JP2004000867A - Apparatus for denitrating exhaust gas, and urea vaporizer used therefor - Google Patents

Apparatus for denitrating exhaust gas, and urea vaporizer used therefor Download PDF

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Publication number
JP2004000867A
JP2004000867A JP2002165400A JP2002165400A JP2004000867A JP 2004000867 A JP2004000867 A JP 2004000867A JP 2002165400 A JP2002165400 A JP 2002165400A JP 2002165400 A JP2002165400 A JP 2002165400A JP 2004000867 A JP2004000867 A JP 2004000867A
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Prior art keywords
urea
exhaust gas
urea water
section
vaporizer
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JP3869314B2 (en
Inventor
Shinichiro Nomura
野村 伸一郎
Akira Baba
馬場 彰
Toshifumi Mukai
向井 利文
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Mitsubishi Power Ltd
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Babcock Hitachi KK
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  • Exhaust Gas After Treatment (AREA)
  • Treating Waste Gases (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a urea vaporizer which prevents deposition of cyanuric acid or isocyanic acid as pyrolysates of urea and can continuously be operated without inducing chalking, and to provide an apparatus for denitrating exhaust gas by using the vaporizer. <P>SOLUTION: The apparatus has a passage for exhaust gas containing nitrogen oxides, a supply means for a reducing agent for nitrogen oxides disposed in the passage, and a denitrating part for exhaust gas disposed in the slip stream side of the supply means of the reducing agent. The supply means for the reducing agent has a urea water injecting part 1 to inject urea water, a vaporizing part 6 to vaporize the urea water injected from the urea injecting part, a hydrolyzing part 6 to hydrolyze urea disposed in the slip stream side of the vaporizing part 6, and a reducing agent spraying part to spray and supply a gas containing ammonia produced in the above parts into the exhaust gas. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明は、排ガス脱硝装置およびこれに用いる尿素気化装置に関し、特に窒素酸化物を含有する排ガス、例えばディーゼル機関からの排ガスの処理において、尿素を窒素酸化物の還元剤として用いる排ガス脱硝装置およびこれに用いる尿素気化器に関するものである。
【0002】
【従来の技術】
近年、地球温暖化の問題がクローズアップされており、化石燃料を大量に消費して生成される窒素酸化物の排出量の低減が急務である。特にディーゼル機関から排出されるガスは、PM(粒子)、窒素酸化物を含有する排ガスであり、この窒素酸化物は、ガソリンエンジンからのそれより、燃焼温度が高いことから、高濃度で、排ガス中の酸素濃度が高いこともあって、ガソリンエンジン排ガスの三元触媒のように、排ガス中の炭化水素を利用した窒素酸化物の還元効果を得ることができないので低減が難しいとされている。このような窒素酸化物の低減対策として、エンジン排気系統に尿素水を直接噴射供給する方法がボッシュ社などから提案されている。尿素は液体で取り扱いが容易であることに加えて、肥料にも使用されるように安価であることから、脱硝剤としては適切であるが、その安定運用は難しい。また尿素は常温では固体であり、水に溶けやすい性質を持ち、加熱すると、低温で溶融するが、複雑な有機化合物が生成されることから、気化は難しいとされている。また液体の状態で、燃焼排ガス中に噴霧するのは、単純で安定な運用が可能なように推測されがちではあるが、実際は、ノズル閉塞が発生しやすいと言われている。
【0003】
図7は、従来の尿素水の直接噴射による排ガス脱硝方法の一例を示したものである(特開2001−317346)。ディーゼル機関の排ガス14は、酸化触媒の充填された酸化室8で酸化された後、連絡菅15を通り、脱硝触媒を充填した脱硝室9に入るが、連絡管に設けられたノズル12により、タンク11から供給される尿素水11が噴霧される。10はポンプである。排ガスに吹き込んだ尿素は、雰囲気温度が400℃を越えることから、気化し、脱硝室9内で窒素酸化物を還元する。
【0004】
しかしながらこの装置は、ノズル12の噴射部分から、触媒部分までの距離が十分に取れないことに加えて、雰囲気温度が変化するといった、尿素分解に関しては難しい環境での供給となっているので、安定した尿素分解およびアンモニアの供給が困難であった。
【0005】
【発明が解決しようとする課題】
これらの尿素吹き込み装置では、噴霧ノズル12の部分やその後部において尿素の熱分解生成物であるシアヌル酸((HNCO))、イソシアン酸(3HNCO)や固形物のビュレットが、その搬送の過程で配管内に付着して閉塞するという大きな問題がある。
【0006】
本発明の課題は、尿素の熱分解生成物であるシアヌル酸やイソシアン酸などの付着を防止して、閉塞を起こさないで連続運転を可能にする尿素気化器およびこれを用いた排ガス脱硝装置を提供することにある。
【0007】
【課題を解決するための手段】
上記課題を達成するために、本願で特許請求される発明は下記のとおりである。
(1)窒素酸化物含有排ガスの流路と、該流路に設けられた窒素酸化物の還元剤の供給手段と、前記還元剤の供給手段の後流側に設けられた排ガス脱硝部とを有する排ガス脱硝装置であって、前記還元剤の供給手段は、尿素水を噴出させる尿素水噴出部と、該尿素水噴出部から噴出した尿素水を蒸発させる蒸発部と、その後流部に設けられた、尿素を加水分解する加水分解部と、これらの部分で発生したアンモニアを含むガスを、前記排ガス中に噴射供給する還元剤噴射部とを有することを特徴とする排ガス脱硝装置。
【0008】
(2)前記蒸発部と加水分解部のうち、少なくとも蒸発部において、前記装置内部及び外部にヒータを有することを特徴とする(1)記載の排ガス脱硝装置。(3)前記蒸発部と加水分解部を別容器として形成し、それぞれに温度制御装置を設けたことを特徴とする排ガス脱硝装置。
(4)前記蒸発部には、充填物として金属またはセラミックスの粒子またはハニカムが充填されていることを特徴とする(1)ないし(3)のいずれかに記載の排ガス脱硝装置。
【0009】
(5)前記加水分解部には、尿素の加水分解を促進する充填物として、γアルミナまたは炭酸カリウム(KCO)を担持した粒子が充填されていることを特徴とする(1)ないし(4)のいずれかに記載の排ガス脱硝装置。
(6)筒状容器内に、尿素水噴出部、尿素水蒸発部、尿素加水分解部および分解ガス出口部を順に形成した尿素気化器であって、該尿素水噴出部に尿素水噴霧ノズルを設置し、その下部に前記噴霧に必要な空間部分と、微粒化した尿素粒子を受け止める受液部とを順次設けて尿素水蒸発部を形成し、該受液部上に尿素水の蒸発を促進する充填物を充填したことを特徴とする尿素気化器。
【0010】
(7)前記尿素水噴出部は、尿素水噴出ノズルと、該尿素水噴出ノズルを尿素気化器本体に装着するためのフランジ部とを有し、該フランジ部は、前記尿素水噴出ノズルを取り囲み、かつ、該フランジ部の内周に沿って接線方向に気体を供給するように気体供給孔が設けられていることを特徴とする(6)記載の尿素気化器。
(8)前記受液部の充填物が、後記加水分解部の充填物よりも熱伝導率の良好な物質からなることを特徴とする(7)記載の尿素気化器。
【0011】
(9)前記受液部の充填物が金属またはセラミックスの粒子またはハニカムである(7)または(8)記載の尿素気化器。
(10)前記加水分解部には、尿素の加水分解を促進する充填物として、γアルミナまたは炭酸カリウム(KCO)を担持した粒子が充填されていることを特徴とする(6)ないし(9)のいずれかに記載の尿素気化器。
【0012】
本発明においては、尿素気化器の容器を均一加熱し、内部に向けて尿素水(尿素濃度30%〜50%)を吹き込むと、容器内部で水と尿素が蒸発し、内部に充填した触媒粒子、例えばγアルミナ粒子、炭酸カリウムを担持した粒子等の表面において下式に示すように尿素が加水分解し、アンモニアガスが生成される。
【0013】
(NHCO+HO→2NH+CO
気化器の内部は、450℃以上を保持する構成とし、尿素が加熱分解する過程で発生するシアヌル酸やイソシアン酸などの固体が副生しないように、急速蒸発加熱を促進する構造とすることが好ましい。通常、高温に保った容器に尿素水を噴射すると、液滴を受ける面での温度が低下し、固体が析出して閉塞につながり、また内部の温度制御が極めて難しい。本発明では、液体噴霧における蒸発部分に着目し、尿素噴霧流量が著しく変化しても、容器内部の温度変動を抑制できるように蒸発面の伝熱促進に注力した構造、具体的には、加水分解部に充填したγアルミナ粒子等の上部(または前流側)に、これよりも熱伝導率の優れるシリコンカーバイドや、鉄、ステンレスの球、メタルハニカム等を充填した構造とした。これらの充填物は熱伝導が良好である上、球構造、ハニカム構造であることから、尿素水の液滴が衝突する際、凹凸部で受け止めることになることから、蒸発量の増加が期待できる。また容器内部と外部にヒータを設けた場合には、これらのヒータからの熱伝達率の向上に寄与する。
【0014】
また尿素水噴霧ノズルの周囲、すなわち気化器本体に該ノズルを固定するフランジ部に気体供給孔を設け、ここから該フランジ部の内周に沿って下方に冷却用気体(例えば空気)を供給することにより、ノズル周辺の析出物による詰まり等を防止するようにした。
【0015】
【発明の実施の形態】
【実施例】
以下、本発明の尿素気化器の一実施例を図1に示す。この装置は、筒状容器30の頂上部から下方に向けて、尿素水入口部、尿素水蒸発部(5)、尿素加水分解部(7)および分解ガス出口部(31)を順に形成し、該尿素水入口部に尿素水インジェクタ1を設置し、その下部に噴霧に必要な空間部分として尿素水噴霧部6と、微粒化した尿素粒子を受け止める受液部(スクリーン4)を順次設け、該スクリーン4上の受液部に尿素水の蒸発を促進する充填物5を充填したものである。容器30は、内部ヒータ2と外周ヒータ3で均一加熱され、容器内部が可能な限り均一な温度になるように制御される。尿素水は、装置の最上部分に位置するインジェクタ1によって容器30内部に向かって噴霧供給される。噴霧された尿素水は、装置内部の蒸発部充填物5に衝突し、瞬時に蒸発する。ここでインジェクタ1から、当該蒸発部充填物までの空間部分(尿素水噴霧部6)は、尿素水の噴霧及び微粒化に必要な空間である。尿素水は、一旦この空間に充満し、容器の壁にも衝突付着するが、ここも外周ヒータ3によって高温に保持されていることから、尿素の蒸発に寄与する。蒸発した水と尿素は、容器下部の加水分解充填物7に到達し、これでアンモニアと二酸化炭素(CO)に分解され、分解ガスは出口31から取り出され、ディーゼル排ガス系に噴出される。図中、34は充填物の支持固定のためのスクリーンである。
【0016】
図2は、図1における尿素水噴霧用インジェクタ1およびその取付部分の説明図、図3は、図2のIII−III線に沿って切断した矢視方向の平面図である。
【0017】
インジェクタ1は、インジェクタ本体1Aに尿素水導入管31およびノズル20を設けたものからなり、尿素水が噴出されるインジェクタノズル20の周囲には、空気が流通する程度の間隔を隔てて一対のフランジ21および22が設けられている。インジェクタ本体1は段差部32を有し、該段差部32は、上部フランジ21上に支持されている。上部フランジ21には気体供給孔24が窄設され、下部フランジ22には、該気体供給孔24と連通して気体噴出孔23が設けられている。該気体噴出孔23は、図3に示すように、ノズル20とフランジ21または22との間の間隙に開口し、ノズル20の周囲に接線方向に空気を供給し、ノズルを空気流によって冷却するとともに、噴霧された気液を冷却する。すなわち、冷却用の空気は、上部フランジの気体供給孔24から上部フランジ21に供給され、上部フランジ内の流路を通り、上部フランジと下部フランジの間の流路に供給され、次いで中央部のインジェクタ1との隙間から下方の蒸発部充填物5に向けて供給される。
【0018】
なお、尿素水を噴霧するノズル20としては、尿素水のみを噴霧する1流体ノズル、および尿素水と気体を混合して噴霧する2流体ノズルのどちらを用いてもよい。またインジェクタ1の流量調整は、機械式の他に電磁(ソレノイド)式で行うものでもよい。いずれの方式においても,昇温時(噴霧が行われていない)にはノズル自体高温になって、ノズル内部に残存している尿素水が熱分解して固形物を形成してノズル閉塞したり、電磁式であれば耐熱温度が、例えば130℃以下と低いので、故障する問題があるが、本発明による冷却機構を持ったインジェクタおよび気化器の採用によって、尿素水が熱分解過程で発生するシアヌル酸やイソシアン酸の副生が阻止され、安定したインジェクタの運用が可能になる。従って本発明は、ディーゼル燃焼排ガスのパイプが閉塞することを回避できることに加えて、気化器内部においても当該固形物の付着成長が無いことから、長期間にわたって安定な運転が継続できる効果を有する。
【0019】
図4は、本発明の排ガス脱硝装置を用いた排ガス浄化系統の一例を示す説明図である。この装置は、酸化触媒反応器8の出口に設けられた、窒素酸化物含有排ガスの流路としての管15と、該流路に設けられた窒素酸化物の還元剤の供給手段(ノズル12)と、前記排ガス流路の還元剤供給手段の後流側に設けられた排ガス脱硝反応器9とを有する排ガス脱硝装置であり、前記還元剤供給手段として、図1に示したような尿素気化器1を用いたものである。尿素水は、タンク11からポンプ10によって約0.3MPaまで加圧された後、インジェクタ1および気化器13によって気化され、ノズル12からディーゼル系排ガス中に供給され、ここで脱硝反応器9に入ってNO還元触媒表面で反応し、排ガス中のNOがNに還元される。
【0020】
なお、比較として上記気化器で充填物を用いない場合、尿素の噴霧液滴は、ヒータ表面や壁に直接衝突して、一部が蒸発するものの、蒸発部分の熱容量が低いことが原因で温度低下し、シアヌル酸、イソシアン酸その他の固形物を生成して蓄積し、また粗大な液滴は蒸発せずに容器下部にまで到達する。この位置はヒータがないことから低温で、尿素の結晶を生成しやすい。
【0021】
図5は、本発明の他の実施例を示すもので、図1と異なる点は、蒸発を促進する充填物として、メタルハニカムを用い、加水分解部の充填物7(γアルミナ)の劣化を抑制するために気化器本体13から加水分解部を切り離した構造としたものである。この実施例によれば、加水分解部の充填物の劣化を抑え、長寿命化を図ることができる。
【0022】
図6は、図1における気化器本体30を傾斜させて設置した実施例を示す。この実施例では、装置本体の傾斜によって噴霧液の下降が緩和されるので、図1で設けた受液部のスクリーン4が省略されている。
【0023】
【発明の効果】
請求項1〜5記載の発明によれば、ディーゼル機関燃焼排ガスのように窒素酸化物含有ガスの脱硝を、尿素水を用いて配管等への固形物の付着を防止しつつ、安定して行うことができる。
【0024】
また請求項6〜10記載の発明によれば、尿素水が熱分解過程で発生するシアヌル酸、イソシアン酸その他の副生を阻止し、ディーゼル燃焼排ガスのパイプが閉塞することを回避できることに加えて、気化器内部においても当該固形物の付着成長が無いことから、長期間にわたって安定な運転が継続できる。
【図面の簡単な説明】
【図1】本発明の尿素気化器の一実施例を示す説明図。
【図2】図1の尿素水インジェクタノズル付近の詳細断面図。
【図3】図2のIII−III線に沿った矢視方向平面図。
【図4】本発明の尿素気化器を用いた排ガス脱硝装置の一実施例を示す系統図。
【図5】本発明の尿素気化器の他の実施例を示す説明図。
【図6】尿素気化器を傾斜させた本発明の他の実施例を示す説明図。
【図7】従来の尿素直接噴射式排ガス脱硝装置例を示す説明図。
【符号の説明】
1…インジェクタ、2…内部ヒータ、3…外周ヒータ、4…スクリーン、5…蒸発部充填物、6…尿素水噴霧部、7…加水分解部充填物、9…脱硝反応器、12…吹込みノズル、13…気化器本体、30…筒状容器、31…分解ガス出口。
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to an exhaust gas denitration apparatus and a urea vaporizer used for the same, and particularly to an exhaust gas denitration apparatus using urea as a nitrogen oxide reducing agent in the treatment of an exhaust gas containing nitrogen oxides, for example, exhaust gas from a diesel engine, and an apparatus therefor. The present invention relates to a urea vaporizer to be used for urea.
[0002]
[Prior art]
In recent years, the problem of global warming has been highlighted, and there is an urgent need to reduce the emission of nitrogen oxides generated by consuming a large amount of fossil fuels. In particular, the gas discharged from a diesel engine is an exhaust gas containing PM (particles) and nitrogen oxides. Since the nitrogen oxide has a higher combustion temperature than that of a gasoline engine, it has a high Due to the high oxygen concentration in the gas, it is said that it is difficult to reduce the nitrogen oxide reduction effect using hydrocarbons in the exhaust gas, unlike a three-way catalyst for gasoline engine exhaust gas. As a measure for reducing such nitrogen oxides, a method of directly injecting and supplying urea water to an engine exhaust system has been proposed by Bosch Corporation or the like. Urea is suitable as a denitration agent because it is liquid and easy to handle, and is inexpensive as used in fertilizers, but its stable operation is difficult. Urea is a solid at room temperature, has a property of being easily dissolved in water, and melts at a low temperature when heated, but it is considered difficult to vaporize because a complex organic compound is generated. Spraying in a flue gas in a liquid state is often supposed to enable simple and stable operation, but it is actually said that nozzle clogging is likely to occur.
[0003]
FIG. 7 shows an example of a conventional exhaust gas denitration method by direct injection of urea water (JP-A-2001-317346). After the exhaust gas 14 of the diesel engine is oxidized in the oxidation chamber 8 filled with the oxidation catalyst, the exhaust gas 14 passes through the communication pipe 15 and enters the denitration chamber 9 filled with the denitration catalyst. Urea water 11 supplied from the tank 11 is sprayed. 10 is a pump. Since the atmospheric temperature exceeds 400 ° C., the urea blown into the exhaust gas is vaporized and reduces nitrogen oxides in the denitration chamber 9.
[0004]
However, in this device, the supply from the injection portion of the nozzle 12 to the catalyst portion is not sufficient, and the supply is performed in an environment in which urea decomposition is difficult, such as a change in ambient temperature. It was difficult to decompose urea and supply ammonia.
[0005]
[Problems to be solved by the invention]
In these urea blowing devices, cyanuric acid ((HNCO) 3 ), isocyanic acid (3HNCO), which is a thermal decomposition product of urea, and burettes of solid matter are transported in the part of the spray nozzle 12 and the rear part thereof in the course of transport. There is a big problem that it adheres to the inside of the pipe and becomes blocked.
[0006]
An object of the present invention is to provide a urea vaporizer that prevents continuous adhesion of cyanuric acid and isocyanic acid, which are thermal decomposition products of urea, without causing blockage, and an exhaust gas denitration apparatus using the same. To provide.
[0007]
[Means for Solving the Problems]
The invention claimed in the present application to achieve the above object is as follows.
(1) A flow path for the nitrogen oxide-containing exhaust gas, a supply means for the nitrogen oxide reducing agent provided in the flow path, and an exhaust gas denitration unit provided on the downstream side of the supply means for the reducing agent. In the exhaust gas denitration apparatus having the above, the supply means for the reducing agent is provided in a urea water jetting section for jetting urea water, an evaporating section for evaporating urea water jetted from the urea water jetting section, and a downstream section thereof. An exhaust gas denitration apparatus comprising: a hydrolysis section for hydrolyzing urea; and a reducing agent injection section for injecting and supplying gas containing ammonia generated in these sections into the exhaust gas.
[0008]
(2) The exhaust gas denitration apparatus according to (1), wherein a heater is provided inside and outside the apparatus at least in the evaporating section of the evaporating section and the hydrolysis section. (3) The exhaust gas denitration apparatus wherein the evaporating section and the hydrolyzing section are formed as separate vessels, and a temperature control device is provided for each of them.
(4) The exhaust gas denitration apparatus according to any one of (1) to (3), wherein the evaporating section is filled with metal or ceramic particles or honeycomb as a filler.
[0009]
(5) The hydrolysis section is filled with particles supporting γ-alumina or potassium carbonate (K 2 CO 3 ) as a filler for promoting the hydrolysis of urea. The exhaust gas denitration apparatus according to any one of (4).
(6) A urea vaporizer in which a urea water ejection section, a urea water evaporation section, a urea hydrolysis section, and a decomposition gas outlet section are sequentially formed in a cylindrical container, and a urea water spray nozzle is provided at the urea water ejection section. A urea water evaporator is formed by sequentially providing a space necessary for the spraying and a liquid receiving part for receiving the atomized urea particles at a lower part thereof, and promotes the evaporation of the urea water on the liquid receiver. A urea vaporizer characterized by being filled with a filling material.
[0010]
(7) The urea water jetting portion has a urea water jetting nozzle and a flange for mounting the urea water jetting nozzle on the urea vaporizer main body, and the flange surrounds the urea water jetting nozzle. The urea vaporizer according to (6), wherein a gas supply hole is provided so as to supply gas in a tangential direction along an inner periphery of the flange portion.
(8) The urea vaporizer according to (7), wherein the filler in the liquid receiving part is made of a substance having a higher thermal conductivity than the filler in the hydrolysis part.
[0011]
(9) The urea vaporizer according to (7) or (8), wherein the filling of the liquid receiving portion is metal or ceramic particles or honeycomb.
(10) The hydrolyzing section is filled with particles supporting γ-alumina or potassium carbonate (K 2 CO 3 ) as a filler for accelerating the hydrolysis of urea. The urea vaporizer according to any one of (9).
[0012]
In the present invention, when the container of the urea vaporizer is uniformly heated and urea water (urea concentration: 30% to 50%) is blown into the inside, the water and urea evaporate inside the container, and the catalyst particles filled in the inside For example, urea is hydrolyzed as shown in the following formula on the surface of γ-alumina particles, particles supporting potassium carbonate, etc., and ammonia gas is generated.
[0013]
(NH 2 ) 2 CO + H 2 O → 2NH 3 + CO 2
The inside of the vaporizer should be maintained at 450 ° C or higher, and should be structured to promote rapid evaporation heating so that solids such as cyanuric acid and isocyanic acid generated in the process of thermal decomposition of urea are not by-produced. preferable. Normally, when urea water is injected into a container kept at a high temperature, the temperature at the surface receiving the liquid drops is reduced, solids are deposited, which leads to blockage, and it is extremely difficult to control the internal temperature. In the present invention, attention is paid to the evaporation portion in the liquid spray, and even if the urea spray flow rate changes significantly, the structure focused on promoting the heat transfer on the evaporation surface so as to suppress the temperature fluctuation inside the container, The upper part (or the upstream side) of the γ-alumina particles or the like filled in the decomposition part was filled with silicon carbide, iron, stainless steel spheres, metal honeycomb, or the like having a higher thermal conductivity than this. Since these fillers have good heat conduction, and have a spherical structure and a honeycomb structure, when urea water droplets collide, they are caught by the uneven portions, so that an increase in the amount of evaporation can be expected. . Further, when heaters are provided inside and outside the container, it contributes to improvement of the heat transfer coefficient from these heaters.
[0014]
Further, a gas supply hole is provided around the urea water spray nozzle, that is, in a flange portion for fixing the nozzle to the vaporizer main body, and a cooling gas (for example, air) is supplied downward along the inner periphery of the flange portion from here. This prevents clogging or the like due to deposits around the nozzle.
[0015]
BEST MODE FOR CARRYING OUT THE INVENTION
【Example】
FIG. 1 shows one embodiment of the urea vaporizer of the present invention. This device forms a urea water inlet, a urea water evaporator (5), a urea hydrolysis unit (7), and a cracked gas outlet (31) in this order from the top of the cylindrical container 30 downward, A urea water injector 1 is installed at the urea water inlet, and a urea water spray section 6 and a liquid receiving section (screen 4) for receiving atomized urea particles are sequentially provided below the urea water injector 1 as a space required for spraying. The liquid receiving portion on the screen 4 is filled with a filler 5 that promotes the evaporation of urea water. The container 30 is uniformly heated by the inner heater 2 and the outer peripheral heater 3, and is controlled so that the temperature inside the container is as uniform as possible. The urea water is sprayed and supplied toward the inside of the container 30 by the injector 1 located at the uppermost part of the apparatus. The sprayed urea water collides with the evaporator filling 5 inside the apparatus and evaporates instantaneously. Here, the space from the injector 1 to the filling of the evaporating section (urea water spraying section 6) is a space necessary for spraying and atomizing urea water. The urea water once fills this space and collides and adheres to the walls of the container. However, since this space is also maintained at a high temperature by the outer peripheral heater 3, it contributes to the evaporation of urea. The evaporated water and urea reach the hydrolyzed packing 7 at the bottom of the container, where they are decomposed into ammonia and carbon dioxide (CO 2 ), and the decomposed gas is taken out from the outlet 31 and jetted into the diesel exhaust system. In the figure, reference numeral 34 denotes a screen for supporting and fixing the filler.
[0016]
FIG. 2 is an explanatory view of the urea water spray injector 1 in FIG. 1 and a mounting portion thereof, and FIG. 3 is a plan view cut along the line III-III in FIG.
[0017]
The injector 1 includes an injector body 1A provided with a urea water introduction pipe 31 and a nozzle 20. A pair of flanges are provided around the injector nozzle 20 from which the urea water is jetted at an interval such that air flows. 21 and 22 are provided. The injector body 1 has a step 32, which is supported on the upper flange 21. The upper flange 21 is provided with a gas supply hole 24, and the lower flange 22 is provided with a gas ejection hole 23 communicating with the gas supply hole 24. As shown in FIG. 3, the gas ejection hole 23 opens in a gap between the nozzle 20 and the flange 21 or 22, supplies tangential air around the nozzle 20, and cools the nozzle by an air flow. At the same time, the sprayed gas-liquid is cooled. That is, the cooling air is supplied to the upper flange 21 from the gas supply hole 24 of the upper flange, passes through the flow path in the upper flange, is supplied to the flow path between the upper flange and the lower flange, and then is supplied to the central portion. It is supplied from the gap with the injector 1 toward the evaporator filling 5 below.
[0018]
As the nozzle 20 for spraying urea water, either a one-fluid nozzle for spraying urea water alone or a two-fluid nozzle for mixing and spraying urea water and gas may be used. The flow rate of the injector 1 may be adjusted by an electromagnetic (solenoid) type in addition to a mechanical type. In either method, when the temperature rises (no spraying is performed), the temperature of the nozzle itself becomes high, and the urea water remaining inside the nozzle is thermally decomposed to form a solid and block the nozzle. In the case of the electromagnetic type, since the heat-resistant temperature is as low as 130 ° C. or less, for example, there is a problem of failure. By-products of cyanuric acid and isocyanic acid are prevented, and stable operation of the injector becomes possible. Accordingly, the present invention has an effect that a stable operation can be continued for a long period of time because the solid matter does not adhere and grow inside the vaporizer in addition to the fact that the pipe of the diesel combustion exhaust gas can be prevented from being clogged.
[0019]
FIG. 4 is an explanatory diagram showing an example of an exhaust gas purification system using the exhaust gas denitration apparatus of the present invention. This apparatus includes a pipe 15 provided at the outlet of the oxidation catalyst reactor 8 as a flow path of the nitrogen oxide-containing exhaust gas, and a means for supplying a nitrogen oxide reducing agent provided in the flow path (nozzle 12). And an exhaust gas denitration reactor 9 provided downstream of the reducing agent supply means in the exhaust gas flow path, wherein the reducing agent supply means is a urea vaporizer as shown in FIG. 1 is used. The urea water is pressurized from a tank 11 to about 0.3 MPa by a pump 10, vaporized by an injector 1 and a vaporizer 13, supplied to a diesel exhaust gas from a nozzle 12, and then enters a denitration reactor 9. And reacts on the NO reduction catalyst surface, and NO in the exhaust gas is reduced to N 2 .
[0020]
As a comparison, when the filler is not used in the vaporizer, the sprayed droplets of urea directly collide with the heater surface or wall and partially evaporate, but the temperature drops due to the low heat capacity of the evaporating part. Drops, forming and accumulating cyanuric acid, isocyanic acid and other solids, and coarse droplets reach the bottom of the container without evaporation. Since this position does not have a heater, urea crystals are easily generated at a low temperature.
[0021]
FIG. 5 shows another embodiment of the present invention. The difference from FIG. 1 is that a metal honeycomb is used as the filler for promoting the evaporation, and the deterioration of the filler 7 (γ-alumina) in the hydrolysis section is reduced. The structure is such that the hydrolysis section is separated from the vaporizer body 13 in order to suppress it. According to this embodiment, deterioration of the filler in the hydrolysis section can be suppressed, and the life can be prolonged.
[0022]
FIG. 6 shows an embodiment in which the vaporizer main body 30 in FIG. 1 is installed at an angle. In this embodiment, since the descent of the spray liquid is reduced by the inclination of the apparatus main body, the screen 4 of the liquid receiving section provided in FIG. 1 is omitted.
[0023]
【The invention's effect】
According to the first to fifth aspects of the present invention, denitration of a nitrogen oxide-containing gas such as diesel engine combustion exhaust gas is stably performed while preventing solid matter from adhering to a pipe or the like using urea water. be able to.
[0024]
According to the invention of claims 6 to 10, in addition to the fact that urea water can prevent cyanuric acid, isocyanic acid and other by-products generated in the thermal decomposition process, it is possible to avoid clogging the pipe of diesel combustion exhaust gas. Since there is no growth of the solid matter inside the vaporizer, stable operation can be continued for a long period of time.
[Brief description of the drawings]
FIG. 1 is an explanatory view showing one embodiment of a urea vaporizer of the present invention.
FIG. 2 is a detailed cross-sectional view around the urea water injector nozzle of FIG. 1;
FIG. 3 is a plan view in the direction of arrows along the line III-III in FIG. 2;
FIG. 4 is a system diagram showing one embodiment of an exhaust gas denitration apparatus using the urea vaporizer of the present invention.
FIG. 5 is an explanatory view showing another embodiment of the urea vaporizer of the present invention.
FIG. 6 is an explanatory view showing another embodiment of the present invention in which the urea vaporizer is inclined.
FIG. 7 is an explanatory view showing an example of a conventional urea direct injection type exhaust gas denitration apparatus.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Injector, 2 ... Internal heater, 3 ... Outer periphery heater, 4 ... Screen, 5 ... Evaporation part filling, 6 ... Urea water spraying part, 7 ... Hydrolysis part filling, 9 ... Denitrification reactor, 12 ... Blowing Nozzle, 13: vaporizer main body, 30: cylindrical container, 31: cracked gas outlet.

Claims (10)

窒素酸化物含有排ガスの流路と、該流路に設けられた窒素酸化物の還元剤の供給手段と、前記還元剤の供給手段の後流側に設けられた排ガス脱硝部とを有する排ガス脱硝装置であって、前記還元剤の供給手段は、尿素水を噴出させる尿素水噴出部と、該尿素水噴出部から噴出した尿素水を蒸発させる蒸発部と、その後流部に設けられた、尿素を加水分解する加水分解部と、これらの部分で発生したアンモニアを含むガスを、前記排ガス中に噴射供給する還元剤噴射部とを有することを特徴とする排ガス脱硝装置。Exhaust gas denitration having a nitrogen oxide-containing exhaust gas flow path, a nitrogen oxide reducing agent supply means provided in the flow path, and an exhaust gas denitration unit provided downstream of the reducing agent supply means An apparatus, wherein the reducing agent supply means includes: a urea water ejection unit for ejecting urea water, an evaporation unit for evaporating the urea water ejected from the urea water ejection unit, and a urea An exhaust gas denitration apparatus, comprising: a hydrolysis section for hydrolyzing the water; and a reducing agent injection section for injecting and supplying gas containing ammonia generated in these sections into the exhaust gas. 前記蒸発部と加水分解部のうち、少なくとも蒸発部において、前記装置内部及び外部にヒータを有することを特徴とする請求項1記載の排ガス脱硝装置。The exhaust gas denitration apparatus according to claim 1, wherein a heater is provided inside and outside of the apparatus at least in the evaporation section of the evaporation section and the hydrolysis section. 前記蒸発部と加水分解部を別容器として形成し、それぞれに温度制御装置を設けたことを特徴とする排ガス脱硝装置。An exhaust gas denitration apparatus, wherein the evaporating section and the hydrolysis section are formed as separate vessels, and a temperature control device is provided for each of them. 前記蒸発部には、充填物として金属またはセラミックスの粒子またはハニカムが充填されていることを特徴とする請求項1ないし3のいずれかに記載の排ガス脱硝装置。The exhaust gas denitration apparatus according to any one of claims 1 to 3, wherein the evaporating section is filled with metal or ceramic particles or honeycomb as a filler. 前記加水分解部には、尿素の加水分解を促進する充填物として、γアルミナまたは炭酸カリウム(KCO)を担持した粒子が充填されていることを特徴とする請求項1ないし4のいずれかに記載の排ガス脱硝装置。5. The hydrolyzing section is filled with particles supporting γ-alumina or potassium carbonate (K 2 CO 3 ) as a filler for accelerating the hydrolysis of urea. An exhaust gas denitration apparatus according to any one of the above. 筒状容器内に、尿素水噴出部、尿素水蒸発部、尿素加水分解部および分解ガス出口部を順に形成した尿素気化器であって、該尿素水噴出部に尿素水噴霧ノズルを設置し、その下部に前記噴霧に必要な空間部分と、微粒化した尿素粒子を受け止める受液部とを順次設けて尿素水蒸発部を形成し、該受液部上に尿素水の蒸発を促進する充填物を充填したことを特徴とする尿素気化器。A urea vaporizer in which a urea water ejection unit, a urea water evaporation unit, a urea hydrolysis unit, and a decomposition gas outlet unit are sequentially formed in a cylindrical container, and a urea water spray nozzle is installed in the urea water ejection unit. A space portion necessary for the spraying and a liquid receiving portion for receiving finely divided urea particles are sequentially provided at a lower portion thereof to form a urea water evaporating portion, and a filler for promoting evaporation of urea water is provided on the liquid receiving portion. A urea vaporizer characterized by being filled with: 前記尿素水噴出部は、尿素水噴出ノズルと、該尿素水噴出ノズルを尿素気化器本体に装着するためのフランジ部とを有し、該フランジ部は、前記尿素水噴出ノズルを取り囲み、かつ、該フランジ部の内周に沿って接線方向に気体を供給するように気体供給孔が設けられていることを特徴とする請求項6記載の尿素気化器。The urea water ejection section has a urea water ejection nozzle, and a flange portion for mounting the urea water ejection nozzle to the urea vaporizer main body, the flange portion surrounds the urea water ejection nozzle, and 7. The urea vaporizer according to claim 6, wherein a gas supply hole is provided so as to supply gas tangentially along an inner periphery of the flange portion. 前記受液部の充填物が、後記加水分解部の充填物よりも熱伝導率の良好な物質からなることを特徴とする請求項7記載の尿素気化器。8. The urea vaporizer according to claim 7, wherein the filler in the liquid receiving part is made of a substance having a higher thermal conductivity than the filler in the hydrolysis part. 前記受液部の充填物が金属またはセラミックスの粒子またはハニカムである請求項7または8記載の尿素気化器。9. The urea vaporizer according to claim 7, wherein the filler in the liquid receiving portion is metal or ceramic particles or a honeycomb. 前記加水分解部には、尿素の加水分解を促進する充填物として、γアルミナまたは炭酸カリウム(KCO)を担持した粒子が充填されていることを特徴とする請求項6ないし9のいずれかに記載の尿素気化器。10. The method according to claim 6, wherein the hydrolyzing section is filled with particles supporting γ-alumina or potassium carbonate (K 2 CO 3 ) as a filler for promoting the hydrolysis of urea. A urea vaporizer as described in Crab.
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