according to a first embodiment of the invention , a particle is in the form of a sphere . however , it will be understood that it may also take a form which deviates from the shape of a sphere , for example ellipsoidal or irregular form . the particle has a core of a polymer material , in this case of polymethyl methacrylate ( pmma ), which is surrounded by an intermediate layer formed from polyvinylpyrrolidone ( pvp ). this material forms a polar , hydrophilic outer surface . suitable polyvinylpyrrolidones are marketed under the names luviskol and luvitec by basf ; an acrylic polymer marketed under the name bellac by belland ag is also suitable . the intermediate layer is produced by dissolving the polyvinylpyrrolidone in an aqueous medium , applying the solution to the particles and drying the particles . the solvent used in this case is preferably water , since this has the advantage of evaporating without leaving any residues . ( however , ethanol or an aqueous ethanol solution is also suitable .) for the coating operation , the particles are fluidized in a fluidized bed by a hot airstream and are simultaneously sprayed with the solution . drops of the solution which come into contact with particles and surround the latter evaporate in the hot airstream , with the result that the dissolved polyvinylpyrrolidone remains behind and forms the intermediate layer . the resulting layer thickness can be controlled using the concentration of the solution / suspension / dispersion used and the duration of the treatment , as well as the temperature in the fluidized bed . alternatively , it is also possible to apply an intermediate layer of the acrylic polymer bellac by the latter being dissolved in a basic aqueous medium with a ph of at least 10 . the surface layer formed from the surfactant sodium lauryl sulfate is produced in a similar way to the intermediate layer of pvp by spraying the particles , which have been fluidized in the fluidized bed , with a second solution which is a very dilute solution of the surfactant in acetone . since pvp is not soluble in acetone , the intermediate layer consisting of this compound is not attacked in this second coating operation . in the case of an intermediate layer formed from the basic - soluble bellac , by contrast , a dilute aqueous surfactant solution with a ph not exceeding 9 . 5 is used . this does not attack the bellac layer . on account of the highly dilute nature of the surfactant solution , only a monomolecular surfactant layer is formed on the intermediate layer of pvp or bellac , and the nonpolar groups of this surfactant layer are uniformally facing outward , thereby producing nonpolar particles with little tendency to agglomerate and good flow properties . to produce an object from particles of this type , a layer of these particles is placed on a base and sprayed from above with a binder liquid in accordance with a predetermined pattern . for this spraying operation , it is possible to use an appliance similar to a generally known ink - jet printer ; appliances of this type are described in the european patents referred to in the introduction and are not explained in more detail here . suitable binder liquids are basic aqueous solutions , such as for example ammonia solution , which were also used for depositing the intermediate layer of bellac , since they dissolve both intermediate layers and the surfactant layer but not the pmma core . to set a desired viscosity of the binder liquid , it is possible , for example , to add glycol . printing parts of the particle layer with the binder liquid at least partially dissolves the surface layer and the intermediate layer but not the core which they enclose . the binder liquid is evaporated / vaporized , and the joined - together coatings together with the cores which they enclose remain behind , so that the previously separate particles form a cohesive body ; cf . in this respect the joined , hatched particles in fig1 . in the area surrounding this region , which has not been affected by the binder liquid , the particles remain separate , in unchanged form . repeated application of a layer of particles to the previous layer and printing of regions of the new layer with binder liquid in accordance with a predetermined pattern , which may vary from layer to layer , ultimately produces a cohesive body formed from joined particles , from which it is then merely necessary to remove the surrounding particles which have remained separate . since the basic aqueous ammonia solution used as binder liquid does not dissolve the pmma cores of the particles , their original form remains unchanged in the finished object , and consequently the shrinkage of the finished object can be no stronger than the ratio of the thickness of the intermediate layer to a mean radius of the cores of the particles . this thickness may , for example , amount to 0 . 5 μm for a mean radius of approx . 10 μm . the nonpolar nature of the outer surfaces of the particles makes the powder insensitive to atmospheric humidity and thereby prevents agglomeration of the particles . it therefore ensures the formation of uniform spaces between the unjoined particles and accordingly also ensures a uniform propagation of binder liquid which is sprayed on . consequently , the surfaces of the object obtained are uniformally smooth and accurately follow the predetermined pattern of the distribution of the binder liquid . in an exemplary embodiment for 3d laser sintering , the particles have a core of polymethyl methacrylate ( pmma ), which is surrounded by an intermediate layer with a low softening point (& lt ; 70 ° c . ), in this case a poly ( ethylene glycol ) amine or - amide . this material forms a polar , hydrophilic outer surface . suitable poly ( ethylene glycol ) amines or - amides are listed in known databases , such as beilstein or gmelin . the intermediate layer is produced by dissolving the poly ( ethylene glycol ) amine in methanol , applying the solution to the particles and drying the particles . other suitable solvents are tertiary butyl methyl ethers or ethyl acetate , each likewise with low boiling points . for the coating operation , the particles are fluidized in a fluidized bed by an airstream and are simultaneously sprayed with the solution . drops of the solution which come into contact with particles and surround them evaporate in the airstream , with the dissolved poly ( ethylene glycol ) amine remaining behind and forming the intermediate layer . the resulting layer thickness can be controlled using the concentration of the solution used and the duration of the treatment . the surface layer formed from the surfactant sodium lauryl sulfate is produced in a similar way to the intermediate layer by spraying the particles which have been fluidized in the fluidized bed with a second solution , which is a highly dilute solution of the surfactant in a relatively long - chain alcohol , e . g . ethanol or propanol . since poly ( ethylene glycol ) amine is not soluble in relatively long - chain alcohols , the intermediate layer consisting of this material is not attacked in this second coating operation . on account of the highly dilute nature of the surfactant solution , after evaporation of the solvent only a monomolecular surfactant layer is formed on the intermediate layer , and the nonpolar groups of this surfactant layer are uniformally directed outward , thereby producing nonpolar particles with little tendency to agglomerate and good flow properties . to produce an object from particles of this type , a layer of these particles is placed on a base and irradiated from above with a laser beam in , accordance with a predetermined pattern , corresponding to a cross - section of the object , so that the particles are joined in the selected part . then , the application and irradiation steps are repeated for a plurality of layers , so that the joined parts of the adjacent layers are joined together in order to form the object . a process of this type and a suitable apparatus are known , for example , from de 690 31 061 t2 and are not explained in more detail at this point . since the softening point of the pmma cores of the particles , at approx . 124 ° c ., is significantly higher than that of poly ( ethylene glycol ) amine , at approx . 60 ° c ., the original form of these cores is retained unchanged in the finished object if the introduction of laser energy is suitably restricted , with the result that the shrinkage of the finished object can be scarcely any greater than the ratio of the thickness of the intermediate layer to a mean radius of the cores of the particles . this thickness may , for example , be 0 . 5 μm for a mean radius of approx . 10 μm . the softening point of the surfactant monolayer is of no importance on account of its low thickness and the associated minimal absorption of energy . the nonpolar nature of the outer surfaces of the particles prevents agglomeration of the particles before the softening of the ( surface and ) intermediate layer and thereby ensures uniform spaces between the unjoined particles and accordingly also ensures a uniform introduction of energy from the laser beam into the layer of particles . consequently , the surfaces of the object obtained are uniformally smooth and accurately follow the predetermined pattern of the laser irradiation .