JP3287243B2 - Oxygen scavenger - Google Patents
Oxygen scavengerInfo
- Publication number
- JP3287243B2 JP3287243B2 JP31814096A JP31814096A JP3287243B2 JP 3287243 B2 JP3287243 B2 JP 3287243B2 JP 31814096 A JP31814096 A JP 31814096A JP 31814096 A JP31814096 A JP 31814096A JP 3287243 B2 JP3287243 B2 JP 3287243B2
- Authority
- JP
- Japan
- Prior art keywords
- oxygen
- boiler
- oxygen scavenger
- heterocyclic compound
- dissolved oxygen
- 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
Links
Landscapes
- Preventing Corrosion Or Incrustation Of Metals (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Removal Of Specific Substances (AREA)
- Pyridine Compounds (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は脱酸素剤に関し、更
に詳しくは、水中の溶存酸素を効率よく除去することが
でき、とくにボイラ給水の溶存酸素を除去することによ
りボイラシステムの腐食防止にとって有効な脱酸素剤に
関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a deoxidizer, and more particularly to a deoxidizer capable of efficiently removing dissolved oxygen in water, and particularly effective for preventing corrosion of a boiler system by removing dissolved oxygen in boiler feed water. Related to various oxygen absorbers.
【0002】[0002]
【従来の技術】ボイラ給水に含まれている溶存酸素は、
ボイラ本体、当該ボイラ本体の前段に配置される熱交換
器やエコノマイザ,蒸気復水系配管などの腐食を引き起
こす原因を構成する。したがって、これらボイラシステ
ムの腐食を防止するためには、使用するボイラ給水に対
し脱酸素処理を行ってボイラ給水中の溶存酸素を除去す
ることが必要である。2. Description of the Related Art Dissolved oxygen contained in boiler feedwater is:
This constitutes a cause of corrosion of the boiler main body, a heat exchanger, an economizer, a steam condensing pipe, etc. disposed in a stage preceding the boiler main body. Therefore, in order to prevent the corrosion of these boiler systems, it is necessary to remove the dissolved oxygen in the boiler feed water by performing a deoxygenation treatment on the boiler feed water used.
【0003】そのため従来から、脱酸素処理として化学
的処理と物理的処理が実施されている。例えば、化学的
処理としては、ヒドラジン(N2H4)および亜硫酸ナト
リウム(Na2SO3)を脱酸素剤としてボイラ給水に添
加する方法が広く採用されている。[0003] Therefore, chemical treatment and physical treatment have been conventionally performed as deoxygenation treatment. For example, as a chemical treatment, a method of adding hydrazine (N 2 H 4 ) and sodium sulfite (Na 2 SO 3 ) to a boiler feedwater as a deoxidizer has been widely adopted.
【0004】[0004]
【発明が解決しようとする課題】ところで、上記した化
学的処理において、ヒドラジンや亜硫酸ナトリウムを脱
酸素剤として使用する方法には次のような問題がある。
まず、ヒドラジンは人体に対する安全性の面で問題視さ
れている。また、亜硫酸ナトリウムの場合は、酸素との
反応速度が大きすぎるので、次のような問題が起こる。However, in the above-mentioned chemical treatment, the method using hydrazine or sodium sulfite as an oxygen scavenger has the following problems.
First, hydrazine is regarded as a problem in terms of safety for the human body. Further, in the case of sodium sulfite, the following problem occurs because the reaction rate with oxygen is too high.
【0005】すなわち、ボイラ給水への添加に先立ち、
亜硫酸ナトリウムを溶解タンクで水に溶解するときに、
当該亜硫酸ナトリウムは溶存酸素と反応してその濃度低
下を引き起こすので注入量不足になり、結局、ボイラシ
ステムの腐食を助長することになってしまう。更に、亜
硫酸ナトリウムで処理したボイラ給水には、新たに硫酸
イオンが生成するので、ボイラシステムでは腐食やスケ
ール付着が起こりやすくなる。That is, prior to the addition to the boiler feed water,
When dissolving sodium sulfite in water in the dissolution tank,
The sodium sulfite reacts with the dissolved oxygen to cause a decrease in the concentration thereof, resulting in an insufficient injection amount, which ultimately promotes the corrosion of the boiler system. Furthermore, since sulfuric acid ions are newly generated in the boiler feedwater treated with sodium sulfite, corrosion and scale adhesion are likely to occur in the boiler system.
【0006】したがって、脱酸素剤としてヒドラジンや
亜硫酸ナトリウムを使用する方法は、必ずしも工業的に
有利な方法であるとはいいがたい。本発明は、例えばボ
イラ給水の脱酸素を化学的処理で行うときに使用する従
来の脱酸素剤における上記した問題を解決し、ボイラ給
水の溶存酸素を効率よく除去することができ、また高い
安全性を備えた新規な脱酸素剤の提供を目的とする。Therefore, the method using hydrazine or sodium sulfite as the oxygen scavenger is not necessarily industrially advantageous. The present invention solves the above-described problems in the conventional oxygen absorber used when performing deoxidation of boiler feedwater by chemical treatment, for example, and can efficiently remove dissolved oxygen in boiler feedwater, and can provide high safety. The purpose of the present invention is to provide a new oxygen scavenger having a property.
【0007】[0007]
【課題を解決するための手段】上記した目的を達成する
ために、本発明においては、N−置換アミノ基を有する
複素環式化合物を有効成分とすることを特徴とする脱酸
素剤が提供される。 In order to achieve the above-mentioned object, in the present invention, a compound having an N-substituted amino group is provided.
An oxygen scavenger characterized by comprising a heterocyclic compound as an active ingredient is provided .
【0008】[0008]
【0009】[0009]
【0010】[0010]
【0011】[0011]
【0012】[0012]
【0013】[0013]
【0014】[0014]
【発明の実施の形態】本発明の脱酸素剤は、以下の複素
環式化合物を有効成分として含有するものを好適とす
る。すなわち、BEST MODE FOR CARRYING OUT THE INVENTION The oxygen scavenger of the present invention is preferably one containing the following heterocyclic compound as an active ingredient. That is,
【0015】[0015]
【0016】[0016]
【0017】[0017]
【化1】 Embedded image
【0018】これらの複素環式化合物は、それぞれ単独
で用いてもよく、また2種以上を組み合わせて用いても
よい。さらに、本発明の脱酸素剤は、環内にN−N結合
を有する複素環式化合物(以下、複素環式化合物Aとい
う),次式: These heterocyclic compounds may be used alone or in combination of two or more. Further, the oxygen scavenger of the present invention has an NN bond in the ring.
(Hereinafter, referred to as heterocyclic compound A)
U), the following equation:
【化2】 (式中、a,bは、いずれも0〜5の整数であり、か
つ、2≦a+b≦5の 関係を満足する整数である)で示
される複素環式化合物(以下、複素環式化合物Bとい
う),次式: Embedded image (Where a and b are each an integer of 0 to 5,
And an integer satisfying the relationship 2 ≦ a + b ≦ 5 )
(Hereinafter, referred to as heterocyclic compound B)
U), the following equation:
【化3】 (式中、R 1 ,R 2 ,R 3 ,R 4 は同じであっても異なって
いてもよく、水素、 または炭素数1〜8の低級アルキル
基もしくはアリール基のいずれかを表 し、Xは、水素,
アミノ基,炭素数1〜8のアルキルアミノ基もしくはジ
アルキルアミノ基、または炭素数1〜8の低級アルキル
基もしくはアリー ル基のいずれかを表す)で示される複
素環式化合物(以下、複素環式化合物Cという),なら
びにアゾジカルボンアミド(NH 2 CON=NCON
H 2 )からなる群より選ばれる1種また は2種以上の化
合物を有効成分とする脱酸素剤と組み合わせて用いても
良い。 この場合、複素環式化合物Aは、以下の複素環式
化合物を好適とする。すなわち、 Embedded image (Wherein R 1 , R 2 , R 3 , and R 4 are different even if they are the same.
May be hydrogen or lower alkyl having 1 to 8 carbon atoms
Represents any group or aryl group, X is hydrogen,
Amino group, alkylamino group having 1 to 8 carbon atoms or diamino
Alkylamino group or lower alkyl having 1 to 8 carbon atoms
Double represented by represents any one group or aryl Le group)
A cyclic compound (hereinafter, referred to as a heterocyclic compound C),
Azodicarbonamide (NH 2 CON = NCON
One or two or more of selected from the group consisting of H 2)
The compound can be used in combination with an oxygen absorber as an active ingredient.
good. In this case, the heterocyclic compound A is the following heterocyclic compound
The compounds are preferred. That is,
【化4】 そして、複素環式化合物Bとしては、次のようなものを
好適例とすることができる。 Embedded image And, as the heterocyclic compound B,
It can be a preferred example.
【化5】 また、複素環式化合物Cとしては、次のようなものを好
適例とすることができる。 Embedded image Further, as the heterocyclic compound C, the following compounds are preferable.
This can be a case in point.
【化6】 Embedded image
【0019】[0019]
【0020】[0020]
【0021】[0021]
【0022】[0022]
【0023】[0023]
【0024】[0024]
【0025】[0025]
【0026】以上、列記した各有効成分の使用量は、対
象とする水の溶存酸素の量に応じて適宜に決められるの
で格別限定されるわけではないが、通常、水1リットル
に対し、0.001〜1000mg、好ましくは1から30
0mgであることが望ましい。The amount of each of the active ingredients listed above is not particularly limited since it is appropriately determined according to the amount of dissolved oxygen in the target water. 0.001 to 1000 mg, preferably 1 to 30
Desirably, it is 0 mg.
【0027】[0027]
【実施例】実施例1〜11 本発明 の脱酸素剤の効果を次のようにして確認した。室
温下において空気中の酸素で飽和させた軟化水を、容量
5リットルの蒸気発生試験オートクレーブに給水し、下
記の条件で運転して蒸気を発生させた。EXAMPLES Examples 1 to 11 The effects of the oxygen scavenger of the present invention were confirmed as follows. Softened water saturated with oxygen in the air at room temperature was supplied to a 5-liter steam generation test autoclave and operated under the following conditions to generate steam.
【0028】温度:185℃,圧力:1MPa,蒸発量:
12リットル/hr,ブロー率:10% 発生した蒸気を完全に凝縮し、得られた凝縮水中の溶存
酸素濃度を溶存酸素計を用いて測定した。この値を比較
例1のデータとする。ついで、給水に脱酸素剤を添加し
て同様の条件で蒸気を発生させ、その蒸気の凝縮水中の
溶存酸素濃度を測定した。そして、前記比較例1のデー
タとの差を除去量として算出し、その除去量の比較例1
のデータに対する割合を除去率(%)として算出した。Temperature: 185 ° C., pressure: 1 MPa, evaporation amount:
12 liters / hr, blow rate: 10% The generated steam was completely condensed, and the concentration of dissolved oxygen in the obtained condensed water was measured using a dissolved oxygen meter. This value is used as data of Comparative Example 1. Next, a deoxidizer was added to the feed water to generate steam under the same conditions, and the concentration of dissolved oxygen in the condensed water of the steam was measured. Then, the difference from the data of Comparative Example 1 was calculated as the removal amount, and the removal amount was compared with that of Comparative Example 1.
Was calculated as the removal rate (%).
【0029】なお、給水への脱酸素剤の添加に関して
は、表1に示した複素環式化合物を前記軟化水に溶解し
て所定濃度の水溶液を調製し、その水溶液を定量ポンプ
で前記給水に供給し、給水中の複素環式化合物の濃度を
表1で示したように調整した。以上の結果を表1に示し
た。As for the addition of the oxygen scavenger to the feed water, the heterocyclic compound shown in Table 1 was dissolved in the softened water to prepare an aqueous solution having a predetermined concentration, and the aqueous solution was added to the feed water by a constant-rate pump. The concentration of the heterocyclic compound in the feed and feed water was adjusted as shown in Table 1. Table 1 shows the above results.
【0030】[0030]
【0031】[0031]
【0032】[0032]
【表1】 [Table 1]
【0033】[0033]
【0034】[0034]
【0035】[0035]
【0036】[0036]
【0037】[0037]
【0038】[0038]
【0039】[0039]
【0040】[0040]
【発明の効果】以上の説明で明らかなように、本発明の
脱酸素剤は、水中の溶存酸素を効率よく除去することが
できる。とくに、ボイラ給水の脱酸素剤として使用した
場合、溶存酸素によるボイラ本体や蒸気復水系配管の腐
食を防止することができ、その工業的価値は極めて大で
ある。As apparent from the above description, <br/> oxygen scavenger of the present invention can be in the water dissolved oxygen efficiently removed. In particular, when used as a deoxidizer for boiler feedwater, corrosion of the boiler body and steam condensing system piping due to dissolved oxygen can be prevented, and its industrial value is extremely large.
【0041】[0041]
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C02F 1/58,1/72 C23F 11/14 C07D 239/54 C07D 213/73 F22D 11/00 JICSTファイル(JOIS) CA(STN)────────────────────────────────────────────────── ─── Continued on the front page (58) Fields surveyed (Int. Cl. 7 , DB name) C02F 1/58, 1/72 C23F 11/14 C07D 239/54 C07D 213/73 F22D 11/00 JICST file ( JOIS) CA (STN)
Claims (1)
物を有効成分とすることを特徴とする脱酸素剤。1. An oxygen scavenger comprising a heterocyclic compound having an N-substituted amino group as an active ingredient.
Priority Applications (18)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP31814096A JP3287243B2 (en) | 1996-11-28 | 1996-11-28 | Oxygen scavenger |
| EP97309363A EP0845438B1 (en) | 1996-11-28 | 1997-11-20 | Oxygen scavenger and boiler water treatment chemical |
| DE69706810T DE69706810T2 (en) | 1996-11-28 | 1997-11-20 | Oxygen removal agent as a compound for the treatment of scale feed water |
| US08/975,000 US5989440A (en) | 1996-11-28 | 1997-11-20 | Method of using oxygen scavenger and removing oxygen from water |
| MYPI97005606A MY122031A (en) | 1996-11-28 | 1997-11-21 | Oxygen scavenger and boiler water treatment chemical. |
| CNB2004100474733A CN100335427C (en) | 1996-11-28 | 1997-11-28 | Oxygen scavenger and boiler water treatment chemical |
| CNB021018510A CN1187271C (en) | 1996-11-28 | 1997-11-28 | Oxygen decontaminated agent |
| CNB2007100044917A CN100528762C (en) | 1996-11-28 | 1997-11-28 | Oxygen scavenger and boiler water treatment chemical |
| CN97114370A CN1103748C (en) | 1996-11-28 | 1997-11-28 | oxygen scavenger |
| KR1019970063766A KR100317967B1 (en) | 1996-11-28 | 1997-11-28 | Oxygen scavenger and boiler water treatment chemical |
| MXPA/A/1997/009264A MXPA97009264A (en) | 1996-11-28 | 1997-11-28 | Oxygen eliminator and cald water treatment chemical product |
| BR9706050A BR9706050A (en) | 1996-11-28 | 1997-11-28 | Oxygen and chemical remover for boiler water treatment |
| CNB2007100044921A CN100528763C (en) | 1996-11-28 | 1997-11-28 | Oxygen scavenger and boiler water treatment chemical |
| US09/404,202 US6346206B1 (en) | 1996-11-28 | 1999-09-23 | Oxygen scavenger and boiler water treatment chemical |
| KR1020010037957A KR100342269B1 (en) | 1996-11-28 | 2001-06-29 | Oxygen scavenger and boiler water treatment chemical |
| US09/984,435 US20020046976A1 (en) | 1996-11-28 | 2001-10-30 | Oxygen scavenger and boiler water treatment chemical |
| CNB021018529A CN1205134C (en) | 1996-11-28 | 2002-01-11 | Methods of Using Oxygen Scavenger |
| US10/322,500 US6861032B2 (en) | 1996-11-28 | 2002-12-19 | Oxygen scavenger and boiler water treatment chemical |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP31814096A JP3287243B2 (en) | 1996-11-28 | 1996-11-28 | Oxygen scavenger |
Related Child Applications (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001229557A Division JP3624944B2 (en) | 2001-07-30 | 2001-07-30 | Oxygen scavenger |
| JP2001229558A Division JP3624945B2 (en) | 2001-07-30 | 2001-07-30 | Oxygen scavenger |
| JP2001229556A Division JP3705355B2 (en) | 2001-07-30 | 2001-07-30 | Oxygen absorber for boiler feed water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH10158872A JPH10158872A (en) | 1998-06-16 |
| JP3287243B2 true JP3287243B2 (en) | 2002-06-04 |
Family
ID=18095953
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP31814096A Expired - Lifetime JP3287243B2 (en) | 1996-11-28 | 1996-11-28 | Oxygen scavenger |
Country Status (3)
| Country | Link |
|---|---|
| JP (1) | JP3287243B2 (en) |
| CN (2) | CN100528762C (en) |
| BR (1) | BR9706050A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6540923B2 (en) | 2000-12-05 | 2003-04-01 | Kurita Water Industries Ltd. | Oxygen scavenger |
| JP4950391B2 (en) * | 2001-06-27 | 2012-06-13 | 上野製薬株式会社 | Oxygen absorber |
| JP3855961B2 (en) | 2003-04-28 | 2006-12-13 | 栗田工業株式会社 | Oxygen absorber and deoxygenation method |
| JP4745990B2 (en) * | 2007-01-31 | 2011-08-10 | 三菱重工業株式会社 | Turbine equipment and initial switching method for oxygen treatment of turbine equipment |
-
1996
- 1996-11-28 JP JP31814096A patent/JP3287243B2/en not_active Expired - Lifetime
-
1997
- 1997-11-28 CN CNB2007100044917A patent/CN100528762C/en not_active Expired - Fee Related
- 1997-11-28 CN CNB2007100044921A patent/CN100528763C/en not_active Expired - Fee Related
- 1997-11-28 BR BR9706050A patent/BR9706050A/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| CN100528763C (en) | 2009-08-19 |
| CN100528762C (en) | 2009-08-19 |
| CN100999343A (en) | 2007-07-18 |
| CN100999342A (en) | 2007-07-18 |
| JPH10158872A (en) | 1998-06-16 |
| BR9706050A (en) | 1999-06-29 |
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