EP0526416A2 - Dissolver apparatus - Google Patents
Dissolver apparatus Download PDFInfo
- Publication number
- EP0526416A2 EP0526416A2 EP92830352A EP92830352A EP0526416A2 EP 0526416 A2 EP0526416 A2 EP 0526416A2 EP 92830352 A EP92830352 A EP 92830352A EP 92830352 A EP92830352 A EP 92830352A EP 0526416 A2 EP0526416 A2 EP 0526416A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- fact
- nozzles
- dissolver
- dissolver apparatus
- tub
- 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- Withdrawn
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F21/00—Dissolving
- B01F21/20—Dissolving using flow mixing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
Definitions
- the invention relates to a dissolver apparatus.
- This kind of apparatus is commonly used in the chemical field and is more specifically used for the preparation of liquid solutions or mixtures.
- dissolver apparatus it is usual to prepare solutions using only ordinary diffusion.
- the dissolver apparatuses which employ only this principle for solution preparation are normally constituted by cylindrical recipients having a flat or concave bottom into which the solid, that is the solute, is loaded discontinuously, while the liquid, that is the solvent, is made to flow in continuously from below.
- this type of dissolver apparatus is strictly connected to the parameters influencing the dissolution velocity, that is the form and the size of the solute particles and the size and the shape of the dissolver apparatus.
- the productive capacity of a dissolver apparatus thus made is directly proportional to the contact surface between solvent and solute; thus, to reach optimal performance level, this first type of apparatus is normally constituted by large recipients with a capacity of up to 1000 cubic metres.
- an ordinary-diffusion dissolver apparatus is a very simple device, on the other hand its performance is conditioned by its size.
- a further disadvantage is its discontinuous function.
- the prior art also teaches a second type of dissolver apparatus, wherein solutions are prepared using a turbulent diffusion process.
- Such dissolver apparatuses are substantially constituted like the above-mentioned ordinary dissolver apparatus, but are equipped with internal appropriate mechanical paddles to agitate the solution.
- An essential aim of the present invention is thus that of obviating the above-described drawbacks manifested in the discontinuous ordinary dissolver apparatus and the discontinuous turbulent-diffusion apparatus by providing a dissolver apparatus which, depending on the loading mechanism, can be either continuous or discontinuous, with an elevated productive capacity and which is smaller with respect to the above-described dissolver apparatus given a similar productive capacity.
- the dissolver apparatus which is of the type constituted by a mixing tub and by at least two feeding devices of at least one liquid part and at least one solid part as well as a recycling device, and which is characterised by the fact that inside the mixing tub mixing means are arranged into which are conveyed respectively, the solid part constituting the solute, through an aperture, and the liquid part constituting the solution, by means of a series of first and second nozzles, the liquid part being the solvent, and also characterised by the fact that the resulting solution formed within the mixing means, which is equipped with an overflow, flows through this last and is conveyed into the mixing tub.
- the dissolver apparatus is formed by a tub 1 equipped with a recycling device 2.
- a box 15 is inserted into the tub 1, supported on uprights 20.
- Mixing means 3 are housed inside the said box 15 and are fixed to the cover 21 of the tub 1; the said mixing means 3 being constituted of a multiple basket 9 formed by vertical baffles 10 arranged concentrically.
- the vertical baffles 10 form a labyrinthine course, commonly referred to as a "chicane filter", equipped with an overflow 8 and a filter 14.
- first nozzles 5 are inserted, which first nozzles 5 are of preferably tubular shape and are equipped centrally with holes 12 and, at the free end, with a spout 13 of preferably arched shape, while second nozzles 6 can be positioned between the baffles 10.
- the superior part of the multiple basket 9 is equipped with an ingress aperture 4 for the solid material.
- a sump 17 is housed, which is connected to the recycling device 2 fed by a pump 18.
- a third type of nozzle 19 Internally to the tub 1 and connected to the recycling device 2 are housed a third type of nozzle 19.
- the functioning of the invention is as follows: The solid part, that is the solute, is brought into the central part of the basket 9, where it is bombarded with jets exiting from the lateral holes 12 and the spout 13 of the first nozzles 5. Thus begins the turbulent dissolving process of the solute.
- the solution 7 formed in which solid not-yet dissolved particles are suspended, follows the course imposed by the baffles 10, between which the second nozzles 6 are inserted, which second nozzles 6 impose a second turbulent movement, and furthermore prevent any eventual sedimentation at the base of the basket 9 between the interspaces.
- the solution 7 formed is kept in agitation by a third type of nozzle 19 connected also to the recycling device 2 fed by the pump 18.
- the dissolver apparatus according to the invention can be equipped with all the prior art devices and components according to the technical conditions. For this reason the electric command organs are not described herein, nor the dosing organs, the extraction organs and so on.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Extraction Or Liquid Replacement (AREA)
Abstract
Description
- The invention relates to a dissolver apparatus. This kind of apparatus is commonly used in the chemical field and is more specifically used for the preparation of liquid solutions or mixtures.
- At present, in accordance with a first type of prior art dissolver apparatus, it is usual to prepare solutions using only ordinary diffusion. The dissolver apparatuses which employ only this principle for solution preparation are normally constituted by cylindrical recipients having a flat or concave bottom into which the solid, that is the solute, is loaded discontinuously, while the liquid, that is the solvent, is made to flow in continuously from below.
- The performance of this type of dissolver apparatus is strictly connected to the parameters influencing the dissolution velocity, that is the form and the size of the solute particles and the size and the shape of the dissolver apparatus. The productive capacity of a dissolver apparatus thus made is directly proportional to the contact surface between solvent and solute; thus, to reach optimal performance level, this first type of apparatus is normally constituted by large recipients with a capacity of up to 1000 cubic metres.
- If on the one hand an ordinary-diffusion dissolver apparatus is a very simple device, on the other hand its performance is conditioned by its size.
- A further disadvantage is its discontinuous function.
- The prior art also teaches a second type of dissolver apparatus, wherein solutions are prepared using a turbulent diffusion process.
- Such dissolver apparatuses are substantially constituted like the above-mentioned ordinary dissolver apparatus, but are equipped with internal appropriate mechanical paddles to agitate the solution.
- A disadvantage of the above systems is their discontinuous functioning and the presence of mechanical organs which require maintenance.
- An essential aim of the present invention is thus that of obviating the above-described drawbacks manifested in the discontinuous ordinary dissolver apparatus and the discontinuous turbulent-diffusion apparatus by providing a dissolver apparatus which, depending on the loading mechanism, can be either continuous or discontinuous, with an elevated productive capacity and which is smaller with respect to the above-described dissolver apparatus given a similar productive capacity.
- Further aims of the present invention are also:
- a) making use of water jet mixers instead of mechanical agitators;
- b) reducing to a minimum the use of mechanical devices equipped with kinematic parts and thus subject to wear;
- c) obtaining, thanks to recycling mechanisms, saturated and homogeneous solutions.
- These and other aims besides are all attained by the dissolver apparatus according to the present invention, which is of the type constituted by a mixing tub and by at least two feeding devices of at least one liquid part and at least one solid part as well as a recycling device, and which is characterised by the fact that inside the mixing tub mixing means are arranged into which are conveyed respectively, the solid part constituting the solute, through an aperture, and the liquid part constituting the solution, by means of a series of first and second nozzles, the liquid part being the solvent, and also characterised by the fact that the resulting solution formed within the mixing means, which is equipped with an overflow, flows through this last and is conveyed into the mixing tub.
- Further characteristics and advantages of the dissolver apparatus according to the invention will better emerge from the detailed description that follows, of a preferred embodiment illustrated in the accompanying diagrams purely in the form of a non-limiting example, and in which:
- Figure 1 shows a vertical section of the dissolver apparatus according to the invention;
- Figure 2 shows the feeding circuit of the first and second feeding devices;
- Figure 3 shows the body of the first feeding device.
- With reference to the accompanying drawings, the dissolver apparatus according to the invention is formed by a
tub 1 equipped with arecycling device 2. - A
box 15 is inserted into thetub 1, supported onuprights 20. -
Mixing means 3 are housed inside the saidbox 15 and are fixed to thecover 21 of thetub 1; the said mixing means 3 being constituted of amultiple basket 9 formed byvertical baffles 10 arranged concentrically. - The
vertical baffles 10 form a labyrinthine course, commonly referred to as a "chicane filter", equipped with anoverflow 8 and afilter 14. At the centre of themultiple basket 9first nozzles 5 are inserted, whichfirst nozzles 5 are of preferably tubular shape and are equipped centrally withholes 12 and, at the free end, with aspout 13 of preferably arched shape, whilesecond nozzles 6 can be positioned between thebaffles 10. - The positioning and the connecting of the
first nozzles 5 and thesecond nozzles 6 to therecycling device 2 is schematically represented in figure 2. - The superior part of the
multiple basket 9 is equipped with an ingress aperture 4 for the solid material. - Beneath the
tub 1, at the level of theconical aperture 16 of thebox 15, asump 17 is housed, which is connected to therecycling device 2 fed by apump 18. - Internally to the
tub 1 and connected to therecycling device 2 are housed a third type ofnozzle 19. - The functioning of the invention is as follows:
The solid part, that is the solute, is brought into the central part of thebasket 9, where it is bombarded with jets exiting from thelateral holes 12 and thespout 13 of thefirst nozzles 5. Thus begins the turbulent dissolving process of the solute. - The solution 7 formed, in which solid not-yet dissolved particles are suspended, follows the course imposed by the
baffles 10, between which thesecond nozzles 6 are inserted, whichsecond nozzles 6 impose a second turbulent movement, and furthermore prevent any eventual sedimentation at the base of thebasket 9 between the interspaces. - The solution, overflowing from the
basket 9, returns to thetub 1, while eventual solid parts still present in the solution, passing from thefilter 14 positioned along theoverflow 8, are intercepted by thebox 15 and thus conveyed towards thesump 17 and by action of therecycling device 2 are redeposited in thebasket 9 whence the cycle recommences. - Once the loading of the solute is finished, the solution 7 formed is kept in agitation by a third type of
nozzle 19 connected also to therecycling device 2 fed by thepump 18. - Naturally the dissolver apparatus according to the invention can be equipped with all the prior art devices and components according to the technical conditions. For this reason the electric command organs are not described herein, nor the dosing organs, the extraction organs and so on.
Claims (10)
- A dissolver apparatus of the type consituted by a mixing tub (1) and by at least two feeding devices of at least one liquid part and at least one solid part as well as a recycling device (2), and which is characterised by the fact that inside the mixing tub (1) mixing means (3) are arranged into which are conveyed respectively, the solid part constituting the solute, through an aperture (4), and the liquid part constituting the solution, by means of a series of first and second nozzles (5 and 6), the liquid part being the solvent, and also characterised by the fact that the resulting solution (7) formed within the mixing means (3), which is equipped with an overflow (8), flows through the said overflow (8) and is conveyed into the mixing tub (1).
- A dissolver apparatus as in claim 1, characterised by the fact that the said mixing means (3) is constituted by a multiple basket (9) in which the said first nozzles (5) and the said second nozzles (6) are inserted.
- A dissolver apparatus as in claim 2, characterised by the fact that the said multiple basket (9) is constituted by a series of vertical baffles (10) arranged concentrically and forming a labyrinthine course.
- A dissolver apparatus according to claims 1 and 2, characterised by the fact that the said first nozzles (5) are inserted inthe central part of the said basket (9).
- A dissolver apparatus as in claims 2 and 3, characterised by the fact that the said second nozzles (6) are inserted in the interspaces (11) between the said baffles (10), forming the said labyrinth.
- A dissolver apparatus according to claims 2, 4 and 5, characterised by the fact that the said first nozzles (5) are constituted in their central parts by a body of preferably cylindrical shape equipped with lateral holes (12) and, at their free end, by a spout (13) which spout (13) characteristics dictate the shape of the resulting jet.
- A dissolver apparatus according to claim 1, characterised by the fact that the said overflow (8) is equipped with a filter (14).
- A dissolver apparatus according to claims 1, 2, 3 and 7 characterised by the fact that the said multiple basket (9) is inserted in a box (15) which is in its turn inserted in the said tub (1), terminating in an funnel-type or conical aperture (16), aimed at conveying towards the sump (17) any eventual parts of solute which have remained undissolved after having passed through the filter (14).
- A dissolver apparatus according to claims 1 and 8, characterised by the fact that the said funnel-type or conical aperture (16) is at the level of the said sump (17) constituting the ingress point of the said recycling device (2).
- A dissolver apparatus as in claims 1, 2, 8 and 9, characterised by the fact that the said recycling device (2) is constituted by at least one pump 18, by the said first nozzles (5) and the said second nozzles (6) and by at least a third type of nozzle (19) arranged between the said tub (1) and the said box (15).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ITBZ910022A IT1253330B (en) | 1991-07-11 | 1991-07-11 | PHYSICAL DISSOLUTOR |
ITBZ910022 | 1991-07-11 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0526416A2 true EP0526416A2 (en) | 1993-02-03 |
EP0526416A3 EP0526416A3 (en) | 1993-05-05 |
Family
ID=11346514
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19920830352 Withdrawn EP0526416A3 (en) | 1991-07-11 | 1992-07-03 | Dissolver apparatus |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP0526416A3 (en) |
IT (1) | IT1253330B (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ITVR20080088A1 (en) * | 2008-08-11 | 2010-02-12 | Agristrade S P A | DEVICE FOR THE PREPARATION OF AN AQUEOUS SOLUTION OF CALCIUM CHLORIDE, PARTICULARLY FOR USE AS A SURFACE ANTI-FREEZE |
WO2010018140A2 (en) * | 2008-08-11 | 2010-02-18 | Agristrade S.P.A. | Device for preparing an aqueous solution of salt, particularly of calcium chloride, for use as a surface deicer |
ITVR20080143A1 (en) * | 2008-12-30 | 2010-06-30 | Agristrade S P A | DEVICE FOR THE PREPARATION OF AN AQUEOUS SALT SOLUTION, IN PARTICULAR OF CALCIUM CHLORIDE, FOR USE AS A SURFACE ANTIFREEZE |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE859602C (en) * | 1940-07-06 | 1952-12-15 | Murk Boerstra | Device for preparing solutions |
US2699379A (en) * | 1949-04-22 | 1955-01-11 | Luque Jose Aramburu | Extraction apparatus |
GB2055050A (en) * | 1979-06-22 | 1981-02-25 | Burgert H | Loop reactor |
-
1991
- 1991-07-11 IT ITBZ910022A patent/IT1253330B/en active IP Right Grant
-
1992
- 1992-07-03 EP EP19920830352 patent/EP0526416A3/en not_active Withdrawn
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE859602C (en) * | 1940-07-06 | 1952-12-15 | Murk Boerstra | Device for preparing solutions |
US2699379A (en) * | 1949-04-22 | 1955-01-11 | Luque Jose Aramburu | Extraction apparatus |
GB2055050A (en) * | 1979-06-22 | 1981-02-25 | Burgert H | Loop reactor |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ITVR20080088A1 (en) * | 2008-08-11 | 2010-02-12 | Agristrade S P A | DEVICE FOR THE PREPARATION OF AN AQUEOUS SOLUTION OF CALCIUM CHLORIDE, PARTICULARLY FOR USE AS A SURFACE ANTI-FREEZE |
WO2010018140A2 (en) * | 2008-08-11 | 2010-02-18 | Agristrade S.P.A. | Device for preparing an aqueous solution of salt, particularly of calcium chloride, for use as a surface deicer |
WO2010018140A3 (en) * | 2008-08-11 | 2010-04-29 | Agristrade S.P.A. | Device for preparing an aqueous solution of salt, particularly of calcium chloride, for use as a surface deicer, and device for distributing an aqueous solution for use as a surface deicer |
ITVR20080143A1 (en) * | 2008-12-30 | 2010-06-30 | Agristrade S P A | DEVICE FOR THE PREPARATION OF AN AQUEOUS SALT SOLUTION, IN PARTICULAR OF CALCIUM CHLORIDE, FOR USE AS A SURFACE ANTIFREEZE |
Also Published As
Publication number | Publication date |
---|---|
ITBZ910022A1 (en) | 1993-01-11 |
ITBZ910022A0 (en) | 1991-07-11 |
IT1253330B (en) | 1995-07-24 |
EP0526416A3 (en) | 1993-05-05 |
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