US722071A - Still. - Google Patents
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- US722071A US722071A US12935502A US1902129355A US722071A US 722071 A US722071 A US 722071A US 12935502 A US12935502 A US 12935502A US 1902129355 A US1902129355 A US 1902129355A US 722071 A US722071 A US 722071A
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- Prior art keywords
- ether
- alcohol
- condenser
- conduit
- column
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/001—Processes specially adapted for distillation or rectification of fermented solutions
- B01D3/003—Rectification of spirit
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
PATENTED MAR. 3., 1903.
G. F. AHLERS.
STILL.
APPLICATION FILED 00130, 1902.
5] n man 170':
N0 MODEL.
lJNlTED STATES ATET OFFICE.
GEORGE F. AHLERS, OF COVINGTON, KENTUCKY, ASSIGNOR TO HOFFMAN, AI'ILERS (h COMPANY, OF CINCINNATI, OHIO, A CORPORATION.
STILL.
SPECIFICATION forming part of Letters Patent No. 722,071, dated March 3, 1903.
Application filed October 30, 1902. Serial No. 129,355. (No model.)
To all whmn it may concern:
Be it known that I, GEORGE F. AHLEns, a citizen of the United States, residing at Covington, in the county of Kenton and State of 5 Keutucky,have invented certain new and useful Improvements in Stills, of which the following is a specification.
My invention relates to an improved apparatus for distilling ether and alcohol from spirits such as commercial high-wines.
The objects of my invention are, first, to separately recover the distilled other at the beginning of the operation; second, to separately collect the alcohols of the different I proofs absolutely free from contaminating ether, and, third, to rapidly and efficiently recover the low-proof alcohol remaining in the residue of the charge after the ether and higher-proof alcohol have been separately collected.
Other objects of my invention relate to the production of simple devices for accomplishing these objects incorporated into one continuously-operating system.
The features of my invention will be more fully set forth in the description of the accompanying drawing, forming a part of this specification, in which the figure is a side elevation of my apparatus with various parts shown in 0 section.
A represents the ordinary rectifying apparatus, having the usual blow-off pipe a and steam heating-coil a. B represents the conduit leading from the dome of this apparatus to the base of the ordinary refining-column C, having therein the ordinary series of boiling-pipes b and drip-pans c. From the top of this refining-column a pipe D leads to the usual goose-condenser E, in which d represents the goose-coil. e represents a returnpipe tapping the pipe f, which in turn taps the bottom of the goose-coil d, whereby the alcohol condensed in the chamber E returns to the dripping-pans in column C. F repre- 5 sents a pipe leading from the goose-coil d to the final condenser G, which discharges into the alcohol-separating box H. These parts and arrangements are of the ordinary construction in the present mode of refining highwines. As the operation was conducted in this apparatus, at the beginning of a given operation there remains collected in the drip- .pans of the column C the second grade of al cohol left over from the previous operation.
At the beginning of this new operation the ether is first driven off and passes upwardly through the column C, boiling the alcohol held in the series of pans and being absorbed largely thereby. So much of the ether as is not absorbed in the column C and not condensed in the condenser E passes over and is condensed in the final vertical condenser G, where it is separated from the first-grade alcohol. As the result of this operation all the alcohol held by the column C is badly contaminated by the ether and the Whole system is fouled with the ether-vapors. So much of the alcohol as becomes contaminated with the ether-vapor at this primary portion of the distillation is an impure mixture requiring 7o redistillation at a constant loss to render it suitable for commercial uses. In order to avoid this loss of alcohol and theconsequent loss of time, in order to keep the apparatus pure, and in order to separately collect the different products in condition suitable for commercial purposes and free from alcohol,
I have provided the following instrumentalities:
I represents an ether-conduit leading from So the top of the conduit B to the top of an ethercondensing tank J, having condensing-tubes g therein.
K represents a separatingbox for the ether, communicating by means of a pipe h with the condenser J.
j represents a pipe leading from the separating-box to the ether-reservoir L, where it is stored under air-pressure for distribution as needed. 0
70 represents a valve in the pipe I. The ordinary charging-pipes, gages, &c., of the distilling apparatus are shown, but need not be described.
Z represents Water-inlet pipes entering the 5 pipe B and provided with the valve m.
M represents a water-pipe leading from the bottom of the column C into the distilling vessel A. It is provided with the cook 41.
0 represents a draw-off pipe leading from [00 the bottom of the column 0 for draining.
Mode of operation: The old charge having the bottom of column 0 are Water-sealed.v
The water-level is raised in the column 0 and in the alcohol-conduit B to a level slightly below the level at which the ether-conduit I communicates with said conduit B. N represents an air-compressor communicating with the air-coil p in the steam-heating chest 0, the said coil communicating with the vessel A through the top thereof. Q represents a steam-inlet to said chest, and R the steamoutlet. .9 represents a perforated distributing hot-air coil in the bottom of the vessel A, supplied with a pipe leading from the coil p. The valve being open, n closed, and a water-level established as directed, heat is applied to the charge, and the compressed hot air from the coil 19 is supplied to the bottom of the charge, thoroughly agitating the same and supplying the oxidizing agent in a condition best adapted to liberate the ether. The ether being driven off at a lower temperature than the evaporating-point of alcohol is rapidly expelled from the charge, and being shut off by the water seal from entrance into the column 0 it enters the ether-condensing systemthroughthepipel. Thecondensed liquid is drawn oif and tested from time to time, and the operation is allowed to continue as long as the tests showthe ether to be pure. When these tests show that the ether is all driven oi, the valve 70 is closed, the valve it opened, discharging the water from the column, and the alcohol,entirely free from ether, is allowed to pass though the alcohol-condensing system. When the operation has been continued until all of the high-proof alcohol has been elimi nated from the charge, a small per cent. of lowproof alcohol remains, which as the operation was carried on heretofore was either wasted in the blow-off or driven at the expense of considerable time and heat. With my apparatus, when this stage of the operation is reached I again treat the charge to the agitation and oxidation of the hot compressed air, which quite rapidly and economically drives 0d the low-proof alcohol remaining in the charge, so saving all the alcohol without the loss of additional time, heat, and labor.
By this apparatus and operation I produce for the first time in one apparatus and one continuous operation a commercially-pure ether and a commercially-pure alcohol of two grades, these three products being separately collected.
Having described my invention, I claim 1. In combination with a distilling vessel, an alcohol-condensing chamber, a conduit leading from the top of the distilling vessel to the bottom of the condenser, means for supplying water to and draining water from said condenser, an ether-condenser, a conduit connecting the said ether-condenser with the said alcohol-conduit, avalve in the said ether-conduit, means for separately collecting the condensed alcohol and the condensed ether, and means for establishing awater seal in the alcohol-condenser, whereby communication is shut off between the same and the distilling vessel during the primary operation in which the ether is supplied to its separate condensing system, substantially as described.
2. In combination with a distilling vessel, an alcoholcondensing chamber, a conduit leading from the top of the distilling vessel to the bottom of the condenser, means for supplying water to and draining water from said condenser, an ether-condenser, a conduit connecting the said ether-condenser with the said alcohol-conduit, a valve in the said ether-conduit, means for separately collecting the condensed alcohol and the condensed ether, and means for establishing a water seal in the alcohol-condenser,wherebycommunicationis shut off between the same and the distilling vessel during the primary operation in which the ether is supplied to its separate condensing system, and means for supplying hot compressed air through the distilling vessel, substantially as described.
In testimony whereof I have hereunto set my hand.
GEO. F. AHLERS.
Witnesses:
OLIVER B. KAISER, IDA J. LUCAS.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12935502A US722071A (en) | 1902-10-30 | 1902-10-30 | Still. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12935502A US722071A (en) | 1902-10-30 | 1902-10-30 | Still. |
Publications (1)
Publication Number | Publication Date |
---|---|
US722071A true US722071A (en) | 1903-03-03 |
Family
ID=2790586
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US12935502A Expired - Lifetime US722071A (en) | 1902-10-30 | 1902-10-30 | Still. |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3530043A (en) * | 1968-07-04 | 1970-09-22 | Ici Ltd | Purification of vinyl or allyl acetate by treatment with alkali metal compounds during distillation and evaporation with purging of concentrate streams |
US3530044A (en) * | 1968-03-04 | 1970-09-22 | Ici Ltd | Purification of vinyl or allyl acetate by treatment with a lithium compound during distillation and with a sodium or potassium salt during evaporation |
-
1902
- 1902-10-30 US US12935502A patent/US722071A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3530044A (en) * | 1968-03-04 | 1970-09-22 | Ici Ltd | Purification of vinyl or allyl acetate by treatment with a lithium compound during distillation and with a sodium or potassium salt during evaporation |
US3530043A (en) * | 1968-07-04 | 1970-09-22 | Ici Ltd | Purification of vinyl or allyl acetate by treatment with alkali metal compounds during distillation and evaporation with purging of concentrate streams |
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