Search Images Maps Play YouTube News Gmail Drive More »
Sign in
Screen reader users: click this link for accessible mode. Accessible mode has the same essential features but works better with your reader.

Patents

  1. Advanced Patent Search
Publication numberUS1461640 A
Publication typeGrant
Publication dateJul 10, 1923
Filing dateAug 15, 1921
Priority dateAug 15, 1921
Publication numberUS 1461640 A, US 1461640A, US-A-1461640, US1461640 A, US1461640A
InventorsElias Wirth-Frey
Original AssigneeFirm Ag Kummler & Matter
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Process and apparatus for evaporating liquids
US 1461640 A
Abstract  available in
Images(1)
Previous page
Next page
Claims  available in
Description  (OCR text may contain errors)

jufiy w, 1923- 2,4616% E. WmTH-FREY PROCESS AND APPARATUS FOR EVAPORATING LIQUIDS Filed Aug.'l5, 1921 Patented duty 1, 123.

ELIAS WIRTH-FREY, OF AARAU, SWITZERLAND, ASSIGNOR TO THE FIRM AKTIEN- GESELLSCHAFT KUMMLER & MATTER, OF AABAU, SWITZERLAND.

PROCESS AND APPARATUSIOR EVAPORATING LIQUIDS.

Application filed August 15, 1921. Serial No. 492,456.

(GRANTED UNDER THE PROVISIONS OF THE ACT OF MARCH 3, 1921, 41 STAT. L, 1313.)

To all whom it may concern:

Be it known that I, ELIAS WInTH-FREY,

a citizen of the Republic of Switzerland, re-

siding at Laurenzenvorstadt, Aarau, Switzerland, have invented certain new and useful Improvements in Processes and Apparatus for Evaporating Liquids, (for which I have filed applications in Germany, Nov. 11, 1917, application No. 29882; in France,Dec.

to 12, 1918, Patent No. 493794; in Italy, Dec.

16, 1918, Patent No. 80/490; in Germany, Mar. 5, 1918, application No. 30286; in Spain, Jan. -1, 1919, Patent No. 68782; in England, Oct. 20, 1918, Patent No. 123716;

1a in Switzerland, May 8, 1920,, Patent No.-

87745; in Germany, April 13', 1920, application No. 33277; in Switzerland, May 21, a 1920, application No. 5767; in Sweden, June 26, 1920, application No. 3134/; in Nor- June 30, 1920,- application No. 21184/20; in Germany June14, 1920, application No. 33565; in Switzerland, Mar. 31, .1921, application No. 12123; in Italy, April 4, 1921, application No. 301/1430;

andin Canada, June 10. 1921, application No. 255139); and I do hereby declare the following to be a clear, full,- and exact description of the invention, such as will enable others skilled in the art to whichit appertains to make and use the same, reference being had to the accompanying drawings, and to letters or figures of reference marked thereon, which form a part of this specification.

This invention relates to improvements in a process for improving the working of compressors and of evaporating plants and has particular reference" to evaporating plants in which the vapours emanating from the liquid to be evaporatedare used in a compressed condition in ,a closed heating body for heating said liquid. It is 'a wellknown fact that the utilization. of compressed vapours for,'evaporating purposesis only economical if said vapours are compressed to a comparatively low surplus pressure. In such cases, however, the danger exists, that already with small variations in the evaporation the working of the com- 59 pressor becomes unstable'i. e. that a working condition presents itself. in which the output of the compresor has diminished to such an extent that the pressure rise caused evaporation will be completely interrupted.

Although such disturbances might be small during the normal working of an evaporating plant, they may occur in quick succession during short intervals and thus cause a considerable decrease in the specific evap-.

oration figure and thereby in the eiiiciency of the whole plant.

. The object of the present process is to prevent the unfavorable action of such disturbances on the working of the plant. According tothe invention part of the vapours emanating from the liquid and then compressed are' introduced directly into the liquid to be evaporated. In this way a steady and uniform evaporation is promoted and maintained and an interruption of the evaporation is effectively prevented under any working conditions. A working of the evaporating plant that is free of interruptions and is satisfactory as regards efiiciency may in many circumstances only be made possible by the process according "to-the invention.

It has already been known to conduct small quantities of steam into the liquid to v beevaporated. This procedure however, only serves, in lieu of stirring devices or screw conveyors, to impart that strong mechanical motion to the thickened liquid that is necessary for preventing the latter from becoming burnt. v

As the quantity of vapors directly introduoed into the liquid to be evaporated in the form of open jet-sfor the purpose of improving the working of the compressor and of the evaporating plant circulates through the vessel containing the liquid and through the compressor a certain amount of compression work has to be permanently performed in addition to the work for compressing the vapors utilized in the heating body. In order to decrease that additional compressionwork, the-compression of the part of thevapors that is introduced directly into the liquid may according to another feature of the invention, only be efiected to a pressure sufiicient to overcome the'h ydrostatic raeaeeo head in the vessel at the point pf introduction. This means a comparatively important saving in compression work. The vapor directly introduced into the liquid to be adapted to compress the bulkof the vapors utilized for heating purposes.

The accompanying drawing shows by way of example in a diagrammatic manner two arrangements of apparatus for carrying out the process according to the Invention.

Figure 1 is a view partly in section of one form of .apparatus, and

Fig. 2 is a like view of a modification.

1 denotes the vessel containing the liquid to be evaporated. The vapors emanating from the liquid are conducted by a conduit 3 to the suction end of a rotary compressor 4, in which they are compressed and discharged through a conduit 5 to a heating body 2 inside the vessel 1. The compressed vapors deliver their heat to the liquid surroundin bein led off by means of the conduit 6. The eating body 1 is provided with apertures at 9 through which part of the compressed vapors is directly introduced into the liquid to be evaporated in the form of open ets. This arrangement in which the heating body 2 serves at the same time as distributor to the vapors directly introduced into the liquid to be evaporated presents the advantage, that the heating bodyis vented i-nasmuch asqan air collecting inside said body, which air hasafdetrimental effect on the transmission of heat, can escape.

The second constructional example illustrated in Fig. 2 differs .from that shown in Fig. '1 in as much as a special distributor 8 is arranged inside the vessel 1 through 'aper: tures of which the part of the compressed vapors, utilized for improving the working of the compressor and of the evaporatin plant is directly introduced into the liqui n the arrangementshown said vapour is led to the distributor 8-through a conduit 7 which is connected up to a lowervpressure stage of the compressor 4 (i. e. the second pressure stage of a five stage compressor).

the heating body, whereby they are con ensed, the product of condensation In this way the vapors directly introduced into the li uid are only compressed to a pressure su cient to overcome the hydrostatic head present in the vessel 1 above the distributor 8, whereas the greater portion of the vapors utilized for heating purposes is passed through all-the stages of the compressor 4 and com ressed to a higher degree than the vapor le to the distributor 8.

I claim:

1. A process of evaporation. of a liquid, comprising with drawing all the vapors emanating from the liquid to be evaporated, compressmg them, indirectly heating the liquid by means of a portion of such com pressed vapors and liberating a second portion of the compressed vapors within the body of the liquld.

2. A process of evaporation of a liquid, comprising withdrawing all the vapors emanating from the liquid to be evaporated, compressing the greater part of said vapors, indirectly heating the llqllld' by said compressed vapors, compressing a second portion of said first mentioned vapors to a pressure sufiicient to overcome the hydrostatic head in said liquid and freein such second portion of vapor within the ody of said liquid.

3. Apparatus for evaporating liquids, comprising a vessel for containing the liquid to be evaporated, heating means therefor, .means for withdrawing and for compressing the vapors from said vessel and for supplying said. compressed vapors to said heatin means, and means for liberating a portion of the compressed vapors within the'lower part of said vessel.

4. Apparatus for evaporating liquids,

COIIIPIlSlIlg a vessel adapted to contain the liquid to be evaporated, heating means therefor, means for withdrawing and for compressing the'vapors from said vessel and for supplying the greater part of the-compressed vapors to said heating means, means

Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2515013 *Apr 10, 1946Jul 11, 1950Edward R KruhminVapor compression distillation apparatus
US2585591 *Oct 21, 1948Feb 12, 1952Roper John HHeating system
US2704120 *Dec 10, 1951Mar 15, 1955Swift & CoMethod of concentration of charrable heat-sensitive liquid
US2742102 *Dec 15, 1948Apr 17, 1956Internat Carbonic EngineeringProcess and apparatus for recovering carbon dioxide from exhaust gases
US2762429 *Nov 16, 1951Sep 11, 1956Swift & CoApparatus for concentrating heat sensitive liquids
US3189080 *Dec 14, 1961Jun 15, 1965Shell Oil CoCirculating solids dispersed in a liquid
US3249147 *Jun 14, 1963May 3, 1966Burnett & Rolfe LtdFilm evaporators
US3251428 *Oct 22, 1962May 17, 1966 Recovery op polyolepins from solution in a fluidized dryer
US3370636 *Feb 3, 1967Feb 27, 1968Combustion EngApparatus for reconcentrating liquid desiccant
US3595299 *Jul 28, 1969Jul 27, 1971Linde AgApparatus for the evaporation of low-temperature liquefied gases
US3956072 *Aug 21, 1975May 11, 1976Atlantic Fluidics, Inc.Vapor distillation apparatus with two disparate compressors
US4186058 *Apr 18, 1977Jan 29, 1980Fogel S JMethod and apparatus for high volume distillation of liquids
US4186060 *Feb 22, 1977Jan 29, 1980Fogel S JMethod and apparatus for high volume distillation of liquids
US4217176 *Feb 6, 1978Aug 12, 1980Aqua-Chem, Inc.Evaporator
US4259160 *Aug 4, 1978Mar 31, 1981Aqua-Chem, Inc.Vapor compression distiller and method
US4282067 *Aug 10, 1979Aug 4, 1981Jerome KatzApparatus for high volume distillation of liquids
US4282070 *May 30, 1978Aug 4, 1981Dan EgosiEnergy conversion method with water recovery
US4319964 *Aug 10, 1979Mar 16, 1982Jerome KatzApparatus for high volume distillation of liquids
US4322265 *Jun 3, 1980Mar 30, 1982Maloney-Crawford CorporationAtmospheric glycol reclaimer with vapor recycle
US4420373 *Aug 3, 1981Dec 13, 1983Dan EgosiEnergy conversion method and system
US4882009 *Jul 13, 1987Nov 21, 1989Four Nines, Inc.Apparatus for concentrating brine waters or dewatering brines generated in well drilling operation
US5645694 *Mar 31, 1993Jul 8, 1997Vacom Ii, L.P.Process and apparatus for vapor compression distillation
US6436242 *Feb 10, 2000Aug 20, 2002Pedro Joaquin Sanchez BelmarDevice and method for distilling water
US8608841Oct 18, 2010Dec 17, 2013Drystill Holdings Inc.Stripping absorption module
US8757599Oct 19, 2011Jun 24, 2014Drystill Holdings Inc.Stripping absorption module
Classifications
U.S. Classification159/16.3, 159/47.1, 122/26, 159/24.1, 203/26
International ClassificationB01D1/00, B01D1/28
Cooperative ClassificationB01D1/2843
European ClassificationB01D1/28D2