozzle 24 into the exhaust gas G in accordance with the NOx concentration in the exhaust gas, the amount of exhaust gas, and the like that change depending on the operating state of the internal combustion engine 2. A control device for exhaust gas purification that adjusts the supply amount of the reducing agent R is provided. Normally, this exhaust gas purification control device is incorporated in the operation control device of the internal combustion engine 2.

また、還元剤冷却システム30は、船側外板3と還元剤タンク21との間のコファダム(空所)31と、上甲板4と還元剤タンク21との間に設けられたコファダム31と、これらのコファダム31と海水取入口37とを接続する通水用配管33と、この通水用配管33に設けられた通水用ポンプ34と、制御弁35,36とから構成される。なお、コファダム31に通水した海水(又は水)を船体外部に排出する排出用の配管等(排出ライン)を設ける。この還元剤Rが尿素水の場合には、腐食性を考慮して、鉄、銅、砲金、アルミニウム、アルミニウム合金等の使用を避けて、ステンレス材料を用いるか、あるいは、耐腐食塗装やポリエチレン等の樹脂材料でコーティングする。   Further, the reducing agent cooling system 30 includes a cofferdam (vacant space) 31 between the ship-side outer plate 3 and the reducing agent tank 21, a cofferdam 31 provided between the upper deck 4 and the reducing agent tank 21, and these The cofferdam 31 and the seawater intake port 37 are connected to a water passage pipe 33, a water passage pump 34 provided in the water passage pipe 33, and control valves 35 and 36. In addition, the discharge piping etc. (discharge line) which discharge | emit the seawater (or water) which passed the cofferdam 31 to the hull exterior are provided. When this reducing agent R is urea water, in consideration of corrosiveness, avoid the use of iron, copper, gunmetal, aluminum, aluminum alloy, etc., use stainless steel, or use corrosion resistant paint, polyethylene, etc. Coating with resin material.

更に、還元剤タンク21の還元剤Rの温度を計測するために温度センサ( 図示しない)を設け、この温度センサ( 図示しない)の出力を基に、通水用ポンプ34、制御弁35,36と排出ライン(図示しない)の制御弁( 図示しない)を制御する制御装置を、排気ガス浄化用の制御装置又は内燃機関2の運転制御装置に組み込む。なお、還元剤Rの水位が変化しても、一つの温度センサで済むように低部に設置するか、フロートタイプの温度センサとする。   Further, a temperature sensor (not shown) is provided to measure the temperature of the reducing agent R in the reducing agent tank 21. Based on the output of this temperature sensor (not shown), the water flow pump 34 and the control valves 35, 36 are provided. And a control device for controlling a control valve (not shown) of an exhaust line (not shown) is incorporated into the exhaust gas purification control device or the operation control device of the internal combustion engine 2. In addition, even if the water level of the reducing agent R changes, it is installed in a low part so that only one temperature sensor is required, or a float type temperature sensor is used.

この選択接触還元触媒は、チタン・バナジウム系の触媒で形成され、尿素水((NH22CO)等の還元剤Rから加水分解((NH22CO+H2O→2NH3+CO2)等によって発生するアンモニア(NH3)を用いて、窒素酸化物(NOx)の一酸化窒素(NO) と二酸化窒素(NO2)を触媒作用(4NO+4NH3+O2→4N2+6H2O、NO+NO2+2NH3→2N2+3H2O)により窒素(N2)と水(H2O) に還元する。 This selective catalytic reduction catalyst is formed of a titanium / vanadium-based catalyst and hydrolyzed from a reducing agent R such as urea water ((NH 2 ) 2 CO) ((NH 2 ) 2 CO + H 2 O → 2NH 3 + CO 2 ). Using ammonia (NH 3 ) generated by the above, nitrogen oxide (NOx), nitric oxide (NO) and nitrogen dioxide (NO 2 ) are catalyzed (4NO + 4NH 3 + O 2 → 4N 2 + 6H 2 O, NO + NO 2 Reduction to nitrogen (N 2 ) and water (H 2 O) by + 2NH 3 → 2N 2 + 3H 2 O).

この選択接触還元触媒に使用される還元剤Rとしては、アンモニア、アンモニア水、又は、アンモニアを発生する還元剤があるが、比較的安全性の高いに尿素水を用いることが多く、この実施の形態でも尿素水を用いる。この尿素水は、尿素濃度約32%〜33%の場合には、約40℃では製品寿命が4カ月程度となり、温度上昇により大きく製品寿命が低下するので、常に約30℃以下で保管することが好ましい。また、この尿素水はマイナス10℃付近で結晶化するため、還元剤タンク21内の還元剤Rの温度はマイナス10℃以上の液温になるように管理する必要がある。   Examples of the reducing agent R used in the selective catalytic reduction catalyst include ammonia, aqueous ammonia, and a reducing agent that generates ammonia. However, urea water is often used because of its relatively high safety. Urea water is also used in the form. When the urea concentration is about 32% to 33%, the product life will be about 4 months at about 40 ° C, and the product life will be greatly reduced due to temperature rise, so always store it at about 30 ° C or less. Is preferred. Further, since the urea water is crystallized around minus 10 ° C., it is necessary to manage the temperature of the reducing agent R in the reducing agent tank 21 so that the liquid temperature becomes minus 10 ° C. or more.

一方、夏場などでは外気温が30℃を超える場合があり、しかも、直射日光が照射する船側外板3や上甲板4は、30℃を超える温度になるため、この船側外板3や上甲板4から還元剤Rへの熱伝達も考慮する必要がある。更に、機関室5の温度は40℃を超えるので、内燃機関2が配置される機関室5に隣接して還元剤タンク21を設ける場合には、機関室5側からの熱が還元剤Rに伝達されるので、この対策が必要となる。   On the other hand, the outside air temperature may exceed 30 ° C in summer, and the ship side skin 3 and upper deck 4 irradiated with direct sunlight reach temperatures exceeding 30 ° C. It is also necessary to consider the heat transfer from 4 to the reducing agent R. Furthermore, since the temperature of the engine room 5 exceeds 40 ° C., when the reducing agent tank 21 is provided adjacent to the engine room 5 in which the internal combustion engine 2 is disposed, heat from the engine room 5 side is supplied to the reducing agent R. This is necessary because it is communicated.

これらの還元剤タンク21への熱伝達に対して、還元剤タンク21内の還元剤Rの温度管理をする必要があり、還元剤タンク21の機関室側壁8に防熱材等で断熱処理を施す。また、還元剤用配管22における熱伝達量を少なくしたり、還元剤用配管22の防熱処理を簡単にしたりするためにも、内燃機関2の排気ガスGの排出ガス通路11と還元剤タンク21の間を接続する還元剤用配管22を短くすることも得策であるので、還元剤タンク21を図2及び図3に示すように機関室5に隣接して設ける。図2は機関室前部から前方を見た横断面を示し、図3は機関室後部から後方を見た横断面を示す。   For heat transfer to these reducing agent tanks 21, it is necessary to control the temperature of the reducing agent R in the reducing agent tank 21, and the engine room side wall 8 of the reducing agent tank 21 is subjected to heat insulation treatment with a heat insulating material or the like. . Further, the exhaust gas passage 11 and the reducing agent tank 21 for the exhaust gas G of the internal combustion engine 2 can also be used to reduce the amount of heat transfer in the reducing agent pipe 22 and to simplify the heat-proofing of the reducing agent pipe 22. Since it is also a good idea to shorten the reducing agent pipe 22 connecting the two, the reducing agent tank 21 is provided adjacent to the engine room 5 as shown in FIGS. FIG. 2 shows a cross section viewed from the front of the engine room, and FIG. 3 shows a cross section viewed from the rear of the engine room.

この還元剤タンク21はできるだけ、船側外板3の外側が海水又は水に浸っていて冷却され易い喫水より下側の部分に設けることが望ましいが、船尾部は狭く、満載喫水(L.W.L.)6より下に、特にバラスト喫水(B.W.L.)7よりも下に還元剤タンク21を設けることは困難であるので、多くの場合は、大きな容量を確保し易い船側の上方に設けることになる。また、還元剤タンク21を船体付きタンクとして形成することで、船内の容積を有効利用して大容量タンクの確保ができる。   The reducing agent tank 21 is preferably provided in a portion below the draft that is easily cooled because the outside of the ship-side outer plate 3 is immersed in seawater or water, but the stern portion is narrow and the full draft (L.W. L.) It is difficult to provide the reducing agent tank 21 below 6, especially below the ballast draft (BWL) 7, and in many cases, the ship side is easy to ensure a large capacity. It will be provided above. Further, by forming the reducing agent tank 21 as a tank with a hull, it is possible to secure a large capacity tank by effectively using the capacity of the ship.

図1〜図3に示す実施の形態では、機関室5側においては、機関室5の容積をできるだけ広く利用するために、コファダムを設けずに、機関室5から還元剤タンク21への熱伝達量を少なくするために、防熱塗装をしたり、遮熱材を張り付けたりする。また、上甲板4においては、できるだけ、コファダム(空所)31を設けて空気層で上甲板4から還元剤タンク21への熱伝達を遮るように構成するが、容積等の関係で、コファダム31を設けられない場合には、還元剤タンク21の上側部分の上甲板4を防熱塗装したり、この部分の上甲板4に遮熱材を張り付けたりする。   In the embodiment shown in FIGS. 1 to 3, heat transfer from the engine room 5 to the reducing agent tank 21 is not provided on the engine room 5 side without providing a cofferdam in order to use the volume of the engine room 5 as widely as possible. In order to reduce the amount, heat-resistant paint or heat-shielding material is attached. In addition, the upper deck 4 is configured so that a cofferdam (vacant space) 31 is provided as much as possible so that heat transfer from the upper deck 4 to the reducing agent tank 21 is blocked by the air layer. Is not provided, the upper deck 4 of the upper part of the reducing agent tank 21 is heat-resistant coated, or a heat shielding material is attached to the upper deck 4 of this part.

また、船側外板3側も還元剤タンク21が喫水線6,7より上に設けられると、船側外板3側から還元剤タンク21に熱伝達が生じる可能性が高まるので、また、還元剤Rを冷却する必要があるので、この船側外板3と還元剤タンク21との間にコファダム(空所)31を設けると共に、このコファダム31に冷却用の海水(又は水)Wを通水できるように還元剤冷却システム30を設ける。   Further, if the reducing agent tank 21 is also provided above the draft lines 6 and 7 on the ship side outer plate 3 side, the possibility of heat transfer from the ship side outer plate 3 side to the reducing agent tank 21 is increased. The cofa dam (vacant space) 31 is provided between the ship side skin 3 and the reducing agent tank 21, and the cooling seawater (or water) W can be passed through the cofa dam 31. Is provided with a reducing agent cooling system 30.

この通水を還元剤タンク21に設けた温度センサ(図示しない)で計測した還元剤Rの温度Trに基づいて、通水用ポンプ34と制御弁35,36と排水ライン(図示しない)の制御弁(図示しない)を制御して行う。この船体の外部の水(海水又は水)Wの通水により、還元剤タンク21の外側を冷却して、還元剤Rの温度Trが保管温度の範囲内になるように制御する。   Based on the temperature Tr of the reducing agent R measured by a temperature sensor (not shown) provided in the reducing agent tank 21, the water supply pump 34, the control valves 35 and 36, and the drain line (not shown) are controlled. This is done by controlling a valve (not shown). The outside of the reducing agent tank 21 is cooled by passing water (seawater or water) W outside the hull so that the temperature Tr of the reducing agent R falls within the storage temperature range.

この通水は、還元剤Rの温度Trや通水用ポンプ34に使用できるポンプの容量等を勘案して、一時的、断続的、あるいは、連続的(常時)に通水する。なお、常時通水する際には、通水量を一定にしてもよく、必要に応じて通水量を増減してもよい。また、通水せず水を貯めておくのみで、還元剤Rの温度Trが保管温度の範囲内におさまるような航路や外気温度や還元剤タンク21とコファダム31の容量等の条件下では、水を入れ変えることなく貯めておくことでもよい。   In consideration of the temperature Tr of the reducing agent R and the capacity of a pump that can be used for the water pump 34, the water is passed temporarily, intermittently, or continuously (always). In addition, when always passing water, the amount of water flow may be made constant, or the amount of water flow may be increased or decreased as necessary. In addition, under conditions such as the channel, the outside air temperature, the capacity of the reducing agent tank 21 and the cofferdam 31 such that the temperature Tr of the reducing agent R is kept within the storage temperature range by simply storing water without passing water, It may be stored without changing water.

次に、上記の構成におけるNOx低減装置を配備した船舶における排気ガスの浄化方法について説明する。   Next, a method for purifying exhaust gas in a ship provided with the NOx reduction device having the above configuration will be described.

先ず、出港に際して、還元剤タンク21に還元剤Rを積み込む。この還元剤タンク21に隣接するコファダム31には、船体外部の海水(又は水)Wを通水し、コファダム31内に入れておく。   First, when leaving the port, the reducing agent R is loaded into the reducing agent tank 21. Seawater (or water) W outside the hull is passed through the cofferdam 31 adjacent to the reducing agent tank 21 and placed in the cofadam 31.

そして、機関室5や外気や直射日光により還元剤タンク21内の還元剤Rの温度が上昇し、温度センサ38で検出された温度が予め設定された保管温度の範囲(例えば、マイナス5℃〜30℃)から外れた場合には、制御弁35,36を開弁して、通水用ポンプ34を駆動して、コファダム31に海水(又は水)を注入する。なお、必要に応じて、図示しない別の排水ラインからコファダム31内の海水(又は水)を船外に排水する。   Then, the temperature of the reducing agent R in the reducing agent tank 21 rises due to the engine room 5, outside air, or direct sunlight, and the temperature detected by the temperature sensor 38 is within a preset storage temperature range (for example, minus 5 ° C. to When the temperature deviates from 30 ° C., the control valves 35 and 36 are opened, the water pump 34 is driven, and seawater (or water) is injected into the cofferdam 31. If necessary, seawater (or water) in the cofferdam 31 is drained out of the ship from another drainage line (not shown).

船体の外部の海水(又は水)の温度は通常は還元剤Rの保管温度の下限値(例えば、マイナス5℃)よりも高く、上限値(例えば、30℃)よりも低いので、通水量を調整することにより、還元剤Rの温度を保管温度の範囲内にすることができる。この通水は、一時的又は断続的又は連続的に行われ、通水の有無や通水量で冷却量を調整して還元剤Rの温度を調整管理する。   The temperature of seawater (or water) outside the hull is usually higher than the lower limit (eg, minus 5 ° C) of the storage temperature of the reducing agent R and lower than the upper limit (eg, 30 ° C). By adjusting, the temperature of the reducing agent R can be kept within the storage temperature range. This water flow is performed temporarily or intermittently or continuously, and the temperature of the reducing agent R is adjusted and managed by adjusting the cooling amount according to the presence / absence of the water flow or the water flow rate.

なお、コファダム31内の海水(又は水)Wの排出に際しては、還元剤Rが漏出していないかを検査し、還元剤Rがコファダム31内に漏出していないことを確認してから排出する。これにより、還元剤Rの漏れに関する安全性を確保する。   In addition, when discharging the seawater (or water) W in the cofferdam 31, it is inspected whether the reducing agent R has leaked out, and after confirming that the reducing agent R has not leaked into the cofferdam 31, it is discharged. . Thereby, the safety | security regarding the leakage of the reducing agent R is ensured.

そして、内燃機関2の運転時で、排気ガスG中のNOxを低減する必要があるときには、還元剤供給システム20により、還元剤Rを還元剤噴霧ノズル24から排気ガスG中に噴霧して、NOx低減装置12の選択接触還元触媒に供給する。この供給量は、内燃機関の運転状態(NOx濃度、排気ガス量等)と選択接触還元触媒の状態(温度や劣化等)に応じて変化するが、例えば、内燃機関2で消費する燃料の10%程度である。   When it is necessary to reduce NOx in the exhaust gas G during operation of the internal combustion engine 2, the reducing agent supply system 20 sprays the reducing agent R from the reducing agent spray nozzle 24 into the exhaust gas G. It supplies to the selective catalytic reduction catalyst of the NOx reduction device 12. This supply amount varies depending on the operation state (NOx concentration, exhaust gas amount, etc.) of the internal combustion engine and the state (temperature, deterioration, etc.) of the selective catalytic reduction catalyst. For example, the amount of fuel consumed by the internal combustion engine 2 is 10%. %.

この還元剤Rの供給により、尿素水の場合には加水分解でアンモニアが発生し、このアンモニアとNOxとが触媒作用による反応で窒素と水になり、排気ガス中のNOxは浄化される。   By supplying the reducing agent R, in the case of urea water, ammonia is generated by hydrolysis. The ammonia and NOx are converted into nitrogen and water by a reaction by the catalytic action, and NOx in the exhaust gas is purified.

上記の構成のNOx低減装置を配備した船舶によれば、外気温度や機関室5内の温度が高温になっても、尿素水等の還元剤Rの温度Trを適正な保管温度の範囲内に維持できて、還元剤Rの寿命の低下を防ぐことができ、しかも、内燃機関2の排気ガスGの排出経路11と還元剤タンク21の間の距離を短くすることができる。また、還元剤タンク21が腐食した場合や、衝突や座礁等により船側外板3が損傷した場合でも、還元剤Rが船側外板3から直接船体外部に漏出することを防止できる。   According to the ship provided with the NOx reduction device having the above-described configuration, even if the outside air temperature or the temperature in the engine room 5 becomes high, the temperature Tr of the reducing agent R such as urea water is within an appropriate storage temperature range. Thus, the life of the reducing agent R can be prevented from decreasing, and the distance between the exhaust gas G discharge path 11 of the internal combustion engine 2 and the reducing agent tank 21 can be shortened. Further, even when the reducing agent tank 21 is corroded or when the ship side skin 3 is damaged due to a collision or grounding, the reducing agent R can be prevented from leaking directly from the ship side skin 3 to the outside of the hull.

本発明のNOx低減装置を配備した船舶は、外気温度や機関室内の温度が高温になっても、尿素水等の還元剤の温度を適正な温度範囲内に維持できて、還元剤の寿命の低下を防ぐことができ、しかも、内燃機関の排気ガスの排出経路と還元剤タンクの間の距離を短くすることができるので、NOxを低減する環境にやさしい船舶として利用できる。   A ship equipped with the NOx reduction device of the present invention can maintain the temperature of a reducing agent such as urea water within an appropriate temperature range even if the outside air temperature or the temperature in the engine room becomes high, and the life of the reducing agent is reduced. The reduction can be prevented, and the distance between the exhaust gas exhaust path of the internal combustion engine and the reducing agent tank can be shortened, so that it can be used as an environment-friendly ship that reduces NOx.

2 内燃機関
3 船側外板
4 上甲板
5 機関室
6 満載喫水
7 バラスト喫水(軽荷喫水)
8 機関室側板
11 排気通路
12 NOx低減装置
20 還元剤供給システム
21 還元剤タンク
22 還元剤用配管
23 還元剤用ポンプ
24 還元剤噴霧ノズル
31 コファダム(空所)
33 通水用配管
34 通水用ポンプ
G 排気ガス
R 還元剤
W 海水又は水(船体外部の水)
2 Internal combustion engine 3 Ship side shell 4 Upper deck 5 Engine room 6 Full draft 7 Ballast draft (light draft)
8 Engine room side plate 11 Exhaust passage 12 NOx reduction device 20 Reducing agent supply system 21 Reducing agent tank 22 Reducing agent piping 23 Reducing agent pump 24 Reducing agent spray nozzle 31 Cofferdam (vacant space)
33 Pipe for water flow 34 Pump for water flow G Exhaust gas R Reducing agent W Seawater or water (water outside the hull)

Claims (2)

船舶に搭載した内燃機関から排出される排気ガス中のNOxを浄化するための選択接触還元触媒を備えたNOx低減装置を配備した船舶において、前記選択接触還元触媒に供給する還元剤を貯蔵するための還元剤タンクの外側の一部又は全部にコファダムを設けて船体付タンクとして形成すると共に、前記コファダムの一部又は全部に通水できるように構成したことを特徴とするNOx低減装置を配備した船舶。   In order to store a reducing agent to be supplied to the selective contact reduction catalyst in a ship provided with a NOx reduction device equipped with a selective contact reduction catalyst for purifying NOx in exhaust gas discharged from an internal combustion engine mounted on the ship. Provided with a cofferdam on the outside or part of the reducing agent tank to form a tank with a hull, and deployed a NOx reduction device configured to allow water to pass through part or all of the cofferdam. Ship. 船側外板、又は、貨物艙との間に前記コファダムを設けて、前記還元剤タンクを機関室に隣接させて配設したことを特徴とする請求項1記載のNOx低減装置を配備した船舶。   The ship provided with the NOx reduction device according to claim 1, wherein the cofferdam is provided between a ship side outer plate or a cargo trough and the reducing agent tank is disposed adjacent to an engine room.
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