FR2608587A1 - Process for the purification of industrial effluents using "lithotamnium calcareum" - Google Patents

Process for the purification of industrial effluents using "lithotamnium calcareum" Download PDF

Info

Publication number
FR2608587A1
FR2608587A1 FR8617719A FR8617719A FR2608587A1 FR 2608587 A1 FR2608587 A1 FR 2608587A1 FR 8617719 A FR8617719 A FR 8617719A FR 8617719 A FR8617719 A FR 8617719A FR 2608587 A1 FR2608587 A1 FR 2608587A1
Authority
FR
France
Prior art keywords
calcareum
purification
column
lithotamnium
effluents
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.)
Granted
Application number
FR8617719A
Other languages
French (fr)
Other versions
FR2608587B3 (en
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.)
Timac SA
Original Assignee
Timac SA
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 Timac SA filed Critical Timac SA
Priority to FR8617719A priority Critical patent/FR2608587B3/en
Publication of FR2608587A1 publication Critical patent/FR2608587A1/en
Application granted granted Critical
Publication of FR2608587B3 publication Critical patent/FR2608587B3/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/281Treatment of water, waste water, or sewage by sorption using inorganic sorbents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/286Treatment of water, waste water, or sewage by sorption using natural organic sorbents or derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/006Radioactive compounds

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Removal Of Specific Substances (AREA)

Abstract

The process for purification of industrial effluents involves passing these industrial effluents through a column of screened and dried Lithotamnium Calcareum, which has a particle size of between 10 mm and 0.1 mm. The industrial effluent capable of being treated by this process may contain one or more of the following ions: nickel, zinc, copper, cadmium, iron, indium, manganese, molybdenum, cobalt, ruthenium, titanium, phosphate, sulphate, fluoride, iodide, caesium.

Description

Le procédé consiste en l'élimination d'un ou plusieurs compose indésirables dans les effluents d'origine industrielle Cette épuration est effectuée par le passage des effluents industriels dans une colonne contenant du Lithotamnium Calcareum criblé. séché. ayant une granulométrie comprise entre 0,1 mm et 10 mm. The process consists in the elimination of one or more undesirable compounds in the effluents of industrial origin. This purification is carried out by the passage of industrial effluents in a column containing screened Lithotamnium Calcareum. dried. having a particle size between 0.1 mm and 10 mm.

L'utilisation de ce produit est connue pour la desacidification des eaux potables, mais jamais un procédé mettent en jeu ce produit n'avait été réalisé pour traiter des effluents industriels pollués par les cations suivants nickel, zinc, cuivre, cadmium fer indium, manganèse.  The use of this product is known for the deacidification of drinking water, but never a process involve this product had not been carried out to treat industrial effluents polluted by the following cations nickel, zinc, copper, cadmium iron indium, manganese .

molybdène, cobalt, ruthenium, titane, césium et les anions suivants phosphate, sulfate, fluorure, iodure.molybdenum, cobalt, ruthenium, titanium, cesium and the following anions phosphate, sulfate, fluoride, iodide.

Le Lithotamnium Calcareum est une algue calcifièe provenant de la calcification des familles suivantes les Cryptonèmiales. lei Corallinacbes et les Melobosiees, dont les principaux constituent. sont les suivants
- Carbonate de calcium 84 S + ou - 4 S
- Carbonate de magnesium 1 11% + ou - 3
- Soufre 0,6 S + ou - 0.2 %
- Phosphore 0.35 .S + ou - 0.1 %
-Chlore 0,2% + ou - 0,15%
-Potassium 0.2',, + ou - 0.15 t-
-Sodium u.17 + ou - 0.1 -t' et de caractéristiques physiques suivantes
Le produi't-naturel, pour être efficace. doit etre crible et seche le manière â ce que les effluents industriels soient en contact intime avec lui
La densité apparente est comprise entre 1,04 et 1 1,0s, la densite réelle étant de 2,7 Ce produit a une treks grande porosité. c'est en particulier cette caractéristique qui explique ses performances supérieures comparées au produit de nature chimique similaire utilise antérieurement.
Lithotamnium Calcareum is a calcified alga from the calcification of families following the Cryptonemales. lei Corallinacbes and Melobosiees, the main ones of which are. are the following
- Calcium carbonate 84 S + or - 4 S
- Magnesium carbonate 1 11% + or - 3
- Sulfur 0.6 S + or - 0.2%
- Phosphorus 0.35 .S + or - 0.1%
-Chlore 0.2% + or - 0.15%
-Potassium 0.2 ',, + or - 0.15 t-
-Sodium u.17 + or - 0.1 -t 'and with the following physical characteristics
The natural product, to be effective. must be screened and dried so that industrial effluents are in intimate contact with it
The bulk density is between 1.04 and 1.0s, the actual density being 2.7. This product has very high porosity. it is in particular this characteristic which explains its superior performance compared to the product of similar chemical nature used previously.

Les dimensions du produit naturel peuvent aller Jusqu a 5 cm et plus. Nous avons expliqué que la mise en oeuvre du produit qui permet d'obtenir de bons résultats nécessite un séchage et un criblage du
Lithotamnium Calcareum pour avoir une granulométrie comprise entre 0,1 mm et 10 mm et nous avons constaté que les résultats étaient encore meilleurs pour un criblage compris entre 0,5 et 4 mm.
The dimensions of the natural product can range up to 5 cm and more. We have explained that the implementation of the product which makes it possible to obtain good results requires drying and screening of the
Lithotamnium Calcareum to have a particle size between 0.1 mm and 10 mm and we found that the results were even better for a screening between 0.5 and 4 mm.

Le passage de lteffluent s'effectue dans une colonne garnie de
Lithotamnium Calcareum . La structure micro poreuse du produit ainsi que la granulométrie permettent d'obtenir un produit efficace. utilisable industriellement. ce qui n'est pas. le cas avec les produit tels que la chaux. la dolomie. ou la giobertite qui bien qu'utilisés actuellement industriellement se colmatent des la mise en service ou créent une route
Dur laquelle ruisselle l'effluent conduisant à une epuration peu performante.
The passage of the effluent takes place in a column lined with
Lithotamnium Calcareum. The micro-porous structure of the product as well as the particle size make it possible to obtain an effective product. industrially usable. which is not. the case with products such as lime. dolomite. or giobertite which, although currently used industrially, clogs up when put into service or creates a road
During which the effluent flows, leading to an ineffective purification.

L'une des caractéristiques du produit est sa capacité a conserver les impuretes épurées sans les relacher par lixivation
Le procedé met en oeuvre une colonne contenant le Lithotammum Calcareum.
One of the characteristics of the product is its capacity to preserve the purified impurities without loosening them by leaching.
The process uses a column containing the Lithotammum Calcareum.

Le débit du passage des effluents sera fonction de la charge en impuretés des effluents . A titre indicatif une colonne contenant 1 m3 de
Lithotamnium calcereum pourra ëtre traversee par un effluent avec un débit d' 1 m3 heure. Dans le cas de charge faible. le débit pourra etre de 10 m3 heure. et dans le cas de charge plus importante il pourra être reduit jusqu'à 0.2 m3 heure.
The flow rate of the effluent passage will depend on the load of impurities in the effluents. As an indication, a column containing 1 m3 of
Lithotamnium calcereum can be crossed by an effluent with a flow of 1 m3 per hour. In the case of low load. the flow rate could be 10 m3 per hour. and in the case of a higher load it can be reduced up to 0.2 m3 an hour.

EXEMPLE I Installation de traitement de surface avant peintures utilisant des agents de phosphatations cristallines. EXAMPLE I Installation for surface treatment before paints using crystalline phosphating agents.

De manière a ce que les couches de peinture puissent adhérer -sur les surfaces metalliques acier. aluminium. zinc. il est nécessaire de procéder à la phosphatation de ces surfaces. Cette phosphatation peut effectuer dans des bains dits de pnosphatation cristalline contenant lei ions suivants phosphate. zinc. nickel, fer, titane. manganese. Les produits usages ainsi que les eaux de rincage sont rejetés et de ce fait les phosphates. le zinc. le nickel et le fer doivent être eliminés.Cette opération est effectue par passage dans une colonne de 10 mi de
Lithotamnium Calcareum de 1,8 m de diamètre et 4 m de heuteur ave- un debit du passage de l'effluent de 2 m3/Heure et de granulometrie comprise entre 0,2' mm et 4 mm.
In such a way that the paint layers can adhere to the metallic steel surfaces. aluminum. zinc. it is necessary to carry out the phosphating of these surfaces. This phosphating can take place in so-called crystalline phosphating baths containing the following phosphate ions. zinc. nickel, iron, titanium. manganese. Used products as well as rinsing water are rejected and therefore phosphates. zinc. nickel and iron must be removed. This is done by passing through a 10 mi column.
Lithotamnium Calcareum, 1.8 m in diameter and 4 m in height, with an effluent flow of 2 m3 / hour and with a particle size between 0.2 'and 4 mm.

Le procédé permet d'obtenir les résultats de decontamination suivants
Teneur en ppm Teneur en ppm
avant traitement apres traitement
Fer 25 1
Nickel 24 2
Zinc 55 0,3
Phosphate 72r 42
Titane 12 4 Manganèse 1 7
On note la capacite du produit a effectuer une décontamination simultanee de six constituants.
The process provides the following decontamination results
Content in ppm Content in ppm
before treatment after treatment
Iron 25 1
Nickel 24 2
Zinc 55 0.3
Phosphate 72r 42
Titanium 12 4 Manganese 1 7
The capacity of the product to carry out a simultaneous decontamination of six components is noted.

EXEMPLE 2 Installation de traitement de surface avant peintures utilisant des agents de phosphatations amorphes.EXAMPLE 2 Installation for surface treatment before paints using amorphous phosphating agents.

En utilisant une installation comprenant une colonne de 10 m3 de
Lithotamnium Calcareum criblé, séché, d'une granulométrie comprise entre 0,2 et 4 mm,ayant les dimensions suivantes : 1,8 m m de diametre et 4 m de hauteur. Le passage de l'effluent s'effectue dans cette installation avec un débit de 5 m3/Heure.
Using an installation comprising a 10 m3 column of
Lithotamnium Calcareum screened, dried, with a particle size between 0.2 and 4 mm, having the following dimensions: 1.8 mm in diameter and 4 m in height. The effluent is passed through this installation with a flow of 5 m3 / hour.

Teneur en ppm Teneur en ppm
avant traitement aprés traitement
Phosphate 430 32
Fer 48
Molybdène 1
Titane 8 EXEMPLE 3 Installation d'anodisation
L'anodisation de l'aluminium nécessite pour les operatlorlr de colmatage a froid l'utilisation de fluorure de nickel ain..i que des phosphates et des sulfates.De maniere a épurer les eaux resultant de ci procede de fabrication, on utilise une colonne de 10 m3 de de Lithotan'iniurn
Calcareum de dimensions suivantes 1 .80 m de diamétre et 4 m de hauteur. le passage de l'effluent @effectuant avec un debit de 10 rr-l- .Heure. La granulométrie du Lithotamnium Calcareum est comprise entre 0,1 mm et @ mm.
Content in ppm Content in ppm
before treatment after treatment
Phosphate 430 32
Iron 48
Molybdenum 1
Titanium 8 EXAMPLE 3 Anodizing installation
The anodization of aluminum requires for cold sealing operatlorlr the use of nickel fluoride as well as phosphates and sulfates. In order to purify the water resulting from this manufacturing process, a column is used of 10 m3 of Lithotan'iniurn
Calcareum with the following dimensions 1.80 m in diameter and 4 m in height. the passage of the effluent @effectuant with a flow of 10 rr-l- .Hour. The particle size of Lithotamnium Calcareum is between 0.1 mm and @ mm.

Les résultats de décontamination obtenus. sont les suivantes
Teneur en ppm Teneur en ppm
avant traitement sprés traitement
Phosphate 80
Nickel 3.5
Fluorure 25
Sulfate 10
EXEMPLE 4: Unité d'épuration en industrie agro-alimentaire
En brasserie, on utilise de nombreux produits pour l'hygiéne industrielle. Ceux-ci après utilisation sont présents dans les effluents aussi retrouve-t-on les ions phosphates et iodures. ainsi que de faible'-.- quantités de cuivre dans ceux-ci.
The decontamination results obtained. are the following
Content in ppm Content in ppm
before treatment sprés treatment
Phosphate 80
Nickel 3.5
Fluoride 25
Sulfate 10
EXAMPLE 4: Purification unit in the food industry
In the brewery, many products are used for industrial hygiene. These after use are present in the effluents so do we find phosphate and iodide ions. as well as small amounts of copper therein.

Les effluents de brasserie résultant des processus de nettoyage passent sur une colonne de 5 m3 de Lithotamnium Calcareum criblé séché, dont les dimensions sont les suivantes . 1,90 m de diamétre et
1,90 m de hauteur. La granulométrie est. comprise entre 0,2 mm et 10 mm
Le passage de l'effluent s'effectué avec un débit de 5 m3 heure. On obtient les résultats suivants
Teneur en ppm Teneur en ppm
avant traitement aprés traitement
Phosphate 250 30
Cuivre 3 0,5 lodure 14 1
EXEMPLE 5 Unité de traitement en industrie utilisant des radio-éléments
Dans les laboratoires effectuant des analyses radio immunologiques, on utilise de nombreux rsdio-élements en quantité tres faible tel que le cadmium, le césium. le ruthénium. le molgbdene, l'indium, le cobalt. Les eaux provenant du laboratoire sont decontaminees sur une colonne de 1 m3-. de Lithotammum Calcareum ayant une dimension de 0.8 m de diemétre 2 m de hauteur. La gr@nulometrie du Lithoth@mmun
Caloareum est de 0,1 @ 2 mm Le debit de passage des effluents est de
O 1 m3 heure
Les resultets d'efficacite du procede sont les suivants un
Drelevement est effectue avant passage Apres evaperation la matiere seche donne au compteur d'impulsion en une derm minute 13215 apre@ passage dans la colonne un prelevement d'un volume identique donne en une demi minute au compteur d'impulsion 185.
The brewery effluents resulting from the cleaning processes pass over a 5 m3 column of dried screened Lithotamnium Calcareum, the dimensions of which are as follows. 1.90 m in diameter and
1.90 m high. The grain size is. between 0.2 mm and 10 mm
The flow of the effluent is carried out with a flow of 5 m3 per hour. The following results are obtained
Content in ppm Content in ppm
before treatment after treatment
Phosphate 250 30
Copper 3 0.5 lodure 14 1
EXAMPLE 5 Processing unit in industry using radio-elements
In laboratories performing radio immunological analyzes, many elements are used in very small quantities such as cadmium, cesium. ruthenium. molgbdenum, indium, cobalt. The water from the laboratory is decontaminated on a column of 1 m3-. of Lithotammum Calcareum having a dimension of 0.8 m in diameter and 2 m in height. The gr @ nulometry of Lithoth @ mmun
Caloareum is 0.1 @ 2 mm The flow rate for effluents is
O 1 m3 hour
The efficiency results of the process are as follows:
Detection is carried out before passage After evaporation the dry matter gives to the pulse counter in one derm minute 13215 after @ passage in the column a sample of the same volume given in half a minute to the pulse counter 185.

Claims (3)

REVENDICATIONS 1- Procédé d'épuration d'effluents industriels caractérisé par le passage de ces effluents industriels e travers une colonne de 1- Process for the purification of industrial effluents characterized by the passage of these industrial effluents through a column of Lithotamnium Calcareum criblé et séché. ayant une granulometrie comprise entre 10 mm et 0,1 mm. L'effluent industriel pouvant contenir l'un ou plusieurs des ions suivants nickel. zinc, cuivre,' cadmium. fer.Screened and dried Lithotamnium Calcareum. having a particle size between 10 mm and 0.1 mm. Industrial effluent which may contain one or more of the following nickel ions. zinc, copper, cadmium. iron. indium, manganèse, molybdène, cobalt, ruthenium, titane, phosphate.indium, manganese, molybdenum, cobalt, ruthenium, titanium, phosphate. sulfate, fluorure, iodure, césium.sulfate, fluoride, iodide, cesium. 2- Procédé d'épuration selon le revendication 1 caractérisé en ce que le Lithotamnium Calcareum crible, séché, et a de préférence une granulométrie comprise entre 0,5 mm et 2 mm. 2- Purification process according to claim 1 characterized in that the Lithotamnium Calcareum screens, dried, and preferably has a particle size between 0.5 mm and 2 mm. 3-Procédé d'épuration selon les revendications 1 et 2, Caractrise en ce que le passage des effluents est réalisé dans une colonne remplie de Lithotamnium Calcareum crible. séché, dont les dimensions de 1 colonne sont telles que le dismetre soit au plus égal a la hauteur.  3-Purification process according to claims 1 and 2, Characterization in that the passage of the effluents is carried out in a column filled with screened Lithotamnium Calcareum. dried, whose dimensions of 1 column are such that the dismetre is at most equal to the height.
FR8617719A 1986-12-18 1986-12-18 PROCESS FOR THE PURIFICATION OF INDUSTRIAL EFFLUENTS BY "LITHOTAMNIUM CALCAREUM" Expired FR2608587B3 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
FR8617719A FR2608587B3 (en) 1986-12-18 1986-12-18 PROCESS FOR THE PURIFICATION OF INDUSTRIAL EFFLUENTS BY "LITHOTAMNIUM CALCAREUM"

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR8617719A FR2608587B3 (en) 1986-12-18 1986-12-18 PROCESS FOR THE PURIFICATION OF INDUSTRIAL EFFLUENTS BY "LITHOTAMNIUM CALCAREUM"

Publications (2)

Publication Number Publication Date
FR2608587A1 true FR2608587A1 (en) 1988-06-24
FR2608587B3 FR2608587B3 (en) 1989-05-26

Family

ID=9342033

Family Applications (1)

Application Number Title Priority Date Filing Date
FR8617719A Expired FR2608587B3 (en) 1986-12-18 1986-12-18 PROCESS FOR THE PURIFICATION OF INDUSTRIAL EFFLUENTS BY "LITHOTAMNIUM CALCAREUM"

Country Status (1)

Country Link
FR (1) FR2608587B3 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2644451A1 (en) * 1989-03-20 1990-09-21 Norsolor Sa USE OF ZEOLITES FOR THE PURIFICATION OF SATURATED CARBOXYLIC ACIDS WITH A RESIDUAL CONTENT OF FLUORIDES AND METHOD OF PURIFYING SAME
WO1993024205A1 (en) * 1992-06-02 1993-12-09 Richard Berney Biofiltration of gases
CN113387472A (en) * 2021-06-07 2021-09-14 先导薄膜材料有限公司 Method for removing cadmium and thallium from indium-containing wastewater

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2644451A1 (en) * 1989-03-20 1990-09-21 Norsolor Sa USE OF ZEOLITES FOR THE PURIFICATION OF SATURATED CARBOXYLIC ACIDS WITH A RESIDUAL CONTENT OF FLUORIDES AND METHOD OF PURIFYING SAME
WO1990011270A1 (en) * 1989-03-20 1990-10-04 Norsolor Defluoridation of carboxylic acids using zeolites
WO1993024205A1 (en) * 1992-06-02 1993-12-09 Richard Berney Biofiltration of gases
CN113387472A (en) * 2021-06-07 2021-09-14 先导薄膜材料有限公司 Method for removing cadmium and thallium from indium-containing wastewater

Also Published As

Publication number Publication date
FR2608587B3 (en) 1989-05-26

Similar Documents

Publication Publication Date Title
US5725753A (en) Apparatus and method for cleaning semiconductor wafers
US20140042086A1 (en) Method for improving a wastewater purification process
CN105129832B (en) The method that liquid calcium chloride is continuously produced using fluorine-containing by-product waste hydrochloric acid
US3802910A (en) Recovery of mercury from mercurous bearing liquids
FR2608587A1 (en) Process for the purification of industrial effluents using "lithotamnium calcareum"
US4100065A (en) Method for removing of multivalent heavy metals from metal plating waste effluents
CA1115437A (en) Process for treating waste water
US5013698A (en) Method of reducing carbon loss in regeneration process
EP0466987A1 (en) Purification of hydrogen peroxide
JP3238745B2 (en) Method of treating ammonium fluoride-containing water
CN110668909B (en) Purification method of environment-friendly n-hexane
US2105701A (en) Process for purification of beverages
JP2005008455A (en) Method for separating and recovering iron and manganese which coexist in water
DE1052962B (en) Process for the separation of hydrofluoric acid from solutions containing other acids
EP0162491B1 (en) Process for inhibiting corrosion of a metallic mass in contact with an acidic bath containing ferric ions
JPS5832805A (en) Red tide treating agent and its preparation
JPH0450859B2 (en)
RU2001126463A (en) The method of processing wastewater galvanic production containing heavy metals
SU1719314A1 (en) Method of cleaning sewage containing petroleum products
CN217627981U (en) High salt waste water treatment and resource system
RU2068030C1 (en) Method of treatment of aluminum and its alloys equipment designated for operation in hydrogen peroxide solutions
JP3923913B2 (en) Wash water reuse method and reuse system
US1147515A (en) Process of obtaining base-exchanging substances.
FR2669324A1 (en) PROCESS FOR THE REMOVAL OF NITRATES FROM WATERS USING DRINKING WATERS USING MEMBRANE AND SIMILAR SYSTEMS.
Masawi et al. Removal of Iron (II) From Aqueous Solution by Cucurbita Moschata Peel Powder (CMPP)

Legal Events

Date Code Title Description
ST Notification of lapse