Abstract:
An electromagnetic steel sheet has an electrically insulating coating with superior weldability, formed by coating a treatment solution on the electromagnetic steel sheet and baking the same, the treatment solution containing a synthetic resin fine-particle emulsion having resistance against chromic and/or bichromic acid and exhibiting a peak temperature not lower than 400° C. at which a weight change rate is maximized when a sample is heated at a constant rate in differential thermal gravimetry, a chromate and/or bichromate base aqueous solution containing at least one kind of two-valence metal, and an organic reducer. The steel sheet is superior in electrical insulation, adhesion, punching ability, weldability and corrosion resistance.

Description:
FIELD OF THE INVENTION 
     The present invention relates to an electromagnetic steel sheet having an electrically insulating coating primarily consisting of a chromate and/or bichromate and an organic resin, and method of manufacture. A core formed by laminating pieces punched out from the steel sheet exhibits superior weldability at its end faces. 
     DESCRIPTION OF THE RELATED ART 
     There are various characteristics required for insulating coatings of electromagnetic steel sheets, such as electrical insulation, adhesion, punching ability, weldability, and corrosion resistance. To meet those requirements, a variety of studies have been conducted and many techniques have been proposed in relation to methods of forming insulating coatings on surfaces of electromagnetic steel sheets and compositions of the insulating coatings. 
     In particular, a laminated or composite coating consisting of a chromate and/or bichromate and an organic resin is becoming more widely utilized because it can remarkably improve the punching ability of steel sheets as compared with the phosphate and chromate and/or bichromate base inorganic coatings conventionally employed. 
     For example, Japanese Patent Publication No. 60-36476 discloses a method of forming insulating coatings on electromagnetic steel sheets in which a treatment solution is prepared by mixing a bichromate and/or bichromate base aqueous solution containing at least one kind of two-valence metal with, with respect to 100 weight parts of CrO 3  in the aqueous solution, 5 to 120 weight parts of a resin emulsion in terms of resin solid, as an organic resin, the resin having a vinyl acetate / VEOVE (Vinyl Ester of Versatic Acid) ratio of 90/10 to 40/60, and 10 to 60 weight parts of an organic reducer, the prepared treatment solution is coated on surfaces of a base iron sheet, and the resultant coating is subject to baking in a normal manner. 
     Also, Japanese Patent Laid-Open No. 62-100561 discloses a method of forming an insulating coating on electromagnetic steel sheets in which a resin mixture solution is prepared by mixing an aqueous emulsion of pH 2 to 8 in which an organic substance base coating forming resin consisting of either one or both of acrylic resin and acrylic--styrene resin is emulsified and dispersed, with an aqueous dispersant of pH 6 to 8 in which acrylonitrile resin is dispersed, but an emulsifying dispersant is not substantially present, such that a nonvolatile component of the latter is present in an amount of 10 to 90 weight % with respect to the total amount of nonvolatile components of both the former and the latter, the prepared resin mixture solution is added and mixed with an aqueous solution of an inorganic substance base coating forming material containing a chromate and/or bichromate as a third ingredient such that a nonvolatile component of the resin mixture solution is present in an amount of 15 to 120 weight parts with respect to 100 weight parts of the chromate and/or bichromate in the aqueous solution in terms of CRO 3 , and a resultant electromagnetic steel sheet insulating coating forming composition is coated on an electromagnetic steel sheet and then heated at temperatures of 300° C. to 500° C. to form an insulating coating at a density in the range of 0.4 to 2.0 g/m 2 . 
     As the organic resin to be mixed with the chromate and/or bichromate chemical in the above methods, thermoplastic resins such as vinyl acetate resin, VEOVE (Vinyl Ester of Versatic Acid) resin, acrylic resin, polystyrene resin, acrylonitrile resin, polyester resin, and polyethylene resin have been used so far. These thermoplastic resins have the disadvantage of deteriorating corrosion resistance, because they start a pyrolysis reaction at relatively low temperatures in the baking step and decomposed gas produces a number of voids in the electrically insulating coating. 
     The above problem could be solved by utilizing organic thermosetting resins which have a cross-linked structure and start a pyrolysis reaction at high temperatures. However, since most thermosetting resins, not cross-linked, contain many reaction groups such as hydroxyl groups and epoxy groups, there would occur a reaction when mixed with the chromate and/or bichromate chemical, resulting in gelation. This would give rise to a serious problem from the viewpoint of industrial application since stability of the coating solution would deteriorate during storage prior to forming the electrically insulating coating. Furthermore, using a resin which has been subject to thermosetting beforehand has not been put into practice because of difficulty in dispersing such a resin as fine particles in an aqueous medium. 
     SUMMARY OF THE INVENTION 
     We have now found a thermosetting resin which does not gel when mixed with chromate and/or bichromate base chemical, and have accomplished the present invention which overcomes the foregoing problems. 
     More specifically, the present invention provides an electromagnetic steel sheet having an electrically insulating coating with superior weldability, wherein the electrically insulating coating is formed by coating a treatment solution on surfaces of the electromagnetic steel sheet and baking the same, the treatment solution containing a synthetic resin fine-particle emulsion having resistance against chromic and/or bichromic acid and exhibiting a peak temperature not lower than 400° C. at which a weight change rate is maximized when a sample is heated at a constant rising speed in differential thermal gravimetry, a chromate and/or bichromate base aqueous solution containing at least one kind of two-valence metal, and an organic reducer. 
     The synthetic resin fine-particle emulsion preferably contains at least a thermosetting synthetic resin capable of forming a cross-linked structure. 
     The synthetic resin fine-particle emulsion having resistance against chromic and/or bichromic acid preferably comprises thermosetting synthetic resin particles having outer layers formed by coating a synthetic resin having resistance against chromic and/or bichromic acid. 
     The thermosetting synthetic resin capable of forming a cross-linked structure is preferably an epoxy resin. 
     The synthetic resin having resistance against chromic and/or bichromic acid is preferably a polymer formed by emulsion-polymerizing ethylenically unsaturated carboxylic acid and an ethylenically unsaturated monomer which can copolymerize with the ethylenically unsaturated carboxylic acid. 
     The electrically insulating coating is preferably deposited in amount of 0.2 to 4.0 g/m 2  per unit area of the base iron sheet. 
     The treatment solution used in the present invention contains: 
     (a) aqueous emulsion of resin fine particles, 
     (b) chromate and/or bichromate base aqueous solution containing at least one kind of two-valence metal, and 
     (c) organic reducer. 
     Specific compositions of these three components are as follows. The component (a) is added to the component (b) such that, with respect to 100 weight parts of CrO 3  in the chromate and/or bichromate chemical, the former is preferably present in an amount of about 5 to 120 weight parts, more preferably about 20 to 80 weight parts in terms of resin solid in the emulsion. The amount of the component (c) added is preferably about 10 to 60 weight parts, more preferably about 20 to 50 weight parts, with respect to 100 weight parts of CrO 3  in the chromate and/or bichromate chemical. 
     The present invention is featured in a resin making up fine particles in the aqueous emulsion of the component (a). The resin used has resistance against chromic and/or bichromic acid and exhibits a maximum peak temperature not lower than about 400° C., preferably not lower than about 410° C., for a weight change rate when a sample is heated at a constant rate in differential thermal gravimetry. 
     Herein, the expression maximum peak temperature for a weight change rate in differential thermal gravimetry (DTG) means a temperature at which the weight change rate dG/dt (G is the sample weight and t is time) is maximized when a sample is heated in an inert atmosphere at a constant rate, e.g., 20° C. per minute. The amount by which the sample weight is reduced with respect to temperature is measured. Thermochemical behavior of materials is measured using thermal gravimetry (TG), differential thermal gravimetry (DTG), differential thermal analysis (DTA), etc. Thermochemical properties of the resin used in the present invention can be evaluated with the maximum peak temperature as a parameter. The maximum peak temperature can be determined by using a commercially available measuring apparatus for differential thermal analysis and thermal gravimetry, e.g., Model SSC/560GH manufactured by Daini Seiko-sha Co., Ltd., picking up a sample of about 10 mg, raising its temperature from 30° C. to 550° C. at a heat rate of 20° C./minute, and reading the resultant DTG graph. 
     While any kind of such resins can be used, the resin preferably contains a thermosetting synthetic resin capable of forming a cross-linked structure and has resistance against reaction with chromic and/or bichromic acid. 
     The resin used may comprise fine particles in one uniform layer or fine particles in a multi-layered structure. 
     In the case of a multi-layered structure, at least the resin making up one layer may exhibit a maximum peak temperature not lower than about 400° C. for a weight change rate when a sample is heated at a constant rising speed in differential thermal gravimetry, and at least the resin making up the other layer may have resistance against reaction with chromic and/or bichromic acid. 
     Pyrolysis of resins can be controlled by generating a cross-linked structure in fine particles. Accordingly, such control is achieved by employing a thermosetting resin. However, since most of the thermosetting resins which are able to form a cross-linked structure contain many functional groups such as hydroxyl groups and epoxy groups which are not cross-linked, those resins are inferior in resistance against chromic and/or bichromic acid and tend to easily gel with chromic and/or bichromic acid. This problem can be avoided by providing resin layers which have resistance against reaction with chromic and/or bichromic acid, on those surfaces of the fine particles which come into contact with chromic and/or bichromic acid. 
     Such a resin fine particle preferably comprises an inner layer (core) formed of a thermosetting resin capable of forming a cross-linked structure and an outer layer (shell) formed of a thermosetting resin having resistance against reaction with chromic and/or bichromic acid. 
     More specifically, examples of the thermosetting resin forming the inner layer (core) are phenol resin (such as phenol/formaldehyde resin, xylenol/formaldehyde resin, cresol/formaldehyde resin, and resorcinol/formaldehyde resin), epoxy resin (such as bisphenol type epoxy resin, alicyclic epoxy resin, Novolac type epoxy resin, aliphatic epoxy resin, and epoxidated urethane resin), furfural resin, urethane resin, unsaturated polyester resin, amino resin, polyimide resin, and polyamideimide resin. Other resins can also be employed so long as they can form a cross-linked structure. 
     It is essential that the core-coating resin having resistance against chromic and/or bichromic acid unifies with the thermosetting resin of the core to form an emulsion. This requirement is satisfied by a resin formed of ethylenically unsaturated carboxylic acid and a monomer which can copolymerize with the former. 
     Examples of the ethylenically unsaturated carboxylic acid employed herein are ethylenically unsaturated mono-basic carboxylic acids such as acrylic acid, methacrylic acid and crotonic acid, and ethylenically unsaturated dibasic carboxylic acids such as itaconic acid, maleic acid and fumaric acid. Further, examples of the ethylenically unsaturated monomer are alkyl esters of acrylic acid or methacrylic acid, such as (meth-)acrylic methyl, (meth-)acrylic ethyl, (meth-)acrylic n-butyl, (meth-)acrylic isobutyl, and (meth-)acrylic 2-ethylhexyl, and other monomers having ethylenically unsaturated bonds which can copolymerize with any of the above examples, such as styrene, a-methylstyrene, vinyl toluene, t-butylstyrene, ethylene, propylene, vinyl acetate, vinyl chloride, vinyl propionate, acrylonitrile, methacrylonitrile, (meth-)acrylic dimethylaminoethyl, vinyl pyridine, and acrylamide. Two or more kinds of those monomers may be used. 
     The resin fine particles described above have no limitations in diameter, but the mean particle diameter is preferably in the range of about 0.03 to 0.3 μm. 
     If the mean particle diameter is greater than 0.3 μm, three-dimensional roughness of the coating would be increased to further improve weldability, but the area occupation rate is reduced. Therefore, such a mean particle diameter is not preferable as an insulating coating for general purposes. 
     On the other hand, if the mean particle diameter is lower than about 0.03 μm, the resin surface area would be increased and a large amount of surfactant would have to be used to ensure stability in chromic and/or bichromic acid. This is unfavorable because of reducing weldability. 
     A preferable method of manufacturing the aqueous emulsion of core/shell type resin fine particles used in the present invention will be described below in detail. 
     Emulsion polymerization is a multi-stage process comprising at least two stages; i.e., first-stage emulsion polymerization for forming core resin particles, and second-stage emulsion polymerization for forming a coating of a shell copolymer on surfaces of the core resin particles. In the first-stage emulsion polymerization, cores are first formed. More specifically, a thermosetting resin used as fine particles making up the cores can easily be prepared by dissolving a water-insoluble thermosetting resin in an ethylenically unsaturated monomer used for emulsion polymerization, and subjecting them to emulsion polymerization in a known manner. Alternatively, such a thermosetting resin can be prepared by adding and dispersing a water-insoluble thermosetting resin in the water phase which contains an emulsifier, and subjecting it to emulsion polymerization while adding an ethylenically unsaturated monomer. The water-insoluble thermosetting resin may be any selected from among commercially available resins such as phenol resin, epoxy resin, furfural resin, urethane resin, unsaturated polyester resin, amino resin, polyimide resin, and polyimideamide resin, which is insoluble or nearly insoluble in water. 
     In the second-stage emulsion polymerization, shells coating the cores are formed. To provide the resin particles with a two-layered structure, in the second-stage emulsion polymerization, no emulsifier is newly added, or an emulsifier is added, if so, in such a small amount as not to form new resin particles, so that the polymerization substantially progresses on the surfaces of the resin particles formed in the first-stage emulsion polymerization. It is essential that the shells formed in the second-stage emulsion polymerization are hydrophilic. Therefore, the ethylenically unsaturated monomer containing an amino group is suitably used as the ethylenically unsaturated monomer, and preferable examples are N-methylaminoethyl acrylate or methacrylate, monopyridines such as vinyl pyridine, vinyl ethers having alkyl amino groups, such as dimethylaminoethyl vinyl ether, and unsaturated amides having alkyl amino groups, such as N-(2-dimethylaminoethyl) acrylic amide or methacrylic amide. The ethylenically unsaturated monomer containing an amino group may be employed as a single polymer, but it is most advantageous to use the monomer as a copolymer with another ethylenically unsaturated monomer. 
     In the second-stage emulsion polymerization, ethylenically unsaturated carboxylic acid may be used as part of the ethylenically unsaturated monomer. 
     Specifically, examples of the ethylenically unsaturated carboxylic acid are ethylenically unsaturated mono-basic carboxylic acids such as acrylic acid, methacrylic acid and crotonic acid, and ethylenically unsaturated bi-basic carboxylic acids such as itaconic acid, maleic acid or fumaric acid. One or two or more of these examples may be employed. 
     The emulsion polymer prepared in the first stage is added to a water phase and is subjected to emulsion polymerization in a known manner while similarly adding a mixture of ethylenically unsaturated monomers and a radical generation initiator, whereby the aqueous emulsion of resin fine particles according to the present invention is formed. An emulsifier may be added to prevent generation of agglomerates and to ensure stability of the polymerization reaction. The emulsifier used in the present invention may be of the type typically used in normal emulsion polymerization, for example, an anionic emulsifier such as sodium alkylbenzene sulfonate or a non-ionic emulsifier such as polyoxyethylene alkyl ether. 
     The radical generation initiator used in the emulsion polymerization reaction may be selected from potassium persulfate, ammonium persulfate, azobisisobutyronitrile, etc. The concentration during the emulsion polymerization is generally preferably selected so that the resin in the final aqueous emulsion has a solids content of about 25 to 65 weight %. Further, the temperature during the emulsion polymerization reaction may be in the normal range where well-known processes are practiced, and emulsion polymerization is usually carried out under normal pressure. 
     The mixing rate of the core thermosetting resin to the shell resin having resistance against chromic and/or bichromic acid, both the resins making up the aqueous emulsion of resin fine particles, is preferably selected such that the resin having resistance against chromic and/or bichromic acid is present in an amount of about 2 to 100 weight parts with respect to 100 weight parts of the thermosetting resin. Specifically, if the mixing percentage of the resin having resistance against chromic and/or bichromic acid is not greater than about 2 weight parts, the core thermosetting resin could not be completely coated and hence would be subjected to gelling when mixed with the chromate and/or bichromate base chemical. On the other hand, if the mixing percentage of the resin having resistance against chromic and/or bichromic acid is not less than about 100 weight parts, resistance against pyrolysis may not be improved. 
     The component (b) of the treatment solution used in the present invention is preferably a chromate and/or bichromate base aqueous solution containing at least one kind of two-valence metal. Thus, it is an aqueous solution using at least one of chromic and/or bichromic anhydride, chromate and/or bichromate, and bichromate and/or bichromate as a main ingredient. 
     Examples of the chromates and/or bichromates which can be used are salts of sodium, potassium, magnesium, calcium, manganese, molybdenum, zinc, aluminum, etc. 
     As the two-valence metal to be dissolved, oxides such as MgO, CaO and ZnO, hydroxides such as Mg(OH) 2 , Ca(OH) 2  and Zn(OH) 2 , as well as carbonates such as MgCO 3 , CaCO 3  and ZnCO 3  can be used. 
     The desired chromate and/or bichromate base aqueous solution is prepared by dissolving at least one of chromic and/or bichromic anhydride, chromate and/or bichromate, and bichromate and/or bichromate, as a main ingredient, in an aqueous solution. 
     The treatment solution further contains, as the component (c), an organic reducer for making the coating insoluble. The organic reducer is preferably any of polyhydric alcohols such as glycerin, ethyl glycol, and cane sugar (sucrose), i.e., a reducer suitable for 6-valent chromium. The amount of organic reducer added is preferably about 10 to 60 weight parts with respect to 100 weight parts of CrO 3 , but is not particularly limited. 
     If the mixing percentage of the organic reducer is less than about 10 weight parts, water resistance of the coating would tend to be deteriorated. On the other hand, if it is greater than about 60 weight parts, a reducing reaction would tend to take place in the treatment solution, resulting in gelation of the treatment solution. 
     In addition a borate, a phosphate or the like may be added to further increase the heat resistance of the coating. Further, colloidal materials such as colloidal silica or inorganic fine particles such as silica powder may be added to improve interlayer resistance after annealing for removal of distortions. 
     The electromagnetic steel sheet of the present invention is manufactured as follows. 
     The treatment solution having the above-described compositions is continuously coated over surfaces of the electromagnetic steel sheet by using a roll coater or the like, and is then baked to solidify in a short period of time at temperatures of a drying furnace atmosphere ranging from 300° to 700° C. As a result, an objectively satisfactory electrically insulating coating is formed. The amount of coating deposited after baking is about 0.2 to 4 g/m 2 , preferably about 0.3 to 3 g/m 2 . If the amount is less than about 0.2 g/m 2 , a coverage rate of the insulating coating would be reduced, and if it exceeds about 4 g/m 2 , adhesion of the insulating coating would tend to deteriorate. 
     It has been confirmed that the insulating coating thus obtained is not only superior in weldability, but also quite satisfactory in other various characteristics required for insulating coating, such as adhesion, electrical insulation, corrosion resistance, heat resistance, and resistance against pharmaceuticals. 
    
    
     DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS 
     The present invention will hereinafter be described in more detail in conjunction with embodiments or examples. But it is to be noted that the present invention is not limited to the examples below. 
     The resin emulsion (El) for use in the present invention was manufactured by using the following materials and method. The following materials were put into and dissolved in a reaction container having a volume of 1.5 L and equipped with an agitator, a circulating condenser, and a dipping funnel: 
     
         ______________________________________deionized water            3240 partsEmulgen 931                10.0 parts(nonioic emulsifier by Kao Co., Ltd.)Neogen R                   4.0 parts(anioic emulsifier by Dai-ichi Kogyo Seiyaku Co.,Ltd.)______________________________________ 
    
     Then, the following mixture was put into the dipping funnel for the first-stage emulsion polymerization: 
     
         ______________________________________bisphenol type epoxy resin                   100 partsbutyl acrylate          200 partsmethyl methacrylate     100 partsacrylic acid            8.0 parts______________________________________ 
    
     The temperature in the reaction container was raised to 60° C. under agitation while introducing nitrogen gas, and 40 parts of a 2% aqueous solution of potassium persulfate dissolved in deionized water was added thereto. After that, 20% of the epoxy resin and the monomer mixture of butyl acrylate, methyl methacrylate and acrylic acid, all put in the dipping funnel, was added thereto. A temperature rise due to the polymerization heat was controlled by a water bath to keep the temperature in the reaction container at 80° C. Then, the remainder of the epoxy resin and the monomer mixture and 80 parts of a 2% aqueous solution of potassium persulfate were dipped over 2 hours for progress of the polymerization. After holding the reaction container at 80° C. for another 2 hours, the content was cooled down to room temperature and then filtered with a 200-mesh filtering cloth to obtain an emulsified polymer as seed or core particles. The nonvolatile component of this polymer had a content of 50.3 wt % and a pH of 2.8. 
     452 parts of the emulsified polymer obtained above and 125 parts of water were put in a similar reaction container having a volume of 1.5 L. Then, the following mixture of ethylenically unsaturated monomers was prepared and put into a dipping funnel for the second-stage emulsion polymerization: 
     
         ______________________________________ethyl acrylate            60 partsmethyl methacrylate       30 partsdimethylaminoethyl methacrylate                    2.0 partsacrylic acid             1.0 part______________________________________ 
    
     The temperature in the reaction container was raised to 70° C. under agitation while introducing nitrogen gas, and 60 parts of a 2% aqueous solution of potassium persulfate put into another dipping funnel, and the above monomer mixture was dipped for polymerization. This dipping was conducted over 2 hours while keeping the temperature in the reaction container at 70° C. After holding the reaction container at 70° C. for another 2 hours, the content was cooled down to room temperature and then filtered with a 200-mesh filtering cloth to obtain a polymer emulsion for use in the present invention. The resin solid in the resultant polymer emulsion had a content of 48 wt %. 
     The resin emulsion (E2) for use in the present invention was manufactured by using the following materials and method. 
     The following mixture was employed for the first-stage emulsion polymerization: 
     
         ______________________________________bisphenol type epoxy resin              100 partsethyl acrylate     300 partsmethyl methacrylate              100 partsmethacrylic acid    8.0 parts______________________________________ 
    
     The following mixture was employed for the second-stage emulsion polymerization: 
     
         ______________________________________ethyl acrylate    50 partsmethyl methacrylate             30 partsacrylic acid     2.0 partsbuthyl acrylate  2.0 parts______________________________________ 
    
     The other part of the method was the same as in the above example. The resin solid in the resultant polymer emulsion had a content of 52 wt %. 
     The resin emulsion (E3) for use in the present invention was manufactured by using the following materials and method. 
     The method was the same as in the above first example except for using the following mixture for the first-stage emulsion polymerization: 
     
         ______________________________________resol type phenol formaldehyde resin                  100 partsethyl acrylate         200 partsmethyl methacrylate    100 partsmethacrylic acid        8.0 parts______________________________________ 
    
     The resin emulsion (E4) for use in the present invention was manufactured by using the following materials and method. 
     The following mixture was employed for the second-stage emulsion polymerization. The resin solid in the resultant polymer emulsion had a content of 46 wt %. 
     
         ______________________________________ethyl acrylate          50 partsmethyl methacrylate     30 partsvinyl pyridine         1.0 partacrylic acid           1.0 part______________________________________ 
    
     The other part of the method was the same as in the above first example. 
     The resin emulsion (E5) for use in the present invention was manufactured by using the following materials and method. 
     The following mixture was employed for the second-stage emulsion polymerization. The resin solid in the resultant polymer emulsion had a content of 46 wt %. 
     
         ______________________________________ethyl acrylate          50 partsmethyl methacrylate     30 partsacrylic amide          1.0 partacrylic acid           1.0 part______________________________________ 
    
     The other part of the method was the same as in the above first example. 
     The treatment solutions consisted of various components shown in Table 1. They were each coated over surfaces of an electromagnetic steel sheet 0.5 mm thick, and then baked for 80 seconds at 450° C. in a hot air furnace to form an insulating coating on the steel sheet surfaces. 
     In the examples, the coating operation and stability of the treatment solutions over time were very satisfactory, and uniform coatings were obtained in amounts deposited, as shown in Table 2. In some of the comparative examples, however, the resin emulsions in the coating solutions gelled so as to prevent painting on the coatings. 
     Subsequently, sheet pieces each being 30 mm wide, 130 long and 0.5 mm thick were blanked out by a shearing machine from the resultant electromagnetic steel sheet having the insulating coating with the rolling direction facing transversely. The sheet pieces were laminated and clamped under a clamping pressure of 100 kg/cm. The resultant laminate was subject as its laminated section to TIG welding under conditions of 120 A current and Ar shield gas (flow rate of 6 l/min). During the welding, generation of blow holes was checked and the maximum welding speed free from blow holes was measured in unit of cm/min. The measured result was shown in Table 2 along with other characteristics of the coating. Measuring methods and determination criteria for those characteristics are as follows. 
     (1) Interlayer resistance 
     Interlayer resistance was measured in accordance with JIS, second method. The greater the interlayer resistance value, the better the electrical insulation. 
     (2) Adhesion 
     before annealing: the sheet was bent to measure the diameter (cm) at which the coating does not peel off. 
     after annealing: tape peeling of the coating was observed for the flat sheet. 
     The less peeling, the better the adhesion. 
     (3) Corrosion resistance 
     A salt water spray test was conducted and the rusting rate on the surface after 7 hours was measured in units of %. The smaller the rusting rate, the better the corrosion resistance. 
     (4) Coolant resistance 
     The sheet was left in a mixture of Freon 22: refrigerator oil=9:1 for 10 days at 80° C., and the amount of weight reduced was measured. 
     The smaller the weight reduction, the better the coolant resistance. 
     (5) Oil resistance 
     The sheet was immersed in No. 1 insulating oil for 72 hours at 120° C., and the amount of weight reduced was measured. 
     The smaller the weight reduction, the better the oil resistance. 
     (6) Punching ability 
     The number of repeated punching steps until the burr height reached 50 μm was measured by using a steel die of 15 mmu. 
     The larger the number of punching times until the burr height reached 50 μm, the better the punching ability. 
     (7) Heat resistance 
     A sample was heated in an inert atmosphere at a rate of 20° C. per minute in differential thermal gravimetry, and the amount of sample weight reduced was measured with respect to temperature to determine the peak temperature at which a weight change rate dG/dt was maximized. The higher the maximum peak temperature, the better the heat resistance. 
     Resins used in the comparative examples were as follows. 
     R1: bisphenol type epoxy resin aqueous emulsion (content of solid resin; 40 wt %) 
     R2: vinyl acetate resin aqueous emulsion (content of solid resin; 45 wt %) 
     R3: resol type phenol resin aqueous emulsion (content of solid resin; 53 wt %) 
     R4: polyester resin aqueous emulsion (content of solid resin; 55 wt %) 
     R5: acrylic resin aqueous emulsion (content of solid resin; 47 wt %) 
      copolymer of 50 weight parts of methyl acrylate and 30 weight parts of butyl acrylate 
     R6: styrene resin aqueous emulsion (content of solid resin; 46 wt %) 
     As described above, the present invention provides an electromagnetic steel sheet having an electrically insulating coating which is formed by coating a treatment solution on surfaces of the steel sheet and baking, the treatment solution being composed of a particular resin fine-particle emulsion, a chromate and/or bichromate base aqueous solution, and an organic reducer. The steel sheet is superior in electrical insulation, adhesion, punching ability and corrosion resistance, and a core formed by laminating pieces punched out from the steel sheet exhibits superior weldability at its end faces. 
     
                                           TABLE 1__________________________________________________________________________(weight parts)    EXAMPLE 1       EXAMPLE 2 EXAMPLE 3   EXAMPLE 4__________________________________________________________________________TYPE OF  E 1             E 1       E 1         E 2EMULSIONAMOUNT OF    25              10        80          40EMULSIONADDED*TYPE AND CHROMIC ANHYDRIDE: 30                    CALCIUM   CHROMIC     CHROMICAMOUNT OF    MAGNESIA: 7     BICHROMATE: 30                              ANHYDRIDE: 30                                          ANHYDRIDE: 30CHROMATE WATER: 100      WATER: 100                              ZINC HYDROXIDE: 7                                          MAGNESIUMADDED                              WATER: 100  CARBONATE: 16                                          WATER: 100TYPE AND ETHYLENE GLYCOL: 10                    GLYCERIN: 20                              SUCROSE: 60 ETHYLENEAMOUNT OF                                      GLYCOL: 30REDUCERADDED**TYPE AND COLLOIDAL SILICA: 15                    BORIC ACID: 10                              CALCIUM     COLLOIDALAMOUNT OF                          PHOSPHATE: 20                                          SILICA: 15ASSISTANT***__________________________________________________________________________(weight parts)    EXAMPLE 5       EXAMPLE 6        EXAMPLE 7__________________________________________________________________________TYPE OF  E 3             E 4              E 5EMULSIONAMOUNT OF    25              30               25EMULSIONADDED*TYPE AND CHROMIC ANHYDRIDE: 30                    CHROMATE ANHYDRIDE: 30                                     CHROMATEAMOUNT OF    CALCIUM OXIDE: 12                    ZINC OXIDE: 7    ANHYDRIDE: 30CHROMATE WATER: 100      MAGNESIA: 10     MAGNESIA: 7ADDED                    WATER: 100       WATER: 100TYPE AND ETHYLENE GLYCOL: 50                    ETHYLENE GLYCOL: 10                                     ETHYLENE GLYCOL: 10AMOUNT OFREDUCERADDED**TYPE AND COLLOIDAL ALUMINUM: 15                    ZIRCONIA SOL: 15 COLLOIDAL SILICA: 15AMOUNT OFASSISTANT***__________________________________________________________________________ *AMOUNT IN TERMS OF RESIN SOLID WEIGHT PARTS OF CHROMIC ANHYDRIDE **AMOUNT WITH RESPECT TO 100 WEIGHT PARTS OF CHROMIC ANHYRIDE ***AMOUNT IN TERMS OF SOLID WITH RESPECT TO 100 WEIGHT PARTS OF CHROMIC ANHYRIDE 
    
     
                                           TABLE 2__________________________________________________________________________         EXAMPLE 1                EXAMPLE 2                       EXAMPLE 3                              EXAMPLE 4                                     EXAMPLE 5                                            EXAMPLE                                                   EXAMPLE__________________________________________________________________________                                                   7STABILITY OF  GOOD   GOOD   GOOD   GOOD   GOOD   GOOD   GOODCOATING SOLUTIONAMOUNT OF COATING         0.9    1.0    0.6    0.8    1.2    3.0    0.3DEPOSITED (g/m.sup.2)INTERLAYERRESISTANCE (Ω-cm.sup.2 /sec)BEFORE ANNEALING         36     42     23     27     21     OVER 200                                                   16AFTER ANNEALING         5.9    6.4    3.8    5.1    6.2    8.7    2.8ADHESION (cm)BEFORE ANNEALING         10     10     10     15     10     20     10BENTAFTER ANNEALING         NO     NO     NO     NO     NO     NO     NOFLAT          PEELING                PEELING                       PEELING                              PEELING                                     PEELING                                            PEELING                                                   PEELINGCORROSION     LESS THAN                LESS THAN                       LESS THAN                              LESS THAN                                     LESS THAN                                            LESS THAN                                                   LESS THANRESISTANCE RUSTING         20     20     15     20     20     5      20RATE (%)WELDABILITY (cm/min)         60     60     50     60     60     40     120MAX-SPEED FREEFROM BLOW HOLESPUNCHING ABILITY         OVER 150                OVER 150                       100    OVER 150                                     OVER 150                                            OVER 150                                                   80(MILLION TIMES)COOLANT RESISTANCE         ALMOST ALMOST ALMOST ALMOST ALMOST ALMOST ALMOSTWEIGHT CHANGE NONE   NONE   NONE   NONE   NONE   NONE   NONEOIL RESISTANCE         ALMOST ALMOST ALMOST ALMOST ALMOST ALMOST ALMOSTWEIGHT CHANGE NONE   NONE   NONE   NONE   NONE   NONE   NONEPYROLYSIS TEMPERA-         423    423    423    438    416    412    420TURE PEAKTEMPERATURE (°C.)__________________________________________________________________________ 
    
     
                                           TABLE 3__________________________________________________________________________(weight parts)         COMPARATIVE       COMPARATIVE     COMPARATIVE         EXAMPLE 1         EXAMPLE 2       EXAMPLE__________________________________________________________________________                                           3TYPE OF EMULSION         R 1               R 2             R 3AMOUNT OF EMULSION         20                25              20ADDED*TYPE AND AMOUNT OF         MAGNESIUM BICHROMATE: 30                           CALCIUM BICHROMATE: 30                                           MAGNESIUMCHROMATE ADDED         WATER: 100        WATER: 100      BICHROMATE: 30                                           WATER: 100TYPE AND AMOUNT OF         SUCROSE: 15       GLYCERIN: 10    GLYCERIN: 8REDUCER ADDED**TYPE AND AMOUNT OF         COLLOIDAL SILICA: 20                           BORIC ACID: 15  COLLOIDALASSISTANT***                                    ALUMINUM:__________________________________________________________________________                                           25(weight parts)         COMPARATIVE     COMPARATIVE     COMPARATIVE         EXAMPLE 4       EXAMPLE 5       EXAMPLE 6__________________________________________________________________________TYPE OF EMULSION         R 4             R 5             R 6AMOUNT OF EMULSION         30              15              27ADDED*TYPE AND AMOUNT OF         CHROMIC ANHYDRIDE: 30                         CALCIUM BICHROMATE: 30                                         CHROMIC ANHYDRIDE: 30CHROMATE ADDED         MAGNESIA: 7     WATER: 100      ZINC OXIDE: 15         WATER: 100                      WATER: 100TYPE AND AMOUNT OF         SUCROSE: 10     ETHYLENE GLYCOL: 55                                         GLYCERIN: 20REDUCER ADDED**TYPE AND AMOUNT OF         ZIRCONIA SOL: 18                         BORIC ACID: 12  CALCIUM PHOSPHATE: 20ASSISTANT***__________________________________________________________________________ *AMOUNT IN TERMS OF RESIN SOLID WEIGHT PARTS OF CHROMIC ANHYDRIDE **AMOUNT WITH RESPECT TO 100 WEIGHT PARTS OF CHROMIC ANHYRIDE ***AMOUNT IN TERMS OF SOLID WITH RESPECT TO 100 WEIGHT PARTS OF CHROMIC ANHYRIDE 
    
     
                                           TABLE 4__________________________________________________________________________            COMPARA- COMPARA-                            COMPARA- COMPARA-                                            COMPARA-                                                   COMPARA-            TIVE     TIVE   TIVE     TIVE   TIVE   TIVE            EXAMPLE 1                     EXAMPLE 2                            EXAMPLE 3                                     EXAMPLE 4                                            EXAMPLE                                                   EXAMPLE__________________________________________________________________________                                                   6STABILITY OF COATING            X (GELATION)                     ◯                            X (GELATION)                                     ◯                                            ◯                                                   ◯SOLUTIONAMOUNT OF COATING            SOUND    1.1    SOUND    0.9    2.2    0.6DEPOSITED (g/m.sup.2)            COATING         COATINGINTERLAYER RESISTANCE            NOT             NOT(Ω-cm.sup.2 /sec)            PRODUCED        PRODUCEDBEFORE ANNEALING          21              16     27     8AFTER ANNEALING           1.8             1.6    2.9    5.7ADHESION (cm)BEFORE ANNEALING BENT     10              10     20     10AFTER ANNEALING FLAT      NO              NO     NO     NO                     PEELING         PEELING                                            PEELING                                                   PEELINGCORROSION RESISTANCE      40              30     10     20RUSTING RATE (%)WELDABILITY (cm/min)      40              30     10     40MAX-SPEED FREE FROMBLOW HOLESPUNCHING ABILITY          &gt;150            &gt;150   &gt;150   100(MILLION TIMES)COOLANT RESISTANCE        ALMOST          A LITTLE                                            ALMOST ALMOSTWEIGHT CHANGE             NONE                   NONE   NONEOIL RESISTANCE WEIGHT     ALMOST          A LITTLE                                            ALMOST ALMOSTCHANGE                    NONE                   NONE   NONEPYROLYSIS TEMPERATURE     360             345    390    395PEAK TEMPERATURE (°C.)__________________________________________________________________________