EP2231329A2 - Poudre de catalyseur - Google Patents

Poudre de catalyseur

Info

Publication number
EP2231329A2
EP2231329A2 EP08870192A EP08870192A EP2231329A2 EP 2231329 A2 EP2231329 A2 EP 2231329A2 EP 08870192 A EP08870192 A EP 08870192A EP 08870192 A EP08870192 A EP 08870192A EP 2231329 A2 EP2231329 A2 EP 2231329A2
Authority
EP
European Patent Office
Prior art keywords
particles
catalyst
precipitation
catalyst powder
catalytically active
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Withdrawn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
EP08870192A
Other languages
German (de)
English (en)
Inventor
Juliane Meese-Marktscheffel
Armin Olbrich
Matthias Jahn
Gerd Maikowske
Wilfried Gutknecht
Theodor KÖNIG
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.)
HC Starck GmbH
Original Assignee
HC Starck GmbH
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 HC Starck GmbH filed Critical HC Starck GmbH
Publication of EP2231329A2 publication Critical patent/EP2231329A2/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/14—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of germanium, tin or lead
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/02—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the alkali- or alkaline earth metals or beryllium
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/06—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of zinc, cadmium or mercury
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/32—Manganese, technetium or rhenium
    • B01J23/34—Manganese
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/72—Copper
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74—Iron group metals
    • B01J23/745—Iron
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74—Iron group metals
    • B01J23/75—Cobalt
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/889—Manganese, technetium or rhenium
    • B01J23/8892—Manganese
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/396—Distribution of the active metal ingredient
    • B01J35/397—Egg shell like
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/0215—Coating
    • B01J37/0221—Coating of particles
    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/03—Precipitation; Co-precipitation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B82—NANOTECHNOLOGY
    • B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B82—NANOTECHNOLOGY
    • B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y40/00—Manufacture or treatment of nanostructures
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00—Carbon; Compounds thereof
    • C01B32/15—Nano-sized carbon materials
    • C01B32/158—Carbon nanotubes
    • C01B32/16—Preparation
    • C01B32/162—Preparation characterised by catalysts
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F9/00—Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments
    • D01F9/08—Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments of inorganic material
    • D01F9/12—Carbon filaments; Apparatus specially adapted for the manufacture thereof
    • D01F9/127—Carbon filaments; Apparatus specially adapted for the manufacture thereof by thermal decomposition of hydrocarbon gases or vapours or other carbon-containing compounds in the form of gas or vapour, e.g. carbon monoxide, alcohols
    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/16—Reducing
    • B01J37/18—Reducing with gases containing free hydrogen

Definitions

  • carbon nanotubes carbon nanotubes
  • CCVD process catalytic carbon vapor deposition
  • the contacting of catalytically active Metals with the gaseous carbon compound, in particular low molecular weight hydrocarbons takes place in a fixed bed (powder bed), in a moving fixed bed or in a fluidized bed.
  • the catalyst is used in a calcined form in the reactor, wherein the beginning of the reaction, the active centers of the catalyst are reduced from oxide to metal.
  • the diameter of the carbon nanotubes and fibers is determined essentially by the dimension of the catalytically active metal particles.
  • the metal particles whose dimensions must be in the nanometer range, and to ensure the handling of the catalysts, they are applied to catalytically inert support materials, usually oxide ceramics, which are not reduced by hydrogen in the catalytically reaction, so that they are superficial domains of catalytically active Form metals whose dimensions determine the diameter of the fibers.
  • a disadvantage of the CCVD process is that the catalyst becomes inactive in the reaction by increasing the access of the gaseous carbon compound to the catalytically active domains by the fibers formed is hampered.
  • the yield of CNT per g of catalyst is dependent on the starting carbon compounds, the type of catalyst, its structure and the process conditions such as temperature, pressure, concentration, etc.
  • EP 1401763 B1 is based on finely divided aluminum hydroxide
  • Support material which is recovered from a gel by drying and milling, which is mixed with a solution of cobalt acetate and iron nitrate in a mortar and then dried.
  • Other support materials such as oxides, hydroxides and carbonates of calcium, magnesium, cerium, titanium and lanthanum and their combinations and catalytically active metals Ni, Cu, V, Mo and Sn and mixtures thereof are also described.
  • the weight ratio of carrier material to catalytically active metals is about 30: 1. It is achieved a yield of up to 200% carbon nanotubes or fibers based on the weight of the catalyst. The catalyst must therefore be removed from the carbon nanotubes or fibers consuming.
  • such a multi-stage production process for the catalyst is complicated and leads only to a small proportion of catalytically active metals, correspondingly low yields of CNT based on the catalyst.
  • WO 2006/050903 a single-stage precipitation process for the catalyst is also already disclosed in which support material and active metals are precipitated together from aqueous solutions of the respective nitrates.
  • the teaching of the WO document is concerned in particular with the optimization of the composition of the catalytically active metals to obtain a high yield of CNT based on the catalyst used, with active metal compositions Mn-Co, which may optionally further contain Mo, with MgO as a carrier material, with 60 mol.% of active metal and 40 mol.% of support metal yields of 5 to 350 times CNT based on the weight of the catalyst.
  • Catalyst is therefore not required in most applications.
  • the co-precipitation of catalytically active metals and support material is, however, in relation to the desired properties for the preparation of CNT (reproducible catalytic activity and uniformity of dimensions of the catalytically active domains) difficult to control.
  • the processing of the nitrate-containing mother liquor from the precipitation which is already necessary for reasons of environmental protection, is complicated.
  • the catalyst particles consisting of support materials and domains of catalytically active metals have sufficient fluidity with regard to handling, ie have at least an average particle size in the range of a few ⁇ m, and, on the other hand, decay during the catalytic process, so that the catalytically active domains or primary particles remain well accessible or accessible even with growing CNT for the gaseous starting carbon compound. Due to the co-precipitation of support materials and catalytically active metals as hydroxides and subsequent thermal conversion into oxides, it comes to a strong, the disintegration of
  • the object of the invention is to provide a simple process for the preparation of catalysts, which overcomes the disadvantages of the prior art.
  • the precipitation of catalytically active metals and support materials from corresponding salt solutions takes place locally without any intermediate work-up prior to the combination of locally separate precipitation suspensions.
  • This makes it possible, in particular to control the precipitation of the catalytically active metals in the sense of a uniform particle size to produce uniform diameter of the CNT and to produce clearly separated primary particles of support materials and catalytically active metals.
  • the novel process is preferably based on a sulfate system, ie the starting compounds for the catalytically active metals and the support materials are used as aqueous sulfate solutions.
  • chlorides also leads to good products and is unproblematic in terms of wastewater.
  • the precipitation is preferably carried out by means of alkali hydroxide, in particular ammonia and / or sodium hydroxide solution, so that after removal of the precipitated solid, a mother liquor containing readily worked-up ammonium sulfate and / or sodium sulfate is formed.
  • alkali hydroxide in particular ammonia and / or sodium hydroxide solution
  • the precipitation preferably takes place in a common container with two regions for mixing the salt solution containing the catalytically active metals with the base solution on the one hand and the carrier material salt solution with the mother liquor or further base solution on the other hand. This allows the separate control of the precipitation conditions such as pH, concentration and temperature for the precipitation of catalytically active metals on the one hand and
  • the two mixing ranges are expediently equipped with one stirrer each.
  • the mixture may also be characterized by e.g. tangential or countercurrent injection of the respective reaction solutions in the respective mixing area.
  • the mixing range for precipitating the catalytically active metals is preferably less than 1/100, more preferably less than 1/500, and more than 1/3000 of the container volume, with a correspondingly short residence time in the mixing range of less than one minute.
  • Suitable catalytically active metals are unstable carbide-forming metals, in particular Fe, Ni, Co, Cu, Mn, Sn and Zn and mixtures thereof. They are present after the precipitation as hydroxides or oxyhydroxides. Particularly preferred are mixtures of Co and Mn in the ratio of 1: 3 to 3: 1 molar, optionally further modified by Mo in an amount up to 10% molar.
  • the metal salt solutions of the catalytically active metals are introduced into the region of a first stirrer, wherein a high supersaturation of the mother liquor in the region of the first stirrer is produced, preferably by simultaneous excess introduction of alkali into the region of this first stirrer.
  • the pH in the area of the first stirrer becomes lower
  • oxygen or oxygen-containing gas such as air can be injected into the region of the first stirrer in order to produce a simultaneous one
  • the carrier metal salt solutions are introduced into the second stirrer zone and mixed here with the alkaline mother liquor, wherein the hydroxides of the carrier metal are precipitated.
  • a basic solution preferably ammonia solution and / or sodium hydroxide solution
  • a pH of 8 to 11 is generally sufficient here.
  • the precipitation of the support materials takes place at a pH of 9 to 10.5.
  • Preferred support metals are Mg, Al, Ca, Si, Ti, Y, Zr and mixtures thereof, which can be modified by contents of V, Mo and / or W. Preference is given to Mg or Al, in particular Mg, more preferably up to 10 mol% Mo.
  • the precipitation conditions for the carrier metal hydroxides are adjusted to produce hydroxide particles having an average diameter of 2 to 10 times the diameter of the hydroxide particles of the catalytically active metals.
  • the salts of the catalytically active metals and the salts of the carrier metals are introduced into the reactor in a molar ratio of between 0.2 and 2, preferably between 0.7 and 1.3, calculated as oxides.
  • the suspension obtained is stirred for a period of time, so that an agglomeration of the hydroxide particles is effected. This period may extend over 0.5 to 10 hours, preferably 1 to 3 hours.
  • different hydroxide particles are initially deposited on each other, so that in the agglomerates predominantly carrier material primary particles are superficially agglomerated with superficial particles of active material.
  • Spheroidal agglomerate particles are predominantly obtained which have a mean agglomerate diameter of up to 80 ⁇ m, preferably 2 to 50 ⁇ m, particularly preferably less than 20 ⁇ m.
  • the spherical ones Agglomerate particles have a porosity of> 5% by volume, preferably> 10% by volume and more preferably of> 20% by volume.
  • the resulting, consisting of carrier primary particles and catalytically active primary particles agglomerates are separated from the mother liquor, washed neutral and dried and calcined in air at 350 to 500 0 C.
  • the calcination subsequent to drying may also be carried out immediately before the catalytic process is carried out before or during the activation phase.
  • FIG. 1 shows schematically a reactor 1 suitable for the preferably continuous performance of the process according to the invention.
  • the reactor has a reactor vessel 2 with two agitators 3 and 4, with corresponding mixing areas in which the agitators develop shearing action on the vessel liquid.
  • the stirrer area for the precipitation of the catalytically active metals is shielded by a cylindrical shield plate 5 which is open in the vertical direction. In the volume small
  • Stirrer area in the agitator 3 is fed via line 6 in the preferred case, aqueous active metal sulfate solution and via line 7 sodium hydroxide solution and / or aqueous ammonia solution.
  • the carrier metal sulfates are fed via line 8 and optionally sodium hydroxide solution and / or ammonia solution via line 9.
  • dilution water can be fed via line 10 to control the maturation and agglomeration process of the hydroxides precipitated in the stirrer zones.
  • precipitation suspension is withdrawn via line 11.
  • a reactor is shown schematically, the third stirrer 12 and a shield 13 for more separate precipitation of the carrier metals having.
  • the same reference numerals as in Figure 1 denote the same elements.
  • the separation of particles from the mother liquor can be carried out by methods known per se, for example by sedimentation, in cyclones, rotary separators or by filtration.
  • the catalyst powders according to the invention can be used for the production of carbon nanotubes and / or carbon fibers.
  • a reactor according to FIG. 1 is used.
  • the laboratory reactor has a liquid volume of 10 I.
  • the stirrer area 3 has a volume of 20 ml.
  • the streams 6 to 10 corresponding to the reference numbers in FIG. 1 are supplied at room temperature in the amount and concentration shown in Table 1.
  • the material flows are regulated gravimetrically. In each case after setting stationary conditions, the solid is filtered off from the mother liquor over 3 hours, washed neutral on the filter and dried at 150 ° C. and calcined at 420 ° C. in air.
  • the average catalyst particle size becomes optically 35 to 40 ⁇ m
  • the particles consist of spherically agglomerated carrier particles which are superficially coated with a large number of smaller oxide particles of the catalytically active metals.
  • the activity of the catalyst powders is tested as follows: 0.5 g of each
  • Catalyst powder are filled in a thin layer in a quartz boat, which is inserted into a quartz glass tube.
  • the quartz glass tube is placed in a tube furnace and connected to gas pipes on both sides.
  • the Quartz glass tube is rinsed with a mixture of 60 vol .-% hydrogen and 40 vol.% Argon and heated slowly under flowing purge gas to 630 0 C, wherein the oxide particles of the catalytically active metals are reduced to the metal. Due to the consequent decrease in volume of the catalytically active primary particles, there are stresses in the agglomerates which lead to the disintegration of the agglomerates. After 60 minutes then 50% of the purge gas is replaced by ethene (ethylene).

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Nanotechnology (AREA)
  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Thermal Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Textile Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Composite Materials (AREA)
  • Catalysts (AREA)

Abstract

L'invention concerne une nouvelle poudre de catalyseur, son procédé de production, ainsi que son utilisation pour la production de nanotubes de carbone et/ou de fibres.
EP08870192A 2008-01-11 2008-12-18 Poudre de catalyseur Withdrawn EP2231329A2 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102008004135.1A DE102008004135B4 (de) 2008-01-11 2008-01-11 Katalysatorpulver
PCT/EP2008/067877 WO2009087040A2 (fr) 2008-01-11 2008-12-18 Poudre de catalyseur

Publications (1)

Publication Number Publication Date
EP2231329A2 true EP2231329A2 (fr) 2010-09-29

Family

ID=40718845

Family Applications (1)

Application Number Title Priority Date Filing Date
EP08870192A Withdrawn EP2231329A2 (fr) 2008-01-11 2008-12-18 Poudre de catalyseur

Country Status (4)

Country Link
EP (1) EP2231329A2 (fr)
DE (1) DE102008004135B4 (fr)
TW (1) TWI433728B (fr)
WO (1) WO2009087040A2 (fr)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102013214229A1 (de) * 2013-07-19 2015-01-22 Bayer Materialscience Ag Verfahren zur Herstellung eines effizienten Katalysators für die Produktion mehrwandiger Kohlenstoffnanoröhrchen, mehrwandiges Kohlenstoffnanoröhrchen und Kohlenstoffnanoröhrchenpulver
EP2835177A1 (fr) * 2013-08-06 2015-02-11 Bayer Technology Services GmbH Procédé de préparation de catalyseurs à base de carbone et leur utilisation
DE102015108749A1 (de) 2015-06-02 2016-12-08 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Verfahren zur großmaßstäblichen, nasschemischen Herstellung von ZnO Nanopartikeln mit Hilfe von Luftblasen

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT36124B (de) 1905-04-17 1909-02-10 Albert Hellwig Apparat zur Beschleunigung des Filtrierens und Auslaugens extrakthaltiger Substanzen.
NL190750C (nl) * 1984-06-21 1994-08-01 Unilever Nv Nikkelaluminaat katalysator, de bereiding daarvan en het hydrogeneren van onverzadigde organische verbindingen daarmee.
EP0200315A3 (fr) * 1985-03-25 1988-05-25 Imperial Chemical Industries Plc Catalyseurs
CA1321863C (fr) * 1986-06-06 1993-09-07 Howard G. Tennent Feuilles de carbone, methode de production connexe, et compositions contenant de tels elements
IT1248656B (it) * 1990-05-29 1995-01-26 Mini Ricerca Scient Tecnolog Processo per la produzione del precursore di un catalizzatore precipitato per la sintesi dell`ammoniaca.
JP3858625B2 (ja) * 2000-07-27 2006-12-20 株式会社豊田中央研究所 複合酸化物とその製造方法及び排ガス浄化用触媒とその製造方法
FR2826596B1 (fr) * 2001-06-28 2004-08-13 Toulouse Inst Nat Polytech Compositon catalytique pour la fabrication selective de nanotubes de carbone ordonne en lit fluidise, et son procede de fabrication
DE60203508T3 (de) 2001-07-03 2010-09-02 Facultés Universitaires Notre-Dame de la Paix Katalysatorträger und hierauf hergestellte kohlenstoffnanoröhren
JP3797313B2 (ja) * 2002-10-28 2006-07-19 トヨタ自動車株式会社 金属酸化物粒子の製造法及び排ガス浄化用触媒
UY28921A1 (es) * 2004-05-28 2005-06-30 Mintek Catalizador y produccion y uso del mismo
DE102004054959A1 (de) * 2004-11-13 2006-05-18 Bayer Technology Services Gmbh Katalysator zur Herstellung von Kohlenstoffnanoröhrchen durch Zersetzung von gas-förmigen Kohlenverbindungen an einem heterogenen Katalysator
DE102005032071A1 (de) * 2005-07-08 2007-01-11 Zentrum für Sonnenenergie- und Wasserstoff-Forschung Baden-Württemberg Gemeinnützige Stiftung e.V. Nanoporöse Katalysatorteilchen, deren Herstellung und deren Verwendung
DE102006007147A1 (de) * 2006-02-16 2007-08-23 Bayer Technology Services Gmbh Verfahren zur kontinuierlichen Herstellung von Katalysatoren

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2009087040A2 *

Also Published As

Publication number Publication date
TW200948478A (en) 2009-12-01
TWI433728B (zh) 2014-04-11
DE102008004135B4 (de) 2014-03-06
DE102008004135A1 (de) 2009-07-23
WO2009087040A3 (fr) 2012-03-29
WO2009087040A2 (fr) 2009-07-16

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