JPS5831081B2 - Method for producing printing paste for reactive dyes by solid-phase reaction - Google Patents
Method for producing printing paste for reactive dyes by solid-phase reactionInfo
- Publication number
- JPS5831081B2 JPS5831081B2 JP54046600A JP4660079A JPS5831081B2 JP S5831081 B2 JPS5831081 B2 JP S5831081B2 JP 54046600 A JP54046600 A JP 54046600A JP 4660079 A JP4660079 A JP 4660079A JP S5831081 B2 JPS5831081 B2 JP S5831081B2
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- cellulose
- sodium
- nacmc
- reaction
- solid
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Description
【発明の詳細な説明】
本発明は反応性染料用捺染糊料としての繊維素グIJ
’ =r−ル酸ソーダの製造方法に関する(以降、繊維
素グリコール酸ソーダをNaCMCと略記とする)。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to the use of cellulose IJ as a printing paste for reactive dyes.
'=r-Relating to a method for producing sodium phosphate (hereinafter, cellulose sodium glycolate is abbreviated as NaCMC).
NaCMCは繊維素、カセイソーダ、モノクロル酢酸ソ
ーダと水とを反応させて製造されるものであり、各種の
製造方法が開発され近来捺染用糊料としての需要が増大
している。NaCMC is produced by reacting cellulose, caustic soda, sodium monochloroacetate, and water, and various production methods have been developed, and demand for it as a printing paste has increased in recent years.
しかし、反応性染料の捺染には脱糊性不良のため、実用
化は殆んど不可能であり、今日なお、反応性染料用の捺
染糊料としては、アルギン酸ソーダのみが、殆んど唯一
のもののように用いられている。However, it is almost impossible to put it into practical use when printing reactive dyes due to poor desizing properties, and even today, sodium alginate is almost the only printing paste used for reactive dyes. It is used like something.
本発明者は反応性染料の捺染の糊料とした場合に、すぐ
れた脱糊性を有するNaCMCの製造方法を開発するた
めの研究を行い、本発明を完成した。The present inventor conducted research to develop a method for producing NaCMC, which has excellent desizing properties when used as a thickening agent for printing reactive dyes, and completed the present invention.
すなわち、本発明は繊維素、カセイソーダ、モノクロル
酢酸ソーダ及び水とを反応させてNaCMCを製造する
方法において、反応生成物に晒粉を加えて少量の水を媒
体として固相反応させる工程を含有するものであり、そ
の反応生成物であるNaCMCの25℃における1%水
溶液の相対粘度が5.0以下とすることを特徴とするも
のである。That is, the present invention is a method for producing NaCMC by reacting cellulose, caustic soda, sodium monochloroacetate, and water, which includes a step of adding bleaching powder to the reaction product and performing a solid phase reaction using a small amount of water as a medium. It is characterized in that the relative viscosity of a 1% aqueous solution of the reaction product NaCMC at 25° C. is 5.0 or less.
固相反応を行う反応生成物は食塩、グリコール酸ソーダ
、カセイソーダ、炭酸ソーダ等の塩類、残存遊離アルカ
リ等を含有する膨潤粗製NaCMC1或は精製NaCM
Cのいずれでもよく、さらに製造工程の初期に繊維素と
カセイソーダとを混合して苛烈な条件で熟成后、エーテ
ル化し本発明の固相反応を行っても目的を達することが
できる。The reaction product of the solid phase reaction is swollen crude NaCMC1 or purified NaCM containing salts such as common salt, sodium glycolate, caustic soda, and soda carbonate, and residual free alkali.
Any of C may be used, and the purpose can also be achieved by mixing cellulose and caustic soda at the beginning of the production process, aging them under severe conditions, and then etherifying them to carry out the solid phase reaction of the present invention.
さて、従来NaCMCの反応性染料の捺染適性の改善に
ついては、殆んど注目すべき研究報告はなかったが、近
年本発明者のNaCMCの晒粉による酸化に関連するも
のとしてつぎの2.3の文献がある。Now, in the past, there have been almost no noteworthy research reports regarding the improvement of the printing suitability of reactive dyes of NaCMC, but in recent years, the following 2.3 studies have been made related to the oxidation of NaCMC by bleaching powder by the present inventor. There is a literature on this.
即ち(1)M、Kamelら、Tex、Res、J、4
15.450−4 1971 : AmericanD
yestuff Reporter 64 (3)
、22.24−51975、(2)A、 K 、Nar
karら、Tex、Dyer &p rinter、9
.1.41−4 1975、(3)高頭正元ら、日本特
許出願公告、昭53−1876などである。Namely (1) M. Kamel et al. Tex. Res. J. 4
15.450-4 1971: AmericanD
yestuff Reporter 64 (3)
, 22.24-51975, (2) A, K, Nar
Kar et al., Tex, Dyer & Printer, 9
.. 1.41-4 1975, (3) Masamoto Takato et al., Japanese Patent Application Publication, 1982-1876, etc.
上記(1)、(2)の方法はNa0C1水溶液による酸
化であるが、これらの酸化系はいずれも多量の水を含有
するので、NaCMCは水に溶けて粘稠な糊液を形成し
、酸化反応はすべて液相で行なわれ、また(3)の方法
は媒体として水を用いず、特に高濃度(80%以上)の
アルコールを用いるものである。Methods (1) and (2) above involve oxidation using an aqueous Na0C1 solution, but since both of these oxidation systems contain a large amount of water, NaCMC dissolves in water to form a viscous paste liquid and is oxidized. All reactions are carried out in a liquid phase, and method (3) does not use water as a medium, but uses particularly high concentration (80% or more) alcohol.
なお、上記(3)の文献には媒体として水のみを用いた
場合にはCMCの分子内の結合が酸化剤により、切断さ
れるという記載があるが、これらはあきらかに多量の水
が存在する所謂液相反応についての現象をのべているも
のであって、本発明の少量の水の存在する固相反応に関
するものではなく、工業的に最も緊要な酸化反応条件と
生成物の捺染適性との相互関係に就いては一切の記述は
なく、従って過去いずれの文献からも、今日未だ上記の
最も緊要な課題は全く不明である。Note that the above document (3) states that when only water is used as a medium, the bonds within the CMC molecules are broken by an oxidizing agent, but these clearly indicate that a large amount of water is present. It describes the phenomenon of the so-called liquid phase reaction, and does not relate to the solid phase reaction of the present invention in which a small amount of water is present, but rather describes the oxidation reaction conditions and the printing suitability of the product, which are the most important industrially. There is no description of the interrelationship between the two, and therefore, the most important issue mentioned above is still completely unclear from any past literature.
しかるに本発明の方法は、その上記課題の好適条件とし
ては、反応媒体としては単に少量の水を用いるに止まり
、前記(1)、(2)のようなNaCMCの粘稠な糊液
としての液相酸化ではなく固相の酸化反応であり、又(
3)のような特異な反応媒体を用いる異質の酸化反応で
もなく、また目的の脱糊性に必要な酸化度を系統的な研
究の結果、酸化石の生成物の粘度的見地からあきらかに
したもので、上記すべての引用文献の方法とは本質的に
全く異なり、薬品経済上置も有利な、かつ工業的応用操
作の最も簡便な方法である。However, the method of the present invention requires only a small amount of water to be used as the reaction medium, and a viscous paste solution of NaCMC as described in (1) and (2) above. It is not a phase oxidation reaction but a solid phase oxidation reaction, and (
It is not a heterogeneous oxidation reaction using a unique reaction medium as in 3), and the degree of oxidation necessary for the desired desizing property was clarified from the viewpoint of the viscosity of the oxide stone product as a result of systematic research. This method is essentially completely different from the methods described in all of the above-mentioned documents, is advantageous from a pharmacoeconomic standpoint, and is the simplest method for industrial application.
本発明の内容をさらに詳しくのべると、晒粉による固相
酸化反応を一般的なNaCMCの製造法に適用すること
によりふつうに製造されたNaCMCをとくに脱糊性に
すぐれた反応性染料の捺染糊料に改質することができる
。To describe the content of the present invention in more detail, NaCMC, which is normally produced by applying a solid-phase oxidation reaction using bleaching powder to a general NaCMC production method, is used as a printing paste of a reactive dye that has particularly excellent desizing properties. It can be reformed into raw materials.
また添加する晒粉の量は上記のようにNaCMCの25
℃における1%水溶液の相対粘度を、5.0以下とする
ような量を用いることが不可欠の条件である。Also, the amount of bleaching powder to be added is 25% of NaCMC as described above.
An essential condition is to use an amount such that the relative viscosity of a 1% aqueous solution at °C is 5.0 or less.
さらに具体的にのべるとNaCMCに対して、普通有効
塩素量として1%〜5%の晒粉を用いて酸化する方法で
ある。More specifically, it is a method of oxidizing NaCMC using bleaching powder with an amount of 1% to 5% of available chlorine.
なお固相反応は通常のNaCMC製造の反応末期、食塩
、グリコール酸ソーダ、カセイソーダ、炭酸ソーダ等の
塩類、残存遊離アルカリ等を含有するまSの膨潤粗製繊
維素グリコール酸ソーダについて、或はさらに、これを
精製した後のNaCMCのいずれに適用してもその目的
を達することができる。In addition, the solid phase reaction is performed at the final stage of the normal NaCMC production, for the swollen crude cellulose sodium glycolate containing salts such as common salt, sodium glycolate, caustic soda, and soda carbonate, and residual free alkali, or in addition, The purpose can be achieved by applying this to any NaCMC after purification.
またNaCMCの製造初期に於てアルカリ繊維素の熟成
を特に苛烈な条件で行った場合には所要晒粉の量を相当
程度(例えば半量)節約することができる。Furthermore, if the alkali cellulose is aged under particularly severe conditions in the early stages of NaCMC production, the amount of bleaching powder required can be reduced to a considerable extent (for example, by half).
ただし、単なる熟成操作のみではこれをいかに苛酷に行
って生成物の粘度を既定の粘度以下に低下させても、目
的の満足な捺染適性は得られず、目的の捺染用糊料製造
法としては、晒粉による固相酸化は絶対不入の条件であ
る。However, no matter how severe the aging process is to reduce the viscosity of the product to a predetermined viscosity or less, the desired printing suitability cannot be obtained, and the desired printing paste production method cannot be achieved. , solid phase oxidation by bleaching is an absolute must.
本発明の特徴をまとめると次の如くになる。The features of the present invention can be summarized as follows.
■、すでに述べたように、反応性染料の捺染糊料として
、その脱糊性の立場から、酸化反応后の生成物の水溶液
の相対粘度をNaCMCとしての1.0%濃度、25℃
で5.0以下にまで低下さすことが、最も重要不可欠な
条件であることを確認、究明したこと。(2) As mentioned above, from the standpoint of desizing properties of reactive dyes as printing pastes, the relative viscosity of the aqueous solution of the product after oxidation reaction is 1.0% concentration as NaCMC, 25°C.
It has been confirmed and investigated that the most important and essential condition is to reduce the value to 5.0 or less.
2、酸化剤として比較的安価な晒粉(次亜塩素酸のCa
塩)を用いること。2. Relatively inexpensive bleaching powder (hypochlorous acid Ca) as an oxidizing agent
salt).
この酸化反応は常温で行われるが、晒粉はおよそ35℃
以下の常温では自己分解をほとんど起さず、したがって
使用の全晒粉が反応に使用される。This oxidation reaction takes place at room temperature, but bleached powder is approximately 35°C.
Self-decomposition hardly occurs at room temperature below, so all bleached powder used is used in the reaction.
ゆえにNaCMCの晒粉水溶液による粘度低下は他の諸
条件よりも事実上NaCMCに対する晒粉使用量ともつ
とも密接な関係がある。Therefore, the viscosity reduction caused by the aqueous bleaching powder solution of NaCMC is actually more closely related to the amount of bleaching powder used for NaCMC than other conditions.
したがって前記の粘度低下は主として晒粉のみによって
簡単に調節することができる。Therefore, the above-mentioned viscosity reduction can be easily controlled mainly by bleaching alone.
3、酸化反応の媒体として有機溶剤などを用いず、少量
の水を用いて固相反応させること。3. Do not use an organic solvent or the like as a medium for the oxidation reaction, but use a small amount of water to carry out the solid phase reaction.
したがって湿潤微粉末やパン屑様の膨潤繊維状態のまま
で反応を完結できるので、そのまま実用に供することが
できる。Therefore, the reaction can be completed in the state of wet fine powder or swollen fibers like bread crumbs, so it can be put to practical use as it is.
酸化反応条件についてはpH等に限定されず一般に常温
でかつ通常2〜3時間の短時間で完結できる。The oxidation reaction conditions are not limited to pH, etc., and can generally be completed at room temperature in a short time of 2 to 3 hours.
次に本発明を実施例、比較例にもとづいて説明する。Next, the present invention will be explained based on Examples and Comparative Examples.
本実施例、比較例においての目的の捺染適性の標準試験
方法としては、すべて色糊として、反応性染料レマゾー
ルブラックB(ヘキスト社製)5%、基糊60%(これ
は試料の粘度に対応してそれぞれ記載濃度で調製)、尿
素5%、炭酸ソーダ1%、水29%(計100%)の組
成のものを用い、レーヨンおよび綿布のスクリーン捺染
を行ない、いずれも同一条件で風乾、蒸熱後、またそれ
ぞれ基準の方法で(風乾後の染布を室温10〜25℃の
水中に約15分浸漬後、さらに約20分を要して染布を
上下左右に計320回宛静かに動かす)、水洗後の染布
の脱糊性、風合い、色相などを肉眼的に、或いは徒手に
よる触感から比較判定した。The standard test method for printing suitability for the purposes of these Examples and Comparative Examples was to use 5% reactive dye Remazol Black B (manufactured by Hoechst) as color paste, and 60% base paste (depending on the viscosity of the sample). Rayon and cotton fabrics were screen-printed using a composition of 5% urea, 1% soda carbonate, and 29% water (total 100%), prepared at the respective concentrations listed, and air-dried under the same conditions. After steaming and using the standard method (air-dried), the dyed fabric is immersed in water at a room temperature of 10 to 25°C for about 15 minutes, and it takes about 20 minutes to gently shake the dyed fabric up and down and left and right a total of 320 times. The desizing properties, texture, hue, etc. of the dyed fabrics after washing were compared visually and by hand.
たgし、色相その他に殆んど差異を認めなかったので、
捺染適性の評定はすべて単に脱糊性のみを対象として記
入した。There was almost no difference in hue or anything else, so
All evaluations of suitability for printing were made based solely on desizing properties.
捺染成績×印は不良、○印は優良、Dは○と×の中間程
度、2個印のものはその両者の中間程度を示す。Printing results marked with an x mark indicate poor quality, a mark with an ○ mark indicates an excellent quality, a mark D indicates an intermediate level between ○ and an x mark, and a printing result with two marks indicates an intermediate level between the two.
なお捺染成績○印と記入したものは、いずれも対照とし
て平行に試験したアルギン酸ソーダに比較して、その脱
糊性が少くとも同等以上であり、かつ色調その他の一般
捺染効果にもなんらの差異のないことを基準として判定
したものであ※る。Printing results marked with a circle indicate that the desizing property is at least equivalent to or better than that of sodium alginate, which was tested in parallel as a control, and that there is no difference in color tone or other general printing effects. The judgment was based on the absence of *.
実施例、比較例1
製法の異る3種の精製NaCMC粉末を用い晒粉の添加
量を種々変えて、常温2時間の固相反応を行わせた。Examples, Comparative Example 1 Using three types of purified NaCMC powders with different manufacturing methods and varying the amount of bleaching powder added, a solid phase reaction was performed at room temperature for 2 hours.
この酸化には有効塩素濃度29.2グ/lの晒粉水溶液
を用いた。For this oxidation, a bleached powder aqueous solution with an available chlorine concentration of 29.2 g/l was used.
NaCMC粉末は/161〜5はモノクロル酢酸ソーダ
法−硫酸精製法によるもの、屑6〜11はモノクロル酢
酸ソーダ法−メタノール精製法によるもの、412〜1
5はアルセル法−メタノール精製法によるものであり、
それぞれの平均エーテル化度(DS)は0.73.0.
62.0.92である。NaCMC powder /161-5 is obtained by monochlorosodium acetate method-sulfuric acid purification method, scraps 6-11 are obtained by monochlorosodium acetate method-methanol purification method, 412-1
5 is based on the Arcel method-methanol purification method,
The average degree of etherification (DS) of each is 0.73.0.
62.0.92.
固相酸化条件、生成NaCMCの相対粘度、及び捺染試
験結果を第1表に示す。Table 1 shows the solid phase oxidation conditions, the relative viscosity of the NaCMC produced, and the printing test results.
上記表は糊料の粘度低下に対応して捺染成績が明らかに
向上する傾向のあることを示している。The above table shows that there is a clear tendency for printing performance to improve as the viscosity of the paste decreases.
そしてその好適粘度低下については生成物の粘度(1%
、25℃)が6.5の程度では未だ不充分であり、本実
験例では4.0のようなごく低粘度において、はじめて
目的の反応性染料の捺染に用いた場合の、すぐれた脱糊
性をもつ糊料の得られることがわかる。And for the preferred viscosity reduction, the viscosity of the product (1%
, 25°C) of 6.5 is still insufficient, and in this experimental example, a very low viscosity of 4.0 was used to achieve excellent desizing when used for the first time for printing with the target reactive dye. It can be seen that a paste with properties can be obtained.
本実施例、比較例に用いた精製NaCMCのDSは若干
異るが、第1表はいずれの場合にも、粘度5を変曲点と
して起る、一種の著量な臨界的の現象であると云える。Although the DS of purified NaCMC used in the present example and comparative example is slightly different, Table 1 shows that in both cases, it is a kind of significant critical phenomenon that occurs with the viscosity of 5 as the inflection point. I can say that.
本発明において、晒粉による固相酸化の好適反応条件と
して、生成物の粘度を1%、25℃で5.0以下と規定
せる所以である。This is why, in the present invention, the viscosity of the product can be defined as 1% and 5.0 or less at 25° C. as suitable reaction conditions for solid-phase oxidation using bleaching powder.
実施例、比較例2
二種類の製造方法について、それぞれの反応末期に晒粉
(実施例、比較例1と同条件)を加えて固相酸化を行い
、生成せる塩類、遊離アルカリ等を含む粗製物、及びメ
タノール精製せる精製物についての脱糊性を検討した。Example, Comparative Example 2 For two types of production methods, bleaching powder (same conditions as Example and Comparative Example 1) was added at the end of each reaction to perform solid phase oxidation, resulting in a crude product containing salts, free alkalis, etc. The desizing properties of the purified products obtained by purifying methanol were investigated.
固相酸化条件及び結果を第2表に示す。Solid phase oxidation conditions and results are shown in Table 2.
表において/i61〜5はモノクロル酢酸ソーダ法で、
繊維素のC6基本分子1モル当りモノクロル酢酸ソーダ
1.4モルを用いており、又//66〜9はアルセル法
で、繊維素のC6基本分子1モル当りモノクロル酢酸ソ
ーダ1.7モルを用いた。In the table, /i61-5 is the monochloroacetic acid soda method,
1.4 mol of sodium monochloroacetate is used per mol of C6 basic molecule of cellulose, and 1.7 mol of sodium monochloroacetate is used per mol of C6 basic molecule of cellulose in the Arcel method for //66 to 9. there was.
そして上記はいずれの場合も反応末期に上述の固相酸化
を行った。In each case, the solid phase oxidation described above was performed at the end of the reaction.
第2表によれば添加量に対応して生成物の粘度は低下し
、また捺染適性についての好適粘度としては、粗製物の
メタノール精製後の純NaCMCの1%水溶液25℃で
、6〜70程度では未だ明らかに不充分であり、すぐれ
た脱糊性を確保する条件としては粘度5以下とする程度
の酸化が必要である。According to Table 2, the viscosity of the product decreases in accordance with the amount added, and the preferred viscosity for printing suitability is 6 to 70 ml of a 1% aqueous solution of pure NaCMC after methanol purification of the crude product at 25°C. The degree of oxidation is still clearly insufficient, and the condition for ensuring excellent desizing properties requires oxidation to a degree that the viscosity is 5 or less.
また脱糊性を粗製物と精製物とについて比較すると、後
者の方が幾分優位性も認められるが、一般的にいへば粗
製、精製の別なく、脱糊性はきわめて優秀であり、従っ
て一般に晒粉酸化後のNaCMCは必ずしもこれを精製
する必要はない。Also, when comparing the desizing properties of the crude product and the purified product, the latter is seen to be somewhat superior, but in general, regardless of whether it is crude or purified, the desizing properties are extremely excellent. Therefore, it is generally not necessary to purify NaCMC after bleaching and oxidation.
実施例、比較例3
NaCMC製造工程の初期にアルカリ繊維素の熟成を特
に苛烈な条件で行った場合の本発明の効果を調べた。Example, Comparative Example 3 The effect of the present invention was investigated when the alkali cellulose was aged under particularly harsh conditions at the beginning of the NaCMC manufacturing process.
その結果を第3表に示す。実験/161〜5はアルカリ
繊維素の熟成のみを行い晒粉処理を行わなかった場合、
/f66〜9は熟成を行い、かつ晒糊処理も行った場合
を示す。The results are shown in Table 3. In Experiment/161-5, when only the alkali cellulose was aged and no bleaching treatment was performed,
/f66-9 indicates the case where aging was performed and bleaching process was also performed.
/161〜5に示す如く、熟成の程度を増大するとNa
CMCの相対粘度は低下するが、いくら低下しても脱糊
性は改善されない。/161-5, as the degree of ripening increases, Na
Although the relative viscosity of CMC is reduced, no matter how much it is reduced, the desizing properties are not improved.
しかし/166〜9が示すように苛烈な熟成と晒粉処理
とを組合わせれば、晒糊量を相当量節減しうろことがわ
かる。However, as shown in /166-9, if severe aging and bleaching treatment are combined, the amount of bleaching paste can be reduced by a considerable amount.
Claims (1)
水を反応させて繊維素グリコール酸ソーダを製造する方
法に於て、 反応生成物を少量の水を媒体として晒粉で固相酸化処理
を行い、処理后の生成物の繊維素グリコール酸ソーダの
25℃における1%水溶液の相対粘度を5.0以下とす
ることを特徴とする固相反応による反応性染料用捺染糊
料製造方法。 2 反応生成物は膨潤粗製繊維素グリコール酸ソーダで
ある特許請求の範囲第1項の製造方法。 3 反応生成物は精製縁、維素グリコール酸ソーダであ
る特許請求の範囲第1項の製造方法。 4 繊維素、カセイソーダ、モノクロル酢酸ソーダと水
とを反応させる方法において、まず繊維素とカセイソー
ダとを混合して苛烈な条件で熟成后、エーテル化する工
程を含む特許請求の範囲第1項の製造方法。[Claims] 1. In a method for producing cellulose sodium glycolate by reacting cellulose, caustic soda, sodium monochloroacetate, and water, the reaction product is subjected to solid-phase oxidation with bleaching powder using a small amount of water as a medium. A method for producing a printing paste for reactive dyes by a solid-phase reaction, characterized in that the relative viscosity of a 1% aqueous solution of sodium cellulose glycolate at 25° C. after the treatment is 5.0 or less. . 2. The manufacturing method according to claim 1, wherein the reaction product is swollen crude cellulose sodium glycolate. 3. The manufacturing method according to claim 1, wherein the reaction product is refined edible fibers and sodium glycolate. 4. The method of reacting cellulose, caustic soda, sodium monochloroacetate, and water, which includes the step of first mixing cellulose and caustic soda, aging them under harsh conditions, and then etherifying them. Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54046600A JPS5831081B2 (en) | 1979-04-18 | 1979-04-18 | Method for producing printing paste for reactive dyes by solid-phase reaction |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54046600A JPS5831081B2 (en) | 1979-04-18 | 1979-04-18 | Method for producing printing paste for reactive dyes by solid-phase reaction |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS55152702A JPS55152702A (en) | 1980-11-28 |
| JPS5831081B2 true JPS5831081B2 (en) | 1983-07-04 |
Family
ID=12751784
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP54046600A Expired JPS5831081B2 (en) | 1979-04-18 | 1979-04-18 | Method for producing printing paste for reactive dyes by solid-phase reaction |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5831081B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS531876A (en) * | 1976-06-29 | 1978-01-10 | Yamamoto Electric Ind Co Ltd | Construction of switch case |
-
1979
- 1979-04-18 JP JP54046600A patent/JPS5831081B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS55152702A (en) | 1980-11-28 |
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