CN102219295B - Dissolving and adding system for permanganate composite medicament - Google Patents
Dissolving and adding system for permanganate composite medicament Download PDFInfo
- Publication number
- CN102219295B CN102219295B CN 201110102666 CN201110102666A CN102219295B CN 102219295 B CN102219295 B CN 102219295B CN 201110102666 CN201110102666 CN 201110102666 CN 201110102666 A CN201110102666 A CN 201110102666A CN 102219295 B CN102219295 B CN 102219295B
- Authority
- CN
- China
- Prior art keywords
- dissolving
- guiding device
- vessel
- dissolving vessel
- water inlet
- 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.)
- Expired - Fee Related
Links
Images
Abstract
The invention discloses a dissolving and adding system for permanganate composite medicament, and relates to a dissolving and adding system. The dissolving and adding system aims at solving the problem that in the existing medicament dissolving tank, the medicament dissolving effect is poor, which results in inaccurate medicament batching, thus directly affecting water treatment effect. In the invention, a material inlet part is arranged on a grid, a material transmission part is arranged in a dissolving tank, an outer-circulation hydraulic-power stirring device is arranged at the left side of the dissolving tank, a first flow guiding device and a second flow guiding device are both arranged in the dissolving tank obliquely, the inner part of the dissolving tank is divided into three dissolving cavities, the blades of a direct-blade layer are arranged on the stirring shaft of a first dissolving cavity, two wing-shaped blades are respectively arranged on stirring shafts in a second dissolving cavity and a third dissolving cavity, three ultrasonic generators are respectively arranged on the inner walls of dissolving tanks in the three dissolving cavities, slag discharging pipes are arranged at the bottom ends of the dissolving tanks in a penetrating manner, and slag discharging pipe valves are arranged on the slag discharging pipes. The dissolving and adding system is used for dissolving and processing process.
Description
Technical field
The present invention relates to a kind of dissolving dosing system, be specifically related to a kind of dissolving dosing system of permanganate composite chemical, belong to water-treatment technology field.
Background technology
In water treatment procedure, medicament dissolving vessel commonly used adopts the mechanical stirring mixed dissolution usually, earlier quantitative medicament is added in the dissolving vessel, carries out water filling in the jar again.Carry out mechanical stirring after the water filling; This medicament dissolving whipping appts; For common liquid type medicament and solvability medicament preferably, can satisfy the requirement of abundant dissolving blended, but it is more to produce dust for some; Especially the stronger powder medicine of insoluble corrodibility, this dissolver solute effect is just undesirable; The agitating vane of traditional medicament dissolving vessel mostly is straight leaf layer blade, can not form a jar internal recycle during stirring, and the medicament solute effect at the bottom of sinking to jar is poor, and it is inaccurate to cause medicament to be batched, thereby has directly influenced the treatment effect of water.
Summary of the invention
It is poor to the objective of the invention is for the medicament solute effect that solves existing medicament dissolving vessel, and it is inaccurate to cause medicament to be batched, thereby directly influences the problem of water treatment effect, and then a kind of dissolving dosing system of permanganate composite chemical is provided.
Technical scheme of the present invention is: a kind of dissolving dosing system of permanganate composite chemical comprises dissolving vessel, agitator motor, stir shaft, straight leaf layer blade, liquid level sensor, under meter, tensimeter, inlet valve, water inlet pipe, rising pipe, flowing water Valve, graticule mesh, feedwater equipment, shaft coupling and three ultrasonic generators, and rising pipe is located in the right-hand member bottom of dissolving vessel, and flowing water Valve is arranged on the rising pipe; One end of water inlet pipe is located in the left end top of dissolving vessel, and the other end of water inlet pipe is connected with feedwater equipment, and inlet valve, tensimeter and under meter are successively set on the water inlet pipe from top to bottom; Liquid level sensor is arranged in the dissolving vessel; The graticule mesh lid is contained on the port of dissolving vessel, and agitator motor is packed in the center of graticule mesh, and stir shaft is connected with the output shaft of agitator motor through shaft coupling; And stir shaft places in the dissolving vessel; The dissolving dosing system also comprises top feeding unit, outer circulation waterpower whipping appts, two airfoil fans, first guiding device, second guiding device, scum pipe and scum pipe valves, and the top feeding unit comprises feeding part and material transfer part, and feeding part is arranged on the graticule mesh; Material transfer partly is arranged in the dissolving vessel; And material transfer partly be positioned at feeding part under, outer circulation waterpower whipping appts is arranged on the left side of dissolving vessel, first guiding device and second guiding device all are obliquely installed in dissolving vessel; One end of first guiding device is packed on the dissolving vessel; The other end of first guiding device suspends, and an end of second guiding device is packed on the dissolving vessel, and the other end of second guiding device suspends; One end of first guiding device and an end of second guiding device are separately positioned on the both sides of dissolving vessel; The inside of dissolving vessel is divided into three dissolving chambers, and three dissolving chambers are followed successively by the first dissolving chamber, the second dissolving chamber and the 3rd dissolving chamber from top to bottom, and straight leaf layer blade is arranged on the stir shaft of the first dissolving chamber; Two airfoil fans are separately positioned on the indoor stir shaft of the second dissolving chamber and the 3rd lysing chamber; Three ultrasonic generators are separately positioned on the indoor dissolving vessel inwall of three lysing chambers, and scum pipe is located in the bottom of dissolving vessel, and the scum pipe valve is arranged on the scum pipe.
The present invention compared with prior art has following effect: 1. the present invention adds medicament through the speed adjustment to feeding part and material transfer part accurately, makes that dissolving is more thorough, and strength of solution is set arbitrarily according to concrete processing requirement.2. the integrated equipment of total system of the present invention is convenient to install and use.3. the present invention is under the rotation of stir shaft, and airfoil fan makes the liquid under the impeller carry out two kinds of motions, and first liquid moves in a circle with blade; It two is under the lift effect, to axially move, thereby makes the mixing liquid of solvent and solute form circulation at the 3rd dissolving chamber, makes that dissolving is more abundant.4. first guiding device of the present invention and second guiding device have effectively increased the duration of contact of medicament and current, make medicament and water dissolution more abundant.5. the present invention is simple in structure, and perfect in shape and function is easy to realize.6. the present invention has reduced the dust that powder medicine causes in the process of adding.7. ultrasonic generator of the present invention has effectively been accelerated the medicament dissolution rate.
Description of drawings
Fig. 1 is a structural representation of the present invention; Fig. 2 is the vertical view of Fig. 1; Fig. 3 is the structural representation of airfoil fan; Fig. 4 is the structural representation of first guiding device.
Embodiment
Embodiment one: combine Fig. 1-Fig. 4 that this embodiment is described; The dissolving dosing system of a kind of permanganate composite chemical of this embodiment comprises dissolving vessel 1, agitator motor 9, stir shaft 10, straight leaf layer blade 11, liquid level sensor 13, under meter 14, tensimeter 15, inlet valve 16, water inlet pipe 17, rising pipe 24, flowing water Valve 25, graticule mesh 26, feedwater equipment 28, shaft coupling 29 and three ultrasonic generators 8; Rising pipe 24 is located in the right-hand member bottom of dissolving vessel 1, and flowing water Valve 25 is arranged on the rising pipe 24, and an end of water inlet pipe 17 is located in the left end top of dissolving vessel 1; The other end of water inlet pipe 17 is connected with feedwater equipment 28; Inlet valve 16, tensimeter 15 and under meter 14 from top to bottom are successively set on the water inlet pipe 17, and liquid level sensor 13 is arranged in the dissolving vessel 1, and graticule mesh 26 lids are contained on the port of dissolving vessel 1; Agitator motor 9 is packed in the center of graticule mesh 26; Stir shaft 10 is connected with the output shaft of agitator motor 9 through shaft coupling 29, and stir shaft 10 places in the dissolving vessel 1, dissolves dosing system and also comprises top feeding unit 30, outer circulation waterpower whipping appts 31, two airfoil fans 12, first guiding device 32, second guiding device 33, scum pipe 22 and scum pipe valve 23; Top feeding unit 30 comprises feeding part and material transfer part; Feeding part is arranged on the graticule mesh 26, and material transfer partly is arranged in the dissolving vessel 1, and material transfer partly be positioned at feeding part under; Outer circulation waterpower whipping appts 31 is arranged on the left side of dissolving vessel 1; First guiding device 32 and second guiding device 33 all are obliquely installed in dissolving vessel 1, and an end of first guiding device 32 is packed on the dissolving vessel 1, and the other end of first guiding device 32 suspends; One end of second guiding device 33 is packed on the dissolving vessel 1; The other end of second guiding device 33 suspends, and an end of an end of first guiding device 32 and second guiding device 33 is separately positioned on the both sides of dissolving vessel 1, and the inside of dissolving vessel 1 is divided into three dissolving chambers; Three dissolving chambers are followed successively by the first dissolving chamber 1-1, the second dissolving chamber 1-2 and the 3rd dissolving chamber 1-3 from top to bottom; Straight leaf layer blade 11 is arranged on the stir shaft 10 of the first dissolving chamber 1-1, and two airfoil fans 12 are separately positioned on the stir shaft 10 in the second dissolving chamber 1-2 and the 3rd dissolving chamber 1-3, and three ultrasonic generators 8 are separately positioned on indoor dissolving vessel 1 inwall of three lysing chambers; Scum pipe 22 is located in the bottom of dissolving vessel 1, and scum pipe valve 23 is arranged on the scum pipe 22.
The dissolving vessel 1 of this embodiment adopts glass-reinforced plastic material to process, and the inwall of dissolving vessel 1 adopts epoxy resin to carry out rotproofing.
The airfoil fan 12 of this embodiment tilts to be fixed on the stir shaft 10, and at water exercise, the fluid relative current is crossed airfoil fan 12 to airfoil fan 12 along with the rotation of stir shaft 10; Airfoil fan 12 streamlined just opposite with wing; Make that the flow velocity above the airfoil fan 12 is little, pressure is big, and the flow velocity below the airfoil fan 12 is big, pressure is little; Fluid firmly is downward to the cooperation of airfoil fan 12, and the reactive force of airfoil fan convection cell makes progress.Under the rotation of stir shaft 10, airfoil fan 12 is carrying out two kinds of motions like this, and first liquid moves in a circle with airfoil fan 12; It two is to axially move at lift effect airfoil blade 12.Thereby make the mixing liquid of solvent and solute in the 3rd dissolving chamber 1-3, form circulation.
Embodiment two: combine Fig. 1 that this embodiment is described; The feeding part of the top feeding unit 30 of this embodiment comprises no base cone shape explosive box 2 and soaks device 4; No base cone shape explosive box 2 is arranged on the upper surface of graticule mesh 26; Soak device 4 and be positioned at the left side of no base cone shape explosive box 2, and soak device 4 and be positioned on the lower surface of graticule mesh 26.So be provided with; During work, soak device 4 and constantly spray water droplet, powder medicine is soaked; The water that the wetted medicament falls in back and the water inlet pipe is mixed in the dissolving vessel 1; Effectively reduce the dust that powder medicine causes in the process that falls, obtained good confection simultaneously, avoided the generation of caking phenomenon.Other composition is identical with embodiment one with annexation.
Embodiment three: combine Fig. 1 that this embodiment is described; The material transfer of the top feeding unit 30 of this embodiment partly comprises medicament transport unit 3 and conveyor belt flights 5; Medicament transport unit 3 is arranged in the dissolving vessel 1, and medicament transport unit 3 be arranged on no base cone shape explosive box 2 under, conveyor belt flights 5 is packed on the dissolving vessel 1; Conveyor belt flights 5 is positioned at the below of medicament transport unit 3, and leaves the gap between conveyor belt flights 5 and the medicament transport unit 3.So be provided with; Press close to medicament transport unit 3 below be provided with conveyor belt flights 5, the medicament that sticks on the medicament transport unit 3 is got in the dissolving vessels 1 along conveyor belt flights 5, the transmission precision of medicament transport unit 3 is high; The concentration accurate and adjustable of solution, concentration stabilize.Other composition is identical with embodiment one or two with annexation.
When medicament transport unit 3 did not rotate, when medicament was poured in the no base cone shape explosive box 2, medicament can directly pass through discharge port to medicament transport unit 3; When the height of on medicament transport unit 3, piling up along with medicament raises, will block the discharge port of no base cone shape explosive box 2 gradually, block no base cone shape explosive box 2 discharge ports after; Continuation adds medicament in no base cone shape explosive box 2; Until required pharmaceutical quantities, when medicament transport unit 3 rotated, the medicament of no base cone shape explosive box 2 discharge port lower ends was along with 3 motions of medicament transport unit; Under action of gravity, the medicament in the no base cone shape explosive box 2 will continuously replenish on the medicament transport unit 3.
Embodiment four: combine Fig. 1 that this embodiment is described, the conveyor belt flights 5 and the gap H between the medicament transport unit 3 of this embodiment are 3mm-10mm.So be provided with, be convenient to the medicament that sticks on the medicament transport unit 3 is got in the dissolving vessel 1 along conveyor belt flights 5.Other composition is identical with embodiment three with annexation.
Embodiment five: combine Fig. 1 that this embodiment is described; The outer circulation waterpower whipping appts 31 of this embodiment comprises that outer circulation waterpower stirs water inlet pipe 18, valve 19, outer circulation pump 20 and flow deflector 21; The two ends that outer circulation waterpower stirs water inlet pipe 18 all are located on the dissolving vessel 1; Valve 19 is successively set on outer circulation waterpower with outer circulation pump 20 and stirs on the water inlet pipe 18, and flow deflector 21 is arranged on the inwall of dissolving vessel 1, and outer circulation waterpower stirs water inlet pipe 18 and is positioned on the flow deflector 21.So be provided with,, can play the effect of dilution lower floor solution on the one hand because the strength of solution of upper strata liquid level is lower, can make on the other hand the not pharmaceutical dissolution that sinks at the bottom of 1 jar of the dissolving vessel suspend with water in continue mixed dissolution, effectively raise dissolution rate.Other composition is identical with embodiment one or four with annexation.
Embodiment six: combine Fig. 1 that this embodiment is described, the end that the outer circulation waterpower of this embodiment stirs water inlet pipe 18 is located in the second dissolving chamber 1-2, and the other end that outer circulation waterpower stirs water inlet pipe 18 is located in the 3rd dissolving chamber 1-3.So be provided with, be convenient to the lower water of strength of solution in the second dissolving chamber 1-2 of upper strata is extracted out, flow in the 3rd dissolving chamber 1-3, effectively utilized water resources, practiced thrift cost.Other composition is identical with embodiment five with annexation.
Embodiment seven: combine Fig. 1 and Fig. 4 that this embodiment is described, first guiding device 32 of this embodiment is installed in the dissolving vessel 1, and the upper surface of first guiding device 32 and horizontal tilt angle alpha are 30 °-40 °.So be provided with, be convenient to a part of mixed solution under the effect of first guiding device 32, get in the second dissolving chamber 1-2 along first guiding device 32.Other composition and annexation and embodiment one or six phase are together.
Embodiment eight: combine Fig. 1 and Fig. 4 that this embodiment is described, second guiding device 33 of this embodiment is installed in the dissolving vessel 1, and the upper surface of second guiding device 33 and horizontal inclination angle beta are 30 °-40 °.So be provided with, the mixed solution after being convenient in the second dissolving chamber 1-2, stir gets in the 3rd dissolving chamber 1-3 along second guiding device 33 under the effect of second guiding device 33.Other composition is identical with embodiment one with annexation.
Embodiment nine: combine Fig. 1 and Fig. 4 that this embodiment is described, first guiding device 32 of this embodiment and second guiding device 33 include flow deflector 6 and perforate swash plate 7, and flow deflector 6 vertically is packed on the perforate swash plate 7.So be provided with, first guiding device 32 and second guiding device 33 have effectively increased the duration of contact of medicament and current, make medicament and water dissolution more abundant.Other composition is identical with embodiment eight with annexation.
Embodiment ten: combine Fig. 1 that this embodiment is described, the dissolving dosing system of a kind of permanganate composite chemical of this embodiment also comprises shower nozzle 27, and shower nozzle 27 is arranged in the dissolving vessel 1, and shower nozzle 27 is connected with placing dissolving vessel 1 interior water inlet pipe 17.So be provided with, be convenient to the medicament on the conveyor belt flights 5 is washed away.Other composition is identical with embodiment one or nine with annexation.
The working process of this embodiment is:
The present invention's design is divided into two sections with required dissolution time; The last period, dissolution time carried out in the jar water filling and medicament adds; Meanwhile carry out mechanical stirring; And when the liquid level in 1 jar of the dissolving vessel surpasses the height of ultrasonic generator 8, just start corresponding with it ultrasonic generator 8, so that medicament carries out the UW dissolving in that each dissolving is indoor.Concrete dissolution process is:
Powder medicines in the no base cone shape explosive box 2 are delivered to by medicament transport unit 3 earlier and are soaked device 4 belows, and the powder medicine after soaking falls at the end of medicament transport unit 3, and are mixed in the dissolving vessel 1 with water in the water inlet pipe.Under the effect of first guiding device 32; The mixed solution part of medicament and current gets in the second dissolving chamber 1-2 through the circular hole on the perforate swash plate 7 of first guiding device 32; Part mixed solution gets in the second dissolving chamber 1-2 along perforate swash plate 7 under the effect of the perforate swash plate 7 of first guiding device 32.Enter into the interior medicament of the second dissolving chamber 1-2 and the mixed solution of current; At second guiding device 33 with under the effect of airfoil fan 12; After mixing stirring and dissolving; The mixed solution part of medicament and current gets in the 3rd dissolving chamber 1-3 through the circular hole on the perforate swash plate 7 of second guiding device 33, and a part of mixed solution gets in the 3rd dissolving chamber 1-3 along perforate swash plate 7 under the effect of the perforate swash plate 7 of second guiding device 33.The one section dissolution time in back is in 1 jar of dissolving vessel, to be filled to liquid level constant (the highest liquid level) and to stop under the situation that medicament adds; Open outer circulation pump 20; Carrying out waterpower stirs; Accompany by the dissolving of mechanical stirring and UW simultaneously, be stamped a graticule mesh 26, can prevent effectively that foreign material from falling at the upper surface of dissolving vessel 1; Liquid level sensor 13 level condition in personnel's jar of can reporting is timely controlled flooding quantity and dosage with this.
Claims (10)
1. the dissolving dosing system of a permanganate composite chemical; It comprises dissolving vessel (1), agitator motor (9), stir shaft (10), straight leaf layer blade (11), liquid level sensor (13), under meter (14), tensimeter (15), inlet valve (16), water inlet pipe (17), rising pipe (24), flowing water Valve (25), graticule mesh (26), feedwater equipment (28), shaft coupling (29) and three ultrasonic generators (8); Rising pipe (24) is located in the right-hand member bottom of dissolving vessel (1); Flowing water Valve (25) is arranged on the rising pipe (24); One end of water inlet pipe (17) is located in the left end top of dissolving vessel (1), and the other end of water inlet pipe (17) is connected with feedwater equipment (28), and inlet valve (16), tensimeter (15) and under meter (14) from top to bottom are successively set on the water inlet pipe (17); Liquid level sensor (13) is arranged in the dissolving vessel (1); Graticule mesh (26) lid is contained on the port of dissolving vessel (1), and agitator motor (9) is packed in the center of graticule mesh (26), and stir shaft (10) is connected with the output shaft of agitator motor (9) through shaft coupling (29); And stir shaft (10) places in the dissolving vessel (1); It is characterized in that: the dissolving dosing system also comprises top feeding unit (30), outer circulation waterpower whipping appts (31), two airfoil fans (12), first guiding device (32), second guiding device (33), scum pipe (22) and scum pipe valve (23), and top feeding unit (30) comprises feeding part and material transfer part, and feeding part is arranged on the graticule mesh (26); Material transfer partly is arranged in the dissolving vessel (1); And material transfer partly be positioned at feeding part under, outer circulation waterpower whipping appts (31) is arranged on the left side of dissolving vessel (1), first guiding device (32) and second guiding device (33) all are obliquely installed in dissolving vessel (1); One end of first guiding device (32) is packed on the dissolving vessel (1); The other end of first guiding device (32) suspends, and an end of second guiding device (33) is packed on the dissolving vessel (1), and the other end of second guiding device (33) suspends; One end of one end of first guiding device (32) and second guiding device (33) is separately positioned on the both sides of dissolving vessel (1); The inside of dissolving vessel (1) is divided into three dissolving chambers, and three dissolving chambers are followed successively by the first dissolving chamber (1-1), the second dissolving chamber (1-2) and the 3rd dissolving chamber (1-3) from top to bottom, and straight leaf layer blade (11) is arranged on the stir shaft (10) of the first dissolving chamber (1-1); Two airfoil fans (12) are separately positioned on the stir shaft (10) in the second dissolving chamber (1-2) and the 3rd dissolving chamber (1-3); Three ultrasonic generators (8) are separately positioned on indoor dissolving vessel (1) inwall of three lysing chambers, and scum pipe (22) is located in the bottom of dissolving vessel (1), and scum pipe valve (23) is arranged on the scum pipe (22).
2. the dissolving dosing system of a kind of permanganate composite chemical according to claim 1; It is characterized in that: the feeding part of top feeding unit (30) comprises no base cone shape explosive box (2) and soaks device (4); No base cone shape explosive box (2) is arranged on the upper surface of graticule mesh (26); Soak device (4) and be positioned at the left side of no base cone shape explosive box (2), and soak device (4) and be positioned on the lower surface of graticule mesh (26).
3. the dissolving dosing system of a kind of permanganate composite chemical according to claim 1 and 2; It is characterized in that: the material transfer of top feeding unit (30) partly comprises medicament transport unit (3) and conveyor belt flights (5); Medicament transport unit (3) is arranged in the dissolving vessel (1); And medicament transport unit (3) be arranged on no base cone shape explosive box (2) under; Conveyor belt flights (5) is packed on the dissolving vessel (1), and conveyor belt flights (5) is positioned at the below of medicament transport unit (3), and leaves the gap between conveyor belt flights (5) and the medicament transport unit (3).
4. the dissolving dosing system of a kind of permanganate composite chemical according to claim 3 is characterized in that: the gap (H) between conveyor belt flights (5) and the medicament transport unit (3) is 3mm-10mm.
5. according to the dissolving dosing system of claim 1 or 4 described a kind of permanganate composite chemicals; It is characterized in that: outer circulation waterpower whipping appts (31) comprises that outer circulation waterpower stirs water inlet pipe (18), valve (19), outer circulation pump (20) and flow deflector (21); The two ends that outer circulation waterpower stirs water inlet pipe (18) all are located on the dissolving vessel (1); The outer circulation waterpower that is successively set on valve (19) and outer circulation pump (20) stirs on the water inlet pipe (18); Flow deflector (21) is arranged on the inwall of dissolving vessel (1), and outer circulation waterpower stirs water inlet pipe (18) and is positioned on the flow deflector (21).
6. the dissolving dosing system of a kind of permanganate composite chemical according to claim 5; It is characterized in that: the end that outer circulation waterpower stirs water inlet pipe (18) is located in the second dissolving chamber (1-2), and the other end that outer circulation waterpower stirs water inlet pipe (18) is located in the 3rd dissolving chamber (1-3).
7. according to the dissolving dosing system of claim 1 or 6 described a kind of permanganate composite chemicals; It is characterized in that: first guiding device (32) is installed in the dissolving vessel (1), and the upper surface of first guiding device (32) and horizontal angle of inclination (α) are 30 °-40 °.
8. the dissolving dosing system of a kind of permanganate composite chemical according to claim 1; It is characterized in that: second guiding device (33) is installed in the dissolving vessel (1), and the upper surface of second guiding device (33) and horizontal angle of inclination (β) are 30 °-40 °.
9. the dissolving dosing system of a kind of permanganate composite chemical according to claim 8; It is characterized in that: first guiding device (32) and second guiding device (33) include flow deflector (6) and perforate swash plate (7), and flow deflector (6) vertically is packed on the perforate swash plate (7).
10. according to the dissolving dosing system of claim 1 or 9 described a kind of permanganate composite chemicals; It is characterized in that: said dissolving dosing system also comprises shower nozzle (27); Shower nozzle (27) is arranged in the dissolving vessel (1), and shower nozzle (27) water inlet pipe (17) interior with placing dissolving vessel (1) is connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110102666 CN102219295B (en) | 2011-04-22 | 2011-04-22 | Dissolving and adding system for permanganate composite medicament |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110102666 CN102219295B (en) | 2011-04-22 | 2011-04-22 | Dissolving and adding system for permanganate composite medicament |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102219295A CN102219295A (en) | 2011-10-19 |
| CN102219295B true CN102219295B (en) | 2012-12-05 |
Family
ID=44776048
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201110102666 Expired - Fee Related CN102219295B (en) | 2011-04-22 | 2011-04-22 | Dissolving and adding system for permanganate composite medicament |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102219295B (en) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102897922A (en) * | 2012-09-28 | 2013-01-30 | 邓杰帆 | Ultrasonic catalysis/biochemistry waste liquid treatment reactor and waste liquid treating method thereof |
| CN104307579A (en) * | 2014-10-28 | 2015-01-28 | 赵永兴 | Ion exchange column |
| CN106050192A (en) * | 2016-06-06 | 2016-10-26 | 成都大漠石油技术有限公司 | Agent-feeding device improvement structure |
| CN105889757A (en) * | 2016-06-06 | 2016-08-24 | 成都大漠石油技术有限公司 | Chemical feeding device based on improving mixing uniformity of chemical |
| CN108328673A (en) * | 2018-01-30 | 2018-07-27 | 福建聚云科技股份有限公司 | A kind of urban lake-reservoir water environment pollution restoration system |
| CN108409037A (en) * | 2018-03-24 | 2018-08-17 | 薛静泽 | A kind of recovery and processing system for handling acidic industrial effluent |
| CN109511850A (en) * | 2018-12-29 | 2019-03-26 | 中国农业科学院农产品加工研究所 | The preparation method of black five cereals beverage |
| CN111520975A (en) * | 2020-06-02 | 2020-08-11 | 湖南省湘衡盐化有限责任公司 | Industrial salt drying system and method |
| CN115197778A (en) * | 2022-09-15 | 2022-10-18 | 山东康境海洋生物工程有限公司 | Enrichment and purification device for krill oil phospholipid and implementation method thereof |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2186810A1 (en) * | 1996-02-23 | 1997-08-24 | Ralph H. Larson | Permanganate feeder for iron filter |
| CN2794621Y (en) * | 2005-05-31 | 2006-07-12 | 江阴市科达机械电子有限公司 | Supersonic paint emulsifying stirrer |
| CN201295597Y (en) * | 2008-11-10 | 2009-08-26 | 江苏伊思达电池有限公司 | Outer circulation type slurry vacuum mixer |
-
2011
- 2011-04-22 CN CN 201110102666 patent/CN102219295B/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2186810A1 (en) * | 1996-02-23 | 1997-08-24 | Ralph H. Larson | Permanganate feeder for iron filter |
| CN2794621Y (en) * | 2005-05-31 | 2006-07-12 | 江阴市科达机械电子有限公司 | Supersonic paint emulsifying stirrer |
| CN201295597Y (en) * | 2008-11-10 | 2009-08-26 | 江苏伊思达电池有限公司 | Outer circulation type slurry vacuum mixer |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102219295A (en) | 2011-10-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102219295B (en) | Dissolving and adding system for permanganate composite medicament | |
| CN205412792U (en) | Thick liquids agitator tank | |
| CN201644051U (en) | Automatic agent feeding system for slime water | |
| CN209378867U (en) | A kind of new and effective blender | |
| CN108236860A (en) | A kind of automatically cleaning vertical mixer | |
| CN107953454A (en) | A kind of concrete mixer | |
| CN218573485U (en) | Water-soluble fertilizer diluting equipment | |
| CN204208501U (en) | The anti-blocking solid-liquid mixer of a kind of high efficiency | |
| CN208005964U (en) | Mortar stock stirring device | |
| CN207105262U (en) | Visual device in a kind of mixer production process | |
| CN202497851U (en) | High-speed stirring system with moving function | |
| CN107790010A (en) | A kind of medicine production agitating device | |
| CN206381996U (en) | A kind of hydrogenation reaction cauldron | |
| CN203355669U (en) | Stirrer with rotatable nozzle | |
| CN211051351U (en) | Stirrer for preparing sulfadoxine sodium salt | |
| CN209302626U (en) | A kind of multilayer guide flow tube stirrer for sewage treatment mixing dosing pond | |
| CN103357337B (en) | Mixer with rotatable nozzle | |
| CN203710928U (en) | High-speed mixing equipment for chemical agents | |
| CN209968297U (en) | Strong stirring tank device | |
| CN208097948U (en) | It can produce the Water-borne Coatings Emulsion production mixing tank of irregular mixing effect | |
| CN207221770U (en) | A kind of modified form chemicals dosing plant | |
| CN103357338B (en) | Electric mixer | |
| CN208594213U (en) | Suspension organic water-soluble fertilizer is concentrated with three-dimensional chelatropic reaction device | |
| CN207387995U (en) | A kind of regeneration mixed mud production agitating device | |
| CN205925498U (en) | Solid -liquid gas mixing stirring device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121205 |