CN105664758A - High cut disperse emulsification tank and application method thereof - Google Patents
High cut disperse emulsification tank and application method thereof Download PDFInfo
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- CN105664758A CN105664758A CN201610088124.9A CN201610088124A CN105664758A CN 105664758 A CN105664758 A CN 105664758A CN 201610088124 A CN201610088124 A CN 201610088124A CN 105664758 A CN105664758 A CN 105664758A
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- high cut
- shear
- cut disperse
- disperse emulsification
- emulsification tank
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/85—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with two or more stirrers on separate shafts
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/41—Emulsifying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/43—Mixing liquids with liquids; Emulsifying using driven stirrers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/07—Stirrers characterised by their mounting on the shaft
- B01F27/074—Stirrers characterised by their mounting on the shaft having two or more mixing elements being concentrically mounted on the same shaft
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/90—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/90—Heating or cooling systems
- B01F35/95—Heating or cooling systems using heated or cooled stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/90—Heating or cooling systems
- B01F2035/98—Cooling
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/40—Mixing of ingredients for oils, fats or waxes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Accessories For Mixers (AREA)
Abstract
The invention provides a high cut disperse emulsification tank and an application method thereof. The high cut disperse emulsification tank is provided with a stirring shaft along the middle axis of a tank body, stirring teeth are arranged at the bottom end of the stirring shaft, the top end of the stirring shaft is connected with a stirring motor, a feed inlet is formed in the top of the tank body, a discharge opening is formed in the bottom of the tank body, one or more shear shafts are arranged in the tank body, each shear shaft is provided with one or more cut disperse teeth, and the top end of each shear shaft is connected with a corresponding shear motor. The high cut disperse emulsification tank can be used for preparing a special fatting agent for fur, and the prepared special fatting agent for fur is good in shear emulsification effect and stable in property.
Description
Technical field
The present invention relates to fur coat material type of latex type product special equipment technical field, in particular to a kind of high cut disperse emulsification tank and application process thereof.
Background technology
At present, the special fatting agent production of fur coat out after, in application process in the outward appearance of product, storge quality and product stability etc. require significantly high. For the fatting agent obtaining outward appearance, performance is more stable, the special fatting agent series products of fur coat must use fur coat Special high shear dispersion and emulsion tank to produce.
The shearing equipment of prior art is generally adopted stirring-type single shear structure. This shearing work inefficiency, emulsification pretreatment weak effect, easily there are the phenomenons such as material layering, caking in the fatting agent of production, is unsuitable for producing the special fatting agent of high-quality fur coat.
In view of this, the special proposition present invention.
Summary of the invention
The first object of the present invention is in that to provide a kind of high cut disperse emulsification tank, and described high cut disperse emulsification jar structure is simple, and emulsification pretreatment is effective, the fatting agent stable in properties of production, and equipment runs safety.
The second object of the present invention is in that to provide the application process of a kind of described high cut disperse emulsification tank, and described high cut disperse emulsification tank can be used for the preparation of the special fatting agent of fur coat, and prepared fur coat special fatting agent emulsification pretreatment is respond well, stable in properties.
In order to realize the above-mentioned purpose of the present invention, spy by the following technical solutions:
A kind of high cut disperse emulsification tank, arranges shaft along tank body axis; Shaft bottom arranges stirrer gear; Shaft top is connected with stirring motor; Tank body top arranges charging aperture, and tank base arranges discharging opening; One or more shear axis is set in tank body; Each shear axis arranges one or more shearing and disperses tooth; Each shear axis top is connected with corresponding shear motor respectively; Preferably, in described tank body, 2 shear axis are set in shaft lateral symmetry, each shear axis arrange 2 and shears dispersion tooth.
High cut disperse emulsification tank of the present invention, being provided with on the basis of shaft and stirrer gear, arranges one or more shear axis in tank body; Each shear axis arranges one or more shearing and disperses tooth; High cut disperse emulsification tank of the present invention carries out shearing dispersion while dispersed with stirring, it is possible to efficient stable operation, it is possible to ensure product emulsion dispersion effect.
Preferably, each shear axis be arranged in parallel with shaft respectively.
Preferably, each position shearing dispersion tooth is respectively higher than the position of stirrer gear.
Preferably, on each shear axis, the shearing dispersion tooth of bottom lays respectively at identical level height. Preferably, different dispersion teeth of shearing lay respectively at different level heights.
Preferably, on each shear axis, the shearing dispersion tooth of bottom lays respectively at identical level height, and other are sheared dispersion tooth and lay respectively at different level heights.
Adopt specific shearing to disperse tooth set-up mode, contribute to increasing the effective contact area shearing dispersion tooth and material, reduce emulsion particle diameter, the more electrolyte-resistant of the fatting agent after clipped dispersion further.
Preferably, at tank body arranged outside heat-insulation layer.
Preferably, described heat-insulation layer is respectively provided with thermal insulation medium entrance and thermal insulation medium outlet.
Preferably, described thermal insulation medium entrance is arranged on heat-insulation layer bottom, and the outlet of described thermal insulation medium is arranged on heat-insulation layer top.
Heat-insulation layer helps to ensure that the high cut disperse emulsification tank of the present invention temperature stabilization when shearing dispersion, is conducive to shearing and scattered carry out and ensure emulsifying materials effect.
Preferably, the heat sink of correspondence it is respectively provided with outside each shear axis.
Preferably, each heat sink is respectively provided with temperature-reducing medium entrance and temperature-reducing medium outlet.
Preferably, described heat sink is arranged on outside tank body to the corresponding shear axis between shear motor.
Preferably, described temperature-reducing medium entrance is arranged on bottom heat sink, and the outlet of described temperature-reducing medium is arranged on heat sink top.
Heat sink can provide effective temperature-reducing to shear axis, owing to shear axis is in high-speed rotation state when shearing dispersion, it contacts easily heating with fixing device, and shear axis can effectively be lowered the temperature by heat sink, the shear axis life-span can be extended, ensure production safety.
Preferably, tank body arranges temperature-detecting device.
Temperature-detecting device is used for real-time monitoring of tank temperature, it is ensured that the high cut disperse emulsification tank of the present invention temperature stabilization when shearing dispersion, is conducive to shearing and scattered carry out and improve emulsifying materials effect.
Preferably, tank body arranges observation mirror.
Observation mirror is used for real-time monitored tank interior shear agitation situation, contributes to investigation hidden danger, it is ensured that production safety.
Preferably, described stirrer gear is anchor formula stirrer gear.
Anchor formula stirrer gear contributes to increasing effective contact area of stirrer gear and material, and the dispersed with stirring of material is uniform, contributes to material and disperses tooth to be fully contacted with shearing, reduces emulsion particle diameter further, make gained fatting agent more electrolyte-resistant.
The application process of a kind of high cut disperse emulsification tank, described high cut disperse emulsification tank is used for producing the special fatting agent of fur coat.
Described high cut disperse emulsification tank can be used for the preparation of the special fatting agent of fur coat, adopt stirrer gear and shear the mode that dispersion tooth coordinates, contribute to reducing emulsion particle diameter, make gained fatting agent more electrolyte-resistant, prepared fur coat special fatting agent emulsification pretreatment is respond well, stable in properties.
Compared with prior art, the invention have the benefit that
1. high cut disperse emulsification tank of the present invention arranges shaft on tank body axis, and shaft is provided above stirring motor, and shaft is arranged below stirrer gear. Additionally arranging one or more shear axis, shear axis is provided above shear motor, and shear axis is arranged below shearing dispersion tooth.Tank body upper end arranges charging aperture, and lower end arranges discharging opening, temperature-detecting device, and tank body sets heat-insulation layer, and high cut disperse emulsification tank of the present invention can efficient stable operation, it is possible to ensures product emulsifying effectiveness, and can guarantee that plant equipment safety.
2. dispersion tooth sheared by high cut disperse emulsification tank of the present invention, shears dispersion tooth and is arranged by special distribution, increases the effective contact area shearing dispersion tooth and material, it is possible to make emulsion particle diameter be down to 1-3 μm by about 25 μm. Emulsion particle diameter determines fur coat special fatting agent advantage in stability of emulsion, the more electrolyte-resistant of the fatting agent after clipped.
3. heat sink sheared by high cut disperse emulsification tank of the present invention, cooling can be provided to shear axis, owing to shear axis is in high-speed rotation state when shearing dispersion, it contacts easily heating with fixing device, shear axis can effectively be lowered the temperature by heat sink, the shear axis life-span can be extended, ensure production safety.
4. high cut disperse emulsification tank temperature-detecting device of the present invention, it is possible to detect pot temperature in real time, it is ensured that shear the stablizing of temperature during dispersion, is conducive to shearing and scattered carry out and improve emulsifying materials effect.
Accompanying drawing explanation
In order to be illustrated more clearly that the specific embodiment of the invention or technical scheme of the prior art, the accompanying drawing used required in detailed description of the invention or description of the prior art will be briefly described below, apparently, accompanying drawing in the following describes is some embodiments of the present invention, for those of ordinary skill in the art, under the premise not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
The structural representation of the high cut disperse emulsification tank that Fig. 1 provides for the embodiment of the present invention 1;
Accompanying drawing labelling:
1-stirring motor; 2-shear motor; 3-charging aperture;
4-shear axis; 5-shears dispersion tooth; 6-temperature-detecting device;
7-temperature-reducing medium exports; 8-temperature-reducing medium entrance; 9-observation mirror;
10-shaft; 11-thermal insulation medium exports; 12-heat-insulation layer;
13-thermal insulation medium entrance; 14-stirrer gear; 15-discharging opening.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, technical scheme is clearly and completely described, but it will be understood to those of skill in the art that, following described embodiment is a part of embodiment of the present invention, rather than whole embodiments, it is merely to illustrate the present invention, and is not construed as restriction the scope of the present invention. Based on the embodiment in the present invention, the every other embodiment that those of ordinary skill in the art obtain under not making creative work premise, broadly fall into the scope of protection of the invention. Unreceipted actual conditions person in embodiment, conventionally the condition of condition or manufacturer's suggestion carries out. Agents useful for same or the unreceipted production firm person of instrument, be and can pass through the commercially available conventional products bought and obtain.
In describing the invention, it should be noted that, orientation or the position relationship of the instruction such as term " " center ", " on ", D score, "left", "right", " vertically ", " level ", " interior ", " outward " be based on orientation shown in the drawings or position relationship; be for only for ease of the description present invention and simplifying and describe; rather than instruction or imply indication device or element must have specific orientation, with specific azimuth configuration and operation, be therefore not considered as limiting the invention.Additionally, term " first ", " second ", " the 3rd " are only for descriptive purposes, and it is not intended that indicate or hint relative importance.
In describing the invention, it is necessary to explanation, unless otherwise clearly defined and limited, term " installation ", " being connected ", " connection " should be interpreted broadly, for instance, it is possible to it is fixing connection, it is also possible to be removably connect, or connect integratedly; Can be mechanically connected, it is also possible to be electrical connection; Can be joined directly together, it is also possible to be indirectly connected to by intermediary, it is possible to be the connection of two element internals. For the ordinary skill in the art, it is possible to concrete condition understands above-mentioned term concrete meaning in the present invention.
The special fatting agent production of fur coat out after, in application process in the outward appearance of product, storge quality and product stability etc. require significantly high. For the fatting agent obtaining outward appearance, performance is more stable, the special fatting agent series products of fur coat must use fur coat Special high shear dispersion and emulsion tank to produce.
Shearing equipment of the prior art adopts stirring-type single shear structure. This shearing work inefficiency, emulsification pretreatment weak effect, easily there are the phenomenons such as material layering, caking in the fatting agent of production, is unsuitable for producing the special fatting agent of high-quality fur coat.
In view of this, the invention provides a kind of high cut disperse emulsification tank, as it is shown in figure 1, high cut disperse emulsification tank of the present invention arranges shaft 10 along tank body axis; Shaft 10 is provided above stirring motor 1, and shaft 10 is arranged below stirrer gear 14; Additionally arranging one or more shear axis 4, shear axis 4 is provided above shear motor 2, and shear axis 4 is arranged below shearing dispersion tooth 5; Tank body upper end arranges charging aperture 3, and lower end arranges discharging opening 15, temperature-detecting device 6, and tank body sets heat-insulation layer 12, and high cut disperse emulsification tank of the present invention can efficient stable operation, it is possible to ensures product emulsifying effectiveness, and can guarantee that plant equipment safety.
Preferably, by welding or the fixing connection of nut between described shaft 10 and stirrer gear 14, more preferably nut is fixing connects, it is possible to is easily installed and dismantles.
Preferably, described stirring motor 1 is connected with shaft 10, drives shaft 10 to rotate, it is further preferred that the output shaft of described stirring motor 1 is connected with shaft 10 with shaft coupling by decelerator, thus driving shaft 10 to rotate.
High cut disperse emulsification tank of the present invention is being provided with on the basis of shaft 10 and stirrer gear 14, arranges one or more shear axis 4 in tank body; Each shear axis 4 arranges one or more shearing and disperses tooth 5; High cut disperse emulsification tank of the present invention carries out shearing dispersion while dispersed with stirring, it is possible to efficient stable operation, it is possible to ensure product emulsion dispersion effect.
Preferably, each shear axis 4 be arranged in parallel with shaft 10 respectively.
Preferably, each position shearing dispersion tooth 5 is respectively higher than the position of stirrer gear 14.
Preferably, on each shear axis 4, the shearing dispersion tooth 5 of bottom lays respectively at identical level height.
Preferably, different dispersion teeth 5 of shearing lay respectively at different level heights.
Preferably, on each shear axis 4, the shearing dispersion tooth 5 of bottom lays respectively at identical level height, and other are sheared dispersion tooth 5 and lay respectively at different level heights.
High cut disperse emulsification tank of the present invention is sheared dispersion tooth 5 and is arranged by special distribution, increases the effective contact area shearing dispersion tooth 5 and material, it is possible to make emulsion particle diameter be down to 1-3 μm by about 25 μm.Emulsion particle diameter determines fur coat special fatting agent advantage in stability of emulsion, the more electrolyte-resistant of the fatting agent after clipped.
Shear dispersion tooth and be mainly used in the liquid such as coating, pigment, dyestuff, paint, ink, food, adhesive, medicine, daily use chemicals, emulsion and the pulverizing of stock product, stirring, the grinding such as liquid-solid, be the conventional fitment of the plant equipment such as dispersion machine, grinder, pulverizer, blender, mulser.
Preferably, described shear dispersion tooth 5 for square position serration type shear dispersion tooth, three justice paddle shear dispersion teeth, dish-style shear dispersion tooth, how tooth-like shear dispersion tooth, three tooth-like shear dispersion teeth, high viscosity shear dispersion tooth, middle low-viscosity shear dispersion tooth, single cog shear dispersion tooth, double cog shear dispersion tooth, peripheral teeth shear dispersion tooth, internal-gear type shear dispersion tooth, monolayer shear dispersion tooth, Double shears cutting dissipate tooth, multilamellar shear dispersion tooth in one or more.
Described dispersion tooth 5 of shearing is the accessory being matched in high cut disperse emulsification tank of the present invention, is connected to corresponding shear axis 4. When shear axis 4 runs up, shear dispersion tooth 5 upper and lower and present rotation status, turbulent area can be formed simultaneously at 2.5-5mm place, edge. The materials such as coating, paint, dry powder, solid-liquid are carried out shearing at a high speed, shock, pulverizing, dispersion by the sawtooth sheared on dispersion tooth 5, in order to reach the state of rapid mixing, dissolving, dispersion, refinement.
Preferably, need before use to check two parts: one is check to shear to disperse whether tooth deforms, being about to break falls or even lack; Two be check shear dispersion fluted disc body whether deform, thinning.
Preferably, described shear dispersion tooth 5 can adopt 304, other ceramic material of 316L rustless steel.
Preferably, each dispersion tooth 5 and corresponding shear axis 4 sheared connects respectively through welding or nut are fixing, and more preferably nut is fixing connects, it is possible to is easily installed and dismantles, and is arranged as required to consumption and position each other.
Preferably, described shear motor 2 is connected with corresponding shear axis 4, drives shear axis 4 to rotate, it is further preferred that the output shaft of described shear motor 2 is connected with shear axis 4 with shaft coupling by decelerator, thus driving shear axis 4 to rotate.
Preferably, at tank body arranged outside heat-insulation layer 12.
Preferably, described heat-insulation layer 12 is respectively provided with thermal insulation medium entrance 13 and thermal insulation medium outlet 11.
Preferably, described thermal insulation medium entrance 13 is arranged on heat-insulation layer 12 bottom, and described thermal insulation medium outlet 11 is arranged on heat-insulation layer 12 top.
Heat-insulation layer 12 helps to ensure that the high cut disperse emulsification tank of the present invention temperature stabilization when shearing dispersion, is conducive to shearing and scattered carry out and ensure emulsifying materials effect.
Preferably, the outside heat sink being respectively provided with correspondence of each shear axis 4.
Preferably, each heat sink is respectively provided with temperature-reducing medium entrance 8 and temperature-reducing medium outlet 7.
Preferably, described heat sink is arranged on outside tank body outside to the corresponding shear axis 4 between shear motor 2.
Preferably, described temperature-reducing medium entrance 8 is arranged on bottom heat sink, and described temperature-reducing medium outlet 7 is arranged on heat sink top.
High cut disperse emulsification tank heat sink of the present invention provides cooling can to shear axis 4, owing to shear axis 4 is in high-speed rotation state when shearing dispersion, it contacts easily heating with fixing device, shear axis 4 can effectively be lowered the temperature by heat sink, shear axis 4 life-span can be extended, ensure production safety.
Preferably, tank body arranges temperature-detecting device 6.
High cut disperse emulsification tank temperature-detecting device of the present invention 6 is for real-time monitoring of tank temperature, it is ensured that the high cut disperse emulsification tank of the present invention temperature stabilization when shearing dispersion, is conducive to shearing and scattered carry out and improve emulsifying materials effect.
Preferably, tank body arranges observation mirror 9.
Observation mirror 9, for real-time monitored tank interior shear agitation situation, contributes to investigation hidden danger, it is ensured that production safety.
Preferably, described stirrer gear 14 is anchor formula stirrer gear 14.
Anchor formula stirrer gear simple in construction, it is adaptable to viscosity is in the fluid agitation of below 100Pa s, when fluid viscosity is when 10～100Pa s, the horizontal blade that can add in the middle of anchor formula stirrer gear, it is frame type stirring tooth, to increase the mixing in container.
This type of stirrer gear is type agitator at a slow speed, is usually used in the process such as medium-high viscosity liquid mixing, heat transfer reaction, it is preferred to following one of several:
1. can obtain big shearing force along wall during anchor frame (MKS) low speed rotation, sedimentation and wall attachment, bottom shape laminating oval can and middle base bearing can be prevented.
2. anchor belt (MDS) is the combination of ribbon and frame, combines the effect of helical-ribbon type and gate stirrer.
3. block form (FKS), side's grating (FSS), simple shape makes easily, the same frame of usefulness, moderately viscous mixing, dissolves and is more suitable for.
4. plate and frame (BKS) is the high efficient mixed impeller that a range of viscosities application is very wide, and blade wheel structure is simple, and the vertical section area ratio that impeller projected area on the vertical section of agitator tank accounts for tank is very big. There is significantly high mixing efficiency, and have bigger shearing force, it is adaptable to solid-liquid suspension, liquid-liquid dispersions and make gas-liquid mass transfer and the heat transfer operations that gas from liquid surface sucks.
Preferably, anchor formula stirrer gear outer rim shape wants consistent with inner tank wall, only has only small gap therebetween, can remove the viscous reaction product being attached on inwall or be piled up in the solids of tank base, keeping good heat-transfer effect. The peripheral speed of anchor formula stirrer gear outer rim is 0.5～1.5m/s, can be used for stirring Newton type fluid and the pseudoplastic fluid of viscosity up to 200Pa s.
Anchor formula stirrer gear 14 contributes to increasing effective contact area of stirrer gear 14 and material, and the dispersed with stirring of material is uniform, contributes to material and disperses tooth 5 to be fully contacted with shearing, reduces emulsion particle diameter further, make gained fatting agent more electrolyte-resistant.
Further preferably, the invention provides the high cut disperse emulsification tank of a kind of structure as shown in Figure 1, main by anchor formula stirrer gear 14, stirring motor 1, shear motor 2, charging aperture 3, shaft 10, shear axis 4, tank body, heat-insulation layer 12, temperature-detecting device 6, observation mirror 9, shearing dispersion tooth 5, temperature-reducing medium outlet 7, temperature-reducing medium entrance 8, thermal insulation medium entrance 13, thermal insulation medium outlet 11, discharging opening 15 is constituted. Arranging shaft on high cut disperse emulsification tank axis of the present invention, shaft is provided above stirring motor, and shaft is arranged below anchor formula stirrer gear. Shaft both sides are respectively parallel to shaft and arrange shear axis, shear axis is provided above shear motor, shear axis is arranged below shearing dispersion tooth, each shear axis is respectively provided with two and shears dispersion tooth, 2 the shearing dispersion teeth settings laying respectively at 2 shear axis bottoms are positioned at identical level height, shear dispersion teeth setting for all the other 2 and are positioned at differentiated levels.Tank body upper end arranges charging aperture, and lower end arranges discharging opening, temperature-detecting device 6, and tank body sets heat-insulation layer, and high cut disperse emulsification tank of the present invention can efficient stable operation, it is ensured that product emulsifying effectiveness, and can guarantee that plant equipment safety.
The present invention shears dispersion tooth 5 and is provided with four, and shears dispersion tooth 5 and be positioned at three planes, increases and shears dispersion tooth 5 and effective contact area of material, it is possible to makes emulsion particle diameter be down to 1-3 μm by about 25 μm. Emulsion particle diameter determines fur coat special fatting agent advantage in stability of emulsion, the more electrolyte-resistant of the fatting agent after clipped.
High cut disperse emulsification tank heat sink of the present invention is arranged on outside tank body outside to the corresponding shear axis 4 between shear motor 2, and described shearing heat sink can give shear axis effective temperature-reducing; Owing to shear axis 4 is in high-speed rotation state when shearing dispersion, it contacts easily heating with fixing device, and shear axis 4 can effectively be lowered the temperature by heat sink, it is possible to extend shear axis 4 life-span, ensures production safety.
High cut disperse emulsification tank temperature-detecting device 6 of the present invention, it is possible to detect pot temperature in real time, it is ensured that shear the stablizing of temperature during dispersion, is conducive to shearing and scattered carry out and improve emulsifying materials effect.
Although illustrate and describing the present invention with specific embodiment, however it will be appreciated that may be made that when without departing substantially from the spirit and scope of the present invention many other change and amendment. It is, therefore, intended that include all such changes and modifications belonging in the scope of the invention in the following claims.
Claims (10)
1. a high cut disperse emulsification tank, it is characterised in that shaft is set along tank body axis; Shaft bottom arranges stirrer gear; Shaft top is connected with stirring motor; Tank body top arranges charging aperture, and tank base arranges discharging opening; One or more shear axis is set in tank body; Each shear axis arranges one or more shearing and disperses tooth; Each shear axis top is connected with corresponding shear motor respectively; Preferably, in described tank body, 2 shear axis are set in shaft lateral symmetry, each shear axis arrange 2 and shears dispersion tooth.
2. a kind of high cut disperse emulsification tank according to claim 1, it is characterised in that the position of each shearing dispersion tooth is respectively higher than the position of stirrer gear, on each shear axis, the shearing dispersion tooth of bottom lays respectively at identical level height.
3. a kind of high cut disperse emulsification tank according to claim 1, it is characterised in that described stirrer gear is anchor formula stirrer gear.
4. a kind of high cut disperse emulsification tank according to claim 1, it is characterised in that different dispersion teeth of shearing lay respectively at different level heights.
5. a kind of high cut disperse emulsification tank according to claim 1, it is characterised in that at tank body arranged outside heat-insulation layer.
6. a kind of high cut disperse emulsification tank according to claim 5, it is characterised in that be respectively provided with thermal insulation medium entrance and thermal insulation medium outlet on described heat-insulation layer.
7. a kind of high cut disperse emulsification tank according to claim 1, it is characterised in that be respectively provided with the heat sink of correspondence outside each shear axis.
8. a kind of high cut disperse emulsification tank according to claim 7, it is characterised in that be respectively provided with temperature-reducing medium entrance and temperature-reducing medium outlet on each heat sink.
9. a kind of high cut disperse emulsification tank according to claim 1, it is characterised in that temperature-detecting device is set on tank body.
10. the application process of the arbitrary described a kind of high cut disperse emulsification tank of claim 1-9, it is characterised in that described high cut disperse emulsification tank is used for producing the special fatting agent of fur coat.
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| CN201610088124.9A CN105664758A (en) | 2016-02-16 | 2016-02-16 | High cut disperse emulsification tank and application method thereof |
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| CN201610088124.9A CN105664758A (en) | 2016-02-16 | 2016-02-16 | High cut disperse emulsification tank and application method thereof |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107362707A (en) * | 2017-08-17 | 2017-11-21 | 李纳 | Suitable for there is the high-shear emulsion machine of temperature requirement |
| CN112121664A (en) * | 2020-09-09 | 2020-12-25 | 江西澳科新材料科技有限公司 | Tungsten alloy compounding device |
Citations (4)
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| JPH05212261A (en) * | 1992-01-31 | 1993-08-24 | Ube Ind Ltd | Agitation tank for high-viscosity liquid |
| CN203507886U (en) * | 2013-10-14 | 2014-04-02 | 济宁市连翔石化有限公司 | High-shear emulsification tank |
| CN203648423U (en) * | 2013-12-10 | 2014-06-18 | 上海依多科化工有限公司 | Mixing tank |
| CN204865580U (en) * | 2015-08-03 | 2015-12-16 | 天津欧凯米特科技有限公司 | High speed shearing emulsification tank of preparation medicine emulsion |
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| JPH05212261A (en) * | 1992-01-31 | 1993-08-24 | Ube Ind Ltd | Agitation tank for high-viscosity liquid |
| CN203507886U (en) * | 2013-10-14 | 2014-04-02 | 济宁市连翔石化有限公司 | High-shear emulsification tank |
| CN203648423U (en) * | 2013-12-10 | 2014-06-18 | 上海依多科化工有限公司 | Mixing tank |
| CN204865580U (en) * | 2015-08-03 | 2015-12-16 | 天津欧凯米特科技有限公司 | High speed shearing emulsification tank of preparation medicine emulsion |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107362707A (en) * | 2017-08-17 | 2017-11-21 | 李纳 | Suitable for there is the high-shear emulsion machine of temperature requirement |
| CN112121664A (en) * | 2020-09-09 | 2020-12-25 | 江西澳科新材料科技有限公司 | Tungsten alloy compounding device |
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Application publication date: 20160615 |