Scholars' Mine Masters Theses Student Research & Creative Works 1971 Phase equilibrium and thermodynamic study of the iron-copper-carbon system Krishna Parameswaran Follow this and additional works at: http://scholarsmine.mst.edu/masters_theses Part of the Metallurgy Commons Department: Materials Science and Engineering Recommended Citation Parameswaran, Krishna, "Phase equilibrium and thermodynamic study of the iron-copper-carbon system" (1971). Masters Theses. 7220. http://scholarsmine.mst.edu/masters_theses/7220 This Thesis - Open Access is brought to you for free and open access by Scholars' Mine. It has been accepted for inclusion in Masters Theses by an authorized administrator of Scholars' Mine. This work is protected by U. S. Copyright Law. Unauthorized use including reproduction for redistribution requires the permission of the copyright holder. For more information, please contact [email protected]. /.' PHASE EQUILIBRIUM AND THERMODYNAMIC ·--· ~ ·-'~•.7 STUDY OF THE IRON-COPPER-CARBON SYSTEM BY KRISHNA PARAMESWARAN, 1946A THESIS Presented to the Faculty of the Graduate School of the UNIVERSITY OF MISSOURI-ROLLA In Partial Fulfillment of the Requirements for the Degree MASTER OF SCIENCE IN METALLURGICAL ENGINEERING 1971 Approved by ---6,...:.-£2-=-_rz_~-~<Advisor> T2537 78 pages c.l ii ABSTRACT Gas carburization experiments were conducted at 950°C in order to study the phase relations and to determine the activity of carbon in the iron-rich corner of the iron-copper-carbon system. of graphite in 0 0 eq~ilibrium 950 , 1000 , and 1050 0 c. The solubility with iron-copper alloys was determined at The results of gas carburization and graphite solubility experi~ents at 950°C were used in constructing an isothermal section of the iron-rich end of the iron-copper-carbon phase diagram, on which are superimposed carbon isoactivity lines. Graphite solubil- ity data at 1000° and 1050°C were used to construct similar diagrams without the isoactivity lines. The effect of carbon content on the solidus temperature of an alloy initially containing 90% copper and 10% iron was studied by gas carburization and graphite equilibration techniques. The effect of copper on the rate of carburization was determined in a semi-quantitative way. The results are discussed in terms of application to heat treatment of copper bearing steels and to the liquid phase sintering of iron-copper-carbon powder metallurgy parts. iii ACKNOWLEDGEMENTS The author gratefully acknowledges the invaluable guidance of his advisor Dr. A.E. Morris during the entire project. He would like to thank the International Copper Research Association for the financial support. iv TABLE OF CONTENTS Page ABSTRACT ••••••••• ii ACKNOWLEDGEMENTS. . iii LIST OF FIGURES. ... .... LIST OF TABLES •• I. II. REVIEW OF LITERATURE ••• B. IV. . viii INTRODUCTION •• A. III. .... vi 1 . ...... 3 Phase Diagrams ••• 3 1. Iron-Copper System. 3 2. Copper-Carbon System. 5 3. Iron-Carbon System ••• 6 4. Iron-Copper-Carbon System •• 6 Physical Metallurgical Considerations ••.••••••. 6 1. Effect of Copper on Transformation Temperatures. 6 2. Microstructure •••••••••.••.••••. 10 c. Thermodynamics of Related Systems ••• 10 D. Copper in Steel and Cast Iron. 11 E. Copper in Powder Metallurgy. 12 EXPERIMENTAL PROCEDURE. 16 A. General . . . . . . . . . . . . . 16 B. Furnaces and Temperature Control •• 16 c. Temperature Measurements •• 19 D. Atmosphere Control •• 19 E. Starting Materials •. 23 F. Alloy Preparation .••••..•••••. 24 G. Gas Carburization Experiments. 24 H. Graphite Solubility Experiments. 25 I. Solidus Temperature Determination •• 27 EXPERIMENTAL RESULTS AND DISCUSSION. 28 A. Presentation .••.••••.• 28 B. Discussion of Results. 42 1. Gas Carburization and Graphite Solubility. 42 2. Solidus Temperature Determination .•. 45 3. Kinetics of Carburization •.••••••••. 45 c. Suggestions for Further Work ................•.......•. 46 v Page v. SUMMAR):' AND CONCLUSIONS • •..• , •••.••• , ............. , • • · • · ..... . BIBL IOGRA.PHY • ••••••••.••••••••.••. I ••••••••••••••••••••••••••••••••• 48 49 VITA . . . . • . . • . . . . • . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . • . • . • . . . • . . . . . . . . . . 53 APPENDICES • ••••••••••••••.••••• - •.••• 54 I. IIIJ . . . . . . . . . . , •••••••••••••••••••• CALCULATION OF ATMOSPHERES WITH A SPECIFIC 0 ACTIVITY OF CARBON AT 950 C •••••••••••• , •• , . . . . . . . . . . . . . . . . II. III. 0 A. Gurry's Diagram at 950 C and 1 Atm Pressure •••••••••••• 55 B. Source of Data for the Calculations •••••••••••••••••••• 57 STARTING MATERIALS AND LIST OF ALLOYS PREPARED ••••••••••••• 59 WEIGHING PROCEDURE AND SOURCES OF ERRORS IN THERMOGRAVIMETRY. • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • IV. 55 60 SUMUARY OF EXPERIMENTAL RESULTS,. • • • • • • • • • • • • • • • • • • • • • • • • • • 62 A. Gas Carburization Experiments. • • • • • • • • • • • • • • • • • • • • . • • • • 62 B. Graphite Solubility Experiments •••••••••••••••••••.•••• C. Solidus Temperature Determination....... • • • • • • • • • • • • • • • 68 D. Rate of Carburization.............. • • • • • • • • • • • • • • • • • • • • 68 E. Activity Coefficients for Carbon... • • • • • • • • • • • • • • • • • • • • 69 67 vi LIST OF FIGURES Figure Page 1. The Iron-Copper Phase Diagram. • • • . • • • . • • • . . • • . . . . . . • . • . • • • • . . . 2. The Iron-Copper-Carbon System - Composition of Conjugate Liquids at Liquidus Temper a tures. . • . . • • • . . . . . • . • • . . . • . • . • . . . . . 3. 4 7 The Iron-Copper-Carbon System - Lower Limit of the Austenite Field. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8 4(a) Effect of Copper on Allotropic Temperatures for a 0.5% Carbon Steel.................................................. 9 4(b) Effect of Copper on M Temperature for a 0.5% Carbon Steel •••• 9 s 5. Effect of Copper on Carbon Pickup During Sintering ••••.•••..•• 14 6. Schematic Diagram of the Apparatus for Gas Carburization Experiments. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 7. 17 Schematic Diagram of the Apparatus for Graphite Solubility Experiments. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 18 8(a) Schematic Diagram of the Apparatus for Solidus Temperature Experiments (Gas Carburization)............................... 20 8(b) Schematic Diagram of the Apparatus for Solidus Temperature 9. Experiments (Equilibrium with Graphite) ..••.•••...•••••.•.••.• 21 The Carbon-Oxygen-Hydrogen System at 950°C and 1 Atm Pressure. 22 lO(a) Activity of Carbon vs % Carbon at 950°C for a 0.3% Copper Alloy . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 29 lO(b) Activity of Carbon vs% Carbon at 950°C for a 0.7% Copper Alloy......................................................... 30 lO(c) Activity of Carbon vs % Carbon at 950°C for a 1.0% Copper Alloy. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 31 lO(d) Activity of Carbon vs % Carbon at 950°C for a 1.3% Copper Alloy. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 32 lO(e) Activity of Carbon vs % Carbon at 950°C for a 2.5% Copper Alloy. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 33 lO(f) Activity of Carbon vs % Carbon at 950°C for a 3.0% Copper Alloy......................................................... 34 lO(g) Activity of Carbon vs % Carbon at 950°C for a 3.5% Copper Alloy. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11. 35 Isothermal Section of the Iron-Rich End of the Iron-Copper- Carbon Phase Diagram.......................................... 36 vii Page 12. The Effect of Temperature on the Extent of the Austenite Field. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 13. The Effect of Copper on the Solubility of Graphite in Iron-Copper Alloys. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14. 38 39 The Effect of Carbon Activity on the Solidus Temperature for a 90% Copper Alloy. • . • . • . • . • . • • • • • • • . • • • • • • . • . • . . • . . • . • • . • • 40 15. The Effect of Copper Content of the Alloy on Time to Reach the Equilibrium Carbon Content During Gas Carburization .•.••••• 41 16. The Effect of Copper on the Activity Coefficient of Carbon •.••. 44 viii LIST OF TABLES Table Page I. 62 II. 62 III. 63 IV. 63 v. 64 VI. 64 VII. 65 VIII. 65 IX. 66 X(a) Solubility of Graphite in Iron-Copper Alloys .•••...•••••.....•. 67 X(b) Comparison of Graphite Solubility Values for Pure Iron With Published Data. • . • • . • . . • • • • . . • • . . . . • . . . • • • • . . . . . • • • • . . . . . . 6 7 XI. Solidus Temperatures for a 90% Copper Alloy ...••.......•...•... 68 XII. Times to Attain Equilibrium Carbon Content During Gas Carburiza tion. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 68 XIII (a) Activity Coefficients of Carbon at 950°C for Pure Iron •..•• 69 XIII(b) Activity Coefficients of Carbon at 950°C for a 0.3% Copper Alloy. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . XIII(c) 69 Activity Coefficients of Carbon at 950°C for a 0.7% Copper Alloy. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 70 1 I. INTRODUCTION The effects of copper in steels and cast irons have been known and utilized commercially even though the reason for these effects may not have been fully understood. Copper is also one of the most im- portant alloying elements in ferrous alloys used in powder metallurgy. The addition of copper to low alloy steels improves strength and gives good impact and abrasion resistance. Copper has been used in high alloy and stainless steels to improve corrosion resistance in specific environments, reduce susceptibility to stress corrosion cracking and to impart age hardenability. appreciably affect weldability. Small copper additions do not Up to 0.5% copper has been added to certain steels for deep drawing applications. One of the deterrents to the use of copper as an alloying element in steel is its tendency to promote "hot shortness" above 1090°C and over about 0.3% copper. The preferential oxidation of iron, during hot working operations, causes the concentration of copper to increase on the surface. At hot rolling or forging temperatures this high copper material becomes liquid, and surface cracks occur. In cast irons, copper is used to improve tensile strength and transverse strength. izes pearlite. It gives the desired type of graphite and stabil- The effect of copper is more pronounced in nodular cast irons than in flake graphite forms. Copper is becoming increasingly important as an alloying element to iron parts made by the powder metallurgy process. It is possible, by adjustment of the proportions of the constituents in iron-copper and iron-copper-carbon compacts, to minimize dimensional changes during sintering and to obtain optimum mechanical properties. Experience has shown that a knowledge of the phase diagram is very useful for explaining alloy behaviour. In the iron-copper-carbon system, knowledge of the austenite phase boundary can be used in designing heat treatment procedures for copper bearing steels. The deter- mination of solidus temperatures in the system can contribute to a better understanding of liquid phase sintering of iron-copper-carbon powder metallurgy alloys. Such information can also shed light on the 2 temperature and composition ranges where "hot shortness" occurs in steels containing copper. In the present investigation, the iron-rich end of the ironcopper-carbon phase diagram was studied at 950°C by gas carburization experiments. The solubility of graphite in iron-copper alloys was 0 0 0 determined at 950 , 1000 , and 1050 C and the solidus temperature was determined for a 90% copper-iron alloy. 3 II. REVIEW OF LITERATURE Much has been published about the use of copper in ferrous alloys, particularly in terms of phase transformations and heat treatment procedures for copper bearing steels. Hot shortness in copper contain- ing steels and the problem of copper accumulation in steel scrap has been discussed in the literature. The effect of copper on the pro- perties of cast irons has also been extensively studied. Despite the importance and use of copper in ferrous systems, there is still, however, no complete phase diagram for the iron-copper-carbon system. A bibliography1 entitled "Copper in Steel" was published by the British Iron and Steel Research Association and covers work done during the period 1951-1963. Another bibliography 2 to be published by INCRA, covers the period 1964 to 1970, plus some important earlier work, and contains references on copper in iron, steels and related systems. The literature has been reviewed in the following section under the headings of: (A) Phase Diagrams, (B) Physical Metallurgical Considerations, (C) Thermodynamics of Related Systems, (D) Copper as an Alloying Element in Steel and Cast Irons, and (E) The Use of Copper in Powder Metallurgy. A. Phase Diagrams 1. Iron-Copper System The iron-copper phase diagram, taken from Hansen, 3 is presented in Figure 1. Hansen 3 also gives a thorough review of the work done on the system up to 1957. was done by A review of more recent work, up to 1963 Elliott~ The most recent version of the phase diagram is presented by Hultgren et a1, 5 but their diagram is essentially the same as presented in Hansen. 3 The stable solid phases that exist in this system are: delta o, austenite y, ferrite a, and epsilon E. One of the points of great controversy in earlier work was the existence of a wide miscibility gap in the liquid state. It was be- lieved that liquid segregation occured in iron-copper alloys. However, 6 on the basis of later, more careful work, by Maddocks and Claussen, it was found that with the use of relatively pure iron and copper no 4 WEIGHT 10 I 160 0 20 I 30 I 1500 1400 (.) i/ 1300 .. 120 0 w 0:: ~ 0:: w a.. ~ w 1- 110 0 10830 I'" 40 I 50 I 60 I IRON 70 I _.. 80 I - - LIQUID 90 I 1484 ~ ~ cf~ I ~ I I ~ I •Y : 1094° 4.5 (4.0) -92.5\ (91. 5) \ 5 100 0 r-/2.9 (2.6) ~ \ E \ \ 1.6 (1.4) 1 - - -~--- 10 \A w -835° 80 0 0.35 70 0 (0.3) - 20 9 -97 J.l:_59Cl r-- j_9~.5) 7 MAGN. ..TRANSFoRMATION 30 40 50 60 70 80 90 ATOMIC PER CENT IRON Figure 1. (I I I 1 90 0 (I I j I 3.2(2.8) 0 :::> ,.. PER CENT The Iron-Copper Phase Diagram (Hansen 3 ). 100 Fe 5 miscibility gap existed. Liquid segregation was apparently promoted by the presence of impurities such as carbon and silicon. The presently accepted value for the peritectic temperature involving the delta phase is 1484°C. The peritectic temperature in- volving austenite phase is taken as 1094°C, for the eutectoid reaction y = a + The reported temperatures E, differ widely. Hansen 3 takes + 15°C. A similar uncertainty exists for the eutectoid composition; Hansen3 reports it to lie between 2.5-3.5%* copper. a value of 835 The solubility limits of copper in austenite and ferrite phases were determined by Speich et a1. 7 They determined the interdiffusion coefficients for copper in austenite and ferrite from concentration penetration curves obtained by electron microprobe analysis. They calculated the solubility limits for copper in the austenite (temperaa o o o ture range 929 -1020 C) and ferrite (temperature range 699 -859 C) phases, by extrapolation of the diffusion data. The solubility limits were represented as equations obtained by least square analysis and are given below: =- yFe: log C(% Cu) 2574 + 2.716 (1) aFe: log C(% Cu) = - 4 ~ 00 + 4.335 (2) T where T is in °K. The austenite solubilities of Speich et al. are 3 lower than the values reported by Hansen. An extrapolation of their austenite solubility data gave a eutectoid composition of 2.6% copper. This is in good agreement with the value of 2.8% copper, which they obtained by a thermodynamic treatment. 2. Copper-Carbon System The solubility of carbon in copper is exceedingly small. Hansen 3 reports the following solubility values: 0.0001% carbon at 1100°C, 0.00015% carbon at 1300°C, 0.0005% carbon at 1500°C and 0.003% carbon at 1700°C. * % in this work, refers to weight percent. 6 3. Iron-Carbon System The iron-carbon diagram is fairly well known and excellent re. v1ews are ava1.1 a bl e. 3-5,8 4. Iron-Copper-Carbon System Prior to 1934, the only available data on the iron-copper-carbon system was the work of Ishiwara et al. 9 They constructed a possible phase diagram that satisfied the phase rule and attempted to locate various surfaces of the diagram by experimental study of iron-rich alloys containing up to 30% copper. Their work has been critically evaluated by Gregg and Daniloff. 10 Some of the features of their system are: A two liquid region extends over a large part of the ternary system and intersects the iron-copper liquidus curve. This latter observation has been proven incorrect, as mentioned earlier. The line along which liquid, and cementite (graphite?), are in equilibrium intersects the two liquid region, necessitating the need for an invariant reaction in which an iron-rich liquid is decomposed into gamma iron, cementite (graphite) and a copper rich liquid. Maddocks and Claussen 6 placed the ends of the monotectic four phase horizontal at 3% iron, 0.01% carbon, and 2 to 2.5% copper, 4.2% carbon at 1150°C. Figure 2, taken from Maddocks and Claussen 6 shows the compositions of conjugate liquids at liquidus temperatures. Maddocks and Claussen 6 concluded that the peritectic temperature of 1094°C in the iron-copper system was not changed by the presence of carbon. Austenite decomposes in this system by a ternary eutectoid reaction, which according to Ishiwara et al. 9 occurs at 700°C and at a composition of 1.9% copper and 0.9% carbon. A version of the lower limit of the austenite field is shown in Figure 3, taken from Gregg and Daniloff. 10 The region of austenite is limited below by the surfaces of separation of alpha, graphite and epsilon. B. Physical Metallurgical Considerations 1. Effect of Copper on Transformation Temperatures Habraken and Greday 11 briefly reviewed the effect of copper on the transformation temperatures. Figures 4(a) and (b) taken from the 7 (.) 0 u.f QOO\t__L_:~-+--\--t--t= I ~ QQ\\ I ~ cr:: uJ 0.. ~ uJ t- Figure 2. The Iron-Copper-Carbon System - Composition of Conjugate Liquids at Liquidus Temperatures (Maddocks and Claussen6). 8 0 0 2 I 01 CARBON, Figure 3. /o 0 The Iron-Copper-Carbon System - Lower Limit of the Austenite Field (Gregg and DanilofflO). 9 -101------ -u 0 ® -20r-------~---------r--------4---~~~ 1.0 0.5 0 2.0 1.5 COPPER 0 -5 <l ~• -10 ~ -15 -. ~ @ -20 0.5 0 1.0 "• ~~ ~ 1.5 2.0 COPPER (0/o) figure 4(a) Effect of Copper on Allotropic Temperatures 11 for a 0.5% Carbon Steel (Habraken and Greday ). Figure 4(b) Effect of Copper on M Temperature for a 0.5% Carbon Ste~l (Habraken and Greday 11 ). 10 work represents the effect of copper on the lowering of the allotropic and M temperatures for a 0.5% carbon steel. They have also reviewed s work done on continuous transformation diagrams of copper-containing steels. They report that copper retards the transformation of austen- ite more or less equally at all temperatures and that it increases the resistance to softening during tempering. 2. Microstructure Lund and Lawson12 examined the microstructure of quenched 4.8% and 7.5% copper, iron-copper alloys by X ray diffraction, optical, and electron microscopy. The 7.5% copper alloy showed epsilon phase along the austenite grain boundaries and was believed to be proeutectoid in origin. They found that the austenite phase in the iron-copper system transforms to produce massive martensite of the same composition as the parent phase and that the transformation is accompanied by shear. C. Thermodynamics of Related Systems The activity of carbon in austenite13 - 16 and in molten iron17 • 18 has been determined by a number of investigators, generally by equilibration with co-co 2 mixtures. The most recent work is by Ban-Ya et a1. 13 ~n which new data on the activity of carbon in austenite in the 0 0 temperature range 900 -1400 C was obtained. They derived the follow- ing equation for the activity of carbon in austenite as a function of temperature, with graphite as the standard state for carbon: log a 3770 c 3860 y c -T- + 2. 72 log T - 10.525 + ---=+ log z c T (3) o Yc where T is in K, y is the atom ratio of carbon to iron, and z . . .19 c . c 1-y Chr1st1n1 determ1ned the activity of iron in the iron-copper c system at 1050 0 0 to 1300 C, by a solid electrolyte technique. The activity of copper was calculated by a Gibbs-Duhem integration. Dem- chalk20 determined the activity of iron and copper in iron-copper austenite in the temperature range 1300°-1466°C, by bringing discs of iron-copper solid solutions in contact with liquid silver-copper alloys of known copper activity. The copper content in the iron-copper alloys was determined by microprobe analysis and in silver-copper alloys by 11 atomic absorption spectrophotometry. He also determined the effect of carbon on the activity of copper at 1300°C. His equation for the 0 activity coefficient of copper Ycu' at 1300 C, is given below: ln y Cu 3.558- 32.75 XCu + (4) 27.00 XC XCu' XC are mole fractions of copper and carbon. The published data on the activity of carbon in alloyed austenite 21 has been reviewed by Chipman and Brush. The Henrian activity coefficient at 1000°C was expressed in terms of interaction parameters among the solute elements. Yoshida and Sano 22 found a slight decrease in the activity of carbon with copper addition in the temperature range 850-950°C. Chipman and Brush, in noting the work of Yoshida and Sano, mention a lack of quantitative data for establishing interaction parameters for copper-carbon austenite. D. Copper in Steel and Cast Iron A recent review of the effects of copper in steels is given by Habraken and Greday. 11 They cited three advantages of copper addition to steels: improved mechanical properties, increased wear resistance, and improved corrosion resistance. The most widely used copper bear- ing steels contain between 0.2-0.6% copper. The best known copper con- taining steels are high strength low alloy grades, that had higher yield strength than ordinary steels while the ductility remained comparable. The strengthening was due to solid solution hardening. Copper substantially raises the atmospheric corrosion resistance of steel. Moss 23 mentions that 1-5% copper has been added to high alloy and stainless steels to improve corrosion resistance in specific environments and reduce susceptibility of austenitic stainless steels to stress corrosion cracking. 11 Habraken and Greday mention the development of a rimmed steel containing 0.2-0.5% copper to replace more expensive aluminum-killed steel for deep drawing applications. They note that the presence of copper in limited amounts did not appreciably affect weldability. They have mentioned the use of copper steels for architectural applications. Corrosion resistant low alloy steel was used in the 12 unpainted condition as structural material; on weathering, a somewhat pleasant rust color was obtained that was esthetically acceptable. Two test structures in the U.S. built with Cor-Ten (U.S. Steel grade containing 0.25-0.40% copper and 0.04% max. phosphorous) as the main structural material after six years weathered to a uniform rust color with no localized corrosion. Copper in conjunction with phosphorous enhances the corrosion resistance of the steel. One of the problems associated with copper bearing steel scrap is that such scrap used in steel making contributes copper to the finished steel, since copper is not removed during steel making. The severity of the problem varies, depending on the use of the finished steel and source of the scrap. Other sources of copper come from scrap automobiles. The effect of copper in cast irons has been investigated exten. 1 y. Mass 23 ment1ons . . . tens1"1 e strengt h an d s1ve t h e 1mprovement 1n transverse strength by copper additions to cast irons. He notes that copper stabilizes pearlite and that the effect of copper was more pronounced in nodular than in flake graphite forms. Corsetti and 24 Valota note that copper was found to improve hardenability, machinability and promote graphitization. E. Copper in Powder Metallurgy Bockstiegel 25 has studied the nature and causes of volume changes in the sintering of iron-copper and iron-copper-carbon powder compacts. He indicated the possibility of obtaining optimum mechanical properties by skillful adjustment of the constituents and careful control of the sintering conditions. He observed excessive swelling of iron-copper compacts if the sintering was done above 1083°C or at a lower temperature for longer times. He attributes the phenomena to the solution of copper in austenite, since he observed the volume increase to be proportional to the copper content of the compact up to the solubility limit. In iron-copper-carbon compacts, he observed less swelling, and attributed the phenomena to the possible presence of an iron-rich ternary liquid phase. Shoji and Yamada 26 have studied the effects of sintering and carburizing times on the carburizing behaviour of sintered iron-copper 13 and iron-nickel compacts. Copper did not exhibit an accelerating effect on sintering as did nickel. Shorter carburizing times were found adequate for iron-copper compacts, compared with iron-nickel compacts. The case hardness was lower for the iron-copper compacts. They attributed the above observations to the greater porosity of iron-copper compacts. The toughness of quenched iron-copper compacts decreased markedly beyond 3% copper. In a later investigation Shoji et al. 27 determined the effect of copper on the activity of carbon in austenite from experiments involving gas carburization of iron and iron-copper powders. The results indicate a slight decrease in the carbon content with copper addition at a fixed carbon activity. appears to be very limited. Shoji and However, the data presented ~amada 28 discussed the possibil- ity of carbon control using denatured propane gas as a furnace atmosphere in the sintering of iron and iron-copper powders. Sorokin 29 studied the effect of copper and graphite on the properties of sintered iron-based alloys. He found a copper-rich phase only in alloys with 10-15% copper, as inclusions along the boundaries of pearlite colonies. Copper addition improved tensile strength and did not appreciably affect elongation. Sorokin 30 also mentions earlier work on the subject of carburizing during sintering of iron-copper compacts. He cites an earlier work where a compact containing 2.7% copper absorbed 50% less carbon than pure iron, during carburization at 930°C for 8 hours. Sorokin's result is presented in Figure 5. Sorokin also studied the effects of copper in improving the sintering characteristics of stainless steel powders and in increasing the 31 strength of compacts. 32 Domsa reported that the addition of copper to iron-graphite compacts restricted cementite formation. One of the difficulties in producing iron-graphite parts was the occurrence of cementite after normal sintering. For carbon contents less than 3%, it could be avoid- ed by shorter sintering times and step sintering methods. For higher carbon contents an alloying element like copper was found to restrict cementite formation. He attributed this behaviour to the effect of 14 SINTERING TIME: cfl. 90 MINUTES 0.8 900° C 950° 4 8 12 16 COPPER IN CHARGE, o/o Figure 5. Effect of Copper on Carbon Pickup During Sintering (Sorokin30). c 15 copper in restricting the diffusion of carbon in iron. Crosby et a1. 33 substituted cement copper for commercial copper in a 7% copper subs~itute 1% carbon - iron powder metallurgy alloy. The alloy showed lower strength properties; this was attributed to poor sinterability. 16 III. A. EXPERIMENTAL PROCEDURE General In order to determine the limit of the austenite phase field at 950°C, gas carburization experiments were conducted. Iron-copper compacts were equilibrated with gas mixtures of fixed carbon activities. The reaction was monitored by weight gain measurements utilizing a Cahn electrobalance. The solubility of graphite in various iron-copper alloys up to 6% copper, was determined at 950°, 1000° and 1050°C in a horizontal tube furnace. Wet hydrogen (dew point 25°C) was passed over samples surrounded by powdered graphite. The solidus temperature was determined as a function of the activity of carbon up to graphite saturation, for a 90% copper-iron alloy. B. Furnaces and Temperature Control Three furnaces were used in this investigation. A "wire wound" horizontal furnace was used for preparing homogeneous iron-copper samples. A "wire wound" vertical tube furnace was used for carburiz- ing and weight gain experiments. A silicon carbide resistance-heated furnace with a vertical tube was used for determination of the solidus temperature. For the gas carburization experiments, a Marshall furnace with 38 mm bore and 35 ems heated length was used. A vertical mullite tube 32 mm ID and 76 ems long was used as the reaction chamber. At the lower end of the mullite tube a side arm was attached which served as inlet for the gas. The lower end of the tube was corked; above the cork was a set of mullite baffles, which acted as a gas mixer and radiation shield. The tube was covered at the top with a pyrex plate containing two holes; one for a thermocouple and the other for a fused silica suspension rod. Figure 6 shows a sketch of the apparatus used. A Marshall furnace of 38 mm bore and 35 ems heated length was used both for the preparation of iron-copper alloys and for graphite solubility experiments. A horizontal fused silica tube, 22 mm ID and 92 ems long was used as the reaction chamber. Figure 7 shows a sketch 17 TO POTENTIOMETER J::::=:::::::;, TO PAN OF ELECTROBALANCE r;::::::= CON TROLLING PLATINEL MULLITE TUBE PLATINEL THERMOCOUPLE ----"~ THERMOCOUPLE (TO CONTROL UNIT} • • FURNACE SAMPLE GAS INLET Figure 6. Schematic Diagram of the Apparatus for Gas Carburization Experiments. BOAT CONTAINING SAMPLES PACKED WITH GRAPHITE POWDER CRUCIBLE PACKED WITH GRAPHITE POWDER SAMPLE HOLDER •• BAFFLE GAS INLET FURNACE .... ~ ·-·-· Figure 7. Schematic Diagram of the Apparatus for Graphite Solubility Experiments. 1-' 00 19 of the apparatus. The solidus temperature was determined in a silicon carbide resistance heated furnace. ems long was used. ed for gas inlet. A vertical mullite tube, 16 mm ID and lOZ At the lower end o£ the tube, a side arm was attachThe lower end of the tube was made tight by a water seal and the upper end covered by a tight-fitting refractory cap. Figures 8(a) and (b) schematically represent the apparatus used in this experiment. Each furnace temperature was controlled by a Barber Colman Z7Z P Capacitrol temperature control unit with a Platinel II thermocouple, which regulated the temperature to C. + Z°C. Temperature Measurements A Platinel II thermocouple was used for temperature measurement. A similar Platinel thermocouple, calibrated by the National Bureau of Standards at 900°, 1000°, and 1100°C was used for calibration purposes. In most of the runs a fixed furnace temperature was needed. The furnace temperature was set using the controller setting and checked by the calibrating thermocouple. The working thermocouple was used for temperature measurement before each run initially and later on after alternate runs. This was found satisfactory, as the temperature re- mained essentially constant. Periodic checks of the furnace tempera- ture were made with the calibrating thermocouple. The temperatures measured and controlled as described above were estimated to be reproducible to ± 5°C, except as noted later in cer- tain runs to determine the solidus temperature. the temperature was estimated to be correct to D. In this experiment, + Z°C. Atmosphere Control Thermodynamic calculations were made to determine the relation- ship between gas composition and carbon activity at a given temperature, for the carbon-oxygen-hydrogen system. The results were plotted similar 34 to the diagrammatic method of representation devised by Gurry and are presented in Figure 9. Many of the possible gas mixtures were eliminated from the standpoint of difficulty in mixing or controling. Some of the binary and ternary gas mixtures indicated to be suitable from Figure 9 were found not to give the equilibrium gas 20 1.5 V DC A CIRCUIT TO POTENTIOMETER :::::=::1 MULLITE TUBE PLATINEL THERMOCOUPLE SAMPLE GAS SEAL __.. Figure 8(a) -- - ----- Schematic Diagram of the Apparatus for Solidus Temperature Experiments. 21 TO POTENTIOMETER =~ r;::::::::: TO CIRCUIT MULL ITE TUBE PLATINEL THERMOCOUPLE SAMPLE GRAPHITE CRUCIBLE GRAPHITE ROD ASSEMBLY-------;~ -~~ =--- -·~ -~-:: Figure 8(b) Schematic Diagram of the Apparatus for Solidus Temperature Experiments (Equilibrium with Graphite). 22 H 5.15% C0 2 (C0z!H 2 ) 91.35% C0 2 (C0 2 /CO) 20.90% C02 (C02 /CO) 5.12% C0 2 (C0 2 /CO) D • .& • 0 .t:. o CH 3 COOH C 2 H 5 0H CH 3 0H - - CARBON ISOACTIVITY LINES - - - Feo.947 -Fe I I ICI> 0 0 0 0 0 :! 0 c; I~ 1.,0 ,~ I I I C0 2 0 Figure 9. I '- 0 /co CIS- c 0 The Carbon-Oxygen-Hydrogen System at 950 C and 1 Atm Pressure. 23 composition because of incomplete reaction at 950°C. As an example, CH4 -co 2 mixtures oxidized iron even at high carbon activities. Details of the computer calculations used in calculating Figure 9 are included in Appendix I. At 950°C, CO-C0 2 mixtures were found to be the most suitable. For lower carbon activities pure CO and co 2 were used. Higher carbon activities were generated using a premixed CO-co 2 mixture with pure co. The method of mixing CO and co 2 in the exact desired proportions 14 35 was similar to that used by Darken and Gurry and later by Muan except that gases were passed individually through calibrated flowmeter tubes of a Model 665 Matheson Gas Proportioner. tubes were calibrated with a soap bubble column. The flowmeter This column consist- ed of a graduated glass burette, with a small reservoir of soap solution at the bottom in series with the flowmeter. The rate at which a soap bubble traveled up the column permitted a calculation of the When calibrating co 2 or mixtures containing co 2 , a soap solution presaturated with co 2 was used. gas flow rate. E. Starting Materials For sintering iron-copper compacts, an atmosphere of ultra high purity hydrogen was used. atmospheres were used. For gas carburization experiments, CO-C0 2 The co 2 was supplied by the Matheson Company as Coleman Instrument grade, with a reported purity of 99.99% min. by volume. The purity of the CO used (Matheson C.P. grade) was in excess of 99.5% with 8 ppm. 0 2 . Cylinders of premixed CO and co 2 were prepared and analyzed by the Matheson Company. Iron and copper powders were obtained from the United Mineral & Chemical Corp.; the iron powder was reported to be over 99.99% pure and copper powder reported to be 99.999% pure. In order to allow for the surface oxide on the powders, the loss of weight in hydrogen at 1050°C was determined for iron and copper powders. presented in Appendix II~ These results are along with the chemical analyses of the metal powders, supplied by the United Mineral & Chemical Corp. Graphite powder was Fisher #38 reagent grade, the same as was used by Gurry. 36 24 F. Alloy Preparation Alloys up to 10% Cu were made by a powder metallurgy technique. A list of the alloys prepared is presented in Appendix II. Iron and copper powders were weighed out on an analytical balance and thoroughly mixed in a smooth glass mortar. This mixture was com- pacted into cylindrical pellets 12 mm dia. and 12 mm high. The com- pacts were sintered in hydrogen for 24 hours at 1050°C and quickly cooled in the hydrogen. The sintered pellets were cold pressed to half their height between flat die plates and then reannealed in evacuated fused silica capsules at 1050°C for a minimum of 24 hours. The samples were quenched by cracking the capsules open under water. This processing procedure gave fairly homogeneous alloys as verified by an electron microprobe scan. Optical microscopy verified the absence of free copper. The quenched samples were cold rolled into sheet 0.5 mm thick. The surface was cleaned by sanding with emery paper followed by ultrasonic cleaning in acetone. Samples were cut from the sheet as pieces of average size 12 mm x 12 mm and were ultrasonically cleaned in acetone before each run. G. Gas Carburization Experiments These experiments involved the study of equilibrium of the following reaction: C0 2 + £ = 2CO (where £ refers to carbon dis- solved in austenite). Such a technique has been used quite extensively to measure carbon activities in the binary Fe-C as well as ternary 12-18 Fe-C-X systems. The experimental technique has been discussed in detail. 14 • 15 Iron-copper compacts were equilibrated with CO-C0 2 gas mixtures of known carbon activities, at 9S0°C. The weight gain of the sample was continuously measured with a Cahn electrobalance, Constant sample weight was the criterion for assurance that equilibrium had been attained. be measured. Weight changes of 0.01% for a 1 gm sample could Pure iron samples were run periodically to calibrate the various gas mixtures for their carbon activity. 25 The apparatus used in these experiments is shown in Figure 6. The sample was suspended from a hooked fused silica suspension rod through a hole in the sample. The sample was held at the top of the furnace for 10 minutes, after insertion into the furnace, while the air was flushed from the tube with a mixture of CO and co 2 • The sample was then lowered by the fused silica suspension rod to the hot zone. The upper end of the fused silica rod was then attached to a hook on the left pan of the electrobalance. The weight gain of the sample measured by the electrobalance was displayed on a chart recorder. A more detailed account of the weighing procedure is included in Appendix III. The sample was first held in a CO-C0 2 atmosphere of low carbon activity, until the sample weight became constant. The carbon activity was then increased in a stepwise fashion and the weight gain after every activity change was noted. Initially the carbon activity of the mix- ture was calculated from gas ratios and equilibrium constant data. These were in agreement with the activities to within+ 0.02 calculated on the basis of the weight gain of a pure iron sample and the activity-composition relations for carbon in Fe-C alloys established by Ban-Ya et a1. 13 On account of the above observation, in later experiments the carbon potential of the gas was established by the weight gain for a pure iron sample. This method was judged to be a more accurate way of determining the carbon potential of the gas mixture as the absolute value was not as important as comparison between the weight gain of the Fe-Cu alloy and pure iron. Such a method also took care of changes in buoyancy as a function of gas composition since the buoyancy was expected to be the same for the alloy as for pure iron. A number of data points were checked by decarburization by lowering from a higher carbon activity to a lower one. The weight became constant to within 0.1 mg of the original weight. H. Graphite Solubility Experiments The experimental technique used was similar to that of Gurry 36 for the determination of graphite solubility in gamma iron and later by Fray and Chipman37 for graphite solubility in Fe-Co and Fe-Ni alloys. 26 Gurry saturated his samples at temperature in a hydrogen-toluene atmosphere in equilibrium with graphite, at a flow rate of less than 40 cc./min. Fray and Chipman used hydrogen saturated with isopropyl alcohol at room temperature. In this investigation, graphite solubil- o ity was determined at 950 , 1000 0 0 and 1050 C by saturation of samples with an atmosphere of wet hydrogen (dew point about 25°C) in equilibrium with graphite. The purpose of water-vapour was to generate CO and along with methane, and thus to speed up the reaction rate. co 2 Water vapour was preferred over hydrocarbons or other organic liquids, because there is a lesser possibility of intermediate decomposition products giving a carbon activity greater than one. A sketch of the apparatus is shown in Figure 7. A sample of pure iron and a number of iron-copper alloys were weighed on the electrobalance, and then packed in fine graphite powder in the center of a nickel boat 6.3 em long. The boat was pushed in and out of the furnace by an iron wire. The boat with the samples was placed in the cold zone of the furnace whjle it was flushed with nitrogen. The nitrogen was then replaced by hydrogen and the tube flushed for 10 mins. before pushing the boat into the hot zone. The position of the samples was confined to a zone having a temperature profile not less than 2°C below the maximum temperature of the furnace. In order to minimize carbon con- sumption, the hydrogen flow rate was kept at less than 8 cc./min. After equilibration times of 24, 48, 72, 96, 120 and 144 hours, the boat was pulled to the cold end and the samples removed, cleaned and weighed on the electrobalance. The experiment was continued till the samples attained constant weight. The cleaning procedure for the samples consisted of brushing to remove the adhering graphite followed by ultrasonic cleaning in acetone. The weight gain of the pure iron sample compared well with published data13 , 36 and served as a check on the accuracy of the method. A comparison of the results of the present work with published data is presented in Table X(b) in Appendix IV. 27 I. Solidus Temperature Determination The solidus temperature was determined for a 90% Cu-Fe alloy, as a function of the carbon activity. The presence of liquid, formed as the sample was heated in a carburizing atmosphere, was detected by the loss of strength of the sample suspended between two hooks. The equipment used in this experiment is shown in Figure 8(a) The furnace was flushed with a gas mixture of fixed carbon activity, while the sample was held at the top of the furnace. The sample was then lowered to a position where the temperature was accurately known by a previous calibration experiment 0 0 (temperature range 1050 -1100 C), Initially the sample was held at 1050°C for 3 hours. Next it was lowered to positions where the temperature varied from 1060° to 1100°C and at each position it was held for 20 minutes. At the solidus temper- ature, a liquid phase formed, and the sample no longer supported its own weight. As the sample dropped from the hooks, at the solidus temper- ature a circuit was broken and gave a clear indication of melting. The thermal decomposition of gas mixtures high in CO in the furnace tube below the sample made it impossible to generate carbon activities greater than 0.2, with CO-C0 2 mixtures. This problem of the thermal decomposition of high CO mixtures at temperatures above 1000°C was discussed by Phelps 38 and Ban-Ya et a1. 13 In order to obtain the solidus temperature in equilibrium with graphite a modified technique was used. The apparatus used is illustrated schematically in Figure 8(b). A CO-C0 2 mixture containing 5.72% co 2 was allowed to come to equilibrium with a graphite assembly before it passed over the sample, which was in turn surrounded by a perforated graphite crucible containing graphite powder. 28 IV. EXPERIMENTAL RESULTS AND DISCUSSION The experimental results are presented in two forms: a tabular form in Appendix IV and in the form of graphs and diagrams in the following sections. The experiments were designed to determine the limits of the austenite field of the iron~copper-carbon system at 950°C and the extent of graphite solubility in iron-copper alloys as a function of temperature, Additional experiments were conducted to study the effect of carbon on the solidus temperature. The effect of copper on the carburization rate was also observed. A. Presentation of Results The experimental results are presented in tabular form in Appendix IV. The results of gas carburization experiments are present- ed in Tables I through VIII. Figures lO(a) through (g) summarize the same data in the form of graphs of carbon activity vs. % carbon. The activity-composition curve for pure iron is superimposed on each of these graphs to permit a ready comparison of a specific iron-copper alloy with pure iron. Table IX is a presentation of carbon isoactivity data derived from Figures lO(a) through (g). 0 0 The results of graphite solubility experiments at 950 , 1000 , and 1050°C are presented in Table X(a). The results at 950°C, in conjunction with isoactivity data from gas carburization experiments, were used in constructing the 950°C isothermal section of the iron rich end of the iron-copper-carbon phase diagram (Figure 11). y/y + £ The phase boundary indicated by a dashed line is a possible boundary based on apparent "breaks" in the activity-composition curves as discussed later. In order to determine accurately the y/y + £ phase boundary, sev- eral iron-copper-carbon alloys were quenched in water from the carburizing temperature of 950°C, after a holding period of 24 hours. A metallographic examination at 1000 X showed massive martensite with no visible precipitate of epsilon before or after etching. Apparent- ly, the time required to achieve a precipitate, visible at 1000 X, is in excess of 24 hours at 950°C. 29 1.0 0.9 • • 0.3 °/o COPPER PURE IRON 0.8 z 0 0.7 ([) 0::: <( 0.6 (.) LL 0.5 0 >- I- -> - 0.4 I- u <( 0.3 0.2 0.1 0.2 0.4 1.2 WT PCT CARBON Figure lO(a) Activity of Carbon vs % Carbon at 950°C for a 0.3% Copper Alloy. 1.4 30 1.0 0.9 • • 0.7 °/o COPPER PURE IRON 0.8 z 0.7 OJ 0:: 0.6 0 <( u LL 0.5 t- >- 0.4 u <( 0.3 0 > t- 0.2 0.1 0.2 0.4 0.6 0.8 1.0 1.2 WT. PCT. CARBON Figure lO(b) Activity of Carbon vs % Carbon at 950°C for a 0.7% Copper Alloy. 1.4 31 1.0 0.9 1.0 °/o COPPER PURE IRON • • 0.8 z 0 ([) 0::: <( 0.6 LL 0.5 >- 0.4 I- 0.3 u 0 I- -> u <( 0.2 0.4 0.6 0.8 1.0 1.2 WT. PCT CARBON Figure lO(c) Activity of Carbon vs % Carbon at 950°C for a 1.0% Copper Alloy. 1.4 32 1.0 0.9 1.3 °/o COPPER PURE IRON • • 0.8 z 0 0.7 a:l a:: <( u 0.6 lJ... 0 0.5 >.,_ > .-,_ 0.4 u <( 0.3 0.2 0.1 0.2 0.4 0.6 0.8 1.0 1.2 WT. PCT CARBON Figure lO(d) Activity of Carbon vs % Carbon at 950°C for a 1.3% Copper Alloy. 1.4 33 • • 2.5 °/o COPPER PURE IRON z 0 (]) a: u <( LL. 0 >- ~ 0.4 u <( 0.3 > 1- 0.2 0.2 0.4 0.6 0.8 1.2 WT. PCT. CARBON Figure lO(e) Activity of Carbon vs % Carbon at 950°C for a 2.5% Copper Alloy. 1.4 34 0.9 • 3.0 °/o COPPER • PURE IRON 0.8 z 0.7 0 CD 0:: <( 0.6 u LL 0 >- t- - 0.5 I I I 0.4 I > t- u - .... .... I I 0.3 I <( 0.2 0.1 0.2 0.4 0.6 0.8 1.0 WT. PCT CARBON Figure lO(f) Activity of Carbon vs % Carbon at 950°C for a 3.0% Copper Alloy. 1.4 35 • • 3.5 °/o COPPER PURE IRON z 0 m a:: <( u LJ.. 0 >- I- -> -I- u 0.4 0.3 <( 0.2 0.1 0.2 0.4 0.6 1.0 1.2 WT. PCT. CARBON Figure lO(g) Activity of Carbon vs % Carbon at 950°C for a 3.5% Copper Alloy. 1.4 36 - - ISOACTIVITY LINES - - - POSSIBLE PHASE BOUNDARIES 950° y + E c + C(gr) y + C(gr) 2.0 3.0 WT. PCT CARBON Figure 11. Isothermal Section of the Iron-Rich End of the Iron-Copper-Carbon Phase Diagram. 4.0 37 The solubility of copper in iron-copper austenite was taken from the work of Speich et al. 7 The solubility of co~per, obtained by solving their equation is given in the table below; Solubility of Copper in Austenite* Temperature 0 c Solubility % Cu 1000 4.086 4.943 1050 6.172 950 * From Equation 1, p. 5 Figure 12 shows the extent of the stable austenite field based on graphite solubility measurements. y/y + £ As indicated earlier the phase boundary at 950°C was based on apparent "breaks" in isoactivity curves. At 1000°C and 1050°C 1 this boundary was taken as a line joining the break in the graphite solubility curve and the y/y + £ boundary points in the iron-copper system. 0 0 The effect of copper 0 content on graphite solubility at 950 , 1000 , and 1050 C is presented in Figu:re 13. The results of the solidus determination for an iron-copper alloy containing 90% copper initially are presented in Table XI. is a graphical representation of the same data. Figure 14 The effect of carbon activity, up to 0.2, was obtained by a gas carburization technique and is indicated in Figure 14 by a bold line. This line is extended as a dashed line to meet the point representing the solidus temperature in equilibrium with graphite. The solidus temperature in this work is the temperature at which the first liquid forms, and is the copperrich peritectic temperature referred to by Maddocks and Claussen. 6 Table XII contains the time for various alloys (up to 1.3% copper) 0 to reach the equilibrium carbon content at 950 C. ly represents this data. Figure 15 graphical- The time given represents the time for a 38 - - GRAPHITE SOLUBILITY - - - POSSIBLE PHASE BOUNDARIES • 950 oc .. 1000 °C • 1050 °C 0 eo· I I I o I (I)· \ I \ I \ I \ I \ I \ I \ \ \ ~ 2.0 3.0 WT. PCT. CARBON Figure 12. The Effect of Temperature on the Extent of the Austenite Field. 4.0 39 ~ t-= 3: z l.J.J ...._ :r: CL <( a:: (!) LL 0 0.6 _J CD ::> 950° c 1000° c • 1050° c • >...._ 0.4 4 " POSSIBLE BOUNDARY _J 0 en 2.0 WT. PCT. COPPER Figure 13. The Effect of Copper on the Solubility of Graphite in Iron-Copper Alloys. 4.0 40 1100 1096 (.) 0 1092 w -- ------ a:: ::::> 1088 I<( a:: a.. w ~ w 1084 1080 I- -- -- -..._ en ::::> 1076 - -- -- -.. 0 _J 0 en 1072 1068 0.1 0.7 0.8 0.9 ACTIVITY OF CARBON Figure 14. The Effect of Carbon Activity on the Solidus Temperature for a 90% Copper Alloy 1.0 41 (/) TEMPERATURE 950° C 7 CARBON ACTIVITY 0.08 a:: ::::> 0 6 z 5 I w ~ f- z 0 f- - <( 0::: 4 3 2 (I) .....1 -::::> 0 w 0.2 0.4 0.6 0.8 1.0 1.2 1.4 WT. PCT. COPPER Figure 15. The Effect of Copper Content of the Alloy on Time to Reach the Equilibrium Carbon Content During Gas Carburization. 1.6 42 sample containing no carbon to come to equilibrium with a gas whose carbon activity was 0.08. A similar time could not be read directly from the weight gain data for higher carbon levels because the time to reach equilibrium could be compared only if the initial and final activity was the same. B. This generally was not the case. Discussion of Results 1. Gas Carburization and Graphite Solubility Copper and carbon are both soluble in austenite but they are practically insoluble in each other. Hence, it was expected that, in a ternary alloy, each would have a significant influence on the solubility of the other. Gas carburization and graphite solubility experiments covered the range from low carbon activities to graphite saturation, for iron-copper alloys up to 6 pet. copper. The gas carburization re- sults were plotted in the form of activity-composition curves for carbon. In the single phase region, a smooth curve was expected, with a change in slope or a "break'' as the second phase precipitated. 39 Work on the Ti-0-H system by Hepworth and Schuhmann contains hydrogen solubility plots, which show a discontinuity or "break" corresponding to a transition from aTi to aTi + STi. In the present work, the exact position of the break is not clear for the number of runs made. A larger number of points need to be determined in the vicinity of the break to accurately determine the position of the break. The results of gas carburization experiments show that, in general, the addition of copper increases the activity of carbon.* This effect of copper is in agreement with Sorokin's observation 30 of a decrease in carbon content with copper addition during sintering of iron-copper compacts in a carburizing medium at 950°C. Figure 5, p. 14) * (see He cites an earlier work in which the addition of The alloy containing 1% copper exhibited an anomalous behaviour above a carbon activity of about 0.4 where a lowering of carbon activity was observed with covper addition. 43 2.7% copper reduced the carbon absorbtion by 50%. Shoji et al. 27 also report a slight decrease in the carbon content with copper addition, at 930°C and a tixed carbon activity (their pure iron sample picked up 0.85% carbon), Since their data is so fragmentary~ a qualitative agreement with the present work is all that can be noted. The present result is in apparent disagreement with the work of Yoshida and Sano. 22 They noted a slight decrease in carbon activity by copper addition in the temperature range 850°-950°C. Chipman and Brush 21 indicate a lack of quantitative data for establishing interaction parameters for the activity of carbon in copper-alloyed austenite. The calculated values of the activity coefficient of carbon in austenite at 950°C, for copper contents up to 0.7% are presented in Table XIII and graphically in Figure 16. the standard state for carbon. Graphite was taken as The activity coefficient was defined as follows: f c = a c I (%C) (5) It was not possible to carry out a similar calculation for higher copper contents, as too few points were available in the single phase field. As seen from Figure 16, copper increased the activity coeffic- ient of carbon in austenite. Graphite solubility decreased with the addition of copper at all three temperatures. This behaviour seems to confirm the results of gas carburization experiments where the solubility of carbon in ironcopper alloys at high carbon activities was less than that for pure iron. The effect of copper is similar to that of nickel, cobalt and silicon. 37 The graphite solubility values for high copper alloys were lower than the corresponding values obtained by extrapolation of the gas carburization data to an activity of carbon of one. this must await further work. The reason for The effect of copper on the graphite solubility is more pronounced at 950°C than at 1050°C (Figure 13). The knowledge of the austenite fields in the form of isothermal diagrams, such as Figures 11 and 12, can be utilized by the heat treater in selecting heat treatment conditions for copper bearing steels. This may involve selecting an austenitizing temperature for a hardening operation or a normalizing operation. 44 TEMPERATURE 950°C • • • 0.7 °/o COPPER 0.3 °/o COPPER PURE IRON -0.3 -0.2 ...... (.) 0 0 -0.1 0.2 0.4 0.6 0.8 1.0 1.2 WT. PCT. CARBON Figure 16. The Effect of Copper on the Activity Coefficient of Carbon. 1.4 1.6 45 2. Solidus Temperature Determination The temperature referred to in the present investigation as the "solidus temperature" is the copper~rich peritectic temperature determined by Maddocks and Claussen 6 by thermal analysis. Copper melts at 0 1083 C; however, for Fe-Cu alloys containing more than about 5% iron, the lowest temperature at which a liquid forms is 1094°c. 3 It was of interest to determine if this temperature could be lowered by carbon addition. As mentioned earlier carbon activities up to 0.2 were obtained by gas carburization, and an activity of one was obtained by equilibrium with graphite. A lowering of the peritectic temperature was observed, with the temperature dropping from 1095°C in the binary iron-copper system to 1078°C in equilibrium with graphite. Maddocks and Claussen 6 state that the peritectic temperature does not change due to the presence of carbon. Their data does show an appreciable lowering, however, in two alloys investigated. The temperatures were measured accurately in this experiment so that it seems that the lowering was real and not due to fluctuation in temperature. The solidus temperature in the iron-copper system was determined as 1095°C, which agrees well with 0 the reported value of 1094 C. 3 In the present work, phases occurring after melting were not identified. A more accurate determination with greater emphasis on the assurance of attainment of equilibrium, and identification of the phases after melting should yield a better insight in understanding liquid phase sintering and the volume changes occurring in the sintering of iron-copper-carbon alloys. Such determinations can also give information on temperatures and compositions at which "hot shortness" would occur in steels. 3. Kinetics of Carburization Although the present investigation was concerned mostly with the thermodynamics and phase relations of the system, certain observations were made on the rate of carburization from weight gain vs. time data. As mentioned earlier, the experimental technique permitted a continuous measurement of the weight gain as the sample came to equilibrium with the gas. 46 The e~~ect of copper is to shorten the time required to reach equilibrium carbon content at 950°C trom a gas having a carbon activity of 0.08, for samples containing initially no carbon. A similar effect was observed during carburization at higher activities of carbon but no quantitative results could be obtained because exactly identical carbon activities were not maintained for different alloys. This observation compares with the remark of Shoji and Yamada 26 where a shorter carburizing time was found for sintered iron-copper alloyed powders in comparison to nickel alloyed powders. C. Suggestions for Further Work On the basis of this investigation certain areas seems particular- ly interesting for further work: For the temperatures investigated, additional data points should be obtained around the vicinity o;f the "break", in order to accurately fix the position of the "break". Longer equilibration times or examina- tion of carburized specimens by electron microscopy would accurately locate the y/y + E phase boundary. The solubility of graphite in high copper alloys needs to be redetermined with longer equilibration times, in order to resolve the discrepancy between graphite solubility and gas carburization data. The ternary austenite field needs to be investigated at other temperatures, both higher and lower than investigated here. This would involve determination of both isothermal sections and carbon activities. Of particular importance would be the composition of austenite up to the solidus temperature. Equilibrium times needed to render precipitat- ed epsilon phase detectable metallographically should be determined. This would permit an accurate determination of the y/y + E phase bound- ary. With a larger number of data points for the activity of carbon in the single phase field, a ternary Gibbs~Duhem integration can be per. 40 formed us~ng Schuhmann's method to determine the activities of copper and iron in austenite. The complete thermodynamic properties of iron- copper-carbon austenite could then be determined. The peritectic temperature at the copper-rich end needs to be determined to establish the effect of carbon. Emphasis must be made 47 on the assured attainment of equilibrium, and on the identification of the phases after melting. Maddocks and Claussen 6 reported the raising of the iron-carbon eutectic by the presence of copper. The composition of the liquid and austenite phase at this temperature would be useful in understanding the behaviour of copper in cast irons. The kinetics of carburization of sintered iron-copper compacts and of carburizing during sintering needs further work. As part of such an investigation it would be of interest to determine the carbon profile across sintered compacts, to assist in the design of processes for designing powder metallurgy parts. 48 V. SUMMARY AND CONCLUSIONS The 950°C isothermal section of the iron-rich end of the ironcopper-carbon phase diagram was constructed, based on the results of gas carburization experiments in conjunction with graphite solubility results. diagram. Isoactivity lines for carbon are superimposed on the The effect of copper was to increase the activity of carbon and decrease its solubility. Graphite solubility experiments at 950°, 1000°, and 1050°C showed that the graphite solubility was lowered by copper addition. The effect of copper was more pronounced at the lower temperature. For copper rich alloys, a lowering of the solidus temperature was observed with increasing carbon contents. obtained in equilibrium with graphite. A value of 1078° was Copper was also shown to in- crease the rate of carburization. The application of the results of this work has been mentioned and suggestions for further work have been made. 49 BIBLIOGRAPHY 1• "L.1 t era t ure re f erences on Copper in Steel, " 1951-63, British Iron and Steel Research Association, 1964, pp. 20. 2. K. Parameswaran and A.E. Morris, "Bibliography on Copper in Iron, Steel and Related Systems," 1964-70, International Copper Research Association (to be published). 3. Max Hansen, "Constitution of Binary Alloys," McGraw-Hill Book Company, Inc., New York, 1958, pp. 353-365, 580-582. 4. Rodney Elliott, "Constitution of Binary Alloys - 1st Supplement," McGraw-Hill Book Company, Inc., New York, 1965, pp. 212-213, 372-373. 5. Ralph Hultgren, Raymond L, Orr, and Kenneth K. Kelley, "Supplement to Selected Values of Thermodynamic Properties of Metals and Alloys," University of California, Berkeley, California, June 1968. 6. W.R. Maddocks and G.E. Claussen, Iron Steel Institute (London), Special Report No. 14, 1936, pp. 97-117. (Data from above redrawn in Metals Handbook, 1948 Edition, American Society for Metals, Metals Park, Ohio, p. 1250). 7. G.R. Speich, J.A. Gula and R.M. Fisher, "Diffusivity and Solubility Limit of Copper in Alpha and Gannna It:on, The Electron Microprobe," John Wiley and Sons Inc., New York, 1966 7 pp. 525-542. 8. Francis A. Shunk, "Constitution of Binary Alloys- 2nd Supplement," McGraw-Hill Book Company, Inc., New York, 1969, pp. 143-144. 9. T. Ishiwara, T. Yonekura and T. Ishigaki, "On The Ternary Diagram of the System Iron, Carbon, and Copper, 11 Sci. Rep. , Sendai, ser. 1, 1926, Vol. 15, pp. 81-114. 10. J.L. Gregg and B.N. Daniloff, "The Alloys of Iron and Copper," McGraw-Hill Book Company, Inc., New York, 1934, pp. 7-53. 11. L. Habraken and T. Greday, "Copper in Carbon and Low Alloy Steels," Metalen, 1966, Vol. 40, No. 8, pp. 262-273. 12. J.A. Lund and A.M. Lawson, "Massive Martensite Reaction in Eutectoid Iron-Copper Alloys," Trans. Met. Soc. AIME, April 1966, Vol. 235, pp. 581-583. 13. Shiro Ban-Ya, John F. Elliott, and John Chipman, "Thermodynamics of Austenitic Iron-Copper Alloys," Trans. Met. Soc. AIME, May 1970, Vol. 1, pp. 1313-1320, 14. L.S. Darken and R.W. Gurry, ''The System Iron-Oxygen II. Equilibria and Thermodynamics of Liquid Oxide and Other Phases,'' J. Am. Chem. Soc., 1946, Vol. 68, pp. 798-816. 50 15. R.P. Smith, "Equilibrium of Iron-Carbon Alloys with Mixtures of CO-C0 2 and CH 4 -H 2 ," J. Am. Chem. Soc. 1946, Vol. 68, pp. 1163-1175. 16. Shiro Ban-Ya, John F. Elliott and John Chipman, "Activity of Carbon in Fe~c Alloys at 1150°C," Trans. Met. Soc. AIME, 1969, Vol. 245, 1199-1206. 17. Toshisada Mori, Kimio Fujimura, Hiraoki Okajima, and Akio Yamauchi, ''E;(:fects of: Chromium, Copper and Tin on Carbon Activity of High Carbon Liquid Steel," Tetsu-to-Hagane, 1968, Vol. 54, No. 4, pp. 321329. 18. L.A. Shvartsman and I.A. Tomilin, "Activity of Carbon in Molten Iron," Doklady Akad. Nauk SSSR, 1968, Vol. 179, No. 5, pp. 11591162. 19. Theodore P. Christini, "Determination of Iron Activities in Solid Iron-Copper Alloys by Use of a Solid Electrolyte Technique," Ph.D. Thesis, The Pennsylvania State University, 1970. 20. John Joseph Demchalk, "Residual Elements in Scrap Iron - An Equilibrium Study of the Residual Element Copper," Ph.D. Thesis, The Pennsylvania State University, 1970. 21. John Chipman and Edwin F. Brush, "The Activity of Carbon in Alloyed 0 Austenite at 1000 C," Trans. Met. Soc. AIME, January 1968, Vol. 242, pp. 35-41. 22. T. Yoshida and K. Sano, Mem. Fac. Eng., Nagoya University, 1953, Vol. 5, pp. 96-99. 23. Alan Moss, "Copper as an Alloy in Steel and Cast Iron," Australasian Engg., 1967, pp. 33-34, 36. 24. C. Corsetti and N. Valota, "Cast Irons Containing Copper," Fond. Ital., Vol. 15, No. 10, pp. 343-352. 25. G. Bockstiegel, "Nature and Causes of Volume Changes in the Sintering of Iron-Copper and Iron-Copper-Graphite Powder Compacts," Translated from Stahl Und Eisen, 1959, Vol. 17, pp. 1187-1196. 26. K. Shoji and S. Yamada, "Gas Carburizing and Quenching of Sintered Ferrous Materials, 11 Translated from Tetsu-to-Hagane, 1968, Vol. 54, No. 4, pp. 410-415. 27. K. Shoji, H. Mitani and S. Yamada, "Gas Carburizing of Iron and Iron-Copper Powders," Translated from Tetsu-to-Hagane, 1969, Vol. 55, p. S233. 28. K. Shoji and S. Yamada, "Controlled Atmospheres in Furances for the Sintering of Iron Powder Products," Translated from Tetsuto-Hagane, 1963, Vol. 49, No. 10, pp. 1507-1508. 51 29. V.K. Sorokin, "Effect of Copper and Graphite on :Properties of Sintered Iron-Base Alloys," Translated from :Metalloveden;i.e I Term. Obrabotka Metallov, December 1960~ pp. 42-43. 30. V.K. Sorokin, "Effects of Copper on Carbon Absorbtion in Sintering Iron Copper Alloys," Translated from Metallovedenie I. Term. Obrabotka Metallov, October 1959, pp. 61-62. 31. V. K. Sorokin 7 "Effect of Small Additions of Copper on the Sintering of Stainless Steel (Powders)," Translated from Izvest. VuzChern. Met., 1966, Vol, 9, No. 11, pp. 127-128. 32. A. Domsa, "Effect of Copper on the Performance of Bearings of Sintered Iron-Graphite Powders," Translated from Neue Hutte, March 1964, Vol. 9, pp. 186-188. 33. Robert L. Crosby, D.H. Desy, and Robert M. Doerr, "Use of Cement Copper in an Iron-Copper-Carbon Powder Metallurgy Alloy," Report of Investigations No. 7348, U.S. Bureau of Mines, February 1970, pp. 14. 34. R.W. Gurry, "Composition of Atmospheres Inert to Heated Carbon Steels," Trans. AIME., Journal of Metals, April 1950, Vol. 188, pp. 671-687. 35. A. Muan, "Phase Equilibria in the System FeO-Fe 2 o3-Si0 2 ," Trans. AIME, 1955, Vol. 203, pp. 965-976. 36. R.W. Gurry, "The Solubility of Carbon as Graphite in Ganuna Iron," Trans. AIME, 1942, Vol. 150, pp. 147-156. 37. Derek J. Fray and John Chipman, ''The Solubility of Graphite in Iron-Nickel and Iron-Cobalt Alloys at 1000°C, Trans. Met. Soc. AIME, May 1969, Vol. 245, pp. 1143-1144. 38. W.C. Phelps Jr., "Thermodynamics of the Iron-Carbon-Silicon System," Ph.D. Thesis, Purdue University, 1960. 39. M.T. Hepworth and R. Schuhmann, Jr., "Thermodynamic Properties of Titanium-Hydrogen-Oxygen Alloys," Trans. Met. Soc. AIME, October 1962, Vol. 224, pp. 928-935. 40. R. Schuhmann, Jr., "Application of Gibbs-Duhem Equations to Ternary Systems," Acta Metallurgia, May 1955, Vol. 3, pp. 219-226. 41. R. Littlewood, "Thermodynamics of the Interaction of Atmospheres with Alloy Steels," Jour. of the Iron and Steel Institute, February 1964, Vol. 202, pp. 143-146. 52 42. Richard A. Robie and David R. Waldbaum~ "Thermodynamic Properties o~ Minerals and Related Substances at 298.15°K and One Atmosphere Pressure and at Higher Temperatures~" Geological Survey Bulletin 1259, Washington, 1968, p. 80, 100, 101~ 109, 114. 43. W.B.A. Sharp and D. Mortimer, "Accurate Thermogravimetry in Flowing Gases,'' Jour. of Sci. Inst., 1968, Vol. 1, ser. 2, pp. 843-846. 53 VITA Krishna Parameswaran was born March 3, 1946 in Madras, India. He received his primary and secondary education in Bombay, India. He received a Bachelor of Technology Degree in Metallurgical Engineering from the Indian Institute of Technology, Bombay, India in August 1968. He entered the University of Missouri-Rolla in January 1969 for a Master of Science Degree in Metallurgical Engineering. He is a student member of the American Society of Metals and the Metallurgical Society of AIME. 54 APPENDICES 55 APPENDLX I CALCULATION OF ATMOSPHERES WITH A SPECIFIC ACTIVITY OF CARBON AT 950°C A. Gurry's Diagram at 950°C and 1 Atm Pressure In Gurry's 34 diagramatic method of representation~ the equilibrium compositions are represented by atomic fractions of the constituents of the gas phase. The principal advantage of Gurry's method, is that the entire range of composition can be covered in a single diagram. Atomic fractions can be easily correlated with the room temperature analysis. A representation involving atomic fractions is independent of temperature in contrast with equilibrium compositions in terms of molecular species in a gas mixture, which change with temperature. The only aspect not covered by such a representation is the molecular constitution of the equilibrated gas. Endothermic atmospheres used in carburizing are composed of CO, C0 2 , CH 4 , H2 , H2 0 and N2 • The atmosphere is in equilibrium with a steel (comprised of Fe and C). Such a system is a five component system. If there is a single condensed phase, such as austenite, in equilibrium with the atmosphere then the degrees of freedom as given by the phase rule is 5. A set of 3 independent reactions chosen are: 2CO (6) (7) (8) Two degrees of freedom remain after the temperature, total pressure and carbon activity are fixed. In the present calculations, nitrogen free atmospheres were considered. Hence, by choosing the CO content of the atmosphere arbitrarily, the composition of the rest of the gas phase was fixed by chemical equilibrium. (9) 56 (CH 4 ) :::: (H 2 0) :::: Kzac (Hz) 2 (10) (C0 2 ) (H 2 ) (11) acK1K3 (CO) + (C0 2 ) + (CH4 ) + (H 2 ) + (H 2 0) p (12) where = molecular partial = total pressure in (X) P a pressure of constitutent X atmospheres = activity of carbon (standard state graphite) c At a given temperature, activity of carbon, total pressure and chosen (CO) content, the (C0 2 ) content was determined from Equation (9). Equations (10), (11) and (12) were then solved simultaneously to obtain the (cH 4 ), (H 2 ), and (H 2 0) contents. The equilibrium composition was converted to atomic partial pressures as follows: (13) (14) (15) H s C + 0 + (16) H A computer program was written to carry out these calculations and the atomic fractions C/S, 0/S, and H/S were printed out for various carbon activities. Littlewood. 41 pressure. The program is similar to the one used by The calculations were done for 950°C and 1 atm total The results are plotted in Figure 9 (p.ZO ), where the coordinates are the atomic fractions. On this plot various molecular constituents were represented by appropriate points. Gas mixtures to give a desired carbon activity can be calculated by the application of the lever rule. 57 The atomic fractions representing conditions where iron is in equilibrium with wustite at 950°C were calculated using equilibrium constant 42 data from Robie and Waldbaum. The results are superimposed on the diagram as a dashed line. Gas mixtures lying to the left of this line tend to oxidize iron. B. Source of Data for the Calculations The thermodynamic data used for the calculations was obtained from a recent compilation. 42 Log K values for the formation of CO, co 2 , 0 0 0 CH 4 and H2 0 at 1100 K, 1300 K, and 1500 K were used to calculate the constants A, B, and C for the formula: Log K eq =A + B+ T CT (17) where T is °K c A B co 5738 4.843 -1.22 X 10-4 co 2 20592 0.115 -0.30 X 10- 4 H2 12843 -2.673 -1.09 X 10- 4 4639 -5.563 -0.91 X 10- 4 CH4 From this data Log K for the three reactions of interest (Equations (6), (7) and (8) are: i - 91 6 + 9.572 - 2.14 Log Kl X l0- 4T Log K2 = 4639 --T 5.563 - 0.91 X l0- 4 T Log K3 = 2011 --T 2.055 + 2.01 X l0- 4 T 58 These values of these equilibrium constants were calculated at 50°C intervals for the temperature range 700°C-1400°C and are shown below: T°C Kl K2 K3 700 0.98 0.130 1.61 750 2.8 0.076 1. 31 800 7.0 0.046 1.1 850 16 0.029 0.91 900 35 0.019 o. 78 950 71 0.013 0.68 1000 140 0.0092 0.60 1050 250 0.0067 0.53 1100 440 0.0049 0.48 1150 730 0.0037 0.44 1200 1170 0.0028 0.40 1250 1820 0.0022 0.37 1300 2750 0.0017 0.34 1350 4050 0.0014 0.32 1400 5800 0.0011 0.30 59 APPENDIX II STARTING MATERIALS AND LIST OF ALLOYS PREPARED The chemical analysis of the metal powders as supplied by the United Mineral & Chemical Corp. is given below: Iron powder, Grade I Iron Sponge, -325 mesh, Reported purity 99.99% min. Spectrographic analysis: Cu lppm. Mg Mn Si lppm. 3ppm. 2ppm. max. Copper powder, -325 mesh, Reported purity 99.999% min. Spectrographic analysis: Cd Cr Mn Si lppm. lppm. lppm. lppm. lppm. max. max. max. max. Ag Fe lppm. max. Graphite powder, Acheson No. 38 grade. In order to account for the surface oxide on metal powders a loss of weight in hydrogen at 1050°C was determined and is reported below: Batch 1 Iron powder 1.150%, Copper powder 0.188% Batch 2 Iron powder 1.365%, Copper powder 0.266% Alloys having the following % Cu were prepared: 0.0, 0.1, 0.2, 0.3, 0.5, 0.7, 1.0, 1.3, 1.6, 2.0, 2.5, 3.0, 3.5, 4.0, 4.5, 5.0, 6.0, 7.0, 8.0, 9.0, 10.0, 90.0. in one or more of the experiments, Alloys underlined were used the others kept for future use. 60 ,AJ;JPENDIX lU WEIGHING PROCEDURE AND SOUR.CES OF ERROR IN THERMOGRAVJMETR.Y The weight gain of the samples in gas carburization experiments was measured on a Cahn RH electrobalance and recorded on a Texas Instruments chart recorder. The balance was calibrated for a weight of 7 gms. A brief outline of the calibrating procedure is outlined below: Balance control setting. Mass Dial range: 100 mgs. Recorder range: 10 mgs. Hi-Lo: Lo Factor: 1 Filter: 3 Calibrating weight: 0.5 x Mass dial range (50 mgs.) The maximum sample weight was 2 gm and was expected to gain less than 2% or 40 mg. To allow for greater flexibility the next highest range was selected. (1) The mass dial was set on 0.5000 and the recorder was zeroed in with the set 50% control. (2) The calibrating weight was removed. The mass dial was set to 0.0000 and the recorder zeroed in with the set 0-100% control. (3) to 0.5000. The calibrating weight was replaced and mass dial set back Steps (1), (2), (3) were repeated till no adjustment was necessary in going back to (1). (4) Leaving the calibrating weight on, the recorder range switch was set at 10% of mass dial range or 10 mg. Mass dial was set on 0.4000 and the recorder was set at 100% using the calibrate recorder control. The calibration was checked from time to time with 1, 5, and 10 mg calibrating weights. The sample was weighed on an analytical balance. The weights on the left pan of the electrobalance were adjusted so that the fused 61 silica rod suspension assembly and the sample would weigh within the calibrated range. The weight of the sample at any time was the sum of the mass dial reading and the recorder reading. The precision in measurement was 0.01%. and The usual sources of error in thermogravimetry discussed by Sharp . 43 Mort~mer are: (1) Heating of the balance from furnace heat. Only the lower part 0 of the hangdown tube was heated to about 10 C above room temperature. Also, since most of the runs were isothermal, error from balance heating was not significant. (2) Electrostatic effects due to charges on glass components. (3) Bouyancy errors. (4) Gas turbulence. In these experiments, the technique was to compare the weight gain of an alloy with pure iron. Bouyancy errors were assumed to be of the same magnitude for iron as for iron-copper alloys. on the chart was within ! The random noise 0.1 mg with no sharp changes; so that it was assumed that errors due to electrostatic and gas turbulence effects were not significant. 62 APJ?ENDI.X IV SUMMARY OF EXPERIMENTAL RESULTS A. Gas Carburization Experiments The results of gas carburization experiments at 950°C are present- ed in Tables I through VIII. The carbon content was determined from the weight gain measurements on the electrobalance. Table I Activity of Carbon vs % Carbon for Pure Iron Activity of Carbon a c Table II Wt. % Carbon %c 0.08 0.17 0.12 0.27 0.20 0.40 0.29 0.55 0.37 0.67 0.43 0.76 0.68 1.07 o. 79 1.18 1. 00 1.37 Activity of Carbon vs % Carbon for 0.3% Cu Alloy Activity of Carbon a c Wt. % Carbon %c 0.08 0.04 0.16 0.26 0.33 0.48 0.44 0.66 0.61 0.90 0.69 0.96 63 Table III Activity of Carbon vs% Carbon for 0.7% Cu Alloy Activity of Carbon a Wt. % Carbon %c 0.07 0.03 0.17 0.21 0.30 0.41 0.40 0.56 0.61 0.87 0.69 0.96 0.92 1.25 c Table IV Ac tivi ty of Carbon vs % Carbon for 1. 0% Cu Alloy Activity of Carbon a c Wt. % Carbon %c 0.07 0.13 0.11 0.18 0.27 0.41 0.44 0.86 0.61 1.11. 0.71 1.36 64 Table V Activity of Carbon vs % Carbon for 1.3% Cu Alloy Activity of Carbon a c Table VI Wt. % Carbon %c 0.06 0.14 0.13 0.25 0.23 0.42 0.46 0.67 0.55 0.91 0.71 1.09 0.81 1.19 0.95 l. 29 Activity of Carbon vs % Carbon for 2.5% Cu Alloy Activity of Carbon ac Wt. % Carbon %c 0.06 0.12 0.16 0.25 0.26 0.41 0.46 0.54 0.53 o. 79 0.66 0.87 0.74 1.01 0.82 1.08 0.90 1.15 0.96 1.18 65 Table VII Activity of Carbon vs% Carbon for 3.0% Cu Alloy Activity of Carbon a c Table VIII Wt. % Carbon %c 0.07 0.11 0.11 0.18 0.25 0.38 0.49 0.66 0.56 0.80 0.71 0.94 0.84 1.07 Activity of Carbon vs % Carbon for 3.5% Cu Alloy Activity of Carbon a c Wt. % Carbon %c 0.06 0.12 0.15 0.29 0.21 0.37 0.25 0.47 0.35 0.54 0.53 o. 79 0.64 0.94 0.82 1.14 0.94 1.14 66 Table IX presents isoactivity data, obtained ;(rom ;Figures 10 (a) through lO(g) -Gas Carburization Experiments. Table IX Activity of carbon a c Isoactivity of Carbon at Di;fferent Copper Alloys % Copper 0.0 0.3 0.7 1.0 1.3 2.5 3.0 3.5 0.1 0.22 0.10 0.08 0.17 0.22 0.19 0.16 0.20 0.2 0.41 0.28 0.25 0.32 0.37 0.33 0.32 0.36 0.3 0.57 0.45 0.41 0.47 0.50 0.45 0.45 0.50 0.4 0. 72 0.60 0.57 o. 70 0.60 0.52 0.55 0.64 0.5 0.86 0.75 0.72 0.94 o. 71 0.65 0.71 0.78 0.6 0.98 0.88 0.85 1.10 0.98 0.83 0.85 0.90 0.7 1.10 0.97 0.98 1.32 1.08 0.97 0.94 1. 02 0.8 1.20 1.11 1.18 1.07 1. 03 1.11 0.9 1.29 1.23 1.26 1.14 1.0 1. 37 67 B. Graphite Solubility Experiments Table X(a) summarizes the results of graphite solubility experi- ments. Table X(b) gives a comparison of these results of this work for pure iron with published data. Table X(a) Alloy Content % Cu Solubility of Graphite in Iron-Copper Alloys Graphite Solubility (% C) Temperature 950°C 1050°C l000°c 0.0 1.32 1.51 1.65 0.2 1. 25 1.45 1. 57 0.3 1.60 0.5 1.10 1.37 1.58 0.7 1. 00 1.35 1. 56 1.0 0.99 1.32 1.52 1.3 0.95 1.27 1.54 2.0 1.37 2.5 0. 72 0.99 3.0 0.81 1.12 6.0 0.76 0.86 Table X(b) This Work 1.36 Comparison of Graphite Solubility Values for Pure Iron with Published Data Gurry* 950 1. 32 1.37 1000 1.51 1.53 1050 1.65 1. 69 36 37 . F ray & Ch ~pman Ban-Ya et al.+13 1. 37 1. 5 + o. 02 1.56 1. 71 * By interpolation and extrapolation of experimental data at 957° and 1104°C of 1.39 and 1.86% resp. + Obtained by solving equation 3 at temperature and a =1.0. c 68 C. Solidus Tempe~ature Determination The results oe solidus temperature determination are presented in Table XI Table XI Solidus Temperatures for a 90% Copper Alloy Activity of Carbon a c D. Temperature oc (:t 0.00 1095 0.04 1093 0.08 1091 0.12 1089 0,19 1088 1.00 1078 20) Rate of Carburization Table XII gives the time required to attain equilibrium for some iron-copper alloys for gas carburization at an activity of carbon of 0.08. These values were obtained from weight gain profiles in gas carburization experiments. Table XII Times to Attain Equilibrium Carbon Content During Gas Carburization Alloy Content % Cu Time to Attain equilibrium, in hrs. 0.0 7.25 0.3 4.50 0.7 4.00 1.0 3.25 1.3 1.50 69 E. Activity Coefficients for Carbon The standard state in these calculations was chosen as graphite. The activity coefficient was defined as f Table XIII (a) c ~a c /(%C). Activity Coefficients of Carbon at 950 for :Pure Iron Table XIII(b) Wt. % Carbon Log f c 0.17 -0.347 0.27 -0.337 0.40 ~0.398 0.55 -0.283 0.67 -0.260 o. 76 -0.247 1. 07 -0.196 1.18 -0.174 1. 37 -0.137 Activity Coefficients of Carbon at 950°C for a 0.3% Cu Alloy Wt. % Carbon Log f c 0.26 -0.206 0.48 -0.159 0.66 -0.173 0.90 -0.167 0.96 -0.144 0 c, 70 Table XIII(c) Activity Coe~ficients £or Carbon at 950°C for a 0.7% Cu Alloy Wt. % Carbon Log f c 0.21 -0.090 0.41 -0.136 0.56 -0.148 0.87 -0.155 0.96 -0.148
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