JPH0251898B2 - - Google Patents
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- Publication number
- JPH0251898B2 JPH0251898B2 JP11937687A JP11937687A JPH0251898B2 JP H0251898 B2 JPH0251898 B2 JP H0251898B2 JP 11937687 A JP11937687 A JP 11937687A JP 11937687 A JP11937687 A JP 11937687A JP H0251898 B2 JPH0251898 B2 JP H0251898B2
- Authority
- JP
- Japan
- Prior art keywords
- pdta
- reaction
- trivalent
- oxidation
- iron
- 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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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は例えばカラー写真焼付の際の酸化剤等
として使用することができる1,3−ジアミノプ
ロパン4酢酸鉄2アンモニウム塩に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a 1,3-diaminopropane-tetraacetic acid iron diammonium salt which can be used, for example, as an oxidizing agent in color photographic printing.
[従来の技術]
カラー写真焼付用酸化剤(以下単に酸化剤とい
うことがある)としては従来EDTA・FeNa(エ
チレンジアミン4酢酸鉄ナトリウム塩)や
EDTA・FeNH4(エチレンジアミン4酢酸鉄2ア
ンモニウム塩)が使用されている。[Prior art] Conventional oxidizing agents (hereinafter simply referred to as oxidizing agents) for color photographic printing include EDTA/FeNa (ethylenediaminetetraacetic acid iron sodium salt) and
EDTA/FeNH 4 (ethylenediaminetetraacetic acid iron diammonium salt) is used.
[発明が解決しようとする問題点]
上記化合物を酸化剤として使用するに当つて
は、前記化合物の水溶液にアンモニア水を添加し
てPHを調整することが行なわれており、水溶液中
でEDTA・Fe(NH4)2に変化させることによつて
酸化作用が発揮されるものであると考えられてい
る。即ちEDTA・Fe(NH4)2は溶液状でのみ存在
し、固体としては得られていない。その為
EDTA・Fe(NH4)2については物理的及び化学的
特性が十分に解明されておらず、またその他の酸
化剤応用可能分野への展開ということもなされて
いない。本発明はこの様な事情に鑑みてなされた
ものであつて、EDTA・Fe(NH4)2そのものの結
晶化については断念し、近縁化合物についての結
晶化研究を試みた結果、カラー写真焼付の際の酸
化剤として使用するとができる結晶性の新規化合
物を見出し本発明を完成したものである。[Problems to be Solved by the Invention] When using the above compound as an oxidizing agent, aqueous ammonia is added to an aqueous solution of the compound to adjust the pH. It is thought that the oxidizing effect is exerted by changing it to Fe(NH 4 ) 2 . That is, EDTA.Fe(NH 4 ) 2 exists only in a solution form and has not been obtained as a solid. For that reason
The physical and chemical properties of EDTA/Fe(NH 4 ) 2 have not been fully elucidated, nor has it been developed into other fields where it can be applied as an oxidizing agent. The present invention was made in view of these circumstances, and as a result of giving up on the crystallization of EDTA/Fe(NH 4 ) 2 itself and attempting crystallization research on closely related compounds, color photographic printing has been developed. The present invention was completed by discovering a new crystalline compound that can be used as an oxidizing agent in the process.
[発明の構成]
本発明の1,3−ジアミノプロパン4酢酸鉄2
アンモニウム塩[1,3−PDTA・Fe
(NH4)2OH]は下記式で示される。[Structure of the invention] 1,3-diaminopropane-tetraacetic acid iron 2 of the present invention
Ammonium salt [1,3-PDTA・Fe
(NH 4 ) 2 OH] is represented by the following formula.
この新規化合物の合成方法を例示すれば次の通
りである。 An example of the method for synthesizing this new compound is as follows.
まず1,3−PDTA(1,3−ジアミノプロパ
ン4酢酸)にアンモニア水とFe3O4を作用させ
る。次式で示す様にFe(2価)NH4塩とFe(3
価)・NH4塩の混合物を製造する。 First, 1,3-PDTA (1,3-diaminopropane tetraacetic acid) is reacted with aqueous ammonia and Fe 3 O 4 . As shown in the following formula, Fe (divalent) NH 4 salt and Fe (3
Produce a mixture of NH4 salts.
1,3−PDTA+NH4OH+Fe3O4→
1,3−PDTA・Fe(2価)(NH4)
+1,3−PDTA・Fe(3価)(NH4)
この反応はPH:3〜6、より好ましくは3〜5
で行なわれる。PHが3未満の場合1,3−
PDTA・Fe・Hが析出して反応が進行しなくな
るおそれがあり、またPHが6を超えると反応速度
が遅くなる。各原料を等モル量ずつ混合し反応さ
せることによつてPHは上記の好ましい範囲に調整
することができる。1,3-PDTA+NH 4 OH + Fe 3 O 4 → 1,3-PDTA・Fe (bivalent) (NH 4 ) +1,3-PDTA・Fe (trivalent) (NH 4 ) This reaction has a pH of 3 to 6, More preferably 3-5
It will be held in 1,3- if PH is less than 3
There is a risk that PDTA, Fe, and H will precipitate and the reaction will not proceed, and if the pH exceeds 6, the reaction rate will slow down. By mixing equimolar amounts of each raw material and reacting them, the pH can be adjusted to the above-mentioned preferred range.
反応速度は50〜100℃が好ましい。50℃未満で
は反応速度が遅くなり、一方100℃を超えると分
解反応が起るおそれがあり、より好ましくは60〜
80℃である。 The reaction rate is preferably 50 to 100°C. If it is less than 50℃, the reaction rate will be slow, while if it exceeds 100℃, there is a risk of decomposition reaction.
It is 80℃.
反応時間は特に限定されるものではないが通常
は5〜20時間の範囲で行なわれる。 Although the reaction time is not particularly limited, it is usually carried out within a range of 5 to 20 hours.
この反応で生成するFe錯化合物は前記反応式
で示した様に、2価と3価の鉄が混在する為反応
液を更に酸化処理に付して2価鉄を3価鉄にする
ことが必要である。酸化時間は酸化条件により異
なるが、収率を向上させる為には、2価鉄をチエ
ツクしてその存在量が0.1%以下になる迄酸化を
行なうことが好ましく、この工程によつてFe錯
化合物の全てが
で示される1,3−PDTA・Fe(3価)(NH4)
になる。 As shown in the reaction formula above, the Fe complex compound produced in this reaction contains a mixture of divalent and trivalent iron, so the reaction solution can be further oxidized to convert divalent iron to trivalent iron. is necessary. The oxidation time varies depending on the oxidation conditions, but in order to improve the yield, it is preferable to check for divalent iron and oxidize until the amount of divalent iron is 0.1% or less. everything about 1,3-PDTA・Fe (trivalent) (NH 4 ) represented by
become.
この酸化方法は特に限定されないが副反応が起
りにくいO2或か空気による酸化が好ましい。酸
化温度は40〜80℃、より好ましくは40〜60℃であ
る。80℃を超えると分解反応を生じる傾向が強
く、40%未満では酸化速度が遅くなる。酸化時の
反応液のPHは4〜7、より好ましくは4〜6に調
整することが必要でありPHが高すぎると酸化速度
が遅くなる。次に反応液を濾過して未反応酸化鉄
を除去するが、酸化工程の前に濾過を行なつても
よい。 The oxidation method is not particularly limited, but oxidation using O 2 or air, which is less likely to cause side reactions, is preferred. The oxidation temperature is 40-80°C, more preferably 40-60°C. If it exceeds 80°C, there is a strong tendency for decomposition reactions to occur, and if it is less than 40%, the oxidation rate becomes slow. It is necessary to adjust the pH of the reaction solution during oxidation to 4 to 7, more preferably 4 to 6; if the pH is too high, the oxidation rate will be slow. Next, the reaction solution is filtered to remove unreacted iron oxide, but filtration may be performed before the oxidation step.
次に反応液にアンモニア水を作用させて1,3
−PDTA・Fe(3価)OH(NH4)2を得る。即ち
1,3−PDTA・Fe(3価)(NH4)NH4OH
―
―
―
―
―
―
―
→
1,3−PDTA・Fe(3価)・OH(NH4)2
この場合PHを8〜8.5とすることが好ましく、
1,3−PDTA・Fe(3価)(NH4)と等モルの
アンモニア水を添加すればPHを上記の範囲に保つ
ことができる。この場合反応温度は反応速度の保
持、分解反応抑制の観点から40〜60℃とすること
が好ましい。 Next, aqueous ammonia was applied to the reaction solution to give 1,3
−PDTA·Fe(trivalent)OH(NH 4 ) 2 is obtained. That is, 1,3-PDTA・Fe (trivalent) (NH 4 )NH 4 OH ― ― ― ― ― ― → 1,3-PDTA・Fe (trivalent) ・OH (NH 4 ) 2 In this case, the pH is 8 It is preferable to set it to ~8.5,
The pH can be maintained within the above range by adding 1,3-PDTA.Fe (trivalent) (NH 4 ) and equimolar ammonia water. In this case, the reaction temperature is preferably 40 to 60°C from the viewpoint of maintaining the reaction rate and suppressing the decomposition reaction.
反応終了後、減圧下で反応液の濃縮を行ない、
蒸発水分を除去して結晶を析出させ、濾過して得
られた結晶体をメタノール等で洗浄し乾燥させる
と、1,3−PDTA・Fe(3価)(NH4)2OHの結
晶が得られる。尚減圧時の圧力は分解反応の抑制
及び濃縮効率保持の見地から50〜150mmHgとする
ことが好ましい。 After the reaction is completed, the reaction solution is concentrated under reduced pressure.
By removing evaporated moisture and precipitating crystals, washing the obtained crystals with methanol etc. and drying them, crystals of 1,3-PDTA・Fe (trivalent) (NH 4 ) 2 OH are obtained. It will be done. The pressure at the time of decompression is preferably 50 to 150 mmHg from the viewpoint of suppressing decomposition reactions and maintaining concentration efficiency.
以上本発明における合成方法の例を述べたが、
他の例として、1,3−PDTA・(NH4)3・Hに
FeCl3を反応させ、更にNH4OHを添加する方法、
つまり
1,3−PDTA・(NH4)3・H+FeCl3→
1,3−PDTA・Fe(3価)・H+3NH4Cl
1,3−PDTA・Fe(3価)・H+2NH4OH→
1,3−PDTA・Fe(3価)(NH4)2OH+H2O
の反応を経る方法もある。 Although examples of the synthesis method in the present invention have been described above,
As another example, 1,3-PDTA・(NH 4 ) 3・H
A method of reacting FeCl 3 and further adding NH 4 OH,
In other words, 1,3-PDTA・(NH 4 ) 3・H+FeCl 3 → 1,3-PDTA・Fe (trivalent)・H+3NH 4 Cl 1,3-PDTA・Fe (trivalent)・H+2NH 4 OH→ 1,3 -PDTA・Fe (trivalent) (NH 4 ) 2 OH + H 2 O reaction is also available.
以下実施例について説明するが本発明は下記実
施例に限定されるものではなく、前・後記の趣旨
に徴して適宜設計変更することは本発明の技術的
範囲に含まれる。 Examples will be described below, but the present invention is not limited to the following examples, and it is within the technical scope of the present invention to make appropriate design changes in accordance with the spirit described above and below.
[実施例]
1,3−PDTA:1000g
25%アンモニア:218g
水:1300g
Fe3O4(Fe含量71重量%):238g
の各原料を混合し反応させた後、反応液を冷却し
てから空気酸化に付した。この工程における反応
条件は
反応温度:70℃
PH:3.5
反応時間:16時間
冷却温度:40〜50℃
空気酸化時間:10時間
であつた。[Example] 1,3-PDTA: 1000g 25% ammonia: 218g Water: 1300g Fe 3 O 4 (Fe content 71% by weight): 238g After mixing and reacting each raw material, the reaction solution was cooled and then Subjected to air oxidation. The reaction conditions in this step were reaction temperature: 70°C, pH: 3.5, reaction time: 16 hours, cooling temperature: 40-50°C, and air oxidation time: 10 hours.
次に反応液を濾過して未反応物を除去した。反
応率は95%であつた。 Next, the reaction solution was filtered to remove unreacted substances. The reaction rate was 95%.
更にこの反応液に25%アンモニア水210gを添
加してPHを8.2に調整し100mmHgの減圧下で濃縮
を行ない、約1100gの蒸発水を抜き出し、析出し
た結晶を濾過した後メタノールで洗浄すると、
1,3−PDTA・Fe(3価)(NH4)2・OHの暗赤
色結晶526gが得られた。収率は39%であり物性
は次の通りであつた。 Further, 210 g of 25% ammonia water was added to this reaction solution to adjust the pH to 8.2, and the mixture was concentrated under a reduced pressure of 100 mmHg. Approximately 1100 g of evaporated water was extracted, and the precipitated crystals were filtered and washed with methanol.
526 g of dark red crystals of 1,3-PDTA.Fe (trivalent) (NH 4 ) 2.OH were obtained. The yield was 39%, and the physical properties were as follows.
分子量:411
5%溶液PH:8.16
溶解度(25℃):52重量%
融点:178℃(分解)
特性赤外線吸収(KBr):第1図
鉄含有量:13.8%
尚上記鉄含有量は理論値の分子量から算出され
る値に対して101.51%であり更にZn−XO含量も
理論値に対して101.8%であり、誤差は実験誤差
の範囲内であつた。Molecular weight: 411 5% solution PH: 8.16 Solubility (25℃): 52% by weight Melting point: 178℃ (decomposition) Characteristic infrared absorption (KBr): Figure 1 Iron content: 13.8% The above iron content is the theoretical value. It was 101.51% of the value calculated from the molecular weight, and the Zn-XO content was also 101.8% of the theoretical value, and the error was within the experimental error range.
[発明の効果]
本発明は以上の様に構成されているから、カラ
ー写真焼付の際の酸化剤等として使用することが
できる結晶性の新規化合物、1,3−ジアミノプ
ロパン4酢酸鉄2アンモニウム塩を得ることがで
きる。[Effects of the Invention] Since the present invention is configured as described above, a new crystalline compound, 1,3-diaminopropane-tetraferric acetate diammonium, which can be used as an oxidizing agent, etc. during color photographic printing You can get salt.
第1図は本発明に係る新規物質の赤外線吸収ス
ペクトルを示す図である。
FIG. 1 is a diagram showing the infrared absorption spectrum of the new substance according to the present invention.
Claims (1)
ロパン4酢酸鉄2アンモニウム塩。[Claims] 1 formula An iron diammonium salt of 1,3-diaminopropane-tetraacetate, characterized by the following:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11937687A JPS63284154A (en) | 1987-05-15 | 1987-05-15 | Iron diammonium 1,3-diaminopropanetetraacetate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11937687A JPS63284154A (en) | 1987-05-15 | 1987-05-15 | Iron diammonium 1,3-diaminopropanetetraacetate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63284154A JPS63284154A (en) | 1988-11-21 |
| JPH0251898B2 true JPH0251898B2 (en) | 1990-11-08 |
Family
ID=14759978
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11937687A Granted JPS63284154A (en) | 1987-05-15 | 1987-05-15 | Iron diammonium 1,3-diaminopropanetetraacetate |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63284154A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6471842A (en) * | 1987-09-11 | 1989-03-16 | Nitto Chemical Industry Co Ltd | Production of aminopolycarboxylic acid iron (ii) complex ammonium salt |
| US5900499A (en) * | 1997-07-08 | 1999-05-04 | The Dow Chemical Company | Preparation of aminopolycarboxylate-ferric solutions with improved long-term stability |
| US7034172B1 (en) | 2005-06-07 | 2006-04-25 | Basf Corporation | Ferric and acid complex |
-
1987
- 1987-05-15 JP JP11937687A patent/JPS63284154A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63284154A (en) | 1988-11-21 |
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