JPH0568403B2 - - Google Patents
Info
- Publication number
- JPH0568403B2 JPH0568403B2 JP61028296A JP2829686A JPH0568403B2 JP H0568403 B2 JPH0568403 B2 JP H0568403B2 JP 61028296 A JP61028296 A JP 61028296A JP 2829686 A JP2829686 A JP 2829686A JP H0568403 B2 JPH0568403 B2 JP H0568403B2
- Authority
- JP
- Japan
- Prior art keywords
- exchange resin
- hydrogen peroxide
- pyridine
- anion exchange
- based anion
- 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 - Fee Related
Links
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 38
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 claims description 29
- 239000003957 anion exchange resin Substances 0.000 claims description 24
- 238000000746 purification Methods 0.000 claims description 17
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims description 13
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 claims description 13
- 238000004519 manufacturing process Methods 0.000 claims description 8
- 239000003729 cation exchange resin Substances 0.000 claims description 7
- 239000003456 ion exchange resin Substances 0.000 claims description 7
- 229920003303 ion-exchange polymer Polymers 0.000 claims description 7
- 125000004076 pyridyl group Chemical group 0.000 claims description 6
- 238000005342 ion exchange Methods 0.000 claims description 3
- 229920000642 polymer Polymers 0.000 claims description 3
- 230000000694 effects Effects 0.000 description 9
- 238000000034 method Methods 0.000 description 8
- 238000000354 decomposition reaction Methods 0.000 description 7
- 238000005259 measurement Methods 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- 229920005989 resin Polymers 0.000 description 4
- 229920001429 chelating resin Polymers 0.000 description 3
- QOSATHPSBFQAML-UHFFFAOYSA-N hydrogen peroxide;hydrate Chemical compound O.OO QOSATHPSBFQAML-UHFFFAOYSA-N 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 150000001450 anions Chemical class 0.000 description 2
- WGQKYBSKWIADBV-UHFFFAOYSA-N benzylamine Chemical compound NCC1=CC=CC=C1 WGQKYBSKWIADBV-UHFFFAOYSA-N 0.000 description 2
- 239000000645 desinfectant Substances 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- -1 poly(styrene-divinylbenzene) Polymers 0.000 description 2
- 229920005990 polystyrene resin Polymers 0.000 description 2
- 125000001453 quaternary ammonium group Chemical group 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- CHRJZRDFSQHIFI-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;styrene Chemical compound C=CC1=CC=CC=C1.C=CC1=CC=CC=C1C=C CHRJZRDFSQHIFI-UHFFFAOYSA-N 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- NDKBVBUGCNGSJJ-UHFFFAOYSA-M benzyltrimethylammonium hydroxide Chemical compound [OH-].C[N+](C)(C)CC1=CC=CC=C1 NDKBVBUGCNGSJJ-UHFFFAOYSA-M 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000012459 cleaning agent Substances 0.000 description 1
- XXBDWLFCJWSEKW-UHFFFAOYSA-N dimethylbenzylamine Chemical compound CN(C)CC1=CC=CC=C1 XXBDWLFCJWSEKW-UHFFFAOYSA-N 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000003505 polymerization initiator Substances 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000011403 purification operation Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 229910001415 sodium ion Inorganic materials 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 235000012431 wafers Nutrition 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Description
〔発明の利用分野〕
本発明は、高純度過酸化水素水の製造方法に関
する。
〔発明の背景〕
過酸化水素水は、酸化剤、漂白剤、殺菌剤、消
毒剤等として、また、重合開始剤や爆薬、燃料等
として工業的に広く用いられている。特に最近で
は、電子工業界に於てシリコンウエフアー等の洗
浄剤として重用されており、特にこの業界では高
純度であることが要求されている。一般に、過酸
化水素水は蒸留等で製造した直後に於ては高純度
であるが、貯蔵中、輸送中に容器の材質が侵され
溶出したり、輸送中の安全確保のため分解防止用
安定剤が添加されていたりすることにより、使用
者に渡るときには各種の不純物が混入されてい
る。上記電子工業用薬剤として用いる場合に於て
は、これらの不純物は製品にさまざまな悪影響を
与えるため、これら不純物を除去するための精製
法がこれまで種々検討されている。過酸化水素水
中の金属イオン、例えばナトリウムイオン等につ
いては、カチオン交換樹脂、例えば交換基として
−SOO3Hを有するポリスチレン系イオン交換樹
脂であるアンバーライトIR−120B(オルガノ(株)社
商品名)等によつて除去することができるが、他
の金属イオンやアニオンについてはこれによつて
は除去不可能であつた。また、アニオン類を除去
する方法としては、例えば第4級アンモニウムポ
リスチレン樹脂〔例えば水酸化トリメチルベンジ
ルアンモニウム(スチレン−ジビニルベンゼン)〕
を用いる精製法がある(Pol.Pat.50982号、U.S.
Pat.3294488号等)が、周知の如く、過酸化水素
はアルカリ性の状態では激しく発泡するため、操
作温度は低温、例えば10℃以下、望ましくは0℃
以下にする必要がある。一方、低温で操作しても
過酸化水素の分解が全くなくなるということはな
く、分解して発生した酸素ガスは精製用樹脂カラ
ムに滞留してカラム精製効果を著しく低下させた
り、全く精製できなくさせたりすることがある。
また、操作温度が上昇したりすれば、過酸化水素
は激しく分解して事故が起こることも当然予想さ
れる。
また、第4級アンモニウムポリスチレン樹脂よ
り弱い塩基性であるアニオン交換樹脂、例えばジ
メチルベンジルアミンポリ(スチレン−ジビニル
ベンゼン)も同様の目的で使用することができる
が、やはり低温で操作しなくてはならないという
欠点が存する。
〔発明の目的〕
本発明は上記した如き状況に鑑みなされたもの
で、より高純度の過酸化水素が容易に且つより安
全に得られる製造方法を提供することを目的とす
る。
〔発明の構成〕
本発明は、ピリジン系アニオン交換樹脂を用い
て精製することを特徴とする、高純度過酸化水素
水の製造法である。
本発明に於て用いられるピリジン系アニオン交
換樹脂としては、イオン交換基として一般式
〔)
[Field of Application of the Invention] The present invention relates to a method for producing high-purity hydrogen peroxide solution. [Background of the Invention] Hydrogen peroxide is widely used industrially as an oxidizing agent, bleaching agent, disinfectant, disinfectant, etc., and as a polymerization initiator, explosive, fuel, etc. Particularly recently, it has been used heavily as a cleaning agent for silicon wafers, etc. in the electronics industry, and in this industry, high purity is particularly required. In general, hydrogen peroxide is highly pure immediately after it is produced by distillation, etc., but during storage and transportation, the material of the container is corroded and eluted, and in order to ensure safety during transportation, it must be stabilized to prevent decomposition. Due to the addition of agents, various impurities are mixed into the product when it reaches the user. When used as chemicals for the electronic industry, these impurities have various adverse effects on the product, so various purification methods have been studied to remove these impurities. For metal ions such as sodium ions in hydrogen peroxide water, use a cation exchange resin such as Amberlite IR-120B (trade name of Organo Co., Ltd.), which is a polystyrene ion exchange resin with -SOO 3 H as an exchange group. However, other metal ions and anions cannot be removed by this method. In addition, methods for removing anions include, for example, quaternary ammonium polystyrene resin [e.g., trimethylbenzylammonium hydroxide (styrene-divinylbenzene)].
There is a purification method using (Pol.Pat.50982, US
Pat. 3294488, etc.), but as is well known, hydrogen peroxide foams violently in alkaline conditions, so the operating temperature is low, e.g. 10°C or lower, preferably 0°C.
It is necessary to do the following. On the other hand, operating at low temperatures does not completely eliminate the decomposition of hydrogen peroxide, and the oxygen gas generated by decomposition remains in the purification resin column, significantly reducing the column purification effect or preventing purification at all. Sometimes I let them do it.
Furthermore, if the operating temperature rises, it is naturally expected that hydrogen peroxide will violently decompose and an accident will occur. Anion exchange resins that are less basic than quaternary ammonium polystyrene resins, such as dimethylbenzylamine poly(styrene-divinylbenzene), can also be used for similar purposes, but they must also be operated at low temperatures. There is a drawback. [Object of the Invention] The present invention was made in view of the above-mentioned situation, and an object thereof is to provide a production method that allows hydrogen peroxide of higher purity to be obtained easily and more safely. [Structure of the Invention] The present invention is a method for producing a high-purity hydrogen peroxide solution, which is characterized by purification using a pyridine-based anion exchange resin. The pyridine-based anion exchange resin used in the present invention has the general formula [) as an ion exchange group.
【化】
(但し、R1〜R4は夫々独立して水素又は炭素数
1〜3のアルキル基を表わす。)で示されるピリ
ジル基又は置換ピリジル基を有するポリマーから
なるイオン交換樹脂が挙げられる。
本発明に係るピリジル基又は置換ピリジル基を
有するポリマーとしては、例えば、式
[Chemical formula] (However, R 1 to R 4 each independently represent hydrogen or an alkyl group having 1 to 3 carbon atoms.) Examples include ion exchange resins made of polymers having a pyridyl group or a substituted pyridyl group represented by: . Examples of the polymer having a pyridyl group or a substituted pyridyl group according to the present invention include the formula
実施例 1
ピリジン系アニオン交換樹脂の過酸化水素水に
よる前処理
ピリジン系アニオン交換樹脂〔広栄化学製
KEX−212〕50gと35%過酸化水素水50mlをビー
カー中各種温度で撹拌処理し、過酸化水素の濃度
変化を測定した。但し、処理温度は20℃、40℃、
60℃とした。測定結果を第1図に示す。
第1図より明らかな如く、該イオン交換樹脂の
前処理は低温でも行なえるが、加温すればより短
時間で処理できるし、また処理後の樹脂は過酸化
水素の分解を促進することが殆どないことが判
る。
実施例 2
実施例1の方法に準じて40℃で12時間前処理し
た本発明に係るピリジン系アニオン交換樹脂(2
種)と他のアニオン交換樹脂(3種)を用いて
夫々過酸化水素水を精製し、過酸化水素の安定性
及び精製効果を比較した。
<方法>
イオン交換樹脂各100mlを夫々カラム(24mmφ
×110cm)につめ、これを用いて過酸化水素水の
精製を行なつた。
処理条件及び結果を表1に示す。
Example 1 Pretreatment of pyridine-based anion exchange resin with hydrogen peroxide solution Pyridine-based anion exchange resin [manufactured by Koei Chemical Co., Ltd.]
50 g of KEX-212] and 50 ml of 35% hydrogen peroxide solution were stirred at various temperatures in a beaker, and changes in the concentration of hydrogen peroxide were measured. However, the processing temperature is 20℃, 40℃,
The temperature was 60℃. The measurement results are shown in Figure 1. As is clear from Figure 1, the pretreatment of the ion exchange resin can be carried out at low temperatures, but it can be done in a shorter time if heated, and the resin after treatment can accelerate the decomposition of hydrogen peroxide. It turns out that there are hardly any. Example 2 Pyridine-based anion exchange resin (2
hydrogen peroxide solution was purified using each of the following anion exchange resins (species) and other anion exchange resins (three types), and the stability and purification effect of hydrogen peroxide were compared. <Method> Add 100 ml of each ion exchange resin to each column (24 mmφ
x 110cm) and used this to purify the hydrogen peroxide solution. The treatment conditions and results are shown in Table 1.
【表】
*過酸化水素分解のため樹脂が浮き上がり正常
なカラム精製操作ができない。
表1に示される如く、強塩基性アニオン交換樹
脂による精製は低温(5℃)でも不可能であり、
また、弱塩基性アニオン交換樹脂でも−N
(CH3)2基をイオン交換基とするアンバーライト
IRA−93の場合は、低温(5℃)で操作しなけれ
ば使用不能であるが、本発明のピリジン系アニオ
ン交換樹脂は室温で操作できるうえ、精製効果も
上記アンバーライトIRA−93の低温使用と同等若
しくはそれ以上であり、本発明のピリジン系アニ
オン交換樹脂による精製の優位性は明らかであ
る。
実施例 3
実施例1の方法に準じて60℃で8時間前処理し
たピリジン系アニオン交換樹脂〔広栄化学製
KEX−212〕を用いて、その精製効果を調べた。
<方法>
上記イオン交換樹脂100mlをカラム(24mmφ×
110cm)につめ、これを用いて30℃で過酸化水素
水の精製を行なつた。
測定結果を表2に示す。[Table] *Resin floats due to hydrogen peroxide decomposition and normal column purification operation cannot be performed.
As shown in Table 1, purification using strongly basic anion exchange resins is impossible even at low temperatures (5°C);
Also, even with weakly basic anion exchange resins, -N
Amberlite with two (CH 3 ) groups as ion exchange groups
In the case of IRA-93, it cannot be used unless it is operated at a low temperature (5°C), but the pyridine-based anion exchange resin of the present invention can be operated at room temperature, and the purification effect is also , and the superiority of purification using the pyridine-based anion exchange resin of the present invention is clear. Example 3 Pyridine-based anion exchange resin pretreated at 60°C for 8 hours according to the method of Example 1 [manufactured by Koei Chemical Co., Ltd.]
KEX-212] was used to investigate its purification effect. <Method> Transfer 100ml of the above ion exchange resin to a column (24mmφ
110 cm), and used to purify hydrogen peroxide solution at 30°C. The measurement results are shown in Table 2.
【表】【table】
【表】
実施例 4
過酸化水素水精製プロセスの決定
実施例3と同様に前処理したピリジン系アニオ
ン交換樹脂〔広栄化学製KEX−212〕と交換基と
して−SO3H基を有するカチオン交換樹脂〔アン
バーライトIR−200CH〕とを夫々別々に用いた
場合と両者を併用した場合の過酸化水素水の精製
効果の比較を行つた。
<方法>
イオン交換樹脂各100mlを夫々カラム(24mmφ
×110cm)につめ、これを用いて過酸化水素水の
精製を行なつた。但し、流速はいずれも137ml/
minで行つた。
測定結果を表3に示す。但し、結果は原料過酸
化水素水の品質に対する増減で表わした。
また、ピリジン系アニオン交換樹脂とカチオン
交換樹脂を併用して精製する場合、ピリジン系ア
ニオン交換樹脂で精製後、カチオン交換樹脂で精
製した場合をアニオン交換樹脂→カチオン交換樹
脂で表わし、その逆をカチオン交換樹脂→アニオ
ン交換樹脂で表わした。[Table] Example 4 Determination of hydrogen peroxide water purification process Pyridine-based anion exchange resin [KEX-212 manufactured by Koei Chemical Co., Ltd.] pretreated in the same manner as in Example 3 and cation exchange resin having -SO 3 H group as an exchange group [Amberlite IR-200CH] was used to compare the purification effects of hydrogen peroxide water when used separately and when both were used together. <Method> Add 100 ml of each ion exchange resin to each column (24 mmφ
x 110cm) and used this to purify the hydrogen peroxide solution. However, the flow rate is 137ml/
I went with min. The measurement results are shown in Table 3. However, the results were expressed as an increase or decrease in the quality of the raw hydrogen peroxide solution. In addition, when purifying using a pyridine-based anion-exchange resin and a cation-exchange resin together, the case where the pyridine-based anion-exchange resin is used for purification and then the cation-exchange resin is expressed as anion exchange resin → cation exchange resin, and the reverse is expressed as cation exchange resin. Expressed as exchange resin → anion exchange resin.
【表】【table】
以上述べた如く、本発明は、高純度の過酸化水
素水が容易に且つより安全に得られる製造方法を
提供するものであり、従来のベンジルアミンを基
本骨格とするアニオン交換樹脂による過酸化水素
水の精製が、過酸化水素の分解を抑えるため低温
で行なわなければならなかつたのに対し、本発明
で使用するピリジン系アニオン交換樹脂の場合
は、これを前処理して用いれば、室温或はそれ以
上の温度でも過酸化水素の分解を促進するような
ことがないので、保安及び設備面で非常に有利で
ある点、及び精製効果もベンジルアミン系アニオ
ン交換樹脂よりも優れている点等に顕著な効果を
奏する発明であつて、斯業に貢献する処大なるも
のである。
As described above, the present invention provides a manufacturing method for easily and safely obtaining a high-purity hydrogen peroxide solution. Whereas water purification had to be carried out at low temperatures in order to suppress the decomposition of hydrogen peroxide, the pyridine-based anion exchange resin used in the present invention can be purified at room temperature or Since it does not accelerate the decomposition of hydrogen peroxide even at higher temperatures, it is very advantageous in terms of safety and equipment, and its purification effect is also superior to that of benzylamine-based anion exchange resins. It is an invention that has a remarkable effect on the industry, and it is a great contribution to the industry.
第1図は、実施例1に於ける測定結果を表わ
し、横軸は撹拌時間(時間)を示し、縦軸は過酸
化水素濃度(%)を示す。また●――●、△―・―
△、×…×は夫々60℃、40℃、20℃で前処理を行
なつたときの結果を表わす。
FIG. 1 shows the measurement results in Example 1, where the horizontal axis shows the stirring time (hours) and the vertical axis shows the hydrogen peroxide concentration (%). Also ●――●, △――・―
Δ, ×...× represent the results when pretreatment was performed at 60°C, 40°C, and 20°C, respectively.
Claims (1)
ることを特徴とする、高純度過酸化水素水の製造
法。 2 過酸化水素水で前処理したピリジン系アニオ
ン交換樹脂を用いる、特許請求の範囲第1項記載
の製造法。 3 ピリジン系アニオン交換樹脂とカチオン交換
樹脂を併用する、特許請求の範囲第1項又は第2
項記載の製造法。 4 ピリジン系アニオン交換樹脂がイオン交換基
として、一般式〔〕 【化】 (但し、R1〜R4は夫々独立して水素又は炭素数
1〜3のアルキル基を表わす。) で示されるピリジル基又は置換ピリジル基を有す
るポリマーからなるイオン交換樹脂である、特許
請求の範囲第1項、第2項又は第3項記載の製造
法。[Scope of Claims] 1. A method for producing high-purity hydrogen peroxide solution, which is characterized by purification using a pyridine-based anion exchange resin. 2. The manufacturing method according to claim 1, which uses a pyridine-based anion exchange resin pretreated with a hydrogen peroxide solution. 3 Claim 1 or 2, in which a pyridine-based anion exchange resin and a cation exchange resin are used together
Manufacturing method described in section. 4 Pyridine - based anion exchange resin as an ion exchange group is pyridyl represented by the general formula: The manufacturing method according to claim 1, 2 or 3, which is an ion exchange resin made of a polymer having a group or a substituted pyridyl group.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61028296A JPS62187103A (en) | 1986-02-12 | 1986-02-12 | Production of high-purity aqueous hydrogen peroxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61028296A JPS62187103A (en) | 1986-02-12 | 1986-02-12 | Production of high-purity aqueous hydrogen peroxide |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62187103A JPS62187103A (en) | 1987-08-15 |
JPH0568403B2 true JPH0568403B2 (en) | 1993-09-28 |
Family
ID=12244655
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61028296A Granted JPS62187103A (en) | 1986-02-12 | 1986-02-12 | Production of high-purity aqueous hydrogen peroxide |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62187103A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01153509A (en) * | 1987-12-11 | 1989-06-15 | Tokai Denka Kogyo Kk | Production of high-purity hydrogen peroxide |
-
1986
- 1986-02-12 JP JP61028296A patent/JPS62187103A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS62187103A (en) | 1987-08-15 |
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