PL101B1 - Boiler feed water distillation device. - Google Patents

Boiler feed water distillation device. Download PDF

Info

Publication number
PL101B1
PL101B1 PL101A PL10118A PL101B1 PL 101 B1 PL101 B1 PL 101B1 PL 101 A PL101 A PL 101A PL 10118 A PL10118 A PL 10118A PL 101 B1 PL101 B1 PL 101B1
Authority
PL
Poland
Prior art keywords
water
feed water
boiler feed
distillation device
steam
Prior art date
Application number
PL101A
Other languages
Polish (pl)
Filing date
Publication date
Application filed filed Critical
Publication of PL101B1 publication Critical patent/PL101B1/en

Links

Description

Wiadomem jest, ze uzyteczna praca przyrzadów do destylacji moze zostac zwiekszona przez to, ze czesc pary, po¬ wstalej z wrzatku w warniku, zostaje odessana zapomoca pomp}^, poddana wy¬ sokiemu cisnieniu i skierowana do miej¬ sca ogrzewania. Ta sprezona paca sluzy wtedy jako para ogrzewajaca, przez co zaoszczedza sie znacznie swieza pare.Jako pompa sprezajaca jest zazwyczaj w tym wypadku uzywana strumienica parowa.W tym wypadku para zostaje malo sprezona, w praktyce osiaga sie zaledwie 0,4—0,5 atm. zwyzki w cisnieniu. Z tego powodu temperatura sprezanej pary wy¬ nosi tylko okolo 108° C. gdy w miejscu gotowania panuje cisnienie atmosferycz¬ ne, a wiec temperatura 100° C. Stad wy¬ nika, ze gotowanie odbywa sie przy bar¬ dzo malej róznicy temperatury, co wy¬ twarza trudnosci przy konstruowaniu ulatniacza.Niniejszy wynalazek usuwa powyzsze niedogodnosci i polega na nastepujacem: W miejscu gotowania panuje tempe¬ ratura 100° C. w miejscu ogrzewania — 108° C. W dolnej czesci rur ogrzewajacych woda znajduje sie pod cisnieniem okolo 1.2 atm. Temu cisnieniu odpowiada juz temperatura okolo 104° C. Woda mu¬ sialaby wiec zostac ogrzana znacznie po¬ nad 104° C, azeby otrzymala chocby naj¬ slabsza podniete do pedu w góre.W rurash wiec nie bedzie prawie zadnego krazenia wody, gdyz ogrzanie jest zbyt male; wytworza sie ostatecznie pecherzyki pary, ale nie beda one mialy okreslonego kierunku. W skraplaczach przeto o tak malej róznicy temperaturypowstaje niedostateczne krazenie, co stoi na przeszkodzie energicznemu parowaniu.Niniejszy wynalazek usuwa te niedo¬ godnosc sztucznie, powiekszajac kraze¬ nie wody przez to, ze woda zostaje wpro¬ wadzona w ruch zapomoca pompy, przy- czem wodzie moze byc nadana w rurach dowolna szybkosc. Woda zostaje w krót¬ szym czasie przeniesiona do górnej czesci skraplacza i oddaje tam pare nawet przy ogrzaniu do 101°—102° C. To sztuczne kra¬ zenie zapewnia prawidlowe dzialanie skraplacza i zwieksza prace uzyteczna, gdyz, przy energicznem poruszaniu sie wody, przenoszenie sie ciepla jest wieksze, a osiadanie pecherzy pary jest usuniete.Na rysunku jest schematycznie przed¬ stawiony w przekroju podluznym aparat destylacyjny, skonstruowany wedlug po¬ wyzszego wynalazku, a przedstawia miej¬ sce gotowania o temperaturze 100° C, d strumienice parowa, b miejsce ogrze¬ wania o temperaturze 108° C Sztuczny obieg wody w rurach zostaje osiagniety przez urzadzenie kanalu obwodowego (u) i pompy (c) umieszczonej w tym kanale. PLIt is known that the useful work of the distillation apparatus can be increased by the fact that a part of the steam, formed from the boiling in the digester, is sucked off by a pump, subjected to high pressure and directed to the place of heating. This compressed float then serves as heating steam, which saves considerably fresh steam. As a compression pump, a steam ejector is usually used in this case. In this case, the steam is not fully compressed, in practice it only reaches 0.4-0.5 atm. . gains in pressure. For this reason, the temperature of the compressed steam is only about 108 ° C. when there is atmospheric pressure in the place of cooking, i.e. the temperature of 100 ° C. It follows that cooking takes place with a very small difference in temperature, which The present invention overcomes the above-mentioned inconvenience and consists of the following: The temperature of the cooking point is 100 ° C, and the heating point is 108 ° C. In the lower part of the heating pipes the water is under a pressure of about 1.2 atm. . This pressure already corresponds to a temperature of about 104 ° C. The water must therefore be heated well above 104 ° C in order to get at least the slightest stimulus to the shoot upwards. So there will be almost no circulation of water in the pipe, because heating is too small; Bubbles of steam will eventually form, but will not have a specific direction. In condensers, therefore, an insufficient circulation is created at such a small temperature difference, which prevents vigorous evaporation. The present invention removes this inconvenience artificially by increasing the circulation of water by causing the water to move by a pump, including water. any speed can be given in the pipes. The water is transferred to the top of the condenser in a shorter time and gives off vapor there even when heated to 101 ° -102 ° C. This artificial circulation ensures the correct operation of the condenser and increases the useful work, because, with vigorous water movement, The heat flow is greater and the sedimentation of the steam bubbles is removed. The figure shows schematically a longitudinally sectioned distillation apparatus, constructed in accordance with the above invention, and shows a cooking area at 100 ° C, a steam jets, of heating at a temperature of 108 ° C. The artificial circulation of water in the pipes is achieved by a perimeter channel device (u) and a pump (c) placed in this channel. PL

Claims (1)

1. Zastrzezenia patentowe. Przyrzad do destylacji wody zasilaja¬ cej kotly, ogrzewany sprezona para, tern znamienny, ze posiada z boku rure okrez¬ na, laczaca górne warstwy gotujacej sie w przyrzadzie wody z dolnemi, w która to rure jest wlaczona pompa, wywoluja¬ ca krazenie wody.Do opisu patentowego N« 101. -^H i i —i ZAKl.3RAF.KOZIANSKICH W WARSZAWIE PL1. Patent claims. The boiler feedwater distillation apparatus, heated by compressed steam, characterized by having a specific pipe on the side connecting the upper layers of the water boiling in the apparatus with the lower one, in which the pump is connected to circulate the water. To the patent description N '101. - ^ H ii - and ZAKl.3 KOZIANSKI RANKS IN WARSAW PL
PL101A 1918-10-30 Boiler feed water distillation device. PL101B1 (en)

Publications (1)

Publication Number Publication Date
PL101B1 true PL101B1 (en) 1924-05-26

Family

ID=

Similar Documents

Publication Publication Date Title
CN105833555A (en) Plate heat exchanger concentration system and concentration process thereof
PL101B1 (en) Boiler feed water distillation device.
US2027395A (en) Water reclaimer
SE505603C2 (en) Method of final evaporating black liquor in several stages where the liquor is passed in series through the steps and primary steam is added to each step
DE102018109846A1 (en) High-temperature energy storage - pressureless
US3151461A (en) Means for removing non-condensible gases from boiler feedwater in a power plant
US3239200A (en) Autoclave decompression system
CN205598682U (en) Concentrated system of plate heat exchanger
CA1120798A (en) Method and apparatus for feeding condensate to a high pressure vapor generator
US1758566A (en) Method and apparatus for deaerating and evaporating liquid
US1592195A (en) Boiler-feed-water-supply plant
US1550116A (en) Feed-water heater
SE466458B (en) SET UP TO GET A COOKER TO COOK TEMPERATURE
US2011819A (en) Cleaning apparatus for boilers
GB295871A (en) Improvements relating to the de-aerating of feed water for boilers
US327583A (en) Feed-water heater
AT100291B (en) Device for feeding steam boilers, especially locomotive boilers.
SU17237A1 (en) Device for heating and purification of feed water in steam boilers
US52402A (en) Improved evaporator
US834735A (en) Circulation device for hot-water heating plants.
US1573582A (en) Power plant
SU77758A1 (en) Water overheating deaerator
US1724916A (en) Heater
AT118122B (en) Multi-stage steam power plant with multi-stage reheating.
US42243A (en) Improvement in water-heaters for steam-boilers