FR2554614A1 - Method permitting sequential processing of liquids, principally by electrolysis, whatever the variations in arrival flow rate - Google Patents
Method permitting sequential processing of liquids, principally by electrolysis, whatever the variations in arrival flow rate Download PDFInfo
- Publication number
- FR2554614A1 FR2554614A1 FR8316100A FR8316100A FR2554614A1 FR 2554614 A1 FR2554614 A1 FR 2554614A1 FR 8316100 A FR8316100 A FR 8316100A FR 8316100 A FR8316100 A FR 8316100A FR 2554614 A1 FR2554614 A1 FR 2554614A1
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- FR
- France
- Prior art keywords
- electrolysis
- liquid
- solenoid valve
- principally
- flow rate
- 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.)
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Classifications
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C7/00—Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
- C25C7/06—Operating or servicing
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Metals (AREA)
Abstract
Description
La présente invention concerne le domaine technique de l'électrolyse de récupératio utilisée en photographie et en radiologie et où il est nécessaire à la complète récupération de maintenir un certain volume de liquide pendant un temps déterminé dans une zone de traitement alors rrcême que le débit du liquide en maont de la cuve d'électrolyse est variable.The present invention relates to the technical field of recovery electrolysis used in photography and in radiology and where it is necessary for complete recovery to maintain a certain volume of liquid for a determined time in a treatment area then rrcme that the flow of liquid upstream of the electrolytic cell is variable.
Dans certains dispositifs antérieurs 1 'aspect continu de 'électrolyse se caractérisait par le fait que l'admission d'une certaine quantité de liquide à électrolyse entraînait l'évacuation simultanée par trop-plein dune quantité égale de liquide.In certain prior devices, the continuous aspect of electrolysis was characterized by the fact that the admission of a certain quantity of liquid to electrolysis resulted in the simultaneous evacuation by overflow of an equal quantity of liquid.
L'inadaptation aux variations de débit contraignait à l'utilisation d'un ampérage faible pour éviter les sulfurations aux moments de faible débit avec, en corollaire, une récupération seulement partielle aux moments de fort débit.The unsuitability for variations in flow forced the use of low amperage to avoid sulfurization at times of low flow with, as a corollary, only partial recovery at times of high flow.
Dans d'autres dispositifs antérieures la transformation de liarrivée erratique du liquide à traiter ne supprimait pas l'élimination par trop-plein d'une certaine quantité de liquide non encore traite par électrolyse.In other prior devices the transformation of the erratic arrival of the liquid to be treated did not eliminate the elimination by overflow of a certain quantity of liquid not yet treated by electrolysis.
Le problème technique à résoudre était de transformer 1 'arrivée variable du liquide à électrolyser en traitement séquentiel sans permettre l'évacuation de liquide non traité ou insuffisemment traité. La rapidité souhaitable de l'électrolyse entraîne l'utilisation d'un ampérage relativement élevé et, pour éviter en contrecoup des manifestations chimiques secondaires, la rotation de la cathode.Ce mouvement de rotation de la cathode étant susceptible de gèner les utilisateurs par son bruit, un dispositif de retard d'exécution sera joint chaque fois que ce sera souhaitable,
Pour résoudre ce problème', le liquide à traiter est admis dans la cuve d'électrolyse par séquences d'une duree règlable d'un temps nécessaire au retrait de la totalité du métal à récupérer pendant que le liquide ultérieurement admis est stocké dans un bac tampon.The technical problem to be solved was to transform the variable inlet of the liquid to be electrolyzed into sequential treatment without allowing the evacuation of untreated or insufficiently treated liquid. The desirable rapidity of electrolysis leads to the use of a relatively high amperage and, in order to avoid secondary chemical manifestations, rotation of the cathode. This rotation movement of the cathode being liable to annoy users by its noise , a delay device will be attached whenever it is desirable,
To solve this problem, the liquid to be treated is admitted into the electrolysis tank in sequences of a duration adjustable from a time necessary for the withdrawal of all of the metal to be recovered while the liquid subsequently admitted is stored in a tank. buffer.
Pour ce faire, le liquide pénètre dans l'appareil, traverse par gravité le premier bac (tampon) séparé de la cuve à électrolyse par une électro-vanne n"1 en position ouverte.To do this, the liquid enters the device, passes by gravity through the first tank (buffer) separated from the electrolysis tank by a solenoid valve n "1 in the open position.
La montée du niveau du liquide dans la cuve à électrolyse déclenche, quand la quantité pré-déterminée est atteinte, le cycle d'opérations suivant 1") fermeture de l'électro-vanne n01; 20) mise en route du moteur de rotation de cathode et de la fonction électrolyse pour une durée pré-programmée sur minuterie en fonction de la teneur de l'électrolytr en métal; 3 ) éventuellement mise en route du différé de démarrage de rotation de la cathode et de la fonction électrolyse;; 4 ) sinon, aLrèt de la fonction électrolyse et de la rotation de la cathode après temporisation nécessaire, 50) ouverture de l'électrovanne n"2 et évacuation par gravité du liquide dekaréssé en totalité du métal initialement contenu; 6 ) fermeture de l'électro-vanne n 2 rendant opérationnelle la cuve à électrolyse; 7 ) ouverture de l'électro-vanne n01 et recommencement du cycle.The rise in the level of the liquid in the electrolysis tank triggers, when the predetermined quantity is reached, the following operating cycle 1 ") closing of the solenoid valve n01; 20) starting the rotation motor cathode and the electrolysis function for a duration pre-programmed on a timer depending on the metal content of the electrolytr; 3) possibly starting the delayed start of rotation of the cathode and the electrolysis function ;; 4) otherwise, when the electrolysis function and cathode rotation have stopped after the required time delay, 50) opening of the solenoid valve no. 2 and evacuation by gravity of the dekaréssé liquid in all of the metal initially contained; 6) closing of the electrovalve n 2 making the electrolysis tank operational; 7) opening of solenoid valve n01 and restarting the cycle.
I1 y a évidemment adéquation entre le volume du bac tampon et le temps d'électrolyse.There is obviously a match between the volume of the buffer tank and the electrolysis time.
Ce procédé, objet de l'invention, peut être utilisé dans tous les cas où il est nécessaire de transformer l'arrivée sporadique d'un liquide en mouvement permettant le traitement sequentiel dudit liquide.This process, object of the invention, can be used in all cases where it is necessary to transform the sporadic arrival of a moving liquid allowing the sequential processing of said liquid.
Des applications particulièrement intéressantes peuvent être trouvées dans le dcmaine de la récupération de l'argent-métal dans les bains de fixateur utilisés en photogrphie et en radiologie. Particularly interesting applications can be found in the field of silver-metal recovery in fixative baths used in photography and radiology.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8316100A FR2554614A1 (en) | 1983-10-06 | 1983-10-06 | Method permitting sequential processing of liquids, principally by electrolysis, whatever the variations in arrival flow rate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8316100A FR2554614A1 (en) | 1983-10-06 | 1983-10-06 | Method permitting sequential processing of liquids, principally by electrolysis, whatever the variations in arrival flow rate |
Publications (1)
Publication Number | Publication Date |
---|---|
FR2554614A1 true FR2554614A1 (en) | 1985-05-10 |
Family
ID=9292981
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR8316100A Withdrawn FR2554614A1 (en) | 1983-10-06 | 1983-10-06 | Method permitting sequential processing of liquids, principally by electrolysis, whatever the variations in arrival flow rate |
Country Status (1)
Country | Link |
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FR (1) | FR2554614A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0627504A1 (en) * | 1993-05-08 | 1994-12-07 | Eastman Kodak Company | Method and apparatus for controlling electrolytic silver recovery for two film processing machines |
AU678615B2 (en) * | 1993-11-13 | 1997-06-05 | Mintek | A process for controlling a series of flotation cells |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2061668A1 (en) * | 1969-09-11 | 1971-06-25 | Photographic Silver Reco | |
GB1445960A (en) * | 1975-07-10 | 1976-08-11 | Pennellier Co Ltd D | Apparatus for recovering material from liquid waste |
GB2067598A (en) * | 1980-01-17 | 1981-07-30 | Photographic Silver Recovery | Electrolytic recovery of silver |
EP0094275A1 (en) * | 1982-04-30 | 1983-11-16 | Jean Pierre Martineau | Apparatus for the continuous electrolytic recovery of metals from the processing baths of machines for developing sensitive surfaces |
-
1983
- 1983-10-06 FR FR8316100A patent/FR2554614A1/en not_active Withdrawn
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2061668A1 (en) * | 1969-09-11 | 1971-06-25 | Photographic Silver Reco | |
GB1445960A (en) * | 1975-07-10 | 1976-08-11 | Pennellier Co Ltd D | Apparatus for recovering material from liquid waste |
GB2067598A (en) * | 1980-01-17 | 1981-07-30 | Photographic Silver Recovery | Electrolytic recovery of silver |
EP0094275A1 (en) * | 1982-04-30 | 1983-11-16 | Jean Pierre Martineau | Apparatus for the continuous electrolytic recovery of metals from the processing baths of machines for developing sensitive surfaces |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0627504A1 (en) * | 1993-05-08 | 1994-12-07 | Eastman Kodak Company | Method and apparatus for controlling electrolytic silver recovery for two film processing machines |
AU678615B2 (en) * | 1993-11-13 | 1997-06-05 | Mintek | A process for controlling a series of flotation cells |
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