US748457A - Apparatus for continual charring and dry distillation of organic substances. - Google Patents
Apparatus for continual charring and dry distillation of organic substances. Download PDFInfo
- Publication number
- US748457A US748457A US15359003A US1903153590A US748457A US 748457 A US748457 A US 748457A US 15359003 A US15359003 A US 15359003A US 1903153590 A US1903153590 A US 1903153590A US 748457 A US748457 A US 748457A
- Authority
- US
- United States
- Prior art keywords
- chamber
- charring
- continual
- organic substances
- dry distillation
- 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
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B7/00—Coke ovens with mechanical conveying means for the raw material inside the oven
- C10B7/14—Coke ovens with mechanical conveying means for the raw material inside the oven with trucks, containers, or trays
Definitions
- This invention relates to an apparatus for continual charring or, generally speaking, for dry distillation of organic substances;
- the object of the invention is to provide an apparatus in which the charring process is efiected in the same manner as in charcoal piles-z'. e., in vertical direction from the top to the bottom.
- Figure 1 is a vertic-a1 sectional view of the distilling chamber or furnace.
- Fig. 2 is atop view of the entire apparatus, partly in section. tion on the line 3 3 of Fig. 1.
- Fig. 4 is a section on the line 4 4 of Fig. 1, and
- Fig. 5 is a cross-section of the apparatus through the passage for leading away the products of the condensed gases.
- 1 is the distilling-furnace consisting of an inclined extended chamber made of bricks or other suitable material.
- the outsides of the walls are preferably covered with sand or other insulating'substance.
- 2 2 are tracks extending along the chamber and supporting trucks 3, which carry the substance to be.
- the said chamber 1 is at both ends divided into two compartments 4 4 and 5 5, respectively, separated from the chamber proper by means of gates 66 and 7 7, suspended in chains 8, passing over pulleys 9 and provided with counterweights 10.
- the outerends of the said compartments are closed by gates 11 11 and 12 12.
- one of the gates 6 is closed and the other opened.
- At the lower end of the chamber means are provided for bringing the trucks into the chamber.
- the said means consist of chains 14, passing round pulleys 13, suitably journaled under the chamber.
- One end of the chain is fixed to a rod 15, mounted in a channel 16 and passing through Fig. 3 is a sec-.
- the top end of the chamber 1 is connected with a regenerator 18 by means of a channel 19.
- the said regenerator consists of two chambers and is arranged in usual manner.
- 20 is a furnace, and 21 is a chimney, which is connected with the said chambers alternately.
- the lower end of thechamber 1 is connected with condensers 23 by means of a channel 22.
- the said condensers may be of any suitable construction and are therefore not described.
- 24 is a fan connected with the said condensers and the regenerator.
- the heat necessary for the char-ring process is effected by the gas generated in the furnace 20, which is burned in one of the chambers of the regenerator 18 and then passes to the chimney 21.
- Gases generated in the chamber 1 during the charring process are drawn by the fan 24 from the lower end of the said chamber through the channel 22 and into the condensers 23.
- the non-condensable part of the said gases which consists of carbonic acid,carbonic oxid, and some hydrocarbons, is forced by the fan 24 through the other chamber of the regenerator 18, which chamber has previously been heated in the same manner as. the chamber first mentioned.
- the gases last mentioned enter the top end of the chamber lthrough the channel 19 and pass through the entire chamber, the greater part of their heat being successively transmitted during the said passage to the substance to be charred. They are then again, together with gases generated during the chat-ring process, sucked through the condensers and circulated in the said manner until the temperature of the gases when leaving the regenerator is insufficient for the charring process.
- the gas-current is then led through the other heated chamber of the regenerator, and the first chamber of the same is heated by means of gas from the generator 20.
- the excess of combustible noncondensable gases generated during the charring process is led into the chamber of the regenerator which is being heated and is burned in the same.
- the products resulting from the condensation of gases in the chamber 1 may be led away from said chamber to a suitable receptacle by the way of a passage 26.
- a suitable receptacle In consequence of the said circulation the substance situated in the top end of the chamber 1 will be subjected to the comparatively highest temperature. In this manner the substance is thoroughly charred in the top part of the chamber While being successively and preparatively heated in the lower part of the chamber, the charring process being thus continuous and executed in the same manner as in piles.
- a charring and distilling apparatus the combination of an extended, inclined chamber, means for transporting the substance to be charred from the lower end of the chamber to its top end, means for introducing heated gas into the said top end, and outlet-openings for the gas at the lower end substantially as described.
- a charring and distilling apparatus the combination of an extended, inclined chamber, means for transporting the substance to be charred from the lower end of the chamber to its top end, means outside the chamber for conveying gases from the said lower end into the top end and means for heating the said gases before entering the chamber, substantially as described.
- a charring and distilling apparatus the combination of an extended, inclined chamber, means for successively transporting the substance to be charred from the lower end of the chamber to its top end, a passage leading gases generated in the chamber from its lower end to the top end, and condensers, a fan and a heatingdevice mounted in the said passage between the said lower end and the top end, substantially as described.
Description
No. 748,457. PATBNTED DEC. 2: H. 0. AMINOFF.
APPARATUS FOR UONTINUAL GHARRING AND DRY DISTILLATIUA ORGANIC SUBSTANCES;
APPLIOATION FILED APR. 21, 1903.
Si N Q UNITE STATES Patented December 29, 1903.
PATENT ()FFICE.
HINRIK OONSTANTIN AMINOFF, OE DOMNARFVET, SWEDEN, ASSIGNOR TO ANDERS CONRAD MARK, OF GOTHENBURG, SWEDEN.
APPARATUS FOR CONTINUAL CHARRING AND DRY DlSTlLLATION OF ORGANIQ SUBSTANCES.
SPECIFICATION forming part of Letters Patent No. 748,457, dated December 29, 1903. Application filed April 21, 1903. Serial Nol53.590. (N model.)
bad therein to the accompanying drawings.
This invention relates to an apparatus for continual charring or, generally speaking, for dry distillation of organic substances; and
, the object of the invention is to provide an apparatus in which the charring process is efiected in the same manner as in charcoal piles-z'. e., in vertical direction from the top to the bottom.
In the accompanying drawings,which serve to illustrate the invention, Figure 1 is a vertic-a1 sectional view of the distilling chamber or furnace. Fig. 2 is atop view of the entire apparatus, partly in section. tion on the line 3 3 of Fig. 1. Fig. 4 is a section on the line 4 4 of Fig. 1, and Fig. 5 is a cross-section of the apparatus through the passage for leading away the products of the condensed gases.
1 is the distilling-furnace consisting of an inclined extended chamber made of bricks or other suitable material. The outsides of the walls are preferably covered with sand or other insulating'substance. 2 2 are tracks extending along the chamber and supporting trucks 3, which carry the substance to be.
charred. The said chamber 1 is at both ends divided into two compartments 4 4 and 5 5, respectively, separated from the chamber proper by means of gates 66 and 7 7, suspended in chains 8, passing over pulleys 9 and provided with counterweights 10. The outerends of the said compartments are closed by gates 11 11 and 12 12. In Fig. 4 one of the gates 6 is closed and the other opened. At the lower end of the chamber means are provided for bringing the trucks into the chamber. In the drawings the said means consist of chains 14, passing round pulleys 13, suitably journaled under the chamber. One end of the chain is fixed to a rod 15, mounted in a channel 16 and passing through Fig. 3 is a sec-.
a tube 17. When a truck is to be brought into the chamber, the gate 11 is opened and the truck pushed into the compartment 4. The said chain 14 is then connected with the rear end of the truck and the gate 11 is closed. When the gate 6 has been opened, the truck is advanced by pulling in the rod 16, which is connected with a winch or the like. (Not shown in the drawings.) Finally the gate 6 is closed. In this manner the tracks are suc cessively filled with trucks so that when a new truck is drawn into the chamber at the lower end of the same the truck at the top end of the chamber will be pushed out simultaneously by the following trucks. The gates 7 and 12 are successively opened and closed in order to permitthe top truck being brought out of the chamber.
The top end of the chamber 1 is connected with a regenerator 18 by means of a channel 19. The said regenerator consists of two chambers and is arranged in usual manner. 20 is a furnace, and 21 is a chimney, which is connected with the said chambers alternately. The lower end of thechamber 1 is connected with condensers 23 by means of a channel 22. The said condensers may be of any suitable construction and are therefore not described. 24 is a fan connected with the said condensers and the regenerator.
The heat necessary for the char-ring process is effected by the gas generated in the furnace 20, which is burned in one of the chambers of the regenerator 18 and then passes to the chimney 21. Gases generated in the chamber 1 during the charring process are drawn by the fan 24 from the lower end of the said chamber through the channel 22 and into the condensers 23. At the same time the non-condensable part of the said gases, which consists of carbonic acid,carbonic oxid, and some hydrocarbons, is forced by the fan 24 through the other chamber of the regenerator 18, which chamber has previously been heated in the same manner as. the chamber first mentioned. The gases last mentioned enter the top end of the chamber lthrough the channel 19 and pass through the entire chamber, the greater part of their heat being successively transmitted during the said passage to the substance to be charred. They are then again, together with gases generated during the chat-ring process, sucked through the condensers and circulated in the said manner until the temperature of the gases when leaving the regenerator is insufficient for the charring process. The gas-current is then led through the other heated chamber of the regenerator, and the first chamber of the same is heated by means of gas from the generator 20. The excess of combustible noncondensable gases generated during the charring process is led into the chamber of the regenerator which is being heated and is burned in the same. The products resulting from the condensation of gases in the chamber 1 may be led away from said chamber to a suitable receptacle by the way of a passage 26. In consequence of the said circulation the substance situated in the top end of the chamber 1 will be subjected to the comparatively highest temperature. In this manner the substance is thoroughly charred in the top part of the chamber While being successively and preparatively heated in the lower part of the chamber, the charring process being thus continuous and executed in the same manner as in piles.
Having now described my invention, what I claim as new, and desire to secure by Letters Patent, is-
1. In a charring and distilling apparatus the combination of an extended, inclined chamber, means for transporting the substance to be charred from the lower end of the chamber to its top end, means for introducing heated gas into the said top end, and outlet-openings for the gas at the lower end substantially as described.
2. In a charring and distilling apparatus the combination of an extended, inclined chamber, means for transporting the substance to be charred from the lower end of the chamber to its top end, means outside the chamber for conveying gases from the said lower end into the top end and means for heating the said gases before entering the chamber, substantially as described.
3. In a charring and distilling apparatus the combination of an extended, inclined chamber, means for successively transporting the substance to be charred from the lower end of the chamber to its top end, a passage leading gases generated in the chamber from its lower end to the top end, and condensers,a fan and a heatingdevice mounted in the said passage between the said lower end and the top end, substantially as described.
In witness whereof I have hereunto signed my name in the presence of two subscribing witnesses.
HINRIK CONSTANTIN AMINOFF.
Witnesses:
ROBERT APALZREN, AUG SORCERSEN.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US15359003A US748457A (en) | 1903-04-21 | 1903-04-21 | Apparatus for continual charring and dry distillation of organic substances. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US15359003A US748457A (en) | 1903-04-21 | 1903-04-21 | Apparatus for continual charring and dry distillation of organic substances. |
Publications (1)
Publication Number | Publication Date |
---|---|
US748457A true US748457A (en) | 1903-12-29 |
Family
ID=2816951
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US15359003A Expired - Lifetime US748457A (en) | 1903-04-21 | 1903-04-21 | Apparatus for continual charring and dry distillation of organic substances. |
Country Status (1)
Country | Link |
---|---|
US (1) | US748457A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2804855A (en) * | 1952-02-23 | 1957-09-03 | Surface Combustion Corp | Furnace door construction |
-
1903
- 1903-04-21 US US15359003A patent/US748457A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2804855A (en) * | 1952-02-23 | 1957-09-03 | Surface Combustion Corp | Furnace door construction |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US748457A (en) | Apparatus for continual charring and dry distillation of organic substances. | |
US433800A (en) | Warren spear mayo | |
US704886A (en) | Apparatus for drying and distilling wood, sawdust, peat, or the like, and for treating other substances. | |
US1414401A (en) | Process for the destructive distillation of coal and other material | |
US786365A (en) | Non-oxidizing annealing-furnace. | |
US413306A (en) | Edward wilkes rathbijn | |
US978209A (en) | Dry-kiln. | |
US2112401A (en) | Apparatus for coking solid fuel briquettes | |
US374636A (en) | Half to ludwig hansen | |
US860483A (en) | Apparatus for carbonizing wood, peat, and the like. | |
US1500862A (en) | Drier | |
US3519540A (en) | Carbonizing oven having parallel horizontal flues and u-shaped air ducts | |
US1025419A (en) | Coke-oven. | |
US283643A (en) | Foubth to thomas p | |
US300385A (en) | Retort for carbonizing wood | |
US885308A (en) | Apparatus for the manufacture of gas. | |
US996943A (en) | Drier. | |
US715314A (en) | Brick-drier. | |
US568691A (en) | lekeux | |
US249972A (en) | Fruit-drier | |
US1678687A (en) | Apparatus for carbonization | |
US1355268A (en) | Process osi and oven fob the continuous distillation ob gasification oe | |
US1115453A (en) | Apparatus for treating coals and other hydrocarbonaceous substances. | |
US1603346A (en) | Kiln for the continuous destructive distillation of organic material | |
US1468990A (en) | Apparatus for drying brick and other clay articles |