JPS632256B2 - - Google Patents
Info
- Publication number
- JPS632256B2 JPS632256B2 JP12377080A JP12377080A JPS632256B2 JP S632256 B2 JPS632256 B2 JP S632256B2 JP 12377080 A JP12377080 A JP 12377080A JP 12377080 A JP12377080 A JP 12377080A JP S632256 B2 JPS632256 B2 JP S632256B2
- Authority
- JP
- Japan
- Prior art keywords
- acid
- reaction
- temperature
- metadiaminobenzene
- water
- 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
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- WZCQRUWWHSTZEM-UHFFFAOYSA-N 1,3-phenylenediamine Chemical compound NC1=CC=CC(N)=C1 WZCQRUWWHSTZEM-UHFFFAOYSA-N 0.000 claims description 14
- 238000006277 sulfonation reaction Methods 0.000 claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 239000000203 mixture Substances 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 6
- JVMSQRAXNZPDHF-UHFFFAOYSA-N 2,4-diaminobenzenesulfonic acid Chemical compound NC1=CC=C(S(O)(=O)=O)C(N)=C1 JVMSQRAXNZPDHF-UHFFFAOYSA-N 0.000 claims description 5
- 239000002253 acid Substances 0.000 description 27
- 238000006243 chemical reaction Methods 0.000 description 25
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 16
- 238000000034 method Methods 0.000 description 7
- 239000013078 crystal Substances 0.000 description 6
- 239000006227 byproduct Substances 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- GEYOCULIXLDCMW-UHFFFAOYSA-N 1,2-phenylenediamine Chemical compound NC1=CC=CC=C1N GEYOCULIXLDCMW-UHFFFAOYSA-N 0.000 description 3
- KEQGZUUPPQEDPF-UHFFFAOYSA-N 1,3-dichloro-5,5-dimethylimidazolidine-2,4-dione Chemical compound CC1(C)N(Cl)C(=O)N(Cl)C1=O KEQGZUUPPQEDPF-UHFFFAOYSA-N 0.000 description 3
- XTHPWXDJESJLNJ-UHFFFAOYSA-N chlorosulfonic acid Substances OS(Cl)(=O)=O XTHPWXDJESJLNJ-UHFFFAOYSA-N 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000004128 high performance liquid chromatography Methods 0.000 description 2
- 239000005457 ice water Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- UGEHFOSBNBEWMP-UHFFFAOYSA-N 2,3-diaminobenzenesulfonic acid Chemical compound NC1=CC=CC(S(O)(=O)=O)=C1N UGEHFOSBNBEWMP-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- VYZAHLCBVHPDDF-UHFFFAOYSA-N Dinitrochlorobenzene Chemical compound [O-][N+](=O)C1=CC=C(Cl)C([N+]([O-])=O)=C1 VYZAHLCBVHPDDF-UHFFFAOYSA-N 0.000 description 1
- OLKQHKAXAXIAAT-UHFFFAOYSA-N NC1(C(C=CC(=C1)N)S(=O)(=O)O)S(=O)(=O)O Chemical compound NC1(C(C=CC(=C1)N)S(=O)(=O)O)S(=O)(=O)O OLKQHKAXAXIAAT-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000006326 desulfonation Effects 0.000 description 1
- 238000005869 desulfonation reaction Methods 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 239000012456 homogeneous solution Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 125000000449 nitro group Chemical group [O-][N+](*)=O 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 125000000542 sulfonic acid group Chemical group 0.000 description 1
- HIFJUMGIHIZEPX-UHFFFAOYSA-N sulfuric acid;sulfur trioxide Chemical compound O=S(=O)=O.OS(O)(=O)=O HIFJUMGIHIZEPX-UHFFFAOYSA-N 0.000 description 1
- 238000004809 thin layer chromatography Methods 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
【発明の詳細な説明】
本発明は2・4−ジアミノベンゼンスルホン酸
の製造法に関し、更に詳しくは、メタジアミノベ
ンゼンを直接スルホン化して得られるスルホン化
反応マスに水を加え、120〜150℃に加熱すること
により、副生した2・4−ジアミノベンゼン−
1・5−ジスルホン酸(以下、ジスルホン酸とい
う)を脱モノスルホン化して目的とする2・4−
ジアミノベンゼンスルホン酸(以下、モノスルホ
ン酸という)に転換せしめることからなるモノス
ルホン酸の改良製法である。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing 2,4-diaminobenzenesulfonic acid, and more specifically, water is added to a sulfonation reaction mass obtained by direct sulfonation of metadiaminobenzene, 2,4-diaminobenzene produced as a by-product by heating to
1,5-disulfonic acid (hereinafter referred to as disulfonic acid) is demonosulfonated to obtain the desired 2,4-
This is an improved method for producing monosulfonic acid, which involves converting it into diaminobenzenesulfonic acid (hereinafter referred to as monosulfonic acid).
従来、モノスルホン酸の製造法としては2・4
−ジニトロクロルベンゼンを原料として、亜硫酸
塩でクロル基をスルホン酸基に変え、ついでニト
ロ基を還元する方法がよく知られているが、この
方法では高純度品が得られるものの反応工程が長
く、また有機溶媒を使用するため廃液処理にも
種々の困難がある等の欠点があつた。 Conventionally, the manufacturing method for monosulfonic acid is 2.4.
- A well-known method is to use dinitrochlorobenzene as a raw material, convert the chloro group into a sulfonic acid group with sulfite, and then reduce the nitro group. Although this method yields a highly pure product, the reaction process is long; Furthermore, since an organic solvent is used, there are various difficulties in waste liquid treatment.
また、メタジアミノベンゼンを発煙硫酸等によ
り直接スルホン化する方法も知られている。この
方法は反応工程も短かく、操作的には前者よりも
有利であるが、モノスルホン化と同時にジスルホ
ン化もおこり、反応物は両者の混合物となり、ジ
スルホン化を抑えるために反応条件を弱くすると
反応が十分に進行せずにモノスルホン酸の収量が
減少するのみならず、ジスルホン化をなくすこと
もできない。また、このようにして得られたモノ
およびジスルホン酸混合物より両者を分離し、精
製することは装置的、操作的にも容易でなく、工
業的に実施するには不利である。 Also known is a method of directly sulfonating metadiaminobenzene with fuming sulfuric acid or the like. This method has shorter reaction steps and is more operationally advantageous than the former, but disulfonation also occurs at the same time as monosulfonation, and the reactant is a mixture of both, so if the reaction conditions are weakened to suppress disulfonation, Not only does the reaction not proceed sufficiently, resulting in a decrease in the yield of monosulfonic acid, but also disulfonation cannot be eliminated. In addition, it is not easy to separate and purify the mono- and disulfonic acid mixture obtained in this way both in terms of equipment and operation, and it is disadvantageous for industrial implementation.
本発明者は、工業的に有利なモノスルホン酸の
製造法について種々検討したが、メタジアミノベ
ンゼンの直接スルホン化方法において、スルホン
化反応マスより副生ジスルホン酸を目的物である
モノスルホン酸に転換し得れば極めて有利な製造
法となり得ることに着目し、更に検討の結果、ジ
スルホン酸はメタジアミノベンゼンの直接スルホ
ン化における反応の初期から副生しはじめ、反応
原料が殆んど消失する反応終了時には約30%に達
する量が生成するが、かかるスルホン化反応マス
に水を加え、120〜150℃に加熱することによりジ
スルホン酸の脱モノスルホン化がおこり、ジスル
ホン酸をモノスルホン酸に変換し得ることを見出
し、本発明に至つた。 The present inventor has investigated various industrially advantageous methods for producing monosulfonic acid, and in the direct sulfonation method of metadiaminobenzene, the by-product disulfonic acid is converted to the target monosulfonic acid from the sulfonation reaction mass. Noting that it could be an extremely advantageous production method if it could be converted, further study revealed that disulfonic acid begins to be produced as a by-product from the early stage of the reaction in the direct sulfonation of metadiaminobenzene, and most of the reaction raw materials disappear. At the end of the reaction, an amount reaching approximately 30% is produced, but by adding water to the sulfonated reaction mass and heating it to 120-150°C, demonosulfonation of disulfonic acid occurs, converting disulfonic acid to monosulfonic acid. It has been discovered that this can be converted, leading to the present invention.
すなわち本発明は、メタジアミノベンゼンのス
ルホン化反応マスに水を加え、120〜150℃に保温
することからなるモノスルホン酸の製造法であ
る。 That is, the present invention is a method for producing monosulfonic acid, which comprises adding water to a sulfonation reaction mass of metadiaminobenzene and keeping the mixture at a temperature of 120 to 150°C.
本発明によれば、副生したジスルホン基のうち
の1つが脱離して目的物であるモノスルホン酸と
なり、その結果反応マス中のジスルホン酸量が減
少し、モノスルホン酸量が増加して90%を越える
好収率が得られる。 According to the present invention, one of the by-produced disulfonic groups is eliminated and becomes the target monosulfonic acid, and as a result, the amount of disulfonic acid in the reaction mass decreases, and the amount of monosulfonic acid increases. Good yields exceeding % can be obtained.
以下、本発明を詳しく説明する。 The present invention will be explained in detail below.
本発明でいうスルホン化反応マスはジアミノベ
ンゼンの直接スルホン化反応により得られるもの
を指すが、該スルホン化反応を実施するにあた
り、ジアミノベンゼンは98〜100%硫酸に予め溶
解しておくのがよく、この際使用する硫酸量はジ
アミノベンゼンに対して5重量倍以上であること
が好ましい。 In the present invention, the sulfonation reaction mass refers to the mass obtained by direct sulfonation reaction of diaminobenzene, but when carrying out the sulfonation reaction, it is preferable to dissolve diaminobenzene in 98 to 100% sulfuric acid in advance. In this case, the amount of sulfuric acid used is preferably at least 5 times the weight of diaminobenzene.
スルホン化剤としては各種濃度の発煙硫酸、ク
ロルスルホン酸などが使用できるが、発煙硫酸を
使用する場合に低濃度発煙硫酸では使用量が多く
なり、また排出する廃酸が著しく多くなるので不
利となる等のことから、65%発煙硫酸を使用する
のが好ましい。 As a sulfonating agent, various concentrations of oleum, chlorosulfonic acid, etc. can be used, but when using oleum, a low concentration of oleum is disadvantageous because it requires a large amount of use and a significant amount of waste acid is emitted. For this reason, it is preferable to use 65% oleum.
その他、反応温度、反応時間等の諸反応条件に
ついても従来公知の方法で実施される。 In addition, various reaction conditions such as reaction temperature and reaction time are carried out using conventionally known methods.
かくして得られた反応マスに水を加えて脱モノ
スルホン化を行うが、水の添加により激しい発熱
がみられるので、通常はあらかじめ該反応マスを
結晶が析出しない程度の130〜140℃程度にまで冷
却したのち、ゆつくりと水を加える。 Demonosulfonation is carried out by adding water to the reaction mass obtained in this way, but since the addition of water causes severe heat generation, the reaction mass is usually heated in advance to a temperature of about 130 to 140°C, which is the temperature at which crystals do not precipitate. After cooling, slowly add water.
反応マスに加える水の量は、反応マス中の硫酸
濃度が60〜90%、好ましくは70〜85%になる量で
ある。 The amount of water added to the reaction mass is such that the sulfuric acid concentration in the reaction mass is 60-90%, preferably 70-85%.
脱モノスルホン化温度は120〜150℃の範囲が好
ましい。これより低温では反応物の結晶化を生
じ、反応が極めて遅くなつてジスルホン酸が残存
し、一方これより高温では一部分解が起こり、収
率が低下する傾向がある。上記温度で所定時間保
温することにより脱モノスルホン化反応は完了す
るが、その後反応マスに更に水を加えて硫酸濃度
を下げ、冷却することにより目的とするモノスル
ホン酸を結晶として得ることができる。 The demonosulfonation temperature is preferably in the range of 120 to 150°C. At temperatures lower than this, crystallization of the reactants occurs and the reaction becomes extremely slow and disulfonic acid remains, while at temperatures higher than this, partial decomposition occurs and the yield tends to decrease. The demonosulfonation reaction is completed by keeping the temperature at the above temperature for a predetermined period of time, but after that, water is further added to the reaction mass to lower the sulfuric acid concentration, and by cooling, the desired monosulfonic acid can be obtained as crystals. .
かくして得られたモノスルホン酸中にはもはや
ジスルホン酸は殆んど含まれず、非常に高純度で
ある。 The monosulfonic acid thus obtained contains almost no disulfonic acid and has extremely high purity.
以下、本発明を実施例により説明する。 Hereinafter, the present invention will be explained by examples.
実施例 1
100%硫酸660gを仕込んだ1四ツ口フラスコ
にメタジアミノベンゼン108gを100℃以下で約1
時間も要して加えた。Example 1 108 g of metadiaminobenzene was added to a 14-necked flask containing 660 g of 100% sulfuric acid at a temperature below 100°C.
It took some time to add it.
これに65%発煙硫酸155gを100℃で10分間かか
つて加え、あと1時間要して155℃迄昇温する。 Add 155 g of 65% oleum at 100°C for 10 minutes, and then raise the temperature to 155°C over another hour.
5時間この温度に保温してスルホン化反応を終
える。 The sulfonation reaction is completed by keeping the temperature at this temperature for 5 hours.
反応終了後放冷し、内容物の温度が130〜135゜
になつたところで200gの水を1時間かけて注入
する。この間空冷しながら140℃に保つようにす
る。 After the reaction is completed, the mixture is allowed to cool, and when the temperature of the contents reaches 130 to 135°, 200 g of water is poured over 1 hour. During this time, keep it at 140℃ while air cooling.
ついで氷水500gを入れた2ビーカーに上記
反応液を注ぎ、10℃に冷却したのち更にこの温度
にて1時間撹拌し、充分結晶を析出させたのち
過する。 Next, the above reaction solution was poured into two beakers containing 500 g of ice water, cooled to 10°C, and further stirred at this temperature for 1 hour to sufficiently precipitate crystals, and then filtered.
得られた過ケーキは246gあつた。 The obtained overcake weighed 246 g.
高速液体クロマトグラフイーで分析の結果、該
ケーキは2・4−ジアミノベンゼンスルホン酸の
含量は71%、末反応メタジアミノベンゼンの含量
は0.1%以下であり、2・4−ジアミノベンゼン
ジスルホン酸は認められなかつた。2・4−ジア
ミノベンゼンスルホン酸の収率は93%であつた。 As a result of analysis by high performance liquid chromatography, the content of 2,4-diaminobenzenesulfonic acid in the cake was 71%, the content of terminally reacted metadiaminobenzene was 0.1% or less, and the content of 2,4-diaminobenzenedisulfonic acid was 71%. It was not recognized. The yield of 2,4-diaminobenzenesulfonic acid was 93%.
実施例 2
1四ツ口フラスコに100%硫酸660gを仕込ん
だ1四ツ口フラスコに撹拌しながらメタジアミ
ノベンゼン108gを約1時間を要して加えた。こ
の間冷却を行い100℃以上にならない様にした。Example 2 108 g of metadiaminobenzene was added to a 1-4-neck flask containing 660 g of 100% sulfuric acid with stirring over a period of about 1 hour. During this time, it was cooled to prevent the temperature from exceeding 100°C.
これにクロルスルホン酸150gを100℃より加え
はじめ、2時間を要して145℃まで昇温し、この
間に滴下を終えるようにする。このあと145℃に
2時間保温、撹拌してスルホン化反応を終了す
る。 Add 150 g of chlorosulfonic acid to this mixture starting at 100°C, and the temperature will rise to 145°C over 2 hours, during which time the dropwise addition will be completed. Thereafter, the mixture was kept at 145°C for 2 hours and stirred to complete the sulfonation reaction.
その後内容物を徐冷し、135〜140℃になつたと
ころで200gの水を1時間かけて加える。この間
発熱するが140℃を保つように冷却を行い、同温
度で1時間保温する。この時点で反応液の一部を
薄層クロマトグラフイーで観察すると副生ジスル
ホン酸が消失していることがわかる。ついで氷水
500gを入れた2ビーカーに上で反応液を注ぎ、
10℃迄冷却したのち1時間撹拌し、析出晶を過
する。得られた湿ケーキは230gであり、高速液
体クロマトグラフイーで分析の結果2・4−ジア
ミノベンゼンスルホン酸の含量は73.5%、メタジ
アミノベンゼンの含量は0.1%以下であり、2・
4−ジアミノベンゼンジスルホン酸は検出されな
かつた。 Thereafter, the contents were slowly cooled, and when the temperature reached 135-140°C, 200 g of water was added over 1 hour. During this time, it will generate heat, but it will be cooled to maintain it at 140℃ and kept at that temperature for 1 hour. At this point, when a part of the reaction solution is observed by thin layer chromatography, it is found that the by-product disulfonic acid has disappeared. Then ice water
Pour the reaction solution into 2 beakers containing 500g,
After cooling to 10°C, stir for 1 hour and filter out the precipitated crystals. The obtained wet cake weighed 230 g, and as a result of analysis by high performance liquid chromatography, the content of 2,4-diaminobenzenesulfonic acid was 73.5%, the content of metadiaminobenzene was less than 0.1%, and the content of 2.
4-diaminobenzenedisulfonic acid was not detected.
比較例 1
1四ツ口フラスコに100%硫酸を660g仕込ん
だ1四ツ口フラスコに、メタジアミノベンゼン
108gを100℃以下で約1時間で加える。これにク
ロルスルホン酸155gを実施例2と同じようにし
て加え、同温度、同時間反応させてスルホン化反
応を行つた。Comparative Example 1 Metadiaminobenzene was added to a four-necked flask containing 660g of 100% sulfuric acid.
Add 108g in about 1 hour at below 100℃. To this, 155 g of chlorosulfonic acid was added in the same manner as in Example 2, and the reaction was carried out at the same temperature and for the same time to perform a sulfonation reaction.
反応液の一部をサンプリングし、50%硫酸にな
るように水で粉釈したのち、析出する結晶を分析
したところ結晶中の成分はメタジアミノベンゼン
65%、メタジアミノベンゼンジスルホン酸34%と
微量のメタジアミノベンゼンであつた。 After sampling a portion of the reaction solution and pulverizing it with water to make 50% sulfuric acid, the crystals that precipitated were analyzed and found to be metadiaminobenzene.
65%, metadiaminobenzenedisulfonic acid, 34%, and trace amounts of metadiaminobenzene.
反応液に水300mlを加え、同時に110℃迄冷却し
た。スルホン酸の析出がはじまり、内容物が固化
するまでになつた。このあと150℃まで昇温した
が均一な溶液は得られなかつた。3時間保温した
のち結晶を分離、分析したところジスルホン酸を
30%以上含存しており脱スルホン化前と殆んど変
わらなかつた。 300 ml of water was added to the reaction solution, which was simultaneously cooled to 110°C. Sulfonic acid began to precipitate and the contents solidified. After this, the temperature was raised to 150°C, but a homogeneous solution could not be obtained. After keeping it warm for 3 hours, the crystals were separated and analyzed, and disulfonic acid was found.
The content was more than 30%, almost unchanged from before desulfonation.
Claims (1)
に水を加え、120〜150℃に保温することを特徴と
する2・4−ジアミノベンゼンスルホン酸の製造
法。1. A method for producing 2,4-diaminobenzenesulfonic acid, which comprises adding water to a sulfonation reaction mass of metadiaminobenzene and keeping the mixture at a temperature of 120 to 150°C.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12377080A JPS5748961A (en) | 1980-09-05 | 1980-09-05 | Preparation of 2,4-diaminobenzenesulfonic acid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12377080A JPS5748961A (en) | 1980-09-05 | 1980-09-05 | Preparation of 2,4-diaminobenzenesulfonic acid |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5748961A JPS5748961A (en) | 1982-03-20 |
JPS632256B2 true JPS632256B2 (en) | 1988-01-18 |
Family
ID=14868843
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12377080A Granted JPS5748961A (en) | 1980-09-05 | 1980-09-05 | Preparation of 2,4-diaminobenzenesulfonic acid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5748961A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05117313A (en) * | 1990-03-08 | 1993-05-14 | Basf Ag | Process for manufacturing stable water/oil emulsion of polymer prepared by hydrolysis of n-vinylamide |
JPH08329634A (en) * | 1995-05-31 | 1996-12-13 | Nec Corp | Magnetic head |
CN100386312C (en) * | 2006-07-18 | 2008-05-07 | 上海世景国际贸易有限公司 | Process for synthesizing 2,4-diamino benzene sulfonic acid and its salt |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10243028A1 (en) * | 2002-09-17 | 2004-03-25 | Bayer Ag | Process for the preparation of isolated 3,4-diaminobenzenesulfonic acid |
CN102516137A (en) * | 2011-12-08 | 2012-06-27 | 江苏远征化工有限公司 | Production method of 2, |
CN103553982A (en) * | 2013-08-22 | 2014-02-05 | 上海鸿源鑫创材料科技有限公司 | Preparation technology of 2,4-diaminobenzenesulfonic acid |
CN108675946A (en) * | 2018-06-21 | 2018-10-19 | 中北大学 | A method of preparing 2,4- diamino benzene sulfonic acids |
-
1980
- 1980-09-05 JP JP12377080A patent/JPS5748961A/en active Granted
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05117313A (en) * | 1990-03-08 | 1993-05-14 | Basf Ag | Process for manufacturing stable water/oil emulsion of polymer prepared by hydrolysis of n-vinylamide |
JPH08329634A (en) * | 1995-05-31 | 1996-12-13 | Nec Corp | Magnetic head |
CN100386312C (en) * | 2006-07-18 | 2008-05-07 | 上海世景国际贸易有限公司 | Process for synthesizing 2,4-diamino benzene sulfonic acid and its salt |
Also Published As
Publication number | Publication date |
---|---|
JPS5748961A (en) | 1982-03-20 |
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