FR2758551A1 - Method for augmenting the porosity of clay supports such as sepiolite - Google Patents
Method for augmenting the porosity of clay supports such as sepiolite Download PDFInfo
- Publication number
- FR2758551A1 FR2758551A1 FR9700519A FR9700519A FR2758551A1 FR 2758551 A1 FR2758551 A1 FR 2758551A1 FR 9700519 A FR9700519 A FR 9700519A FR 9700519 A FR9700519 A FR 9700519A FR 2758551 A1 FR2758551 A1 FR 2758551A1
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- supports
- outlet
- treated
- capacity
- drying
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/12—Naturally occurring clays or bleaching earth
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- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Dispersion Chemistry (AREA)
- Geochemistry & Mineralogy (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
Description
La présente invention concerne un dispositif de traitement des supports duThe present invention relates to a device for processing the supports of the
type ARGILE comportant essentiellement dans leurs structures moléculaires des atomes métalliques en général et son application particulière pour la sépiolite qui peut servir de support et constituant de base pour la constitution de matières et produits absorbants des composés volatils de l'atmosphère Ces supports argileux, présentent des structures particulières caractérisant une grande porosité intéressante pour les surfaces d'échanges avec les gaz de l'atmosphère. La caractérisation pour la circulation des gaz dans ces porosités est déterminée par CLAY type essentially comprising in their molecular structures metal atoms in general and its particular application for sepiolite which can serve as a support and basic constituent for the constitution of materials and products absorbing volatile compounds from the atmosphere These clay supports have particular structures characterizing a large porosity which is interesting for the surfaces of exchange with gases from the atmosphere. The characterization for the circulation of gases in these porosities is determined by
l'ouverture de ces canaux intercristallins. the opening of these intercrystalline canals.
Dans le cas particulier de la sépiolite, la constitution des porosités longitudinales est définie par une distribution en feuilles d'unités de silices tétraédriques liées au moyen d'atomes d'oxygène à une feuille octaèdrique comportant les atomes de magnésium pour les supports du type magnésien. Cette structure particulière caractérise les porosités cylindriques dont l'ouverture est conditionnée par le positionnement des atomes métalliques dont les atomes de magnésium pour la sépiolite de magnésium en particulier Cette distribution est représentée schématiquement dans un seul plan pour la bonne In the particular case of sepiolite, the constitution of the longitudinal porosities is defined by a distribution in sheets of units of tetrahedral silicas linked by means of oxygen atoms to an octahedral sheet comprising magnesium atoms for supports of the magnesian type. . This particular structure characterizes the cylindrical porosities whose opening is conditioned by the positioning of the metallic atoms including the magnesium atoms for magnesium sepiolite in particular This distribution is represented schematically in a single plane for the correct
compréhension fonctionnelle du dispositif par la figure 2. functional understanding of the device in Figure 2.
La figure 2, représente les canaux des porosités unitaires comportant dans la section tétraèdrique les atomes de silice (21) les atomes d'oxygènes (22) et les atomes de magnésium (23) qui sont positionnés en liaison octaèdrique sur l'extrémité des canaux cylindriques. Cette distribution consolide les canaux cylindriques (20) des porosités et les canaux (30) caractérisent l'ouverture FIG. 2 represents the channels of the unit porosities comprising in the tetrahedral section the silica atoms (21) the oxygen atoms (22) and the magnesium atoms (23) which are positioned in octahedral connection on the end of the channels cylindrical. This distribution consolidates the cylindrical channels (20) of the porosities and the channels (30) characterize the opening
octaèdrique des porosités.octahedral porosity.
Pour favoriser la circulation des composés volatils de l'atmosphère dans ces canaux, le dispositif objet de l'invention consiste à ouvrir ces porosités et de les allèger des atomes mètailiques lourds qui par leur poids ont la tendance naturelle des liaisons à se fermner et provoquer ainsi une obstruction plus ou moins To promote the circulation of volatile compounds from the atmosphere in these channels, the device which is the subject of the invention consists in opening these porosities and in lightening them from heavy metallic atoms which by their weight have the natural tendency of bonds to close and cause thus a more or less obstruction
importante des ouvertures octaèdriques. important octahedral openings.
Pour favoriser la capacité de réactions physico chimiiques, pour transformer les composés volatils circulant dans ces canaux, il est utile d'assurer un prétraitenient de ces centres actifs d'absorption pour sensibiliser et augmenter les capacités d'interéactions des groupes hydroxyles de silice avec les molécules externes en formant des liens covalents avec certains réactifs organiques. Le dispositif objet de l'invention réalise particulièrement ce traitement de sensibilisation par lavage acide et l'ouverture des porosités est augmentée d'une valeur significative par la centrifugation de la sépiolite pour éliminer les atomes lourds de To favor the capacity of physico-chemical reactions, to transform the volatile compounds circulating in these channels, it is useful to ensure a pretreatment of these active centers of absorption to sensitize and increase the capacities of interactions of the silica hydroxyl groups with the external molecules by forming covalent bonds with certain organic reagents. The device which is the subject of the invention particularly performs this sensitization treatment by acid washing and the opening of the porosities is increased by a significant value by the centrifugation of the sepiolite to remove the heavy atoms from
magnésium à l'ouverture des porosités. magnesium at the opening of the porosities.
La figure i représenie l'appareillage de traitement permettant d e conditionner l'ouverture des porosités et de sensibiliser les Figure i shows the treatment equipment to condition the opening of the pores and to sensitize the
surfaces d'échanges internes.internal exchange surfaces.
Le dispositif comporte une capacité de lavage de prétraitement (1) une machine de centrifugation (7) avec son multiplicateur (8) et son enveloppe de chauffage (6). La matière à traiter, l' argile et la sépiolite de magnésium en particulier est injectée sous pression et atomisée à la partie supérieure de la capacité (1). Les arrivées de liquide acide sous pression sur les buses de pulvérisation (3) et (4) de la capacité (1) permet de réaliser un lavage mécanique énergique de ia matière introduite (2) sous une granulométrie très fine à la partie supérieure de la capacité (1). Ce traitement acide énergique en ambiance fluidisée augmente d'une manière significative la section croisée des canaux intercristallins des porosités de la The device comprises a pretreatment washing capacity (1) a centrifugation machine (7) with its multiplier (8) and its heating jacket (6). The material to be treated, the clay and the magnesium sepiolite in particular is injected under pressure and atomized at the top of the tank (1). The arrivals of acidic liquid under pressure on the spray nozzles (3) and (4) of the capacity (1) makes it possible to carry out an energetic mechanical washing of the material introduced (2) under a very fine particle size at the top of the capacity (1). This energetic acid treatment in a fluidized environment significantly increases the cross section of the intercrystalline channels of the porosities of the
matière ainsi traitée.material thus treated.
Ce constituant mélangé et fluidisé avec un liquide acide, est introduit à la partie haute de la centrifugeuse (7). La centrifugation du mélange, s'effectue à une vitesse de rotation supérieure à 10 000 tours par minute et dans une enveloppe maintenue à une température comprise entre 150 et 200 degrés centigrades par des cannes This constituent, mixed and fluidized with an acidic liquid, is introduced into the upper part of the centrifuge (7). The mixture is centrifuged at a speed greater than 10,000 revolutions per minute and in an envelope maintained at a temperature between 150 and 200 degrees centigrade by canes
chauffantes (6) de chauffage de l'enveloppe de la centrifugeuse (7). heating (6) for heating the casing of the centrifuge (7).
Le traitement en température de la matière dont la sépiolite dans un milieu acide augmente la section croisée des canaux des porosités. La centrifugation à grande vitesse du mélange, permet par l'effet cisaille la mise en contrainte de la liaison moléculaire silice et magnésium de la structure ouverte des porosités comme représentées par la figure 2. Les forces de contraintes externes des atomes lourds métalliques dont le magnésium pour la structure particulière de la sépiolite, induites par la centrifugation, sont caractérisées par l'établissement d'un champ de contraintes (24) de traction sur les atomes de magnésium (23) pour opérer l'effet cisaille (26) de la liaison silice (21). La liaison cisaillée (26) libérée du poids des atomes métalliques amène une ouverture (30) plus The temperature treatment of the material, the sepiolite in an acid medium increases the cross section of the porosity channels. The high speed centrifugation of the mixture allows, by the shear effect, the stressing of the molecular bond silica and magnesium of the open structure of the porosities as shown in Figure 2. The external stress forces of heavy metal atoms including magnesium for the particular structure of sepiolite, induced by centrifugation, are characterized by the establishment of a tensile stress field (24) on the magnesium atoms (23) to operate the shear effect (26) of the bond silica (21). The sheared bond (26) freed from the weight of the metal atoms leads to an opening (30) more
grande des porosités de la matière traitée. large porosity of the treated material.
A la sortie inférieure des étages de centrifugation, les résidus lourds comportant entre autres les atomes métalliques sont extraits en périphérie (9), le liquide est sorti en (10) et la matière traitée ressort à la partie centrale pour entrer dans la capacité de At the lower outlet of the centrifugation stages, the heavy residues comprising inter alia the metallic atoms are extracted at the periphery (9), the liquid is discharged at (10) and the treated material leaves the central part to enter the capacity for
séchage (11).drying (11).
Le séchage des granulés de matière traitée est assuré par ondes ultra sonores à fréquence et puissance modulables émises par les bases (12) positionnées en périphérie de la capacité de séchage (11) Les granulés séchés sortent par la tuyère (13) pour être pulverises dans un réservoir tampon (16). Le résevoir (16) comporte un tambour de chauffage (17) qui permet de maintenir en température et parfaire le séchage de la matière ainsi traitée. La matière argile ou sépiolite en particulier ainsi traitée peut être dirigée The drying of the granules of treated material is ensured by ultrasonic waves at adjustable frequency and power emitted by the bases (12) positioned at the periphery of the drying capacity (11) The dried granules exit through the nozzle (13) to be sprayed into a buffer tank (16). The reservoir (16) comprises a heating drum (17) which makes it possible to maintain the temperature and perfect the drying of the material thus treated. The clay or sepiolite material in particular thus treated can be directed
vers les installations de transformations (19). towards processing facilities (19).
Le liquide de procédé peut être dirigé directement dans les Process liquid can be directed directly into the
bioréacteurs de traitements par les liaisons (18). bioreactors of link processing (18).
Les capacités (11) et (16) sont ventilées et mis en dépression par un ventilateur (14) et un filtre (15) Cette mise en dépression énergique des capacités (11) et (16) favorise essentiellement l'écoulement et le séchage de la matière traitée qui circule en The capacities (11) and (16) are ventilated and put under vacuum by a fan (14) and a filter (15) This energizing depression of the capacities (11) and (16) essentially promotes the flow and drying of the treated material which circulates in
lit fluidisé.fluidized bed.
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR9700519A FR2758551A1 (en) | 1997-01-20 | 1997-01-20 | Method for augmenting the porosity of clay supports such as sepiolite |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR9700519A FR2758551A1 (en) | 1997-01-20 | 1997-01-20 | Method for augmenting the porosity of clay supports such as sepiolite |
Publications (1)
Publication Number | Publication Date |
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FR2758551A1 true FR2758551A1 (en) | 1998-07-24 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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FR9700519A Pending FR2758551A1 (en) | 1997-01-20 | 1997-01-20 | Method for augmenting the porosity of clay supports such as sepiolite |
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FR (1) | FR2758551A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000003798A1 (en) * | 1998-07-17 | 2000-01-27 | Cca Food Technologies (Uk) Plc | Treatment method and device for increasing clay porosity and use for producing absorbents |
WO2000064577A1 (en) * | 1999-04-27 | 2000-11-02 | Ectium Bv | Material and method for treating gaseous media containing volatile organic compounds |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1819496A (en) * | 1926-05-22 | 1931-08-18 | Filtrol Company Of California | Activated clay and method of producing same |
US2563977A (en) * | 1949-12-08 | 1951-08-14 | Filtrol Corp | Process for continuously acid activating clay |
US2968633A (en) * | 1958-05-27 | 1961-01-17 | Minerals & Chem Philipp Corp | Adsorptive porous mineral mass and method of making same |
GB939937A (en) * | 1958-12-19 | 1963-10-16 | Fullers Eari I | Process for activating clays with acid |
FR2157166A5 (en) * | 1971-10-20 | 1973-06-01 | Carbon Charbons Actifs | Adsorbent/absorbent silica granules prodn - by heating agglomerated clay, and treating with acid |
JPS57136938A (en) * | 1981-11-30 | 1982-08-24 | Chiyoda Chem Eng & Constr Co Ltd | Porous modified sepiolite catalyst |
EP0398636A1 (en) * | 1989-05-16 | 1990-11-22 | Engelhard Corporation | A process for making acid activated bleaching earth |
-
1997
- 1997-01-20 FR FR9700519A patent/FR2758551A1/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1819496A (en) * | 1926-05-22 | 1931-08-18 | Filtrol Company Of California | Activated clay and method of producing same |
US2563977A (en) * | 1949-12-08 | 1951-08-14 | Filtrol Corp | Process for continuously acid activating clay |
US2968633A (en) * | 1958-05-27 | 1961-01-17 | Minerals & Chem Philipp Corp | Adsorptive porous mineral mass and method of making same |
GB939937A (en) * | 1958-12-19 | 1963-10-16 | Fullers Eari I | Process for activating clays with acid |
FR2157166A5 (en) * | 1971-10-20 | 1973-06-01 | Carbon Charbons Actifs | Adsorbent/absorbent silica granules prodn - by heating agglomerated clay, and treating with acid |
JPS57136938A (en) * | 1981-11-30 | 1982-08-24 | Chiyoda Chem Eng & Constr Co Ltd | Porous modified sepiolite catalyst |
EP0398636A1 (en) * | 1989-05-16 | 1990-11-22 | Engelhard Corporation | A process for making acid activated bleaching earth |
Non-Patent Citations (2)
Title |
---|
CHEMICAL ABSTRACTS, vol. 124, no. 8, 19 February 1996, Columbus, Ohio, US; abstract no. 91724g, V. RODRIGUEZ: "ACID ACTIVATION OF A SPANISH SEPIOLITE" page 284; column 2; XP002044223 * |
PATENT ABSTRACTS OF JAPAN vol. 6, no. 235 (C - 136) * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000003798A1 (en) * | 1998-07-17 | 2000-01-27 | Cca Food Technologies (Uk) Plc | Treatment method and device for increasing clay porosity and use for producing absorbents |
WO2000064577A1 (en) * | 1999-04-27 | 2000-11-02 | Ectium Bv | Material and method for treating gaseous media containing volatile organic compounds |
FR2792849A1 (en) * | 1999-04-27 | 2000-11-03 | Ectium Bv | MATERIAL AND METHOD FOR THE TREATMENT OF GASEOUS MEDIA CONTAINING VOLATILE ORGANIC COMPOUNDS |
US6723296B2 (en) | 1999-04-27 | 2004-04-20 | Ectium B.V. | Material and method for treating gaseous media containing volatile organic compounds |
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