US20090203518A1 - Catalyst additives - Google Patents
Catalyst additives Download PDFInfo
- Publication number
- US20090203518A1 US20090203518A1 US12/298,378 US29837807A US2009203518A1 US 20090203518 A1 US20090203518 A1 US 20090203518A1 US 29837807 A US29837807 A US 29837807A US 2009203518 A1 US2009203518 A1 US 2009203518A1
- Authority
- US
- United States
- Prior art keywords
- nickel
- slurry
- catalyst
- nickel slurry
- rheology modifier
- 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.)
- Abandoned
Links
- 239000003054 catalyst Substances 0.000 title description 16
- 239000000654 additive Substances 0.000 title description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims abstract description 96
- 229910052759 nickel Inorganic materials 0.000 claims abstract description 39
- 239000002002 slurry Substances 0.000 claims abstract description 38
- 239000006254 rheological additive Substances 0.000 claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 230000000694 effects Effects 0.000 claims abstract description 9
- 229920001285 xanthan gum Polymers 0.000 claims description 4
- 229940082509 xanthan gum Drugs 0.000 claims description 4
- 235000010493 xanthan gum Nutrition 0.000 claims description 4
- 239000000230 xanthan gum Substances 0.000 claims description 4
- 239000000839 emulsion Substances 0.000 claims description 3
- 229920002678 cellulose Polymers 0.000 claims description 2
- 235000010980 cellulose Nutrition 0.000 claims description 2
- 150000004676 glycans Chemical class 0.000 claims description 2
- 229920001282 polysaccharide Polymers 0.000 claims description 2
- 239000005017 polysaccharide Substances 0.000 claims description 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- 239000002245 particle Substances 0.000 description 7
- 239000000047 product Substances 0.000 description 6
- 239000000463 material Substances 0.000 description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- AZUYLZMQTIKGSC-UHFFFAOYSA-N 1-[6-[4-(5-chloro-6-methyl-1H-indazol-4-yl)-5-methyl-3-(1-methylindazol-5-yl)pyrazol-1-yl]-2-azaspiro[3.3]heptan-2-yl]prop-2-en-1-one Chemical compound ClC=1C(=C2C=NNC2=CC=1C)C=1C(=NN(C=1C)C1CC2(CN(C2)C(C=C)=O)C1)C=1C=C2C=NN(C2=CC=1)C AZUYLZMQTIKGSC-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000004128 high performance liquid chromatography Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000002243 precursor Substances 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000012018 catalyst precursor Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000013256 coordination polymer Substances 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- BNIILDVGGAEEIG-UHFFFAOYSA-L disodium hydrogen phosphate Chemical compound [Na+].[Na+].OP([O-])([O-])=O BNIILDVGGAEEIG-UHFFFAOYSA-L 0.000 description 1
- 229910000397 disodium phosphate Inorganic materials 0.000 description 1
- 239000003480 eluent Substances 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 150000002815 nickel Chemical class 0.000 description 1
- 150000002816 nickel compounds Chemical class 0.000 description 1
- -1 nickel halides Chemical class 0.000 description 1
- 229910000480 nickel oxide Inorganic materials 0.000 description 1
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical class [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Images
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
- B01J23/70—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
- B01J23/755—Nickel
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C209/00—Preparation of compounds containing amino groups bound to a carbon skeleton
- C07C209/24—Preparation of compounds containing amino groups bound to a carbon skeleton by reductive alkylation of ammonia, amines or compounds having groups reducible to amino groups, with carbonyl compounds
- C07C209/26—Preparation of compounds containing amino groups bound to a carbon skeleton by reductive alkylation of ammonia, amines or compounds having groups reducible to amino groups, with carbonyl compounds by reduction with hydrogen
Definitions
- the present invention relates to a nickel slurry comprising a nickel catalyst, water and additives to improve the flow behaviour of the nickel slurry.
- Nickel sponge catalysts generally consist of milled polymorphic particles up to 20 micrometers in size. These particles are commonly sold in drums containing alkaline water and nickel at a weight ratio of approximately 90:85 (Ni:water). The catalyst must be contained in water as it is pyrophoric and can spontaneously combust if allowed to dry out in air. Such a catalyst in water system is known as a ‘nickel slurry’.
- nickel oxides may be sold as catalysts for example nickel oxides, nickel halides, nickel complexes and nickel carbonyls but these are not generally provided as slurries.
- nickel compounds including those listed above will be suitable for use as a catalyst since certain properties of any material are key as to whether it is able to perform as a catalyst. Such properties include the requirement that the material has a clean surface and a high surface area thereby to enable the reactants to access the surface of the catalyst.
- WO 2006/063600 relates to adjusting catalysts' and catalyst precursors' suspension and settling properties using rheology modifiers, and concentrates on using rheology modifiers that speed up the rate of settling with nickel catalysts.
- additives may be used to improve the flow behaviour of the nickel slurry without detrimentally affecting the activity of the nickel catalyst.
- the invention provides a nickel slurry comprising a nickel catalyst, water and at least one rheology modifier, characterised in that the activity of the nickel catalyst is equal to or greater than the activity of the equivalent nickel catalyst contained in a slurry which does not comprise rheology modifiers, wherein the at least one rheology modifier provides high viscosity at low shear stress and low viscosity at high shear stress.
- Rheology modifiers are used to alter the flow characteristics of a material. We have found that to improve the flowability of the nickel slurry, it was necessary to have a continuous dispersion with very high viscosity at low shear stress, and low viscosity at high shear stress. This is sometimes referred to as pseudoplasticity and results from the structure of the rheology modifier forming a network at low shear stress that breaks down under high shear stress.
- rheology modifiers used in this invention are used to modify the flow characteristics of the nickel slurry itself, not to modify the flow characteristics of the dry nickel catalyst prior to slurry formation.) These characteristics enable the nickel particles to be suspended when at rest, thereby avoiding the formation of a dense cake of catalyst, but also allow the viscosity of the solution to drop when being poured, enhancing flowability and allowing the catalyst to be readily transferred from its container.
- Certain polymers and emulsions can be used to increase the viscosity of aqueous slurries and dispersions, including: polysaccharides, celluloses, hydrophobically modified alkali-swellable emulsions and polyhydroxycellulose derivatives, such as Xanthan gum and Rheovis 152 (Ciba Speciality Chemicals).
- a nickel slurry according to the invention may comprise from 1 ⁇ 10 ⁇ 3 wt % to 3 wt % rheology modifiers relative to the total weight of the slurry.
- Rheovis 152 is useful as a rheology modifier for nickel slurry as it is at its most efficient at approx. pH 11.
- FIG. 1 is a photograph of a sample of nickel slurry containing a rheology modifier, taken 16 hours after shaking.
- Example la The experiment described in Example la was repeated using 0.46 grams of Rheovis 152 (containing 0.18 grams active ingredient) in place of the Xanthan gum. Only a minimal amount of sedimentation was observed, directly after cessation of stirring and 16 hours later.
- a nickel catalyst sample prepared according to Example la was tested for its activity in a hydrogenation reaction.
- Catalytic hydrogenation converts a cyano-precursor into the corresponding methylamino substituent.
- Side products of the reaction may arise such as unknown materials, and secondary products from uncatalysed reactions of the product (see impurity 1 below).
- Each catalyst sample was shaken to allow a representative sample to be taken, then 2 ⁇ 1.4 grams of suspended catalyst was weighed into 2 tubes.
- To each tube 1.0 grams of cyano-substituted precursor, 7 ml methanol and 0.1 ml ‘880’ ammonia was added.
- the tubes were then sealed in a Baskerville multi-well autoclave and the apparatus purged three times with argon then 3 times with hydrogen before being pressurized to 4.5 bar hydrogen and heated to 40° C.
- the reaction mixture in each of the tubes was stirred and heated under constant pressure of hydrogen (maintained by a Buchi press-flow controller) overnight, the apparatus was then allowed to cool under hydrogen and finally the pressure within the autoclave was vented and the samples recovered. Samples from each tube were filtered and diluted 1:1 with water for analysis by HPLC.
- the nickel catalyst sample treated with the rheology modifier did not show a reduced catalytic activity relative to the untreated sample.
- the activity of the nickel catalyst sample treated with the rheology modifier appears to have increased, as evidenced by the increased conversion of starting material (note: Product 1 and Product 2 may be combined during further processing).
Abstract
A nickel slurry comprising a nickel catalyst, water and at least one rheology modifier, the activity of the nickel catalyst being equal to or greater than the activity of the equivalent nickel catalyst contained in a slurry which does not comprise rheology modifiers, wherein the at least one rheology modifier provides high viscosity at low shear stress and low viscosity at high shear stress.
Description
- The present invention relates to a nickel slurry comprising a nickel catalyst, water and additives to improve the flow behaviour of the nickel slurry.
- Nickel sponge catalysts generally consist of milled polymorphic particles up to 20 micrometers in size. These particles are commonly sold in drums containing alkaline water and nickel at a weight ratio of approximately 90:85 (Ni:water). The catalyst must be contained in water as it is pyrophoric and can spontaneously combust if allowed to dry out in air. Such a catalyst in water system is known as a ‘nickel slurry’.
- Other compounds of nickel may be sold as catalysts for example nickel oxides, nickel halides, nickel complexes and nickel carbonyls but these are not generally provided as slurries.
- Not all nickel compounds (including those listed above) will be suitable for use as a catalyst since certain properties of any material are key as to whether it is able to perform as a catalyst. Such properties include the requirement that the material has a clean surface and a high surface area thereby to enable the reactants to access the surface of the catalyst.
- Nickel particles in a nickel slurry tend to settle within the container in which they are housed, e.g. a drum, due to the high density of nickel compared to water (density of nickel=9 g cm−3, density of water=1 g cm−3). These particles may even form a dense cake of sediment. Banging and vibration of the nickel slurry container, such as might occur during transportation, appears to make the cake more dense. The settling of the nickel catalyst makes it difficult to pour or remove from the drum, this poor flow behaviour being especially problematic due to the pyrophoric nature of the dry catalyst.
- WO 2006/063600 relates to adjusting catalysts' and catalyst precursors' suspension and settling properties using rheology modifiers, and concentrates on using rheology modifiers that speed up the rate of settling with nickel catalysts.
- We have now found, surprisingly, that additives may be used to improve the flow behaviour of the nickel slurry without detrimentally affecting the activity of the nickel catalyst.
- According to one aspect, the invention provides a nickel slurry comprising a nickel catalyst, water and at least one rheology modifier, characterised in that the activity of the nickel catalyst is equal to or greater than the activity of the equivalent nickel catalyst contained in a slurry which does not comprise rheology modifiers, wherein the at least one rheology modifier provides high viscosity at low shear stress and low viscosity at high shear stress.
- Rheology modifiers are used to alter the flow characteristics of a material. We have found that to improve the flowability of the nickel slurry, it was necessary to have a continuous dispersion with very high viscosity at low shear stress, and low viscosity at high shear stress. This is sometimes referred to as pseudoplasticity and results from the structure of the rheology modifier forming a network at low shear stress that breaks down under high shear stress. (Note the rheology modifiers used in this invention are used to modify the flow characteristics of the nickel slurry itself, not to modify the flow characteristics of the dry nickel catalyst prior to slurry formation.) These characteristics enable the nickel particles to be suspended when at rest, thereby avoiding the formation of a dense cake of catalyst, but also allow the viscosity of the solution to drop when being poured, enhancing flowability and allowing the catalyst to be readily transferred from its container. Certain polymers and emulsions can be used to increase the viscosity of aqueous slurries and dispersions, including: polysaccharides, celluloses, hydrophobically modified alkali-swellable emulsions and polyhydroxycellulose derivatives, such as Xanthan gum and Rheovis 152 (Ciba Speciality Chemicals).
- A nickel slurry according to the invention may comprise from 1×10−3 wt % to 3 wt % rheology modifiers relative to the total weight of the slurry.
- Typically the nickel slurry will be alkaline, e.g. pH=11. We have found that Rheovis 152 is useful as a rheology modifier for nickel slurry as it is at its most efficient at approx. pH 11.
- In order that the invention may be more fully understood the following Examples are provided by way of illustration only and with reference to the accompanying drawings, in which:
-
FIG. 1 is a photograph of a sample of nickel slurry containing a rheology modifier, taken 16 hours after shaking. - 46 grams of a nickel catalyst slurry was placed in a jar and shaken. To this slurry 0.16 grams of Xanthan gum (CP Kelco, Kelzan HP) was added and the contents of the jar stirred for 20 minutes. On cessation of stirring, the nickel particles did not form a sediment. Furthermore, 16 hours after cessation of stirring no sedimentation of nickel particles could be seen (see
FIG. 1 ). - The experiment described in Example la was repeated using 0.46 grams of Rheovis 152 (containing 0.18 grams active ingredient) in place of the Xanthan gum. Only a minimal amount of sedimentation was observed, directly after cessation of stirring and 16 hours later.
- A nickel catalyst sample prepared according to Example la was tested for its activity in a hydrogenation reaction. Catalytic hydrogenation converts a cyano-precursor into the corresponding methylamino substituent. Side products of the reaction may arise such as unknown materials, and secondary products from uncatalysed reactions of the product (see impurity 1 below).
- Each catalyst sample was shaken to allow a representative sample to be taken, then 2×1.4 grams of suspended catalyst was weighed into 2 tubes. To each tube 1.0 grams of cyano-substituted precursor, 7 ml methanol and 0.1 ml ‘880’ ammonia was added. The tubes were then sealed in a Baskerville multi-well autoclave and the apparatus purged three times with argon then 3 times with hydrogen before being pressurized to 4.5 bar hydrogen and heated to 40° C. The reaction mixture in each of the tubes was stirred and heated under constant pressure of hydrogen (maintained by a Buchi press-flow controller) overnight, the apparatus was then allowed to cool under hydrogen and finally the pressure within the autoclave was vented and the samples recovered. Samples from each tube were filtered and diluted 1:1 with water for analysis by HPLC.
-
-
Equipment: Agilent 1100 Column: YMC basic, 25 × 0.46 cm Column temperature: 35° C. Eluent: Either 33/67 MeOH/H2O or 27/73 MeOH/H2O containing 0.005 M Na2HPO4 acidified with H3PO4 to pH 2 Flow rate: 1 ml/min Injection vol. 20 microlitres Detection: Refractive index, 35° C. -
-
Starting Sample Product 1 Product 2 Material Impurity 1 Example 1a (unmodified) 5 6 69 20 Example 1a (modified) 16.2 12.8 45 25 - As can be seen the nickel catalyst sample treated with the rheology modifier did not show a reduced catalytic activity relative to the untreated sample. In fact the activity of the nickel catalyst sample treated with the rheology modifier appears to have increased, as evidenced by the increased conversion of starting material (note: Product 1 and Product 2 may be combined during further processing).
Claims (8)
1. A nickel slurry comprising a nickel catalyst, water and at least one rheology modifier, wherein the activity of the nickel catalyst is equal to or greater than the activity of an equivalent nickel catalyst contained in a slurry which does not comprise rheology modifiers, wherein the at least one rheology modifier provides high viscosity at low shear stress and low viscosity at high shear stress.
2. A nickel slurry according to claim 1 wherein the at least one rheology modifier is selected from the group consisting of polysaccharides, celluloses, hydrophobically modified alkali-swellable emulsions, polyhydroxycellulose derivatives and any combination thereof.
3. A nickel slurry according to claim 1 , wherein the nickel slurry comprises from 1×10−3 wt % to 3 wt % rheology modifiers relative to the total weight of the slurry.
4. A nickel slurry according to claim 1 , wherein the nickel slurry is alkaline.
5. A nickel slurry according to claim 2 , wherein the nickel slurry comprises from 1×10−3 wt % to 3 wt % rheology modifiers relative to the total weight of the slurry.
6. A nickel slurry according to claim 2 , wherein the nickel slurry is alkaline.
7. A nickel slurry according to claim 3 , wherein the nickel slurry is alkaline.
8. A nickel slurry according to claim 1 , wherein the at least one rheology modifier is xanthan gum.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GBGB0608359.6A GB0608359D0 (en) | 2006-04-28 | 2006-04-28 | Catalyst additives |
| GB0608359.6 | 2006-04-28 | ||
| PCT/GB2007/050206 WO2007125361A1 (en) | 2006-04-28 | 2007-04-23 | Catalyst additives |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/GB2007/050206 A-371-Of-International WO2007125361A1 (en) | 2006-04-28 | 2007-04-23 | Catalyst additives |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US12/825,971 Division US8501660B2 (en) | 2006-04-28 | 2010-06-29 | Catalyst additives |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20090203518A1 true US20090203518A1 (en) | 2009-08-13 |
Family
ID=36589928
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US12/298,378 Abandoned US20090203518A1 (en) | 2006-04-28 | 2007-04-23 | Catalyst additives |
| US12/825,971 Active US8501660B2 (en) | 2006-04-28 | 2010-06-29 | Catalyst additives |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US12/825,971 Active US8501660B2 (en) | 2006-04-28 | 2010-06-29 | Catalyst additives |
Country Status (14)
| Country | Link |
|---|---|
| US (2) | US20090203518A1 (en) |
| EP (1) | EP2012919B1 (en) |
| JP (1) | JP5380279B2 (en) |
| KR (1) | KR101426967B1 (en) |
| CN (1) | CN101426578B (en) |
| BR (1) | BRPI0710804B1 (en) |
| CA (1) | CA2646394C (en) |
| ES (1) | ES2773058T3 (en) |
| GB (1) | GB0608359D0 (en) |
| MX (1) | MX2008013778A (en) |
| PL (1) | PL2012919T3 (en) |
| RU (1) | RU2404856C2 (en) |
| WO (1) | WO2007125361A1 (en) |
| ZA (1) | ZA200808688B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10124323B2 (en) * | 2016-12-22 | 2018-11-13 | National Cheng Kung University | Nano-nickel catalyst and hydrogenation device of carbon oxides |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3310870A (en) * | 1967-03-28 | Process for producing nickel-coated steel | ||
| US3989863A (en) * | 1975-07-09 | 1976-11-02 | The International Nickel Company, Inc. | Slurry coating process |
| US4867857A (en) * | 1987-03-14 | 1989-09-19 | Deutsche Automobilgesellschaft Mbh | Method for the manufacture of catalyst electrodes with structurally connected carrier bodies and suitable catalyst suspensions |
| US20020028860A1 (en) * | 1999-04-16 | 2002-03-07 | E. Michael Kerr | Method of modifying rheology of slurries in mineral processing |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4155943A (en) * | 1977-11-11 | 1979-05-22 | The Goodyear Tire & Rubber Company | Hydrogenation using surfactants |
| US5019135A (en) * | 1987-10-13 | 1991-05-28 | Battelle Memorial Institute | Method for the catalytic conversion of lignocellulosic materials |
| GB8728483D0 (en) * | 1987-12-04 | 1988-01-13 | Ciba Geigy Ag | Chemical compounds |
| CA2131173C (en) * | 1992-03-16 | 1998-12-15 | Brian J. Roselle | Fluid compositions containing polyhydroxy fatty acid amides |
| JPH09225317A (en) * | 1996-02-26 | 1997-09-02 | Kemipuro Kasei Kk | Nickel/noble metal binary metal cluster and catalyst made from the cluster and its preparation |
| WO1998000256A1 (en) | 1996-06-28 | 1998-01-08 | Sandvik Ab (Publ) | Method of spray drying powder mixtures |
| US6379640B1 (en) * | 1999-03-05 | 2002-04-30 | E. I. Du Pont De Nemours And Company | Process for the decomposition of nitrous oxide |
| AU2002219935A1 (en) * | 2000-11-28 | 2002-06-11 | Focal, Inc. | Polyalkylene glycol viscosity-enhancing polymeric formulations |
| JP2003068292A (en) | 2001-08-23 | 2003-03-07 | Hitachi Maxell Ltd | Electrode and battery using the same |
| US20090264679A1 (en) | 2004-12-14 | 2009-10-22 | Daniel Ostgard | Control of metal catalyst settling rates, settling densities and improved performance via use of flocculants |
-
2006
- 2006-04-28 GB GBGB0608359.6A patent/GB0608359D0/en not_active Ceased
-
2007
- 2007-04-23 EP EP07733628.7A patent/EP2012919B1/en active Active
- 2007-04-23 PL PL07733628T patent/PL2012919T3/en unknown
- 2007-04-23 ES ES07733628T patent/ES2773058T3/en active Active
- 2007-04-23 MX MX2008013778A patent/MX2008013778A/en active IP Right Grant
- 2007-04-23 KR KR1020087026266A patent/KR101426967B1/en active IP Right Grant
- 2007-04-23 WO PCT/GB2007/050206 patent/WO2007125361A1/en active Application Filing
- 2007-04-23 RU RU2008146973/04A patent/RU2404856C2/en active
- 2007-04-23 CN CN2007800139667A patent/CN101426578B/en not_active Expired - Fee Related
- 2007-04-23 CA CA2646394A patent/CA2646394C/en active Active
- 2007-04-23 US US12/298,378 patent/US20090203518A1/en not_active Abandoned
- 2007-04-23 JP JP2009507179A patent/JP5380279B2/en not_active Expired - Fee Related
- 2007-04-23 BR BRPI0710804A patent/BRPI0710804B1/en not_active IP Right Cessation
-
2008
- 2008-10-10 ZA ZA200808688A patent/ZA200808688B/en unknown
-
2010
- 2010-06-29 US US12/825,971 patent/US8501660B2/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3310870A (en) * | 1967-03-28 | Process for producing nickel-coated steel | ||
| US3989863A (en) * | 1975-07-09 | 1976-11-02 | The International Nickel Company, Inc. | Slurry coating process |
| US4867857A (en) * | 1987-03-14 | 1989-09-19 | Deutsche Automobilgesellschaft Mbh | Method for the manufacture of catalyst electrodes with structurally connected carrier bodies and suitable catalyst suspensions |
| US20020028860A1 (en) * | 1999-04-16 | 2002-03-07 | E. Michael Kerr | Method of modifying rheology of slurries in mineral processing |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10124323B2 (en) * | 2016-12-22 | 2018-11-13 | National Cheng Kung University | Nano-nickel catalyst and hydrogenation device of carbon oxides |
Also Published As
| Publication number | Publication date |
|---|---|
| EP2012919A1 (en) | 2009-01-14 |
| EP2012919B1 (en) | 2019-12-11 |
| RU2404856C2 (en) | 2010-11-27 |
| CN101426578A (en) | 2009-05-06 |
| BRPI0710804B1 (en) | 2018-10-23 |
| PL2012919T3 (en) | 2020-10-05 |
| RU2008146973A (en) | 2010-06-10 |
| KR20090010967A (en) | 2009-01-30 |
| GB0608359D0 (en) | 2006-06-07 |
| JP2009535192A (en) | 2009-10-01 |
| JP5380279B2 (en) | 2014-01-08 |
| CA2646394A1 (en) | 2007-11-08 |
| US8501660B2 (en) | 2013-08-06 |
| KR101426967B1 (en) | 2014-08-06 |
| US20100280274A1 (en) | 2010-11-04 |
| WO2007125361A1 (en) | 2007-11-08 |
| CN101426578B (en) | 2012-07-04 |
| BRPI0710804A2 (en) | 2011-08-23 |
| ZA200808688B (en) | 2009-12-30 |
| MX2008013778A (en) | 2009-02-03 |
| ES2773058T3 (en) | 2020-07-09 |
| CA2646394C (en) | 2014-06-03 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US10898883B2 (en) | Silicalite-1 molecular sieve-based catalyst and preparation method for 1,2-pentanediol using said catalyst | |
| CA2816628A1 (en) | Process for preparing an industrial hydroconversion catalyst, catalyst thus obtained and use thereof in a hydroconversion process | |
| CA2630365A1 (en) | Ultradispersed catalyst compositions and methods of preparation | |
| CA2615210A1 (en) | Process for slurry hydroconversion of heavy hydrocarbon charges in the presence of a dispersed active phase and an alumina oxide | |
| CN102648048B (en) | Faujasite zeolite preparation process | |
| GB1593007A (en) | Hydrogenation catalysts | |
| US8501660B2 (en) | Catalyst additives | |
| JP3341011B2 (en) | Catalyst support and hydrogenation catalyst | |
| JP5794527B2 (en) | Immobilized palladium catalyst | |
| EP1896363B1 (en) | Euo structural type zeolite containing the cation n,n- dimethyl-n,n-di(3,3-dimethylbutyl)ammonium, and the production method thereof | |
| CN101084064B (en) | The improved control of metal catalyst settling rates, settling densities and improved performance via use of flocculants | |
| CN101942322A (en) | Lubricating oil base oil producing method | |
| CA2366424A1 (en) | A process for hydroconverting a heavy hydrocarbon chargestock | |
| CN111841630A (en) | Fatty acid nickel oil-soluble catalyst for coal/heavy oil hydrogenation co-refining and application thereof | |
| Jordão et al. | Characterization of Pt/HUSY and Pt-Ni/HUSY catalysts by transmission electron microscopy | |
| RU2675249C1 (en) | Method for obtaining suspension of molybden-containing composite catalyst for hydroconversion of heavy oil stock | |
| EP0527219B1 (en) | Ruthenium sulphur hydrorefining catalyst, synthesis thereof and hydrorefining method using said catalyst | |
| ZA200103926B (en) | Catalytic dewaxing process. | |
| CN105582983B (en) | A kind of paraffin hydrocarbon selects the preparation method of type isomerization catalyst | |
| WO2023187732A1 (en) | Renewable biomass feed slurry hydroprocessing | |
| CA2431535A1 (en) | Colloidal catalyst | |
| CN117101673A (en) | Ni-Re bimetallic-based catalyst and preparation method and application thereof | |
| EP0556108A1 (en) | Use in a hydrocarboneous charge hydrorefining process of a gallium phosphate containing catalyst | |
| Osseo-Asare et al. | Novel nanodispersed coal liquefaction catalysts: Molecular design via microemulsion-based synthesis. Technical progress report, October--December 1991 | |
| JPH03275728A (en) | Production of powdery blocked polyisocyanate |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: JOHNSON MATTHEY PLC, UNITED KINGDOM Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:DALTON, JAMES SPENCER;REEL/FRAME:021748/0776 Effective date: 20080919 |
|
| STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |