US284058A - Method of distilling and charring wood and kiln therefor - Google Patents

Method of distilling and charring wood and kiln therefor Download PDF

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US284058A
US284058A US284058DA US284058A US 284058 A US284058 A US 284058A US 284058D A US284058D A US 284058DA US 284058 A US284058 A US 284058A
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wood
kiln
distilling
gases
charring
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B49/00Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/02Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
    • C10B49/04Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated

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  • the object of my invention is to withdraw from a charring chamber kiln, or oven the gases evolved in the carbonization of wood, to convey them through one or more condensers, and to project the uncondensed portion of these gases into a furnace for fuel purposes.
  • the figure of the drawing represents a vertical longitudinal section of a charcoalkiln and of a condensing apparatus connected therewith.
  • V D is the flue through which the uncondensed gases are exhausted.
  • K K are air-inlets, and H H are gasoutlet-s.
  • E is a steam-pipe, and G is a steanrejector.
  • S S are dampers in fines C C.
  • the operation of the above-described apparatus is as follows: The kiln is first filled with wood. Then it is closed and hermetically sealed, excepting at the bottom, where the holes K K are kept open for the admission of air. Fire is then communicated to the wood in the kiln, and the carbonization of the charge commences.
  • vents H H In the ordinary process of making charcoal the gases thrown off as the charring progresses find egress through the vents H H. In my method these vents H H are closed, and the gases evolved are steadily exhausted from the kiln A through fines C C, and through the condensers B B and flue D, by means of steamejector G.
  • This liquid pyroligneons acid is treated in the usual manner for acetic acid, acetate of lime, wood alcohol, and tarry compounds.
  • the uncondensable gases are withdrawn from the exit end of condenser B and driven through flue D to the fur nace, where they are used for fuel.
  • these uncondensable gases become irregular, fitful, and highly inflammable.
  • these gases may be for fuel purposes, it is highly dangerous to use them when in this condition, owing to their tendency to violent explosions in kilns constructed and operated in the usual manner.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Coke Industry (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Description

(No Model.)
H. M. PIERO EH METHOD OF DISTILLING AND GHARRING WOOD AND KILN THEREFOR. No. 284,068. Patented Aug. 28, 1883.
/ v a z N. vmzns, mwum nur. Wm: n nnnn n.
' B B, condensers.
lTED STATES PATENT OFFICE.
HENRY M. PIERCE, OF CHICAGO, ILLINOIS.
METHOD OF DISTILLING AND CHARRING WOOD A ND KILN THEREFOR.
SPECIFICATION forming part of Letters Patent No. 284,058, dated August 28, 1883.
Application filed June 2,1883.- (No model.)
To aZZ whom it may concern.-
Be it known that I, HENRY M. PIERCE, a citizen of the United States, residing at Chicago, in the county of Cook and State of Illinois, have invented certain new and useful Improvements in Methods of Distilling and Charring \Vood and Kilns therefor; and I do here by declare that the following is a full, clear, and exact description of the invention, which will enable others skilled in the art to which it appertains to make and use the same, reference being had to the accompanying drawing, and to the letters of reference marked thereon, which forms part of this specification.
The object of my invention is to withdraw from a charring chamber kiln, or oven the gases evolved in the carbonization of wood, to convey them through one or more condensers, and to project the uncondensed portion of these gases into a furnace for fuel purposes.
The figure of the drawing represents a vertical longitudinal section of a charcoalkiln and of a condensing apparatus connected therewith. I
A is the kiln in which the wood is treated; C C are fiues respectively connecting the top and bottom of the kiln A with condensing apparatus B B. V D is the flue through which the uncondensed gases are exhausted. K K are air-inlets, and H H are gasoutlet-s. E is a steam-pipe, and G is a steanrejector. S S are dampers in fines C C.
The operation of the above-described apparatus is as follows: The kiln is first filled with wood. Then it is closed and hermetically sealed, excepting at the bottom, where the holes K K are kept open for the admission of air. Fire is then communicated to the wood in the kiln, and the carbonization of the charge commences.
In the ordinary process of making charcoal the gases thrown off as the charring progresses find egress through the vents H H. In my method these vents H H are closed, and the gases evolved are steadily exhausted from the kiln A through fines C C, and through the condensers B B and flue D, by means of steamejector G.
WVhen the resinous wood of the South is being treated in kiln A for charcoal, the flue C is used in the earlier stages of the process, and before the dry distillation of the wood actually commences, for withdrawing and econo mizing the turpentine vapors that first come over with the vapors of the water held. free in the body of the wood. After all the turpentine has been distilled over and condensed in vessels B B, damper S in fine C is closed and damper Sin flue C opened, and this arrangement of flue and damper maintained until the close of the operation. In passing through the condensers or coolers B B about three quarters in weight and volume of these gases are reduced to liquid form. This liquid pyroligneons acid is treated in the usual manner for acetic acid, acetate of lime, wood alcohol, and tarry compounds. The uncondensable gases are withdrawn from the exit end of condenser B and driven through flue D to the fur nace, where they are used for fuel. As the process of carbonization of thewood in the kiln advances, these uncondensable gases become irregular, fitful, and highly inflammable. However valuable these gases may be for fuel purposes, it is highly dangerous to use them when in this condition, owing to their tendency to violent explosions in kilns constructed and operated in the usual manner. These eX- plosions extend backward through flue D, condensers B B, to kiln A, with danger to operatives and injury to fines and condensing apparatus. At such periods my application of the steam-ejector is not only most beneficial, but absolutely necessary to the utilization of these gases with safety. The steanrejector, applied at or near the point where the uncondensable gases issue from the condenser, moistens these gases, distributes them through steam-vapors, and projects them in a strong current to the place of combustion without diminishing their value as a fuel. The value and importance of this application of the steamejector are better appreciated when we realize the fact that these uncondensable gases contain about twenty per cent. of the heat-generating power of wood-that is, they represent twenty per cent of the full value of the wood.
Havingdescribedmyinvention,whatIclaim, and desire to secure by Letters Patent, is-
1. The method of distilling and charring IOO tion with steam-nozzle G, for the purpose of moistening, giving body to, and projecting the non-condensable gases cooled in the carboni- 15 zation of wood to a place of combustion.
In testimony that I claim the foregoing as my own I affix my signature in presence of two witnesses.
HENRY M. PIERCE.
i VVitnesses:
DENNIS CHURCH, WILLARD WARNER.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4280878A (en) * 1979-10-30 1981-07-28 Sprenger Gerald E Structure and process for reclaiming heat from charcoal production facility

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4280878A (en) * 1979-10-30 1981-07-28 Sprenger Gerald E Structure and process for reclaiming heat from charcoal production facility

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