CS223313B1 - Method of increasing the exploitation degree of the dissolved gas in the liquid and device for executing the same method - Google Patents

Abstract

The area of application of the invention is in the chemical industry, food industry and other industries, water purification and mainly wastewater treatment. According to the invention, the utilisation factor of gas dissolved in liquid can be increased by feeding a mixture of liquid and gaseous components into a secondary mixture in a covered duct which is preferably disposed in a circulation channel, achieving an increase in the utilisation factor for the dissolved gas while maintaining the flow velocities in the circulation channel which are induced in the direction of the longitudinal axis by the energy of the outflowing mixture, while at the same time the gas/liquid output ratio is reduced and the output of the liquid component is increased. <IMAGE>

Description

The present invention relates to saturation parameters in the gas saturation of liquids.

CEM K ^{y k} and ^P n ^ply Alin ^{y s p} sing from early and zanzern Úsobí ^{p, p} napíMad solution ccording DOS 26 12 255 ^Y u ^Gd weighing Inje ^kt or ^of its electrical supply in the OTO ^H trough. E ^{k ka} Onomichi dials Nost ^d t: EC ^h this method relies on the utilization of dissolved gas.

Very in ^hours aqueous work up of ^PU with ^b em saturation ^to apahny ^p l ^{y NEM} e.g. ^Cart Ia ^d in nejbežnějšnn ^{EXAMPLE IP ga} in ^dy mod ^d U ^s Nym ^alkyl sl ^{Cart em} at ^ka based flow ^Y prices ^and sv ^{y REC} using the ^H and ^{d H} ovýc phenomenon ⁱⁿ current-nt esp ^{é P eh} axis ^to rstencov ^EXPERIMENT.

The amount of dissolved gas is limited by the saturation concentration of the liquid under the conditions. The degree of utilization of dissolved gas, defined by the amount maiden ^p u ^{TEN eh} of ^ply nu ^to CE ^o b ^s he ^p rive ^d en ^é he amount depends inter alia largely on the relative flow rate of the gaseous components (= the flow rate ratio gaseous and liquid components] in mixing the flow and it is limited. Zmenšemm ^{relatively eh} diameter of ^{the UT} at the ^ply number nn ^{é clippers} can increase the degree of utilization of the dissolved gas.

This can be no appreciable loss of energy expended dissolution achieved by the present solution, the essence of which is the outlet pipe supplying the mixture of liquid and gaseous component ^Y comprising solvent-Nu ^ply ns ^p ol with other gases formed preferably transient currents (e.g., ring jump] in the direction of the longitudinal axis of the circulation trough where the input power of the liquid gas causes circulation of the liquid in the trough, and the thus formed mixture of liquid with gas is ^p rive ^d ena ^d of ^ylw Abu secular mixing positioned · preferably circulatory trough where at speed flow 'in

Claims (3)

Subject 1. ^{From the} mouth ^b is ^also raised. 'Stupirá ^{characterized} using rozluštěného gas in the liquid at a flow mixing, preferably transients Prou ^ga n ^e v ^ trubt example ^p rstencovým the flux, wherein the mixture of liquid and gaseous components formed by dissolving a gas together with other gases is by ^{Yu TE} to ^d oo ^b z- ^é lato it ^out in the direction of its longitudinal axis and its output energy to induce circulation of the liquid in the trough, characterized in that the formed mixture of liquid and gaseous components are separately mixed · liquid obíhajírn in žtabu. 2. An apparatus for increasing the utilization rate of a circulating trough by mixing the supplied mixture with the liquid circulating through the trough will increase the utilization rate of the dissolved gas by reducing the relative flow rate of the gaseous component. 11 is not aerated liquid is supplied directly and for ^C erp ^{and tub, d} e is an inflow ^straight Ečer ^Fr van ^Star fluid to the pump bore in a new streamlined revN ^{d p p} N rato keeps flow rates in the trough. If multiple circulation channels are used for mixing, they can be connected in parallel or in series, depending on the nature of the saturation process. ^N, and bonded ^{with the} above RESEC ^h, sc ^h OPICS ^y shows an exemplary apparatus for performing the described method. 1 shows a longitudinal section and FIG. 2 is a plan view. FIG. Into the circulation trough (troughs] 1 in the direction of its longitudinal axis above vyiistěn ^{s t} o r ^p of ^{ky tu} otovýc ^h mixer 2, the chute extending into .krytého three secondary mixing. 4 supply of carbonated fluid to the pump 5 is going opening 6 in the bottom Circulation threshold seventh drains are connected in serial connections ^E m ^P otrubím 8 jetož inlet end is preferably submerged at the bottom and outlet. ^p circumscribed MDs ^at with ^b and zařfaern maj ^{í characterized} using vc ^h em ⁱ c ^Kem and jinmn dia ^ u, aquatic Hosp ^d ar ^st to ^i, esp ^E on when ^read m wastewater in ^DK oxtáaci in ^soil at ^bi olo ^g ick cleaning. ^p of manufacture ^{KL D} Perform ^d ern: ^{In the} circulatory gutter cleaning by ^dp and ^d --N ^H VOD content 760 m ^{3 p} s ^p řečerpávání to flow mixers 2X X ^0, l ⁷⁵ m ^{3 /} s Uve e ^d in ^d and ^ylw abu ^d o ^p oh ^{bu y ry} ch ^{l tic 0.7} m / s, i.e. in Abu hu ^ ^d ^ e recirtotov flow rate ^6.7 m ^{3 / d} for the ^{d and some} amount ^{of p} extended ^STE n ^eh of ^alkyl sl ^{Cart of} UIM will take ^to reverse to oxidačrn had increased ^{about 56%;} INVENTION pouštěného gas in a liquid, wherein the reaction container is at least one circulation trough, characterized in that the circulating ^TL and ^b u ^(1] is ^{characterized} in formed ^TL and ^{b (3)} of the secondary mixing in the form covered channels which is the inlet of the mixture of liquid and gas. ³ . IZařrzem This increases ^longitude measurement stage in ^{the Y} use r ^o ZPO ^US T ^e n ^eh of ptynu in ka ^p Alina ^p ccording to claim ^{2, characterized in} the ^{price that} the vinegar ^ylw ab ⁽¹⁾ MEASURES ⁿ protonicově ^R E ^W eným ^d Rahe new ^{P m (7} L in _rém ^who is vytooren opening (6) connected to the ^p er ^No. Sarna said handle (5K