A PROCESS FOR CASE HARDENING STEEL

Abstract: A process for case hardening steel is described. A fused bath of inert salt is provided which is comprised of alkali halides, alkali earth halides, or mixtures thereof, and alkali oxides, alkaline earth oxides, alkali carbonates, alkaline earth carbonates, or mixtures thereof. There is added to this fused bath, after suspending the steel therein, urea, dicyano­ diamide, pyrolysis/condensation products of urea or dicyanodiamide, or combinations thereof. This will form active ions containing carbon and/or nitrogen, and either the nitrogen and/or carbon will diffuse into the surface of a steel piece suspended in the bath to form either a nitrided, carbonitrided or carburized case depending upon the temperature of the bath, which is selectively maintained between above 540°C. and about 950°C.

Description: A PROCESS FOR CASE HARDENING STEEL This invention relates to a process for case hardening steel and, particularly, to a process for riitriding, carbonitriding, and carburizing of steel parts. There have been many prior art proposals for the nitriding, carbonitriding, and carburizing of steel parts. These have taken the form of cyanide salt baths, cyanide/cyanate salt baths, gas carburizing, and so forth. Up until now, each of these prior art processes has been performed. independently of the others. For example, the nitriding process has operating conditions and parameters so different from those needed for carburizing that separate processing equipment and chemicals have to be maintained for each process. As a result, the operating conditions for each conventional process are rather inflexible; and can produce only a narrowly defined type of case. Additionally, each of these types of processes has certain serious limitations. The cyanide or cyanide/cyanate processes require baths to be maintained with a relatively high concentration of active ingredients, which is both expensive and presents a toxic material waste problem. - Gas carburizing and carbonitriding require a high investment for equipment, high energy consumption, and a need for precise atmosphere control. Pack carburizing is very dirty, time consuming, and limited in scope. Furthermore, none of these processes are designed to operate in the 600-7600C. (ll00-I4000F.) temperature range. This range could hold great benefits for case hardening. of steel parts in certain applications. According to the present. invention, there is provided a process for forming a hardened case on a ferrous metal, including the steps of providing a fused chemical salt bath consisting essentially of a first material selected from the group consisting of alkali halides, or. alkaline earth halides, or mixtures thereof, and a second material selected from the group consisting of alkali oxides, alkaline earth oxides, alkali carbonates, alkaline earth carbonates, or mixtures thereof; maintaining said fused chemical salt bath at a temperature from about 540 C. to about 9500C.; maintaining said bath free of cyanide and cyanate salts; suspending the metal workpiece in the bath; thereafter adding to said bath a third material or combination of materials selected from the group consisting of urea, dicyanodiamide, any of the pyrolysis/condensation products of urea or dicyanodiamide, or combinations thereof; at a rate which will not produce cyanide or cyanate salts, whereby to form in situ active case-producing ingredients to thereby produce a case on said workpiece; removing said workpiece; and thereafter maintaining said bath free of cyanide and cyanate salts such that only the first and second materials remain. DESCRIPTION OF THE DRAWING The single figure is a graphical representation of the optimum rates of addition of urea to the fused bath as a function of temperature and size of the load being treated. The graph is intended as a rough guideline for most low carbon, low alloy steel treatment. According to the present invention, a method and composition are provided which allow one to selectively nitride, carbonitride, or carburize a steel workpiece to provide the desired case thereon. The method employs a fused, nonactive chemical salt bath to which is added an organic material which will form certain carbon and nitrogen compounds, said compounds having the ability to add carbon, nitrogen, or both to a steel surface immersed in the bath. As used herein, nonactive bath means a bath which itself neither generates nor contains "active" compounds. "Active" compounds are those which, upon giving up carbon and/or nitrogen to the steel to form a case thereon, are transformed into nonactive compounds. The characteristics of the case on the steel will depend primarily on the temperature of the bath and the rate at which organic materials presented to the bath, so that either a nitrided, carbonitrided, or carburized case may selectively be obtained. A nitrided case is defined herein to mean a case comprised essentially of iron and nitrogen, usually in the form of iron nitrides. A carburized case is defined to -mean a case comprised essentially of iron and carbon, and a- carbonitrided case is defined as one which contains iron with significant amounts of both carbon and nitrogen. The organic material usually is added only so long as there is work in the bath to be treated. After the treatment is finished, the addition of material may be ceased. The result is that carbon and nitrogen-containing compounds are no longer generated, and residual active compounds are slowly destroyed by thermal decomposition, or by reaction with the walls of a metallic salt pot if such type of pot is used. Hence, the bath when not in use becomes nonactive. Thus, there is no need to maintain a high concentration of toxic materials such as cyanides and cyanates. Turning now more specifically to compositions of the materials involved in this invention, the nonactive chemical salt bath may be any fused alkali halide or alkaline earth halide, or combination of such halides, with from about 1 to about 20 weight percent added thereto of an alkali oxide or alkaline earth oxide or carbonate, or mixtures of such carbonates and oxides. A preferable composition is from 64-68 weight percent calcium chloride, ' Cacti2; 30-32 weight percent sodium chloride, Nazi; and 1-5 weight percent calcium carbonate, CaCO3. The melting point of this composition is about 5100C. (9500F.). The organic material for addition to the bath may be urea or dicyanodiamide. It may also be any of the pyrolysis/condensation products of urea or dicyanodiamide, such as melamine, melem, melam, and melon. It may also be ' any combination of the aforesaid organic materials. In operation, the nonactive bath is first brought to the desired operating temperature, chosen from within the range of about 5400C. (10000F.) to about 9500C. (17500F.). The selection of the temperature will be discussed presently. The organic material is then added to the bath, preferably slowly, continuously, and at 9 constant rate. Somewhat complicated reactions now occur, which may be summarized as follows: Organic material + Oxide (62) and/or carbonate EMI5.1 Cyanamide (CN2 ) + nonactive compounds The amount of cyanamide formed is limited by the initial concentration of oxide/carbonate. Thus, if the initial oxide/carbonate amount was 3 weight percent, the maximum amount of cyanamide that can form in the bath is also 3 weight percent. Excess organic material is thermally decomposed and is lost. The workpieces to be treated may be immersed in the salt bath either before or after addition of organic material has begun. The pieces should be clean and dry. The pieces are maintained in the bath for virtually any amount of time, depending upon the case thickness required. The general reaction at a steel surface in the bath is as follows: cyanamide ions + iron surface coordination/ decomposition + trace oxygen and/or carbon dioxide oxide (O 2) and/or carbonate (CO -2) ions + carbon (C) and/or nitrogen ( N ) for diffusion into steel. Thus, it can be seen that the nonactive oxides and carbonates, consumed in the generation of active cyanamide ions, are regenerated when the cyanamide decomposes at the steel surface, and hence no waste product salts build up in the bath to interfere in the process. Agitation of the bath during operation is desirable, in order that active compounds may be evenly dispersed to the entire load. Agitation is usually accomplished by means of either a stirring mechanism, or by bubbling a gas such as air or nitrogen through the bath. Repeated analysis of the bath during the process of this invention while the organic material is being added has shown that no alkali and/or alkaline earth metal cyanide and/or alkali and/or alkaline earth metal cyanate salts are products produced, and in fact no cyanides or cyanates are produced. Thus, the bath is free of alkali and/or alkaline earth metal cyanide or alkali and/or alkaline earth metal cyanate salts, and in fact all cyanides and cyanates before the process, during the process, and after the process is completed. The optimum rates of addition of urea for temperatures between 5900C. (11000F.) and 9500C. (17500F.) are shown in graphic form in the figure. As can be seen in the figure, the size of the load being treated has been divided somewhat arbitrarily into three categories; light loads (2 square inches of load surface area per lb. of salt); medium loads (5 sq. inches of surface area of load per ib. of salt); and heavy loads (8 sq. inches of surface area of load per lb. of salt). The rates of addition for each type of load are graphed as the addition rate in % per hour based on bath weight as a function of temperature and varies from about 0.2% to about 4%. Of course, different load surface areas can be extrapolated from those graphed. As noted, the addition rates are based on urea being added, but slight experimentation will determine the optimum rate for other materials. When the desired immersion time is up, the workpieces are withdrawn from the bath and then either slow cooled or quenched in an appropriate quenching medium, again depending upon the case characteristics desired. The addition of organic material, having been continued during the immersion of the pieces, may now be ceased. If desired, organic material addition may be terminated before the pieces are withdrawn, to allow the residual active compounds and the thermal diffusion effects to complete the case formation. One great advantage inherent in this invention is the variety of possible case types, arising from the flexibility of operating conditions. The type of case formed on the steel is primarily dependent upon the temperature at which the bath is maintained, the type of quench applied, and the composition of the base steel. In general, for low carbon low alloy steels, the case formed at or below 590or. (11O00F.) is essentially a nitride case, i.e., a case containing essentially iron and nitrogen. The outermost portion of the case usually consists of iron nitrides E FeN, E Fe3N, and/or y1Fe4N. Below the nitrides, a zone of nitrogen dissolved in alpha iron usually exists. As the treatment temperature rises 0 0 above 590 C. (1100 F.-), the case will contain progressively more carbon and less nitrogen. Hence, the temperature range of about 5900C. (11000F.) to about 8150C. (15000F.) is' termed the "carbonitriding" range. In general, within these operating temperatures the case is formed in conjunction with a fast quench, such as with water or oil. The case formed is primarily martensitic or bainitic, because addition of nitrogen to the iron at these temperatures has stabilized gamma iron, into which carbon may readily dissolve. Because the core material is still below its critical transformation temperature, the fast quench forms martensitic/bainitic structures only in the region of the case; the core material is essentially unaffected. If desired, a high organic material feed rate will produce a case type consisting of an outer layer of essentially iron nitride, under which exists an austenitic or pearlitic zone. From operating temperatures of about 8150C. (15000F.) to about 9500C. (17500F. ), the case consists of essentially iron and carbon; this is the "carburized" case. Again, this case is usually fast quenched to produce a martensitic or bainitic structure. Of course, if there are different alloying elements present, there will be somewhat more complex cases formed, but there will be essentially those general types described, modified by the alloying elements and the modifications of certain of the critical temperatures as is well known in the art. Thus, it will be seen that all of these different case types can be formed in a single fused salt bath using a single organic addition agent which generates active C and N compounds as needed. The cases are varied by merely changing the operating temperature, the quench conditions, and/or the organic feed rate. It should be understood that while this invention has been described with respect to particular embodiments thereof, numerous others will become obvious to those of ordinary skill in the art in light thereof.

Claims: CLAIMS: 1. A process for forming a hardened case on a ferrous metal, including the step of disposing the ferrous 'metal in a chemical salt bath, characterized by the steps of providing a fused chemical salt bath consisting essentially of a first material selected from the group consisting of alkali halides, or alkaline earth halides, or mixtures thereof, and a second material selected from the group consisting of alkali oxides, alkaline earth oxides, alkali carbonates, alkaline earth carbonates, or mixtures thereof; maintaining said fused chemical salt bath at a temperature from about 540 C. to about 9500C.; maintaining said bath free of cyanide and cyanate salts; suspending the metal workpiece in said bath; thereafter adding to said bath . a third material or combination of materials selected from the group consisting of urea, dicyanodiamide, any of the pyrolysis/condensation products' of urea or dicyanodiamide, or combinations thereof; at a rate which will not produce cyanide or cyanate salts, whereby to form in situ active case-producing ingredients to thereby produce a case on said workpiece; , removing said workpiece; and thereafter maintaining said bath free of cyanide and cyanate salts, such that only the first and second materials remain. 2. A process according to Claim 1, characterized in that the temperature of the bath is maintained between about 0 0 540 C. and about 590 C. to form an essentially nitride case. 3. A process according to Claim 1, characterized in that the tempe"rature of the bath is maintained between about 5900C. and about 8150C. to form a carbonitride case. 4. A process according to Claim 1, characterized in that the temperature of the bath is maintained between about 8150C. and about 9500C. to form an essentially carburized case. 5. A process according to any one of the preceding claims, characterized in that the first material is a mixture of CaC12 and NaC1, and wherein said second material is CaCO3. 6. A process according to Claim 5, characterized in that said first material includes about 64-68 percent by weight CaC12, about 30-32 percent by weight NaC1, and wherein said second material includes about 1-5 percent by weight CaCO3. 7. A process according to any one of the preceding claims, characterized in that the third material is urea. 8. A process according to any one of Claims 1-6, characterized in that the third material is dicyanodiamide. 9. A process according to any one of Claims 1-6, characterized in that the third material is a pyrolysis/condensation product of dicyanodiamide. 10. A process according to Claim 7, characterized in that the rate of addition of urea is from about 0.1 to about 4 percent by weight of the bath per hour of addition time. 11. A process according to Claim 7, characterized in that the rate of addition of urea is controlled as a function of temperature and load size as depicted in the graph of the drawing

Inventors: JAKUBOWSKI, THOMAS MICHAEL, WOOD, WILLIAM GEORGE
Applicants: KOLENE CORPORATION
Application year: 1981
Main classification: C23C8
IPC codes: C23C8