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 PDF

Info

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
Authority
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.)
Withdrawn
Application number
FR8316100A
Other languages
French (fr)
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to FR8316100A priority Critical patent/FR2554614A1/en
Publication of FR2554614A1 publication Critical patent/FR2554614A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C7/00Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
    • C25C7/06Operating or servicing

Landscapes

  • 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

The invention is principally in the field of recovery electrolysis. It makes it possible to modify the sporadic flow rate of a removed liquid in order to permit optimum treatment of it in a sequential form (the latter being imperative). During the time necessary for treatment of the liquid given off, a solenoid valve prevents admission of new liquid by trapping it in a buffer vessel. The start of the cycle, controlled by a level detector, starts up for a time which is programmed according to requirements until removal of the treated liquid before restarting a new cycle. Various additions make it possible to vary the processing times or on their time lag. The invention is suitable for permitting complete electrolytic recovery from erratic flow rates (for example).

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)

REVENDICATIONS 1") Procédé de transformation d'un débit de liquide naturellement variable en débit séquentiel, caractérisé par l'utilisation de deux bacs superposés. 1 ") Process for transforming a naturally variable liquid flow into a sequential flow, characterized by the use of two superimposed tanks. reliés l'un à l'autre par une électro-vanne; celle-ci, ouverte en temps normal se ferme quand un détecteur de niveau le commande à partir d'un niveau de liguide atteint dans le bac secondaire; la fermeture de cette électro-vanne déclenche également un cycle de traitement et d'évacuation avant de revenir au point d'attente du départ dgun nouveau cycle.connected to each other by a solenoid valve; the latter, normally open, closes when a level detector commands it from a liquid level reached in the secondary tank; closing this solenoid valve also triggers a treatment and evacuation cycle before returning to the waiting point for the start of a new cycle. 2") Procédé de transformation d'un débit contiu en débit séquentiel selon la revendication n"l, caractérisé en ce qu'il permet l'utilisation de trois paramètres impossible à maitriser en traitement continu : une minuteSEe permettant d'intervenir sur le temps d'électrolyse, un éostat permettant d'intervenir sur l'intensité du courant d'électrolyse, le positionnement de l'électro-vanne d'évacuation permettant d'agir sur la concentration du produit à traiter en ions métalliques.  2 ") Method for transforming a continuous flow into a sequential flow according to claim n" l, characterized in that it allows the use of three parameters which are impossible to control in continuous processing: one minuteSEe allowing intervention on time electrolysis, a pressure switch to intervene on the intensity of the electrolysis current, the positioning of the evacuation solenoid valve to act on the concentration of the product to be treated in metal ions.
FR8316100A 1983-10-06 1983-10-06 Method permitting sequential processing of liquids, principally by electrolysis, whatever the variations in arrival flow rate Withdrawn FR2554614A1 (en)

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
FR (1) FR2554614A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Patent Citations (4)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
US4141312A (en) Apparatus for histological tissue processing
US5146843A (en) Apparatus for thawing frozen food
US3280716A (en) Method of and apparatus for processing photographic materials
EP0548242B1 (en) Water treatment process by electrolysis, in particular, for water decarbonation, and apparatus for carrying out this process
FR2554614A1 (en) Method permitting sequential processing of liquids, principally by electrolysis, whatever the variations in arrival flow rate
ES8100093A1 (en) Method of cleaning a cold trap for liquid metals, and device for carrying out this method.
JPS5851828B2 (en) Gravure cylinder - Senjiyousouchi
US4234429A (en) System for separating particulate matter into soluble and insoluble portions
JPS5494170A (en) Wet process treatment method for recovering oil from oil-containing hot rolled sludge
EP0084476B1 (en) Apparatus for the treatment of liquids by an ion-exchange resin, in particular a domestic water softener
US4561957A (en) Electrolytic silver recovery system
CN216377768U (en) Portable treatment device for mercury-containing waste liquid of seawater matrix
JPS5570559A (en) Planetary revolution type barreling device having tiltable barrel
CN209451353U (en) A kind of biological medicine feeding device
SU125406A1 (en) Instrument for the classification of fine powders
JPS56115936A (en) Sampling device for sample water
Huang et al. Effect of Complex Formation on the Removal of Heavy Metals From Water and Wastewater
RU36825U1 (en) DEVICE FOR ELECTROCHEMICAL CLEANING OF DRINKING WATER
RU2092616C1 (en) Method of processing metal gold-containing concentrate
CN206378439U (en) A kind of rapeseed oil impurity detection device
SU803950A1 (en) Method of carrying out in ion exchange process
SU841647A1 (en) Device for cleaning spent solutions of powderless etching
JPH06125693A (en) Method for removing salt from salted food
JPH07179884A (en) Apparatus for reclaiming edible oil from used edible oil
DE915630C (en) Method of filling contact thermometer tubes

Legal Events

Date Code Title Description
ST Notification of lapse