GB2165768A - Method and apparatus for destroying froth - Google Patents
Method and apparatus for destroying froth Download PDFInfo
- Publication number
- GB2165768A GB2165768A GB08518561A GB8518561A GB2165768A GB 2165768 A GB2165768 A GB 2165768A GB 08518561 A GB08518561 A GB 08518561A GB 8518561 A GB8518561 A GB 8518561A GB 2165768 A GB2165768 A GB 2165768A
- Authority
- GB
- United Kingdom
- Prior art keywords
- froth
- impeller
- turbo
- outlet orifice
- destroying
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/02—Foam dispersion or prevention
Landscapes
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Degasification And Air Bubble Elimination (AREA)
Abstract
The invention relates to a turbo- impeller (20) for destroying the froth forming in fermenter tanks for example. For this purpose, the turbo-impeller (20) is disposed immediately in front of the outlet orifice (18) for the spent air as a result of which the froth is at least substantially prevented from being entrained by the spent air through the outlet orifice (18). The turbo-impeller (20) may be installed with a horizontal or vertical plane of rotation but can also be used, in particular, in an inclined position. <IMAGE>
Description
SPECIFICATION
Method and apparatus for destroying froth
This invention relates to a method and apparatus for destroying froth in reactor tanks. It is particularly applicable to reactor tanks of the type in which there is an outlet orifice for gas, and a turbo-impeller to draw in froth axially and fling it off radially, compressing the froth to liquid droplets in the process.
Froth forms in many chemical and biochemical processes, for example in reactor tanks treated with gas, particularly in fermentation tanks, so-called fermenters.
In order that this froth may not be drawn off from the tanks, for example entrained with waste gas or spent air, it is destroyed by means of froth destroyers, that is to say turbo-impellers which draw the froth in axially and fling it off radially, the froth being compressed into liquid droplets. (When spent air is referred to hereinafter, it means not only air but also other gases).
These turbo-impellers are disposed above the level of the liquid in order to destroy the froth where it forms, as far as possible.
This is possible but it has been found that an optimum destruction of the froth cannot be achieved by this means and, in particular, it is impossible to prevent froth from being entrained with the spent air and carried out of the tank.
It is therefore the object of the invention to dispose the turbo-impeller for destroying the froth so that entrainment of the froth with the spent air and hence a discharge of the froth from the fermenter tank is at least substantially prevented.
According to an aspect of the invention, this is achieved in that the turbo-impeller is disposed immediately in front of the outlet orifice for the waste gas.
The spacing of the turbo-impeller from the outlet orifice is preferably substantially in the range from one-sixth to one-third of the diameter of the turboimpeller.
The diameter of the turbo-impeller may appropriately correspond to the diameter of the outlet orifice; it may also be larger but should not be substantially smaller than the diameter of the outlet orifice.
The invention further relates to a method of destroying the froth, forming in fermenter tanks for example, by means of a turbo-impeller of the abovementioned type, the method being distinguished by the fact that the froth is drawn off immediately in front of the outlet orifice for the spent air and compressed into liquid droplets.
One form of embodiment of the invention is explained by way of example below, with reference to the drawing in which:~
Fig. 1 shows diagrammatically a fermenter tank with a turbo-impeller for destroying the froth disposed according to the invention.
Fig. 2 shows a side view of the turbo-impeller and its arrangement in front of the outlet orifice for the spent air, on a larger scale.
Fig. 1 shows diagrammatically a tank or container 10, for example a fermenter tank, which is filled up to a given height with the liquid to be processed, the level of the liquid being designated by 12. Froth 14 has formed above the level 12 of the liquid and is to be destroyed in order to prevent the froth from being discharged from the tank 10 through an outlet duct 30, through which the spent air flows away.
In order to destroy the froth 14, a turbo-impeller 20, knownperse, is used which is mounted on a drive shaft 22 which is driven by a drive not illustrated in the drawing, for example an electric motor.
As illustrated in Fig. 1, the outlet duct 30 is disposed in the curved region 16 of the wall of the tank 10.
As the Fig. shows, the turbo-impeller 20 is disposed immediately in front of the outlet orifice 18 in the wall of the tank 10, in accordance with the invention.
If desired, the outlet orifice and hence the turboimpeller 20 may be disposed in the plane horizontal region 24, the tapered region 26 or the vertical cylindrical region 28 of the wall of the tank 10, the only important thing being that the turbo-impeller 20 is situated immediately in front of the outlet orifice 18.
Fig. 2 shows the turbo-impeller 20, which is disposed immediately in front of the outlet orifice 18 in the wall of the tank 10, on a larger scale than Fig.
1. As already mentioned, the turbo-impeller 20 is set in rotation via its shaft 22 by a drive not shown, for example an electric motor. It draws the froth in axially along the arrows P1 and flings it off radially in the direction of the arrows P3, the froth being compressed into liquid droplets during and by this centrifuging, as known per se.
Any froth entrained by the spent air is drawn out of the region between the turbo-impeller and the outlet orifice, as indicated diagrammatically by the arrows P2, and is likewise flung away in the direction of the arrows P3, with compression into liquid droplets.
As illustrated in Fig. 2, the outlet duct 30 is secured to the wall of the tank 10 by means of mounting flanges 36,34 and the actual spent-air outlet 32 is branched off from the outlet duct 30. The shaft 22 extends through the outlet duct 30 (not illustrated) to the drive, likewise not shown.
The median plane (that is to say the plane perpendicular to the centre axis of the shaft 22) may appropriately extend parallel to the plane of the outlet orifice 18.
The spacing A between the outlet orifice 18 and the turbo-impeller 20 is preferably in the range from one-sixth to one-third of the diameter D of the turboimpeller 20. The diameter D of the turbo-impeller 20 preferably corresponds substantially to the diameter dofthe outlet orifice 18; it may be larger than the latter but should preferably not be substantially smaller than the diameter d of the outlet orifice 18.
The turbo-impeller 20 can be adapted to all sizes of fermenter and to all sizes of the outiet orifice. it can be used in an inclined position, as illustrated, but may also be positioned in a horizontal or vertical position.
The invention has been described with reference to fermenters, which are understood to mean apparatus in which micro-organisms are cultivated in a liquid, the metabolites of which microorganisms generally represent valuable materials, for example, penicillin. In order to supply the organisms with 02, the fermentation liquid must be aerated.
Since many liquors tend to froth, the froth formed would leave the fermentation tank with the waste gas. This would lead to production losses and in addition the froth would have to be disposed of in some way.
In order to avoid this, the froth is destroyed inside the fermentation tank.
Claims (8)
1. A method of destroying froth in reactor tanks having a gas outlet orifice, in which the froth is drawn into an axial-inflow radial-oufflow turboimpeller and compressed to form liquid droplets, characterised in that the froth is destroyed directly in front of the outlet orifice.
2. A reactor tank for performing the method claimed in claim 1, characterised in that the turboimpeller is disposed directly in front of the outlet orifice.
3. A reactor tank as claimed in claim 2 in which the distance of the turbo-impeller from the outlet orifice is in the range one-sixth to one-third of the turboimpeller diameter.
4. A reactor tank as claimed in claim 2 or claim 3 in which the diameter of the turbo-impeller is substantially equal to the diameter of the outlet orifice.
5. A turbo-impeller and outlet duct assembly for mounting to a container to produce a reactor tank as claimed in any of claims 2 to 4.
6. A method of destroying froth in reactor tanks as claimed in claim 1 and substantially as described.
7. A reactor tank substantially as described with reference to the Drawings.
8. Aturbo-impeller and outlet duct assembly substantially as described with reference to Fig. 2.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19843438657 DE3438657A1 (en) | 1984-10-22 | 1984-10-22 | TURBINE TO DESTROY FOAM |
Publications (2)
Publication Number | Publication Date |
---|---|
GB8518561D0 GB8518561D0 (en) | 1985-08-29 |
GB2165768A true GB2165768A (en) | 1986-04-23 |
Family
ID=6248482
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB08518561A Withdrawn GB2165768A (en) | 1984-10-22 | 1985-07-23 | Method and apparatus for destroying froth |
Country Status (3)
Country | Link |
---|---|
JP (1) | JPS61101213A (en) |
DE (1) | DE3438657A1 (en) |
GB (1) | GB2165768A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5235901A (en) * | 1989-11-27 | 1993-08-17 | Ian M. MacLennan | Method and apparatus for making a fermented beverage |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3900170C2 (en) * | 1989-01-05 | 1994-02-17 | Kammerer F Gmbh | Method and device for reducing the volume of foam over a liquid in a container |
DE3923928A1 (en) * | 1989-07-19 | 1991-01-24 | Werner Prof Dr Ing Stahl | BIOREACTOR |
DE3931311A1 (en) * | 1989-09-20 | 1991-03-28 | Total Feuerschutz Gmbh | METHOD AND DEVICE FOR DISPOSAL OF FIRE EXTINGUISHING FOAM OR OTHER FOAMS |
DE10041941B4 (en) * | 2000-08-25 | 2006-05-04 | Henkell & Söhnlein Sektkellereien KG | Apparatus and method for influencing the foam behavior of liquids, in particular beverages containing carbon dioxide |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1051533A (en) * | ||||
GB1035252A (en) * | 1962-03-09 | 1966-07-06 | Mixing Equipment Co Inc | Method and apparatus for breaking foam |
GB1083060A (en) * | 1966-08-15 | 1967-09-13 | Canadian Breweries Ltd | Method of controlling the size of the yeast cap in a fermentation vessel |
GB1110937A (en) * | 1964-10-02 | 1968-04-24 | Alvin Ward Hughes | Combination emulsifying and deaerating machine for sausage batter and the like |
GB1181877A (en) * | 1967-05-22 | 1970-02-18 | Mixing Equipment Co Inc | Breaking Foam |
GB1263526A (en) * | 1968-02-13 | 1972-02-09 | Process Engineering Co | Improvements in the prevention of encrustation in fermentation apparatus and methods of operating same |
GB1316296A (en) * | 1969-10-14 | 1973-05-09 | New Brunswick Scientific Co | Centrifugal mechanical defoamer |
US4110089A (en) * | 1974-05-13 | 1978-08-29 | Mueller Hans | Apparatus with foam breaker |
-
1984
- 1984-10-22 DE DE19843438657 patent/DE3438657A1/en not_active Withdrawn
-
1985
- 1985-07-23 GB GB08518561A patent/GB2165768A/en not_active Withdrawn
- 1985-08-19 JP JP18160185A patent/JPS61101213A/en active Pending
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1051533A (en) * | ||||
GB1035252A (en) * | 1962-03-09 | 1966-07-06 | Mixing Equipment Co Inc | Method and apparatus for breaking foam |
GB1110937A (en) * | 1964-10-02 | 1968-04-24 | Alvin Ward Hughes | Combination emulsifying and deaerating machine for sausage batter and the like |
GB1083060A (en) * | 1966-08-15 | 1967-09-13 | Canadian Breweries Ltd | Method of controlling the size of the yeast cap in a fermentation vessel |
GB1181877A (en) * | 1967-05-22 | 1970-02-18 | Mixing Equipment Co Inc | Breaking Foam |
GB1263526A (en) * | 1968-02-13 | 1972-02-09 | Process Engineering Co | Improvements in the prevention of encrustation in fermentation apparatus and methods of operating same |
GB1316296A (en) * | 1969-10-14 | 1973-05-09 | New Brunswick Scientific Co | Centrifugal mechanical defoamer |
US4110089A (en) * | 1974-05-13 | 1978-08-29 | Mueller Hans | Apparatus with foam breaker |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5235901A (en) * | 1989-11-27 | 1993-08-17 | Ian M. MacLennan | Method and apparatus for making a fermented beverage |
Also Published As
Publication number | Publication date |
---|---|
DE3438657A1 (en) | 1986-04-24 |
GB8518561D0 (en) | 1985-08-29 |
JPS61101213A (en) | 1986-05-20 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
WAP | Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1) |