CS261545B1 - Process for desorption of gases from liquid solutions - Google Patents
Process for desorption of gases from liquid solutions Download PDFInfo
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- CS261545B1 CS261545B1 CS87191A CS19187A CS261545B1 CS 261545 B1 CS261545 B1 CS 261545B1 CS 87191 A CS87191 A CS 87191A CS 19187 A CS19187 A CS 19187A CS 261545 B1 CS261545 B1 CS 261545B1
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Abstract
Riešenie sa zaoberá desonpciou plynov z kvapalných roztokov. Rozpuštěné plyny v kvapalných rozpúšťadlách pri róznych procesoch chemickej technológie sa odstraňujú diferenciálnou rektifikáciou pri nekonečnem refluxnom pomere prúdom inertného plynu. Efekt delenia je lepší ako pri doteraz používaných spůsoboch a tiež sa znižujú straty kvapalnej fáze.The solution deals with the separation of gases from liquid solutions. Dissolved gases in liquid solvents in various chemical technology processes are removed by differential rectification at an infinite reflux ratio with a stream of inert gas. The separation effect is better than in the methods used so far and the liquid phase losses are also reduced.
Description
Vynález sa zaoberá desofpcioiLjplynOjY1 z> L kvapalných roztokov. V rfti&c&oaíi· <jíieňiic-| ' kej technológie je velmi častým prípaďom, že používané kvapalné média 'V kontaKtél s plynnými zložkami absorbujú časť plynných zložiek.The present invention deals with one of desofpcioiLjplynOjY> L liquid solutions. In rfti & It is a very common case that the liquid media used in the gas component absorb part of the gas component.
Ďalšou příčinou přítomnosti rozpustných plynov je ich uvoínenie chemickou cestou pri technologických procesoch. Vo vačšine prípadov přítomnost rozpustných plynov v kvapalinách je nežiadúcim javom z viacerých příčin. Například dochádza k zhoršeniu kvality použitých rozpúšťadiel, resp. reagentov, opatovne používanie kvapalín v technologických procesoch je nemožné vzhladom na vedíajšie chemické reakcie, rozpuštěné plynné zložky sposobujú mechanické zanášanie aparátov po ich vypadávaní vo formě nerozpustných zlúčenín atd.Another reason for the presence of soluble gases is their release by chemical means in technological processes. In most cases, the presence of soluble gases in liquids is an undesirable phenomenon for several reasons. For example, there is a deterioration in the quality of the solvents used, respectively. the use of liquids in technological processes is impossible due to chemical side reactions, the dissolved gaseous components cause mechanical fouling of the apparatus after its dropping in the form of insoluble compounds, etc.
V praxi sa desorpcia plynov uskutočňuje prúdom iného plynu, destiláciou alebo rektifikáciou, resp. použitím vákua. V případe prchavých kvapalín, alebo pri nízkých koncentráciach rozpuštěného plynu, vzhladom na relativné vysoké straty rozpúšťadiel, uvedené spósoby z ekonomických dóvodov nie sú najvhodnejšie. Straty rozpúšťadla v týchto pripadoch v závislosti od vlastností zmesi a požadovanej úrovně desorpcie móžu byť 5 až 15 %.In practice, desorption of the gases is effected by the flow of another gas, distillation or rectification, respectively. using vacuum. In the case of volatile liquids, or at low dissolved gas concentrations, due to the relatively high solvent losses, these methods are not the most appropriate for economic reasons. The solvent losses in these cases, depending on the properties of the mixture and the desorption level required, may be 5 to 15%.
Dalším nedostatkom je, že dosahovaný deliaci účinok nie je vždy úměrný prevádzkovým nákladom na desorpciu.Another drawback is that the separation effect achieved is not always proportional to the operational cost of desorption.
Uvedené nedostatky odstraňuje spósob podlá vynálezu, jeho podstatou je desorpcia plynov zaležená na diferenciálnej rektifikácii roztoku pri nekonečnom refluxnom pomere prúdom inertu (napr. vzduchu, alebo dusíka], t. j. destilát sa neodoberá. Vo- vynáleze je využívaná tá vlastnost absorbova. ných plynov, že ich rovnovážné zloženie v 'parnej fáze jp vačš^a© v kvapalnej.The present invention is based on the desorption of gases based on differential rectification of the solution at an infinite reflux ratio with an inert stream (e.g., air or nitrogen), i.e. the distillate is not removed. their equilibrium composition in the vapor phase is in the liquid phase.
Rozpúšťadlo po desorpcii podlá předmětného .yyýiáťežú--prakticky neobsahuje rozpustem; plyny. Vplyvom velkého zkoncentrovanla rozpuštěného plynu v parnej fáze na hlavě rektifikačnej kolóny spotřeba Inertu je nízká a straty rozpúšťadla v porovnaní s inými spósobmi sú tiež nízké.The desorption solvent of the present invention is substantially free of solvent; gases. Due to the large concentration of dissolved gas in the vapor phase at the top of the rectification column, the consumption of Inert is low and solvent losses are also low compared to other methods.
PřikladlEXAMPLE
V procese výroby N-fenyl-izopropyl-p-fenyldiamín (Ainitioxidand CD] sa používá metanol ako rozpúšťadlo. Regenerovaný metanol z výroby obsahoval vedlajšou chemickou reakciou vzniknutý amoniak v množstve 0,5 °/o hm, Desorpcia bola robená prúdom dusíka za laboratórnych podmienok. Po 70 minútach metanol obsahoval 0,0’3 % amoniaku. Straty na metanole boli 5 %-né. Desorpciou podlá vynálezu koncentrácie amoniaku poklesla na 0,024 % po 40 minútách. Pozorované straty na metanole boli 1,2 o/o.Methanol is used as a solvent in the process of producing N-phenyl-isopropyl-p-phenyldiamine (Ainitioxidand CD]. The recovered methanol from the production contained 0.5% w / w ammonia by chemical reaction. After 70 minutes, methanol contained 0.0-3% ammonia, losses on methanol were 5%, and by desorption according to the invention, the ammonia concentration decreased to 0.024% after 40 minutes.
Příklad 2Example 2
V druhom případe metanol obsahoval 0,44 percenta amoniaku. Desorpcia bola robené diferenciálnou rektifikáciou pri refluxnom pomere R = 16 v trvání 60 min. Metanol po ukončení obsahoval 0,14 % amoniaku. Množstvo odoberaného destilátu bolo 7,5 % z povodného množstva s obsahom amoniaku 2,8 percenta.In the second case, methanol contained 0.44 percent ammonia. Desorption was performed by differential rectification at a reflux ratio of R = 16 for 60 min. Upon completion, the methanol contained 0.14% ammonia. The amount of distillate collected was 7.5% of the flood level with an ammonia content of 2.8 percent.
Desorpciou podlá vynálezu po 60 minútách sa dosiahlo zníženie amoniaku na 0,02 percenta. Pozorované straty na metanole boli 1,35 %.Desorption according to the invention after 60 minutes resulted in a reduction of ammonia to 0.02 percent. The observed losses on methanol were 1.35%.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CS87191A CS261545B1 (en) | 1987-01-12 | 1987-01-12 | Process for desorption of gases from liquid solutions |
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CS87191A CS261545B1 (en) | 1987-01-12 | 1987-01-12 | Process for desorption of gases from liquid solutions |
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CS19187A1 CS19187A1 (en) | 1988-07-15 |
CS261545B1 true CS261545B1 (en) | 1989-02-10 |
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CS87191A CS261545B1 (en) | 1987-01-12 | 1987-01-12 | Process for desorption of gases from liquid solutions |
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1987
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