US2006088A - Method of separating oil from fuller's earth or similar material - Google Patents

Method of separating oil from fuller's earth or similar material Download PDF

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Publication number
US2006088A
US2006088A US642047A US64204732A US2006088A US 2006088 A US2006088 A US 2006088A US 642047 A US642047 A US 642047A US 64204732 A US64204732 A US 64204732A US 2006088 A US2006088 A US 2006088A
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earth
oil
fuller
hopper
similar material
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US642047A
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Mitchell Edward Ross
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RUSSEL KENDALL
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RUSSEL KENDALL
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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
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal

Definitions

  • fullers earth In oil refineries it is usual to use fullers earth, clay, or similar material in clarifying oil.
  • the fullers earth takes up a certain amount of the oil as it is used, and loses its effectiveness for 5 clarifying purposes, hence has to be discarded and a fresh lot employed.
  • This fullers earth is comparatively expensive, particularly on account of freight charges in the case of refineries located a long distance from the source of supply of the fullers earth.
  • On top of the original expense there is also the expense involved in disposing of the fullers earth after use, as difficulty is often experienced in getting a suitable place for disposal.
  • the oil with which the earth or clay is impregnated is also lost.
  • My object is to devise a simple method and simple apparatus for treating the oil impregnated fullers earth or clay whereby the earth or clay and oil may be satisfactorily separated and at a cost which makes the separation a commercially profitable proposition.
  • the apparatus in the main comprises two superposed hoppers I and 2, the upper hopper I being provided with a funnel-shaped lower portion to guide material into the lower hopper 2, the lower hopper also having a funnel-shaped lower portion to guide material into an outlet or discharge pipe 3.
  • a valve 4 is arrgli ged to control fiow from the hopper I to the hopper 2, and a valve 5 is arranged to control flow from the hopper 2 through the discharge pipe 3.
  • Means B are provided for heating the material in the hopper I, which means may comprise a steam coil such as shown, but it will be understood that any other type of heating means may be provided.
  • the hopper I is provided with an oil discharge I which is provided with a vertically adjustable inlet, preferably by forming the part in two sections flexibly connected together as shown.
  • the method of separation is as follows.
  • the valve 4 being closed, a quantity of a separating medium is placed in the upper hopper I, and also a quantity of oil impregnated fullers earth or clay, the solids in which will be sufficient to fill the hopper 2.
  • substantially two parts of separating medium will be used for one part of oil impregnated earth, while in other cases this proportion may be varied.
  • I find a very satisfactory one comprises a brine solution, in which the salt forms substantially four to six percent of the mixture, but I do not desire to limit myself to this as the amount of salt used will depend considerably on the kind of earth or clay and oil being separated.
  • the mixture of brine solution and oil impregnated earth and clay is brought to the boiling point of the brine solution, and it is found that this causes the oil and earth to separate, and this separation is facilitated if the mixture is subjected to agitation, which may be by mechanical means or by means of steam or air.
  • Suflicient salt must be employed to prevent the oil emulsifying, and if during the boiling process the bubbles or froth are white, it indicates that the brine solution is not sufiiciently strong.
  • valve 4 is then opened allowing the earth or clay to pass into the lower hopper 2.
  • the valve 4 is first closed and the valve 5 then opened, thus allowing the earth or clay to pass off through the discharge pipe 3, after which the valve 5 is again closed.
  • the apparatus is now ready for the treatment of the next batch of oil impregnated sand in a similar manner, and as the separation has been effected without waiting for the brine to cool, the heat retained in the latter is available for the next batch.

Description

June 25, 1935. E, MlTcHELL 2,006,088
METHOD OF SEPARATING OIL FROM FULLERS EARTH OR SIMILAR MATERIAL Filed Nov. 10, 1932 \m'n 10M [E -Fifi I I V l l Hllll I IN]! l I l Patented June 25, 1935 f 2,006,088. a METHOD or *snPARA'rm G on; From" FULLERS EARTH OR SIMILAR RIAL .MATE...
Edward Ross Mitchell, Sarnia, Ontario, Canada, assignor of one-half to Russel Kendall, Sarnia,
Ontario, Canada Application November 10, 1932, Serial No. 642,047
1 Claim.
In oil refineries it is usual to use fullers earth, clay, or similar material in clarifying oil. The fullers earth takes up a certain amount of the oil as it is used, and loses its effectiveness for 5 clarifying purposes, hence has to be discarded and a fresh lot employed. This fullers earth is comparatively expensive, particularly on account of freight charges in the case of refineries located a long distance from the source of supply of the fullers earth. On top of the original expense, there is also the expense involved in disposing of the fullers earth after use, as difficulty is often experienced in getting a suitable place for disposal. The oil with which the earth or clay is impregnated is also lost.
It will be seen therefore that there is considerable advantage in reclaiming the earth so as to render it fit for reuse, and also to reclaim the oil with which the earth is impregnated, but the processes and apparatus heretofore employed for the purpose of reclamation have been so complicated and expensive that it has not been commercially worth while to carry out said separation.
My object, therefore, is to devise a simple method and simple apparatus for treating the oil impregnated fullers earth or clay whereby the earth or clay and oil may be satisfactorily separated and at a cost which makes the separation a commercially profitable proposition.
I attain my object by means of the method and apparatus hereinafter described and illustrated in the accompanying drawing which illustrates diagrammatically suitable apparatus for carrying outthe method.
The apparatus in the main comprises two superposed hoppers I and 2, the upper hopper I being provided with a funnel-shaped lower portion to guide material into the lower hopper 2, the lower hopper also having a funnel-shaped lower portion to guide material into an outlet or discharge pipe 3.
A valve 4 is arrgli ged to control fiow from the hopper I to the hopper 2, and a valve 5 is arranged to control flow from the hopper 2 through the discharge pipe 3.
Means B are provided for heating the material in the hopper I, which means may comprise a steam coil such as shown, but it will be understood that any other type of heating means may be provided.
The hopper I is provided with an oil discharge I which is provided with a vertically adjustable inlet, preferably by forming the part in two sections flexibly connected together as shown.
The method of separation is as follows. The valve 4 being closed, a quantity of a separating medium is placed in the upper hopper I, and also a quantity of oil impregnated fullers earth or clay, the solids in which will be sufficient to fill the hopper 2. In certain cases substantially two parts of separating medium will be used for one part of oil impregnated earth, while in other cases this proportion may be varied. While other separating mediums may answer the purpose, I find a very satisfactory one comprises a brine solution, in which the salt forms substantially four to six percent of the mixture, but I do not desire to limit myself to this as the amount of salt used will depend considerably on the kind of earth or clay and oil being separated.
The mixture of brine solution and oil impregnated earth and clay is brought to the boiling point of the brine solution, and it is found that this causes the oil and earth to separate, and this separation is facilitated if the mixture is subjected to agitation, which may be by mechanical means or by means of steam or air. Suflicient salt must be employed to prevent the oil emulsifying, and if during the boiling process the bubbles or froth are white, it indicates that the brine solution is not sufiiciently strong. By ceasing the agitation of the mixture the heavier sand sinks to the bottom of the hopper and the oil rises to the top above the separating solution, from where it is drawn off through the pipe 1, the mouth of said pipe being dropped to a suitable level so that only the recovered oil is allowed to pass off.
The valve 4 is then opened allowing the earth or clay to pass into the lower hopper 2. When the latter is full, the valve 4 is first closed and the valve 5 then opened, thus allowing the earth or clay to pass off through the discharge pipe 3, after which the valve 5 is again closed.
The apparatus is now ready for the treatment of the next batch of oil impregnated sand in a similar manner, and as the separation has been effected without waiting for the brine to cool, the heat retained in the latter is available for the next batch.
While the oil separated from the sand is not as clear as fresh oil, it is found to be quite a satisfactory oil for most purposes. It is also found that while the reclaimed earth or clay is not quite so effective in clarifying oil as entirely fresh earth, it is found that if a small proportion, say 20%, of fresh earth be added to the reclaimed earth that substantially the same results are obtained as when using new earth altogether.
While the above process and apparatus have been devised particularly for the reclamation of fullers earth used in the clarification of oils, it will be found apparent that the process and apparatus may be utilized in separating oil from natural oil bearing sands such as found in various parts of the world.
From the above description it will be seen that I have devised a method and apparatus which will satisfactorily attain the object of my inve'n tion as set out in the preamble of thisspecification.
What I claim as my invention is:
posit in the bottom of the vessel and the oil to float on the briny solution; and removing the material from below the briny solution.
EDWARD ROSS MITCHELL.
US642047A 1932-11-10 1932-11-10 Method of separating oil from fuller's earth or similar material Expired - Lifetime US2006088A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2577079A (en) * 1948-12-31 1951-12-04 Texaco Development Corp Separation of fatty oil from solid bleaching agents
US2696462A (en) * 1952-04-08 1954-12-07 Socony Vacuum Oil Co Inc Method for regulating the flow of solid adsorbents
US3490592A (en) * 1965-08-02 1970-01-20 Monsanto Co Apparatus for producing filter cakes and recovering a process filtrate therefrom
US10033898B2 (en) * 2016-03-17 2018-07-24 Ricoh Company, Ltd. Information processing system, image forming apparatus, and method of processing information
US20190281178A1 (en) * 2016-03-17 2019-09-12 Ricoh Company, Ltd. Information processing system, information processing apparatus, image forming apparatus, information processing method, and computer program product

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2577079A (en) * 1948-12-31 1951-12-04 Texaco Development Corp Separation of fatty oil from solid bleaching agents
US2696462A (en) * 1952-04-08 1954-12-07 Socony Vacuum Oil Co Inc Method for regulating the flow of solid adsorbents
US3490592A (en) * 1965-08-02 1970-01-20 Monsanto Co Apparatus for producing filter cakes and recovering a process filtrate therefrom
US10033898B2 (en) * 2016-03-17 2018-07-24 Ricoh Company, Ltd. Information processing system, image forming apparatus, and method of processing information
US10382640B2 (en) 2016-03-17 2019-08-13 Ricoh Company, Ltd. Information processing system, information processing apparatus, image forming apparatus, information processing method, and computer program product
US20190281178A1 (en) * 2016-03-17 2019-09-12 Ricoh Company, Ltd. Information processing system, information processing apparatus, image forming apparatus, information processing method, and computer program product
US10735614B2 (en) * 2016-03-17 2020-08-04 Ricoh Company, Ltd. Information processing system, information processing apparatus, image forming apparatus, information processing method, and computer program product
US11212412B2 (en) 2016-03-17 2021-12-28 Ricoh Company, Ltd. Information processing system, information processing apparatus, image forming apparatus, information processing method, and computer program product

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