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Publication numberUS2530376 A
Publication typeGrant
Publication dateNov 21, 1950
Filing dateFeb 27, 1948
Priority dateFeb 27, 1948
Publication numberUS 2530376 A, US 2530376A, US-A-2530376, US2530376 A, US2530376A
InventorsFrancis J Castle, Robert E Beal
Original AssigneeFrancis J Castle, Robert E Beal
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Vacuum distillation
US 2530376 A
Abstract  available in
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Claims  available in
Description  (OCR text may contain errors)

Nov. 21, 1950 F. J. CASTLE ETAL VACUUM DISTILLATION Filed Feb. 27, 1948 3mm R. E.BEAL

F. J.CA$TLE %1 a 2} Patented'Ncv. 21,

VACUUM DISTILLATXON Francis J. Castle and Robert E. Beal, Peoria, 111.,

assignors to United States of America as represented by the Secretary of Agriculture Application February 27, 1948, Serial No. 11.763

(Granted under the act of March 3, 1883, as amended April 30, 1928; 370 0. G. 757) 4 Claims.

This application is made under the act of March 3, 1883, as amended by the act of April 30, 1928, and the invention herein described, if patented in any country, may be manufactured and used by or for the Government of the United States of America throughout the world for governmental purposes without the payment to us of any royalty thereon.

This invention deals with a novel method for effecting low pressure evaporation and an apparatus therefor.

More particularly, the invention deals with vacuum distillation 'in which a film of liquid is caused to move adjacent to a relatively cool con- (lensing surface in a rarified atmosphere. The film and the condensing surfaces are separated by substantially unobstructed space, the film being heated by contact with an evaporation surface.

An object of this invention is to provide an improved method and apparatus for effecting vacuum distillation whereby the efficiency of the process is increased and the cost of the process is considerably decreased.

Another object of the invention is to provide a novel and advantageous means for distributing the film of distilland over an evaporation surface in vacuum stills.

In the past, vacuum stills have been provided with central members, such as domes or columns. over which the distiland descends. Other stills have been employed in which the distilland is caused to move over. a flat evaporation surface adjacent to a flat condensation surface. These prior columns or surfaces of other configuration are usually made of glass or of some inert material presenting a relatively smooth surface, over which the distilland flows and from which vapors of the distillate may leave to condense upon the condensation surfaces. These evaporation surfaces are of varying shape and size, one of the simplest being the outer surface of a hollow cyinder.

In order to increase the sojourn of the distilland and to prevent channeling, it has been proposed to provide the surfaces of evaporation, such as a column, with a glass coil or to fabricate it in such a manner as to provide a winding or tenuous path for the distilland. It has been furevaporation surface.

2 interrupted bands or a helically wound strip of metal gauze.

These prior devices and methods are attended by many disadvantages. Residues of a gummy or tarry nature tend to accumulate upon the Any roughening or unevenness of the surface, such as are caused by grooves and the like, make the surface extremely difficult to clean. Distillands vary in their surface and flow characteristics and any one particular surface is not universally satisfactory. Special fabrication or surfacing increases the cost materially and in the majority of cases reduces the strength of the apparatus. Bands or strips of metal gauze permit fouling of the evaporation surface in the exposed portions, and the distilland tends to accumulate a small but nevertheless objectionable amount of metallic ions from the gauze. In the case of edible oils this metal content hastens flavor deterioration of the oil. The gummy or tarry residue which accumulates on the gauze requires drastic solvent action for removal, which tends to attack the gauze itself.

According to this invention, the evaporation surface is fabricated of a relatively smooth and strong material and over this surface is placed a flexible and pliable substantially complete yet permeable covering of inert material, such as fiberglass cloth, which serves to distribute the distilland and to retain substantially all tarry or gummy residue.

This covering substantially prevents the surface itself from collecting residue material and the still is therefore extremely easy to keep clean. In the usual high vacuum still the inert distributing material may be installed merely by drawing a mesh tube or sleeve of fiberglass or asbestos cloth over the column. The still may be substantially cleared of the fouling matter by merely removing and ceaning the covering sleeve. This sleeve is easy to remove and may be cleaned by immersing or washing in a cleaning medium. The cost is relatively very low compared with the special means of distributing the distilland over the evaporation surface used in the past.

The use of a permeable covering in accordance with this invention accomplishes efiicient distribution of the distilland over the evaporating surface without weakening it or introducing foreign material into the distilland. Moreover, a distinct advantage gained by the use of fiber glass or asbestos cloth is the inertness of the material 9 5h; very strong acid cleaningsolutions which are usually necessary to remove accumulated residues.

Another advantage of our invention is the fact that the capacity of any particular still may be varied between wide limits by varying the specific type of liquid distributor placed upon the evaporation surface. For instance, it may vary from a relatively thin coarsely woven mesh to a relatively thick retentive covering.

For a clearer understanding of the invention, reference is made to the accompanying drawing.

Figure 1 is a vertical view, partly in section, of one form of the invention;

Figure 2 is a cross-section of Figure 1 on line 2-2;

Figure 3 is a vertical view of a modified form of the covering, employing a spirally wound fiber glass or asbestos thread.

Figure 4 illustrates another modification, comprising a spirally wound strip of fiber glass gauze.

Figure 1 illustrates a high vacuum still consisting of a tubular condensing surface 4 inside which is disposed a vaporizing surface 5. Distilland enters through feed inlet I and is fed upon the evaporating surface which is heated internally by means of electrical resistance unit 3.

The evaporation surface is covered by a liquid distributor 6 consisting ofa mesh sleeve of woven fiber glass which distributes the distilland evenly as it descends over the evaporation surface. The uncondensed vapors are drawn off through outlet 2 while the condensed vapors collect on surface 4 and drain into distillate receiver 1. The undistilled residue collects in receiver 8.

While fiber glass cloth is preferred as the material for fashioning the tube or seamless sleeve 6 because of its inertness, flexibility, durability, and ease of removal, we may also use asbestos cloth.

In place of the sleeve 6 we may use a spirally wound thread I I of glass or asbestos, as indicated in Figure 3.

In Figure 4 is shown a spirally wound gauze strip l woven of glass or asbestos thread. The adjacent turns of the strip overlap or are closely contiguous, to cover the evaporating surface 5.

Strip I0 and thread I I may be removably fastened in place by any conventional means, such as fastening clamps or rings.

The evaporation surface has been illustrated in one of its simpler forms, such as that of a vertical cylinder. It may also be a vertical series of bulbous members. The column may be corrugated vertically or horizontally. It may be an upright or inverted truncatoconical or conical member, or it may be a plane surface. The surface may be fixed relative to the condensing surface, or it may be rotatable.

The means for supplying heat to the evaporation surface may be any of the usual means, such as liquid boiling under refiux, heat exchange fluid under circulation, and the like.

The apparatus and process of this invention are not limited to high vacuum distillation but may be applied to any process for distilling in which a materially reduced pressure is used. However, it is particularly advantageous in connection with the molecular distillation where the pressure is .01 mm. of mercury or lower and has been found to give excellent results in removing odorous constituents from vegetable oils.

In high vacuum or molecular distillation the pressure and the distance between the conden ing 4 surface and the surface of the distilland should vary in inverse proportion to each other. In general, due to practical difficulties, the condensing surface should not be more than one inch from the film of distilland.

Due to the flexibility and pliability of the m terial used to cover the evaporation surfacek may easily be made to conform to the shape 0 that surface. When the distributor becomes fouled or when a distilland of a different character is to be distilled, the distributor is simply removed and cleaned or a fresh one substituted.

Having thus described our invention, we claim:

1. A still comprising in combination a condensing surface and a tubular, smooth, heated evaporation surface spaced from the condensing surface, said evaporation surface having tightly fitted thereon a readily removable, flexible, pliable, and permeable covering sleeve of inert, acid-resistant, non-metallic, mesh fabric of mineral matter, to distribute the distilland supplied to the heated evaporation surface and to retain substantially all tarry and gummy residue formed at the evaporation surface and thus prevent the evaporation surface itself from collecting the said residue material, and means to supply distilland to the heated evaporation surface.

2. In a short-path high vacuum still having a tubular distilland evaporating surface and heating means for said surface, and also having a condensing surface; the improvement comprising a fiexible, detachable, pliable, inert, nonmetallic, covering tubular sleeve of fiber glass mesh fabric fitting upon and in contact with and substantially coextensive with the said heated evaporating surface, to distribute distilland supplied to the heated evaporation surface and to retain substantially all tarry and gummy residue formed at the evaporation surface and thus prevent the evaporation surface itself from collecting the said residue material and means to supply distilland to the heated distilling surface.

3. The apparatus of claim 1 in which the sleeve is made of woven fiber glass cloth.

4. The apparatus of claim 1 in which the sleeve is made of asbestos fiber cloth.

, FRANCIS J. CASTLE.

ROBERT E. BEAL.

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

UNITED STATES PATENTS Fenske et al., Packing Material for Fractionating Columns, Ind. and Eng. Chem., Nov. 1944, pp. 1169-1177.

Minard et al., "Fibrous Glass Used in Packing Alcohol Columns, Chem. and Met. Eng, Feb. 1944, pp. 144446.

Stewart, Construction of Glass Helices for Packing Fractionating Columns, Ind. and Eng. Chem. Anal. Ed., vol. 8, No. 6 (1936), pp. 451-45?

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2229209 *Aug 19, 1938Jan 21, 1941Atlantic Refining CoHydrocarbon oil treatment
US2310399 *Sep 10, 1940Feb 9, 1943Carbide & Carbon Chem CorpDistillation process and apparatus
US2313546 *Nov 19, 1940Mar 9, 1943Distillation Products IncDistillation apparatus
FR765588A * Title not available
GB164407A * Title not available
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3123541 *Nov 1, 1960Mar 3, 1964Sun Oil Companydonnell
US3161574 *Aug 21, 1961Dec 15, 1964Daniel W ElamStill having thin resinous heat transfer surfaces
US3170852 *Jun 22, 1962Feb 23, 1965Clyde S BarnhartProximity surface still
US3250687 *Feb 6, 1962May 10, 1966Jenaer Glaswerk Schott & GenApparatus with ground glass surface for film-type distillation
US4113571 *Feb 25, 1976Sep 12, 1978Nils NygardsWater distiller of boiler-condenser type
US4521276 *Apr 29, 1982Jun 4, 1985Oriental Metal Mfg. Co., Ltd.Concentrating apparatus
US4585523 *Feb 27, 1984Apr 29, 1986Giddings Edward HVapor compression distillation apparatus
US4613405 *Aug 16, 1984Sep 23, 1986Roussel UclafApparatus to concentrate solutions and to recover solvents
US5062927 *Jan 5, 1990Nov 5, 1991T And G Technologies, Inc.Condensing vapor on vertical membrane
US6365413 *Feb 25, 1999Apr 2, 2002Savant, Inc.Includes a heatable rod with a helical guide or channel, a supply of oxidant, and a thin film forming unit; for oil testing
US6663750 *Aug 23, 2001Dec 16, 2003Warren CoonMulti-unit, distributive, regenerable, in situ desalination system, apparatus and method
US7351312 *Dec 17, 2003Apr 1, 2008Uop LlcApparatus for obtaining sample and process therefor
US7815776Jan 11, 2005Oct 19, 2010Wilson George EDesalinization by evaporation from capillary material
EP1997545A2 *May 27, 2008Dec 3, 2008Hitachi Plant Technologies, Ltd.Controlling condensation in combination with evaporation
Classifications
U.S. Classification202/187, 202/205, 202/158, 202/236, 392/395, 159/13.2, 159/DIG.280, 392/399, 202/267.1
International ClassificationB01D1/22, B01D3/10
Cooperative ClassificationB01D3/10, B01D1/22, Y10S159/28
European ClassificationB01D1/22, B01D3/10