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JPH0442620B2 - - Google Patents
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JPH0442620B2 - - Google Patents

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Publication number
JPH0442620B2
JPH0442620B2 JP58199261A JP19926183A JPH0442620B2 JP H0442620 B2 JPH0442620 B2 JP H0442620B2 JP 58199261 A JP58199261 A JP 58199261A JP 19926183 A JP19926183 A JP 19926183A JP H0442620 B2 JPH0442620 B2 JP H0442620B2
Authority
JP
Japan
Prior art keywords
gas
column
exchange resin
ammonia gas
sulfur dioxide
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 - Lifetime
Application number
JP58199261A
Other languages
Japanese (ja)
Other versions
JPS6091259A (en
Inventor
Jinkichi Myai
Akiko Tagawa
Masaki Mori
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.)
DKK TOA Corp
Original Assignee
DKK Corp
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 DKK Corp filed Critical DKK Corp
Priority to JP58199261A priority Critical patent/JPS6091259A/en
Publication of JPS6091259A publication Critical patent/JPS6091259A/en
Publication of JPH0442620B2 publication Critical patent/JPH0442620B2/ja
Granted legal-status Critical Current

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Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N27/00Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
    • G01N27/02Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance
    • G01N27/04Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance by investigating resistance
    • G01N27/06Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance by investigating resistance of a liquid
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N33/00Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
    • G01N33/0004Gaseous mixtures, e.g. polluted air
    • G01N33/0009General constructional details of gas analysers, e.g. portable test equipment
    • G01N33/0027General constructional details of gas analysers, e.g. portable test equipment concerning the detector
    • G01N33/0036General constructional details of gas analysers, e.g. portable test equipment concerning the detector specially adapted to detect a particular component
    • G01N33/0042SO2 or SO3
    • 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

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Immunology (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • Biochemistry (AREA)
  • Pathology (AREA)
  • General Physics & Mathematics (AREA)
  • Physics & Mathematics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Food Science & Technology (AREA)
  • Medicinal Chemistry (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Sampling And Sample Adjustment (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は大気中や排ガス中の二酸化硫黄ガスの
濃度を測定するための装置に係り、特に試料ガス
中に共存するアンモニアガスを除去して正確な測
定を可能とした測定装置に関する。 大気中が排ガスに含まれている二酸化硫黄ガス
は公害防止の点から、日本工業規格B7952に規定
される溶液導電率方法によつて測定される。かか
る測定方法は吸収液に試料ガスを通したときの吸
収液の導電率の変化から試料ガス中に含まれる二
酸化硫黄ガス濃度を測定するものであるが、試料
ガス中に塩基性ガス、特にアンモニアガスが含ま
れている場合にはアンモニアガスによつて導電率
が変化して誤差を生じ、正確な測定値が得られな
いという不都合が生じていた。このため、このよ
うなアンモニアガスを測定以前に除去する必要が
ある。 アンモニアガスを除去する方法としては、従来
はシユウ酸などの固体酸を充填したトラツプを二
酸化硫黄ガスの測定装置の前段に取りつけて捕集
する方法が採用されていた。また、交換体を使用
してアンモニアガスを吸着させることも、一般に
は古くから知られている。 しかし、こうした方法は、実用的にはいくつか
の問題点を残している。たとえば、シユウ酸を使
用する方法においては、試料ガスが乾燥状態にあ
る場合、固体酸の一部が昇華して試料ガス中に混
入して正誤差の原因になることがあり、そのため
に試料ガスを冷却して加湿するなどの二次的な対
策を施す必要が生じている。 また、イオン交換体を使用する方法としては、
強酸性の陽イオン交換樹脂を用いる方法が特開昭
58−44344号公報に記載されている。 この方法においては強酸性の陽イオン交換樹脂
から酸性成分の揮発があり、測定に影響を与える
ために、実際には樹脂の材質を選定する必要があ
り、測定に先立つて長時間エージングするなどの
前処理の煩雑さを伴なう。 更に前記公報に記載されたNafion(デユポン社
商品名)は、高価であるうえに単位面積あたりの
交換容量が小さいために、これを用いてアンモニ
アガスの除去装置を構成すると大がかりになり、
かつ装置全体の価格の高騰を免れない。 以上のように二酸化硫黄ガス測定装置における
アンモニアガスの除去は、単にアンモニアガスを
処理するのみならず、次のような条件を具備する
ことが不可欠である。 (1) 濃度ppbレベルの二酸化硫黄を100%通過せ
しめること (2) 1/min程度のガス流量でppb濃度レベル
からppm濃度までのアンモニアガスを吸着する
こと (3) 相当の長寿命を有すること (4) アンモニアガス除去用に用いる物質から測定
に影響を与える化学成分が発生しないこと (5) 室外の測定においても上記(1)ないし(4)の条件
を具備すること 本発明者はこのような見地から検討をした結
果、無極性の非水溶液用につくられた強酸性陽イ
オン交換樹脂がアンモニアガスの除去に最適であ
ることを発見し、これにより本発明を完成したも
のである。すなわち、本発明は非水溶液用強酸性
陽イオン交換樹脂が内部に充填されたカラムを試
料ガス採取の流路内に配設してなることを特徴と
している。 以下、添付の図面を参照して、本発明一実施例
を具体的に説明する。 第1図に図示する測定装置において、測定用の
試料ガスは吸引流路1から吸引されてフイルタ2
で除塵され、流量計3を経た後、測定管4内に導
されるようになつている。この測定管4内には所
定量の硫酸々性の過酸化水素溶液がタンク5から
ポンプ6により充填されており、試料ガス中の二
酸化硫黄はこの溶液内を通気する際に、吸収、酸
化されて硫酸となり、これにより溶液の導電率が
高くなり、電極7,7によりその導電率が測定さ
れるようになつている。そして、試料ガスはこの
測定管4内で二酸化硫黄ガスが吸収された後は排
出ポンプ8で大気中に排気されるようになつてい
る。同図において、9は測定に使用された吸収液
の排液タンク10,10は夫々、電磁弁である。 このような測定装置において、例えば流量計3
と測定管4の間に形成された流路11にはアンモ
ニアガス除去用のカラム20が配設されている。
このカラム20は一例を挙げれば第2図に示すよ
うに、内径10mm、筒長80mm等のガラス管21の両
端部にテフロンフイルター22,22が取り付け
られると共に、内部には非水溶液用強酸性陽イオ
ン交換樹脂23が充填されて形成されており、両
端部のジヨイント部が流路11に接続されて、測
定管内に通気せしめられる前段階で試料ガス中の
アンモニアガスを吸着、除去するようになつてい
る。この場合、使用される非水溶液用強酸性陽イ
オン交換樹脂は無極性非水溶媒用にその表面積や
多孔性を厳密に規定して作られた耐摩耗性を有す
る強酸性陽イオン交換樹脂であり、例えば、スル
ホン基を酸性基としたジビニルベンゼン系樹脂等
が使用される。このような非水溶液用強酸性陽イ
オン交換樹脂としては、例えば、アンバリスト1
5(ロームアンドハース(社)製)があり、市販
されて容易に入手することができる。この非水溶
液用強酸性陽イオン交換樹脂は二酸化硫黄を何ら
吸着することなく、アンモニアガスを選択的に吸
着して除去する性質を有している。又、カラム2
0内に充填される際には、水洗浄等の簡単な表面
処理によつて揮発性の酸性物質が除去せしめら
れ、測定中に支障となる化学成分が発生すること
もない。従つて、正確に二酸化硫黄ガスを測定す
ることができる。さらに、アンモニアガスの除去
に必要とされる非水溶液用強酸性陽イオン交換樹
脂の量は例えば2g程度の少量であり、充填用の
カラムも小さいものを使用できるから、測定測置
に大きな設計変更を要することなく組み込むこと
ができると共に、装置を大がかりのものとする必
要もない。又、さらに、アンモニアガスの吸着量
についても5〜6ミリモル/gと大きいため、長
期に使用できカラムの交換頻度も少なく、操作上
の煩雑さも少ないものである。 なお、この非水溶液用強酸性陽イオン交換樹脂
が充填されたカラム20流量計3と測定管4の間
の流路11に配設されるだけでなく、流量計3と
フイルタ2の間の流路12に配設されてもよく、
又、フイルタ2前方の吸引流路1に配設されても
よく、試料ガスが測定管4内に導入される以前の
流路であれば、その配設場所は限られない。又、
1基のみならず、2基以上配設してもよく、その
数も限定されない。 次に、本発明を実施例につき説明する。 実施例 1 非水溶液用強酸性陽イオン交換樹脂としてアン
バリスト15(ロームアンドハース(社)製)を使用
し、このアンバリスト15をカラム内に2g充填
し、吸引流路1に配設した。次いで二酸化硫黄を
全く含まない試料ガスを流路1/minで第1図
の測定装置に送り、濃度を測定した。比較例とし
て、カラムを配設しない測定装置で同じ試料ガス
を同条件で送り、その濃度を測定した。結果は第
1表に示してあるが、A欄がカラムを取り付けた
場合の測定値、B欄はカラムを取り付けていない
場合の測定値である。同表から、カラムからは測
定に支障を与える化学成分が発生していないこと
がわかる。
The present invention relates to a device for measuring the concentration of sulfur dioxide gas in the atmosphere or exhaust gas, and particularly to a measuring device that enables accurate measurement by removing ammonia gas coexisting in a sample gas. In order to prevent pollution, the sulfur dioxide gas contained in exhaust gas in the atmosphere is measured by the solution conductivity method specified in Japanese Industrial Standard B7952. This measurement method measures the concentration of sulfur dioxide gas contained in the sample gas from the change in conductivity of the absorption liquid when the sample gas is passed through the absorption liquid. When gas is included, the conductivity changes due to ammonia gas, causing an error and causing the inconvenience that accurate measurement values cannot be obtained. Therefore, it is necessary to remove such ammonia gas before measurement. The conventional method for removing ammonia gas has been to attach a trap filled with a solid acid such as oxalic acid to a stage upstream of a sulfur dioxide gas measuring device to collect the trap. It has also been known for a long time to adsorb ammonia gas using an exchanger. However, these methods still have some practical problems. For example, in a method using oxalic acid, if the sample gas is in a dry state, some of the solid acid may sublimate and mix into the sample gas, causing an error in the sample gas. It has become necessary to take secondary measures such as cooling and humidifying the air. In addition, as a method using an ion exchanger,
A method using a strongly acidic cation exchange resin was published in JP-A-Sho.
It is described in Publication No. 58-44344. In this method, acidic components volatilize from the strongly acidic cation exchange resin, which affects the measurement, so it is actually necessary to select the material of the resin, and it is necessary to aging for a long time before measurement. Involves complicated pre-processing. Furthermore, Nafion (trade name of DuPont) described in the above publication is expensive and has a small exchange capacity per unit area, so if it were used to construct an ammonia gas removal device, it would be large-scale.
Moreover, the price of the entire device will inevitably rise. As described above, in order to remove ammonia gas in a sulfur dioxide gas measuring device, it is essential not only to simply treat the ammonia gas, but also to meet the following conditions. (1) Allows 100% of sulfur dioxide at ppb level to pass through.(2) Adsorbs ammonia gas from ppb concentration level to ppm concentration at a gas flow rate of about 1/min.(3) Has a considerably long life. (4) The substance used for ammonia gas removal must not generate any chemical components that would affect the measurement. (5) The conditions (1) to (4) above must be met even in outdoor measurements. As a result of investigation from various viewpoints, it was discovered that a strongly acidic cation exchange resin made for non-polar, non-aqueous solutions is optimal for removing ammonia gas, and the present invention was thus completed. That is, the present invention is characterized in that a column filled with a strongly acidic cation exchange resin for non-aqueous solutions is disposed in a flow path for sample gas collection. Hereinafter, one embodiment of the present invention will be described in detail with reference to the accompanying drawings. In the measuring device shown in FIG.
After passing through a flow meter 3, it is introduced into a measuring tube 4. This measuring tube 4 is filled with a predetermined amount of a sulfuric acid-based hydrogen peroxide solution from a tank 5 by a pump 6, and the sulfur dioxide in the sample gas is absorbed and oxidized when the solution is aerated. The solution becomes sulfuric acid, which increases the conductivity of the solution, and the conductivity is measured by electrodes 7, 7. After the sample gas absorbs sulfur dioxide gas in the measuring tube 4, it is exhausted into the atmosphere by an exhaust pump 8. In the figure, reference numeral 9 designates drain tanks 10 and 10 for the absorption liquid used in the measurement, respectively, which are electromagnetic valves. In such a measuring device, for example, a flowmeter 3
A column 20 for removing ammonia gas is disposed in a flow path 11 formed between the measuring tube 4 and the measuring tube 4 .
For example, as shown in FIG. 2, this column 20 has Teflon filters 22, 22 attached to both ends of a glass tube 21 with an inner diameter of 10 mm and a tube length of 80 mm, and has a strong acid positive polarizer for non-aqueous solutions inside. It is formed by being filled with ion exchange resin 23, and the joint portions at both ends are connected to the flow path 11 to adsorb and remove ammonia gas in the sample gas before it is vented into the measurement tube. ing. In this case, the strongly acidic cation exchange resin for non-aqueous solutions used is a strong acid cation exchange resin with wear resistance that is made for non-polar non-aqueous solvents with its surface area and porosity strictly specified. For example, a divinylbenzene resin in which a sulfone group is an acidic group is used. As such a strong acidic cation exchange resin for non-aqueous solutions, for example, Amberlyst 1
5 (manufactured by Rohm and Haas), and is easily available commercially. This strongly acidic cation exchange resin for non-aqueous solutions has the property of selectively adsorbing and removing ammonia gas without adsorbing any sulfur dioxide. Also, column 2
When the sample is filled into the sample, volatile acidic substances are removed by simple surface treatment such as washing with water, and no chemical components are generated that may cause problems during measurement. Therefore, sulfur dioxide gas can be measured accurately. Furthermore, the amount of strongly acidic cation exchange resin for non-aqueous solutions required to remove ammonia gas is as small as, for example, 2 g, and a smaller column can be used for packing, making it a major design change for measurement equipment. It can be incorporated without requiring any additional equipment, and there is no need to make the device large-scale. Moreover, since the amount of ammonia gas adsorbed is as large as 5 to 6 mmol/g, it can be used for a long period of time, the column needs to be replaced less frequently, and the operation is less complicated. Note that the column 20 filled with this strongly acidic cation exchange resin for non-aqueous solutions is not only disposed in the flow path 11 between the flow meter 3 and the measuring tube 4, but also in the flow path between the flow meter 3 and the filter 2. It may be arranged in path 12,
Further, it may be disposed in the suction channel 1 in front of the filter 2, and its location is not limited as long as it is in the channel before the sample gas is introduced into the measurement tube 4. or,
Not only one unit but two or more units may be provided, and the number is not limited. Next, the present invention will be explained with reference to examples. Example 1 Amberlyst 15 (manufactured by Rohm and Haas) was used as a strongly acidic cation exchange resin for non-aqueous solutions, and 2 g of Amberlyst 15 was packed into a column and placed in the suction channel 1. Next, a sample gas containing no sulfur dioxide was sent to the measuring device shown in FIG. 1 at a flow rate of 1/min, and the concentration was measured. As a comparative example, the same sample gas was sent under the same conditions using a measuring device without a column, and its concentration was measured. The results are shown in Table 1, where column A is the measured value with the column attached, and column B is the measured value without the column attached. From the same table, it can be seen that no chemical components that would interfere with measurement were generated from the column.

【表】 実施例 2 アンバリスト15を充填したカラムを吸引流路
1に配設し、二酸化硫黄の濃度がおおむね40ppb
の試料ガスを実施例1と同条件で測定した。結果
を第2表に示す。同表において、A,Bは実施例
と同様である。この表から、二酸化硫黄ガスはカ
ラム内で何ら吸着されないことがわかる。
[Table] Example 2 A column packed with Amberlyst 15 was placed in the suction channel 1, and the concentration of sulfur dioxide was approximately 40 ppb.
The sample gas was measured under the same conditions as in Example 1. The results are shown in Table 2. In the same table, A and B are the same as in the example. From this table, it can be seen that no sulfur dioxide gas is adsorbed within the column.

【表】 実施例 3 試料ガスとして、二酸化硫黄の濃度45ppb、ア
ンモニアの濃度100ppbの混合気体を使用し、実
施例1と同条件で測定した。結果を第3表に示
す。同表から、カラムを配設しない場合のB欄の
測定値に対し、カラムを配設した場合のB欄測定
値の方がアンモニアガスの影響を受けず、アンモ
ニアガスは非水溶液用強酸性陽イオン交換樹脂に
完全に吸着されているのがわかる。
[Table] Example 3 A mixed gas having a sulfur dioxide concentration of 45 ppb and an ammonia concentration of 100 ppb was used as a sample gas, and measurements were made under the same conditions as in Example 1. The results are shown in Table 3. From the same table, the measured values in column B when a column is installed are not affected by ammonia gas, compared to the measured values in column B when a column is not installed, and ammonia gas is a strong acid positive solution for non-aqueous solutions. It can be seen that it is completely adsorbed on the ion exchange resin.

【表】 実施例 4 非水溶液用強酸性陽イオン交換樹脂がアンモニ
アガス濃度の相違により、どのよに影響を受ける
かを調べるため、濃度が異なつたアンモニアガス
含有の試料ガスをカラムに通して実施例1と同条
件で測定した。結果を第4表に示すが、広範囲の
アンモニアガス濃度に対し安定した吸着を示し、
正確な測定が可能である。
[Table] Example 4 In order to investigate how strongly acidic cation exchange resin for non-aqueous solutions is affected by differences in ammonia gas concentration, sample gases containing ammonia gas with different concentrations were passed through a column. Measurement was carried out under the same conditions as in Example 1. The results are shown in Table 4, showing stable adsorption over a wide range of ammonia gas concentrations.
Accurate measurements are possible.

【表】 実施例 5 室外大気での測定状態では試料ガスが湿つてい
るため、湿度の異なつた試料ガスを実施例1と同
条件で測定した。第5表は湿度0%、温度20℃の
場合の測定結果、第6表は湿度70%、温度20℃の
場合の測定結果であり、れらの条件においてもカ
ラムを配設した測定値(A欄)の方にも湿度の影
などは出ていない。
[Table] Example 5 Since the sample gas is humid when measured in the outdoor atmosphere, sample gases with different humidity were measured under the same conditions as in Example 1. Table 5 shows the measurement results when the humidity is 0% and the temperature is 20℃, and Table 6 shows the measurement results when the humidity is 70% and the temperature is 20℃. There are no signs of humidity in column A) either.

【表】【table】

【表】【table】

【表】 以上、説明したように、本発明は非水溶液用強
酸性陽イオン交換樹脂を充填したカラムに試料ガ
スを通して、アンモニアガスを該樹脂に吸着せし
め、アンモニアガスの影響を除去したから、二酸
化硫黄ガス濃度を正確に測定することができると
いう効果がある。
[Table] As explained above, in the present invention, a sample gas is passed through a column packed with a strongly acidic cation exchange resin for non-aqueous solutions, and ammonia gas is adsorbed by the resin, and the influence of ammonia gas is removed. This has the effect that the sulfur gas concentration can be measured accurately.

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

第1図は本発明の一実施例の全体配置図、第2
図はカラムの断面図である。 1……吸引流路、2……フイルタ、3……流量
計、4……測定管、5……タンク、6……ポン
プ、7……電極、8……ポンプ、9……タンク、
10……電磁弁、11,12……流路、20……
カラム、23……非水溶液用強酸性陽イオン交換
樹脂。
Fig. 1 is an overall layout diagram of one embodiment of the present invention, Fig. 2
The figure is a cross-sectional view of the column. 1... Suction channel, 2... Filter, 3... Flow meter, 4... Measuring tube, 5... Tank, 6... Pump, 7... Electrode, 8... Pump, 9... Tank,
10... Solenoid valve, 11, 12... Channel, 20...
Column, 23... Strongly acidic cation exchange resin for non-aqueous solutions.

Claims (1)

【特許請求の範囲】[Claims] 1 非水溶液用強酸性陽イオン交換樹脂が内部に
充填されたカラムを試料ガス採取の流路内に配設
してなることを特徴とする二酸化硫黄ガスの測定
装置。
1. A sulfur dioxide gas measuring device comprising a column filled with a strongly acidic cation exchange resin for non-aqueous solutions in a flow path for sample gas collection.
JP58199261A 1983-10-26 1983-10-26 Sulfur dioxide gas measuring device Granted JPS6091259A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58199261A JPS6091259A (en) 1983-10-26 1983-10-26 Sulfur dioxide gas measuring device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58199261A JPS6091259A (en) 1983-10-26 1983-10-26 Sulfur dioxide gas measuring device

Publications (2)

Publication Number Publication Date
JPS6091259A JPS6091259A (en) 1985-05-22
JPH0442620B2 true JPH0442620B2 (en) 1992-07-14

Family

ID=16404843

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58199261A Granted JPS6091259A (en) 1983-10-26 1983-10-26 Sulfur dioxide gas measuring device

Country Status (1)

Country Link
JP (1) JPS6091259A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US12061182B2 (en) 2020-07-29 2024-08-13 Saudi Arabian Oil Company Ion conductivity filter and measurement system

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56128568U (en) * 1980-02-29 1981-09-30

Also Published As

Publication number Publication date
JPS6091259A (en) 1985-05-22

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