EP0131970B1 - Process for the production of sulfuric-acid adducts of urea - Google Patents

Process for the production of sulfuric-acid adducts of urea Download PDF

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Publication number
EP0131970B1
EP0131970B1 EP84108556A EP84108556A EP0131970B1 EP 0131970 B1 EP0131970 B1 EP 0131970B1 EP 84108556 A EP84108556 A EP 84108556A EP 84108556 A EP84108556 A EP 84108556A EP 0131970 B1 EP0131970 B1 EP 0131970B1
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Prior art keywords
urea
silver
sulfuric acid
acid
bleaching
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EP84108556A
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German (de)
French (fr)
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EP0131970A1 (en
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Hansjörg Dr. Buser
Adolf Morand
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Novartis AG
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Ciba Geigy AG
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    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03CPHOTOSENSITIVE MATERIALS FOR PHOTOGRAPHIC PURPOSES; PHOTOGRAPHIC PROCESSES, e.g. CINE, X-RAY, COLOUR, STEREO-PHOTOGRAPHIC PROCESSES; AUXILIARY PROCESSES IN PHOTOGRAPHY
    • G03C7/00Multicolour photographic processes or agents therefor; Regeneration of such processing agents; Photosensitive materials for multicolour processes
    • G03C7/28Silver dye bleach processes; Materials therefor; Preparing or processing such materials
    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03CPHOTOSENSITIVE MATERIALS FOR PHOTOGRAPHIC PURPOSES; PHOTOGRAPHIC PROCESSES, e.g. CINE, X-RAY, COLOUR, STEREO-PHOTOGRAPHIC PROCESSES; AUXILIARY PROCESSES IN PHOTOGRAPHY
    • G03C5/00Photographic processes or agents therefor; Regeneration of such processing agents
    • G03C5/26Processes using silver-salt-containing photosensitive materials or agents therefor
    • G03C5/40Chemically transforming developed images
    • G03C5/44Bleaching; Bleach-fixing

Definitions

  • the present invention relates to a method for producing sulfuric acid adducts of urea.
  • steps (B) and (C) and (B), (C) and (D) can be carried out simultaneously in a single bath.
  • the preparations (baths) used for the color and / or silver bleaching or the combined bleach-fixation are strongly acidic, i.e. have a pH of less than 2, especially less than 1.
  • This pH is generally set using strong acids, primarily mineral acids, such as hydrochloric acid, sulfuric acid, nitric or phosphoric acid, and also sulfanic acid. Good results are also obtained with certain strong organic acids, such as p-toluenesulfonic acid.
  • Hydrochloric acid highly volatile and therefore has a particularly corrosive effect on e.g. Apparatus and devices in which the processing of the photographic material is carried out.
  • the use of solid instead of liquid acids is particularly advantageous because it facilitates the preparation, transport and storage of preparations for color and / or silver bleaching.
  • the sulfamic acid which is suitable per se and can easily be produced in free-flowing powder form, can in many cases be used as a substitute for liquid mineral acids.
  • One disadvantage is their relatively poor solubility in water. It has also been shown that it reacts with tertiary phosphines, which are used as bleach accelerators, and leads to unstable bleach baths.
  • p-Toluenesulfonic acid which can also be used in free-flowing powder form, has a high water solubility and provides stable bleaching baths.
  • the object of the present invention is to provide strong mineral acids, as are required in the processing of photographic silver color bleaching materials, in a suitable form in order to overcome the disadvantages mentioned above.
  • sulfuric acid adducts of urea can be used instead of mineral acids. These adducts are solid, of good stability, high solubility in water and they dissociate easily in their original components in aqueous solution.
  • the present invention thus relates to a process for the preparation of sulfuric acid adducts of urea with a urea-sulfuric acid ratio of 2: 1 or 1: 1, characterized in that the solid urea is entered in the stated ratio in 100 percent sulfuric acid, where Entry speed and external cooling are coordinated so that the temperature during the mixing time is between 70 and 100 ° C, and that the neutral or acid urea sulfate obtained in this way is converted into solid form by cooling and, if necessary, comminuted.
  • the adducts of one mole of urea with 0.5 or 1 mole of sulfuric acid are particularly well known.
  • the melting points of these adducts are 80 and 70 ° C, respectively.
  • Information about the properties of these adducts, their stability, the reaction kinetics in the melt and in aqueous solutions can be found, among others. at L.H. Dalman, J.Am.Chem.Soc. 56, 549 (1934) P. Baumgarten, Chem. Ber. 69 1929 (1936), E. Cherbuliez & F. Landolt, Helv. 29, 1438 (1946) and G.M. Schwab & E. Schwab-Agallidis, Angew. Chemie, 65, 418 (1953).
  • the sulfuric acid adducts of urea are prepared either directly from the components or their solutions or also by the action of mineral acid on cyanamide, the latter decomposing to urea, which then forms the addition compound with the acid.
  • the adducts produced according to the invention are stable in solid form and can easily be prepared in the form of free-flowing water-soluble powders or granules.
  • urea sulfate the adduct of two moles of urea with one mole of sulfuric acid
  • urea hydrogen sulfate the adduct of one mole of urea with one mole of sulfuric acid
  • urea is introduced directly into solid form in 100% sulfuric acid (monohydrate) with cooling, the temperature not being allowed to rise above about 100 ° C. (preferably 70 ° C. to 100 ° C.) during the reaction.
  • the compounds are converted into the solid form by cooling and optionally comminuted.
  • the melt can be removed by suitable methods, e.g. used in the production of alkali metal hydroxides (cf. Ullmanns Encyklopadie der Technische Chemie, 4th edition, Verlag Chemie, Weinheim, Vol. 17 (1979), p. 204 f), are converted into a solid form suitable for the application. In particular, it can be crystallized in the form of free-flowing pearls, pills, flakes or flakes that are immediately soluble in water.
  • the sulfuric acid adducts can be brought into the form of beads if they are e.g. sprayed in a cooling tower.
  • This material is constructed in such a way that, when processed with a developer containing a silver ligand, in particular sodium thiosulfate, and the subsequent process steps of color and silver bleaching necessary for the silver color bleaching process, the latter preferably combined in a single step, and finally the fixation, a masking of the blue secondary color densities the purple and cyan layer is effected.
  • a six-layer material is used which in the first layer contains the cyan dye and the associated red-sensitized silver halide emulsion, and in the second layer a thin, pure gelatin-containing intermediate layer in the third layer contains the purple dye with the associated green-sensitized silver halide emulsion, the fourth layer is an intermediate layer consisting of gelatin, the fifth layer contains a silver halide layer containing a yellow dye and finally the sixth layer contains a protective layer of pure gelatin.
  • a second sample strip is exposed and processed in an identical manner, but using a combined bleaching and fixing bath which contains 9.5 g / l of 96% sulfuric acid.

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  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Silver Salt Photography Or Processing Solution Therefor (AREA)
  • Detergent Compositions (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

Die vorliegende Erfindung betrifft ein Verfahren zur Herstellung von Schwefelsäureaddukten des Harnstoffs.The present invention relates to a method for producing sulfuric acid adducts of urea.

Für die Verarbeitung von Silberfarbbleichmaterialien benötigt man in allgemeinen vier Verfahrensstufen:

  • (A) Entwicklung des latenten Silberbildes,
  • (B) Farbbleichung an den metallisches Silber enthaltenden Bildstellen
  • (C) Silberbleichung: Umwandlung des Rest-Silberbildes in komplex lösliche Silberverbindungen
  • (D) Fixierung: Berauslösen und Entfernen aller in Form von Komplexen löslichen Silberrerbindungen,
In general, four processing steps are required to process silver color bleaching materials:
  • (A) development of the latent silver image,
  • (B) Color bleaching at the image areas containing metallic silver
  • (C) Silver bleaching: conversion of the residual silver image into complex soluble silver compounds
  • (D) fixation: removal and removal of all silver bonds that are soluble in the form of complexes,

wobei die Schritte (B) und (C) sowie (B), (C) und (D) im einem einzigen Bad gleichzeitig durchgeführt werden können.wherein steps (B) and (C) and (B), (C) and (D) can be carried out simultaneously in a single bath.

Die für die Farb- und/oder Silberbleichung oder die kombinierte Bleichfixierung verwendeten Zubereitungen (Bäder) sind stark sauer, d.h. weisen einen pH-Wert von unter 2, insbesondere unter 1 auf. Die Einstellung dieses pH-Wertes erfolgt in der Regel mit starken Säuren, in erster Linie Mineralsäuren, wie Salzsäure, Schwefelsäure, Salpeter- oder Phosphorsäure, ferner Sulfaninsäure. Auch mit gewissen starken organischen Säuren, wie etwa p-Toluolsulfosäure, werden gute Resultate erhalten.The preparations (baths) used for the color and / or silver bleaching or the combined bleach-fixation are strongly acidic, i.e. have a pH of less than 2, especially less than 1. This pH is generally set using strong acids, primarily mineral acids, such as hydrochloric acid, sulfuric acid, nitric or phosphoric acid, and also sulfanic acid. Good results are also obtained with certain strong organic acids, such as p-toluenesulfonic acid.

Die bisher für die Bleichbäder am häufigsten verwendeten Mineralsäuren weisen einige wichtige Nachteile auf, die sich für eine allgemeine Verwendung ungünstig auswirken können. So ist z.B. Salzsäure stark flüchtig und wirkt deshalb besonders korrosiv auf z.B. Apparate und Vorrichtungen, in denen die Verarbeitung des photographischen Materials vorgenommen wird. Die meisten Mineralsäuren, mit Ausnahme der Sulfaminsäure sind zudem flüssig. Ihre Verwendung, besonders im Amateurbereich, kann deshalb gewissen Gefahren, z.B. durch Verschütten oder Bruch von Gefässen, mit sich bringen.The mineral acids most commonly used for bleaching baths so far have some important disadvantages that can have an adverse effect on general use. For example, Hydrochloric acid highly volatile and therefore has a particularly corrosive effect on e.g. Apparatus and devices in which the processing of the photographic material is carried out. Most mineral acids, with the exception of sulfamic acid, are also liquid. Their use, especially in the amateur sector, can therefore pose certain dangers, e.g. by spilling or breaking vessels.

Die Verwendung fester an Stelle von flüssigen Säuren ist aus diesem Grunde besonders vorteilhaft.Sie erleichtert die Konfektionierung, den Transport und die Aufbewahrung von Zubereitungen für die Farb-und/oder Silberbleichung. Die an sich geeignete Sulfaminsäure, die leicht in frei fliessender Pulverform hergestellt werden kann, lässt sich in vielen Fällen als Ersatz für flüssige Mineralsäuren verwenden. Ein Nachteil ist jedoch ihre relativ schlechte Löslichkeit in Wasser. Es hat sich ausserdem gezeigt, dass sie mit tertiären Phosphinen, die als Bleichbeschleuniger eingesetzt werden, reagiert und zu instabilen Bleichbädern führt. p-Toluolsulfonsäure, welche ebenfalls in frei fliessender Pulverform eingesetzt werden kann, besitzt eine hohe Wasserlöslichkeit und liefert stabile Bleichbäder. Nachteilig ist ihr gegenüber Mineralsäuren wesentlich höherer Preis, sowie das hohe Molekulargewicht, welches den Einsatz hoher Gewichtsmengen erfordert. Der hohe Kohlenstoffballast der p-Toluolsulfonsäure wirkt sich auch, wegen des hohen Sauerstoffbedarfs in den Abwässern, in oekologischer Hinsicht ungünstig aus.For this reason, the use of solid instead of liquid acids is particularly advantageous because it facilitates the preparation, transport and storage of preparations for color and / or silver bleaching. The sulfamic acid, which is suitable per se and can easily be produced in free-flowing powder form, can in many cases be used as a substitute for liquid mineral acids. One disadvantage, however, is their relatively poor solubility in water. It has also been shown that it reacts with tertiary phosphines, which are used as bleach accelerators, and leads to unstable bleach baths. p-Toluenesulfonic acid, which can also be used in free-flowing powder form, has a high water solubility and provides stable bleaching baths. Disadvantages are the significantly higher price compared to mineral acids, and the high molecular weight, which requires the use of large amounts of weight. The high carbon ballast of p-toluenesulfonic acid also has an adverse ecological impact due to the high oxygen demand in the waste water.

Die Aufgabe der vorliegenden Erfindung ist es, starke Mineralsäuren wie sie bei der Verarbeitung von photographischen Silberfarbbleichmaterialien benötigt werden, in geeigneter Form bereitzustellen, um so die zuvor genannten Nachteile zu überwinden.The object of the present invention is to provide strong mineral acids, as are required in the processing of photographic silver color bleaching materials, in a suitable form in order to overcome the disadvantages mentioned above.

Es wurde nun gefunden, dass man in Bleichbädern für den Silberfarbbleichprozess anstelle von Mineralsäuren Schwefelsäureaddukte des Harnstoffs verwenden kann. Diese Addukte sind fest, von guter Stabilität, hoher Wasserlöslichkeit und sie dissoziieren in wässeriger Lösung leicht in ihre ursprünglichen Bestandteile.It has now been found that in bleaching baths for the silver color bleaching process, sulfuric acid adducts of urea can be used instead of mineral acids. These adducts are solid, of good stability, high solubility in water and they dissociate easily in their original components in aqueous solution.

Gegenstand der vorliegenden Erfindung ist somit ein Verfahren zur Herstellung von Schwefelsäureaddukten des Harnstoffs mit einem Harnstoff-Schwefelsäureverhältnis von 2:1 oder 1:1, dadurch gekennzeichnet, dass man den festen Harnstoff in dem angegebenen Verhältnis in 100-pro-zentige Schwefelsäure einträgt, wobei Eintragsgeschwindigkeit und äussere Kühlung so aufeinander abgestimmt werden, dass die Temperatur während der Mischzeit zwischen 70 und 100°C beträgt, und dass man das so gewonnene neutrale oder saure Harnstoff-Sulfat durch Kühlung in feste Form überführt und gegebenenfalls zerkleinert.The present invention thus relates to a process for the preparation of sulfuric acid adducts of urea with a urea-sulfuric acid ratio of 2: 1 or 1: 1, characterized in that the solid urea is entered in the stated ratio in 100 percent sulfuric acid, where Entry speed and external cooling are coordinated so that the temperature during the mixing time is between 70 and 100 ° C, and that the neutral or acid urea sulfate obtained in this way is converted into solid form by cooling and, if necessary, comminuted.

Besonders gut bekannt sind die Addukte von einem Mol Harnstoff mit 0,5 oder 1 Mol Schwefelsäure. Die Schmelzpunkte dieser Addukte betragen 80 bzw. 70°C. Angaben über die Eigenschaften dieser Addukte, über ihre Stabilität, die Reaktionskinetik in der Schmelze und in wässerigen Lösungen finden sich u.a. bei L.H. Dalman, J.Am.Chem.Soc. 56, 549 (1934) P. Baumgarten, Chem. Ber. 69 1929 (1936), E. Cherbuliez & F. Landolt, Helv. 29, 1438 (1946) und G.M. Schwab & E. Schwab-Agallidis, Angew. Chemie, 65, 418 (1953).The adducts of one mole of urea with 0.5 or 1 mole of sulfuric acid are particularly well known. The melting points of these adducts are 80 and 70 ° C, respectively. Information about the properties of these adducts, their stability, the reaction kinetics in the melt and in aqueous solutions can be found, among others. at L.H. Dalman, J.Am.Chem.Soc. 56, 549 (1934) P. Baumgarten, Chem. Ber. 69 1929 (1936), E. Cherbuliez & F. Landolt, Helv. 29, 1438 (1946) and G.M. Schwab & E. Schwab-Agallidis, Angew. Chemie, 65, 418 (1953).

Die Herstellung der Schwefelsäureaddukte des Harnstoffs erfolgt entweder direkt aus den Komponenten oder deren Lösungen oder auch durch die Einwirkung vom Mineralsäurem auf Cyanamid, wobei sich das letztere zu Harnstoff zersetzt, welcher dann mit der Säure die Additionsverbindung eingeht.The sulfuric acid adducts of urea are prepared either directly from the components or their solutions or also by the action of mineral acid on cyanamide, the latter decomposing to urea, which then forms the addition compound with the acid.

Hinweise auf die Herstellung von Harnstoff-Schwefelsäure-Addukten finden sich u.a. in der deutschen Patentschrift 239 309, der amerikanischen Patentschrift 3 330 864 oder in den 'englischem Patentschriften 196 601 und 1 109 619.Information on the production of urea-sulfuric acid adducts can be found, among others, in German patent specification 239,309, American patent specification 3,330,864 or in 'English patent specifications 196,601 and 1,109,619.

Die erfindungsgemäss hergestellten Addukte sind in fester Form gut haltbar und könnem leicht in Form frei fliessender wasserlöslicher Pulver oder Granulate hergestellt werden.The adducts produced according to the invention are stable in solid form and can easily be prepared in the form of free-flowing water-soluble powders or granules.

Die Addukte des Harnstoffs mit Schwefelsäure existieren in zwei stabilen Formen: Harnstoff-Sulfat, das Addukt von zwei Molen Harnstoff mit einem Mol Schwefelsäure, und Harnstoff-Hydrogensulfat, das Addukt von einem Mol Harnstoff mit einem Mol Schwefelsäure. Beide Formen können erfindungsgemäss nach einem einfachen Herstellungsverfahren direkt in wasserfreier fester Form hergestellt werden;The adducts of urea with sulfuric acid exist in two stable forms: urea sulfate, the adduct of two moles of urea with one mole of sulfuric acid, and urea hydrogen sulfate, the adduct of one mole of urea with one mole of sulfuric acid. According to the invention, both forms can be produced directly in an anhydrous solid form using a simple production process;

Nach diesem Verfahren wird Harnstoff in 100-prozentige Schwefelsäure (Monohydrat) unter Kühlung direkt in fester Form eingetragen, wobei man die Temperatur während der Reaktion nicht über etwa 100°C (vorzugsweise 70°C bis 100°C) steigen lässt. Man erhält auf diese Weise direkt eine Schmelze von Harnstoff-Hydrogensulfat oder Harnstoff-Sulfat, je nachdem ob ein oder zwei Mol Harnstoff pro Mol Schwefelsäure eingetragen wurden. Die Verbindungen werden durch Kühlung im die feste Form überführt und gegebenenfalls zerkleinert.According to this process, urea is introduced directly into solid form in 100% sulfuric acid (monohydrate) with cooling, the temperature not being allowed to rise above about 100 ° C. (preferably 70 ° C. to 100 ° C.) during the reaction. In this way, a melt of urea Hydrogen sulfate or urea sulfate, depending on whether one or two moles of urea have been added per mole of sulfuric acid. The compounds are converted into the solid form by cooling and optionally comminuted.

Bei der Herstellung der genannten Harnstoff-Schwefelsäureaddukte ist es wesentlich, dass eine genau 100- prozentige Schwefelsäure verwendet wird; enthält die Schmelze freies Wasser oder Schwefeltrioxid, so ist die Stabilität der Schmelze deutlich vermindert. Die Schmelze kann durch geeignete Verfahren, wie sie z.B. bei der Herstellung von Alkalihydroxiden verwendet werden (vgl. Ullmanns Encyklopädie der technischen Chemie, 4. Auflage, Verlag Chemie, Weinheim, Bd. 17 (1979), S. 204 f), in eine für die Anwendung geeignete feste Form übergeführt werden. Insbesondere kann sie in der Form von frei fliessenden, in Wasser sofort löslichen Perlen, Pillen, Flocken oder Schuppen kristallisiert werden. In die Form von Perlen kann man die Schwefelsäureaddukte bringen, wenn nan sie z.B. in einem Kühlturm versprüht.When producing the urea-sulfuric acid adducts mentioned, it is essential that exactly 100 percent sulfuric acid is used; If the melt contains free water or sulfur trioxide, the stability of the melt is significantly reduced. The melt can be removed by suitable methods, e.g. used in the production of alkali metal hydroxides (cf. Ullmanns Encyklopadie der Technische Chemie, 4th edition, Verlag Chemie, Weinheim, Vol. 17 (1979), p. 204 f), are converted into a solid form suitable for the application. In particular, it can be crystallized in the form of free-flowing pearls, pills, flakes or flakes that are immediately soluble in water. The sulfuric acid adducts can be brought into the form of beads if they are e.g. sprayed in a cooling tower.

In deh nachfolgendem Beispielem beziehen sich Teile umd Prozente auf das Gewicht, sofern nicht anders angegeben.In the following example, parts and percentages are by weight unless otherwise stated.

Beispiel 1example 1

Ein für die Herstellung von positiven Aufsichtskopien von einer positiven Vorlage geeignetes Material für das Silberfarbbleichverfahren wurde in folgender Weise hergestellt:

  • Auf einen weissopakem Träger werden in der angegebenen Reihenfolge die folgenden Schichteh aufgetragen:
  • Ein rotsensibilisiertes Schichtpaar, bestehend aus
    • 1. einer rotempfindlichen Gelatine-Silberbromidjodid-emulsionsschicht mit einem bleichbarem blaugrünen Azofarbstoff der Formel (101) mit einem Silbergehalt vom 0,144 g Ag/m2
      Figure imgb0001
    • 2. einer von Bildfarbstoff freien Schicht aus einer rotempfindlichem Gelatine-Silberbromidjodid-Emulsion mit einem Silbergehalt vom 0,300 g Ag/m2;
    • 3. eine erste Gelatine-Zwischenschicht;
    • 4. einer grünempfindlichen Gelatine-Silberbromidjodid-Emulsionsschicht mit einem purpurfarbigen bleichbaren Azofarbstoff der Formel (102) und einem Silbergehalt von 0,212 g Ag/m2;
      Figure imgb0002
    • 5. einer von Bildfarbstoff freien Schicht aus einer grünempfindlichem Gelatine-Silberbromidjodid-Emulsion mit einem Silbergehalt von 0,300 g Ag/m2;
    • 6. eine zweite Zwischenschicht, bestehend aus Gelatime mit einem Zusatz von kolloidalem Silber in einer Menge von 0,007 g Ag/m2 und einer nicht spektral sensibilisiertem unempfindlichem Silberbromidemulsion mit einem Silbergehalt vom 0,2 g Ag/m2 ein blauempfindliches Schichtpaar, bestehend aus
    • 7. einer hochempfindlichen jodidfreien Gelatine-Silberbromidschicht mit einem gelben bleichbaren Azofarbstoff der Formel (103) und einem Silbergehalt von 0,360 g Ag/m2:
      Figure imgb0003
    • 8. einer farbstofffreien hochempfindlichen Gelatine-Silberbromidjodidschicht mit niedrigem Jodidanteil mit einem Silbergehalt vom 0,530 g Ag/m2;
    • 9. eine Gelatine-Schutzschicht.
A silver dye bleaching material suitable for making positive overlay copies of a positive original was made in the following manner:
  • The following layers are applied to a white opaque support in the order given:
  • A pair of layers sensitized to red, consisting of
    • 1. a red-sensitive gelatin-silver bromide iodide emulsion layer with a bleachable blue-green azo dye of the formula (101) with a silver content of 0.144 g Ag / m 2
      Figure imgb0001
    • 2. an image dye-free layer of a red-sensitive gelatin-silver bromide iodide emulsion with a silver content of 0.300 g Ag / m2;
    • 3. a first intermediate gelatin layer;
    • 4. a green-sensitive gelatin-silver bromide iodide emulsion layer with a purple-colored bleachable azo dye of the formula (102) and a silver content of 0.212 g Ag / m 2 ;
      Figure imgb0002
    • 5. an image dye-free layer of a green-sensitive gelatin-silver bromide iodide emulsion with a silver content of 0.300 g Ag / m 2 ;
    • 6. a second intermediate layer consisting of gelatin with the addition of colloidal silver in an amount of 0.007 g Ag / m 2 and a non-spectrally sensitized insensitive silver bromide emulsion with a silver content of 0.2 g Ag / m 2 a blue-sensitive layer pair consisting of
    • 7. a highly sensitive iodide-free gelatin-silver bromide layer with a yellow bleachable azo dye of the formula (103) and a silver content of 0.360 g Ag / m 2 :
      Figure imgb0003
    • 8. a dye-free, highly sensitive gelatin-silver bromide iodide layer with a low iodide content with a silver content of 0.530 g Ag / m 2 ;
    • 9. a gelatin protective layer.

Dies Material ist so aufgebaut, dass unter Verarbeitung mit einem einen Silberliganden, insbesondere Natriumthiosulfat enthaltenden Entwickler und dem nachfolgenden für das Silberfarbbleichverfahren notwendigen Verfahrensschritten der Farb- und Silberbleichung, letztere vorzugsweise in einem einzigen Schritt zusammengefasst, und schliesslich der Fixierung, eine Maskierung der blauen Nebenfarbdichten der Purpur- und Blaugrünschicht bewirkt wird.This material is constructed in such a way that, when processed with a developer containing a silver ligand, in particular sodium thiosulfate, and the subsequent process steps of color and silver bleaching necessary for the silver color bleaching process, the latter preferably combined in a single step, and finally the fixation, a masking of the blue secondary color densities the purple and cyan layer is effected.

Von diesem photographischen Material wird ein Probestreifem geschnitten und hinter einem Graukeil wie folgt additiv belichtet:

  • Rotbelichtung: 4 Sekunden
  • Grünbelichtung: 17 Sekunden
  • Blaubelichtung: 4 Sekundem
A sample strip is cut from this photographic material and exposed additively behind a gray wedge as follows:
  • Red exposure: 4 seconds
  • Green exposure: 17 seconds
  • Blue exposure: 4 seconds

Zur Verarbeitung des belichteten Teststreifens wurdem folgende Verarbeitungslösungen in der angegebenen Reihenfolge verwendet:

  • 1. Silberentwicklungsbad 2,5 Minutem Temp. 32°C
    • Natriumpolyphosphat 1 (g/l)
    • Kaliumhydroxid (85%) 27 (g/l)
    • Borsäure 21 (g/l)
    • Kaliummetabisulfit 18 (g/l)
    • Natriunsulfit, wasserfrei 11 (g/l)
    • 1-Phenyl-3-pyrazolidon 0,3 (g/l)
    • Hydrochinon 5 (g/l)
    • Benztriazol 0,6 (g/l)
    • Kaliumbromid 2 (g/l)
    • Natriumthiosulfat, wasserfrei 1,0 (g/l)
  • 2. Wässerung 1 Minute
  • 3. Bleichbad 2,5 Minutem
    • Addukt A. und B. (siehe nachfolgende Tabelle)
    • m-Nitrobenzolsulfonsäure -Na-Salz 7,5 (g/l)
    • Kaliumjodid 5 (g/l)
    • 2,3,6-Trimethylchinoxalin 1,5 (g/l)
    • Bis-(cyanoäthyl)-sulfobutylphosphin (Na-Salz) 4 (g/l)
      Figure imgb0004
  • 4. Wässerung 1 Minute
  • 5. Fixierbad 2,5 Minuten
    • Ammoniumthiosulfat 250 g/1
    • Kaliummetabisuifit 50 g/I
    • Kaliumhydroxid (85%) 20 g/1
  • 6. Wässerung 3 Minuten
    • Totale Verarbeitungszeit 12,5 Minutem
The following processing solutions were used in the order given to process the exposed test strip:
  • 1. Silver developing bath 2.5 minutes at 32 ° C
    • Sodium polyphosphate 1 (g / l)
    • Potassium hydroxide (85%) 27 (g / l)
    • Boric acid 21 (g / l)
    • Potassium metabisulfite 18 (g / l)
    • Sodium sulfite, anhydrous 11 (g / l)
    • 1-phenyl-3-pyrazolidone 0.3 (g / l)
    • Hydroquinone 5 (g / l)
    • Benzotriazole 0.6 (g / l)
    • Potassium bromide 2 (g / l)
    • Sodium thiosulfate, anhydrous 1.0 (g / l)
  • 2. Soak for 1 minute
  • 3. Bleaching bath 2.5 minutes
    • Adduct A. and B. (see table below)
    • m-nitrobenzenesulfonic acid Na salt 7.5 (g / l)
    • Potassium iodide 5 (g / l)
    • 2,3,6-trimethylquinoxaline 1.5 (g / l)
    • Bis- (cyanoethyl) sulfobutylphosphine (Na salt) 4 (g / l)
      Figure imgb0004
  • 4. Soak 1 minute
  • 5. Fixer bath 2.5 minutes
    • Ammonium thiosulfate 250 g / 1
    • Potassium metabisuifit 50 g / I
    • Potassium hydroxide (85%) 20 g / 1
  • 6. Soak 3 minutes
    • Total processing time 12.5 minutes

Nach der anschliessenden Trocknung erhält man positive Graukeile, die über dem ganzen Dichtebereich einen gleichmässigen neutralgrauen Farbton aufweisen, mit Dmax-Werten von 1,77 (grau) und-Dmin-Werten von 0,03 (grau).After the subsequent drying, positive gray wedges are obtained which have a uniform neutral gray shade over the entire density range, with Dmax values of 1.77 (gray) and D min values of 0.03 (gray).

Eine Beeinträchtigung der Bildqualität bei Verwendung der erfindungsgemässem Addukte A. und B. anstelle der bisher üblichen freien Schwefelsäure wird nicht festgestellt.An impairment of the image quality when using the adducts A. and B. according to the invention instead of the previously customary free sulfuric acid is not found.

Beispiel 2Example 2

In diesem Beispiel wird, umter Verwendung der gleichem Farbstoffe wie im Beispiel 1, ein sechsschichtiges Material verwendet, welches in der ersten Schicht dem Blaugrün-Farbstoff und die zugeordnete rotsemsibilisierte Silberhalogenidenulsion, als zweite Schicht eine dünne, reine Gelatine enthaltende Zwischenschicht, in der dritten Schicht den Purpurfarbstoff mit der zugeordneten grünsensibilisierten Silberhalogenidemulsion, als vierte Schicht eine aus Gelatine bestehende Zwischenschicht, als 5. Schicht eine einen gelben Farbstoff enthaltende Silberhalogenidschicht und schliesslich als sechste Schicht eine Schutzschicht aus reiner Gelatine enthält.In this example, using the same dyes as in Example 1, a six-layer material is used which in the first layer contains the cyan dye and the associated red-sensitized silver halide emulsion, and in the second layer a thin, pure gelatin-containing intermediate layer in the third layer contains the purple dye with the associated green-sensitized silver halide emulsion, the fourth layer is an intermediate layer consisting of gelatin, the fifth layer contains a silver halide layer containing a yellow dye and finally the sixth layer contains a protective layer of pure gelatin.

Für die Verarbeitung dieses Materials wird ein sog. Zweibadverfahren gewählt, bestehend aus einem Entwicklerbad und einem nachfolgenden kombinierten Bad, in welchem die Farbstoff- und Silberbleichung und die Fixierung praktisch gleichzeitig erfolgen. Das Silberentwicklungsbad besitzt folgende Zusammensetzung:

  • Silberentwicklung 6 Minuten
  • Na-Polyphosphat 1 (g/l)
  • Na Sulfit, wasserfrei 50 (g/l)
  • Hydrochinon 5 (g/l)
  • Na-Metaborat 15 (g/l)
  • 1-Phenyl-3-pyrazolidon 0,3 (g/I)
  • Kaliumbromid 3 (g/l)
  • Benztriazol 0,2 (g/l)
  • Das kombinierte Bleich- und Fixierbad besitzt folgende Zusammensetzung:
  • Kombiniertes Bleich- und Fixierbad
  • Thioharnstoff-Schwefelsäure-Addukt (1:1) 16 g/l
  • Thioharnstoff 7 g/l
  • m-Nitrobenzolsulfonsäure, (Natriumsalz) 0,8 g/l
  • 1-Phenyl-2-methyl-6,7-dimethoxy-chinoxalin 0,5 g/l
  • Kaliumjodid 3 g/l
For the processing of this material, a so-called two-bath process is selected, consisting of a developer bath and a subsequent combined bath, in which the dye and silver bleaching and the fixing take place practically simultaneously. The silver development bath has the following composition:
  • Silver development 6 minutes
  • Na polyphosphate 1 (g / l)
  • Na sulfite, anhydrous 50 (g / l)
  • Hydroquinone 5 (g / l)
  • Na metaborate 15 (g / l)
  • 1-phenyl-3-pyrazolidone 0.3 (g / l)
  • Potassium bromide 3 (g / l)
  • Benzotriazole 0.2 (g / l)
  • The combined bleaching and fixing bath has the following composition:
  • Combined bleaching and fixing bath
  • Thiourea-sulfuric acid adduct (1: 1) 16 g / l
  • Thiourea 7 g / l
  • m-nitrobenzenesulfonic acid, (sodium salt) 0.8 g / l
  • 1-phenyl-2-methyl-6,7-dimethoxy-quinoxaline 0.5 g / l
  • Potassium iodide 3 g / l

Ein zweiter Probestreifen wird in identischer Weise belichtet und verarbeitet, wobei jedoch ein kombiniertes Bleich- und Fixierbad verwendet wird, das 9,5 g/l 96%-iger Schwefelsäure enthält.A second sample strip is exposed and processed in an identical manner, but using a combined bleaching and fixing bath which contains 9.5 g / l of 96% sulfuric acid.

Die fertig verarbeiteten und getrockneten Probestreifen ergeben je einen positiven Graukeil mit identischen sensitometrischen Werten. Die gemessenen Dichten (Remissionswerte) betragen:

  • Dmax Dmin
  • Rot 1,75 0,05
  • Grün 1,91 0,02
  • Blau 1,97 0,02
The finished and dried test strips each result in a positive gray wedge with identical sensitometric values. The measured densities (reflectance values) are:
  • D ma x D min
  • Red 1.75 0.05
  • Green 1.91 0.02
  • Blue 1.97 0.02

Claims (1)

1. A process for the preparation of an adduct of sulfuric acid and urea, with a urea/sulfuric acid ratio of 2:1 or 1:1, which process comprises introducing the solid urea in the indicated ratio into 100% sulfuric acid, the rate at which the urea is introduced and the external cooling being so matched that during the mixing period the temperature is in the range from 70° to 100° C, and converting the resultant neutral or acid urea-sulfate into the solid form by cooling, and, if desired, comminuting the solid.
EP84108556A 1980-02-22 1981-02-17 Process for the production of sulfuric-acid adducts of urea Expired EP0131970B1 (en)

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CH143580 1980-02-22

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US5374608A (en) * 1981-11-05 1994-12-20 Union Oil Company Of California Compositions containing adducts and surfactants
US5411944A (en) * 1981-11-05 1995-05-02 Union Oil Company Of California Glyphosate-sulfuric acid adduct herbicides and use
US5116401A (en) * 1981-11-05 1992-05-26 Union Oil Company Of California Herbicide and method with the glyphosate-urea adduct of sulfuric acid
US5149355A (en) * 1981-11-05 1992-09-22 Union Oil Company Of California Adduct compositions
US5288692A (en) * 1982-11-17 1994-02-22 Union Oil Company Of California Systemic herbicides and methods of use
EP0149978A3 (en) * 1984-01-20 1988-08-31 Ciba-Geigy Ag Process for the production of photographic images by the silver dye-bleaching process
JPH07122751B2 (en) * 1988-04-28 1995-12-25 富士写真フイルム株式会社 Bleach-fix solution concentrate composition for silver halide color photographic light-sensitive material and processing method
EP0351740A1 (en) * 1988-07-19 1990-01-24 Konica Corporation Method for preparing color filter and color filter prepared by the method
US4962283A (en) * 1989-02-28 1990-10-09 Union Oil Company Of California Single pass continuous urea-sulfuric acid process
JPH0432837A (en) * 1990-05-29 1992-02-04 Fuji Photo Film Co Ltd Vacuum packaged photographic processing agent
US5238905A (en) * 1991-10-28 1993-08-24 Union Oil Company Of California Plant control composition and methods of use with thidiazuron and monocarbamide dihydrogen sulfate
US5221659A (en) * 1991-10-28 1993-06-22 Union Oil Company Of California Plant control composition and methods of use
US5262285A (en) * 1992-05-04 1993-11-16 Eastman Kodak Company Methods and compositions for retouching film images
RU2101293C1 (en) * 1992-12-25 1998-01-10 Товарищество с ограниченной ответственностью "Эфиры целлюлозы" Method of synthesis of cellulose ester
WO1996006672A1 (en) * 1994-08-26 1996-03-07 Us Sulfamate, Inc. Molten urea dehydrate derived compositions

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US3330864A (en) * 1965-04-29 1967-07-11 Conversion Chem Corp Method for making urea nitrate
DE1935705A1 (en) * 1968-07-16 1970-03-19 Fuji Photo Film Co Ltd Process for the production of color photographic images
GB1397945A (en) * 1972-05-04 1975-06-18 Ici Ltd Process for the manufacture of inorganic acid addition salts of urea
CH579292A5 (en) * 1973-05-18 1976-08-31 Ciba Geigy Ag
US4116664A (en) * 1976-11-04 1978-09-26 Jones Leon R Fertilizer composition and method of making same
CH644459A5 (en) * 1978-09-29 1984-07-31 Ciba Geigy Ag METHOD FOR PRODUCING COLOR PHOTOGRAPHIC IMAGES AFTER THE SILVER COLORING METHOD.
US4310343A (en) * 1979-11-27 1982-01-12 Verdegaal Bros. Fertilizer Process for making liquid fertilizer

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JPH0133820B2 (en) 1989-07-14
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JPS56132340A (en) 1981-10-16
DE3170675D1 (en) 1985-07-04
EP0034793A2 (en) 1981-09-02
US4879413A (en) 1989-11-07
EP0131970A1 (en) 1985-01-23
EP0034793B1 (en) 1985-05-29

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