US113811A - Improvement in petroleum-stills - Google Patents

Improvement in petroleum-stills Download PDF

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US113811A
US113811A US113811DA US113811A US 113811 A US113811 A US 113811A US 113811D A US113811D A US 113811DA US 113811 A US113811 A US 113811A
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dome
still
valve
vapor
pipes
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G7/00Distillation of hydrocarbon oils

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  • Fig. 3 shows another arrangement of the inside dome We, J OHN L. STEwARrand JOHN P. LOGAN, of
  • the mai-n features of our invention consist in the f arrangement of thepipes leading from the still to the central dome; inthe construction of a double-walled central dome, in which the vapor is partly condensed; and in the arrangement of the pipes and valve leading from the dome to the condenser.
  • Figure 2 is a vertical section.
  • Figure 3 is a modified form of the interior dome.
  • A is the still, which is nearly filled with crude oil B.
  • the bottom Oi' the still is formed in curved lines, as shown.
  • the top is formed of curved lines like a corrugated disk, the curve near the edge being convex, and having its highest point where the pipe C enters, about iive feet from the edge of the still, the whole diameter of the still being thirty feet.
  • This form of the top causes all the vapoi ⁇ to rise into the pipes C, which, in the still here described, are seventeen in number, and eight inches diameter, each one being placed over a fire.
  • the pipes C lead into a central dome, D, at a slight inclination downward, so that the condensed vapor will drain into the dome D.
  • the dome D is about twelve feet high; the upper part four feet in diameter; the lower part is widened to six feet, and secured tight to the top of the still.
  • dome D Within the dome D is another dome, E, three feet in diameter, thus leaving a space of six inches between the two domes for the passage of the vapor.
  • dome E The lower end of dome E is secured tight to the top of the still, a few small holes only being left at c' to permit the condensed vapor q to occupy the same level at the bottom of each dome.
  • dome E The top of dome E is closed, and extends in height to within six inches of dome D.
  • a valve, h operated by a screw and handle, h1, projecting through the dome D.
  • the condensed vapor is returned to the still by this valve h lthrough a trap, h2, which trap prevents the passage of vapor.
  • the condensed vapor4 g can be drawn od' by pipe It and cock r.
  • valve h in this case is arraiiged between the two shells.
  • a large twenty-inch pipe, K leads from the bottom of dome D, at a' few inches below the level at which the pipe C enters.
  • This pipe K is on a slight incline to the condenser, and laid close to the top of the still.
  • a sluice-valve, L, or a Ludlow valve is placed in the ⁇ pipe close to the dome, and a safety-valve, m, and a vacuum-valve, n, are placed as shown.
  • a twenty-inch pipe, P leads from the top of' the dome D and enters the pipe K beyond the valve L.
  • R R are man-holes.
  • the operation Of the still is in this way: The valve L is first closed, the still is nearly filled with crude oil, and a series ot' fires applied below.
  • the gasoline and benzine pass up the pipes G and into the dome D, where the vapor passes up the annular passage formed between the two domes, and is thus all forced in contact with the cooling surface ot' the dome D. 'lhe gasoline and benzine then pass down pipes P and K to the condenser.
  • the vapor condensed in the pipes C and domeD collects at the bottom of the dome D and runs into the 'dome E by the openings e'.
  • YIhe valve h is openduring this part of the operation', Aand theeondensed vapor passes back to the still through trap h.
  • valve Lv When all the benzine is evaporated the valve Lv is opened and the small one h closed, so that the condensed vapor is prevented from returning to the still, and passes along with the vapor through valve L and pipe K to the condenser.
  • valve h is opened and the condensation of the heavier hydrocarbon forms a liquid which returns to the still, the lighter vapor only passing off through valve L.
  • V lhe central dome D arranged upon thestll A in dome D, or its equivalent,v andstili A, for the purpose the manner shown, as a receptacle for the vapors that of returning the condensed vapor to the still, as herein pass from the still by the collecting-pipes C. described.
  • valve h arranged, in combination with the .K JNO. Gr. UMSTED.

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

'L y tlniit Y hm @ma @ffm JOHN| L. STEWART AND JOHhT P. LOGAN, 0F PHILADELPHIA, PENNSYLVANIA.
Letters Patent No. 113,811, dated April 18, 1871.
IMPROVEM NT IN.V PETROLEUM-STILLS.
The Schedule referred to in these LettersPatent and making part cxf the same.
Fig. 3 shows another arrangement of the inside dome We, J OHN L. STEwARrand JOHN P. LOGAN, of
E, in which it is open to the atmosphere at the top,-
the city and county of Philadelphia and State of Pennsylvania, have `invented an Improved Petroleum- Still, ot' which the following is a specification.
The mai-n features of our invention consist in the f arrangement of thepipes leading from the still to the central dome; inthe construction of a double-walled central dome, in which the vapor is partly condensed; and in the arrangement of the pipes and valve leading from the dome to the condenser.
To enable those skilled in the Vart to make and use our invention, we will proceed to describe its construction and operation, reference being had to the accompanying drawing and to the letters of reference marked thereon, in whichl Figure l is a plan of the still.
Figure 2 is a vertical section.
Figure 3 is a modified form of the interior dome.
A is the still, which is nearly filled with crude oil B.
The bottom Oi' the still is formed in curved lines, as shown.
The top is formed of curved lines like a corrugated disk, the curve near the edge being convex, and having its highest point where the pipe C enters, about iive feet from the edge of the still, the whole diameter of the still being thirty feet.
This form of the top causes all the vapoi` to rise into the pipes C, which, in the still here described, are seventeen in number, and eight inches diameter, each one being placed over a lire.
There are seventeen lires under the still.
The pipes C lead into a central dome, D, at a slight inclination downward, so that the condensed vapor will drain into the dome D.
vThe dome D is about twelve feet high; the upper part four feet in diameter; the lower part is widened to six feet, and secured tight to the top of the still.
Within the dome D is another dome, E, three feet in diameter, thus leaving a space of six inches between the two domes for the passage of the vapor.
The lower end of dome E is secured tight to the top of the still, a few small holes only being left at c' to permit the condensed vapor q to occupy the same level at the bottom of each dome.
The top of dome E is closed, and extends in height to within six inches of dome D.
At the bottom of the inside dome is a valve, h, operated by a screw and handle, h1, projecting through the dome D.
The condensed vapor is returned to the still by this valve h lthrough a trap, h2, which trap prevents the passage of vapor. Or the condensed vapor4 g can be drawn od' by pipe It and cock r.
and has an air-passage,e", atthe bottom, so that a circulation of cold aiigis kept up within it. The valve h in this case is arraiiged between the two shells.
A large twenty-inch pipe, K, leads from the bottom of dome D, at a' few inches below the level at which the pipe C enters.
This pipe K is on a slight incline to the condenser, and laid close to the top of the still.
A sluice-valve, L, or a Ludlow valve, is placed in the `pipe close to the dome, and a safety-valve, m, and a vacuum-valve, n, are placed as shown.
A twenty-inch pipe, P, leads from the top of' the dome D and enters the pipe K beyond the valve L.
R R are man-holes. The operation Of the still is in this way: The valve L is first closed, the still is nearly filled with crude oil, and a series ot' fires applied below.
The gasoline and benzine pass up the pipes G and into the dome D, where the vapor passes up the annular passage formed between the two domes, and is thus all forced in contact with the cooling surface ot' the dome D. 'lhe gasoline and benzine then pass down pipes P and K to the condenser.
The vapor condensed in the pipes C and domeD collects at the bottom of the dome D and runs into the 'dome E by the openings e'. YIhe valve h is openduring this part of the operation', Aand theeondensed vapor passes back to the still through trap h.
When all the benzine is evaporated the valve Lv is opened and the small one h closed, so that the condensed vapor is prevented from returning to the still, and passes along with the vapor through valve L and pipe K to the condenser.
'lhis process .is continued until the oil begins to be highly colored, at which time the valve h is opened and the condensation of the heavier hydrocarbon forms a liquid which returns to the still, the lighter vapor only passing off through valve L.
The advantage of this arrangement of the pipes and lcentral dome D is that it gives great facility for the vapor to pass od from the still as soon as formed, and all the condensation runs down pipes C and is collected in the bottom of dome D; whereas, if the vapor had to pass beneath the top of the still a long distance previous to its escape by a central pipe considerable condensed vapor would fall back again into the still.
1. The still A, with its top in the form of an annular corrugation, ,in combination with a series of pipes the highest part of the said corrugation.
2. V lhe central dome D arranged upon thestll A in dome D, or its equivalent,v andstili A, for the purpose the manner shown, as a receptacle for the vapors that of returning the condensed vapor to the still, as herein pass from the still by the collecting-pipes C. described. A
3. The arrangement ofthe dome E within the dome 6. The combination and arrangement of the still` A, D, so as to bring the uncondensed vapors in contact pipes'O, domes D and E, pipes P and Kranfd valve with the cooling' surface of the dome l), as herein de- L, as hereinv shown and set forth. scribed.
. JOHN L. STEWART. 4. The dome E, made with passages for the free eir- JOHN P. LOGAN. culation of the air, as in jig. 3,`111v combinati-on withY Witnesses: the dome D, for the purpose herein described. EDWD. BRoWN,
5. The valve h arranged, in combination with the .K JNO. Gr. UMSTED.
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