Document 5koy1njMLymrx2wwRy0YeN1d0

Vn ACONDA Lk AI) Pu()l)IK'TS COMPANY km from KAST Cl llOAUO. IN1) 1 ANA September 28th, 1933 Mr. Frederic1: Luist, Vice-President, Anaconda Lead Products Company, Room 1720 - 25 Broadway, iiew York, IT. Dear Mr. Laist:- I am enclosing a description of a "Process for the Manufacture of Easic Culrhst.e Pigment" with attached memorandum by Mr. Bowman which outlines the process we are now using for the production of basic lead sulphate for.use in the manufacture of leaded zinc oxide at East Chicago. This information has been prepared for use by the patent attorneys in preparing an application for a patent on the process. The inventor of the process is Mr. Stephen ", Stockdale and the patent, if obtained, should be assigned to the Anaconda Lead Products Company. It is our understanding that it is doubtful whether a patent will be granted on this process; how ever we desire to have the application made in order to prevent anyone else from obtaining a patent on the particular features which we have found necessary to produce a satisfactory product. GSJ'3 ends. Superintendent. ANACONDA LEAD PRODUCTS COMPANY EAST CHICAGO, INDIANA MEMORANDUM TO; Kr. G. S. Johnson, Superintendent, (Building) SUBJECT: DATE September 17th, 1933 The attached description of a "Process for Manufacture of Basic Sulphate Figment" describes the method of producing Easic Lead Sulphate as developed in the Research Department and now used at the iihite Lead Flant. This description was prepared by Hr. Stockdale to be forwarded to Hr. Lalst for use by the attorneys in preparing an application for patent on the process. The idea and the development were Ur. Stockdale's and application should be filed in his name a3 Inventor. N11463.01 Face; FOB ah j f ac it j r s or EA3ic l ead rjLHiATs f is is it This Invention relates to a process of manufacturing basic lead sulphate pigment from basic lead carbonate by treatment of the latter with sulphuric acid and caustic soda, ar.d particularly concerns itself with the control of various factors 7/hich directly affect the Important physical properties of the product and its worth as a pigment. The following is a clear and exact description of the process together with data showing the influence of various factors effecting the physical properties of the pigment such as will allow others skilled In the art to carry out the same. Basic lead sulphate is an important commodity, and finds many applications in the arts especially as a pigsent, and, as such, it possesses peculiar advantages not common to other pigments, Frevlous ! practice in the manufacture of this plgnent has been to subject lead sulphide or galena concentrates to the action of heat in a suitable furnace wherein the material is sublimed in the presence of oxygen and the resulting product, consisting essentially of lead sulphate, is recovered in settling chambers and bags. A modification of this method, and one which produces a much superior product, is to sublime lead or lead oxide in an atmosphere of sulphur dioxide and oxygen in a furnace of suitable design and recover the product in settling chambers and bags. These" processes are fully described in patents and the technical press, suffice It to say that, -due-to impurities in the raw materials used and the difficulties in controlling furnace conditions, the products made by such processes are not always of uniform composition and will be N11463.02 -2- found to vary somewhat In their physicel properties. Due to these difficulties, a considerable proportion of the product must finally be returned for retreetcent which fact constitutes a major objection to this method of manufacture. From a practical viewpoint, the actual constitution of basic sulphate white lead is immaterial. The quality depends more upon its physical fora than Its chemical composition. A large number cf basic sulphate forrrulees are known, ranging ir. composition from almost FbO, on the one hand, through the so called true basic sulphate, FbSO^'FbO, to normal lead sulphate, FbSG^ , on the other hand. Until further researches have settled the point it cannot be stated whether the various basic sulphates are definite chonicol compounds or solid solutions of two or more constituents. It is probable that the true nature is a solution of FbSG^, in FbO or, what is the same thing, the result of the partial decomposition of FbSO^ according to the equation Fb30 *--> 4 FoUC.'FbO + 30, -*3 and that the constitution of the product depends upon the conditions of the reaction. It is believed that a relationship exists between baslcit and opacity as if a small sphere of FbS04 were covered with a coating of amorphous IbO. The less basic sulphates ere distinctly much whiter in the dry powder but are less opaque in oil. The optimum appears to be at a point about 2FbS04*FbO; on increasing the basicity the product is liable to essume a yellowish cast cf free FbC. The present invention concerns itself with and has for its object a process for making.basic lead sulphate of uniform physical prorerties which ere capable of close control by regulating the conditions under which the same is produced. Kaving nor; described 3 briefly the previous practice cr.d shortcomings of this art, "l will nor describe my own invention the advantages of which "ill be obvious to those familiar with such matters. In order to simplify the disclosure of this invention, one rr-forred application sill be described, but it is understood that the " ' ; ::ay be achieved by certain variations in the conditions without departing from the spirit of the invention or the claims thereto. I start out rith basic carbonate white loci from any source, preferably, but not necessarily, in. the form of a rater pulp of from 15 to 40,1 solids. After .sampling and determining accurately the percentage of solids, I transfer a predetermined volume of this pulp to a treatment tank of suitable size and shape and add sufficient mater to reduce the palp to about 301 collar.. lased upon the amount by dr;.' weight of white lead contained, a calculatedquantity of concentrated sulphuric acid, il.,30 , is added to thepulp and the whole mass agitated by any suitable means to secure good contact of acid and white lead. To assist and speed the reaction the pulp is heated by steam or other means for about 1C hours after which time the following reaction will have taken place 2IbS04'Tb(0H)p + 3 H,,004 -o=> 3K>304 2C02 4H20 or, 1 lb. white lead + .320 lb I'gCC^. --s> 1.172 lb. IbSO^ It is desirable to use a slight excess of acid for two reasons,namely, to insure maximum C0o elimination within a reasonable tine, and to provide an acid solution containing all the iron which may have come into the system from the acid cr from other sources, in a soluble form curable of being -separated from the solids by filtration or decantation. Iron present in the water or acid used, if allowed to precipitate as - 4- ferric hydrate, harmfully affects the color of the final product even though present in minute quantities; by maintaining an acid pulp this precipitation is prevented and a large proportion of the iron may be removed from the -system at this point by separation of solution from solids. For practical purposes it has been found that for every pound of dry basic carbonate contained in the pulp to be treated, C.40 pounds of ICQ/-- H^SC^ is sufficient for these purposes. Upon completion of the sulphating operation, the pulp is ellowed to settle and the clear solution decanted off. The pulp is again thinned with water and the sulphated pulp carefully adjusted to 23-26 percentage solids and again agitated. The temperature of the pulp is then raised to about 62C and a calculated quantity of caustic soda as a 20;j solution is slowly run into the tank. The pulp concentration, temperature, and quantity of caustic soda added at *his point are important factors and each influences the physical character of the product. The following reaction takes place. 3Fb3C. 2ITaCK --= 2FbS0 *IbO Na.SO. K,,0 4 4 24 2 or, 1 lb Th304 .058 lb -TaCi:--^ 0.912 lb. basic sulphate or, 1 lb. white lead .40 lb. acid .103 lb. J'aC-H 5- 1.C7 lb Basic Sulphate For all practical purposes it has been found that from 0.09 to 0.125 pounds IJaOE per pound of dry white lead contained in the starting pulp is sufficient, according to the basicity desired. The pulp is allowed to agitate until 'it becomes just slightly acid to test paper when it is run into another tank, filtered, and washed. The washed filter cake is dried end pulverized ready for use. The product forced by these reactions is capable of considerable variation in its physical character and is dependent upon three important factors, namely the basicity, the temperature of the pulp, and the pulp concentration at the time the caustic soda is added. The control of these variables as specified above comprises part of the tasis for this invention. To illustrate, as examples of the effect cf these variables, the folic-,ring data are tabulated. In order to clarify the comparison and avoid the use of comparative numerical standards, the values are shewn as relative, one to another. For example, under the heading "Effect of Basicity" opposite "Tinting Strength", 1 refers to a higher tinting strength value than 2, 2 higher than 3, 4 being lowest, and so on throughout the table, the object being not to confuse the reader with actual numerical values which themselves require further definition. Effect of Basicity Percentage FbSOa in Product 5?.77-;i 64.6135 63.71-3 73.37;'', Calculated Composition Oil Absorption, Rating * Tinting Strength, Rating Hiding Tower, Rating Color, Rating PbSO.'PbO 41. 1 1 4 1 4FbS0 '3FbO 42 2 2 1 2 5FbS0.*3FbO 34 3 3 2 3' 2PbS0 *FbO 44 4 4 34 Sffect of Pulp Concentration Apparent Density, Rating * Oil Absorption, Rating Tinting Strength, Rating Percentage Solids in Fuln 5Vj 15> 25% 40Ji 1 234 4321 43 21 Effect of Pulp Temperature Tinting Strength, Rating * Brightness, Rating Color, Rating * Rating: 1 Highest, 4 Lowest 30*C~ 4 3 4 Temp e r a t u r e 50"C 75"C 9SbC 13 1 .2 21 2 4 3 It is understood that the above is only one form of the application of this invention. Others are, of course, possible without departing from the scope of the Invention. Sasic carbonate from various sources may be used either in dry or in pulp form, sulphuric acid of satisfactory purity of any source or strength, or other bases such as caustic potash or ammonia may also be used, those specified in the above application being given merely as the preferred use. I am fully aware of the fact that the chemical reactions involved in this process have been well known for a long time. Ko claim is made for them. Vftiat I claim and desire to secure by patent, 13: Claims. The wording of the claims of this specification is left to the discretion of the attorneys but they should specifically include the following: 1. Conversion of basic lead carbonate to normal lead sulphate by treatment of the former with sulphuric acid and the subsequent conversion of the. normal lead sulphate to basic lead sulphate by treatment with caustic soda. 2. The control of the physical properties of the basic lead sulphate by careful control of conditions such as basicity, pulp dilution and pulp temperature. s 9/21/33