referring now to the drawing , fig1 a through 5 depict an example of a two salt bath ferritic nitrocarburizing system ( process and apparatus ) for producing a ferritic nitrocarburized surface treatment of cast iron brake rotors . the following description of the preferred embodiments is merely exemplary in nature and is not intended to limit the invention , its applications , or its uses . fig1 a shows a cross - section of the surface microstructure of a ferrous material 100 , a pearlitic cast iron brake rotor , subjected to the salt bath ferritic nitrocarburizing process according to the present invention . this process initially introduces carbon and nitrogen simultaneously from a nitrocarburizing salt bath into the surface s of the ferrous material 100 ( an aluminum foil a 1 which is shown is merely an artifact of the testing set - up , and it does not form a part of the ferrous material 100 ). thereafter , the ferrous material 100 is treated in an oxidizing salt bath . this step of the process creates a layer of fe 3 o 4 . as a result of this two bath nitrocarburzing process according to the present invention , there are two distinct regions , or zones , of material : a compound zone 102 and a subjacent nitrogen diffusion zone 104 which is not resolvable metallographically in the ferrous material 100 ( pearlitic cast iron ). the compound zone ( layer or region ) 102 is an outer portion of the ferrous material 100 after being treated first in the ferritic nitrocarburizing salt bath , then subsequently in the oxidizing salt bath . the compound zone 102 is formed initially through the reaction between the iron of the ferrous material 100 and nitrogen and carbon species from the nitrocarburizing salt bath . the compound zone 102 at this point is essentially a new phase of material , consisting predominantly of epsilon iron nitride , fe 3 n and a smaller volume of gamma prime iron nitride fe 4 n . thereafter , the ferrous material 100 is subjected to the oxidizing salt bath , whereupon a surface oxide layer 102 a is formed composed of oxidized nitrocarburzied iron , fe 3 o 4 . the diffusion zone ( layer or region ) 104 is disposed subjacent the compound zone 102 ( i . e ., further into the ferrous material 100 ), consisting of the iron base ferrous material with a lower concentration of diffused nitrogen than that found in the compound layer , and with the nitrogen in solid solution with the base material . the depths of these two zones , i . e . compound zone 102 and the diffusion zone 104 , are predictable and reproducible , which is a primary factor in the control of dimensional growth of the brake rotors as a result of the process referring now to fig1 b , shown is an x - ray diffraction pattern 110 of the ferrous material 100 of fig1 a . ( the specimen used to produce the photomicrograph , fig1 a , was taken from the same section of the brake rotor as the specimen used for the x - ray diffraction analysis , fig1 b . technically , they may be considered two adjacent specimens from the same sample , and thus the surfaces examined represent the same microstructural characteristics .). the surface structure of the ferrous material is determined through employing bragg &# 39 ; s law , which relates the angle of x - ray diffraction to the depth of the layer scattering the x - rays . a sufficiently thick layer of material is required in order to create the constructive interference patterns shown in fig1 b . the thicker the layer , the more intense the x - ray scattering , as indicated by higher count levels shown in fig1 b . the feature labeled n is the diffraction peak for iron nitride . the features labeled o 1 through o 4 are associated with layers of fe 3 o 4 , most notably o 2 . this diffraction pattern provides independent corroboration of the photomicrographic assignments of fig1 a . fig2 is a block diagram of the salt bath nitrocarburizing process 200 according to the present invention . the process begins at block 202 , whereat casting of pearlitic cast iron ( ferrous material ) brake rotors is performed in a generally conventional or known manner . at decision block 204 , a decision is made whether to stress relieve the brake rotors from block 202 . if yes , then the process proceeds to block 206 , whereat stress relief is performed and the process then proceeds to block 208 . if no , then the process proceeds directly to block 208 . at block 208 finish machining of the brake rotors is performed . this is performed now because of the dimensional controls of the salt bath nitrocarburizing process of the present invention obviates machining later in the process . in this regard , since the dimensional growth of the brake rotors is predictable , the process is preferably adjusted by empirical or theoretical analysis so that the brake rotors will not require further machining upon completion of the salt bath nitrocarburizing process . at block 210 , the brake rotors are preheated prior to submersion into the ferritic nitrocarburizing salt bath . this is accomplished through air heating in convection ovens or furnaces to about , for example , 400 degrees c . pre - heating ensures the brake rotors will be free of moisture , which , if present , would react violently with the contents of the ferritic nitrocarburizing salt bath . additionally , the pre - heating of the brake rotors is more efficiently performed ex - situ the nitrocarburizing salt bath as compared to allowing the brake rotors to come to thermal equilibrium in the ferritic nitrocarburizing salt bath from a substantially much lower temperature ( i . e ., room temperature ). at block 212 , a nitrocarburizing salt bath is utilized . this salt bath consists of salts and reagents necessary to perform the ferritic nitrocarburizing surface treatment of the cast iron brake rotors . this salt bath consists of between 25 and 57 percent by weight cyanate , calculated as cyanate ion , between 0 and 5 percent by weight cyanide , calculated as cyanide ion , between 0 and 30 percent by weight alkali metal chloride and the balance as potassium ion , sodium ion and carbonate ion . the most preferred embodiment consists of between 34 percent and 38 percent by weight cyanate ion , with a target of 36 percent , between 0 . 5 percent and 3 . 0 percent by weight cyanide ion , with a target of 2 percent , and a target of 20 percent by weight of carbonate ion . in addition , the target ratio of potassium ion to sodium ion is 4 to 1 . an organic polymer regenerator is added to the nitrocarburizing salt bath at regular intervals to maintain stable concentrations of the cyanate ions necessary for the nitrocarburizing reactions . a preferable regenerator is either melamine or urea or a derivative of melamine , such as melam , melem and melom . during processing , the cyanate ions of the salt bath react at the metal surface of the brake rotors as follows : nitrogen and carbon react with the iron of the ferrous material 100 as follows : at block 212 , the brake rotors are immersed ( submerged ) into the nitrocarburizing salt bath at about , for example , 579 degrees c . for a period between one and two hours , more preferably for about one hour . this process introduces nitrogen and carbon into the surface structure of the brake rotor as described with respect to fig1 . at block 214 , the brake rotors are removed from the nirtocarburizing salt bath , transferred to , and thereupon submerged in , an oxidizing salt bath at about 427 degrees c . for about 20 minutes . this oxidizing salt bath is an alkali hydroxide / nitrate mixture that oxidizes nitrocarburized ferrous material forming a combined oxide / nitride compound zone with a high resistance to corrosion . the preferred embodiment contains between 2 percent and 20 percent , most preferably between 10 percent and 15 percent , by weight nitrate ions , in the form of either sodium or potassium nitrate , between 25 percent and 40 percent by weight carbonate ion , in the form of either sodium or potassium carbonate , and the balance as hydroxide ion , in the form of either sodium or potassium hydroxide . cn − 1 + 3oh − 1 + no 3 − 1 → co 3 − 2 + no 2 − 1 + nh 3 + o − 2 [ fe ( cn ) 6 ] − 4 + 6no 3 − 1 → feo + 5co 3 − 2 + 6n 2 + co 2 additionally , the oxidizing salt bath is used as an intermediate thermal quenching step to cool the brake rotors with minimal thermal differentials and mitigation of potential distortions . at block 216 , the brake rotors are removed from the oxidizing salt bath of block 214 and are further cooled to room temperature either by air - cooling or a further step thermal quenching by water application ( spray or dip ) cooling . the nitrocarburized cast iron brake rotors are then water rinsed to remove reagents of block 214 , and then are oil dipped , whereupon the nitrocarburized brake rotors are ready to be shipped for motor vehicle assembly . fig3 a shows a graph 250 with a plot 252 indicative of compositional layers within the ferrous material 100 of fig1 a . the plot 252 shows the depth of the compound zone 102 of fig1 a as a function of the time the brake rotor dwells in the nitrocarburizing salt bath at block 212 . this depth is determined by measuring the depth of the highly concentrated nitrogen species diffusion into the iron substrate 100 of fig1 a . the data shows that after one hour of submersion in the ferritic nitrocarburizing salt bath , the compound zone has a depth of 0 . 011 millimeters . after two hours of submersion in the ferritic nitrocarburizing salt bath , the data shows the compound zone has a depth of 0 . 018 millimeters . fig3 b shows a graph 260 with a plot 262 showing the depth of the total nitrogen diffusion region . the data shows that after one hour of submerssion in the ferritic nitrocarburizing salt bath , the total nitrogen diffusion zone has a depth of 0 . 14 millimeters . after two hours , of submersion in the the ferritic nitrocarburizing salt bath , the data shows the total nitrogen diffusion zone has a depth of 0 . 18 millimeters . this data is important because the depth of nitrogen diffusion into the ferrous material 100 is correlated with enhancement of mechanical engineering properties of the brake rotors turning attention now to fig4 a through 5 , a preferred fixture for placement of the brake rotors into the nitrocarburizing and oxidizing salt baths . referring firstly to fig4 a and 4b , a rotor holder 300 for supporting an individual brake rotor 302 includes a hub 304 having a central opening 306 , which may preferably be of a square shape . a pair of rotor support posts 308 , 310 , are rigidly affixed to the hub 304 , whereby the rotor support posts are at , preferably , 90 degrees to each other , wherein where the hub has a square shape it is preferred for the rotor support posts to be oriented orthogonally to the corners of the hub , as depicted in fig4 a . an l - shaped rotor location post 312 is rigidly affixed to the hub at a location on the opposite side of the hub 304 in relation to a bisection of the angle subtending the rotor support posts . the dimensions of the rotor support posts 308 , 310 and the rotor location post 312 in relation to a brake rotor are as follows : the rotor support posts abut the inner race 302 a of the brake rotor such that the hub is concentrically disposed with respect to the inner race ; and a terminal end 312 a of the rotor location post abuts the inner face 302 b of the brake rotor hat 302 c such that the plane of the center of gravity cg of the brake rotor bisects the rotor support posts , as depicted at fig4 b . it is to be understood from the foregoing structural description , that the rotor holder 300 interfaces with only three local locations a , b , c of the brake rotor 302 , all of which being locations at which an absence of treatment by the two bath nitrocarburizing treatment process according to the present invention has no noticeable effect ; indeed all other areas of the brake rotor are fully exposed , particularly the brake rotor cheeks 302 d , 302 e and the exterior side 302 f of the brake rotor hat 302 c . in addition , it will further be seen that the placement of the brake rotor 302 onto the rotor holder 300 is extremely simplistic , as there are no mechanical interlockings , yet the brake rotor will rest upon the rotor in a completely stable manner . referring now to fig5 , an example of a rotor holder fixture 320 composed of a plurality of the aforedescribed rotor holders 300 will be detailed . the rotor holder fixture 320 is provided with a suitably large circumscribing base 322 for stably resting upon a floor 324 a of a tank 324 , wherein the tank holds a salt bath 326 , either the nitrocarburizing salt bath or the oxidizing salt bath of the two bath nitrocarburizing treatment process according to the present invention . a mast 328 is rigidly affixed centrally to the base 322 and rises up through the tank ( i . e ., extends normal to the floor 324 a ). the mast 328 provides the support of any number of interconnecting segments , as for example segment 328 a , segment 328 b , and segment 328 c , as shown at fig5 . at suitable junctures in height above the base 322 ( to provide adequate bath access spacings between adjacent brake rotors , as discussed hereinbelow ), arms 330 are perpendicularly attached to the main segments , 328 a , 328 b , and 328 c , as for example by welding . in the view of fig5 , there are three vertical sets of pairs of arms 330 ( one pair of arms for each mast segment ), as would suit a tank having an elongated rectangular shape . if the tank were shaped round or square , then an additional three vertical sets of pairs of arms would be attached to the mast ( one additional pair of arms for each mast segment ) in a direction perpendicular to the arms shown ( i . e ., in and out of the plane of the paper ). slid onto each arm 330 , which may or may not include splines 340 therebetween , is a holder sleeve 342 . any number of rotor holders 300 , as above described with respect to fig4 a and 4b , may be connected rigidly to a holder sleeve 342 , as for example by the hub thereof being integral with the holder sleeve . in the exemplar view of fig5 , the hubs of three rotor holders are integral constituents of each holder sleeve . it will be seen by reference to fig5 , that with each rotor holder 300 loaded with its respective brake rotor 302 , the salt bath 326 is able to wet the brake rotors everywhere , except the three aforementioned rotor holder contact locations ( see a , b , c of fig4 b ). additionally , it will be noted that a suitable horizontal distance l is maintained between brake rotors 302 parallel to the arms 330 and vertical distance l ′ parallel to the mast 328 so that the bath 326 has free and open access to each and every brake rotor , whereby dimensional control is provided during treatment in the bath . to vertically lift and lower the rotor holder fixture 320 , a conventional lifting apparatus is utilized ( not shown ) which interfaces with the mast 328 . for example , a crane apparatus may engage the upper end of the mast via a gripper or other mechanism . in operation , the rotor holder fixture is assembled in terms of the base , mast , arms and rotor holder carrying holder sleeves . next , each rotor holder is loaded with its respective brake rotor . the rotor holder fixture is then subjected to the pre - heating step , as described hereinabove , and then the rotor holder fixture is lowered into the tank so that all the brake rotors are wetted by the salt bath . upon completion of the desired bath dwell time , the rotor holder fixture is then removed from the tank for further processing of the brake rotors according to the present invention . dimensional change of the brake rotors during the process according to the present invention may be due to either mechanically induced stresses and / or stresses developed due to thermal conditions . regarding mechanical stresses , there is a benefit to properly supporting the rotor during the process according to the present invention by the configuration of the rotor holder 302 and the fixture 320 . a further advantage of placement of the brake rotors into the salt bath 326 is buoyancy of the brake rotors , whereby the high density of the liquid medium of the salt bath provides added support to the brake rotor during salt bath treatment , which thereby tends to mitigate mechanical stresses . regarding thermally induced stresses , a few processing parameters need to be considered : the temperature of the nitrocarburizing salt bath ; dwell time within the nitrocarburizing salt bath , per its temperature ; and the rate of cooling of the brake rotors thereafter . the temperature of nitrocarburizing salt bath is based on empirically produced microstructural phase diagrams that define the required chemical reactions as a function of temperature . for a nitrocarburizing salt bath as used according to the present invention to treat brake rotors , a temperature of about 580 degrees c . is preferred . the depth of the nitride compound that is formed is dependant on the length of time ( dwell time ) of the brake rotor at this temperature . greater dimensional stability of the rotor can be best achieved by minimizing the dwell time at a given nitrocarburizing salt bath temperature . chemical reactions within the nitrocarburizing salt bath develop a high nitrogen concentration ( activity ) which in turn enables shorter dwell times ( as compared with gaseous dwell times ) at a given temperature . minimizing thermal differentials within the brake rotor as it is cooled from the nitrocarburizing salt bath temperature also helps to reduce thermally induced stresses and , thus , encourages dimensional stability . this is accomplished by interrupted cooling , or step quenching from the nitrocarburizing salt bath temperature to room temperature by using a quench salt bath of about 427 degrees c ., then followed by water or air cooling to room temperature . conventional production brake rotors ( production rotors ) were compared in a series of tests to brake rotors treated by the process according to the present invention ( treated rotors ). in a series of friction tests , the apparent friction of a production rotor was compared to that of a treated rotor and was found to be , on average , only four percent above that of a treated rotor ( indeed , for burnished brake rotors , the treated rotors had higher friction , for both cold and warm tests , than the production rotors ). therefore , it can be concluded that brake rotor friction is acceptably high for brake rotors treated by the process according to the present invention . in a series of wear tests , as shown at fig6 , three production rotors 402 , 404 , 406 were compared , respectively , with three treated rotors 403 , 405 , 407 ( i . e ., production rotor 402 compared to treated rotor 403 , production rotor 404 compared to treated rotor 405 , and production rotor 406 compared to treated rotor 407 ). the resulting graph 400 of lateral run out per thickness variation ( lro / tv ) versus motor vehicle driving mileage indicates that the treated rotors wear quite favorably as compared with the production rotors . a series of thickness variation tests were conducted , shown at fig7 , for pairs of batches of six stress relieved treated rotors and non - stress relieved ( as cast ) treated rotors for one hour nitrocarburizing salt bath treatment , graphs 500 and 502 respectively , and two hour nitrocarburizing salt bath treatment , graphs 504 and 506 , respectively . it will be seen from fig7 that stress relieved treated rotors have a less thickness variation than non - stress relieved treated rotors , and that the treated rotors having one hour dwell in the nitrocarburizing salt bath had less thickness variation than those having a two hour dwell time . a series of noise tests were conducted . as shown by the graph 600 of fig8 a of percent noise versus decibels , cold production rotors 602 , 604 were compared to cold treated rotors 601 , 603 . it is seen from fig8 a that the cold treated rotors had noise levels quite favorable as compared to the cold production rotors . as shown by the graph 610 of fig8 b of percent noise versus decibels , warm production rotors 612 , 614 , 616 , 618 were compared to warm treated rotors 611 , 613 . it is seen from fig8 b that the warm treated rotors had noise levels quite favorable as compared to the warm production rotors . to those skilled in the art to which this invention appertains , the above described preferred embodiment may be subject to change or modification . such change or modification can be carried out without departing from the scope of the invention , which is intended to be limited only by the scope of the appended claims .