JPS598198Y2 - Gas sampling device for 3 continuous measurements of NH↓ - Google Patents

Gas sampling device for 3 continuous measurements of NH↓

Info

Publication number
JPS598198Y2
JPS598198Y2 JP1979020128U JP2012879U JPS598198Y2 JP S598198 Y2 JPS598198 Y2 JP S598198Y2 JP 1979020128 U JP1979020128 U JP 1979020128U JP 2012879 U JP2012879 U JP 2012879U JP S598198 Y2 JPS598198 Y2 JP S598198Y2
Authority
JP
Japan
Prior art keywords
gas
catalyst
sampling device
dust
gas flow
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
JP1979020128U
Other languages
Japanese (ja)
Other versions
JPS55119968U (en
Inventor
武美 中根
俊邦 世良
良弘 白石
道夫 羽田
Original Assignee
三菱重工業株式会社
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 三菱重工業株式会社 filed Critical 三菱重工業株式会社
Priority to JP1979020128U priority Critical patent/JPS598198Y2/en
Publication of JPS55119968U publication Critical patent/JPS55119968U/ja
Application granted granted Critical
Publication of JPS598198Y2 publication Critical patent/JPS598198Y2/en
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 本考案は石炭焚き、重油焚きボイラやセメントキルン、
ガラス溶解炉などから排出される排ガスなどガス流中の
NH3濃度を計器で連続測定する時のガス採取装置に関
するものであり、特にガス中に多量のダストが含有され
ている場合、ダストの影響もなく連続的にかつ有効にガ
ス採取するものに関する。
[Detailed explanation of the invention] This invention is applicable to coal-fired, heavy oil-fired boilers, cement kilns,
This relates to a gas sampling device used to continuously measure the NH3 concentration in a gas stream such as exhaust gas discharged from a glass melting furnace, etc. Especially when a large amount of dust is contained in the gas, the influence of dust may also be detected. It relates to gas collection that can be carried out continuously and effectively.

NH3濃度を計器で測定する方法はイオン電極法、溶液
導電率法、赤外線吸収法、NH3をNOに変換後の化学
発光法、マイクロ波分光法などがあるが、NH3を直接
測定する方法は水分、SOXなどの共存ガスの影響で正
確な濃度を連続測定することができない。
Methods for measuring NH3 concentration with instruments include the ion electrode method, solution conductivity method, infrared absorption method, chemiluminescence method after converting NH3 to NO, and microwave spectroscopy. Continuous measurement of accurate concentration is not possible due to the influence of coexisting gases such as , SOX, etc.

一方化学発光法はNO測定として信頼性の高い計器を利
用するものでありNH3をNOに転化後は共存ガスの影
響もほとんど考慮する必要がなく実用性は高いものと考
えられている。
On the other hand, the chemiluminescence method uses a highly reliable instrument for NO measurement, and it is considered to be highly practical as there is almost no need to consider the effects of coexisting gases after converting NH3 to NO.

この方法では排ガス中のダストを除去しなければサンプ
リングラインや分析計に種々のトラブルを生しるため通
常サンプリングラインの先端に一次フィルターを、分析
計に二次フィルターを設置しており、ダスト濃度の高い
場合には一次フィルターの交換頻度が高くなる。
With this method, if the dust in the exhaust gas is not removed, various problems will occur in the sampling line and analyzer, so a primary filter is usually installed at the tip of the sampling line and a secondary filter is installed at the analyzer. If the value is high, the primary filter will need to be replaced more frequently.

又従来のNH3をNOに変換する触媒は2〜4mmφの
粒状品が使用されており、ダスト濃度の低い場合にはダ
ストの触媒層への閉塞について懸念しなくても良いが、
ダスト濃度が高いと目詰りを生じるのは時間の問題であ
り、粒状品は適用できなくなり、ダストの影響の少ない
形状即ちハニカム状又はパイプ状など、ダスト閉塞が生
じない形状にする必要がある。
In addition, conventional catalysts for converting NH3 to NO use granular products with a diameter of 2 to 4 mm, and when the dust concentration is low, there is no need to worry about dust clogging the catalyst layer.
If the dust concentration is high, it is only a matter of time before clogging occurs, so granular products cannot be used, and it is necessary to use a shape that is less affected by dust, such as a honeycomb shape or a pipe shape, which will not cause dust clogging.

本考案は従来の化学発光法を利用するNH3分析計が有
している欠点を改良するものである。
The present invention improves the drawbacks of conventional NH3 analyzers that utilize chemiluminescence methods.

本考案はダストをできるだけ吸引しない状態でガスサン
プリングできるようにガス導入口を円錐状に広げて且つ
ガス流れの下流側に導入口を向けることと、NH3をN
Oに転換する触媒をダストによる目詰り現象がないよう
にハニカム状又はパイプ状のようなガス流れに平行な触
媒面を有する形状である点が特徴である。
The present invention consists of widening the gas inlet into a conical shape and directing the inlet toward the downstream side of the gas flow so that gas sampling can be performed without sucking in dust as much as possible.
A feature of the catalyst is that it has a honeycomb-like or pipe-like shape with a catalyst surface parallel to the gas flow to prevent clogging due to dust.

即ち、本考案はダストを多量に含むガス中のNH3濃度
を連続測定するためのガス流路内に設けるガス採取装置
において、円錐状など広がり形状のガス流れの下流側に
広がり側を向けて設けるサンプリング孔、前記ガス採取
装置の内部に設けたNH3をNOに転換するためのハニ
カム状又はパイプ状のようなガス流れに平行な触媒面を
有する形状のNH3酸化触媒、並びに該触媒を加熱する
加熱装置を有することを特徴とするNH3連続測定用ガ
ス採取装置である。
That is, the present invention is a gas sampling device installed in a gas flow path for continuously measuring the NH3 concentration in a gas containing a large amount of dust. a sampling hole, an NH3 oxidation catalyst in the shape of a honeycomb or pipe having a catalytic surface parallel to the gas flow for converting NH3 into NO, provided inside the gas sampling device, and heating for heating the catalyst; This is a gas sampling device for continuous measurement of NH3, characterized by having a device.

以下、煙道排ガスに適用する場合を中心として、本考案
の実施態様を述べる。
Hereinafter, embodiments of the present invention will be described, focusing on the case where it is applied to flue gas.

第1図に本考案の一実施例様を示す。FIG. 1 shows an embodiment of the present invention.

ガス導入口1はガス流れの下流側に向けかつ形状を円錐
状に広げることによりサンプリングガスは渦を生じて巻
き込まれるように吸引され、粒子径の大きいダストは導
入されなくなるとともに、円錐状に広がった部分でガス
流速の急激な変化で更に粒子径の大きいダストがふるい
落される効果が倍加されるものであり、本ガス採取装置
へ導入されるダスト濃度は排ガス10中の告〜責に減少
されると共にその平均粒子径は小さくなってくる。
The gas inlet 1 faces the downstream side of the gas flow and expands into a conical shape, so that the sampling gas is sucked in as if it is being drawn into a vortex, and dust with large particle diameters is not introduced, and the gas is spread out in a conical shape. The rapid change in the gas flow rate in this area doubles the effect of sieving out dust with larger particle sizes, and the dust concentration introduced into this gas sampling device is reduced to 10% in the exhaust gas. The average particle size becomes smaller as the particle size increases.

従って本考案以前の採取装置ではガス導入口1の直後に
設置していた一次フィルターは本考案ではほとんど不要
となりNH3酸化触媒3の後に取付けることができるよ
うになった。
Therefore, the primary filter, which was installed immediately after the gas inlet 1 in the sampling device before the present invention, is almost unnecessary in the present invention, and can be installed after the NH3 oxidation catalyst 3.

第1図での実施態様での一次フィルター4は万一の安全
対策のために取付けているものであり、ダスト付着率も
減少し、その交換頻度もおのずと少なくなる。
The primary filter 4 in the embodiment shown in FIG. 1 is installed as a safety measure in case of an emergency, and the rate of dust adhesion is reduced, and the frequency of its replacement is naturally reduced.

NH3酸化触媒3はNH3をNOに転換する触媒であり
、例えばケイソウ土やシリカアルミナなどの多孔性耐火
物にコバルト,銅,クロム,マンガンなどの酸化物を担
持させたものを挙げることができる。
The NH3 oxidation catalyst 3 is a catalyst that converts NH3 to NO, and includes, for example, a catalyst in which oxides such as cobalt, copper, chromium, and manganese are supported on a porous refractory such as diatomaceous earth or silica alumina.

これを通常700℃から800℃に加熱することで95
%以上の転換効率を示す。
By heating this from 700℃ to 800℃,
% or more conversion efficiency.

本考案以前の従来の触媒形状は2〜4mmφの粒状品で
あり、ダストや排ガス中の化学物質による触媒層への目
詰りが生じるので、本考案で適用する触媒はダスト閉塞
の懸念がないハニカム状,パイプ状などのガス流と平行
な面を有する形状の触媒を使用する。
Prior to this invention, the conventional catalyst shape was a granular product with a diameter of 2 to 4 mm, and the catalyst layer was clogged by dust and chemicals in exhaust gas, so the catalyst applied in this invention is a honeycomb shape that does not have the risk of dust clogging. A catalyst with a shape parallel to the gas flow, such as a shape or a pipe, is used.

また、酸化反応に必要な温度にまで上げるため触媒の周
囲をヒーター2で加熱している。
Additionally, the area around the catalyst is heated with a heater 2 to raise the temperature to the level required for the oxidation reaction.

煙道9内に触媒3を設置しているため触媒加熱用ヒータ
ー2の加熱温度は排ガス温度に上乗せするだけで良く、
この点も触媒を煙道内に設置する利点である。
Since the catalyst 3 is installed in the flue 9, the heating temperature of the catalyst heating heater 2 only needs to be added to the exhaust gas temperature.
This point is also an advantage of installing the catalyst in the flue.

即ち、測定対象ガスが高温の場合は、本考案のガス採取
装置をガス流路内に設けることにより、前記の加熱装置
の熱量を節約することができる。
That is, when the gas to be measured has a high temperature, the amount of heat of the heating device can be saved by providing the gas sampling device of the present invention in the gas flow path.

サンプリングガスはガス導入口1からNH3酸化触媒3
,ダストフィルター4を通過し5を経てNOx分析計に
導かれる。
Sampling gas is passed from gas inlet 1 to NH3 oxidation catalyst 3
, passes through a dust filter 4, and is led to a NOx analyzer via 5.

NOx分析計を使用して、本採取装置を利用する場合は
、排ガス中のNH3を触媒層でNOに転換したガスと触
媒層を通過しないガス中のNOx濃度の差を演算するこ
とにより算出される。
When using this sampling device with a NOx analyzer, the NOx concentration is calculated by calculating the difference between the NOx concentration in the gas in which NH3 in the exhaust gas is converted to NO in the catalyst layer and the gas that does not pass through the catalyst layer. Ru.

この場合は本採取装置にはNO検出ラインへのガスサン
プリング管を併設させることも可能である。
In this case, it is also possible to attach a gas sampling pipe to the NO detection line to this sampling device.

以上述べた本考案の実施態様のガス採取装置のガス導入
口1は触媒3と垂直方向に向けているが本考案の他の実
施態様の第2図のように一直線上にする構造でも良いが
、この場合はガス流路が曲管部になっている所に挿入し
てガス流れ10の影響を直接受けないようにすることが
必要である。
Although the gas inlet 1 of the gas sampling device in the embodiment of the present invention described above is oriented perpendicularly to the catalyst 3, it may be arranged in a straight line as shown in FIG. 2 of another embodiment of the present invention. In this case, it is necessary to insert the gas flow path into a curved pipe section so that it is not directly affected by the gas flow 10.

さらにガス採取装置は、ボイラなどの燃焼装置の排ガス
に対しては、通常耐腐食性の材料で構威されることが望
ましい。
Further, it is generally desirable that the gas sampling device be constructed of a material that is resistant to corrosion against the exhaust gases of combustion devices such as boilers.

特に上記のNOx濃度差を算出するNH3測定では、分
析計に導かれるサンプリング管内は石英ガラス,ステン
レス,チタンなどのNH3をNOに転換する作用のない
材質にすべきである。
Particularly in the above-mentioned NH3 measurement for calculating the NOx concentration difference, the inside of the sampling tube led to the analyzer should be made of a material that does not convert NH3 into NO, such as quartz glass, stainless steel, or titanium.

本考案はダストを多量に含有する排ガス中のNH3濃度
を連続的にサンプリングして分析計で測定する時に有力
な手段であり、NH3を使用する脱硝装置でも適用性は
大である。
The present invention is an effective means for continuously sampling and measuring the NH3 concentration in exhaust gas containing a large amount of dust using an analyzer, and is also highly applicable to denitrification equipment that uses NH3.

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

第1図はこの考案の実施態様を原理的に示した縦断面図
であり、図中の符号1はガスサンプリング孔、2は触媒
加熱用ヒーター、3はNH3をNOに転換するハニカム
触媒、4はダストフィルターを示し、NOに転換された
ガスは5より測定装置に導びかれる。 6は加熱ヒーター電気端子、7は触媒3ならびにダスト
フィルター4の挿入蓋フランジ、8は触媒3の位置固定
ピンを示す。 排ガスは煙道9を矢印10の方向に流れる。 第2図はガスサンプリング孔と触媒3を一直線上にした
構造の実施態様を示し、排ガス煙道9が曲管の場合の例
を示す。
FIG. 1 is a longitudinal sectional view showing the principle of an embodiment of this invention, in which reference numeral 1 is a gas sampling hole, 2 is a heater for heating the catalyst, 3 is a honeycomb catalyst for converting NH3 into NO, and 4 5 indicates a dust filter, and the gas converted to NO is led to the measuring device through 5. Reference numeral 6 indicates a heater electric terminal, 7 indicates an insertion lid flange for the catalyst 3 and the dust filter 4, and 8 indicates a position fixing pin for the catalyst 3. The exhaust gas flows through the flue 9 in the direction of the arrow 10. FIG. 2 shows an embodiment of a structure in which the gas sampling hole and the catalyst 3 are arranged in a straight line, and shows an example in which the exhaust gas flue 9 is a curved pipe.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] ダストを多量に含むガス中のNH3濃度を連続測定する
ためのガス流路内に設けるガス採取装置において、円錐
状など広がり形状のガス流れの下流側に広がり側を向け
て設けるサンプリング孔、前記ガス採取装置の内部に設
けたNH3をNOに転換するためのハニカム状又はパイ
プ状のようなガス流れに平行な触媒面を有する形状のN
H3酸化触媒並びに該触媒を加熱する加熱装置を有する
ことを特徴とするNH3連続測定用ガス採取装置。
In a gas sampling device installed in a gas flow path for continuously measuring the NH3 concentration in a gas containing a large amount of dust, a sampling hole provided with the expanding side facing the downstream side of the gas flow having a widening shape such as a conical shape, A honeycomb-shaped or pipe-shaped N catalyst with a catalytic surface parallel to the gas flow is installed inside the sampling device to convert NH3 into NO.
A gas sampling device for continuous measurement of NH3, comprising an H3 oxidation catalyst and a heating device for heating the catalyst.
JP1979020128U 1979-02-19 1979-02-19 Gas sampling device for 3 continuous measurements of NH↓ Expired JPS598198Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1979020128U JPS598198Y2 (en) 1979-02-19 1979-02-19 Gas sampling device for 3 continuous measurements of NH↓

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1979020128U JPS598198Y2 (en) 1979-02-19 1979-02-19 Gas sampling device for 3 continuous measurements of NH↓

Publications (2)

Publication Number Publication Date
JPS55119968U JPS55119968U (en) 1980-08-25
JPS598198Y2 true JPS598198Y2 (en) 1984-03-13

Family

ID=28850510

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1979020128U Expired JPS598198Y2 (en) 1979-02-19 1979-02-19 Gas sampling device for 3 continuous measurements of NH↓

Country Status (1)

Country Link
JP (1) JPS598198Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58109048U (en) * 1982-01-21 1983-07-25 富士電機株式会社 Gas inlet pipe in gas converter

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5213757A (en) * 1975-07-23 1977-02-02 Kazumi Yamashita Sine wave signal generator circuit

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5213757A (en) * 1975-07-23 1977-02-02 Kazumi Yamashita Sine wave signal generator circuit

Also Published As

Publication number Publication date
JPS55119968U (en) 1980-08-25

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