US2004151661A1PendingUtilityA1

Manufacturing method for ferrite type magnets

38
Assignee: UGIMAG SAPriority: Nov 30, 1999Filed: Jan 26, 2004Published: Aug 5, 2004
Est. expiryNov 30, 2019(expired)· nominal 20-yr term from priority
C04B 35/26H01F 41/0273C04B 35/2633
38
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Claims

Abstract

A method for making ferrite magnets of formula M 1-x R x Fe 12-y T y O 19 including: a1) forming a powder mixture MP of related raw materials, a2) transforming into granules in green state A, b) calcining the granules in green state to form clinker B, c) wet ding clinker B to obtain a homogeneous dispersion of fine particles C, d) concentrating and compressing the particles under an orienting magnetic field to form an anisotropic green compact D, and e) sintering the green compact to obtain a sintered element E. In step a1), MP is formed from a dry mixture MS of M and Fe powder elements and a dispersion DF of raw materials related to elements R and T, and in step b) the granules in green state are calcined to obtain a clinker B which is homogeneous in chemical composition and size and with apparent low density, between 2.5 and 3.5.

Claims

exact text as granted — not AI-modified
1 . Manufacturing method for permanent magnets of the ferrite type comprising a magnetoplumbite phase of formula M 1-x R x Fe 12-y T y O 19  in which M=Ba, Sr, Ca or Pb, R=Bi or other elements of the rare earths family, T=Mn,Co,Ni,Zn, with x and y comprised between 0.05 and 0.5 in which: 
 a1) one forms in a mixing means, typically a mixer (3) operating by batch, a pulverulent mixture MP of raw materials related t the elements M, R, Fe and T, typically under the form of oxide, carbonate or hydroxide, comprising water in a predetermined quantity, typically necessary for the formation of granules in the subsequent stage,    a2) next one transforms, typically in a granulator (4), said mixture into green granules A, with a possible addition of extra water,    b) said green granules are calcinated in a calcination furnace (5) to form a clinker B, with a magnetoplumbite phase base of formula M 1-x R x Fe 12-y T y O 19 ,    c) one carries out a wet grinding of said clinker, typically in a dispersion apparatus (6) in aqueous medium, to obtain a homogeneous dispersion C of fine de-agglomerated particles of average particle size less than 1.2 μm,    d) one concentrates and compresses said particles under an orienting magnetic field to form a green compact D, anisotropic, able to be manipulated and of predetermined shape,    e) one sinters said anisotropic green compact D to obtain a sintered element E,    f) one possibly dimensions the final size of said sintered element E, typically by machining, a method characterised in that:    1) at stage a1) of the method, one forms said mixture MP, by introducing into said mixing means (3), a dry mixture MS of powders corresponding to said raw materials relative to the elements M and Fe, typically formed in a dry mixer (1), and a homogeneous fluid dispersion DF of said raw materials relative to the elements R and T typically in said pre-determined quantity of water, formed typically in a dispersion apparatus (2);    2) at stage b) of the method, said green granules A are calcinated at a chosen temperature and for a chosen length of time,    in such a way as to obtain, at the exit from the calcination furnace (5) at the end of stage b), a clinker B which is both homogeneous in chemical composition and size, and of low apparent density, comprised between 2.5 and 3.5 and which can be ground easily during stage c).    
     
     
         2 . Method according to  claim 1  in which said fluid dispersion comprises: 
 water: 55 to 85% by weight  
 element R (expressed in oxide form): 10 to 30% by weight  
 element T (expressed in oxide form): 5 to 15% by weight.  
 
     
     
         3 . Method according to one or the other of claims  1  or  2  in which said fluid dispersion DF comprises a deflocculating agent or dispersing agent, in such a way as to obtain a dispersion with both low viscosity and a state of fine dispersion, the average sizes of the particles or agglomerates relative to elements R and T being less than 25 μm.  
     
     
         4 . Method according to  claim 3  in which said fluid dispersion DF comprises said deflocculating or dispersing agent with a weight content comprised between 0.5 and 2%.  
     
     
         5 . Method according to any one of  claims 1  to  4  in which one introduces into said mixer (3), said dry mixture of powders MS and said fluid dispersion DF, 0.1 to 0.2 litres of said fluid dispersion DF being introduced per kilogram of said dry mixture MS.  
     
     
         6 . Method according to any one of  claims 1  to  5  in which, at stage b), said calcination is carried out at a temperature and for a length of time chosen in order to obtain a clinker B of apparent density d a  ranging from 2.7 to 3.1.  
     
     
         7 . Method according to  claim 6  in which said calcination is carried out at a temperature and during a length of time chosen in order to obtain a clinker B of apparent density d a  ranging from 2.75 to 3.  
     
     
         8 . Method according to any one of  claims 1  to  7  in which one chooses the elements M, R, T and the values x and y in such a way that, at the end of stage b), said clinker B has a value of field of anisotropy Ha at least equal to 1592 kA/m at 20° C.  
     
     
         9 . Method according to claims  8  in which one chooses the elements M, R, T and the values x and y in such a way that, at the end of stage b), said clinker B has a value of field of anisotropy Ha at least equal to 1671 kA/m at 20° C.  
     
     
         10 . Method according to any one of  claims 1  to  9  in which one chooses M=Sr, R=La and T=Co in the formula M 1-x R x Fe 12-y T y O 19 .  
     
     
         11 . Method according to any one of  claims 1  to  10  in which one chooses x=y in the formula M 1-x R x Fe 12-y T y O 19 .  
     
     
         12 . Method according to any one of  claims 1  to  11  in which x and y are comprised between 0.10 and 0.35.  
     
     
         13 . Method according to  claim 12  in which x and y are comprised between 0.15 and 0.25  
     
     
         14 . Method according to any one of  claims 1  to  13  in which, at stage d), said particles are compressed under a pressure of 30-50 MPa under an orienting magnetic field of about 1 Tesla.  
     
     
         15 . Method according to any one of  claims 1  to  14  in which: 
 1) one provides a clinker B′ of formula MFe 12 O 19  ,  
 2) one mixes it with said clinker B of the formula M 1-x R x Fe 12-y T y O 19 , typically during said stage c), in such a way as to obtain permanent magnets at lower cost and with a better performance/price ratio.  
 
     
     
         16 . Method according to  claim 15  in which the weight proportion z of clinker B of the formula M 1-x R x Fe 12-y T y O 19  in the mixture of the two clinkers B and B′ is comprised between 0.20 and 0.80.  
     
     
         17 . Method according to  claim 16  in which the weight proportion z is comprised between 0.30 and 0.70.  
     
     
         18 . Method according to any one of  claims 15  to  17  in which said clinker B′ of the formula M Fe 12 O 19  has an apparent density d, comprised between 2.5 and 3.5.  
     
     
         19 . Method according to any one of  claims 1  to  18  in which stage b) of calcination is piloted, particularly as far as the calcination temperature is concerned, by measuring the apparent density d, of the clinker obtained at the end of this stage b).  
     
     
         20 . Method for manufacturing a ferrite powder by the method for manufacturing permanent magnets according to any one of  claims 1  to  14  in which, a&t the end of stage b), said clinker B is reduced into powder, and in which the following stages c) to f) are suppressed.  
     
     
         21 . Permanent ferrite magnets obtained by the method according to any one of  claims 1  to  19 .  
     
     
         22 . Permanent magnets according to  claim 21  with a field of anisotropy at least equal to 1711 kA/m.  
     
     
         23 . Permanent magnets according to  claim 22  with a field of anisotropy at least equal to 1751 kA/m.  
     
     
         24 . Permanent magnets according to  claim 3  with a field of anisotropy at least equal to 1791 kA/m.  
     
     
         25 . Motors comprising magnets according to any one of  claims 21  to  24 .

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