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Publication numberUS2539915 A
Publication typeGrant
Publication dateJan 30, 1951
Filing dateDec 2, 1948
Priority dateDec 9, 1947
Publication numberUS 2539915 A, US 2539915A, US-A-2539915, US2539915 A, US2539915A
InventorsOlof Lindgren Hans
Original AssigneeSeparator Ab
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Method of purifying heavy boiler oil
US 2539915 A
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Description  (OCR text may contain errors)

i 0, 1951 H. o. LINDGREN 2,539,915

METHOD OF PURIFYING HEAVY BOILER on;

Filed Dec. 2,1948

ln venfo/ Hans 0/07 L inc/gr en Affarneys Patented Jan. 30, 1951 METHOD .OFPURIEYINGLHEAVY BOILER *on.

Hans Olof fliindgren, Smellslatten; Sweden, $3,8- signon-rto iAktiebclaget Separator;1-Stoclihclm,

Sweden, =a-corporation of;Sweden Application December 2, 1948,Serial"N0..63;187

' InSweden Decenribe'r'B; -1947 3 Claims. 1

This invention relates toaprocess for purifyi-ingqheavy boiler or bunker oil containing water rand solid-impurities and intendedforifuelling internal combustion. engines, 'eSpecia-lIy Diesel engines.

Heavy'fuel oil, so-called boiler or bunker oil, is commonly used also as fuel for Diesel engines, be causethis type ,of oil offers considerable economicaladvantagesas.comparedwithDiesel oil, owing to. its lower price- The heavier .boi1er oi1s at .least, being only so-called topped crude oils and not distillates,.containsome veryfine wearing solids, .such assand, crystals or manymetal salts, oxides, etc .which as .a ,rule are not found in the Diesel .oil. When such oils are to he used forfuelling Diesel engines, they .must therefore .be subjected to very careful and effective purification, because otherwise the wear of the injection nozzles, the piston rings and the cylinder liners would be excessive and entail-repair'costs which may equal cor eyen zexceed the: reduction -.of the fuehcosts.

heavyboiler oil and thereby-facilitate the centrifugal separation,-the oil shoiildi be heated to the *highest permissible temperature'which should,

however, always be so high that any existing emulsion of oil and water is broken. It is important that the heating be carried out in the correct manner. If too low a temperature is used, the emulsion is not broken to a sufficient degree and if the temperature is raised too much or the heating is carried out too slowly, there is a risk that quick-burning asphaltic materials contained in the oil are polymerized and precipitated and that. certain impurities combustible only with difficulty are transferred into non-separable form by re-dissolving. This type of fuel also contains some easily volatile fractions which should also be prevented from volatilizing.

The present invention has for its primary object the provision of an improved process for purifying heavy boiler oil containing water and solid impurities, whereby the inconveniences referred to above are avoided.

According to the invention, the heavy boiler oil is subjected to emulsion-breaking heating and subsequent centrifugal separation. However, the emulsion-breaking heating and the separation are effected so rapidly that any appreciable precipitation of quick-burning asphalt substances is prevented. It has been found that the quicker the heatingnand the separation are carried out, the

greateriis .the likelihood that the quality-improvsingasphalt. substances will beiretained intthe oil. "Itiis;.importanttzthatuthexheating beLelfected without access of:the air, that is, whilerexcluding atmospheric air-from theoil. The heatingzshould ibe continuediuntil a temperature of -95 C. is reached, the :mostsuitable.:temperature varying somewhat according to theiikind .andjnature .of .the impurities. Aspreviously mentioned, it .is important that 'thehighest' permissibleutemperaitureriis not.'rexceeded,.ras otherwise .the 'TIIOIldQ- sira'ble free asphalt substanceswvould become dissolved in the oil and couldnot therefore berremoved in the separation. 'The same also applies to athe period of :time during which the oil is kept at :the highest temperature. As .a "rule, theoil .dur-ing ithefheating-and the: separation's'hoiildinot bekept at the highest temperature fora longer period than about ten-minutes. The-simplest manner. toefiect theheatingtand subsequent-cooling isiby using az-heat exchanger of the'so-called plate apparatus type, ,in' which'the ,desiredtemperaturecan easily be maintained with they aid of a. thermostatic regulating device and more con- .siderable variations :can be avoided. The'separationzshould be conducte'd'insuch a manner-that -:the easily volatile fractions are prevented from escaping, and-to this ,end the separation maybe effected either in-so-called hermetic :centrifugal separators or in a closed centrifugal system. In the latter case, communications are preferably provided between the various outlets or between each outlet and the receiving vessel of the separator, or both, so that a pressure equalization takes place in the various vessels and pipes at the same time as a given saturated quantity of air circulates in the system.

The separation may be effected in one or more stages, and preferably in two stages, the separation of the second stage taking place at a somewhat lower temperature than the separation of the first stage. After the first stage separation, the oil should be chilled or allowed to cool off so that its temperature decreases about 5 to 10 0., whereby slow-burning asphalt substances dissolved in the oil are precipitated. They are then removed in the second stage separation, and on being separated they entrain the very finely comminuted solid matters left in the oil after the first stage separation.

In the accompanying drawing, the single illus tration is a schematic view of one form of a plant for purifying heavy boiler oil according to the invention. From a tank I the heavy boiler 011 is pumped by a pump 2 to a heating zone or heater 3 (preferably a plate apparatus) in which the oil is quickly heated to the required temperature, for example 80-95 C., before it is subjected to centrifugal separation, preferably in two stages. The first stage separation is carried out in a centrifugal separator 4 of the hermetic or closed type, whereby the oil is prevented from coming into contact with atmospheric air. The separator 4 is one which effects a three-way separation and discharges the three components separately from the centrifugal bowl, such separators of the hermetic or closed type being well known. In the pipe extending from the heater 3 to the separator 4 a thermostatic regulating device 5, S of conventional construction is interposed. The thermostat 5 controls the valve actuator 6 to increase or decrease the rate at which the heating medium is supplied to the heat exchange zone 3, so as to counteract any substantial change in the temperature of the heated oil passing to separator 4.

From the separator 6 three components are discharged, namely, water, sludge, and separated boiler oil. The water is discharged through a pipe I, the sludge through an outlet 8, and the oil through a pipe 9. The separated oil is fed through pipe 9 to a cooler lil which, like the heater 3, is preferably a plate apparatus and in which the oil, prior to being fed to the second stage separator H, is cooled 5 to 10 C. The separator l I, which is a centrifugal purifier, may also be of the air-tight type, although this is not necessary. The purified oil is discharged from the machine through an outlet ii. In this separator only small amounts of sludge are separated, which are retained in the sludge space of the centrifugal bowl until the separation is completed. As the oil is almost completely liberated from water in the first separating stage, no appreciable amounts of water are separated in the second stage. The heating and the cooling mediums are fed to the apparatus 3 and I I9, respectively, through pipes i3 and Hi.

In the new process, the rapidity of the emulsion-breaking heat treatment and the close control of the temperature prevent the slow-burning asphaltic substances, or those which are combustible only with difiiculty, from dissolving in the oil, but allow the lighter and quick-burning asphaltic substances to remain dissolved in the oil.

Before the latter substances can precipitate or coagulate noticeably, the heated oil is quickly centrifuged so that the quick-burning asphaltic substances pass out with the oil in which they are dissolved, rather than with the precipitated slowburning asphaltic substances or with water. The subsequent limited cooling of the oil will precipitate or re-precipitate remaining slow-burning asphaltic substances in the oil, and these impurities will thus act in the second-stage separation to entrain other solid comminuted impurities not affected by the first stage separation.

I claim:

1. In the purification of heavy boiler oil containing water and solid impurities and intended as fuel for combustion engines, especially Diesel engines, by subjecting the oil to emulsion-breaking heating and subsequent separation of oil from water and solid impurities, the improvement which comprises flowing a stream of the oil through a heating zone and there heating it rapidly to an emulsion-breaking temperature of about 88-95 C., and centrifuging the heated oil before there is any noticeable precipitation of quick-burning asphaltic substances in the oil, the time during which the oil is maintained at the highest temperature in the heating and separating steps being no greater than ten minutes.

2. The improvement according to claim 1, in which the heating is eifected while excluding atmospheric air from the oil.

3. The improvement according to claim 1, comprising also the steps of cooling the centrifugally separated oil to reduce its temperature by about 5 to 10 C., and subjecting the cooled oil to a centrifugal purification treatment.

HANS OLOF LINDGREN.

REFERENCES CITED The following references are of record in the file of this patent:

UNITED STATES PATENTS Number Name Date 1,299,590 McKibben Apr. 8, 1919 1,474,629 Hall Nov. 20, 1923 1,699,379 Sperry Jan. 15, 1929 2,365,256 Edwarsson Dec. 19, 1944

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US1299590 *Oct 24, 1918Apr 8, 1919Charles W MckibbenMethod of and means for separating water from heavy-oil emulsions.
US1474629 *Aug 16, 1921Nov 20, 1923Laval Separator Co DeProcess for purifying liquids
US1699379 *Sep 21, 1925Jan 15, 1929Sperry Dev CoMethod of refining crude fuel oil
US2365256 *Jan 6, 1944Dec 19, 1944Separator AbSeparation of emulsions and colloidal solutions
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2914518 *Aug 24, 1956Nov 24, 1959Phillips Petroleum CoPolymerization catalyst recovery
US2963219 *Apr 22, 1957Dec 6, 1960Separator AbSystem for continuous operation of series connected hermetically closed centrifugal separators
US3013961 *Apr 12, 1954Dec 19, 1961Westfalia Separator AgMethod and apparatus for purifying heavy fuel oils
DE971862C *Apr 12, 1953Apr 9, 1959Westfalia Separator AgVerfahren zum Reinigen von wasserhaltigen schweren Heizoelen
Classifications
U.S. Classification516/195, 210/774, 208/187, 210/258, 210/787, 210/181
International ClassificationC10G33/06, C10G33/00
Cooperative ClassificationC10G33/06
European ClassificationC10G33/06