US1655728A - Briquette and method of manufacture - Google Patents

Briquette and method of manufacture Download PDF

Info

Publication number
US1655728A
US1655728A US90409A US9040926A US1655728A US 1655728 A US1655728 A US 1655728A US 90409 A US90409 A US 90409A US 9040926 A US9040926 A US 9040926A US 1655728 A US1655728 A US 1655728A
Authority
US
United States
Prior art keywords
acid
tars
briquettes
coke
briquette
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
US90409A
Inventor
Lemuel M Johnston
James L Farrell
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 US90409A priority Critical patent/US1655728A/en
Application granted granted Critical
Publication of US1655728A publication Critical patent/US1655728A/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
    • C10L5/14Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders with organic binders

Definitions

  • Our invention relates to briquettes and a method of manufacture, and particularly to the utilization of certain by-products of the petroleum refining industry in making such briquettes.
  • coke in coke stills and in pressure or cracking stills wherein crude petroleum or its derivatives are destructively distilled, coke is formed and must be removed from the stills and disposed of at suitable intervals.
  • This coke is ofsubstantially pure car- 'bon and finds various limited uses, but the supply is so large that the economical disposal thereof is, like the acid tars, a matter of difliculty.
  • Acid tars in proper proportions may then be added to the finely divided coke and the mixture well masticated and mixed. It is preferable to heat the acid tars so as to render the same quite fluid in order to obtain the proper mixture, and it is also desirable to heat the mass while mixing.
  • the mixed coke and tars may then be formed into briquettes under suitable pressure.
  • briquettes will of course contain the acid which was present in the tars, and this acid, if allowed to remain in the finished briquettes would have deleterious effects on the furnaces in which the briquettes are later burned. We therefore sub ect the formed briquettes to a roasting process which evaporates or drives 011' the acid, thus leavin the briquettes substantially free of acid, an therefore suitable for burning in ordinary furnaces.
  • the proportions of carbonaceous materials and acid tars will vary between quite wide limits dependent upon the character and fineness of the carbonaceous material, as well as upon the character and consistency of the acid tars.
  • the tars as ordinarily formed vary in consistency from a heavy asphalt to that of a light road oil, and obviously the amount of tars which can be successfully employed in mixing with car bonaceous materials will depend, as one factorupon the consistency and character of the tars.
  • the proportions of the ingredients of the briquettes should be such that an intimate mixture is obtained, and so that the carbonaceous material will be bound into a relatively uniform, or homogeneous mass, which will not be readily broken or powdered upon being handled, and the percentage of tars must .not be so highthat the form of the briquette will be su stantially altered upon being subjected to the roasting process.
  • 'VVe may say, by wa of example, that with finely divided petro eum coke and an average sample of acid tars, approximately 15% of the tars and 85% of the carbonaceous material will give satisfactory results.
  • the finished briquette of the character above referred to is a superior fuel in that there is substantially no ash residue upon being burned, may be made very dense and compact, will Withstand comparatively rough handling and shipment without substantial breakage or disintegration is easily ignited and burned, and may be burned so as to be substantially smoke free, is comparatively clean to handle, and the heat value is often as high as 15,500 B. t. u. per pound.
  • the acid tars are of a very complex composition and contain many compounds among which may be mentioned ammonia, complex hydrocarbons, and alcohols, such as butyl and propyl alcohol.
  • ammonia complex hydrocarbons
  • alcohols such as butyl and propyl alcohol.
  • the method ofutilizing petroleum coke and acid tars resulting from the refining of petroleum which comprises, mixing the finely divided coke with the acid tars, compressing the mixture into briquettes, and roasting the briquettes to drive off the acid.
  • the method which comprises, pulverizing carbonaceous material. mixing the same with acid tars while heated, forming the mixture into briquettes, and then roasting to drive ofi the acid.
  • a briquette formed of finely divided carbonaceous material and a binder of acid tars, said briquette being readily ignit-able, of high fuel value, leaving substantially no ash residue, and relatively compact and tough to withstand rough handling.
  • the method which comprises, mixing acid tars with carbonaceous material, then heating the mixture to drive ofi' volatile products and collecting those products.

Description

No Drawing.
Patented Jan. 10, 1928.
UNITED STATES PATENT OFFICE.
LEMUEL M. JOHNSTON AND JAMES L. FARRELL, OF PARCO, WYOMING.
' BRIQUETTE AND METHOD OF MANUFACTURE.
Our invention relates to briquettes and a method of manufacture, and particularly to the utilization of certain by-products of the petroleum refining industry in making such briquettes.
In the refining of petroleum, it is common practice to. treat the lighter distillates and lubricating oils with sulphuric acid and such treatment causes a sludge to be precipitated, which sludge is generally called acid tars because of its tarlike characteristics and its acidity. These acid tars can be treated to recover the acid but at great expense, and the economical disposal of the acid tars in refineries is a serious problem.
Further, in coke stills and in pressure or cracking stills wherein crude petroleum or its derivatives are destructively distilled, coke is formed and must be removed from the stills and disposed of at suitable intervals. This coke is ofsubstantially pure car- 'bon and finds various limited uses, but the supply is so large that the economical disposal thereof is, like the acid tars, a matter of difliculty.
It is the principal purpose of our invention to utilize the acid tars of the character above referred to, and petroleum coke or other carbonaceous materials in the manufacture of briquettes, which will be an efficient fuel having many; advantages over other fuels now in use.
In the utilization of the by-products of I the petroleum industry above referred to,
we may first crush or pulverize the petroleum coke. Acid tars in proper proportions may then be added to the finely divided coke and the mixture well masticated and mixed. It is preferable to heat the acid tars so as to render the same quite fluid in order to obtain the proper mixture, and it is also desirable to heat the mass while mixing. The mixed coke and tars may then be formed into briquettes under suitable pressure. The
briquettes will of course contain the acid which was present in the tars, and this acid, if allowed to remain in the finished briquettes would have deleterious effects on the furnaces in which the briquettes are later burned. We therefore sub ect the formed briquettes to a roasting process which evaporates or drives 011' the acid, thus leavin the briquettes substantially free of acid, an therefore suitable for burning in ordinary furnaces.
While we. have mentioned petroleum coke Application filed February 24, 1926. Serial No. 90,409.
as desirable in forming the briquettes as above referred to, we wish it understood stantially pure carbon, and there is little mineral matterin'the acid tars to form ash.
The proportions of carbonaceous materials and acid tars will vary between quite wide limits dependent upon the character and fineness of the carbonaceous material, as well as upon the character and consistency of the acid tars. The tars as ordinarily formed, vary in consistency from a heavy asphalt to that of a light road oil, and obviously the amount of tars which can be successfully employed in mixing with car bonaceous materials will depend, as one factorupon the consistency and character of the tars. The proportions of the ingredients of the briquettes, however, should be such that an intimate mixture is obtained, and so that the carbonaceous material will be bound into a relatively uniform, or homogeneous mass, which will not be readily broken or powdered upon being handled, and the percentage of tars must .not be so highthat the form of the briquette will be su stantially altered upon being subjected to the roasting process. 'VVe may say, by wa of example, that with finely divided petro eum coke and an average sample of acid tars, approximately 15% of the tars and 85% of the carbonaceous material will give satisfactory results. Good results have also been obtained by mixing ground coke with about 6% of-acid sludge and, after briquetting, heating the briquettes to about 350 F. to drive off most of the acids; Higher temperatures produce a less smoky variety of fuel and a harder briquette usually results. Generally speaking the greatest practicable proportion of acid tars will give the greatest economic return since the tars are now of little use and therefore cheap, and the heat value of the tars is quite high.
The finished briquette of the character above referred to is a superior fuel in that there is substantially no ash residue upon being burned, may be made very dense and compact, will Withstand comparatively rough handling and shipment without substantial breakage or disintegration is easily ignited and burned, and may be burned so as to be substantially smoke free, is comparatively clean to handle, and the heat value is often as high as 15,500 B. t. u. per pound.
By so utilizing the two by-products of the petroleum industry above mentioned, we are able to form an excellent fuel, and also to provide a profitable means of disposal of the two byproducts and to thus turn what was formerly a substantial economic loss into a gain.
Another notable feature forming part of our invention is the recovery of certain byproducts from the acid tars and sometimes from the coke. The acid tars are of a very complex composition and contain many compounds among which may be mentioned ammonia, complex hydrocarbons, and alcohols, such as butyl and propyl alcohol. When the acidtars are heated sufficiently many of these compounds and others are vaporized, and since some of these are of considerable value should be recovered. 'We therefore propose to condense or otherwise collect certain or all of the products vaporized when the acid tars and coke are heated to drive off the acid.
In addition to recovering certain valuable I products from the acid tars we secure an added advantage, namely the forming of a usable residue and one which may be readily handled. It may not be necessary in all cases to mix the acid tars or sludge acid with carbonaceous material when the sole object in view is the recovery of the by-products of the acid tars such as those mentioned, and other material might be substituted for the comprises,
carbonaceous material so as to give a residue which is easily handled and disposed of. However, since carbonaceous material has been found to be satisfactory and the residue is a valuable product, namely a valuable fuel, We prefer to employ such carbonaceous ma terial with the acid tars or sludge acids.
lVhile we have described the invention in some detail, it is to be understood that the details may be changed without departing from the invention as defined in the ap pended claims.
e claim:
1. The method of utilizing acid tars which mixing the same with finely divided carbonaceous material, compressing the mixture into briquettes, and roasting to drive off the acid.
2. The method ofutilizing petroleum coke and acid tars resulting from the refining of petroleum which comprises, mixing the finely divided coke with the acid tars, compressing the mixture into briquettes, and roasting the briquettes to drive off the acid.
3. The method which comprises, pulverizing carbonaceous material. mixing the same with acid tars while heated, forming the mixture into briquettes, and then roasting to drive ofi the acid.
a. A briquette formed of finely divided carbonaceous material and a binder of acid tars, said briquette being readily ignit-able, of high fuel value, leaving substantially no ash residue, and relatively compact and tough to withstand rough handling.
5. The method which comprises, mixing acid tars with carbonaceous material, then heating the mixture to drive ofi' volatile products and collecting those products.
LEMUEL M. JOHNSTON. JAMES L FARRELL.
US90409A 1926-02-24 1926-02-24 Briquette and method of manufacture Expired - Lifetime US1655728A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US90409A US1655728A (en) 1926-02-24 1926-02-24 Briquette and method of manufacture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US90409A US1655728A (en) 1926-02-24 1926-02-24 Briquette and method of manufacture

Publications (1)

Publication Number Publication Date
US1655728A true US1655728A (en) 1928-01-10

Family

ID=22222652

Family Applications (1)

Application Number Title Priority Date Filing Date
US90409A Expired - Lifetime US1655728A (en) 1926-02-24 1926-02-24 Briquette and method of manufacture

Country Status (1)

Country Link
US (1) US1655728A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2494420A (en) * 1947-10-09 1950-01-10 Carnegie Illinois Steel Corp Process of utilizing acid sludge
US2530459A (en) * 1947-08-26 1950-11-21 Hanna Furnace Carbon supplying composition
US2591496A (en) * 1946-08-06 1952-04-01 Walter G Berl Coking coal
US2808370A (en) * 1953-10-12 1957-10-01 Great Lakes Carbon Corp Metallurgical coke
US3020210A (en) * 1955-02-24 1962-02-06 Exxon Research Engineering Co Heat hardening fluid coke compactions

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2591496A (en) * 1946-08-06 1952-04-01 Walter G Berl Coking coal
US2530459A (en) * 1947-08-26 1950-11-21 Hanna Furnace Carbon supplying composition
US2494420A (en) * 1947-10-09 1950-01-10 Carnegie Illinois Steel Corp Process of utilizing acid sludge
US2808370A (en) * 1953-10-12 1957-10-01 Great Lakes Carbon Corp Metallurgical coke
US3020210A (en) * 1955-02-24 1962-02-06 Exxon Research Engineering Co Heat hardening fluid coke compactions

Similar Documents

Publication Publication Date Title
US1655728A (en) Briquette and method of manufacture
US3707461A (en) Hydrocracking process using a coal-derived ash
US2008146A (en) Structural activated carbon and process of making same
US1929860A (en) Process of producing fuel briquettes
US4135983A (en) Method for improving coking property of coal for use in production of cokes
US1968847A (en) Structural adsorptive carbon and process of making same
US1968846A (en) Process of making structural adsorptive carbon and product
US1512427A (en) Fuel-producing process and product
US1903237A (en) Method of producing a carbonized fuel briquette
US1815918A (en) Method of coking petroleum residues
US2199841A (en) Method of treating hydrocarbon mixtures
US1899808A (en) Process of coking carbonizable material
US1864720A (en) Method of distilling hydrocarbons and producing coke and product thereof
US2008147A (en) Manufacture of compressed carbonaceous materials and activated carbon
US2091711A (en) Medium temperature carbonization of coal
US1512577A (en) Process for the distillation of bituminous coal
US1793014A (en) Fuel and method of making same
US1838884A (en) Method of producing fuel
US1334170A (en) Ginia
US1814745A (en) Composition of and method for the treatment of hydrocarbon compounds
US2162989A (en) Method of producing fuel briquettes
US1845917A (en) Method of destructive distillation of wood waste
US1477642A (en) Distilling materials in contact with porous substances
US1916306A (en) Carbonaceous fuel and method op producing same
DE584607C (en) Process for the production of coke with the simultaneous production of light oils