SU676291A1 - Water evaporating plant - Google Patents
Water evaporating plantInfo
- Publication number
- SU676291A1 SU676291A1 SU742046804A SU2046804A SU676291A1 SU 676291 A1 SU676291 A1 SU 676291A1 SU 742046804 A SU742046804 A SU 742046804A SU 2046804 A SU2046804 A SU 2046804A SU 676291 A1 SU676291 A1 SU 676291A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- water evaporating
- evaporating plant
- vacuum
- sample
- pipe
- Prior art date
Links
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
конденсируетс на внешней поверхности вакуумного концентратора 2. Образующийс конденсат стекает в полусферический поддон 6 н сбрасываетс через трубки 7 н 8 в гидрозатвор 3. Избыток образующегос пара сбрасываетс по пароотводной трубе 5, через гидрозатвор 3 в атмосферу.condenses on the outer surface of the vacuum concentrator 2. The resulting condensate flows into the hemispherical pan 6 n and is discharged through tubes 7 and 8 into the hydraulic lock 3. Excess steam is discharged through the steam discharge pipe 5, through the hydraulic lock 3 into the atmosphere.
Через устье вертикального участка трубы У проба после первой ступени упарки поступает самотеком в змеевиковый теплообменник 10, который подводит пробу к тангенциальному патрубку 4.Through the mouth of the vertical section of the pipe At the sample after the first stage of the evaporation enters by gravity into the coil heat exchanger 10, which brings the sample to the tangential nozzle 4.
Посто нство перепада давлени между сепаратором и концентратором и посто нство уровн в сепараторе обеспечивает посто нство скорости истечени пробы. Избыток жидкости в сепараторе сбрасываетс через трубу 8 в гидрозатвор.The stability of the pressure differential between the separator and the concentrator and the constancy of the level in the separator ensures the constant flow rate of the sample. The excess liquid in the separator is discharged through pipe 8 to the hydraulic lock.
Благодар указанному условию проба в вакуумном концентраторе 2 упариваетс на посто нную кратную величину, стекает в его нижнюю часть. По сифонной трубе 11 с устьем под зеркалом уровн в его центральной части (где температура пробы стабилизирована и отвечает величине вакуума ) проба подаетс в кондуктометрический датчик 12. Зар дка сифона обеспечиваетс подключением датчика к вакуумной магистрали вентилем 13. В рабочем состо нии вентиль 13 перекрыт.Due to this condition, the sample in the vacuum concentrator 2 is evaporated at a constant multiple value and flows down to its lower part. A siphon pipe 11 with a mouth under the level mirror in its central part (where the sample temperature is stabilized and corresponds to the vacuum) is fed to the conductivity sensor 12. The siphon charge is provided by connecting the sensor to the vacuum line by valve 13. In working condition, valve 13 is closed.
Дл обеспечени действи сифона, предотвращени срыва вакуума в нем дренажна труба 14 от датчика погружена в гидрозатвор на глубину, компенсирующую величину вакуума..To ensure that the siphon acts, to prevent the breakdown of the vacuum in it, the drainage pipe 14 from the sensor is immersed in a hydraulic lock to a depth that compensates for the amount of vacuum.
Вентили 15 служат дл начальной отстойки работы устройства. Вентиль 16 обеспечивает периодическую очистку нижней емкости сепаратора от осадков и взвесей. В рабочем состо нии вентиль 16 перекрыт. The valves 15 are used for initial settling of the device. The valve 16 provides periodic cleaning of the bottom of the tank separator from precipitation and suspensions. In working condition, the valve 16 is closed.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU742046804A SU676291A1 (en) | 1974-07-12 | 1974-07-12 | Water evaporating plant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU742046804A SU676291A1 (en) | 1974-07-12 | 1974-07-12 | Water evaporating plant |
Publications (1)
Publication Number | Publication Date |
---|---|
SU676291A1 true SU676291A1 (en) | 1979-07-30 |
Family
ID=20591900
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU742046804A SU676291A1 (en) | 1974-07-12 | 1974-07-12 | Water evaporating plant |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU676291A1 (en) |
-
1974
- 1974-07-12 SU SU742046804A patent/SU676291A1/en active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4686009A (en) | Distillation system | |
US4536257A (en) | Desalination system | |
EP0048596B1 (en) | Apparatus for removing salts and foreign matter from liquids (water) | |
IL32554A (en) | Apparatus for detecting scale formation in boilers and the like | |
US3300392A (en) | Vacuum distillation including predegasification of distilland | |
SU676291A1 (en) | Water evaporating plant | |
US3494835A (en) | System for the desalination of sea water | |
RU2005133496A (en) | DEVICE FOR SEALING WATER SEA WATER | |
US5232556A (en) | Water desalination apparatus | |
US3849260A (en) | Water distillation apparatus | |
JPS58156391A (en) | Apparatus for desalinating sea water | |
US3096257A (en) | Salt water converting apparatus | |
WO2017107019A1 (en) | Wind-powered seawater desalination apparatus | |
CA2759869C (en) | Control the process of distillation under pressure or vacuum without use of vacuum pumps, distileries are with different volumes, they distilling a raw material in dry or liquid condition, extracting for second time essential oils from liquid results obtained after distilation | |
CN201306703Y (en) | Steam trap | |
KR200179033Y1 (en) | Waste water evaporation concentration plant having function washing | |
SU1574542A1 (en) | Solar sea-water desalination plant | |
US127197A (en) | Improvement in vacuum-stills | |
CN206160799U (en) | Decline water film generating device | |
US1105443A (en) | Multiple-effect evaporating apparatus. | |
CN208532294U (en) | A kind of multiple-effect vertical tube falling evaporation solar energy sea water desalination apparatus | |
Spanhaak | A comparison of the operating characteristics of conventional multi-stage flash evaporation and multi-stage flash/fluidized bed evaporation | |
US747509A (en) | Feed-water heater. | |
KR100621740B1 (en) | Self-Level Control Unit for Desalination Plant | |
RU2296715C2 (en) | Sea water distilling plant |