US2019536A - Process and apparatus for producing finely divided lead and lead compounds - Google Patents

Process and apparatus for producing finely divided lead and lead compounds Download PDF

Info

Publication number
US2019536A
US2019536A US691680A US69168033A US2019536A US 2019536 A US2019536 A US 2019536A US 691680 A US691680 A US 691680A US 69168033 A US69168033 A US 69168033A US 2019536 A US2019536 A US 2019536A
Authority
US
United States
Prior art keywords
lead
chamber
atomizing
finely divided
oxide
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US691680A
Inventor
Kemp Paul
Feuer Emanuel
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Application granted granted Critical
Publication of US2019536A publication Critical patent/US2019536A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/02Making metallic powder or suspensions thereof using physical processes
    • B22F9/06Making metallic powder or suspensions thereof using physical processes starting from liquid material
    • B22F9/08Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying
    • B22F9/082Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying atomising using a fluid
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G21/00Compounds of lead
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G21/00Compounds of lead
    • C01G21/02Oxides
    • C01G21/06Lead monoxide (PbO)

Definitions

  • a further vadvantage of our method is attained by using heating gases which neither react with nor oxidize the lead in the atomizing chamber.
  • the heat of reaction of the burning lead may be used, for example, to heat a container for lead which is to be added to the melt, this container being arranged in the chamber in which 0 the atomized lead is burnt and such additional lead may flow directly to the atomizing chamber.
  • the atomization of the lead may beV effected in any suitable manner, for example by providing on the inner wall of the rotating tube devices which elevate and drop the iiuid lead during rotation. Acceleration of atomization may be achieved by permitting thel descending lead to impact on conical or otherwise suitably formed ribbed surfaces secured to a rapidly rotating shaft within the drum. By proper angular co- Il hurled against the outlet end of the Finely divided lead compounds have heretofore been produced by converting the fluid lead into the vapor stage and then condensing it.
  • the accompanying drawing is a vertical crosssection of an apparatus suitable for the practiceof our method.
  • I denotes a coke burning furnace provided with a grate 2 supporting a charge of coke.3.
  • the heating gases from the furnace I pass into the atomizing chamber 4, which is constructed as a rotating tube, and these gases maintain the temperature in the chamber 4 at the value necessary for atomization.
  • the lead which is raised during rotation by suitable means (not shown) drops onto a plurality of conical surfaces 5 which are secured to a rapidly rotating shaft (not shown) thus atomizing the lead.
  • the dimensions of the oxidizing chamber are preferably such that the speed of the stream of gas issuing out of the atomizing chamber is reduced to such an extent that the lead dust precipitates in the oxidizing chamber.
  • a container 8 for example of cast iron, wherein the lead which is introduced through the openings I0 and II is melted by the heat present in the combustion chamber, whereupon the iiuid lead passes through the overflow tube 9 into-the atomizing chamber.
  • the gases are drawn by a suction device (not shown) through the conduit I2 into a purifying installation.
  • a suction device not shown
  • the base of the combustion chamber 'I we may provide steel balls or the like for the purpose of so comminuting any lumps of oxide of lead which may form in the course of oxidizing the lead, that the balls, acting somewhat like a ball mill, make further grinding superuous.
  • the resulting oxide of lead is discharged through closable openings I3.
  • nely divided lead oxide which comprises melting lead and atomizing the molten lead in a rotary furnace, the steps which consist in maintaining the temperature of the molten lead ready for atomization solely by means of heat of heating gases acting directly on the lead, atomizing the molten lead in one chamber and thereafter passing over to another chamber, the oxidation of the atomized lead being carried out in said other chamber by means of an oxidizing gas introduced into the same, and the heat produced by the oxidation process of the lead being used for melting a further charge of lead to be atomized.
  • Apparatus for producing lead oxide comprising a rotary atomizing chamber, an oxidation chamber connected therewith and provided with means for comminuting the lead oxide falling down and settling at the bottom of said oxidation chamber, means for producing heating gases admitted into the atomizing chamber, a device for receiving a further charge of lead arranged within the oxidizing chamber and capable of being heated by the heat produced in the combustion of lead to lead oxide.

Description

` .P. KEMP EI'AL v.. u N I FS uw NU I0 WP M10 w03 R09 1 PD A 1 REO O FLS. .D S .t www. ADS RA AEd PLS P 1 Anni. 4 EF DD NI AV I s SD `.E C O R P Nov. 5, 1935.
PAUL-KEMP' Patented Nov. 5, 1935 PROCESS AND APPARATUS FOR. PRODUCING FINELY DIVIDED LEAD AND LEAD COM- POUNDS Paul Kemp, Perchtoldsdorf, and Emanuel Feuer, Liesing, Austria Application September 30, 1933, Serial No. 691,680 In Austria September 7, 1932 3 claims. (c1. 23-146) Our invention relates to an improved method for the prod uctlon of iinely divided lead and lead compounds.
In the production of lead oxide, it is old in the art to atomize lead in externally heated boilers or rotating tubes, provided with suitable centrifugal devices, and to pass gas or vapors which oxidize the lead through such boilers or tubes.
We have succeeded in providing a method for the production of iinely divided lead and lead compounds, particularly oxide of lead, which presents a number of substantial advantages over existing methods.
In the first place, by our method we completely obvlate all external heating and the heat which is necessary to maintain lead atomization in a revolving tube is provided exclusively by heating gases acting directly on the lead. This feature not only greatly simpliiles and reduces the cost of the apparatus but also effects a great economy in fuel as compared with prior art methods.
A further vadvantage of our method is attained by using heating gases which neither react with nor oxidize the lead in the atomizing chamber. By using such non-reacting and non-oxidizing gases, the heat of reaction of the burning lead may be used, for example, to heat a container for lead which is to be added to the melt, this container being arranged in the chamber in which 0 the atomized lead is burnt and such additional lead may flow directly to the atomizing chamber.
By operating as above, where the atomization and oxidation of the lead are effected in separate chambers, uninterrupted and unimpeded production of lead oxide is possible while in prior art methods, in which oxidation occurs in the atomizing chamber itself, ordinarily periodical interruption of operation is necessary because incrustation of oxide of lead, which impedes further atomization, forms on the walls of the apparatus on the lead bath itself`and on the mechanism such as agitators, ribs, etc. which serve for atomizing purposes.
The atomization of the lead may beV effected in any suitable manner, for example by providing on the inner wall of the rotating tube devices which elevate and drop the iiuid lead during rotation. Acceleration of atomization may be achieved by permitting thel descending lead to impact on conical or otherwise suitably formed ribbed surfaces secured to a rapidly rotating shaft within the drum. By proper angular co- Il hurled against the outlet end of the Finely divided lead compounds have heretofore been produced by converting the fluid lead into the vapor stage and then condensing it. 'I'he present method differs from this type of operation primarily in the fact that in our invention the 5 ne division of the lead is eilected without converting it into the vapor stage and the directly acting heating gases perform only the function of maintaining the lead at that temperature which is necessary for atomizing the uid lead. It is obvious that in view of the great difference be'- tween the melting and vaporizing temperatures of the lead, the caloric expenditure in our method is only a fraction of that necessary in the vaporizing method.
The accompanying drawing is a vertical crosssection of an apparatus suitable for the practiceof our method. I denotes a coke burning furnace provided with a grate 2 supporting a charge of coke.3. The heating gases from the furnace I pass into the atomizing chamber 4, which is constructed as a rotating tube, and these gases maintain the temperature in the chamber 4 at the value necessary for atomization. The lead which is raised during rotation by suitable means (not shown) drops onto a plurality of conical surfaces 5 which are secured to a rapidly rotating shaft (not shown) thus atomizing the lead. The atomized lead together with the outiiowing gases and with the air which flows in through the adjustable opening 6, ows in the direction of the arrows into the rotatably arranged furnace chamber 1 in which the combustion of the lead takes place. The dimensions of the oxidizing chamber are preferably such that the speed of the stream of gas issuing out of the atomizing chamber is reduced to such an extent that the lead dust precipitates in the oxidizing chamber. Arranged in the oxidizing chamber 'I is a container 8, for example of cast iron, wherein the lead which is introduced through the openings I0 and II is melted by the heat present in the combustion chamber, whereupon the iiuid lead passes through the overflow tube 9 into-the atomizing chamber. The gases are drawn by a suction device (not shown) through the conduit I2 into a purifying installation. I n the base of the combustion chamber 'I we may provide steel balls or the like for the purpose of so comminuting any lumps of oxide of lead which may form in the course of oxidizing the lead, that the balls, acting somewhat like a ball mill, make further grinding superuous. The resulting oxide of lead is discharged through closable openings I3.
What we claim as new and desire to secure by Letters Patent oi the United States isz- .1. In a method of producing ilnely divided lead oxide which comprises melting lead and atomizing the molten lead in a rotary furnace, the steps which consist in maintaining the temperature of the molten lead ready for atomization solely by means of the heat of heating gases acting directly on the lead, atomizing the molten lead in one chamber and thereafter passing over to another chamber, thel oxidation of the atomized lead being carried out in said other chamber by means of an oxidizing gas introduced into the same.
2. In a method oi' producing nely divided lead oxide, which comprises melting lead and atomizing the molten lead in a rotary furnace, the steps which consist in maintaining the temperature of the molten lead ready for atomization solely by means of heat of heating gases acting directly on the lead, atomizing the molten lead in one chamber and thereafter passing over to another chamber, the oxidation of the atomized lead being carried out in said other chamber by means of an oxidizing gas introduced into the same, and the heat produced by the oxidation process of the lead being used for melting a further charge of lead to be atomized. y
3. Apparatus for producing lead oxide comprising a rotary atomizing chamber, an oxidation chamber connected therewith and provided with means for comminuting the lead oxide falling down and settling at the bottom of said oxidation chamber, means for producing heating gases admitted into the atomizing chamber, a device for receiving a further charge of lead arranged within the oxidizing chamber and capable of being heated by the heat produced in the combustion of lead to lead oxide. f
PAUL KEMP.
EMANUEL FEUER.
US691680A 1932-09-07 1933-09-30 Process and apparatus for producing finely divided lead and lead compounds Expired - Lifetime US2019536A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AT2019536X 1932-09-07

Publications (1)

Publication Number Publication Date
US2019536A true US2019536A (en) 1935-11-05

Family

ID=3689632

Family Applications (1)

Application Number Title Priority Date Filing Date
US691680A Expired - Lifetime US2019536A (en) 1932-09-07 1933-09-30 Process and apparatus for producing finely divided lead and lead compounds

Country Status (1)

Country Link
US (1) US2019536A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2984544A (en) * 1956-04-05 1961-05-16 Comp Generale Electricite Process for the preparation of lead oxide

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2984544A (en) * 1956-04-05 1961-05-16 Comp Generale Electricite Process for the preparation of lead oxide

Similar Documents

Publication Publication Date Title
US3209808A (en) Soaking pit burner or the like
JP2750136B2 (en) Method for melting metal scrap and apparatus for performing the method
US1856679A (en) Apparatus for comminuting metals
US1912621A (en) Method and means for roasting sulphide ores
US2019536A (en) Process and apparatus for producing finely divided lead and lead compounds
US2739878A (en) Vertically extending burner apparatus of the cyclone type
US2673787A (en) Method and apparatus for recovering chemical products from waste materials
US1713543A (en) Furnace for melting metals
US1923866A (en) Sulphur bearing ore furnace
US1977117A (en) Process for the separate recovery of volatile metals, nonmetals, or volatile or gaseous metallic or nonmetallic compounds
US2070235A (en) Production of sulphur dioxide
US2822245A (en) Process for manufacturing sulfur dioxide by burning sulfur
US1768465A (en) Process of treating fuller s earth and the like
AT144565B (en) Process for the production of finely divided lead and lead oxide.
US2065218A (en) Manufacture of metallic fume
US2191712A (en) Furnace for burning fuel consisting of combustible and incombustible materials
US2282370A (en) Incinerator
US1372392A (en) Revolving furnace
US949474A (en) Process of refining iron.
US2269355A (en) Manufacturing of zinc oxide
US1833386A (en) Smelting apparatus
US2640532A (en) Reaction furnace and evaporator
US1357494A (en) Forced rotary-draft furnace
US1747740A (en) Ore-reduction furnace
US2025799A (en) Apparatus for roasting fines