US2011172085A1PendingUtilityA1

Nanocrystalline copper oxide, and method for the production thereof

Assignee: SUED CHEMIE AGPriority: May 30, 2008Filed: May 29, 2009Published: Jul 14, 2011
Est. expiryMay 30, 2028(~1.8 yrs left)· nominal 20-yr term from priority
B01J 35/77B01J 35/45B01J 35/393B01J 37/0045C01G 3/02C01P 2006/12C01P 2004/60Y10T428/2982C01P 2006/13B01J 23/72B01J 37/18B01J 37/0236C01P 2006/80B01J 21/16B01J 35/613B01J 35/615
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Claims

Abstract

A nanocrystalline supported or unsupported copper oxide with a residual carbon content of <10% and a BET surface area >95 m 2 /g. Further, a method for the production of a supported or unsupported nanocrystalline copper oxide as well as the use thereof in catalysis, in particular in the steam reforming of methanol or in the hydrogenation of esters.

Claims

exact text as granted — not AI-modified
1 . Nanocrystalline copper oxide with a BET surface area >95 m 2 /g. 
     
     
         2 . Nanocrystalline copper oxide according to  claim 1 , wherein the BET surface area lies in a range of from 95 to 300 m 2 /g. 
     
     
         3 . Nanocrystalline copper oxide according to  claim 2  with a carbon content of <5%. 
     
     
         4 . Nanocrystalline copper oxide according to  claim 3  with a particle size of <100 μm. 
     
     
         5 . Supported nanocrystalline copper oxide according to  claim 1 , wherein the support contains a material selected from the group consisting of SiO 2 , ZrO 2 , bentonite, montmorillonite, Al 2 O 3 , TiO 2 , ZnO, MgSiO 4 , aluminosilicates, or mixtures thereof. 
     
     
         6 . Supported nanocrystalline copper oxide according to  claim 5  with a particle size in the range of from 50 nm to 200 μm. 
     
     
         7 . Shaped bodies containing copper oxide and/or supported copper oxide according to  claim 1 . 
     
     
         8 . Method for the production of nanocrystalline copper oxide comprising the steps of
 a) the introduction of a copper starting compound into a reaction chamber by means of a carrier fluid, and wherein the copper starting compound is introduced into the reaction chamber in the form of a solution, slurry, suspension or in solid aggregate state,   b) a thermal treatment of the copper starting compound in a treatment zone of the reaction chamber by means of a pulsating flow at a temperature of from 200 to 500° C.,   c) the formation of nanocrystalline copper oxide material,   d) the discharge of the nanocrystalline copper oxide material obtained in steps b) and c) from the reactor.   
     
     
         9 . Method according to  claim 8 , wherein the copper starting compound is used as suspension with an average particle size of <10 μm. 
     
     
         10 . Method according to  claim 8 , wherein the particle size is obtained by grinding the copper starting compound before the production of the suspension. 
     
     
         11 . Method according to  claim 8 , wherein the copper starting compound is used as solution. 
     
     
         12 . Method according to  claim 8 , wherein, as copper starting compound, a compound selected from the group consisting of a copper salt of an organic acid, a hydroxide, a nitrate, a carbonate, a hydroxocarbonate or mixtures thereof is used. 
     
     
         13 . Method according to  claim 12 , wherein, as organic acid, an organic acid with fewer than 9 carbon atoms is used. 
     
     
         14 . Method according to  claim 13 , wherein the organic acid is selected from the group consisting of glyoxalic acid, oxalic acid, citric acid, derivatives thereof as well as carbonic acid (carbonate). 
     
     
         15 . Method according to  claim 7 , wherein, in addition to the copper starting compound, further compounds are also used. 
     
     
         16 . Method according to  claim 15 , wherein the further compounds are selected from the group consisting of compounds of silicon, tin, magnesium, titanium, aluminium, zirconium, zinc as well as mixtures thereof. 
     
     
         17 . Use of a nanocrystalline supported or unsupported copper oxide according to  claim 1  as catalyst or catalyst precursor. 
     
     
         18 . Use according to  claim 17  for the steam reforming of methanol or for the hydrogenation of esters. 
     
     
         19 . Use according to  claim 17 , wherein the supported or unsupported copper oxide is reduced to metallic copper before use in a catalytic reaction. 
     
     
         20 . Copper-containing catalyst that can be obtained by reduction of the nanocrystalline supported or unsupported copper oxide according to  claim 1 .

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