FR2965560A1 - Filter for treatment of black liquor, comprises filter elements with composition including activated carbon, settling tank through which black liquor, polyphenols and organic phenols are introduced and then discharged through layer of sand - Google Patents

Filter for treatment of black liquor, comprises filter elements with composition including activated carbon, settling tank through which black liquor, polyphenols and organic phenols are introduced and then discharged through layer of sand Download PDF

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Publication number
FR2965560A1
FR2965560A1 FR1003944A FR1003944A FR2965560A1 FR 2965560 A1 FR2965560 A1 FR 2965560A1 FR 1003944 A FR1003944 A FR 1003944A FR 1003944 A FR1003944 A FR 1003944A FR 2965560 A1 FR2965560 A1 FR 2965560A1
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France
Prior art keywords
filter
sand
black liquor
layer
activated carbon
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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.)
Pending
Application number
FR1003944A
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French (fr)
Inventor
Andreas Anest
Artemis Anest
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Individual
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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.)
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Publication date
Application filed by Individual filed Critical Individual
Priority to FR1003944A priority Critical patent/FR2965560A1/en
Publication of FR2965560A1 publication Critical patent/FR2965560A1/en
Pending legal-status Critical Current

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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
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • 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
    • C02F1/283Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/34Organic compounds containing oxygen
    • C02F2101/345Phenols
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/32Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters
    • C02F2103/322Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters from vegetable oil production, e.g. olive oil production

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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

The filter comprises filter elements having a composition including activated carbon, zeolite and/or sand, a settling tank through which the black liquor, polyphenols and organic phenols are introduced and then discharged through a layer of sand having a thickness of 50 cm, a pump connected with a second filter and third filter having same dimension of the first filter, where the particle size of the filter elements is 0.3-0.6 mm, and baffle separators are perforated with holes of 0.2 mm. The filter elements are combined together, and are placed in a container with a diameter of 2.5 m. The filter comprises filter elements having a composition including activated carbon, zeolite and/or sand, a settling tank through which the black liquor, polyphenols and organic phenols are introduced and then discharged through a layer of sand having a thickness of 50 cm, a pump connected with a second filter and third filter having same dimension of the first filter, where the particle size of the filter elements is 0.3-0.6 mm, and baffle separators are perforated with holes of 0.2 mm. The filter elements are combined together, and are placed in a container with a diameter of 2.5 m and a height of 3m and separated by diaphragms perforated with holes of 1 mm and a particle size of 0.4-0.12 mm.

Description

PROCEDE DE FILTRE ÉCOLOGIQUE POUR LE TRAITEMENT DES MARGINES Description La présente invention concerne la fabrication d'un filtre destiné à l'utilisation pour le traitement des eaux usagées générées par l'industrie de production d'huile d'olive appelées communément margines, et le raffinement de ses résidus jusqu'à la récupération de polyphénols des matières organiques et des sels, et la production d'une eau utilisable pour l' arrosage, par la combinaison en tant que produits filtrants : du charbon actif, du zéolite, et du sable. Il s'agit d'un produit de classe 40. Mode de fabrication: Les Margines récupérées à leur sortie sont dans un premier temps versées dans un bac décanteur à travers un filtre composé de graviers délavés et de sable pour récupérer les parties grosses ligneuses en suspension dans les Margines. Ensuite avec une pompe de 1" les Margines sont envoyées dans un filtre composé d'un récipient d'un diamètre de 2.5 mètres et d'une hauteur de 3m qui contient des couches successives d'une épaisseur de 1 mètre de sable, del mètre de zéolithe, et de 1 mètre de charbon actif, d'une granulométrie relativement importante allant de 0,4 à 0,12 mm. Ces couches sont séparées par un diaphragme présentant des trous de 0.3 mm. Ces couches récupèrent successivement sels, polyphénols et substances organiques, et couleurs. Les Margines sont ensuite conduites dans un seconde bac décanteur de 2m x 2,50m x 2,50m à travers une couche de 20 cm de sable fin destinée à récupérer les parties salines essentiellement composées de sels de potassium. Ensuite les Margines sont envoyées par une autre pompe dans un autre filtre de même dimension que le premier d"un diamètre de 2,50m x 3m ayant des couches successives de zéolithe, de charbon actif et de sable d 'une épaisseur de 1 mètre et d 'une granulométrie allant de 0,3 à 0,6 mm séparées par un diaphragme perforé de trous de 0,2 mm récupérant successivement polyphénols, matières organiques et salins. Ensuite les Margines sont envoyées dans un autre bac décanteur à travers une couche de sable noir très fin d'une épaisseur de 40 cm. Les Margines ainsi débarrassées de parties restantes sont envoyées dans un troisième filtre de 2,50 m x 3 m contenant des couches successives de charbon actif, de sable et de zéolithes d'une épaisseur de 1 mètre et d'une granulométrie allant de 0,2mm à 0,4mm récupérant ainsi les éléments polluant organiques, les sels, les phénols. Ensuite les Margines sont envoyées dans un dernier bac décanteur à travers une couche de sable très fin d 'une épaisseur de 50 cm. A la sortie nous avons de l'eau 35 bonne pour l'irrigation des cultures. The present invention relates to the manufacture of a filter for use in the treatment of waste water generated by the olive oil production industry commonly referred to as "margines", and the production of a filter for the treatment of waste water generated by the olive oil production industry commonly referred to as "margines". refining of its residues until the recovery of polyphenols from organic matter and salts, and the production of a water suitable for watering, by the combination as filtering products: activated carbon, zeolite, and sand . This is a Class 40 product. Method of manufacture: The Margines recovered at their exit are first poured into a decanter tank through a filter composed of washed gravel and sand to recover the large woody parts. suspension in the Margines. Then with a pump of 1 "the Margines are sent in a filter composed of a container of a diameter of 2.5 meters and a height of 3m which contains successive layers with a thickness of 1 meter of sand, del meter zeolite, and 1 meter of activated carbon, of a relatively large particle size ranging from 0.4 to 0.12 mm These layers are separated by a diaphragm having 0.3 mm holes These layers successively recover salts, polyphenols and Organic substances and colors The Margines are then taken to a second 2m x 2.50m x 2.50m decanter tank through a layer of 20 cm of fine sand to recover saline parts mainly composed of potassium salts. the Margines are sent by another pump in another filter of the same size as the first of a diameter of 2.50m x 3m having successive layers of zeolite, activated charcoal and sand with a thickness of 1 meter. and a particle size ranging from 0.3 to 0.6 mm separated by a diaphragm perforated with 0.2 mm holes successively recovering polyphenols, organic materials and saline. Then the Margines are sent to another decanter tank through a layer of very fine black sand with a thickness of 40 cm. Margines thus removed from remaining parts are sent into a third filter of 2.50 mx 3 m containing successive layers of activated carbon, sand and zeolites with a thickness of 1 meter and a particle size ranging from 0.2 mm at 0.4mm thus recovering organic pollutants, salts, phenols. Then the Margines are sent to a final decanter tank through a layer of very fine sand of a thickness of 50 cm. At the exit we have good water for crop irrigation.

Claims (5)

REVENDICATIONS1) Filtre utilisé dans le traitement des Margines, dont les éléments filtrants entrant dans sa composition sont une combinaison de trois substances entièrement écologiques: le charbon actif, le zéolite, et le sable. CLAIMS1) Filter used in the treatment of Margines, whose filter elements used in its composition are a combination of three entirely ecological substances: activated carbon, zeolite, and sand. 2) Filtre selon la revendication (1) caractérisé en ce que les éléments filtrants sont entièrement écologiques, combinés entre eux dans un ordre précis et sont placés dans un récipient d'un diamètre de 2,5 m et d'une hauteur de 3m, séparés entre eux par des diaphragmes perforés de trous de 0.3 mm et d'une granulométrie allant de 0,4 mm à 0,12 mm. 2) Filter according to claim (1) characterized in that the filter elements are entirely ecological, combined with each other in a precise order and are placed in a container with a diameter of 2.5 m and a height of 3m, separated from each other by diaphragms perforated with holes of 0.3 mm and with a particle size ranging from 0.4 mm to 0.12 mm. 3) Filtre selon la revendication (2) comprenant un décanteur dans lequel les Margines ainsi débarrassées d'une part de leurs sels, de leurs polyphénols et de leurs polluants organiques selon la revendication (2), sont ensuite déversées à travers une couche de sable d'une épaisseur de 20 cm; une pompe à l'aide de laquelle elles sont conduites dans un second filtre ayant les mêmes dimensions que le précédent (2,50m x 3m) selon la revendication (2), la granulométrie des éléments filtrants est de 0,3mm à 0,6 mm et l'ordre de leur placement est: zéolite, charbon actif et sable. Les diaphragmes séparateurs sont perforés de trous de 0,2mm. 3) A filter according to claim (2) comprising a settler in which Margins thus cleared of their salts, their polyphenols and their organic pollutants according to claim (2), are then discharged through a layer of sand of a thickness of 20 cm; a pump by means of which they are conducted in a second filter having the same dimensions as the previous one (2.50m x 3m) according to claim (2), the particle size of the filter elements is 0.3mm to 0.6 mm and the order of their placement is: zeolite, activated carbon and sand. The separating diaphragms are perforated with 0.2 mm holes. 4) Filtre selon la revendication (3) qui comprend un autre bac décanteur dans lequel sont versées les Margines à travers une couche de sable noir d'une épaisseur de 40 cm, et à l'aide d'une pompe conduite dans un troisième filtre de même dimension que le filtre selon les revendications (2) et (3) et dont les diaphragmes sont perforés de trous de 1 mm. 4) The filter of claim (3) which comprises another settling tank in which are poured Margines through a layer of black sand of a thickness of 40 cm, and with a pump driven in a third filter the same dimension as the filter according to claims (2) and (3) and whose diaphragms are perforated with holes of 1 mm. 5) Filtre selon la revendication (4) aui comprend un bac décanteur dans lequel sont déversés les Margines, après les traitements précédents à travers une couche de sable très fin d'une épaisseur de 50 cm. 5) Filter according to claim (4) aui comprises a settling tank in which are poured Margines, after previous treatments through a layer of very fine sand with a thickness of 50 cm.
FR1003944A 2010-10-04 2010-10-04 Filter for treatment of black liquor, comprises filter elements with composition including activated carbon, settling tank through which black liquor, polyphenols and organic phenols are introduced and then discharged through layer of sand Pending FR2965560A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
FR1003944A FR2965560A1 (en) 2010-10-04 2010-10-04 Filter for treatment of black liquor, comprises filter elements with composition including activated carbon, settling tank through which black liquor, polyphenols and organic phenols are introduced and then discharged through layer of sand

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR1003944A FR2965560A1 (en) 2010-10-04 2010-10-04 Filter for treatment of black liquor, comprises filter elements with composition including activated carbon, settling tank through which black liquor, polyphenols and organic phenols are introduced and then discharged through layer of sand

Publications (1)

Publication Number Publication Date
FR2965560A1 true FR2965560A1 (en) 2012-04-06

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FR1003944A Pending FR2965560A1 (en) 2010-10-04 2010-10-04 Filter for treatment of black liquor, comprises filter elements with composition including activated carbon, settling tank through which black liquor, polyphenols and organic phenols are introduced and then discharged through layer of sand

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FR (1) FR2965560A1 (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4340485A (en) * 1977-10-07 1982-07-20 Takeda Chemical Industries, Ltd. Countercurrent liquid-solid contacting apparatus
US6039866A (en) * 1997-03-26 2000-03-21 Hitachi, Ltd. Fluidized bed filtering apparatus
WO2003000601A1 (en) * 2001-06-25 2003-01-03 Jose Toro Galvez System for purifying waste water originating from olive processing by means of aeration, neutralisation, active carbon filtration and ozonisation
EP1462416A2 (en) * 2003-03-27 2004-09-29 Akechi Ceramics Kabushiki Kaisha Liquid treating apparatus
ES2224853A1 (en) * 2003-05-21 2005-03-01 Santiago Lopez Martinez Purification of oil mill water comprises flotation, homogenization, settling, filtration, degassing and oxidation, for disposal in drains
US20050236335A1 (en) * 2004-04-23 2005-10-27 Perpetual Water Pty Ltd Method and apparatus for removing contaminants from water

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4340485A (en) * 1977-10-07 1982-07-20 Takeda Chemical Industries, Ltd. Countercurrent liquid-solid contacting apparatus
US6039866A (en) * 1997-03-26 2000-03-21 Hitachi, Ltd. Fluidized bed filtering apparatus
WO2003000601A1 (en) * 2001-06-25 2003-01-03 Jose Toro Galvez System for purifying waste water originating from olive processing by means of aeration, neutralisation, active carbon filtration and ozonisation
EP1462416A2 (en) * 2003-03-27 2004-09-29 Akechi Ceramics Kabushiki Kaisha Liquid treating apparatus
ES2224853A1 (en) * 2003-05-21 2005-03-01 Santiago Lopez Martinez Purification of oil mill water comprises flotation, homogenization, settling, filtration, degassing and oxidation, for disposal in drains
US20050236335A1 (en) * 2004-04-23 2005-10-27 Perpetual Water Pty Ltd Method and apparatus for removing contaminants from water

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