US123907A - Improvement in distilling coal-oils - Google Patents

Improvement in distilling coal-oils Download PDF

Info

Publication number
US123907A
US123907A US123907DA US123907A US 123907 A US123907 A US 123907A US 123907D A US123907D A US 123907DA US 123907 A US123907 A US 123907A
Authority
US
United States
Prior art keywords
oil
oils
burning
condenser
test
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
Publication date
Application granted granted Critical
Publication of US123907A publication Critical patent/US123907A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/06Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
    • F25J3/0605Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the feed stream
    • F25J3/062Refinery gas, cracking gas, coke oven gas, gaseous mixtures containing aliphatic unsaturated CnHm or gaseous mixtures of undefined nature

Definitions

  • the drawing illustrates the ordinary oil-distilling apparatus,exceptin the appliances which facilitate the execution of my improved process.
  • the still a is set in the usual manner, and the pipe b leads to the worm c in the condensing-tub f,'and a pipe, cl, rises from the delivcry-neck e to convey away the uncondensed vapors.
  • the volatile hydrocarbons are evaporated, and the gasoline and similar oil condensed by cold water in the condensertub f around the worm c.
  • the effect of warming up the condenser is to cause the burning-oil to flow over freely from the still in the form of vapor, and the temperature of the condenser is such that the burning-oil will be condensed; but the inflammable impurities usually condensed are not condensed, but pass away by the escape-pipe d.
  • the burning-oil will not inflame at as low a temperature as heretofore usual in oil passing from the still, and the higher the temperature of the condenser, the higher will be the fire-test of the oil; and I find in practice that by keeping the condenser warm the flow of oil will be much more free, and less fuel will be employed beneath the still.
  • the distillate-tank l is provided with a hollow trough, it, around the same, into which the burning-oil runs from the pipe 0, and travels around or along such hollow trough previous to escaping into the tank I.
  • the shallow trough a may pass twice around the distillatetrough, if desired, or extend in astraight line, or zigzag. This trough allows the liquid to cool as well as the volatile matters to pass off.
  • a condenser of a temperature as high as the fire-test of the oil, and passing away the uncondensed vapors freely and directly to the atmosphere, for the purposes set forth.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

S. HUDSON.
Improvement in DistiHing Coal Oils.
N0. 123,907. Patented Feb. 20,1872.
mam. 33M MN m UNITED STATES OFFICE.
SAMUEL HUDSON, OF PLAINFIELD, NEW JERSEY.
Specification forming part of Letters Patent No. 123,907, dated February 20, 1872.
To all whom it may concern:
Be it known that I, SAMUEL HUDSON, of Plainfield, in the county of Union and State of New Jersey, have invented and made an Improvement in Distilling Goal-Oils; and I hereby declare the following to be a correct description thereof.
In distilling coal-oil, great difficulty has heretofore arisen from two causes. The first is in the condensing-worm, and the second is in the low-fire-test that the oil will stand after it passes to the distillate-tank. My invention is for obviating these two difficulties by a peculiar process which I adopt in distilling.
The drawing illustrates the ordinary oil-distilling apparatus,exceptin the appliances which facilitate the execution of my improved process.
The still a is set in the usual manner, and the pipe b leads to the worm c in the condensing-tub f,'and a pipe, cl, rises from the delivcry-neck e to convey away the uncondensed vapors. Afterthe still has been started in the usual manner, the volatile hydrocarbons are evaporated, and the gasoline and similar oil condensed by cold water in the condensertub f around the worm c. After these volatile substances have been distilled, and the burningoil is to be distilled, it frequently happens that the temperature of the still has to be greatly increased before said burning-oil will flow freely, and the oil distilled is almost always of a'low fire-test, requiring subsequent refining to remove the volatile materials and increase the fire-test temperature. To obviate these difficulties, I apply heat to the water in the condenser f by blowing steam into the same by the pipeg or otherwise, so that the temperature is about 130 Fahrenheit, or from that to 200 Fahrenheit, according to the oil distilled or the product required. The effect of warming up the condenser is to cause the burning-oil to flow over freely from the still in the form of vapor, and the temperature of the condenser is such that the burning-oil will be condensed; but the inflammable impurities usually condensed are not condensed, but pass away by the escape-pipe d. Hence the burning-oil will not inflame at as low a temperature as heretofore usual in oil passing from the still, and the higher the temperature of the condenser, the higher will be the fire-test of the oil; and I find in practice that by keeping the condenser warm the flow of oil will be much more free, and less fuel will be employed beneath the still. I furthermore remove from the oil the volatile "substances that lessen the fire-test by exposing the warm oil that-runs from the still to the atmosphere before it enters the distillatetank. For this purpose the distillate-tank l is provided with a hollow trough, it, around the same, into which the burning-oil runs from the pipe 0, and travels around or along such hollow trough previous to escaping into the tank I. Thereby there'will be a large surface exposed to the atmosphere, which will cause most of the volatile matters to pass off from the oil, leaving it comparatively colorless, and of a high fire-test. The shallow trough a may pass twice around the distillatetrough, if desired, or extend in astraight line, or zigzag. This trough allows the liquid to cool as well as the volatile matters to pass off.
I do not claim dist-illin g oils by the use of two condensers, the one nearest the stillbeing heated, so that the easily-volatilized liquids will not be condensed'therein, but pass on to the second condenser, and the more easily c011- densed liquid will run. back to the still, as in the patent of G. M. Warren, April 11, 1865. Neither do I claim a column in which the vapors condense at varying temperatures, as these have been employed. In my apparatus the temperature of the condenser in distilling burning-oils is as high as the. lire-test; therefore the vapors that would render the oil eX- plosive are not condensed, but pass off by the pipe (I.
In cases where the burning-oil is condensed in a warm condenser, and the uncondensed vapors are carried into a cooler condenser, the burning-oil is not of a high fire-test, and the liquid that is condensed is of little value. By confining the vapors to the condensers, instead of affording a free discharge to the atmosphere, the quality of the burning-oil is injured by the said vapors. I find it necessary, in or der to produce the superior quality and high fire-test of the burning-oil, that the condenser shall be at a temperature as high as the fire test of the oil, and that a free discharge be given of the uncondensed vapors to the atmosphere, and also that the burning-oils shall be exposed to atmospheric action as they run from the still and before the volatile portions combine with the burning-oil, as they are liable to do if they remain together.
I claim as my invention 1. In distilling burnin g-oilfrom petroleum, the use of a condenser of a temperature as high as the fire-test of the oil, and passing away the uncondensed vapors freely and directly to the atmosphere, for the purposes set forth.
2. And, in combination with the foregoing an open shallow trough receiving the oil as it runs from the still, and exposing the same to the atmosphere, for the purposes set forth.
Signed by me this 21st day of October, A. D. 1871.
his SAMUEL HUDSON.
mark. I
Witnesses:
LEMUEL W. SERRELL, NELsoN RUNYON.
US123907D Improvement in distilling coal-oils Expired - Lifetime US123907A (en)

Publications (1)

Publication Number Publication Date
US123907A true US123907A (en) 1872-02-20

Family

ID=2193341

Family Applications (1)

Application Number Title Priority Date Filing Date
US123907D Expired - Lifetime US123907A (en) Improvement in distilling coal-oils

Country Status (1)

Country Link
US (1) US123907A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040199406A1 (en) * 2003-03-07 2004-10-07 Raymond Owens System for monitoring payment for provision of services to an entity
US20050010428A1 (en) * 2000-07-27 2005-01-13 Bergeron Heather Ellen Processing transactions using a semantic network
US20100295868A1 (en) * 2009-05-20 2010-11-25 Dacuda Ag Image processing for handheld scanner

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050010428A1 (en) * 2000-07-27 2005-01-13 Bergeron Heather Ellen Processing transactions using a semantic network
US20040199406A1 (en) * 2003-03-07 2004-10-07 Raymond Owens System for monitoring payment for provision of services to an entity
US20100295868A1 (en) * 2009-05-20 2010-11-25 Dacuda Ag Image processing for handheld scanner

Similar Documents

Publication Publication Date Title
US123907A (en) Improvement in distilling coal-oils
US1445134A (en) Device for heating and purifying water
US1464246A (en) Distilling apparatus
US1942858A (en) Distillation apparatus
US31858A (en) Improvement in the manufacture of hydrocarbon oils
US154772A (en) Improvement in apparatus for distilling hydrocarbon oils
US130909A (en) Heney james
US66243A (en) Clarejtce mokfit
US1193541A (en) Method foe converting higher-boiling petroleum hydrocarbons into
US524704A (en) Brough
USRE4375E (en) Improvement in processes and apparatus for distilling, separating
US77070A (en) Improved appaeatus foe distilling peteoleum
US46923A (en) Improved apparatus for distilling petroleum
US58512A (en) Improved double still for petroleum
US1654797A (en) Method of distilling hydrocarbons
US125633A (en) Improvement in the manufacture of illuminating gas
US117406A (en) Improvement in stills for oil
US53964A (en) Improved apparatus for distilling petroleum
US1583746A (en) Apparatus for refining oils
US1208453A (en) Apparatus for destructive distillation.
US1353638A (en) Alvin a
US253990A (en) Apparatus for fractional distillation
US546697A (en) Andrew b
US1472116A (en) Process of distilling oil
USRE4366E (en) X o oils