US1907331A - Apparatus for hardening metals - Google Patents

Apparatus for hardening metals Download PDF

Info

Publication number
US1907331A
US1907331A US527894A US52789431A US1907331A US 1907331 A US1907331 A US 1907331A US 527894 A US527894 A US 527894A US 52789431 A US52789431 A US 52789431A US 1907331 A US1907331 A US 1907331A
Authority
US
United States
Prior art keywords
box
dissociator
nitrogen
furnace
gases
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
US527894A
Inventor
Frank A Milliff
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
Priority to US527894A priority Critical patent/US1907331A/en
Application granted granted Critical
Publication of US1907331A publication Critical patent/US1907331A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C8/00Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C8/06Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases
    • C23C8/08Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases only one element being applied
    • C23C8/24Nitriding
    • C23C8/26Nitriding of ferrous surfaces
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C8/00Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C8/06Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases

Definitions

  • FIG. 1 A first figure.
  • FRANK A MILLI ATTORNEY Patented May 2, 1933 PATENT. OFFICE FRANK A. mmrrr, or nos ANGELES, CALIFORNIA APPARATUS FOR HARDENING METALS Application filed April 6,- 1931. Serial No. 527,894.
  • This invention relates to improvements in' apparatus for hardening metals.
  • the principal object of the invention is to,
  • Another object is to regenerate and conserve the active gases incidental to the-practice of the invention.
  • Another object is to reduce the applied temperature and the time period in the practice of this art.
  • Another object is to so treat the metal and applied gas that the afiinity between them will be increased.
  • a further object is to standardize and control the depth of penetration and reaction in the hardened case.
  • the invention consists in means for heating. the metal in evacuated receptacles and: introducing nascent nitrogen or other active chemicals to the, receptacle 1 at pressure below atmospheric.
  • the boiling point of steel is lowered under vacuum and the nitriding of the case therefore can be accomplished at much lower tem- I peratures than are possible under plus pressures, as heretofore practiced.
  • the application of pressure below atmospheric decreases surface tension, grain growth and distortion and increases the available interstices by extracting the occluded gases.
  • the cooling period is decreased about one-third, by excluding atmospherlc air from mace and p p to the for g g a check the box.
  • Fig. 1 is a diagrammatic front elevation of a hardening apparatus built in accordance with this invention.
  • r Fig. 2 is a horizontal section from above of the same on the line II-II, Fig. 1.
  • naces have the floor 1, side walls 2-3, top 4 and two ends 5-6.
  • the whole interior is lined with refractory material and a suitable door 1 is provided for charging and discharging the furnace.
  • the heat is applied to the interior of the furnace in any conventional manner such as the burner 1".
  • This method is equally applicable to electric furnaces surrounding the nitriding receptacle or box adapted to be evacuated or subjected to pressure below atmospheric.
  • the average temperature for the treatment of steel and nitridable alloys is 900 to 1500 F.
  • the equipment is in accord with common practice.
  • the closed treating boxes 7 are composed of steel or any suitable material not subject to or effected by the nascent gases used.
  • the boxes are rendered vacuum-tight and must withstand the desired temperatures. They may be made to fill the space available within the furnace or in smaller units connected with intakes and outlets for the internal circulation of the desired gases through the boxes.
  • the gas is introduced at the bottom of the box through the perforated pipe 8 and is withdrawn through the pipe 9 beneath the sealed cover 10.
  • the box is provided with the vacuum gage 11, located outside the furon the conditions of vacuum within the box.
  • the pipe 9 leads outside the furnace to the ed to the vertical tube or. tower 20. Just beneath the apex the transverse bypass tube 21 is inserted between the tubes 1819 to which it is welded.
  • tubes 1819 are filled with a suitable catalyst 22. Copper borings are preferred for anhydrous ammonia.
  • the tower 20 is filled with coarse particles of unglazed porcelain 20 among which the separated hydrogen passes upward, as will be hereinafter more fully described.
  • the dissociator is preferably installed within the furnace and is subjected to the same temperature as the box 7 to facilitate the dissociation of the gases.
  • the anhydrous ammonia in the tank 23 is carried through the valve 24 in the pipe 25 to the inlet 26 of the tube 18.
  • the ammonia passing among the heated copper borings 22 begins a natural separation.
  • the nitrogen being heavier settles out, while the lighter hydro gen rises in the tube 18.
  • the nitrogen crosses through the bypass 21 to the tube 19 where the separation continues and the heavy nascent nitrogen passes out at the bottom of the tube 19 into the pipe 28.
  • the lighter hydrogen from both tubes 1819 rises through a screen or perforations at the bottom of the tower 20 which impedes the possible rise of any associated nitrogen.
  • Within the tower the separation is completed by the porcelain 20, and hydrogen escapes at the top of the tower through the pipe 29 and valve 30 to the top of the suction receiver 12. If the needle valve 30 is slightly opened a very low suction or pressure below atmospheric can be exerted on the top of the tower 20, just enough to withdraw the hydrogen without lifting the nitrogen over.
  • the hydrogen and other gases present in ammonia gas dilute the nitrogen and set up reactions impeding I the pentration of the nitrogen into the texture of the metal, rendered more porous by the applied heat.
  • the dissociator Fig. 3. is under a slight pressure above atmospheric from the drum 23, up to the base of the tower 20. It is obvious that the dissociator eventually reduces the major constituent of the gas in the circulatory system to nascent nitrogen.
  • the interstices in the metal are gradually freed of occluded gases by the heat and re Jerusalem pressure within the box and said gases are replaced by the nascent nitrogen absorbed by the expanded metal and retained as the metal cools.
  • the nascent nitrogen may be separated from the ammonia gas in any other manner, for introduction into the reduced pressure Within the box 7. without departing from the spirit of this invention.
  • the outlet pipe 28 from the dissociator is led outside of the furnace and fitted with the stop valve 31 in the pipe 8 leading to the box 7.
  • the valve 32 permits the attachment of a suitable pipette or suitable instrument through which the gas may be bypassed by means of the valve 32 for the purpose of analysis and check on the flow of nascent nitrogen from the dissociator.
  • thermo-couple 7 in the pipe 9 as shown or elsewhere for measuring the temperature of the interior of the box 7.
  • This invention gives purified hydrogen as a valuable byproduct and stabilized nascent nitrogen applied in a manner to give the maximum nitriding effect on the metal with the utmost in conserving the applied gases.
  • the hydrogen and excess nitrogen are recovered at the exhaust 16.
  • This invention is also applicable in carburizing steel by subjecting it to colloidal carbons under suitable conditions of temperature and pressure below atmospheric in the box 7. It is equally obvious that any heat treated object in the box 7 can be subjected to the absorption of any afiinity gases with improved results under the controlled conditions incidental to the practice of the spirit of this invention, by those skilled in the art.
  • a hardening apparatus including a heating furnace; a sealed box and a dissociator in said furnace; means for passing a gas through said dissociator and box at a. pressure below atmospheric.
  • a hardening apparatus including a heating furnace; a sealed box and dissociator in said furnace; means for passing ammonia gas through said dissociator and withdrawing hydrogen from said dissociator and passing the resulting nascent nitrogen through said box at a pressure below atmospheric.
  • a hardening apparatus including a heating furnace; a sealed box and dissociator in said furnace; means for circulating a nitriding gas through said dissociator and box at pressure below atmospheric and withdrawing hydrogen from said dissociator.
  • a hardening apparatus including a heating furnace; a sealed box and dissociator in said furnace; a receiver; a pump having its suction intake connected with said receiver; a circulatory system including said receiver; box and dissociator, and a gas supply connected with said dis'sociator:
  • a hardening apparatus including a gas dissociator having a catalyst therein and a separation tower thereon; a sealed box communicating with said dissociator; a source of ammonia gas communicating with said dissociator; a suction means connected with said box; and means for heating said box.
  • a hardening apparatus including -a dissociator having an arched tube containing a catalyst and connected with a separator at its high point; a source of ammonia gas discharging into said tube; a sealed box communicating with said tube; means for creating a suction on said box and tower and means for heating said box.
  • a hardening apparatus including a heating furnace; a dissociator; a sealed box in said furnace and connected with the lower portion of said dissociator; means for introducing a gas into said dissociator and means for withdrawing the gas from said box at a pressure below atmospheric.
  • a hardening apparatus including a furnace; a dissociator; a sealed box in said furnace connected with said dissociator; means for introducing a nitriding gas into said dissociator; and means for evacuating said box at a pressure below atmospheric.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Solid-Phase Diffusion Into Metallic Material Surfaces (AREA)

Description

INVENTOR:
FIG. 3.
May 2, 1933.
FIG.
FRANK A. MILLIFF ATTORNEY.
y 2, 1933- F. A. MILLIFF 1,907,331
APPARATUS FOR HARDENING METALS Filed April 6, 1931 2 Sheets-Sheet 2 IN TOR:
FRANK A. MILLI ATTORNEY Patented May 2, 1933 PATENT. OFFICE FRANK A. mmrrr, or nos ANGELES, CALIFORNIA APPARATUS FOR HARDENING METALS Application filed April 6,- 1931. Serial No. 527,894.
This invention relates to improvements in' apparatus for hardening metals.
The principal object of the invention is to,
case harden fabricated metals such as ferrous alloys, v
Another object is to regenerate and conserve the active gases incidental to the-practice of the invention.
Another object is to reduce the applied temperature and the time period in the practice of this art.
Another object is to so treat the metal and applied gas that the afiinity between them will be increased.
A further object is to standardize and control the depth of penetration and reaction in the hardened case.
Other objects and advantages will appear as the description progresses.
Broadly stated, the invention consists in means for heating. the metal in evacuated receptacles and: introducing nascent nitrogen or other active chemicals to the, receptacle 1 at pressure below atmospheric. The boiling point of steel is lowered under vacuum and the nitriding of the case therefore can be accomplished at much lower tem- I peratures than are possible under plus pressures, as heretofore practiced.
The application of pressure below atmospheric decreases surface tension, grain growth and distortion and increases the available interstices by extracting the occluded gases. The cooling period is decreased about one-third, by excluding atmospherlc air from mace and p p to the for g g a check the box.
In this specification and the accompany-- ing drawings the invention is disclosed in its preferred form. It is to be understood, how-' ever, that it is not limited to this form because it may be embodied in other forms within the spirit of the claims following the description.
In the two sheets of drawings:
Fig. 1 is a diagrammatic front elevation of a hardening apparatus built in accordance with this invention.
r Fig. 2 is a horizontal section from above of the same on the line II-II, Fig. 1.
3 is an enlarged detail in vertical sec tion of a gas dissociator.
In detail the construction illustrated in the .drawings comprises the conventional muflie Such furfurnace, referring to Fig. 1. naces have the floor 1, side walls 2-3, top 4 and two ends 5-6. The whole interior is lined with refractory material and a suitable door 1 is provided for charging and discharging the furnace. The heat is applied to the interior of the furnace in any conventional manner such as the burner 1".
This method is equally applicable to electric furnaces surrounding the nitriding receptacle or box adapted to be evacuated or subjected to pressure below atmospheric.
In the present invention the average temperature for the treatment of steel and nitridable alloys is 900 to 1500 F. Thus far the equipment is in accord with common practice.
The closed treating boxes 7 are composed of steel or any suitable material not subject to or effected by the nascent gases used. The boxes are rendered vacuum-tight and must withstand the desired temperatures. They may be made to fill the space available within the furnace or in smaller units connected with intakes and outlets for the internal circulation of the desired gases through the boxes. The gas is introduced at the bottom of the box through the perforated pipe 8 and is withdrawn through the pipe 9 beneath the sealed cover 10. The box is provided with the vacuum gage 11, located outside the furon the conditions of vacuum within the box.
The pipe 9 leads outside the furnace to the ed to the vertical tube or. tower 20. Just beneath the apex the transverse bypass tube 21 is inserted between the tubes 1819 to which it is welded.
These tubes 1819 are filled with a suitable catalyst 22. Copper borings are preferred for anhydrous ammonia. The tower 20 is filled with coarse particles of unglazed porcelain 20 among which the separated hydrogen passes upward, as will be hereinafter more fully described.
The dissociator is preferably installed within the furnace and is subjected to the same temperature as the box 7 to facilitate the dissociation of the gases.
For nitriding steel and ferrous alloys the anhydrous ammonia in the tank 23, is carried through the valve 24 in the pipe 25 to the inlet 26 of the tube 18. The ammonia passing among the heated copper borings 22 begins a natural separation. The nitrogen being heavier settles out, while the lighter hydro gen rises in the tube 18. The nitrogen crosses through the bypass 21 to the tube 19 where the separation continues and the heavy nascent nitrogen passes out at the bottom of the tube 19 into the pipe 28. The lighter hydrogen from both tubes 1819 rises through a screen or perforations at the bottom of the tower 20 which impedes the possible rise of any associated nitrogen. Within the tower the separation is completed by the porcelain 20, and hydrogen escapes at the top of the tower through the pipe 29 and valve 30 to the top of the suction receiver 12. If the needle valve 30 is slightly opened a very low suction or pressure below atmospheric can be exerted on the top of the tower 20, just enough to withdraw the hydrogen without lifting the nitrogen over.
The hydrogen and other gases present in ammonia gas dilute the nitrogen and set up reactions impeding I the pentration of the nitrogen into the texture of the metal, rendered more porous by the applied heat.
The dissociator, Fig. 3. is under a slight pressure above atmospheric from the drum 23, up to the base of the tower 20. It is obvious that the dissociator eventually reduces the major constituent of the gas in the circulatory system to nascent nitrogen.
The interstices in the metal are gradually freed of occluded gases by the heat and re duced pressure within the box and said gases are replaced by the nascent nitrogen absorbed by the expanded metal and retained as the metal cools.
The nascent nitrogen may be separated from the ammonia gas in any other manner, for introduction into the reduced pressure Within the box 7. without departing from the spirit of this invention.
The outlet pipe 28 from the dissociator is led outside of the furnace and fitted with the stop valve 31 in the pipe 8 leading to the box 7. The valve 32 permits the attachment of a suitable pipette or suitable instrument through which the gas may be bypassed by means of the valve 32 for the purpose of analysis and check on the flow of nascent nitrogen from the dissociator.
It is Well to provide for the introduction of a thermo-couple 7 in the pipe 9 as shown or elsewhere for measuring the temperature of the interior of the box 7.
It has been the practice heretofore, so far as I am aware, to circulate the anhydrous ammonia gas through closed boxes, similar to 7, at atmospheric or plus pressure and depend upon the steel objects in the box to select the nitrogen from the combined gases until the nitrided case is formed on the objects. This method is wasteful of the gases, uncertain in ultimate eifect, with hit or miss results in the ultimate product.
There has been a further wasteful use of the valuable gases in passing them through the treating boxes to wash out atmospheric 7 air and occluded gases deleterious to the nitriding process, both before and after the application of heat. Such waste is eliminated in the present invention by the dissociator which very quickly reduces the major constituent of the ammonia gas to nascent nitrogen and maintains this condition during the period of operation. a
In the present instance only nitrogen in the active nascent state is fed to the box 7, which is absorbed by the porous surface of the objects in the box at reduced surface tension until the available interstices of the objects are completely filled by the molecules of nascent nitrogen, under constant check, without dilution and the deleterious reactions in-- cidental to the presence of excess hydrogen and any other gases that may be present in commercial anhydrous ammonia as heretofore used in nitriding steel.
This invention gives purified hydrogen as a valuable byproduct and stabilized nascent nitrogen applied in a manner to give the maximum nitriding effect on the metal with the utmost in conserving the applied gases. The hydrogen and excess nitrogen are recovered at the exhaust 16.
This invention is also applicable in carburizing steel by subjecting it to colloidal carbons under suitable conditions of temperature and pressure below atmospheric in the box 7. It is equally obvious that any heat treated object in the box 7 can be subjected to the absorption of any afiinity gases with improved results under the controlled conditions incidental to the practice of the spirit of this invention, by those skilled in the art.
Having thus described this invention what I claim and desire to cover by Letters Patent is:
1. A hardening apparatus including a heating furnace; a sealed box and a dissociator in said furnace; means for passing a gas through said dissociator and box at a. pressure below atmospheric.
2. A hardening apparatus including a heating furnace; a sealed box and dissociator in said furnace; means for passing ammonia gas through said dissociator and withdrawing hydrogen from said dissociator and passing the resulting nascent nitrogen through said box at a pressure below atmospheric.
3. A hardening apparatus including a heating furnace; a sealed box and dissociator in said furnace; means for circulating a nitriding gas through said dissociator and box at pressure below atmospheric and withdrawing hydrogen from said dissociator.
4. A hardening apparatus including a heating furnace; a sealed box and dissociator in said furnace; a receiver; a pump having its suction intake connected with said receiver; a circulatory system including said receiver; box and dissociator, and a gas supply connected with said dis'sociator:
5. A hardening apparatus including a gas dissociator having a catalyst therein and a separation tower thereon; a sealed box communicating with said dissociator; a source of ammonia gas communicating with said dissociator; a suction means connected with said box; and means for heating said box.
6. A hardening apparatus including -a dissociator having an arched tube containing a catalyst and connected with a separator at its high point; a source of ammonia gas discharging into said tube; a sealed box communicating with said tube; means for creating a suction on said box and tower and means for heating said box.
7. A hardening apparatus including a heating furnace; a dissociator; a sealed box in said furnace and connected with the lower portion of said dissociator; means for introducing a gas into said dissociator and means for withdrawing the gas from said box at a pressure below atmospheric.
8. A hardening apparatus including a furnace; a dissociator; a sealed box in said furnace connected with said dissociator; means for introducing a nitriding gas into said dissociator; and means for evacuating said box at a pressure below atmospheric.
In testimony whereof I have hereunto set my hand this 31st day of March, 1931.
FRANK A. MILLIFF.
US527894A 1931-04-06 1931-04-06 Apparatus for hardening metals Expired - Lifetime US1907331A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US527894A US1907331A (en) 1931-04-06 1931-04-06 Apparatus for hardening metals

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US527894A US1907331A (en) 1931-04-06 1931-04-06 Apparatus for hardening metals

Publications (1)

Publication Number Publication Date
US1907331A true US1907331A (en) 1933-05-02

Family

ID=24103380

Family Applications (1)

Application Number Title Priority Date Filing Date
US527894A Expired - Lifetime US1907331A (en) 1931-04-06 1931-04-06 Apparatus for hardening metals

Country Status (1)

Country Link
US (1) US1907331A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2543708A (en) * 1947-05-29 1951-02-27 Comstock & Wescott Heat-treating furnace
US2630315A (en) * 1946-05-11 1953-03-03 Surface Combustion Corp Combination heat-treating furnace and gas generator
US2880986A (en) * 1954-04-20 1959-04-07 Artemas F Holden Salt bath furnaces
FR2674618A1 (en) * 1991-03-27 1992-10-02 Etudes Const Mecaniques Nitriding method and furnace

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2630315A (en) * 1946-05-11 1953-03-03 Surface Combustion Corp Combination heat-treating furnace and gas generator
US2543708A (en) * 1947-05-29 1951-02-27 Comstock & Wescott Heat-treating furnace
US2880986A (en) * 1954-04-20 1959-04-07 Artemas F Holden Salt bath furnaces
FR2674618A1 (en) * 1991-03-27 1992-10-02 Etudes Const Mecaniques Nitriding method and furnace

Similar Documents

Publication Publication Date Title
US3796615A (en) Method of vacuum carburizing
US4386973A (en) Vacuum carburizing steel
US1907331A (en) Apparatus for hardening metals
US2275106A (en) Circulation of heat treatment atmospheres
US1310724A (en) Sxgfrukd westberg
US2792438A (en) Apparatus for producing titanium metal
US2857155A (en) Apparatus for reducing ores
US2365346A (en) Apparatus for manufacturing metals
US9540721B2 (en) Method of carburizing
US2429584A (en) Method of and apparatus for removing zinc from copper base alloys
US2814561A (en) Process and apparatus for reducing metal chlorides employing calcium carbide
US995476A (en) Electrolytic process.
NO118906B (en)
US2346698A (en) Method of producing protective atmospheres
US2061250A (en) Combination distillation and liquation furnace
US2011288A (en) Method of treating furnace charge
US2254158A (en) Process of recovering nickel
US2224823A (en) Method for devolatilizing charcoal
US2810667A (en) Process for heat-treating metals in a space containing a non-oxidizing protective gas atmosphere
US3022059A (en) Apparatus for treating metal melts
US3171759A (en) Method of heat treating high speed steels
US1934614A (en) Furnace
US2416992A (en) Method and apparatus for condensing metallic vapors
US1597718A (en) Apparatus for recovering heat from coke, slags, ashes, and other solid substances
US2266750A (en) Metal purification