US1425005A - Method of evaporating liquors and apparatus therefor - Google Patents
Method of evaporating liquors and apparatus therefor Download PDFInfo
- Publication number
- US1425005A US1425005A US377142A US37714220A US1425005A US 1425005 A US1425005 A US 1425005A US 377142 A US377142 A US 377142A US 37714220 A US37714220 A US 37714220A US 1425005 A US1425005 A US 1425005A
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- United States
- Prior art keywords
- vapor
- evaporating
- heating
- container
- liquid
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Links
- 238000001704 evaporation Methods 0.000 title description 18
- 238000000034 method Methods 0.000 title description 7
- 238000010438 heat treatment Methods 0.000 description 23
- 239000007788 liquid Substances 0.000 description 23
- 230000006835 compression Effects 0.000 description 4
- 238000007906 compression Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003467 diminishing effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 235000002020 sage Nutrition 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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Classifications
-
- 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
- This invention relates to improvements in the method of evaporating liquors and apparatus therefor.
- thermic efficiency is the greater in proportion as the difference of temperature is smaller, that is to say the lower the ratio of compression employed.
- the disadvantage ocours that a considerable portion of the compressed hot vapor which is used as heating vapor is not condensed so that the number of heat units given off by the heating vapor is considerablyless than the heat required for evaporation.
- the deficiency of heat from the heating vapor is covered by the heat of the liquid to be evaporated-the result being that the temperature of the latter falls continuously.
- the evaporating plant ceases to function regularly, the efficiency diminishing and the temperature falling continuously.
- the deficiency of heat from the heating vapor is compensated by the introduction of extraneous heat for example by means of live steam.
- the introduction of live steam can be completely or to a large extent dispensed with by a further measure,
- the pressure of the compressed vapor is the sum of the partial pressures of vapor and air.
- the weight of vapor decreases, that is to say, the partial pressure of the vapor continuously falls, whereas that of the air continuously increases so that the sum of the two remains the same.
- the temperature of such admixture is determined by the partial pressure of the vapor and when this has fallen to such an extent that its value is equal to that of the vaporpressure of the evaporating medium equilibrium of temperature is attained and thus any further heating effect ceases, so that the amount of water vapor which is now still contained in the compressed medium can no longer be utilized for heatingthe evaporator.
- the essential feature of the invention consists in that an amount of heat sufficient for evaporation is made available by the vapor compressor circulating an amount of vapor which is greater than the amount of vapor generated in the evaporator.
- This can be effected by connecting the outlet chamber of the heating-tube system of the evaporator with the evaporating chamber of the evaporator or with the suction pipe of the compressor by means of a pipe suitably provided with a closing means adapted to modify its sectional area.
- a is the evaporator in which the liquid to be evaporated reaches to the level I.
- the vapors generated in the evaporator pass through the tube 0 into the compressor d, are compressed therein and forced through 6 into the heating system
- the condensate and the uncondensed vapors leave at g; the condensate runs oil through h, Whilst the whole or part of the uncondensed vapors are returned to the evaporator' a, through the pipe i provided with the valve is which pipe is essential for carrying out the object of the invention.
- the pipe Z leads into the open air, or in case the plant is working with a vacuum into a condensor provided with an air pump.
- a plant for evaporating liquids comprising a container for the liquid to be evaporated and a chamber for the heating medium in heat exchanging proximity to said liquid, means for withdrawing the vapor from said container, means for withdrawing mixed vapor and condensate from said chamber, separating the vapor from the condensate, and joining said vapor with the vapor generated in said container, and means for compressing these joined vapors and conveying them into said heating chamber.
- a plant for evaporating liquids comprising a container for the liquid to be evaporated, and a chamber for the heating medium in heat exchanging proximity to said liquid, acompressor pump having its low pressure 'side in communication with said container and the outlet of said heating chamber, and its high pressure side discharging into said chamber.
- a plant for evaporating liquids comprising a container for the liquid to be evaporated and a chamber for the heating medium in heat exchanging proximity to said liquid, aline for conveying the vapor away from. said container, means for withdrawing mixed vapor and condensate from said chamber, a trap for separating the vapor from the condensate, a passage of adjustable section connecting said trap and said vapor line for joining the uncondensed vapor with the vapor generated in said'container, and means for compressing these joined vapors andconveying them into said heating chamber.
- a plant for evaporating liquids comprising a container for the liquid, a heating chamber in heat transferring relation to said liquid, a fluid passage connecting said heating chamber with said container for conveying uncondensed vapors from the'former to the latter, a second fluid passage connecting said container with said heating chamber, and a pump in said second pas sage for compressing the vapors from the container and delivering them to said heating chamber at a rate higher than that at which liquid in the said container is being evaporated.
- a plant for evaporating liquids the combination of a container for the liquid to be evaporated, a heat exchanger in said container, means for compressing the hot vapors issuing from said container and passing them through said heat exchanger, outlet means for the uncondensed portion of the vapor from said heat exchanger, and means for joining said uncondensed vapor with the vapor-generated in the container prior to compression.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
v w. GENSECKE. v v METHOD OF EVAPOR'ATING LIQUORS AND APPARATUS THEREFUR.
ARPLICATION FILED APR. 21, 19 20-- 1L 4i25,@5o
. w'mLM zmwzab, Wfiriessea: Inventor:
6W, @w, W $4 LMMk/L,
I WQAMLHAL Patented M489 1922.,
@FWCEO WILHELM GENSECKE, 0F BAD HOMBURG, GERMANY.
METHQD 01E EVAPORATING LIQUORS AND APPARATUS THEREFOR.
memos.
Specification of Letters Patent.
Patented Aug. 8, 1922.,
Application filed April 27, 1920. Serial No. 377,142.
T 0 all whom it may concern:
Be it known that I, WILHELM GENSECKE, citizen of the German Republic, residing at Bad Homburg on the Hohe, I-Iomburgerstrasse 87 Germany, have invented certain new and useful Improvements in Methods of Evaporating Liquors and Apparatus Therefor, (for which I have filed applications in Germany, Ser. No. M. 65107 IV/12a, filed March 13, 1919,Austria, Ser. No. A 4048-19, filed Nov. 3 1919, Switzerland, Ser. No. 2423, filed Nov. 4, 1919, Sweden Ser. No. 5074-1919, filed Nov. 11, 1919, Norway Ser. No. 18417, filed Nov. 21, 1919, CzechiaSer. No. P. 4589-19, filed Dec. 3, 1919, Hungary Ser. No. 16359-M, 6652, filed Dec. 6, 1919, Holland Ser. No. 17465, filed Dec. '18, 1920, Spain Ser. No. 12277-2583, filed Jan. 13, 21, France Ser. No. 122642, filed Jan. 28, 1920, England Ser. No. 389620, filed Febr. 9, 1920 Final NO. 140059, Italy Ser. No. 40629, filed J an. 15, 1921), of which thefollowing is a specification.
This invention relates to improvements in the method of evaporating liquors and apparatus therefor.
In methods of evaporating or concentrating in which the hot vapors after having been compressed are used as heating agent for the evaporators, the thermic efficiency is the greater in proportion as the difference of temperature is smaller, that is to say the lower the ratio of compression employed. However, in this case the disadvantage ocours that a considerable portion of the compressed hot vapor which is used as heating vapor is not condensed so that the number of heat units given off by the heating vapor is considerablyless than the heat required for evaporation. In consequence the deficiency of heat from the heating vapor is covered by the heat of the liquid to be evaporated-the result being that the temperature of the latter falls continuously. The evaporating plant ceases to function regularly, the efficiency diminishing and the temperature falling continuously. In order to maintain a regular working of the evaporating plant according to the present invention the deficiency of heat from the heating vapor is compensated by the introduction of extraneous heat for example by means of live steam. However, also the introduction of live steam can be completely or to a large extent dispensed with by a further measure,
even when the temperature difference in the evaporator is small, that is to say with a small compression ratio in the compressor. This further inventive measure is based on the recognition that the cause of the incomplete condensation of the compressed hot vapor is less attributable to the heating sur face of the evaporator, which for technical reasons is more or less restricted, than to the presence of an admixture of air which in practice can never be completely avoided.
Thisprocess can be explained physically on the base of Daltons law of partial pressures. The pressure of the compressed vapor is the sum of the partial pressures of vapor and air. In proportion as condensation is effected and progresses, the weight of vapor decreases, that is to say, the partial pressure of the vapor continuously falls, whereas that of the air continuously increases so that the sum of the two remains the same. The temperature of such admixture, however, is determined by the partial pressure of the vapor and when this has fallen to such an extent that its value is equal to that of the vaporpressure of the evaporating medium equilibrium of temperature is attained and thus any further heating effect ceases, so that the amount of water vapor which is now still contained in the compressed medium can no longer be utilized for heatingthe evaporator.
The essential feature of the invention consists in that an amount of heat sufficient for evaporation is made available by the vapor compressor circulating an amount of vapor which is greater than the amount of vapor generated in the evaporator. This can be effected by connecting the outlet chamber of the heating-tube system of the evaporator with the evaporating chamber of the evaporator or with the suction pipe of the compressor by means of a pipe suitably provided with a closing means adapted to modify its sectional area. The result thus obtained is that the volume of vapor passed through the heating tube system need not be completely condensed and that the reuired heating effect is attained in spite of tie presence of air.
The drawing represents the embodiment of the object of the invention by way of example. a is the evaporator in which the liquid to be evaporated reaches to the level I. The vapors generated in the evaporator pass through the tube 0 into the compressor d, are compressed therein and forced through 6 into the heating system The condensate and the uncondensed vapors leave at g; the condensate runs oil through h, Whilst the whole or part of the uncondensed vapors are returned to the evaporator' a, through the pipe i provided with the valve is which pipe is essential for carrying out the object of the invention. The pipe Z leads into the open air, or in case the plant is working with a vacuum into a condensor provided with an air pump.
What I claim as new and desire to secare by Letters Patent of the United States 18 1. In a plant for evaporating liquids comprising a container for the liquid to be evaporated and a chamber for the heating medium in heat exchanging proximity to said liquid, means for withdrawing the vapor from said container, means for withdrawing mixed vapor and condensate from said chamber, separating the vapor from the condensate, and joining said vapor with the vapor generated in said container, and means for compressing these joined vapors and conveying them into said heating chamber.
2. Ina plant for evaporating liquids comprising a container for the liquid to be evaporated, and a chamber for the heating medium in heat exchanging proximity to said liquid, acompressor pump having its low pressure 'side in communication with said container and the outlet of said heating chamber, and its high pressure side discharging into said chamber.
3. In a plant for evaporating liquids comprising a container for the liquid to be evaporated and a chamber for the heating medium in heat exchanging proximity to said liquid, aline for conveying the vapor away from. said container, means for withdrawing mixed vapor and condensate from said chamber, a trap for separating the vapor from the condensate, a passage of adjustable section connecting said trap and said vapor line for joining the uncondensed vapor with the vapor generated in said'container, and means for compressing these joined vapors andconveying them into said heating chamber.
4. A plant for evaporating liquids, comprising a container for the liquid, a heating chamber in heat transferring relation to said liquid, a fluid passage connecting said heating chamber with said container for conveying uncondensed vapors from the'former to the latter, a second fluid passage connecting said container with said heating chamber, and a pump in said second pas sage for compressing the vapors from the container and delivering them to said heating chamber at a rate higher than that at which liquid in the said container is being evaporated.
5. In a plant for evaporating liquids the combination of a container for the liquid to be evaporated, a heat exchanger in said container, means for compressing the hot vapors issuing from said container and passing them through said heat exchanger, outlet means for the uncondensed portion of the vapor from said heat exchanger, and means for joining said uncondensed vapor with the vapor-generated in the container prior to compression.
6. The method of evaporating liquids in which the vapor arising from said liquid together with the uncondensed portion of the heating vapor are compressed and used as the'heating medium, thus returning to the liquid all or a part of the heat resident in said uncondensed vapor.
7. The method of evaporating liquids in which the liquid is vaporized, the resulting vapor compressed and passed in heat exchanging proximity to said liquid, and the heat of the uncondensed portion of said heating vapor utilized by uniting said portion directly with the evaporated hot vapor prior to compression.
In testimony whereof, I afl ix my signature in the presence of two witnesses.
WILHELM GENSECKE.
Witnesses
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US377142A US1425005A (en) | 1920-04-27 | 1920-04-27 | Method of evaporating liquors and apparatus therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US377142A US1425005A (en) | 1920-04-27 | 1920-04-27 | Method of evaporating liquors and apparatus therefor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1425005A true US1425005A (en) | 1922-08-08 |
Family
ID=23487930
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US377142A Expired - Lifetime US1425005A (en) | 1920-04-27 | 1920-04-27 | Method of evaporating liquors and apparatus therefor |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1425005A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2440416A (en) * | 1945-03-03 | 1948-04-27 | Alvan A Proudfoot | Vacuum rotary drum drier having means to compress evacuated vapors |
| US2477044A (en) * | 1946-04-22 | 1949-07-26 | James H Carmean | Apparatus for dehydrating materials |
| US2564475A (en) * | 1946-11-15 | 1951-08-14 | Gen Electric | Dehydration of frozen foods |
| US2574298A (en) * | 1946-12-20 | 1951-11-06 | Maytag Co | Heat exchanger clothes drier |
| US2640018A (en) * | 1949-07-25 | 1953-05-26 | Signal Oil & Gas Co | Method of steam distillation |
| US2895546A (en) * | 1955-08-30 | 1959-07-21 | Chicago Bridge & Iron Co | Method and apparatus for recompression evaporation |
| US3099607A (en) * | 1960-07-20 | 1963-07-30 | Gen Electric | Vapor recirculation distillation process and apparatus |
| US3175962A (en) * | 1961-02-28 | 1965-03-30 | Gen Electric | Falling film evaporator |
| US3249147A (en) * | 1962-07-03 | 1966-05-03 | Burnett & Rolfe Ltd | Film evaporators |
-
1920
- 1920-04-27 US US377142A patent/US1425005A/en not_active Expired - Lifetime
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2440416A (en) * | 1945-03-03 | 1948-04-27 | Alvan A Proudfoot | Vacuum rotary drum drier having means to compress evacuated vapors |
| US2477044A (en) * | 1946-04-22 | 1949-07-26 | James H Carmean | Apparatus for dehydrating materials |
| US2564475A (en) * | 1946-11-15 | 1951-08-14 | Gen Electric | Dehydration of frozen foods |
| US2574298A (en) * | 1946-12-20 | 1951-11-06 | Maytag Co | Heat exchanger clothes drier |
| US2640018A (en) * | 1949-07-25 | 1953-05-26 | Signal Oil & Gas Co | Method of steam distillation |
| US2895546A (en) * | 1955-08-30 | 1959-07-21 | Chicago Bridge & Iron Co | Method and apparatus for recompression evaporation |
| US3099607A (en) * | 1960-07-20 | 1963-07-30 | Gen Electric | Vapor recirculation distillation process and apparatus |
| US3175962A (en) * | 1961-02-28 | 1965-03-30 | Gen Electric | Falling film evaporator |
| US3249147A (en) * | 1962-07-03 | 1966-05-03 | Burnett & Rolfe Ltd | Film evaporators |
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