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US1580299A - Process for briquetting wood particles and product thereof - Google Patents

Process for briquetting wood particles and product thereof Download PDF

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Publication number
US1580299A
US1580299A US3796A US379625A US1580299A US 1580299 A US1580299 A US 1580299A US 3796 A US3796 A US 3796A US 379625 A US379625 A US 379625A US 1580299 A US1580299 A US 1580299A
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US
United States
Prior art keywords
particles
parts
briquet
briquetting
during
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
US3796A
Inventor
Hall H Holdaway
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.)
A B FLICKINGER
FLICKINGER AB
LEROY F PIKE
Original Assignee
FLICKINGER AB
LEROY F PIKE
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 FLICKINGER AB, LEROY F PIKE filed Critical FLICKINGER AB
Priority to US3796A priority Critical patent/US1580299A/en
Application granted granted Critical
Publication of US1580299A publication Critical patent/US1580299A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • C10L5/40Solid fuels essentially based on materials of non-mineral origin
    • C10L5/44Solid fuels essentially based on materials of non-mineral origin on vegetable substances
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Definitions

  • My invention has for its object the compacting into briquets of cellulose material
  • terial is dried is brought up to a heat of about 300 Fahrenheit and this may advantageously be a continuation of the. drying step.
  • the briquet in fact' becomes as hot as possible without actually combusting.
  • a chemical gas during, or immediately following the drying step, which gas has a tendency to prepare the outside of each particle of material for interlocking or, agglomeration under the subsequent pressing step.
  • the dried and treated shavings are then immediately intro- 1 **d into-a closed chamber and while having an initial temperature of from 250? to 350 Fahrenheit derived from the above drying and preheating, are immediately compressed to about one sixth of their free volume during which the temperature will rise to from 450 to 500 Fahrenheit.
  • the pressure is then relieved and the smoking briquet, so hot that it has changed color on account of commencing to carbonize, is ejected from the press as a finished article.
  • the chemical gas above described may be injected as a gas or may begasified from a minute quantity of the liquid mixture injected into the mass in the press before, or during compression.
  • the method of briquetting comminuted wood material which consists of drying the material preheating the material to substantially 300 Fahrenheit within an envelope of organic gas and then while so heated rapidly compressing the material into a briquet whereby the temperature during compression 1s raised above 450 Fah- 'renheit.

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Chemical And Physical Treatments For Wood And The Like (AREA)

Description

Patented Apr. .13, 192a.
UNITED STATES PATENT OFFICE.
HALL H. HOLDAWAY OE LOS ANGELES, CALIFORNIA, ASSI GNOB 'I'O LEROY I. PIKE AND A. B. FLICKINGER, BOTH OF RENO, NEVADA.
No Drawing.
To all whom it concern:
Be it known that I, HALL H. HOLDAWAY,
' citizen of the United States, residing at Los Angeles, county of Los Angeles, State of California, have invented new and useful Improvements in Processes for Briquetting Wood Particles and Product Thereof, of which the following is a specification.
My invention has for its object the compacting into briquets of cellulose material,
such as sawdust, wood pulp, shavings and the like, and this object I attain by compressing the wood material under conditions of predetermined initial and final temperatures and pressure. a
In some instances to secure a superior result I have also found it advantageous to treat the material during the process steps with a gaseous mixture which appears tohave the quality of softening the surfaces of the particles so that under pressure the surface fibre of the adjacent particles more securely interlocks or binds together thus forming an integral mass in the press, which retains its shape and dimensions'when released.
I do not employ any binder or other'material toefl'ect a cementation between the.
particles, but rather I treat theparticles by conditioning their surfaces such that they will adhere to adjacent similarly heated particles when-brought together in intimate contact by pressure.
I have found that when the comminuted ,Wood particles are dried by expelling the entrained moisture and are then preheated and the temperature further increased during actual contact between the surfaces of the particles an adherence of the particles results to a degree suflicient to form a briquet of permanence, (efficiency and commercial value. 7
While my process is adapted to various woods, I have chosen below a specific example of its employment in connection with Oregon pine shavings or sawdust or will waste as a raw material. This is first thoroughly dried by any conventional means, and I have found that blowing the material through a tube or compartment with dry .hot air is sufficient. After the raw ma.-
lpplication filed January 21, 1925. Serial lilo. 3,796.
terial is dried is brought up to a heat of about 300 Fahrenheit and this may advantageously be a continuation of the. drying step.
While in this heated condition it is passed directly into a press and rapidl pressed to about one sixth of its normal ree volume. The act of compressing the material results in raising the temperature of the particles while beingpressed together and of the resulting briquetted mass to from 450 to 500 Fahrenheit. ,It is under this final extreme heat that the material takes its final set by the particles adhering together in briquet form in the press. Y
The briquet in fact' becomes as hot as possible without actually combusting. The
increase temperature is reached almost instantly during the pressing operation and I the smoking briquets are immediately freed from press and allowed to cool.
As a variation of the above process giving excellent results with certain woods, I inject a chemical gas during, or immediately following the drying step, which gas has a tendency to prepare the outside of each particle of material for interlocking or, agglomeration under the subsequent pressing step. I have found a mixture of alco- 1101, water, formaldehyde and earbolic acid which, when gasified during the drying or preheating step in the presence of the material to the briquetted will increase the adhering qualities of the particles and secure their close' compacting and adherence when the final briquetting pressure and temperature is reached.
As an example of the employment of such a gas in practicing my process, I pass wood shavings and comminuted through-atubular member by blowing the material therethrough with hot dry air, and at the same time I inject into the said compartm'ent less than one one-ten-thousandth mill waste by weight, of a mixture consisting substantially of one partcarbolieiacid, three parts formaldehyde, forty-eight parts alcohol and sixty-four parts of water. The dried and treated shavings are then immediately intro- 1 duced into-a closed chamber and while having an initial temperature of from 250? to 350 Fahrenheit derived from the above drying and preheating, are immediately compressed to about one sixth of their free volume during which the temperature will rise to from 450 to 500 Fahrenheit. The pressure is then relieved and the smoking briquet, so hot that it has changed color on account of commencing to carbonize, is ejected from the press as a finished article.
If preferred, the chemical gas above described may be injected as a gas or may begasified from a minute quantity of the liquid mixture injected into the mass in the press before, or during compression.
I claim:
1. The method of briquetting comminuted wood material which consists of drying the material preheating the material and then while so heated rapidly compressing the materialinto a briquet to substantially one sixth of its free-volume.
2. The method of briquett-ing comminuted wood material which consists of drying the anaterial preheating the material to Sllb.
stantially 300 Fahrenheit and then while so heated rapidly compressing the material into a briquet to substantially one sixth of its free volume.
3. The method of briquetting comminuted wood material which consists of drying the material within an envelope of organic gas, preheating the material and thenwhile so heated rapidly compressing the material into a briquet whereby the temperature during compression is raised above 450 Fahrenheit.
4. The method of briquetting comminuted wood material which consists of drying the material preheating the material and then while so heated rapidly compressing the material into a briquet to substantially one sixth of its free volume whereby the temperature during compression is raised above 450 Fahrenheit.
5. The method of briquetting comminuted wood material which consists of drying the material preheating the material to substantially 300 Fahrenheit within an envelope of organic gas and then while so heated rapidly compressing the material into a briquet whereby the temperature during compression 1s raised above 450 Fah- 'renheit.
6. The method of briquetting comminuted wood material which consists of drying the material preheating the material to substantially 300 Fahrenheit and. then while so heated rapidly compressing the material into a briquet to substantially one sixth of its free volume, whereby the temperature during compression is raised above 450 Fahrenheit.
3 7. The method of briquet-ting comminuted wood material-which consists of drying the materialpreheating the material while ex tion of a gas composed of substantially one part carbolic acid, three parts formaldehyde, forty-eight parts alcohol and sixty-four parts of water and then while so heated immediately compressing the material into a briquet.
10. The process set forth in claim 4 wherein during the process the material particles are exposed to the action of a. gas.
11. The process set forth in claim 6 wherein during the process the material particles are exposed to the action of a gas.
12. The process set forth in claim 1 wherein during the process the material particles are exposed to the action of a gas composed of substantially onepart carbolic acid, three parts formaldehyde, forty-eight parts alcohol and sixty-four parts of water.
13. The process set forth in claim 2 wherein during the process the 'material particles are exposed to the action of a gas composed of substantially one .part carbolic acid, three parts formaldehyde, forty-eight parts alcohol and sixty-four parts of water.
14. The process set forth in .claim 3 wherein during the process the material particles are exposed to the action of a gas composed of substantially one part carbolic acid, three parts formaldehyde, forty-eight parts alcohol and sixty-four parts of water.
15. The process set forth in claim 4 wherein during the process the material particles are exposed to the action of a of substantially one part carbo 0 acid, three parts formaldehyde, forty-eight parts alcohol and sixty-four parts of water.
16. The process set forth in claim 5 wherein during the process the material particles are exposed to the action of a gas composed of substantially one part carbolic acid, three parts formaldehyde, forty-eight parts alcohol and sixty-four parts of water.
17. 'The process set 'forth in claim 6 wherein during the. process the material particles are exposed to the action of a gas composed of substantially one part carbolic acid, three parts formaldehyde, forty-eight parts alcohol and sixty-fourparts of water.
18. The method of briquetting comminuted wood material whichconsists of drying the material, and then preheating the material 'in a stream of'organic gas and then lgias composed a while so heated, compressing the material into a briquet of substantially one sixth of the-volume of the comminuted particles.
19. The method of bt'iquetting commi- 5 nuted Wood material which consists of drying the material, then pr terial to substantially 300 eheatin the ma- F'. while confined in an envelope and therefore exposed to the action of an organic gasand then while so heated, immediately compressing the material into a briquet of substantially one sixth of the volume of the comminuted particles HALL H. HOLDAWAY.
US3796A 1925-01-21 1925-01-21 Process for briquetting wood particles and product thereof Expired - Lifetime US1580299A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2525624A1 (en) * 1982-04-23 1983-10-28 Shell Int Research PROCESS FOR THE PRODUCTION OF FUEL AGGLOMERS FROM ORGANIC FIBROUS MATERIAL
US5486217A (en) * 1992-10-23 1996-01-23 Biehl; Brent G. Cellulosic composition

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2525624A1 (en) * 1982-04-23 1983-10-28 Shell Int Research PROCESS FOR THE PRODUCTION OF FUEL AGGLOMERS FROM ORGANIC FIBROUS MATERIAL
US5486217A (en) * 1992-10-23 1996-01-23 Biehl; Brent G. Cellulosic composition

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