US946511A - Method of manufacturing carbid. - Google Patents

Method of manufacturing carbid. Download PDF

Info

Publication number
US946511A
US946511A US35714007A US1907357140A US946511A US 946511 A US946511 A US 946511A US 35714007 A US35714007 A US 35714007A US 1907357140 A US1907357140 A US 1907357140A US 946511 A US946511 A US 946511A
Authority
US
United States
Prior art keywords
coal
lime
coke
carbid
manufacturing
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
US35714007A
Inventor
Herman L Hartenstein
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.)
CONTINENTAL INVESTMENT Co
CONTINENTAL INVEST Co
Original Assignee
CONTINENTAL INVEST Co
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 CONTINENTAL INVEST Co filed Critical CONTINENTAL INVEST Co
Priority to US35714007A priority Critical patent/US946511A/en
Priority to US384235A priority patent/US889124A/en
Application granted granted Critical
Publication of US946511A publication Critical patent/US946511A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/90Carbides
    • C01B32/914Carbides of single elements
    • C01B32/942Calcium carbide

Definitions

  • HERMAN L. HARTENSTEIN 0F CONSTANTINE, MICHIGAN. AESIGNOR, BY MESNE AS- SIGNMENTS, TO CONTINENTAL INVESTMENT COMPANY, OF DULUTH. MINNESOTA.
  • This invention relates more particularly to the manufacture of calciumcarbid from limestone or lime and a carbonaceous material, such as coal, et eetera,.and it has for its primary object a method in which all of the advantages of the use of coal may be secured without any of the disadvantages of such fuel, such as excessive smoke generated in the furnace during the reduction operation, and the higher or excessive voltage required by reason of the presence of the particles of hard coal in the charge being treated or reduced.
  • Another object of the invention is to provide an improved method for the manufacture of carbid' in which the small particles of lime or limestone will be bound in intimate association with the small particles of carbonaceous material during the reduction of the calcareous material in the electric furnace.
  • the lime and carbonaceous material in the usual or any suitable proportions as heretofore practiced in this art and the lime is obtained in the usual or any suitable way but preferably by calcining limestone which has been previously pulverized or comminuted.
  • the lime or calcined limestone is taken from the pro-heater or calcining furnace while in its highly heated condition and is mixed with the proper proportion of carbonaceous mat ter which, according to this invention, consists of a mixture of hard coal (anthracite coal) and a highly conductive artificial carbon, such as coke, or charcoal.
  • I preferably employ anthracite coal screenings, which are in a more or less fine or comminuted condition and to eighty or ninety per cent. of this I add from ten to twenty per cent. of the coke or charcoal, which is also previously ground or powdered.
  • the anthracite coal is rich in carbonaceous material but. its use alone is attended by 0bjectionable results, such as excessive smoke which precludes a fair view of the electrodes when the furnace is opened for examination by'the attendant from time to time during the operation; and. moreover. it produces a high resistance to the current and as a consequence requires the use of a higher voltage.
  • These objections are sufficiently overcome by the addition of a small percentage of coke or charcoal which adds greatly to the conductivity of the charge between the electrodes. The result may be still further improved and facilitated by the addition to the carbonaceous constituent of a small percentage (say from three to twenty per cent.) of bituminous coal, rich in tarry compounds, say about five per cent. This, also.
  • the soft coal may also be preliminarily mixed with the anthracite or coke before being placed in the mixer with the highly heated limestone.
  • the temperature is suiliciently high to convert the tar and carbon of the coal into coke, and previous to or during the process of mix ing the sintering coal serves to act as a binder for holding together the coke, anthracite and highly heated limestone of the charged mixture, while the soft coal is like wise converted into a coke and becomes a portion of the charge mixture when it leaves the mixer and. is placed in the electric furnaces.
  • the volatile matter or gases that are expelled during the mixing process furnish heat by their combustion, and at the same time materially aid the mechanicalmixing process, by reason of theboiling or agitation caused by the volatile matter of the soft coal in the presence of heat.
  • the gases produced by the addition of soft coal are also ample .to prevent the admission of air into the mixture furnishing a surmounting and protecting gaseous blanket and thereby prevent any possible oxidation of other carbonaceous material (anthracite or coke) which is lOW in volatile matter.
  • the hereindescribecl method of manueaasii facturing carbid which. comprises fusing lime and a carbonaceous material comprlsing anthracite coal, artificial carbon, and
  • the liereindescribed method of manufacturing carbid which comprises mixing lime with carbonacebus material comprising pulverized anthracite coal and pulverized artificial carbon and fusing the same together.
  • The'hereindescribed method of manufacturing carbid which comprises calcining limestone and mixing with the resultant lime, while hot, a quantity of bituminous coal in a state of fine sub-division, and subsequently fusing the mixture with an admixture of artificial carbon by the electric current.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Description

'oniran s'rarns ra rniar ora ion.
HERMAN L. HARTENSTEIN, 0F CONSTANTINE, MICHIGAN. AESIGNOR, BY MESNE AS- SIGNMENTS, TO CONTINENTAL INVESTMENT COMPANY, OF DULUTH. MINNESOTA.
A CORPORATION OF MINNESOTA.
METHOD OF MANUFACTURING CARBID.
No Drawing.
To all whom it may concern:
Be it known that I, HERMAX L. H.\RTEN- STEIN, a citizen of the United States, residing at Constantine. in the county of St. Joseph and State of Michigam have invented certain new and useful Improvements in the Method of Manufacturing Carbid, of which the following is a full. clear, and exact specification.
This invention relates more particularly to the manufacture of calciumcarbid from limestone or lime and a carbonaceous material, such as coal, et eetera,.and it has for its primary object a method in which all of the advantages of the use of coal may be secured without any of the disadvantages of such fuel, such as excessive smoke generated in the furnace during the reduction operation, and the higher or excessive voltage required by reason of the presence of the particles of hard coal in the charge being treated or reduced.
Another object of the invention is to provide an improved method for the manufacture of carbid' in which the small particles of lime or limestone will be bound in intimate association with the small particles of carbonaceous material during the reduction of the calcareous material in the electric furnace.
In carrying out the invention,I employ lime and carbonaceous material in the usual or any suitable proportions as heretofore practiced in this art and the lime is obtained in the usual or any suitable way but preferably by calcining limestone which has been previously pulverized or comminuted. The lime or calcined limestone is taken from the pro-heater or calcining furnace while in its highly heated condition and is mixed with the proper proportion of carbonaceous mat ter which, according to this invention, consists of a mixture of hard coal (anthracite coal) and a highly conductive artificial carbon, such as coke, or charcoal. I preferably employ anthracite coal screenings, which are in a more or less fine or comminuted condition and to eighty or ninety per cent. of this I add from ten to twenty per cent. of the coke or charcoal, which is also previously ground or powdered. By using amixture of anthracite coal and coke it is practicable to,
utilize the cheaper grades of coke as, for example, breeze or refuse which is higher in Specification of Letters Patent.
Patented Jan. 11, 1910.
Application filed February 13, 1907. Serial No. 357,140.
ash and impurities than lump coke which contains much more than the anthracite coal. These two ingredients are intimately commingled and mixed with the fine or pulverized lime or limestone while the calcareous material is in a highly heated condition and the mass is then subjected 10 the action of the electric current in an electric furnace until reduced to a molten bath according to the established practice of this art.
The anthracite coal is rich in carbonaceous material but. its use alone is attended by 0bjectionable results, such as excessive smoke which precludes a fair view of the electrodes when the furnace is opened for examination by'the attendant from time to time during the operation; and. moreover. it produces a high resistance to the current and as a consequence requires the use of a higher voltage. These objections, however, are sufficiently overcome by the addition of a small percentage of coke or charcoal which adds greatly to the conductivity of the charge between the electrodes. The result may be still further improved and facilitated by the addition to the carbonaceous constituent of a small percentage (say from three to twenty per cent.) of bituminous coal, rich in tarry compounds, say about five per cent. This, also. is employed in a state of fine sub-division and it is mixed with the lime or calcined limestone while the latter is in a highly heated condition after coming from a pro-heater or calcining furnace and by thus intermingling the bituminous coal with the lime or calcined limestone while the latter is hot such coal is converted into coke and its bituminous constituents are more or less liquefied or softened and deposit upon the particles of calcined limestone as well as upon the particleli'f coke and anthracite coal and acts as a binder to hold these constituents of the carbonaceous material in intimate association with the lime, thereby giving every particle of lime its appropriate percentage of carbonaceous material and resulting in a final product which presents a degree of uniform reduction greater than that heretofore secured. The soft coal may also be preliminarily mixed with the anthracite or coke before being placed in the mixer with the highly heated limestone.
I do not herein claim the composition of matter produced as described tlns forming the subject matter of a divisional application Ser. No. 384,235, July 17, 1907 (now Patent No. 889124., May 26, 1908).
The temperature is suiliciently high to convert the tar and carbon of the coal into coke, and previous to or during the process of mix ing the sintering coal serves to act as a binder for holding together the coke, anthracite and highly heated limestone of the charged mixture, while the soft coal is like wise converted into a coke and becomes a portion of the charge mixture when it leaves the mixer and. is placed in the electric furnaces.
It is understood that the particles of hot limestone and coke and anthracite coal become more or less mechanically united while the tarry matter of the soft coal is being expelled therefrom as it is convertedinto coke.
The volatile matter or gases that are expelled during the mixing process furnish heat by their combustion, and at the same time materially aid the mechanicalmixing process, by reason of theboiling or agitation caused by the volatile matter of the soft coal in the presence of heat. I
The gases produced by the addition of soft coal are also ample .to prevent the admission of air into the mixture furnishing a surmounting and protecting gaseous blanket and thereby prevent any possible oxidation of other carbonaceous material (anthracite or coke) which is lOW in volatile matter.
Having thus described my invention, what I claim as new therein and desire to secure by Letters Patent is 1. The hereindescribed method of manufacturin carbid, which comprises fusing lime an a carbonaceous material comprising anthracite coal and artificial carbon.
2. The hereindescribecl method of manueaasii facturing carbid, which. comprises fusing lime and a carbonaceous material comprlsing anthracite coal, artificial carbon, and
bituminous coal. 4
3. The liereindescribed method of manufacturing carbid, which comprises mixing lime with carbonacebus material comprising pulverized anthracite coal and pulverized artificial carbon and fusing the same together. v
4:. The hereindescribed method of manufacturing carbid, which comprises mixing lime with a carbonaceous material consisting of pulverized hard coal, pulverized coke or charcoal and pulverized coal which is rich in tarry matters and fusing the mixture.
5. The'hereindescribed method of manufacturing carbid which comprises calcining limestone and mixing with the resultant lime, while hot, a quantity of bituminous coal in a state of fine sub-division, and subsequently fusing the mixture with an admixture of artificial carbon by the electric current.
6. The hereindescribed method of manufacturing carbid, which consists. in mixing with hot lime, a quantity of coal containing tarry matter and causing the tar thereof to deposit itself upon the particles of lime, mixin with the said mixture pulverized artificial carbon while the mixture is hot and subsequently fusing the mass.
In testimony whereof I have signed my name to this specification, in the presence of two subscribing witnesses, on this 29th day of January A. D. 1907.
HERMAN L. HARTENSTEIN.
Witnesses:
NELLIE ORTON, DANL. Gr. CASH.
US35714007A 1907-02-13 1907-02-13 Method of manufacturing carbid. Expired - Lifetime US946511A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US35714007A US946511A (en) 1907-02-13 1907-02-13 Method of manufacturing carbid.
US384235A US889124A (en) 1907-02-13 1907-07-17 Manufacture of carbid.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US35714007A US946511A (en) 1907-02-13 1907-02-13 Method of manufacturing carbid.

Publications (1)

Publication Number Publication Date
US946511A true US946511A (en) 1910-01-11

Family

ID=3014932

Family Applications (1)

Application Number Title Priority Date Filing Date
US35714007A Expired - Lifetime US946511A (en) 1907-02-13 1907-02-13 Method of manufacturing carbid.

Country Status (1)

Country Link
US (1) US946511A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9481577B2 (en) 2013-10-22 2016-11-01 Lp Amina Llc Reactor with induction heater

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9481577B2 (en) 2013-10-22 2016-11-01 Lp Amina Llc Reactor with induction heater

Similar Documents

Publication Publication Date Title
US3660298A (en) Furnace charge for use in the production of silicon metal
US1848710A (en) Metal sponge
US1923803A (en) Briquette and method of producing same
US946511A (en) Method of manufacturing carbid.
US889124A (en) Manufacture of carbid.
US1838882A (en) Process of producing carbonized particles from coking coal
US1467797A (en) Preliminary preparation of furnace charges for ore-smelting furnaces
US1391211A (en) Otto e
DE4241245A1 (en) Calcium carbide prodn. from calcium oxide and carbonaceous cpd. - derived from crushed plastics waste in presence of granular calcium oxide by pyrolysis and calcination
US568323A (en) Manufacture of graphite
US1494130A (en) Process of and material for the production of carbide and reduction of ore
US1215700A (en) Carbon electrode and method of manufacturing same.
JPS5978914A (en) Manufacture of special carbonaceous material
US619729A (en) John thomas davis
US1896088A (en) Process of reducing ores
US1152506A (en) Method of manufacturing carbid.
US1334180A (en) Method of manufacturing briquets
US844018A (en) Process of utilizing marl, making carbid.
US432383A (en) Charles j
US1499750A (en) Process of producing gas
US791799A (en) Ore-briquet.
US2121160A (en) Method of preparation and use of metallic oxides and solid fuels
US943724A (en) Process of briqueting metallic iron.
US645285A (en) Method of manufacturing graphite.
US958950A (en) Process of manufacturing briquets.