US1518186A - Agglomeration of powdered or finely crushed materials, more particularly fuel, by means of pitch - Google Patents

Agglomeration of powdered or finely crushed materials, more particularly fuel, by means of pitch Download PDF

Info

Publication number
US1518186A
US1518186A US637390A US63739023A US1518186A US 1518186 A US1518186 A US 1518186A US 637390 A US637390 A US 637390A US 63739023 A US63739023 A US 63739023A US 1518186 A US1518186 A US 1518186A
Authority
US
United States
Prior art keywords
pitch
solution
agglomeration
parts
powdered
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
US637390A
Inventor
Boistesselin Henri Du
Tabb Frederick William
Hertenbein Leon
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.)
LEON VARNIER
OCTAVE DUBOIS
Original Assignee
LEON VARNIER
OCTAVE DUBOIS
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 LEON VARNIER, OCTAVE DUBOIS filed Critical LEON VARNIER
Priority to US637390A priority Critical patent/US1518186A/en
Application granted granted Critical
Publication of US1518186A publication Critical patent/US1518186A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00Solid fuels
    • C10L5/02Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/06Methods of shaping, e.g. pelletizing or briquetting
    • C10L5/10Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders

Definitions

  • This invention relates to a process for the agglomeration of powdered or finely crushed materials, and more particularly fuel, by means of pitch.
  • melted pitch that is to' say, a mixture of dry pitch and tar raised to the melting temperature before being mixed with the coal dust.
  • This method of operation enables the proportion of pitch employed to be reduced (to about 5%), in comparison with the processfirst referred to but the agglomerates obtained generate a dense smoke when burning.
  • the pitch serving to agglomerate the powdered or finely crushed materials, and more particularly fuels, is suspended in water in such a manner as to form a pseudo-solution, before being mixed with theimaterial to be agglomerated.
  • the drying is preferably effectedby heat perature which ensures the distillation and the removal ofthe volatile products of the pitch by the steam which isevolved.
  • the combustible agglomerates. obtained according to theprocess forming the subject of the invention burn without producing smoke or odour by reason of the removal of the volatile elements of the pitch during the heating of the agglomerates.
  • the pitch thus brought into suspension in water, is distributed in the latter in a in grinding the pitch, substances adapted to increase the agglutinant power of the solu- .solutions of pitch in the same way that it acts in relation to pseudo-solutions of graphite. It delays fiocula-tion, that is to say, the settling or precipitation of the pitch, and for this purpose it may be used in the same proportions as dextrine, the extracts of cellulose, etc.
  • the pitch solution is added to the dust to be agglomerated in such a manner as to introduce 2 to 4% of pitch.
  • the whole is suitably mixed whilst cold; and then the mass is passed through a press into moulds whic -may or may not beheated.
  • the agglomerates when leaving the press re si'ibjected to a suitable drying operation in the case of fuels the drying is preferably effected in a' stove, heated in any suitable process according to the manner so as to raise the temperature of the agglomerates to a temperature of about 200250 C.
  • the drying is preferably effected in a' stove, heated in any suitable process according to the manner so as to raise the temperature of the agglomerates to a temperature of about 200250 C.
  • oxidizing agents such as chloride of lime, nitrates of metals having two degrees of oxidation, such as the nitrates of iron, chromium, cobalt, etc.; these oxidizing agents are employed in small proportions for example "from 0.1'to 0.5% of the fuel.
  • Example III 100 parts of anthracite dust are mixed with 6 parts of a 50% pitch solution, diluted with 4 parts of water.
  • Example IV 100 parts of Web coal dust are mixed with 1 parts of a 50% pitch solution, diluted with 6 parts of water, to which are added 0.2 parts of cobalt nitrate. It will be understood that these examples are only given by way of explanation.
  • the paste may be heated in any-.suitable apparatus, but is preferably effected in an apparatus comprising heating. surfaces; finally a stream of hot air is passed through the mass of hot paste for the purpose of removing the excess of moisture therefrom (above 2.5 to 3%) due to the water contained in the pseudd-solution of pitch or due to the Humidity of the dust employed.
  • a an example a double-walled cylinder may be employed; heated by steam, hot water or combustion gases, whilst a hollow spiral, or inclined blades arranged in the form of a spiral in the interior thereof, produce by their movement a constant variation of the contact of the mass of paste with the heating surface and with the hot air passing through the cylinder, along the axis thereof, in the opposite direction to the material which is fed'forward by the'movement of, the spiral or of the blades.
  • Example V 100 parts of Cambridge fine coal, of 4%humidity, are mixed with8 parts of a pseudo-solution of pitch, containing pitch, so that about 5 parts of pitch and 3 parts of water are introduced into the mixture.
  • the paste After mixing, whilst cold, the paste isheated to about .to 80 0., whilst the air, also raised to this temperature, is passed through this paste in order to remove 4 parts of Water therefrom.
  • Example VI 100 parts of fine anthracite, with 1% water, are mixed with parts of a pseudo-solution of pitch, with pitch, so that about 5 parts of pitch and 2 parts of water are introduced. After mixing, the mass is heated to 60 to C. without passing hot air through the interior of the heating apparatus.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Description

Patented Dec. 9, 1924.
UNITED STATES PATENT; OFFICE.
HENRI DU BOISTESSELIN, OF BOUEN, FREDERICK WILLIAM v'JJAIBB, O'F PARIS, AND LEON HERTENBEIN, OF LEVALLOIS-PERRET, FRANCE, ASSIGNORS OF ONE-FIFTH IO QCTAVE DUIBOIS AND ONE-FIFTH TO LEON VARNIEBI, BOTH OF ROUEN, FRANCE.
AGGLQMERATION OF POWDERED OR FINELY CRUEEHED MLA'J?IEIBIIALS,v KOBE PAR- TICULARLY FUEL, BY MEANS OF PITCH.
No Drawing.
To all whom it may concern:
Be it known that we, HENRI DU BOISTES- SELIN, a citizen of the French Republic, residing at Rouen, France, FREDERICK W1L- LIAM TABB, av subject of the King of Great Britain, residing at Paris, France, and LF'JON HEnrnNBnIN, a citizen of the French Republic, residing at Levallois-Prret, Seine, France, have invented a newand useful Improvement in Agglomeration of Powdered or Finely Crushed Materials, More Particularly Fuel, by Means of Pitch, of which the following is a true and exact description. i
This invention relates to a process for the agglomeration of powdered or finely crushed materials, and more particularly fuel, by means of pitch.
In practice, for the agglomeration of these materials and especially fuel in a more or less finely ground state is mixed with the dust to be agglomerated, and then the whole is introduced into a mixer, usually heated by steam, in such a manner as to melt the pitch and to enable it to be dis-' tributed throughout the mass. The paste obtained is then moulded 'whilst it is still hot and plastic.
The more finely the,pitch is ground, the more uniformly will it be distributed throughout the mass and this more efficient distribution produces a slight reduction in the percentage of pitch necessary for the agglomeration. i
In some plants melted pitch is used, that is to' say, a mixture of dry pitch and tar raised to the melting temperature before being mixed with the coal dust. This method of operation enables the proportion of pitch employed to be reduced (to about 5%), in comparison with the processfirst referred to but the agglomerates obtained generate a dense smoke when burning.
According to the present invention, the pitch, serving to agglomerate the powdered or finely crushed materials, and more particularly fuels, is suspended in water insuch a manner as to form a pseudo-solution, before being mixed with theimaterial to be agglomerated. I
The mass or paste obtained by mixing, whilst cold, the material to be agglomerated with a suitable proportion of the pseudodu'st, dry pitch Application filed May 7, 1923. Serial No. 637,330}
' solution of pitch may then be introduced into a press, and the agglomeratesobtained may be dried by heating.
- The drying is preferably effectedby heat perature which ensures the distillation and the removal ofthe volatile products of the pitch by the steam which isevolved.
ing the agglomerates in a stove at a tem- By placing thepitch in suspension in wanecessary varies from 2 to 470' for the ag glomeration of fuel-dust -(coal, coke, anthracite, etc.,) instead of the proportion of 7 to 10% necessary in the usual plants,-
the combustible agglomerates. obtained according to theprocess forming the subject of the invention burn without producing smoke or odour by reason of the removal of the volatile elements of the pitch during the heating of the agglomerates.
One satisfactory mode of procedure in carrying out the invention is as follows:- 1 The pitch, coarsely crushed as usual,-is then ground by using water as'the dispersing agent; this grinding can be effected in anysuitable apparatus such for example as a ball mill or pulverizer. The proportions of water and pitch may vary within very wide limits; good results are; obtained by using equal parts by weight of water and pitch.
The pitch, thus brought into suspension in water, is distributed in the latter in a in grinding the pitch, substances adapted to increase the agglutinant power of the solu- .solutions of pitch in the same way that it acts in relation to pseudo-solutions of graphite. It delays fiocula-tion, that is to say, the settling or precipitation of the pitch, and for this purpose it may be used in the same proportions as dextrine, the extracts of cellulose, etc.
We have found that it is possiblev to obtain commercially pseudo-solutions of pitch with a high content of pitch. This content may exceed 70% by weight of the solution,-
which is advantageous in certain industries, especially in the industry for the agglomeration of coal.
The pitch solution is added to the dust to be agglomerated in such a manner as to introduce 2 to 4% of pitch. The whole is suitably mixed whilst cold; and then the mass is passed through a press into moulds whic -may or may not beheated.
The agglomerates when leaving the press re si'ibjected to a suitable drying operation; in the case of fuels the drying is preferably effected in a' stove, heated in any suitable process according to the manner so as to raise the temperature of the agglomerates to a temperature of about 200250 C. In view of the very fine division and intimate mixing, molecule by molecule, of the pitch and water in the mixture, there is produced a thorough distillation of the pitch by the removal, by means of the steam, of the volatile products contained in the pitch, which thus escape, so
.that after this treatment the. fuel agglomerates burn in grates without evolving smoke or odours. Another advantage, due to the resent invention, is that the agglomerates have no tendency to stick together in the grates, which is a disadvantage! observed with ordinary agglomeratesmade with pitch.
To the pitch solution may also be added,
before it is mixed with the fuel dust, oxidizing agents such as chloride of lime, nitrates of metals having two degrees of oxidation, such as the nitrates of iron, chromium, cobalt, etc.; these oxidizing agents are employed in small proportions for example "from 0.1'to 0.5% of the fuel. These' additions, at the time of the 'thermic treatment mentioned above, serve to oxidize the The following are examples of the application of the invention to the manufacture of agglomerated fuels Example I. 100 parts of anthracite dust containing 7% of water are mixed with 8 parts of a 50% pitch solution.
-Example H.100 parts of Cardiff coal dust are mixed with 8 parts of a 50% pitch solution and 0.2 parts by weight of chloride of lime.
Example III. 100 parts of anthracite dust are mixed with 6 parts of a 50% pitch solution, diluted with 4 parts of water.
Example IV. 100 parts of Cardiff coal dust are mixed with 1 parts of a 50% pitch solution, diluted with 6 parts of water, to which are added 0.2 parts of cobalt nitrate. It will be understood that these examples are only given by way of explanation.
Instead of introducing the mass or paste, resulting from the mixing of the material to beagglomerated with the pseudo-solution of pitch, into the press and then drying the agglomerates obtained by heating, it is possible, according to the second method of carrying the invention into effect, to heat this mass or paste to the melting temperature of the pitch, which is generally 60 to 80? C. for the pitch of the coal usually em ployed in the agglomerating industry, before introducing it into the press, as is usual in the present manufacture of agglomerated fuels.
The paste may be heated in any-.suitable apparatus, but is preferably effected in an apparatus comprising heating. surfaces; finally a stream of hot air is passed through the mass of hot paste for the purpose of removing the excess of moisture therefrom (above 2.5 to 3%) due to the water contained in the pseudd-solution of pitch or due to the Humidity of the dust employed.
A an example a double-walled cylinder may be employed; heated by steam, hot water or combustion gases, whilst a hollow spiral, or inclined blades arranged in the form of a spiral in the interior thereof, produce by their movement a constant variation of the contact of the mass of paste with the heating surface and with the hot air passing through the cylinder, along the axis thereof, in the opposite direction to the material which is fed'forward by the'movement of, the spiral or of the blades.
The following are a few examples of the application of this second methodof operation.
Example V. 100 parts of Cardiff fine coal, of 4%humidity, are mixed with8 parts of a pseudo-solution of pitch, containing pitch, so that about 5 parts of pitch and 3 parts of water are introduced into the mixture.
After mixing, whilst cold, the paste isheated to about .to 80 0., whilst the air, also raised to this temperature, is passed through this paste in order to remove 4 parts of Water therefrom.
Example VI. 100 parts of fine anthracite, with 1% water, are mixed with parts of a pseudo-solution of pitch, with pitch, so that about 5 parts of pitch and 2 parts of water are introduced. After mixing, the mass is heated to 60 to C. without passing hot air through the interior of the heating apparatus.
It will be understood that these examples are only given by way of explanation.
What we claim is:
1. A process for the agglomeration powdered or finely crushed materials, and more particularly fuels, consisting in suspending pitch in water, so as to form a pseudo-solution, in mixing, whilst cold, the
materials to be agglomerated with a suitable proportion of said pseudo-solution,-in com.- pressing said mass, and drying by heat the agglomerates obtained, at a temperature of about 200250 U. adapted to ensure distillation and removal of the volatile products of the pitch.
2. A process for the agglomeration of powdered or finely crushed materials, and more particularly fuels, consisting in suspending pitch-in water, so as to form a pseudo-solution, adding to said pitch solution gummy, resinous or mucilaginous substances adapted to increase the agglutinanr.
power of the said pseudo-solutions, in mixing, whilst cold, the materials to be agglomerated with a suitable proportion of said pseudo-solution,-in compressing said mass, and drying by heat the agglomerates obtained.
3. A process for the agglomeration of powdered or finely crushed materials, and more particularly fuels, consisting suspending pitch in water, so as to form a pseudo-solution, adding to said pitch solution oxidizing agents adapted to facilitate the removal of the volatile products of the pitch by heat, in mixing, whilst cold, the
materials to be agglomerated with a snitable proportion of said pseudo-solution,- in compressing said mass, and drying by heat the agglomerates obtained.
4. A process for the agglomeration of powdered 'or finely crushed materials, and more particularly fuels, consisting in suspending pitch in water, so as to form a pseudo-solution, adding to said pitch solu tion gummy, resinous or mucilaginous substances adapted to increase the agglutinant power ofthe said pseudo-solutions, and oxidizing agents adapted to facilitate the removal of the volatile products of the pitch by heat, in mixing, whilst cold, the materials to be agglomerated with a suitable proportion of said pseudo-solution -in compressing said mass, and drying by heat the agglomerates obtained.
In testimony whereof we have signed names to this specification. I
HENRI DU BOISTESS'ELIN. FREDERICK WILLIAM TABB LEON HERTENBEIN. Witnesses:
J. ARMENGANDAINI. ll. Dnrr'xonlnon'r.
US637390A 1923-05-07 1923-05-07 Agglomeration of powdered or finely crushed materials, more particularly fuel, by means of pitch Expired - Lifetime US1518186A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US637390A US1518186A (en) 1923-05-07 1923-05-07 Agglomeration of powdered or finely crushed materials, more particularly fuel, by means of pitch

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US637390A US1518186A (en) 1923-05-07 1923-05-07 Agglomeration of powdered or finely crushed materials, more particularly fuel, by means of pitch

Publications (1)

Publication Number Publication Date
US1518186A true US1518186A (en) 1924-12-09

Family

ID=24555716

Family Applications (1)

Application Number Title Priority Date Filing Date
US637390A Expired - Lifetime US1518186A (en) 1923-05-07 1923-05-07 Agglomeration of powdered or finely crushed materials, more particularly fuel, by means of pitch

Country Status (1)

Country Link
US (1) US1518186A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1128149B (en) * 1959-06-01 1962-04-19 Shell Int Research Process for pelletizing fine-grained ores

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1128149B (en) * 1959-06-01 1962-04-19 Shell Int Research Process for pelletizing fine-grained ores

Similar Documents

Publication Publication Date Title
US700888A (en) Fluid for promoting combustion.
US911960A (en) Composition for treating fuel.
US1518186A (en) Agglomeration of powdered or finely crushed materials, more particularly fuel, by means of pitch
US3336122A (en) Briquets made of char and method for the production thereof
US3370932A (en) Flame coloring product and method of manufacturing same
US617079A (en) Bone-black substitute and method of manufacture
US2824790A (en) Briquetting of coal
US1668643A (en) Manufacture of fuel briquettes
US1893555A (en) Method of manufacturing briquettes
US1512427A (en) Fuel-producing process and product
US1290992A (en) Briquet and method of manufacturing the same.
US2040609A (en) Briquetted fuel and process of making
US619729A (en) John thomas davis
US1790356A (en) Solid fttel
US1000479A (en) Briquet and method of making the same.
US1621506A (en) Manufacture of a finely-divided dry soap product
US1507678A (en) Binding-fuel material and process of producing the same
US1507674A (en) Process of briquetting finely-divided materials
US23005A (en) henry adoiphex a aechereau
US1481942A (en) Fuel briquette and the process of making same
US1560116A (en) Treatment of finely-divided coal
US28579A (en) Material for facing molds for casting metals
US1615463A (en) Artificial fuel and method of making same
US1130564A (en) Artificial fuel and method of making the same.
US2922705A (en) Process for the manufacture of fuel briquettes