‘W. R. KELLY. TREATMENT OF METALS. APPLIOATION FILED JULY '27, 1908. .l 1,019,965, - . Patented Mar. 12, 1912; g ¢ . , ' . ' fyrd ‘ Jaye/afar UNITED STATES PATENT OFFICE. WILLIAM H. KELLY, 0F LOS 'ANGELES, CALIFORNIA. TREATMENT OF METALS. 1,019,965. Speci?cation of Letters Yatent. Patented Mar. 12, 1912. Application ?led July 27, 1908.‘ Serial No. 445,566. To all whom 'it may concern: posed to treat molten metals by the use of Be it known that I, WILLIAM H. KELLY, a superheated steam to remove impurities citizen of the United States, residing at Los therefrom, and I do not desire to be consid Angeles, in the county of Los Angeles and ered as including in this application any -. State _of California, have invented a new 60 such treatment broadly, but on the contrary ~ and useful Improvement in the Treatment desire to be understood as claiming only the of Metals, of which the following is a speci means and method of treating molten metals ?cation. 10 15 20 ' In my application Serial No. 448,971, ?led August 17, 1908, I disclosea process for the reduction of ores and metals by subjecting them to the action of superheated and partly dissociated steam in and during the reduc ing operation. The present invention is dis tinguished therefrom in that the treatment with'part-ly dissociated steam is applied to the metals subsequently to the'reducing op eration, the process herein described being a purifying and not a reducing process. One object of my invention is to provide . cheap and e?'ect-ive means for removing im by the use of nascent hydrogen and oxygen when generated and applied substantially in the manner herein speci?ed. 65 .By my process and apparatusherein set forth, I am enabled to generate nascent hy drogen and oxygen in suitable quantities and, in such a manner as to treat metals while in their molten condition at a slight cost and at the same time avoid any liability of dan ger from explosions, which are liable to oc- ' our when steam. is admitted to the molten metal and dissociated by its contact therewith into hydrogen and oxygen. 75 - The accompanying drawings illustrate purities from metals when the metals are the means and process of carrying out my drawn from the cupola furnace, blast furnace invention. or any melting furnace used for reducing Figure 1 illustrates the means and manner 80 25 metals to a molten condition. of working my invention. Fig. 2 is a detail Another object of 'my invention is to sub of the nozzle and section of the ?exible metal ject molten metals to the action of nascent tube. employed in delivering the hot gases to hydrogen gas to effect their puri?cation the metal. 30 from sulfur, phosphorus and like impurities at a slight cost. ' . 1 is a steam boiler, which. may be of any approved form adapted to generate vapor from water in suitable quantities. 85 Another object of my invention is to pro .vide a process whereby nascent hydrogen gas .2 is a retort, or gasi?er arranged to_ re— and nascent oxygen can be applied to molten ceive steam from the boiler'l. metals to effect the puri?cation of the same,‘ 3 is a pipe connecting the boiler 1 and the 35 in a manner which, while being cheap and inexpensive, will be without danger to the at‘ is a valve in the pipe line 3 arranged to operator. > I regulate the amount of steam admitted to retort In carrying out my invention I'generate nascent hydrogen‘and oxygen in‘ a suitably 40 heated retort from water steam admitted 2. ' . ‘ I - theretort 2. - ‘ ‘ 5 is a, pipe leading from the‘ retort to the stand pipe 6 and coupling 7 to which is con thereto from a suitable steam generator hav nected a suitably insulated ?exible metal ' ing a greater pressure than the pressure of tube v8. the hydrogen and oxygen generated in the At the open end of the metal tube 8 is at :45 retort, and I also provide means 'torallow of tached a nozzle 9 of some suitable ‘refrac 100 the‘ unobstructed ?ow of the hydrogen and tory material.' I have used for this pur-_ oxygen from such retort to the metals to be pose an iron pipe coated with lime. . treated. ' 10, is a wheeled truck or carrier upon The essential feature of the present proc which is carried a pot 11 adapted to contain ess is the treatment of molten metal with a molten metal 12. 13 is a union coupling con 105 gas derived from steam, said steam having sisting of a screw threaded male member 14 been heated to such a temperature as to adapted to screw into an internally screw . _ reach the point- of dissociation, the dissocia tion being started before the gas enters the 1 55 threaded female member 15. . The nozzle 9 is formed of some suitable re~ furnace or metal and being completed as the fractory material of any desired length and 110 gas comes in contact with the heated'metal. is provided with. tapering end 16 which I am aware that it has heretofore beenpro seats in the nozzle socket 17*’ in the union 1,019,965 2 coupling 13. The open end 18 of thenozzle of its uninterrupted egress therefrom, that is provided with slots or notches 19 to allow the hydrogen and oxygen become thoroughly the nascent hydrogen and oxygen to ?ow ?xed at low. pressure, and by providing free from the nozzle in case the end of the nozzle egress from the retort no back pressure re should come in contact with the bottom of the metal receptacle in the treatment. The metal hose 8 is covered with an in sulating covering 20 of asbestos or magnesia sults on the steam which is being fed into the retort from the steam generator, there fore by maintaining a constant pressure upon the boiler a certain and predetermined tov prevent loss of heat. quantity of hydrogen and oxygen is pro duced in the retort. It is to be remembered 75 that in all instances the retort or gasi?er to the retort 2 through thevalve controlled shall be of suitable heating area to allow for pipe 3 in such quantities as may be desired, the perfect dissociation of the steam. sufficient heat being applied to the retort 2' By using my treatment for the puri?ca— to cause the steam to begin to dissociate into tion of metals, molten metals may be run 80 nascent hydrogen and oxygen. The valve 4 into suitable ladles or containers and al is designed to admit a smaller amount of lowed to cool to an appreciable extent, and steam to the pipe 3 than the full capacity of become lower in temperature than the highly the retort 2,__and in consequence thereof the heated. hydrogen and oxygen generated by steam expands to a greater volume in the the retort, and when such partially‘cooled 85 retort and dissociates into nascent hydrogen metals aresubjected to the action of the and oxygen at a low pressure. By thus pro gases the temperature of such metals will be viding'a retort of larger capacity than the increased to a pointabovethat of which it ‘ In practice steam is generated in the boiler 1 in the ordinary manner .and is admitted 15 20 25 30 valve controlled opening thereinto the hy was when it was drawn from the furnace; drogen and oxygen are produced in theirv nascent condition practically without pres sure. The steam containing nascent hydro gen and oxygen thus ?ows fromrthe retort This feature is most valuable when it is de-_ What I claim is :—'~ 1 I'prefer to employ as the?exible metal 100 containing nascent oxygen and hydro en. 7 ‘ ,2. The herein described process 0 treat~ I‘ metal hose constructedof steel or copper and ing molten metal which consists in introduc provide the same with a coating of insulat ing into the mass of metal superheated steam mg ‘material such as asbestos in order to containing nascent oxygen and maintain the gases at the temperature at. under comparatively low pressure. which they are emitted from the retort, for 95 . plete agitation of the metal in order that all l. The herein described process of treat portions of the same may be brought into, ing molten metal which consists in introduc intimate‘ contact with the" nascent gases. ing into themass ‘of metal superheated steam .tube 8,.the ordinary commercially known 40 them to be poured at the same time, for the through the pipe 5, stand pipe 6,,coupling reason that such ladles can all be subjected 7, ?exible tube 8 and nozzle 9 into themeta-l to slmultaneous treatment, purifying them‘ 12 contained in the pot 11, the nozzle mean to a uniform degree and also giving to each while being stirred about by the operator‘ ladle of metal the temperature desired. ' throughout the mass to allow of the com 35 sired to make large ‘castings and it'becomes necessary to ‘tap a number of ladles and hold _ hydrogen 105 3. The herein described process of treat ing molten metal which consists in introduc~ ing into the mass of metalv superheated steam affinity for'carbon, sulfur, phosphorus and containing nascent oxygen and hydrogen at the reason that I have discovered that nas 45 cent hydrogen and oxygen have a greater 110 the like when heated ‘to a high'degree of a temperature substantially the same as the temperature, and combine with the same temperature of the metal. ‘ 1 and carry them off in gases and slags that “4:. The herein described process of treat 50 ?oat on the surface of the metal much more. ing molten metal whichconsists in introduc 115 quickly than when combined'at a low degree ing into the massof metal at different points superheated steam containing nascent oxy In carrying out my invention the nascent gen and hydrogen and thereby causing the hydrogen and oxygen liberated from theirv oxygen and hydrogen to thoroughly agitate of temperature. ' > v ' , 55 combination in water of vapor form are, of the mass and to be commingled therewith. I20 such a temperature as to equal or nearly 5. The herein described process of treat “equal that of the molten metal, ‘and upon ing molten metal which consists in subject- ' 60 their coming into contact therewith, com—' ing steam to ajtemperature above the point bine with the impuritiescausingthem to vof dissociation into nascent oxygen and hy either oxidize or escape in the form of. gases. drogen and then introducing the same into 125 In practice I have found that’? by admit a mass of molten metal and commingling it ting only such amount of steamtothehi' hly heated retort, as shown, as :is required in 6. The herein described process of_ treat~ the treatment of the metal cont‘ainedit‘qinthe ing molten metal which consists in generat pot, ladle or other containerzandiiyallowing ing steam, passing the same into a heating 130 therewith. 65 ' - 1,019,965 3 . ' apparatus and increasing its temperature to ing steam, passing‘the same into a heating ~ and above the point of dissociation of said apparatus in a limited predetermined quan—. steam into nascent oxygen , and hydrogen tity, ‘and with comparatively no pressure, and then introducing said oxygen and hy-_ then heating said steam to a point above dis sociation and permitting the same to expand drogen into'the mass of metal. 7. The‘ herein described process of treat and therebyforming ?xed nascent oxygen ing molten metal Which vconsists in generat ing steam, passing the same in a predeter ' mined amount into a heating apparatus and 10 i and hydrogen gases, and then introducing said gases into themolten m'ass?of material at substantially no pressure. In testimony whereof, I have hereunto set increasing its temperature to a point above thedissociation of the steam into nascent my hand at Los Angeles, California, this . oxygen and hydrogen and then introducing 21st day of July 1908'. said oxygen and hydrogen into the mass of metaland thoroughly commingling the same I 15 therewith. < 8. The herein described process of treat ing molten metalwhich consists in generat .W. H. KELLY. In presence of; LOUIS W. GRATZ, FRANK L. A. GRAHAM. , , ) I 25~
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