US546946A - Eduard theisen - Google Patents
Eduard theisen Download PDFInfo
- Publication number
- US546946A US546946A US546946DA US546946A US 546946 A US546946 A US 546946A US 546946D A US546946D A US 546946DA US 546946 A US546946 A US 546946A
- Authority
- US
- United States
- Prior art keywords
- water
- condenser
- air
- temperature
- condensing
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 32
- 239000007789 gas Substances 0.000 description 16
- 238000001704 evaporation Methods 0.000 description 12
- 239000000498 cooling water Substances 0.000 description 10
- 230000000153 supplemental Effects 0.000 description 10
- 238000009833 condensation Methods 0.000 description 8
- 230000005494 condensation Effects 0.000 description 8
- 238000001816 cooling Methods 0.000 description 8
- 230000000875 corresponding Effects 0.000 description 4
- 230000001627 detrimental Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000002826 coolant Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B1/00—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
- F28B1/02—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using water or other liquid as the cooling medium
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S165/00—Heat exchange
- Y10S165/184—Indirect-contact condenser
- Y10S165/193—First-stage condenser serially connected to second-stage condenser
Definitions
- the rapidity of evaporation of the evaporative condensing-water, and consequently the intensity of the condensation, will depend mainly upon the difierence between the temperature of such water and that of the atmospheric air passing in contact therewith.
- the temperature of the atmospheric air is practically a determined factor, the said difference of temperature will be increased when the temperature of the cooling-water is kept as high as possible, and nearly equal to that of the steam entering the condenser.
- I prevent such detrimental cooling effect, and at the same time reduce the volume of the uncondensed gases before they enter the air-pump by employing the aforesaid supplemental supply of cold condensingwater to cool the uncondensed gases withdrawn from the evaporative surface condenser, and consequently reduce theirsvolume before they enter the air-pump, the supplemental condensing-water being thereby correspondingly raised in temperature before it is added to the main body of evaporative condensing-water of the condenser.
- the exhaust-steam from the steam-engine or other apparatus is condensed on the inner surface of the evaporative surface condenser R, in which the steam enters at A.
- the water of condensation runs down the tubes into the bottom compartment and is drawn off at We.
- the outer surfaces of the condenser R receive a supply of evaporative condensing-water from the supply We, and after flowing down the outer surfaces of the tubes this water is drawn off at We, as indicated by the arrows. Atmospheric air is made to impinge upon the film of water flowing down the tubes R, a portion of which is consequently continuously evaporated and carried off thereby.
- This loss is continuously replaced by an additional supply of condensing water which enters at ⁇ Va, after having been made to pass through a casing ,S' in contact with the refrigerating-worm S, through which the uncondensed gases are drawn off from the condenser R by the air-pump (not shown) connected to S at L, such gases being thus cooled down to a corresponding extent before entering the air-pump, while the additional condensing-water entering at Ta is warmed to a corresponding extent before mixing with the main supply of condensing-water.
Description
(No Model.)
E. THEISEN.
SURFACE CONDENSER.
No. 546,946. Patented Sept. 24, 1895.
a. 91. QM. 2% Q-z ATENT Futon,
EDUARD THEISEN, OF BADEN-BADEN, GERMANY.
SURFACE CONDENSER.
SPECIFICATION forming part of Letters Patent No. 546,946, dated September 24, 1895.
Application filed August 28, 1894. Serial No. 521,555. (No model.) Patented in Belgium August 4, 1894, No. 111,263; in France August 4, 1894, No. 240,538; in England August 11,1894, No. 5,351; in Austria September 21, 1894, N0.
44/4,.978, and in Hungary January 5, 1895,110- 1,862.
To ail whom, it may concern:
Be it known that I, EDUARD THEISEN, engineer, a citizen of the United States, residing at Kronprinzenstrasse 4, Baden-Baden, Germany, have invented a certain new and useful Surface Condenser, (for which I have obtained Letters Patent in Belgium, dated August 4, 1894,No.111,263; in France, dated August 4, 1894, No. 240,538; in Austria, dated September 21, 1894, No. 44/4,.378; in Hungary, dated January 5, 1895, No. 1,862, and in Great Britain, dated August 11, 1894, No. 5,351,) of which the following is a specification.
In surface condensers working with cooling by evaporation, where the actual cooling medium is the atmospheric air, the coolingwater only serving by its evaporation to transfer to the air the heat of the steam which is set free on condensation, there is, in consequen cc of the comparatively high condensing temperature of about centigrade, when compared with the vacuum obtained, a considerable volume of uncondensed gases contained in the condenser. In addition such air as leaks in, owing to want of tightness of the cylinder, stuffing-boxes, pipe connections, &c., is the more detrimental the higher the temperature of the condenser is. This condition is especially to be observed when for the purpose of economy in first outlay and in subsequent working means of cooling the Water are omitted and the cooling-water is used over and over again, with an addition of fresh cooling-water to make good that lost by evaporation, this quantity being nearly equal to that of the water of condensation from the steam. Now the volume of uncondensed gases which have to be withdrawn from the condenser determines the size and working of the air-pump, and on this ground it is desirable that the uncondensed gases should have as low a temperature as possible when entering the air-pump, as the lower the temperature is the smaller will be the volume, and a better vacuum will be easily gained. 0n the other hand, the rapidity of evaporation of the evaporative condensing-water, and consequently the intensity of the condensation, will depend mainly upon the difierence between the temperature of such water and that of the atmospheric air passing in contact therewith. The greater this difference is the more rapid will be the evaporation, or, in other words, the smaller can be the amount of surface of the condenser for performing a certain duty. As now the temperature of the atmospheric air is practically a determined factor, the said difference of temperature will be increased when the temperature of the cooling-water is kept as high as possible, and nearly equal to that of the steam entering the condenser. Now, according to my present invention, I prevent such detrimental cooling effect, and at the same time reduce the volume of the uncondensed gases before they enter the air-pump by employing the aforesaid supplemental supply of cold condensingwater to cool the uncondensed gases withdrawn from the evaporative surface condenser, and consequently reduce theirsvolume before they enter the air-pump, the supplemental condensing-water being thereby correspondingly raised in temperature before it is added to the main body of evaporative condensing-water of the condenser. By this means it will be seen that the double beneficial effect is obtained of, on the one hand, considerably reducing the size and work of the air-pump for performing a certain amount of duty, and, on the other hand, of utilizing, first, the low temperature of the supplemental cooling-water, and, secondly, the quantity of this water for cooling by evaporation.
On the accompanying drawing is shown by way of example a diagrammatic section of an apparatus by which the above described method of operating can be carried out.
The exhaust-steam from the steam-engine or other apparatus is condensed on the inner surface of the evaporative surface condenser R, in which the steam enters at A. The water of condensation runs down the tubes into the bottom compartment and is drawn off at We. The outer surfaces of the condenser R receive a supply of evaporative condensing-water from the supply We, and after flowing down the outer surfaces of the tubes this water is drawn off at We, as indicated by the arrows. Atmospheric air is made to impinge upon the film of water flowing down the tubes R, a portion of which is consequently continuously evaporated and carried off thereby. This loss is continuously replaced by an additional supply of condensing water which enters at \Va, after having been made to pass through a casing ,S' in contact with the refrigerating-worm S, through which the uncondensed gases are drawn off from the condenser R by the air-pump (not shown) connected to S at L, such gases being thus cooled down to a corresponding extent before entering the air-pump, while the additional condensing-water entering at Ta is warmed to a corresponding extent before mixing with the main supply of condensing-water.
It will be evident that the apparatus for carrying out my above-described method of operating can be variously constructed without departing from the nature of my invention. The accompanying diagram is only intended as an example of the mode of carrying the invention into practice.
Having thus described the nature of my invention and the best means I know for carrying the same into practical eti'ect, I claim The combination with an evaporative surface condenser, of a supplemental surface condenser through which the uncondensed gases from the evaporative surface condenser are to be drawn off on their way to an air pump, the outer casing, of the supplemental surface condenser being made to communicate at one end with a supply of cold water and at the other end with the compartment of the evaporative surface condenser into which the worm evaporative condensing water is sent, substantially asshown and described and for the purposes specified.
In testimony whereof I have signed my name to this specification, in the presence of two subscribing witnesses, this 7th day of August, A. D. 1894.
EDUARD TIIEISEN. Witnesses:
ERNEST THERION, T. KLAUSMANN.
Publications (1)
Publication Number | Publication Date |
---|---|
US546946A true US546946A (en) | 1895-09-24 |
Family
ID=2615689
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US546946D Expired - Lifetime US546946A (en) | Eduard theisen |
Country Status (1)
Country | Link |
---|---|
US (1) | US546946A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2868314A (en) * | 1956-01-18 | 1959-01-13 | Black Sivalls & Bryson Inc | Apparatus for separating fluids |
US2944966A (en) * | 1954-02-19 | 1960-07-12 | Allen G Eickmeyer | Method for separation of fluid mixtures |
-
0
- US US546946D patent/US546946A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2944966A (en) * | 1954-02-19 | 1960-07-12 | Allen G Eickmeyer | Method for separation of fluid mixtures |
US2868314A (en) * | 1956-01-18 | 1959-01-13 | Black Sivalls & Bryson Inc | Apparatus for separating fluids |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2548508A (en) | Thermal system | |
GB191218511A (en) | Improvements in Absorption Machines for Transforming Heat, Cold and Mechanical Work. | |
US2353966A (en) | Liquid cooling system for internal-combustion engines | |
JPS60175979A (en) | Multiple effect absorption type refrigerator | |
JPS62500045A (en) | Coolers and heat pumps as well as ejector pumps for them | |
US546946A (en) | Eduard theisen | |
US2907175A (en) | Cold-gas refrigerating apparatus | |
JP3515998B2 (en) | Mechanical compressor | |
US1004468A (en) | Method of drying air. | |
US1134269A (en) | Refrigerating apparatus. | |
US2481520A (en) | Cooling cycle for internal-combustion engines | |
US1960809A (en) | Refrigerating apparatus | |
US2131782A (en) | Cooling fluids to low temperatures and diffusion refrigerating machines therefor | |
US1427395A (en) | Combustion motor | |
US344006A (en) | Cassius clay palmer | |
US670829A (en) | Generator. | |
US2496041A (en) | Locomotive power plant | |
JPS6314674B2 (en) | ||
US1728947A (en) | Art of separation by liquefaction | |
GB190500646A (en) | Improvements in Refrigerating Apparatus. | |
US638491A (en) | Absorption refrigerating-machine. | |
JPH04244565A (en) | Condenser | |
US20240060690A1 (en) | Absorption chiller system with a transport membrane heat exchanger | |
US223555A (en) | Cypbien m | |
US20230234424A1 (en) | Air-conditioning system for motor vehicle |