US1425020A - Method of evaporating liquors - Google Patents
Method of evaporating liquors Download PDFInfo
- Publication number
- US1425020A US1425020A US377141A US37714120A US1425020A US 1425020 A US1425020 A US 1425020A US 377141 A US377141 A US 377141A US 37714120 A US37714120 A US 37714120A US 1425020 A US1425020 A US 1425020A
- Authority
- US
- United States
- Prior art keywords
- pressure
- evaporator
- liquid
- heating
- condenser
- 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
Links
- 238000001704 evaporation Methods 0.000 title description 15
- 238000000034 method Methods 0.000 title description 8
- 238000010438 heat treatment Methods 0.000 description 28
- 239000007788 liquid Substances 0.000 description 22
- 230000008020 evaporation Effects 0.000 description 6
- 230000001276 controlling effect Effects 0.000 description 3
- 230000008016 vaporization Effects 0.000 description 3
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 241000287181 Sturnus vulgaris Species 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000006854 communication Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 235000015203 fruit juice Nutrition 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/0094—Evaporating with forced circulation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/28—Evaporating with vapour compression
Definitions
- the present invention relates to a method for economically effecting the evaporation of liquids and the concentration of liquors, which processes must be accomplished under reduced pressure, such as the evaporation of fruit juices, milk, and the like. It is. an object of the invention to provide a process of this type in which the vapors formed in the evaporator are subjected, by means of a blower, to a somewhat higher absolute pressure and. consequently higher tempera ture than that at which the evaporation is accomplished. The compressed vapors are then utilized as heating medium by passing them through the heating element of the Due to the large volume and the usually small increase in pressure, the
- blower is preferably of the turbo type
- It is a still further object to provide an apparatus of this type comprising a motor driven blower of such character that the blower is operated to maintain the evaporator chamber at an approximately constant pressure, whereby regulation of the above mentioned condenser to alter the amount of vapors which are condensed within the evaporator heating element will efiect a variation in the vapor output of the evaporator.
- the drawing represents by way of example an embodiment of the invention, in which a is the evaporator and b the heating system therefor.
- Liquid may be admitted to the evaporator a through the inlet pipe a.
- the surface of the liquid is preferably maintained at a level below the heating tubes 5, as shown, and after supplying a batch of liquid operation is preferably conducted until concentration of this batch is complete, at which time the concentrated liquid may be drawn off through the outlet (2
- concentration of this batch is complete, at which time the concentrated liquid may be drawn off through the outlet
- the absolute pressure of the vapors is increased by a certain amount in the blower, the vapors being thereupon. passed through the tube 7 into the heating system I) where they efi'eet the evaporation.
- the condensate formed in the tubes of the heating system is passed, together with the still uncondensed portion of the heating vapors through the tube 9 into a condenser 71 rated in circulation and sprays said liquid through the tube 0 over the heating system.
- a motor of this type can be made to regulate for substantially constant pressure within the evaporating chamber throughout the entire range of pressures which it is desired to employ in the condenser h. It is, however, to be understood that a similar result might be obtained by roviding a shunt wound or other type 0F motor whose speed is controlled by means of a pressure or temperature sensitive element placed in communica tion with the evaporating chamber.
- Apparatus for evaporating liquids comprising a container for the liquid, aheating chamber in heat transferrng relation to said liquid, means for Withdrawing vapor from said container and subsequently returning it to said heating chamber at higher pressure, said vapor serving as heating medium tor vaporizing the liquid, and means for controlling the pressure in said heating chamber and the vapor output of the evaporator, said means comprising a condenser for receiving the fluid discharge from the heating chamber, and a vacuum pump connected to said condenser.
- Apparatus for evaporating liquids comprisng a container for the liquid, a heating chamber in heat transferring relation'to said liquid, means for withdrawing vapor from said container and subsequently returning it to said heating chamber at higher pressure, said vapor serving as heating medium for vaporizing the liquid, a condenser connected to the outlet end of said heating chamber, and means for varying the pressure in the condenser for regulating the vapor output of the evaporator.
- Apparatus for evaporating liquids comprising a container for the liquid, said container being maintained at sub-atmospheric pressure, a heating chamber in heat transferring relation to said liquid, means for withdrawing vapor from said container and subsequently returning it to said heating chamber at higher pressure, said vapor serving as heating medium for vaporizing the liquid, a condenser connected to the outlet end of said heating chamber, and means for varying the pressure in the condenser and for regulating the vapor output of the evaporator.
Description
E. JOSSE AND W. GENSECKE.
METHOD OF EVAPORATING LIQUORS.
' APPLICATION FILED APR.27. 1920.
1,4 25,@2@ m d Aug. 8, 1922;,
Q Mal Wfinasa e5: lnventurs may.
' Republic, residing evaporator.
entrain stares rarest series.
EMIL JOSSE, 0F BERLIN-LAUKW'ITZ, AND WILHELM GENSECKE, OF BAD HOMBERG,
GERMANY.
METHOD OF EVAPORATING LIQUORS.
To all whom it may concern:
Be it known that we, EMIL JossE and VVILHELM GnNsEoK-n, citizens of the German at Berlin-Laukwitz, Lessingstrasse 14, respectively, Bad Homburg v. d. Hohe, Homburgerstrasse 87, have invented certain new and useful Improvements in Methods of Evaporating Liquors (for which we'have filed applications as follows: Germany, Ser. No. J. 17235 IV/12a, filed February 27 1915; Austria, Ser. No. A. 4:047-19, filed ovember 3, 1919; Switzerland, Ser. No. 2 122, filed November 4, 1919; Sweden, Ser. No. 5073 -19, filed November Norway, Ser. No. 18318,-filed. November 12, 1919; Hungary, Ser. No. 15157M. 6633, filed November 1 1, 1919; Czechia, Ser. No. P. 41549-1919, filed November 20, 1919; France, Ser. No. 1226 11, filed January 28, 1920'; England, Ser. No. 3895-20, filed February 9, 1920; Holland, Ser. No. 17 186, filed December 21, 1920; Spain, Ser. No. 12276-2582, filed January 13, 1921; Italy, Ser. No. 40628, filed January 15, 1921), of which the following is a specification.
The present invention relates to a method for economically effecting the evaporation of liquids and the concentration of liquors, which processes must be accomplished under reduced pressure, such as the evaporation of fruit juices, milk, and the like. It is. an object of the invention to provide a process of this type in which the vapors formed in the evaporator are subjected, by means of a blower, to a somewhat higher absolute pressure and. consequently higher tempera ture than that at which the evaporation is accomplished. The compressed vapors are then utilized as heating medium by passing them through the heating element of the Due to the large volume and the usually small increase in pressure, the
' blower is preferably of the turbo type, the
excess heat imparted to the vapors by reason of their compression in passing through the blower being eliminated by discharging the uncondensed vapors from the heating system of the evaporator into a condenser, which condenser is preferably water-cooled and effects condensation of these residual vapors, and at the same time establishes a. pressure within the condenser which is materially less than the pressure at the compression side of the blower.
It is a further object to provide in an Specification of Letters Patent.
Application filed April 27, 1920. Serial No. 377,141.
Patented. Au 8, 192a.
apparatus of this type a condenser or' equivalent element associated with the outlet end of the heating tubes, the pressure of which maybe varied so that a greater or lesser quantity of the vapors may be drawn through the heating element uncondensed, with the result that a correspondingly lesser or greater amount of heat is given up to the liquid being vaporized. V
It is a still further object to provide an apparatus of this type comprising a motor driven blower of such character that the blower is operated to maintain the evaporator chamber at an approximately constant pressure, whereby regulation of the above mentioned condenser to alter the amount of vapors which are condensed within the evaporator heating element will efiect a variation in the vapor output of the evaporator.
The drawing represents by way of example an embodiment of the invention, in which a is the evaporator and b the heating system therefor. Liquid may be admitted to the evaporator a through the inlet pipe a. The surface of the liquid is preferably maintained at a level below the heating tubes 5, as shown, and after supplying a batch of liquid operation is preferably conducted until concentration of this batch is complete, at which time the concentrated liquid may be drawn off through the outlet (2 It is to be understood, however, that liquid may be admitted continuously at a and discharged continuously from a if desired. The vapors produced are led through the tube 0 to a blower 0Z actuated by any suitable motor 6. The absolute pressure of the vapors is increased by a certain amount in the blower, the vapors being thereupon. passed through the tube 7 into the heating system I) where they efi'eet the evaporation. The condensate formed in the tubes of the heating system is passed, together with the still uncondensed portion of the heating vapors through the tube 9 into a condenser 71 rated in circulation and sprays said liquid through the tube 0 over the heating system.
Variations in pressure within the condenser it will produce ariations in the total pressure difference impressed across the heating chamber of the evaporator and will change the velocity of the fluid through. this chamber. Consequently more or less of they pors within the heating element 7) and the slower flow of the vapors through the heating element, an increased quantity of heat will be given up to the heat transferring walls of the tubes 5 with. the result that a larger quantity of vapor will be evolved within the evaporator chamber. It is evident that, in order to maintain substantially constant pressure and temperature conditions in this chamber, that the motor 6 must speed up sufliciently to withdraw the excess quantity of vapors formed and still maintain the same pressure within the evaporator chamber. That is, the motor 6! may be a compound wound electric motor whose characteristics are such that its speed increases with increased load. A motor of this type can be made to regulate for substantially constant pressure within the evaporating chamber throughout the entire range of pressures which it is desired to employ in the condenser h. It is, however, to be understood that a similar result might be obtained by roviding a shunt wound or other type 0F motor whose speed is controlled by means of a pressure or temperature sensitive element placed in communica tion with the evaporating chamber.
It is to be noted that a change in the condenser pressure effects passage of more or less uncondensed vapors through the heating element of the evaporator and consequently varies the quantity of heat supplied to the liquid under evaporation. However, since the temperature and pressure conditions within the evaporator chamber are maintained substantially constant, the changed quantity of heat supplied to the liquid under evaporation will be reflected in a correspondingly changed output of the evaporator. It is obvious that further modifications, such as a different method of controlling the operation of the blower, a
changed manner of controlling the conby Letters Patent of the United States is 1. Apparatus for evaporating liquids, comprising a container for the liquid, aheating chamber in heat transferrng relation to said liquid, means for Withdrawing vapor from said container and subsequently returning it to said heating chamber at higher pressure, said vapor serving as heating medium tor vaporizing the liquid, and means for controlling the pressure in said heating chamber and the vapor output of the evaporator, said means comprising a condenser for receiving the fluid discharge from the heating chamber, and a vacuum pump connected to said condenser. I
2. Apparatus for evaporating liquids, comprisng a container for the liquid, a heating chamber in heat transferring relation'to said liquid, means for withdrawing vapor from said container and subsequently returning it to said heating chamber at higher pressure, said vapor serving as heating medium for vaporizing the liquid, a condenser connected to the outlet end of said heating chamber, and means for varying the pressure in the condenser for regulating the vapor output of the evaporator.
3. Apparatus for evaporating liquids, comprising a container for the liquid, said container being maintained at sub-atmospheric pressure, a heating chamber in heat transferring relation to said liquid, means for withdrawing vapor from said container and subsequently returning it to said heating chamber at higher pressure, said vapor serving as heating medium for vaporizing the liquid, a condenser connected to the outlet end of said heating chamber, and means for varying the pressure in the condenser and for regulating the vapor output of the evaporator.
In testimony whereof, we afiix our signa- I H. K601i, I A. SoHijN.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US377141A US1425020A (en) | 1920-04-27 | 1920-04-27 | Method of evaporating liquors |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US377141A US1425020A (en) | 1920-04-27 | 1920-04-27 | Method of evaporating liquors |
Publications (1)
Publication Number | Publication Date |
---|---|
US1425020A true US1425020A (en) | 1922-08-08 |
Family
ID=23487924
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US377141A Expired - Lifetime US1425020A (en) | 1920-04-27 | 1920-04-27 | Method of evaporating liquors |
Country Status (1)
Country | Link |
---|---|
US (1) | US1425020A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2660236A (en) * | 1947-01-15 | 1953-11-24 | Morton Salt Co | Vapor recompression system |
US3245883A (en) * | 1962-01-29 | 1966-04-12 | Aqua Chem Inc | Closed circuit distillant feed with indirect heat exchange condensation |
-
1920
- 1920-04-27 US US377141A patent/US1425020A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2660236A (en) * | 1947-01-15 | 1953-11-24 | Morton Salt Co | Vapor recompression system |
US3245883A (en) * | 1962-01-29 | 1966-04-12 | Aqua Chem Inc | Closed circuit distillant feed with indirect heat exchange condensation |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US20170151507A1 (en) | Combination multi-effect distillation and multi-stage flash evaporation system | |
US1799478A (en) | Method of evaporating liquids and apparatus therefor | |
US849579A (en) | Art of distilling, concentrating, and evaporating liquids. | |
US5417084A (en) | Vacuum concentrating plant | |
US1150713A (en) | Evaporator. | |
US4181577A (en) | Refrigeration type water desalinisation units | |
US3300392A (en) | Vacuum distillation including predegasification of distilland | |
US3165435A (en) | Evaporation apparatus and method | |
US1425020A (en) | Method of evaporating liquors | |
US4292744A (en) | Separation apparatus for a condensation-drying plant | |
US1390677A (en) | Evaporating apparatus | |
US4342624A (en) | Vapor compression liquid treating system | |
US3471373A (en) | Automatic control system for vapor compression distilling unit | |
US2290209A (en) | Distillation apparatus | |
US3901768A (en) | Distillation method and apparatus | |
US236940A (en) | Jules l | |
US3395084A (en) | Multistage still with hot condensate stageheater | |
US2388328A (en) | Still | |
US3360442A (en) | Multi-stage flash evaporator | |
US1508985A (en) | Method and apparatus for treating liquid | |
US2090985A (en) | Evaporating apparatus and method | |
EP0152139A2 (en) | Process and apparatus for the evaporation of liquids | |
US1401116A (en) | System for removing air and gases from water | |
US1463158A (en) | System for removing air and gases from water | |
JPH01284302A (en) | Centrifugal film vacuum evaporator |