PL8180B3 - A method of separating bodies that condense from mixtures with air or others; difficult to deviate gases. - Google Patents
A method of separating bodies that condense from mixtures with air or others; difficult to deviate gases. Download PDFInfo
- Publication number
- PL8180B3 PL8180B3 PL8180A PL818026A PL8180B3 PL 8180 B3 PL8180 B3 PL 8180B3 PL 8180 A PL8180 A PL 8180A PL 818026 A PL818026 A PL 818026A PL 8180 B3 PL8180 B3 PL 8180B3
- Authority
- PL
- Poland
- Prior art keywords
- mixtures
- air
- difficult
- condense
- gases
- Prior art date
Links
- 239000000203 mixture Substances 0.000 title claims description 8
- 239000007789 gas Substances 0.000 title claims description 5
- 238000000034 method Methods 0.000 title claims description 5
- 239000002250 absorbent Substances 0.000 claims description 8
- 230000002745 absorbent Effects 0.000 claims description 7
- 229920006395 saturated elastomer Polymers 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 241000590629 Biblis Species 0.000 claims 1
- 238000000354 decomposition reaction Methods 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Description
Najdluzszy czas trwania patentu do 21 lipca 1941 r.Przedmiot patentu glównego Nr 5425 stanowil siposób 'wydzielania skraplajacych sie c:'al, zapomoca cdchlaniania z miesza¬ nin ich z poiwiietrizem lub innemi gazami z trudnoscia tylko dajacemu! sie bdchla- niac, przyczem pary pochloniete zostaja wydzielane z czynnika chlonnego zajpomo- ca srodka, który w danej Itemperaturze nie podlega skraplaniu, a nastepnie skraplane zapomoca ochladzania. Wedlug wynalazku niniejszego', jako czynnik nosny stosuje sie sama mieszanine zasadnicza, przeznaczona do rozkladu, przeprowadzajac ja przez nasycony osrodek chlonny, jednoczesnie ogrzewany, a nastepnie przez chlodnice, przylegajaca do naczynia chlonnego.Podlug odmiany wykonania tego spo¬ sobu, gdy mianowicie zasadnicza mieszani¬ na gazoiwa lub parowa posiada iciagly ruch strumieniowy, kazdy czynnik chlonny dziala w sposób zimienny, odchlainiaijac 'wydzielajace pary. Przy poslugiwaniu sie tym sposobem zauwazono, ze jest rzecza korzystna mieszanine zasadnicza, nasyconapara wodna, zastosowac do wydzielania par, pochlonietych, w ten sposób bowiem przyspiesza \sie bardgo calkowite ich (wy- cfzielajnie.W tym celu wystarcza strumien rozkla¬ danej zasadniczej mieszaniny ]gazowo-pa- rowej przeprowadzic przez ogrzana wode, o temperaturze utrzymywanej na poziomie 60° — 90° przed wprowadzeniem miesiza- nimy tej ido osrodka chlonnego. Male ilo¬ sci pary wodnej, porwane w ten sposób, skraplaja sie w chlodnicy razem z czescia¬ mi! dajacemi sie skraplac. Osrodek chlon¬ ny nie powinien wysychac przed powtór- nem jego uzyciem. Ten wlasnie sposób ni¬ niejszy rózni sie od znanego sposobu wy¬ parowywania nasyconej masy chlonnej.Staje sie tutaj zbyteczinem wytwarzanie pary, przyczem do .nagrzania wody wystar¬ cza cieplo, rozpiprzadzalne przy wykony¬ waniu najmniejszej juz pracy urzadzenia, Kondensat odlwadnia sie w sposób zna¬ ny. PL PLThe longest term of the patent until July 21, 1941. The subject of the main patent No. 5425 was a method of separating the condensing al, aids to absorb them from mixtures with air-ether or other gases with difficulty only giving! become dehydrated, the absorbed vapors are released from the absorbent agent by an agent that is not subject to condensation in a given item temperature, and then condensed by cooling. According to the present invention, as the carrier agent, the basic mixture itself is used, intended to decompose, passing it through a saturated absorbent medium while being heated, and then through a cooler adjacent to the absorbent vessel. ¬ On gas or steam, there is a continuous jet movement, each absorbent acts in a cold way, deflecting the release of vapors. When using this method, it has been noticed that it is advantageous to use a basic mixture, saturated steam, for the separation of absorbed vapors, because in this way the entirety of them is accelerated (especially, for this purpose, the stream of decomposing the main mixture is sufficient) Pass gas and steam through heated water, kept at a temperature of 60 ° - 90 °, before introducing the mixture into the absorbent medium. Small amounts of water vapor entrained in this way condense in the cooler together with the parts. The absorbent should not dry out before re-using it. This way differs from the known method of evaporating a saturated absorbent mass. The production of steam, for the purpose of heating the water, is a waste here. sufficient heat, dispersible in carrying out the smallest work of the device, the condensate is dehydrated in a known manner. PL PL
Claims (1)
Publications (1)
| Publication Number | Publication Date |
|---|---|
| PL8180B3 true PL8180B3 (en) | 1928-01-31 |
Family
ID=
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2838135A (en) | Process for the recovery of heat from hot gases | |
| FI56933C (en) | FOER REQUIREMENTS | |
| GB719738A (en) | Improvements in or relating to the combustion and evaporation of industrial waste liquors | |
| PL8180B3 (en) | A method of separating bodies that condense from mixtures with air or others; difficult to deviate gases. | |
| CL2010001614A1 (en) | Roasting process of a metal sulfide concentrate carried out in a fluidized bed reactor at a determined temperature with recovery of heat from the waste gases to preheat the fluidized air or the concentrate and the respective roasting plant. | |
| US3456622A (en) | Stack gas cleaning process | |
| ES449796A1 (en) | Method and apparatus for treating gases to remove contaminants therefrom | |
| US5966837A (en) | Wood drying plant and a method of purifying a drying gas from a wood drying device | |
| JPS5935851B2 (en) | Dry cement manufacturing equipment | |
| US4085688A (en) | Treatment of effluent | |
| DE3912586A1 (en) | Process and regeneration device for the thermal treatment, such as drying, low-temperature carbonisation or gasification, of pasty or sludge-like substances | |
| GB989548A (en) | Process for reducing a non-magnetic iron ore to magnetite | |
| ES2079981T3 (en) | PROCEDURE FOR IMPROVED VACUUM EVACUATION IN HOT STEAM DRYING. | |
| JPS5753224A (en) | Treatment of coal ash | |
| GB1120072A (en) | Recovering values from waste pickle liquor | |
| RU2128680C1 (en) | Method of thermally processing high-sulfur fuels | |
| US914279A (en) | Process of obtaining nitrogen from air. | |
| NO306772B1 (en) | Process for recovery of sulfuric acid | |
| GB1056722A (en) | Improvements in or relating to power-generating steam cycle | |
| ES357195A1 (en) | Process for removing hydrogen sulphide from a gas stream and converting it to elemental sulphur | |
| GB349287A (en) | An improved process for the recovery of gas mixtures rich in sulphur dioxide | |
| US2972520A (en) | Pyrolysis of waste sulfite liquor | |
| DE3900069C2 (en) | ||
| CN104342210B (en) | The processing of crude syngas | |
| GB587890A (en) | Improvements in or relating to the continuous drying of material in solid form and to the half-carbonizing or carbonizing of peat and other carbonaceous piece material |