Method of fabricating an article for magnetic heat exchanger

Abstract

In an embodiment, a method of fabricating a working component for magnetic heat exchange comprises arranging at least two articles comprising a magnetocalorically active phase and an elongated form with a long axis having a length l and a shortest axis having a length s, wherein l1.5 s, such that the shortest axes of the at least two articles are substantially parallel to one another and securing the at least two articles in a position within the working component such that the shortest axes of the at least two articles are substantially parallel to one another within the working component.

Claims

1. A method of fabricating a working component for magnetic heat exchange, comprising: providing at least two articles comprising a powder of a magnetocalorically active phase or a precursor powder of a magnetocalorically active phase, a binder and an elongated form with a long axis having a length l and a shortest axis having a length s, wherein l1.5 s, wherein the binder comprises a poly (alkylene carbonate), and the magnetocalorically active phase comprises La.sub.1-aR.sub.a(Fe.sub.1-x-yT.sub.yM.sub.x).sub.13H.sub.xC.sub.b, wherein M is Si and, optionally, Al, T is one or more of the elements from the group consisting of Mn, Co, Ni, Ti, V and Cr and R is one or more of the elements from the group consisting of Ce, Nd, Y and Pr, wherein 0a0.5, 0.05x0.2, 0.003y0.2, 0z3 and 0b1.5; arranging the at least two articles such that the shortest axes of the at least two articles are substantially parallel to one another; sintering the at least two articles such that the shortest axes of the at least two articles are substantially parallel to one another, the sintering being after the arranging the step; and wherein the articles are arranged by subjecting the articles to a magnetic field.

2. The method according to claim 1, wherein the magnetic field rotates in a plane, wherein the plane is aligned with a direction of flow of a heat exchange medium.

3. The method according to claim 2, wherein a temperature of the articles is maintained at a temperature at which at least one component of the article is ferromagnetic.

4. The method according to claim 1, including pressing the articles whilst applying the magnetic field.

5. The method according to claim 1 including pressing the articles after applying the magnetic field.

6. A method of manufacturing a magnetic heat exchanger, comprising the steps of: providing a heat exchange medium flowing in a direction, fabricating a working component by arranging at least two articles comprising a magnetocalorically active phase and an elongated form with a long axis having a length l and a shortest axis having a length s, wherein l1.5 s, such that the shortest axes of the at least two articles are substantially parallel to one another; arranging the at least two articles in a position such that the shortest axes of the at least two articles are substantially parallel to one another, and wherein the shortest axes are arranged substantially perpendicularly to the direction of flow of the heat exchange medium; and wherein the at least two articles are aligned with respect to one another by applying a magnetic field.

7. A method of fabricating a working component for magnetic heat exchange, comprising: arranging at least two articles comprising a magnetocalorically active phase and an elongated form with a long axis having a length l and a shortest axis having a length s, wherein l1.5 s, such that the shortest axes of the at least two articles are substantially parallel to one another; arranging the at least two articles in a position such that the shortest axes of the at least two articles are substantially parallel to one another; and aligning the at least two articles by applying a magnetic field.

8. The method according to claim 6, wherein the articles comprise an ellipsoid form.

9. A method of fabricating a working component for magnetic heat exchange, comprising: arranging a plurality of articles comprising a binder and a magnetocalorically active phase or elements in amounts suitable to produce a magnetocalorically active phase in at least two chains by applying a magnetic field at a temperature at which at least one component of the plurality of articles is ferromagnetic such that the orientation of the at least two chains is substantially parallel, wherein the binder comprises a poly (alkylene carbonate), and the magnetocalorically active phase comprises La.sub.1-aR.sub.a(Fe.sub.1-x-yT.sub.yM.sub.x).sub.13H.sub.xC.sub.b, wherein M is Si and, optionally, Al, T is one or more of the elements from the group consisting of Mn, Co, Ni, Ti, V and Cr and R is one or more of the elements from the group consisting of Ce, Nd, Y and Pr, wherein 0a0.5, 0.05x0.2, 0.003y0.2, 0z3 and 0b1.5; arranging the at least two chains in a position such that the orientation of the at least two chains is substantially parallel after applying the magnetic field; and sintering the at least two chains.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) Embodiments and examples will now be described with reference to the drawings and tables.

(2) FIG. 1 illustrates a schematic diagram of a working component for a magnetic heat exchanger.

(3) FIG. 2 illustrates a schematic diagram of a working component of a magnetic heat exchanger.

(4) FIG. 3 illustrates a schematic diagram of a method for fabricating a working component for a magnetic heat exchanger.

(5) FIG. 4 illustrates a schematic diagram of a method for fabricating a working component for a magnetic heat exchanger.

(6) FIG. 5 illustrates a schematic diagram of a method of fabricating a working component for a magnetic heat exchanger.

(7) FIG. 6 illustrates three differing debinding heat treatment profiles.

(8) FIG. 7 illustrates graphs of carbon and oxygen uptake for samples after debinding a PVP binder.

(9) FIG. 8 illustrates graphs of carbon and oxygen uptake for samples after debinding a PVB binder.

(10) FIG. 9 illustrates graphs of carbon and oxygen uptake for samples after debinding a PPC binder.

(11) FIG. 10 illustrates a schematic diagram of apparatus for fluidized bed granulisation.

(12) FIG. 11 illustrates graphs of the adiabatic temperature change of sintered samples fabricated using fluidized bed granulisation.

(13) FIG. 12 illustrates graphs of entropy change of sintered samples fabricated using fluidized bed granulisation.

DETAILED DESCRIPTION OF EXAMPLE EMBODIMENTS

(14) FIG. 1 illustrates a schematic diagram of a working component 20 for a magnetic heat exchanger. The working component 20 includes a plurality of elongated articles 21 each including a magnetocalorically active phase. The articles 21 have an elongated form with a long axis 22 having a length, l, and a shortest axis 23 having a length, s, whereby the length, l, is greater or equal to 1.5 times the length, s. The shortest axes 23 of the articles 21 are substantially parallel to one another. The articles 21 may be arranged in the working component 20 such that the shortest axes 23 are arranged substantially perpendicular to the direction of flow of the heat exchange medium of the magnetic heat exchanger. The flow of the heat exchange medium is indicated in FIG. 1 by the arrow 24. The long axes 22 of the articles 21 are substantially parallel to the direction of flow of the heat exchange medium.

(15) FIG. 2 illustrates a schematic view of a working component 30 for a magnetic heat exchanger. The working component 30 includes a plurality of articles 31 which may be substantially spherical. The substantially spherical articles 31 are arranged in two or more chains 32 having a length which is substantially longer than the width. The orientation of the chains 32 is substantially parallel. The chains 32 may also considered to be rows or columns of substantially spherical articles 31. The chains 32 may be arranged such that their orientation is substantially parallel to the direction of flow of heat exchange medium within the magnetic heat exchanger. The direction of flow of the heat exchange medium is indicated schematically in FIG. 2 by the arrow 33.

(16) The articles 21, 31 may be arranged within the working component 20, 30, respectively, by applying a magnetic field which causes the articles to align such that the shortest axes are substantially parallel to one another and the longest axes are substantially parallel to one another or such that the particles are aligned in chains. The position of the articles 21, 31 may be secured within the working component 20, 30 by applying an adhesive, such as a resin-based adhesive, by use of a soft solder or by sintering.

(17) Elongate forms including ellipsoid forms are useful for working components of a magnetic heat exchanger since they can be arranged such that the longer axis or dimension is substantially parallel to the direction of the flow of the coolant, indicated in FIG. 1 by arrow 24, and the shortest axis is substantially perpendicular to the direction of flow of coolant. This arrangement reduces turbulence in the coolant flow and increases heat exchange between the working component and the coolant.

(18) Oblate forms including ellipsoid forms can be arranged such that one of the longer axis or dimension is substantially parallel to the direction of the flow of the heat transfer fluid, as indicated schematically in FIG. 1 by arrow 24, another of the longer axis or dimension is substantially parallel to the direction of the magnetic field which is applied during the magnetic cooling cycle, as is indicated in FIG. 1 by arrow 25, and the shortest axis is substantially perpendicular to both the direction of flow of the heat transfer fluid and the magnetic field applied during the operation of the working component, as is indicated in FIG. 1 by the arrow 26. This arrangement reduces the turbulence in the flow of the heat transfer fluid and the demagnetizing field within the individual particles. Both effects may be used to increase the efficiency of the working component.

(19) FIG. 3 illustrates a schematic diagram of a method for fabricating a working component for a magnetic heat exchanger. The least two articles 40 are provided which include a precursor powder 41 of the magnetocalorically active phase and a binder 42. The articles have an elongated form having a long axis 43 having a length l and a shortest axis 44 having a length s. The long axis 1 is at least one half times larger than the shortest axis s. The at least two articles are placed in a container or form 45 and arranged such that the shortest axes 44 of the at least two articles 40 are substantially par-allel to one another.

(20) The articles 40 do not initially include a magnetocalorically active phase. The magnetocalorically active phase may be formed by reactive sintering the precursor powder, as is illustrated schematically in FIG. 3 by the arrows 46. The binder may first be removed from the articles 41 and subsequently a reactive sintering treatment carried out to form the magnetocalorically active phase 47.

(21) The sintering treatment may be also used to join the aligned particles to each other to form a solid working component with continuous fluid channels which are aligned parallel to the direction of flow of the heat transfer fluid.

(22) The articles 41 may be aligned by applying a magnetic field, if the precursor powder includes ferromagnetic material. In some embodiments, the temperature of the articles 41 is adjusted such that the articles are maintained at a temperature at which at least one component of the article is ferromagnetic. This enables the articles to be aligned using magnetic force. In some embodiments, the articles 41 are aligned by pressing or a combination of pressing whilst applying a magnetic field may be used to align the articles such that their shortest axes are substantially parallel to one another.

(23) FIG. 4 illustrates a method for fabricating a working component 50 for magnetic heat exchange. A plurality of articles 51 including a magnetocalorically active phase is provided. Each of the articles 51 has an elongate form. In this embodiment, the articles 51 have an ellipsoid form the articles 51 may be mixed with a soft solder powder 52 and a solvent. The articles 51 are arranged such that the shortest axes 53 are substantially parallel to one another and the longest axis 54 are substantially parallel to one another. The articles 51 may be aligned by pressing and rolling or by application of a magnetic field as is indicated schematically in FIG. 4 by the arrow 55. After the articles 51 have been arranged, the solvent is removed and the articles 51 are secured in positioned within the working component 50 by heat treating at a temperature which is higher than the melting point of the soft solder 52. The heat treatment is indicated schematically in FIG. 4 by the arrows 56. The soft solder 52 melts producing a matrix 57 in which the articles 51 are embedded. Due to the reduced packing density of articles 51 and the removed solvent the matrix contains continuous fluid channels which are substantially parallel to the direction of flow of the heat transfer fluid. Upon cooling below the melting point of the soft solder 52, the soft solder 52 solidifies to produce the working component 50.

(24) FIG. 5 illustrates a schematic diagram of a method for fabricating a working component 60 for a magnetic heat exchanger. A plurality of articles 61 is provided which each include a magnetocalorically active phase and an elongate form. The article 61 may have an ellipsoid form. The articles 61 may be arranged in the matrix 62 such that the shortest axes of the articles 61 are substantially parallel to one another. This intermediate product 63 may be mechanically deformed, for example by pressing, as is schematically indicated by the arrows 64, to increase the packing density of the articles 61 within the intermediate product 63. A further heat treatment may be carried out to secure the position of the articles 61 within the working component 60. In some embodiments, the position of the articles 61 may be secured by applying an adhesive which is then cured to provide a resin matrix for working component 60. In other embodiments, the position of the articles 61 may be secured by sintering the articles 61 to produce a working component with mechanical integrity.

(25) The working components may have an open porosity of 20% to 90%, preferably of 30% to 50%. The smallest dimension of the 25 articles may be 50 pm to 1000 pm, preferably 100 pm to 500 pm.

(26) The articles may be mixed with a solvent in which the adhesive is dissolved. After the articles have been arranged, the solvent may be removed such that the adhesive remains to secure the articles in the desired position. Use of a solvent, which is subsequently removed, may also be used to assist in adjusting the porosity of the working component.

(27) The articles may also be secured in position in the working component by subjecting the intermediate product to a sintering heat treatment. The sintering heat treatment may be carried out under conditions such that a liquid phase is formed which upon solidification provides the mechanical integrity for the working component.

(28) The article may be fabricated from a composite body including a precursor powder or powder including a magnetocalorically active phase and a binder. The composite body may be fabricated by mixing a binder and a solvent with a powder comprising a magnetocalorically active phase.

(29) The binder may comprise a poly(alkylene carbonate), for example poly(ethylene carbonate), poly(propylene carbonate), poly(butylene carbonate) or poly(cyclohexene carbonate). The solvent may comprise 2,2,4-Trimethylpentane, isopropanol, 3 Methoxy-1-butanol, propylacetate, dimethyl carbonate or methylethylketone. The magnetocalorically active phase may be La.sub.1-aR.sub.a(Fe.sub.1-x-yT.sub.yM.sub.z).sub.13H.sub.zC.sub.b wherein M is Si and, optionally, Al, T is one or more of the elements from the group consisting of Mn, Co, Ni, Ti, V and Cr and R is one or more of the elements from the group consisting of Ce, Nd, Y and Pr, wherein 0a0.5, 0.05x0.2, 0.003y<0.2, 0z3 and 0b1.5.

(30) In one particular embodiment, the binder is poly(propylene carbonate) and the solvent is methylethylketone. These compositions of the binder and solvent are found to be suitable for the La.sub.1-aR.sub.a(Fe.sub.1-x-yT.sub.yM.sub.z).sub.13H.sub.zC.sub.b, phase, since they can be removed from powder including this phase leaving an acceptably low residual carbon and oxygen content. Around 0.1% weight percent to 10 weight percent, preferably 0.5 weight percent to 4 weight percent of binder may be added to the powder.

(31) The mixture of the binder, solvent and powder including a magnetocalorically active phase or a precursor powder mixture capable to form a magnetocalorically active phase after reactive sintering may be further processed by removing some or substantially all of the solvent to form a brown body which includes the powder and the binder. The brown body may be plastically deformed to change its shape at temperatures above the glass transition temperature of the binder. The binder may then be removed from the composite body to produce a green body. The green body may then be reactive sintered to produce an article for magnetic heat exchange.

(32) The binder may be removed by heat treating the composite body at a temperature of less than 400 C. in a noble gas atmosphere, a hydrogen containing atmosphere or under vacuum for a period of around 30 min to 20 hours. Preferably, the conditions are selected such that at least 90% by weight or 95% by weight of the binder 10 is removed.

(33) The green body may be sintered at a temperature between 900 C. and 1200 C. in a noble gas atmosphere, a hydrogen containing atmosphere or under vacuum or a combination of these, if the composite body and green body include the magnetocalorically active phase. If the composite body and the green body include elements suitable for forming the magnetocalorically active phase, i e. precursors which are magnetocalorically passive, the green body may be reactive sintered to form the magnetocalorically active phase from the elements or precursors.

(34) In some embodiments, the article may have the form of a granule which is substantially spherical. Granules may be formed by fluidized bed granulisation.

(35) The binder and the treatment for its removal from the composite body may be selected so as to avoid detrimentally affecting the magnetocaloric properties of the working component.

(36) The suitability of different binders for La.sub.1-aR.sub.a(Fe.sub.1-x-yT.sub.yM.sub.x).sub.13H.sub.zC.sub.b, is investigated. The binders polyvinylpyrrolidone (PVP), poly-vinylbutyral (PVB) and polypropylene carbonate (PPC) are investigated. Samples are made using 0.1, 0.5, 1 and 2 weight percent binder (related to the powder), around 40 g of powder and 20 g of solvent. For PVP and PVB, isopropanol is used as a solvent and for PPC, methylethylketone (MEK) is used as the solvent. The mixtures were in each case mixed for 30 minutes in the turbula mixer and dried at 70 C. for 14 hours under vacuum.

(37) FIG. 6 illustrates three types of heat treatment for removing the binder or debinding. In heat treatment 1, the debinding was carried out under vacuum using a constant heating rate to the debinding temperature T.sub.debind which was held for four hours. The heating rate is variable between 2 C. per minute and 4 C. per minute. For the second debinding heat treatment, slower heating rates were used. In a first step, sample was heated at around 3 C. per minute to a first temperature T.sub.onset then the heating rate was slowed to around 0.5 to 1 C. per minute from T.sub.onset to the debinding temperature T.sub.debind which was held for 4 hours. The second debinding treatment was also carried out in vacuum.

(38) The third debinding heat treatment uses the same heat treatment profile as the second debinding treatment. However, after reaching the temperature T.sub.onset, the vacuum is replaced by 1300 mbar argon.

(39) After the debinding treatment, the samples are sintered by heating from the debinding temperature to the sinter temperature in 7 hours under vacuum, held at the sintering temperature for 3 hours, the atmosphere changed to argon and the sample held at the sintering temperature for further 1 hour in argon. A further homogenization heat treatment at 1050 C. for 4 hours in argon is used and the samples cooled quickly to room temperature using compressed air.

(40) FIG. 7 illustrates the carbon uptake and oxygen uptake measured for samples mixed with PVP after the three debinding heat treatments. Values obtained using thermogravimetric analysis (TGA) in nitrogen are included as a comparison. The debinding temperature T.sub.debind is 460 C. and T.sub.onset is 320 C. The debinding treatments carried out entirely under vacuum, that is debinding heat treatments 1 and 2, result in a lower level of increase in carbon than under nitrogen, as is indicated by TGA comparison values illustrated in FIG. 7. The debinding treatment 1 results in the lowest increase in the carbon contents. However, the debinding treatments carried out entirely under vacuum, that is debinding heat treatments 1 and 2, result in a higher level of increase in oxygen than under nitrogen, as is indicated by TGA comparison values illustrated in FIG. 7.

(41) FIG. 8 illustrates the carbon uptake and oxygen uptake measured from samples mixed with PVB after use of each of the three debinding treatments. The debinding temperature 7debind is 400 C. and T.sub.onset is 200 C. The use of a PVB binder results in an increase in the carbon content of around 0.3 weight percent and an increase in the oxygen content of around 0.3 weight percent for a binder amount of 2 weight percent. The uptake of carbon and oxygen for PVB is lower compared to PVP. However, about 30% of the binder remains in the final sintered product which may affect the magnetocaloric properties of the material.

(42) FIG. 9 illustrates a graph of the carbon uptake and oxygen uptake as function of weight percent of PPC binder for samples given each of the three debinding heat treatments. The debinding temperature is 300 C. and T.sub.onset is 100 C. The carbon uptakes for the samples after the debinding treatment is much lower than the TGA values for each of the three debinding heat treatments and it is also much lower compared to PVP and PVB. Also the oxygen uptake is lower than the TGA values for each of the three debinding heat treatments and it is also lower compared to PVP and PVB.

(43) The carbon uptake and oxygen uptake after the three debinding treatments are summarized in table 1.

(44) TABLE-US-00001 TABLE 1 PVP PVB PPC Density (mean value) 5.99 g/cm.sup.3 6.70 g/cm3 6.72 g/cm3 Preferred debinding Vacuum Vacuum or Vacuum or atmosphere Argon Argon Preferred debinding Profile 1 Profile 2/ Profile 1 profile Profile 3 C.sub.x (0.25*PVP + (0.135*PVB + (0.0106*PPC + 0.06) wt. % 0.045) wt. % 0.0153) wt. % O.sub.x (0.12*PVP + (0.10*PVB + (0.0273*PPC + 0.138) wt. % 0.14) wt. % 0.0599) wt. % Compatibility with Low Medium very high LaFeSi

(45) In summary, PPC is a particular suitable binder for the La.sub.1-aR.sub.a(Fe.sub.1-x-yT.sub.yM.sub.x).sub.13H.sub.xC.sub.b, phase since the increase in carbon and oxygen after the debinding treatment is lowest for the three binders investigated.

(46) As discussed above, the mixture of the powder, the binder and solvent may be mechanically formed before removal of solvent, for example by casting or screen printing, or after removal of some or substantially all of the solvent by methods such as extrusion or calendaring of the brown body. In some embodiments, spherical granulates or granules are useful for use in the working component of a magnetic heat exchanger. In some embodiments, the granules including particles of the powder and a binder are plastically deformed, before a subsequent debinding and sintering or reactive sintering treatments.

(47) In some embodiments, the spherical or substantially spherical granules may be made using fluidized bed granualisation. FIG. 10 illustrates apparatus for fluidized bed granualisation.

(48) In the fluidized bed granulisation method, powder including the magnetocalorically active phase or precursors thereof or elements in amounts suitable to produce a magnetocalorically active phase is caused to circulate by application of a gas and a fluid, such as a suitable solvent, is sprayed into the moving particles to create the granules. A binder may be added to form stable granules. As discussed above, PPC and methylethylketone is a combination of binder and solvent which is suitable for the La.sub.1-xR.sub.a(Fe.sub.1-x-yT.sub.yM.sub.x).sub.13H.sub.zC.sub.b phase. The gas temperature and pressure may be and speed may be adjusted to adjust the size of the granules formed.

(49) Conditions suitable for fabricating the granules using fluidized bed granulisation are summarized in table 2.

(50) TABLE-US-00002 TABLE 2 Parameter Value Starting material 200 g powder (<315 urn) or granules (<400 m) Binder 2 wt. % PPC Suspension 60 wt. % LaFeSi, 40 wt. % MEK Gas flow 13 m3/h Temperature 45 C. Spraying rate 29 g/min Spraying pressure 1.5 bar Purging pressure 2 bar

(51) The nominal compositions of the powder in weight percent are summarized in table 3.

(52) TABLE-US-00003 TABLE 3 Charge SE Si L Co M C 0 N Fe MFP- 17.86 4.13 17.85 0.09 1.84 0.015 0.31 0.025 75.73 1384 MFP- 17.82 4.12 17.81 0.1 1.65 0.015 0.3 0.024 75.96 1385 MFP- 17.78 4.09 17.77 0.11 1.47 0.015 0.3 0.023 76.21 1386

(53) For each powder, three runs in the fluidized bed granulisation apparatus were performed. In run 1, the binder containing material is used as the starting material. In run 2, granules with a diameter of less than 400 m obtained from run 1 are mixed with fine powder from the filter and used as the starting powder. In run 3, granules with a diameter less than 400 m obtained from run 2 are mixed with fine powder from the filter and used as starting material.

(54) The results are summarized in table 4.

(55) TABLE-US-00004 TABLE 4 1384 1384 1384 1385 1385 1385 1386 1386 1386 Run 1 Run 2 Run 3 Run 1 Run 2 Run 3 Run 1 Run 2 Run 3 Sprayed 761 g 487 g 405 g 911 g 515 g 679 g 757 g 653 g 468 g material Starting 230 g 200 g 200 g 80 g 200 g 200 g 200 g 200 g 200 g material Fraction <400 m 113 g 62 g 72 g 17 g 7 g 33 g 95 g 97 g 24 g Fraction 400-630 m 210 g 298 g 133 g 71 g 34 g 23 g 133 g 242 g 90 g Fraction >630 m 829 8 g 31 g 372 g 210 g 243 g 248 g 88 g 1 g Yield ~41% ~53% ~39% ~46% ~35% ~34% ~49% ~50% ~17% Filter powder 585 g 318 g 369 g 530 g 462 g 580 g 480 g 425 g 551 g

(56) The granules fabricated by fluidized bed granulisation are subjected to a debinding heat treatment and then sintered to form an article comprising magnetocalorically active material for use in magnetic heat exchange. The magnetocaloric properties of the sintered samples are tested to determine if the use of a binder and solvent and the use of fluidized bed granulation affect the magnetocaloric properties.

(57) The granules are packed in iron foil and gettered before the debinding and sintering heat treatments. The debinding temperature is 300 C. and the sinter temperature is 1120 C. The granules are heated under vacuum in 1 IA hours to the debinding temperature and held that the debinding temperature 300 C. for 4 hours. Afterwards, the temperature is raised in 7 hours under vacuum to the sintering temperature, held for 3 hours at the sintering temperature under vacuum and additionally for one hour at the sintering temperature in argon. Afterwards the granules are cooled to 1050 C. in 4 hours and held at 1050 C. for 4 hours under argon to homogenize the samples. The samples are then cooled quickly under compressed air to room temperature.

(58) The samples were found to have a carbon uptake of 0.04 weight percent to 0.06 weight percent and an oxygen uptake of 0.15% to 0.3 weight percent. These values correspond substantially to those obtained during the investigation of suitable binders.

(59) The sintered granules are hydrogenated by heating the granules in 2 hours under argon to 500 C. and held for one hour at 500 C. Afterwards, the atmosphere is changed to hydrogen and the samples cooled to room temperature in 8 hours and held under hydrogen for 24 hours. The granules are not found to dis-integrate after the hydrogenation treatment.

(60) The magnetocaloric properties of the samples are investigated. FIG. 11 illustrates the diagrams of the adiabatic temperature change and FIG. 12 illustrates diagrams of the entropy change for the samples. The results are also summarized in table 5.

(61) TABLE-US-00005 TABLE 5 1384 1384 1384 1385 1385 1385 1386 1386 1386 @ 1.5 T Run 1 Run 2 Run 3 Run 1 Run 2 Run 3 Run 1 Run 2 Run 3 (g/cm.sup.3) 6.81 6.59 6.92 6.91 6.8 6.45 6.94 6.99 7.07 Nominal T.sub.c 30 35 40 ( C.) T.sub.Peak ( C.) 34.9 35.4 34.2 38.5 36.4 36.6 44.4 44.9 40.8 T ( C.) 3.4 2.9 1.3 3.7 3.4 3.3 4.2 3.8 3.7 T Ref. 4.32 4.36 4.35 ( C.) S (J/KgK) 12.2 9.8 2.9 13 11 11.3 14.9 14.3 13.7 S Ref. 14.7 15.9 16.2 (J/KgK) T.sub.Peak ( C.) 35 35.4 33.9 37.8 36.6 36.5 42.9 43.3 40 -.sup.Fe (wt. %) 3.7 4.7 5.4 3.8 3.3 3.8 6.2 4.7 5.3

(62) The values of the Curie temperature and entropy change for granules fabricated in the first run are comparable to those 15 of the reference sample fabricated by powder metal metallurgical techniques without using a binder.

(63) In a further experiment substantially spherical brown parts containing a precursor powder mixture of La.sub.1-aR.sub.a(Fe.sub.1-x-yT.sub.yM.sub.x).sub.13H.sub.zC.sub.b and PPC as a binder produced by fluidized bed granulation as described above with a diameter of 1.2 to 1.5 mm where plastically deformed. The precursor powder mixture contained beside some La-rich components about 50% of elemental Fe powder. The plastic deformation is done by applying a force of 10-50 N at a temperature of 60 C. which is 20 K above the glass transition temperature of PPC resulting in oblate ellipsoid shaped particles with a diameter of about 2.45 mm and a thickness of about 0.6 mm.

(64) These brown parts have been filled into a small Teflon container. The Teflon container was rotated in a magnetic field of about 800 kA/m. The magnetic field was applied in a direction perpendicular to the rotation axis of the container. During the rotation the particles aligned themselves with their short axis parallel to the rotation axis. After the alignment the container was heated up to about 70 C. and the lid of the container was pressed parallel to the former rotation axis, which is perpendicular to the direction of the applied magnetic field. This pressing above the glass transition temperature of the binder resulted in a working component which could be removed out of the container without losing the alignment of the particles.

(65) The brown working component was then subjected to a debinding, sintering and hydrogenation treatment as described above resulting in a finished working component with similar magnetocaloric properties like the samples shown in FIGS. 11 and 12.