CN202289926U - Temperature-controllable high-speed stirring and dispersing kettle with temperature measurement and discharge flange - Google Patents
Temperature-controllable high-speed stirring and dispersing kettle with temperature measurement and discharge flange Download PDFInfo
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- CN202289926U CN202289926U CN2011205569792U CN201120556979U CN202289926U CN 202289926 U CN202289926 U CN 202289926U CN 2011205569792 U CN2011205569792 U CN 2011205569792U CN 201120556979 U CN201120556979 U CN 201120556979U CN 202289926 U CN202289926 U CN 202289926U
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Abstract
The utility model discloses a temperature-controllable high-speed stirring and dispersing kettle with a temperature measurement and discharge flange. The temperature-controllable high-speed stirring and dispersing kettle comprises a kettle body, a stirring and dispersing device, a stirring and dispersing driving mechanism, a temperature measurement and discharge flange and a temperature measurement device, wherein the stirring and dispersing device consists of a double-layer dispersing disk and a scraped-surface agitator which is matched with a movable polytetrafluoroethylene scraping plate; the double-layer dispersing disk and the scraped-surface agitator do relative motion, so that a stagnant layer, a stirring dead zone and a super shear turbulent area on the barrel wall in the kettle can be eliminated, the circulation in the kettle can be promoted, the heat transfer efficiency can be increased, the dispersion effect is improved, the dispersion time is shortened, and the dispersion efficiency is obviously increased; through a temperature monitoring device which is connected with the temperature measurement and discharge flange into a whole, the temperature at the bottom of the kettle body is monitored, the free radical reaction of a thermosetting material caused by heat produced by friction is avoided, the material is scrapped, and the quality of the material is guaranteed; a vacuum dispersion device can be used for improving the depolymerization efficiency of solid powder and improve the wetting effect and promote the dispersion of a solid and liquid phase material; and the temperature-controllable high-speed stirring and dispersing kettle has the advantages of simple structure, high efficiency, convenience for repair and maintenance and wide application range.
Description
Technical field
The utility model relates to a kind of high-speed stirred dispersing apparatus, relates in particular to the mixing plant of a kind of coating, printing ink industry.
Technical background
High speed dispersor in present coating and printing ink industry does not generally seal; Dispersed with stirring equipment can only be accomplished the stirring work under normal pressure, need or have the technological process of carrying out under the environment of pressure just can't on same equipment, accomplish in vacuum like vacuum froth breaking, vacuum intake, compressed air discharging etc.Traditional device exists problems; For example: production technology is disperseed, operation is not concentrated, serialization production capacity is poor, working strength of workers big, production efficiency is lower, energy consumption is big, if accomplish vacuum or have the technological process of pressure to need more auxiliary equipment, increase the equipment purchasing expense of enterprise; Batch poor stability of product; Simultaneously, the dust pollution that open operation produced seriously endangers operating personnel's health and operating environment.
To the problems referred to above; Though different techniques improvement project and corresponding industrialization product are arranged; For example ZL200620113784.X, ZL200420084214.3 and ZL200920069500.5, still, new problem has appearred in these schemes and product when being applied to ultraviolet light (UV) cured printing ink field.When the UV cured printing ink for the high pigment of being made up of thermosetting light-sensitive materials such as the activated monomer that is rich in free radical, resins disperses; The China ink slurry is acutely rubbing under the drive of dispersion impeller and at the bottom of the still of Scattered Kettle; Produce great amount of heat, these heats cause the radical reaction of the thermosets in the printing ink China ink slurry easily, thereby China ink slurry gelatin phenomenon takes place; This phenomenon can solve through the mode of fast cooling; When but full-bodied printing ink slurry disperseed in stirred vessel, very easily the inwall at container formed thicker retention layer, and retention layer is participated in the mixing and the effect of mass transmitting of internal tank fluid hardly; Heat-transfer effect for the heat that is produced because of acutely rubbing at the bottom of the still of China ink slurry and Scattered Kettle also significantly worsens, and finally causes material to be scrapped.Therefore, when adopting the device fabrication in the such scheme, can't monitor temperature at the bottom of the still first, second can't lower the temperature completely rapidly kettle.So the defective of prior art scheme can not satisfy the specific (special) requirements of production technology far away.
The utility model content
The purpose of the utility model is to overcome above defective; A kind of dispersed with stirring equipment simple in structure, economical and practical, easy to maintenance is provided; Can monitor in real time when this equipment carries out the sealing operation under the environment of vacuum or high pressure slip at the bottom of the Scattered Kettle still in dispersion process in the temperature rise phenomenon that is produced with violent friction at the bottom of the still of Scattered Kettle under the drive of dispersion impeller; And fall through the coolant circulating system exchange heat that is produced that will rub, guarantee that processing temperature is no more than control range.
For reaching above purpose, the utility model adopts following technical scheme:
A kind of closed high-speed stirred Scattered Kettle with thermometric blowing flange; Comprise the dispersion impeller drive motors, scrape wall oar drive motors, reductor, scrape that wall oar support arm, refrigerant exit, double-deck dispersion impeller, Cu-50 copper resistance sensing temperature meter probe, refrigerant inlet, tetrafluoro scraper plate, bimetallic thermometer, gear-box, manhole cover, powder add that inlet, liquid material add inlet, visor lamp, take out (putting) air valve, vacuum meter, manhole cover visor, vavuum pump, air compressor machine, refrigerant chuck cavity, flow-guiding type are strengthened axle in gusset, kettle, the dispersion impeller, scrape wall oar outer shaft, scrape the wall oar, ring, baiting valve bolt locating hole, baiting valve in the cavity, shaft coupling, pedestal, refrigerant chuck, the line of induction, digital display meter, sensor, thermometric blowing flange, sensing temperature meter probe protective casing, flange outer shroud, flange drain hole, flange, it is characterized in that: the Cu-50 copper resistance sensing temperature meter probe and the bimetallic thermometer of described thermometric is installed in the sensing temperature meter probe protective casing of the thermometric blowing flange at the bottom of the still respectively and a side of Scattered Kettle loam cake.
The closed high-speed stirred Scattered Kettle of described band thermometric blowing flange is characterized in that: described tetrafluoro scraper plate is movable, and the tetrafluoro scraper plate can be done the swing of different amplitudes along with the rotation of the friction speed of scraping the wall oar.
The closed high-speed stirred Scattered Kettle of described band thermometric blowing flange; It is characterized in that: the quantity of described tetrafluoro scraper plate is 6; 2 tetrafluoro scraper plates are equipped with in the bottom of scraping the wall oar, and the upright side of scraping the wall oar respectively is equipped with 2 tetrafluoro scraper plates, and install 4 tetrafluoro scraper plate interleaved positions.
The closed high-speed stirred Scattered Kettle of described band thermometric blowing flange; It is characterized in that: the Cu-50 copper resistance sensing temperature meter probe in the described sensor; Be installed in the sensing temperature meter probe protective casing at the flange outer shroud place of blowing oral area thermometric blowing flange at the bottom of the still; The Cu-50 copper resistance sensing temperature meter end of popping one's head in is connected through the line of induction, and the other end is connected with digital display meter; The length of Cu-50 copper resistance sensing temperature meter probe is 5cm; Bimetallic thermometer is fixed on kettle cover top one side, adds inlet with the liquid material and is 180 ° of diagonal bits installations.
The closed high-speed stirred Scattered Kettle of described band thermometric blowing flange is characterized in that: forming test specification by Cu-50 copper resistance sensing temperature meter probe, sensing temperature meter probe protective casing, sensor, the line of induction and digital display meter is 0～150 ℃ Cu-50 copper resistance sensing temperature meter.
The closed high-speed stirred Scattered Kettle of described band thermometric blowing flange; It is characterized in that: described refrigerant chuck cavity is provided with the flow-guiding type reinforcement gusset that is used to increase the refrigerant circular flow; Flow-guiding type reinforcement gusset shape in the shape of a spiral is coiled on the kettle in the refrigerant chuck cavity; Flow-guiding type is strengthened the mode of gusset through welding and is fixed on the outer wall of kettle, is not connected with the inwall of refrigerant chuck, near the part of the refrigerant chuck cavity of autoclave body bottom flow-guiding type is not installed and is strengthened gusset.
The closed high-speed stirred Scattered Kettle of described band thermometric blowing flange is characterized in that: describedly scrape axle in the wall oar support arm, double-deck dispersion impeller, tetrafluoro scraper plate, dispersion impeller, scrape wall oar outer shaft, scrape the wall oar and constitute the dispersed with stirring device; Scrape wall oar drive motors, dispersion impeller drive motors, pedestal, reductor, gear-box, shaft coupling formation dispersed with stirring device driving mechanism; Dispersed with stirring device driving mechanism is installed in the top of kettle, and the dispersed with stirring device is in the inside cavity of kettle and is connected with dispersed with stirring device driving mechanism.
The closed high-speed stirred Scattered Kettle of described band thermometric blowing flange; It is characterized in that: described dispersed with stirring device comprises stirring and disperses the two large divisions; Double-deck dispersion impeller is installed in the bottom of axle in the dispersion impeller, and axle is connected with the dispersion impeller drive motors through shaft coupling in the dispersion impeller; Scrape the outside of wall oar outer shaft axle in dispersion impeller, scrape the wall oar and be fixed on the outside of scraping the wall oar, scrape wall oar support arm and scrape wall oar outer shaft and be 80 ° of angles and fix through scraping wall oar support arm.
The closed high-speed stirred Scattered Kettle of described band thermometric blowing flange; It is characterized in that: the edge of the flange outer shroud of described thermometric blowing flange is fixed on the bottom of kettle with the mode of welding, and thermometric blowing flange is connected with baiting valve through baiting valve bolt locating hole.
The utlity model has following advantage:
1. when the utility model stirring, dispersion, the air occlusion is few.Mix with to mix well effect all good, with in or high-speed stirred can make that material dissolves rapidly, particle diameter diminishes.
2. the utility model adopts concentric twin shaft stirring system, and interior outer shaft can rotate simultaneously, and speed and direction can independent regulation, and the two can be identical, also can be different.Do rightabout when rotation when double-deck dispersion impeller with scraping the wall oar, can significantly promote the axial circulating current motion of slip, suppress the tangential motion of slip, and the full still systemic circulation that can produce slip.Shorten jitter time, can eliminate dead band and superpower shear turbulence district in the still simultaneously, therefore, when Scattered Kettle is maximized, also can guarantee the homogeneous turbulence intensity of full still.
3. the utility model adopts is furnished with scraping the wall oar and can eliminating the retention layer on the still inner barrel wall of movable tetrafluoro scraper plate, can prevent that the material of big proportion is deposited at the bottom of the still, promotes circulation in the material still, improves heat transfer efficiency, improves dispersion effect.
4. the vacuum dispersal device both can have been got rid of bubble and the inner air of bringing in the dispersed with stirring process of solid powder aggregation; The anti-phase meniscus that destroys the capillary pressure extruding of solid powder aggregation inner air liquid body and form and strengthen liquid to solid aggregates or the inner osmosis of agglomerate; Under the effect of the powerful shearing force of double-deck dispersion impeller; Raising improves wetting effect to the depolymerization efficient of solid powder, promotes the dispersion of solid-liquid two phase materials; Shorten jitter time, reduce the viscosity of system rapidly; Can get rid of simultaneously the moisture that solid powder is absorbed in transportation, storage process, thereby guarantee the stable of product batches.
5. the utility model has overcome the shortcoming of legacy equipment function singleness, inefficiency; Can realize the high-speed stirred dispersion under high pressure, low pressure or the vacuum condition; When particularly under vacuum condition, disperseing the printing ink slurry of high pigment; Double-deck dispersion impeller is done rotation in opposite directions with scraping the wall oar under the drive of dispersion impeller drive motors, improved dispersion efficiency, only uses this equipment just can reach at short notice China ink is starched abundant finely dispersed effect; When reduction and other milling apparatus are used the chief engineer who grinds greatly, can more effectively control production cost.
Powder through powder add the inlet be delivered in the still; Avoided the dust pollution question that produces in the reinforced process of legacy equipment; Disperseing whipping process is in the environment of sealing, to carry out; Further reduced dust pollution question, improved operating personnel's operating environment, reduced the infringement of dust operating personnel's health.
7. the utility model adopts contrastive detection temperature system up and down, through the bimetallic thermometer of kettle cover top, can monitor slip top temperature; Can monitor when disperseing the temperature of reacting the core position of aggravating heat release because of the further initiator system of violent frictional heat through being positioned near the drain hole Cu-50 copper resistance sensing temperature meter; Sensing temperature meter probe protective casing directly contacts with material, and detecting temperature promptly and accurately makes the display list can the instant playback material temperature; The sensitivity of bimetallic thermometer is high, can reflect the temperature fluctuation of slip in real time, in case the temperature runaway phenomenon occurs, lowers the temperature through coolant circulating system.Through the monitoring of temperature monitoring system up and down, can guarantee the smooth processing of thermosetting ink or coating.
8. the utility model is simple in structure, is convenient to maintenance, maintenance.
Description of drawings
In order further to set forth the utility model is technological means and the effect thereof that the predetermined purpose of realization is taked; The utility model combines following accompanying drawing to carry out detailed explanation; The purpose of the utility model, characteristic and characteristics; Can obtain thus going deep into and concrete understanding, yet accompanying drawing only provides reference and explanation, is not to be used for the utility model is limited.
Fig. 1 is the overall structure sketch map of the related dispersing apparatus of the utility model.
Fig. 2 is the vertical view of Fig. 1.
Fig. 3 is the overall structure sketch map for the related thermometric blowing flange of the utility model.
Fig. 4 is the vertical view of Fig. 3.
Explain further details below in conjunction with accompanying drawing and the utility model embodiment.
The specific embodiment
As depicted in figs. 1 and 2, the high speed dispersion still of the controllable temperature of this band temperature measuring equipment by dispersion impeller drive motors 1, scrape wall oar drive motors 2, reductor 3, scrape wall oar support arm 4, refrigerant exit 5, double-deck dispersion impeller 6, Cu-50 copper resistance sensing temperature meter probe 7, refrigerant inlet 8, tetrafluoro scraper plate 9, bimetallic thermometer 10, gear-box 11, manhole cover 12, powder add inlet 13, the liquid material adds inlet 14, visor lamp 15, take out (putting) air valve 16, vacuum meter 17, manhole cover visor 18, vavuum pump 19, air compressor machine 20, refrigerant chuck cavity 21, flow-guiding type are strengthened axle 24 in gusset 22, kettle 23, the dispersion impeller, scrape wall oar outer shaft 25, scrape wall oar 26, ring 38, baiting valve bolt locating hole 39, baiting valve 40 constitute in the cavity 27, shaft coupling 28, pedestal 29, refrigerant chuck 30, the line of induction 31, digital display meter 32, sensor 33, thermometric blowing flange 34, sensing temperature meter probe protective casing 35, flange outer shroud 36, flange drain hole 37, flange.
Dispersal device comprises dispersed with stirring device and dispersed with stirring device driving mechanism; Agitator comprises in the dispersion impeller axle 24 and is fixed on the double-deck dispersion impeller 6 on the axle 24 in the dispersion impeller, and double-deck dispersion impeller 6 is installed in the bottom of axle 24 in the dispersion impeller, and axle 24 is connected with dispersion impeller drive motors 1 through shaft coupling 28 in the dispersion impeller; Scrape wall oar outer shaft 25 and be enclosed within the outside of axle 24 in the dispersion impeller; Scrape wall oar 26 and be fixed on the outside of scraping wall oar 26 through scraping wall oar support arm 4; Scrape wall oar support arm 4 and scrape wall oar outer shaft 25 and be 80 ° of angles and fix, scrape wall oar 26 and be fixed on the bottom of scraping wall oar outer shaft 25 through scraping wall oar support arm 4.
6 tetrafluoro scraper plates 9 are housed altogether scraping on the wall oar 26, wherein 2 tetrafluoro scraper plates 9 are contained in the bottom of scraping wall oar 26, in the upright side of scraping wall oar 26 2 tetrafluoro scraper plates 9 are housed respectively; Scraping 4 tetrafluoro scraper plates, the 9 interleaved positions of the upright side of wall oar 26 installs; Tetrafluoro scraper plate 9 is movable; Tetrafluoro scraper plate 9 can be along with the rotation of the friction speed of scraping wall oar 26; Do the swing of different amplitudes; Tetrafluoro scraper plate 9 is 1cm with the minimum clearance of the inwall of kettle 23, and tetrafluoro scraper plate 9 can be adjusted amplitude of fluctuation, the resistance when reducing to scrape wall according to the China ink slurry of different viscosities simultaneously automatically; Dispersed with stirring device driving mechanism comprises dispersion impeller drive motors 1, scrapes wall oar drive motors 2, reductor 3, gear-box 11 and shaft coupling 28; Dispersion impeller drive motors 1 with scrape wall oar drive motors 2 and be installed on the shell of the gear-box 11 on the kettle 23 through pedestal 29 and reductor 3 respectively, reductor 3 with scrape wall oar drive motors 2 and be in transmission connection; Axle 24 is connected with dispersion impeller drive motors 1 through shaft coupling 28 in the dispersion impeller.
The outside of kettle 23 is provided with refrigerant chuck 30; Form refrigerant chuck cavity 21 between refrigerant chuck 30 and the kettle 23; Refrigerant chuck 30 is provided with the refrigerant inlet 8 and refrigerant exit 5 that is communicated with refrigerant chuck cavity 21; In refrigerant chuck cavity 21, be provided with the flow-guiding type reinforcement gusset 22 that is used to increase the refrigerant circular flow, flow-guiding type reinforcement gusset 22 shape in the shape of a spiral is coiled on the outer wall of the kettle 23 in the refrigerant chuck cavity 21, and flow-guiding type is strengthened gusset 22 and is fixed on the outer wall of kettle 23 through the mode of welding; Be not connected with the inwall of refrigerant chuck 30, near the refrigerant chuck cavity part of autoclave body bottom flow-guiding type be not installed and strengthened gusset.
The edge of the flange outer shroud 36 of thermometric blowing flange 34 is fixed on the bottom of kettle 23 with the mode of welding, and thermometric blowing flange 34 is connected with baiting valve 40 through baiting valve bolt locating hole 39.
Device for detecting temperature comprises Cu-50 copper resistance sensing temperature meter probe 7, bimetallic thermometer 10, the line of induction 31, digital display meter 32, sensor 33, thermometric blowing flange 34, sensing temperature meter probe protective casing 35; Cu-50 copper resistance sensing temperature meter probe 7 in the sensor 33 is installed in the sensing temperature meter probe protective casing 35 on the thermometric blowing flange 34; Cu-50 copper resistance sensing temperature meter 7 one ends of popping one's head in are connected through the line of induction 31, and the other end is connected with digital display meter 32; Bimetallic thermometer 10 is fixed on a side of Scattered Kettle kettle cover top, adds inlet 14 with the liquid material and is 180 ° of diagonal bits installations.
Brief description is the operation principle of this Scattered Kettle once:
When disperseing to stir work, at first to use delivery pump that liquid material is added inlet 14 through the liquid material and pump in the cavity 27 of Scattered Kettle, low rate start dispersion impeller drive system adds inlet 13 with solid powder from powder and adds in the cavity 27 of Scattered Kettle.
After dispersion impeller drive motors 1 slowed down through reductor 3, axle 24 rotated in gear-box 11 transmissions drive dispersion impeller, scrapes wall oar drive motors 2 through the frequency converter timing in the control cabinet, and speed adjustable range is at 0～1500rpm/min.Powder material and liquid material tentatively mix under double-deck dispersion impeller 6 and the acting in conjunction of scraping wall oar 26.
In 6 tetrafluoro scraper plates 9 on scraping wall oar 26,2 are installed in the tetrafluoro scraper plate 9 of scraping wall oar 26 bottoms and can prevent that the material of big proportion is deposited at the bottom of the still, the promotion circulation; The interleaved position is installed in 4 movable tetrafluoro scraper plates 9 scraping wall oar 26 upright sides; Can do the swing of different amplitudes along with the rotation of the friction speed of scraping wall oar 26, tetrafluoro scraper plate 9 can be adjusted amplitude of fluctuation according to the China ink slurry of different viscosities simultaneously automatically; Resistance when reducing to scrape wall; Can eliminate the retention layer on the still inner barrel wall, can improve heat transfer efficiency, improve dispersion effect.
Scrape wall oar outer shaft 25 and be counter motion with respect to axle 24 in the dispersion impeller, can significantly promote the axial circulating current motion of material, suppress the tangential motion of material, and produce the full still systemic circulation of fluid, incorporation time is short, has eliminated dead band and superpower turbulent area in the still simultaneously.
When whole materials add finish and tentatively stir after, system viscosity can sharply rise, that opens Scattered Kettle kettle cover top this moment takes out (putting) air valve 16, starts vavuum pump 19,, disperses under vacuum environment at-0.09MPa until vacuum.The vacuum dispersing mode both can be got rid of the bubble of bringing in the dispersed with stirring process, can promote the dispersion of solid-liquid two phase materials again; The vacuum dispersing mode can destroy the capillary pressure extruding of solid powder aggregation inner air liquid body and the anti-phase meniscus that forms and strengthen liquid to solid aggregates or the inner osmosis of agglomerate; Under the effect of the powerful shearing force of double-deck dispersion impeller 6; Raising is to the depolymerization efficient of solid powder; Improve wetting effect, shorten jitter time, reduce the viscosity of system rapidly; Can get rid of simultaneously the moisture that solid powder is absorbed in transportation, storage process, thereby guarantee the stable of product batches.According to the needs of technology, time and the cycle-index that vacuum is disperseed carried out in decision.When carrying out the dispersion of ultraviolet (UV) light-curable ink; Can be divided into the operation that several stages carries out the vacuum breaker supplemental oxygen; Disperse because of long-time vacuum, reach the inner concentration of oxygen of system in the still and reduce, under the effect of high-speed stirred friction; The thermosetting material of ultraviolet (UV) photocuring can aggravate gelation under the environment of anaerobic tendency reaches the effect that resistance gathers through supplemental oxygen.After closing vavuum pump 19, open air compressor machine 20 and in still, replenish the air of handling through clean, thereby improve the stability of technological operation.After fineness of dispersion reaches requirement, when carrying, open air compressor machine 20, under the prerequisite of controlled pressure, can improve the conveying capacity of high viscosity inks China ink slurry.
In carrying out the vacuum dispersion process; Through monitoring sensing temperature meter digital display meter 32 temperature displayed that the inner bimetallic thermometer 10 of kettle is communicated with kettle 23 bottoms; When the temperature of printing ink China ink slurry is too high; Open the refrigerant system immediately, the self cooling matchmaker of refrigerant liquid enters the mouth and 8 gets in the refrigerant chuck cavitys 21, strengthens gusset 22 from bottom to top by refrigerant exit 5 circulations and go out along flow-guiding type; The violent friction great amount of heat that produces at the bottom of the still of printing ink China ink slurry because of high speed rotation and Scattered Kettle is exchanged, be unlikely to gel thereby the assurance scatter operation is carried out smoothly.
Can know that by technological general knowledge the utility model also can be realized through other the embodiment that does not break away from its spirit or essential feature.Therefore above-mentioned disclosed embodiment with regard to each side, all just illustrates, and is not only.All in the utility model scope or the change that is being equal in the scope of the utility model all comprised by the utility model.
Claims (3)
1. controllable temperature high-speed stirred Scattered Kettle with thermometric blowing flange; Comprise dispersion impeller drive motors (1), scrape wall oar drive motors (2), reductor (3), scrape that wall oar support arm (4), refrigerant exit (5), double-deck dispersion impeller (6), Cu-50 copper resistance sensing temperature meter probe (7), refrigerant inlet (8), tetrafluoro scraper plate (9), bimetallic thermometer (10), gear-box (11), manhole cover (12), powder add that inlet (13), liquid material add inlet (14), visor lamp (15), take out (putting) air valve (16), vacuum meter (17), manhole cover visor (18), vavuum pump (19), air compressor machine (20), refrigerant chuck cavity (21), flow-guiding type are strengthened axle (24) in gusset (22), kettle (23), the dispersion impeller, scrape wall oar outer shaft (25), scrape wall oar (26), ring (38), baiting valve bolt locating hole (39), baiting valve (40) in the cavity (27), shaft coupling, (28), pedestal (29), refrigerant chuck (30), the line of induction (31), digital display meter (32), sensor (33), thermometric blowing flange (34), sensing temperature meter probe protective casing (35), flange outer shroud (36), flange drain hole (37), flange, it is characterized in that: it is Nei Yu a side of Scattered Kettle loam cake that Cu-50 copper resistance sensing temperature meter Tan Tou (7) Yu the bimetallic thermometer (10) of described thermometric is installed in the thermometric blowing flange (34) end the still sensing temperature meter & CAT[N
2. the edge of the flange outer shroud (36) of thermometric blowing flange according to claim 1 (34) is fixed on the bottom of kettle (23), and thermometric blowing flange (34) is connected with baiting valve (40).
3. the Cu-50 copper resistance sensing temperature meter of sensor according to claim 1 (33) probe (7) is fixed in the sensing temperature meter probe protective casing (35) that the flange outer shroud (36) of thermometric blowing flange (34) locates.
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| Application Number | Priority Date | Filing Date | Title |
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| CN2011205569792U CN202289926U (en) | 2011-12-22 | 2011-12-22 | Temperature-controllable high-speed stirring and dispersing kettle with temperature measurement and discharge flange |
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| CN2011205569792U CN202289926U (en) | 2011-12-22 | 2011-12-22 | Temperature-controllable high-speed stirring and dispersing kettle with temperature measurement and discharge flange |
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- 2011-12-22 CN CN2011205569792U patent/CN202289926U/en not_active Expired - Lifetime
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| CN102961992A (en) * | 2012-12-04 | 2013-03-13 | 长兴适安特服装材料有限公司 | Paste mixer |
| CN103240018A (en) * | 2013-05-03 | 2013-08-14 | 南通金陵农化有限公司 | Emulsifying and shearing device of suspending agent |
| CN104043360A (en) * | 2013-10-18 | 2014-09-17 | 武汉科技大学 | Leaching tank having adjustable double shaft stirring device |
| CN105013377A (en) * | 2015-08-12 | 2015-11-04 | 吴江佳亿电子科技有限公司 | Automatic stirring device capable of controlling feeding and carrying out vacuumizing |
| CN105413534A (en) * | 2015-11-25 | 2016-03-23 | 郑臣钏 | Efficient chemical mixing device |
| CN105538531A (en) * | 2015-12-31 | 2016-05-04 | 广州市合诚化学有限公司 | Uniform mixing device for preparing high-liquid-content resin powder and application of uniform mixing device |
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