JPS6024385A - Deoxidizer - Google Patents
DeoxidizerInfo
- Publication number
- JPS6024385A JPS6024385A JP13233083A JP13233083A JPS6024385A JP S6024385 A JPS6024385 A JP S6024385A JP 13233083 A JP13233083 A JP 13233083A JP 13233083 A JP13233083 A JP 13233083A JP S6024385 A JPS6024385 A JP S6024385A
- Authority
- JP
- Japan
- Prior art keywords
- aminoguanidine
- catalyst
- water
- hydroquinone
- oxidation
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/08—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
- C23F11/10—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Preventing Corrosion Or Incrustation Of Metals (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、水中に溶存する酸素を化学的に除去する組成
物に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a composition for chemically removing oxygen dissolved in water.
水は大気と接して酸素を溶解しているが、溶存酸素を含
む水を工業用水、例えばゼイラ用水、冷却水として使用
すると溶存酸素に起因する腐食問題が生ずる。このため
、給水前に、あるいは用水使用系内において水中から溶
存酸素を除去する処理が必璧となシ、還元剤による化学
的方法、真空、加熱による物理的方法によって酸素除去
が行われている。Water dissolves oxygen when it comes into contact with the atmosphere, but when water containing dissolved oxygen is used as industrial water, such as zeira water or cooling water, corrosion problems arise due to the dissolved oxygen. For this reason, it is essential to remove dissolved oxygen from the water before water is supplied or within the system where water is used.Oxygen is removed by chemical methods using reducing agents, and physical methods such as vacuum and heating. .
従来、化学的処理方法として、ヒドラジンによる脱酸素
方法が行われている。ヒドラジンはヒドロキノン等の酸
化還元触媒と配合すると、比較的速やかに水中の酸素を
除去するので好ましいものの一つである。しかし、ヒド
ラジンは取シ扱いを誤まると人体に悪影響を及ぼす可能
性が持たれているため、ヒドラジンを使用する業界では
ヒドラジンに代わる物質を見つけることが緊急の課題と
なっている。Conventionally, a deoxygenation method using hydrazine has been used as a chemical treatment method. Hydrazine is one of the preferable compounds because it removes oxygen from water relatively quickly when mixed with a redox catalyst such as hydroquinone. However, hydrazine has the potential to have an adverse effect on the human body if mishandled, so finding a substitute for hydrazine has become an urgent issue for industries that use hydrazine.
本発明の目的はヒドラジンに代わる脱酸振力に優れた脱
酸素剤を提供するPlFKある。An object of the present invention is to provide PIFK, which is a substitute for hydrazine and provides an oxygen scavenger with excellent deoxidizing force.
本発明者らは、鋭意横側の結果、アミノグアニジン又は
その塩は、酸化還元触媒の下でほぼイラ等の腐食の原因
となる溶存6り素を十分に除去できる力を有することを
見い出して本発明に至った。即ち、本発明は酸化還元触
媒とアミノグアニジン又はその塩とを含む脱酸素剤であ
る。As a result of extensive research, the present inventors have discovered that aminoguanidine or its salt has the ability to sufficiently remove dissolved hexagonal ions, which cause corrosion such as irradiation, under a redox catalyst. This led to the present invention. That is, the present invention is an oxygen scavenger containing a redox catalyst and aminoguanidine or a salt thereof.
酸化還元触媒としては、ヒドロキノン、メチルヒドロキ
ノン等の低級アルキルヒドロキノン、及びカテコールか
ら選ばれる少なくとも一種が使用できる。キノン類につ
いては酸化型(キノン、メチルキノン)も使用できる。As the redox catalyst, at least one selected from hydroquinone, lower alkylhydroquinone such as methylhydroquinone, and catechol can be used. As for quinones, oxidized forms (quinone, methylquinone) can also be used.
これらの触媒を配合しないとアミングアニジンの脱酸素
力はほとんど力いが、触媒在存下でアミノグアニジンは
下記式
%式%
に従い脱酸素力を発揮するものと推定される。If these catalysts are not blended, the deoxidizing power of aminoguanidine is almost too strong, but in the presence of a catalyst, aminoguanidine is estimated to exhibit deoxidizing power according to the following formula %.
アミノグアニジンの塩としては、硫酸塩、塩酸塩等が跣
げられる。Examples of aminoguanidine salts include sulfate and hydrochloride.
酸化還元触媒とアミノグアニジンとの配合割合は、アミ
ノグアニジン1重量部に対し、触媒が0.05〜20重
琶部、好ましくは0.1〜5重量部である。1だ、水系
へのアミノグアニジンの添加量は、通常、低圧ゼインで
5〜150ダ/L程度である。The mixing ratio of the redox catalyst and aminoguanidine is 0.05 to 20 parts by weight, preferably 0.1 to 5 parts by weight, per 1 part by weight of aminoguanidine. 1. The amount of aminoguanidine added to the water system is usually about 5 to 150 Da/L for low-pressure zein.
なお、低圧?イラ水の条件は圧力30 Ky / cr
A以下、pH11〜12となっている。アミノグアニジ
ンの脱酸素力自体はpHの影響を受けないが、酸化還元
触媒はpHに依存し、p)(が高いほど触媒効果が良く
なって組成物としての脱酸素力が改善される。Furthermore, low pressure? Ira water condition is pressure 30 Ky/cr
Below A, the pH is 11-12. The deoxidizing power of aminoguanidine itself is not affected by pH, but the redox catalyst is dependent on pH, and the higher p)(, the better the catalytic effect, and the better the deoxidizing power of the composition.
本発明を使用するには、触媒とアミノグアニジンとを予
め配合して水溶液状態としてから水系に添加しても良い
し、各化合物を各々別11・」に水系に添加しても良い
。To use the present invention, the catalyst and aminoguanidine may be blended in advance to form an aqueous solution and then added to the aqueous system, or each compound may be added separately to the aqueous system.
実施例
密栓付き広口ビンに500 ccの純水(飽和浴存酸素
が含有)を供給し、苛性ソータでpHを11.0に調脹
した。温度は20℃とした。Example 500 cc of pure water (containing saturated oxygen) was supplied to a wide-mouth bottle with a tight stopper, and the pH was adjusted to 11.0 using a caustic sorter. The temperature was 20°C.
この水に、アミノグアニジンのits giミスをアミ
ノグアニジンとして50 mfJ/l(ppm)とハイ
ドロキノンを各2 、6 、10 my/l (ppm
)含む水溶液を攪拌下で添加し、溶存酸素おの経時変化
を調べた。結果を図に示した。図中、AGはアミノグア
ニジンを示し、HQはハイドロキノンを示す。To this water, add 50 mfJ/l (ppm) of aminoguanidine as its gi mistake and 2, 6, and 10 my/l (ppm) of hydroquinone, respectively.
) was added under stirring to examine changes in dissolved oxygen over time. The results are shown in the figure. In the figure, AG represents aminoguanidine and HQ represents hydroquinone.
比較のためにハイドロキノンのみを2,6゜1omg/
L添加した場合についてもmt!Aぺ、結果を図に示し
た。For comparison, only hydroquinone was used at 2.6゜1omg/
Even when L is added, mt! A. The results are shown in the figure.
これより、アミノグアニジンをハイドロキノン(酸化還
元触媒)と併用することによって十分な脱酸素効果が得
られることが判る。特にアミノグアニジンとハイドロキ
ノンの配合割合が1 : 0.1以上となると脱酸素効
果が著しく改善される仁とが2)1」る。This shows that a sufficient oxygen removal effect can be obtained by using aminoguanidine in combination with hydroquinone (oxidation-reduction catalyst). In particular, when the blending ratio of aminoguanidine and hydroquinone is 1:0.1 or more, the oxygen scavenging effect is significantly improved.
図はアミノグアニジン(AG、)とハイドロキノン(H
Q)を水中に添加した場合の浴存酸素力i、の経時変化
をグラフ化したものである。
外1名
時間(ガ)The figure shows aminoguanidine (AG, ) and hydroquinone (H
This is a graph showing the change over time in the bath oxygen power i when Q) is added to water. 1 person outside time (ga)
Claims (1)
む脱敢累剤。 2、 酸化還元触媒はヒドロキノン、メチルヒドロキシ
ン及びカテコールからなる群から選ばれる少なくとも一
種であるl1許請求のfliα囲第1項第1項記載素剤
。[Scope of Claims] 1. A de-accumulation agent containing a redox catalyst and aminoguanidine or a salt thereof. 2. The raw material according to item 1, item 1, item 1 of item 11, wherein the redox catalyst is at least one selected from the group consisting of hydroquinone, methylhydroxyne, and catechol.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13233083A JPS6024385A (en) | 1983-07-20 | 1983-07-20 | Deoxidizer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13233083A JPS6024385A (en) | 1983-07-20 | 1983-07-20 | Deoxidizer |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6024385A true JPS6024385A (en) | 1985-02-07 |
Family
ID=15078796
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13233083A Pending JPS6024385A (en) | 1983-07-20 | 1983-07-20 | Deoxidizer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6024385A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002002845A3 (en) * | 2000-06-30 | 2002-03-14 | Caterpillar Inc | Method of treating ferrous-based substrates |
-
1983
- 1983-07-20 JP JP13233083A patent/JPS6024385A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002002845A3 (en) * | 2000-06-30 | 2002-03-14 | Caterpillar Inc | Method of treating ferrous-based substrates |
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