CN107413259A - A kind of coating stirred tank and its application method - Google Patents
A kind of coating stirred tank and its application method Download PDFInfo
- Publication number
- CN107413259A CN107413259A CN201710619164.6A CN201710619164A CN107413259A CN 107413259 A CN107413259 A CN 107413259A CN 201710619164 A CN201710619164 A CN 201710619164A CN 107413259 A CN107413259 A CN 107413259A
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- Prior art keywords
- kettle body
- coating
- thermal medium
- raw material
- kettle
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F29/00—Mixers with rotating receptacles
- B01F29/60—Mixers with rotating receptacles rotating about a horizontal or inclined axis, e.g. drum mixers
- B01F29/64—Mixers with rotating receptacles rotating about a horizontal or inclined axis, e.g. drum mixers with stirring devices moving in relation to the receptacle, e.g. rotating
-
- 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
-
- 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
- B01F35/92—Heating or cooling systems for heating the outside of the receptacle, e.g. heated jackets or burners
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/0066—Stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/28—Moving reactors, e.g. rotary drums
-
- 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
- B01F2035/99—Heating
-
- 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
- B01F2101/30—Mixing paints or paint ingredients, e.g. pigments, dyes, colours, lacquers or enamel
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00094—Jackets
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Accessories For Mixers (AREA)
Abstract
The invention discloses a kind of coating stirred tank, including bottom plate, riser, kettle body, motor, power transmission shaft, puddler and temperature inductor, it is characterised in that：Described riser is vertically set on bottom plate, connecting shaft, feed pipe, discharge nozzle, thermal medium inlet pipe, thermal medium exit tube, thermometer, blast pipe are provided with described kettle body, described motor is arranged on kettle body, described power transmission shaft is arranged in kettle body, described puddler is arranged between connecting plate and connecting plate, and described temperature inductor is arranged in kettle inner body wall.The present invention is provided with interlayer in kettle body, and by interlayer and thermal medium inlet pipe, thermal medium exit tube, can be according to temperature adjustment thermal medium inlet pipe, the thermal medium flow velocity of thermal medium exit tube in coating raw material production process, the intrinsic temperature of kettle is maintained near coating raw material reaction preference temperature, the reaction rate of coating raw material can be promoted.
Description
Technical field
The present invention relates to coating material production technical field, is specifically related to a kind of vertical coating stirred tank and its application method.
Background technology
During coating processing, temperature is one of an important factor for coating raw material reacts, and it, which is directly affected, applies
Expect the reaction rate between raw material, also affect the utilization ratio of coating raw material indirectly, therefore more in the reaction of coating material production
Temperature adjustment function is provided with kettle, such as a kind of coating High Efficiency Energy-Saved Stirring of patent disclosure of Application No. 201621401547.3
Kettle, the problem of stirring scope is small, mixing effect is bad is which solved, but there is the temperature that can not be adjusted in real time in reactor
Degree, the deficiency that coating raw material stirring is insufficient, coating raw material waste is more.
The content of the invention
The purpose of the present invention is to overcome existing coating material production to adjust the temperature in reactor in real time existing for stirred tank
Degree, the insufficient, coating raw material of coating raw material stirring waste the problem of more, there is provided it is a kind of it is reasonable in design, can be according to painting
The response situation of material raw material adjusts temperature in reactor in real time, coating raw material fully reacts, reduces coating raw material waste
Coating stirred tank and its application method with temperature adjustment function.
Present invention solves the technical problem that the technical scheme taken is：
A kind of coating stirred tank, including bottom plate, riser, kettle body, motor, power transmission shaft, puddler and temperature inductor, its feature
It is：Described riser is vertically set on bottom plate, and axle sleeve is provided with riser, and connection is provided with described kettle body
Axle, feed pipe, discharge nozzle, thermal medium inlet pipe, thermal medium exit tube, thermometer, blast pipe, and connecting shaft is arranged in axle sleeve,
Described motor is arranged on kettle body, and power line is provided with motor, and described power transmission shaft is arranged in kettle body, will
Power transmission shaft one end and motor connection, and connecting plate is provided with power transmission shaft, described puddler is arranged on connecting plate with being connected
Between plate, described temperature inductor is arranged in kettle inner body wall, and temperature inductor is connected with thermometer, in kettle body
It is provided with interlayer, and by interlayer and thermal medium inlet pipe, thermal medium exit tube, can be adjusted according to the temperature in coating raw material production process
Thermal medium inlet pipe, the thermal medium flow velocity of thermal medium exit tube are saved, the intrinsic temperature of kettle is maintained the suitable temperature of coating raw material reaction
Near degree, the reaction rate of coating raw material can be promoted, improve the utilization ratio of coating raw material, kettle body is passed through into connecting shaft
The structure that can be rotated between riser and riser is arranged to, rotating kettle body while enabling the coating be stirred in kettle body,
The intrinsic coating raw material of kettle is sufficiently stirred, improves the mixing quality of coating, connecting plate is provided with power transmission shaft, and even
Puddler is provided between fishplate bar and connecting plate, the puddler of suitable construction is selected according to different coating raw materials, can be to kettle
Intrinsic coating is sufficiently stirred, and not only improves the mixing quality of coating raw material, can also expand the scope of application of vertical stirred tank,
Reduce the cost of the more set vertical stirred tanks of manufacture.
Interlayer is provided with described kettle body, and interlayer is connected with thermal medium inlet pipe, thermal medium exit tube, being capable of basis
Temperature adjustment thermal medium inlet pipe, the thermal medium flow velocity of thermal medium exit tube in coating raw material production process, make the intrinsic temperature of kettle
Degree is maintained near coating raw material reaction preference temperature, can be promoted the reaction rate of coating raw material, be improved coating raw material
Utilization ratio.
Described puddler is arranged to any one structure in arc, circle, V-arrangement, U-shaped or S-shaped, according to different paintings
Expect the puddler of raw material selection suitable construction, the intrinsic coating of kettle can be sufficiently stirred, not only improve stirring for coating raw material
Quality is mixed, can also expand the scope of application of vertical stirred tank, reduces the cost of the more set vertical stirred tanks of manufacture.
Described discharge nozzle, thermal medium inlet pipe, thermal medium exit tube, valve is provided with blast pipe, can by valve
The flow velocity of the coating raw material after thermal medium and stirring is controlled, improves operating efficiency.
Described application method comprises the following steps：
First：Check coating stirred tank circuit, pipeline it is whether normal, motor, power transmission shaft whether can normal work, puddler
It is whether intact；
Second：The coating raw material preference temperature produced as needed, selects suitable thermal medium, and thermal medium is entered by thermal medium
Pipe is inputted to the interlayer of kettle body, and thermometer is reflected in carrying out temperature adjustment in kettle body, and by the intrinsic real time temperature of kettle
On, the valve on closing discharge nozzle, the raw material of coating is added in kettle body by feed pipe；
3rd：The power line of motor is connected with external power source, starts motor, the rotation of motor driven power transmission shaft, power transmission shaft drives
Puddler rotation between connecting plate and connecting plate and connecting plate, is stirred to the intrinsic coating raw material of kettle；
4th：In coating raw material production process, the temperature value that is shown according to thermometer, adjusts thermal medium inlet pipe or thermal medium goes out
The thermal medium flow velocity of pipe, make the intrinsic temperature of kettle in the range of ± 0.5 DEG C of industrial chemicals preference temperature
5th：After coating raw material production terminates, motor is closed, opens the valve on discharge nozzle, the coating after production is discharged into kettle
Body, the medium in discharge kettle this interlayer body, the coating of residual, cuts off the electricity supply in cleaning kettle body.
Beneficial effect：The present invention is provided with interlayer in kettle body, and by interlayer and thermal medium inlet pipe, thermal medium exit tube, energy
Enough temperature adjustment thermal medium inlet pipe, thermal medium flow velocitys of thermal medium exit tube in coating raw material production process, make kettle body
Interior temperature is maintained near coating raw material reaction preference temperature, can be promoted the reaction rate of coating raw material, be improved coating
The utilization ratio of raw material, the structure that kettle body is arranged to rotate between riser and riser by connecting shaft, makes coating exist
While stirring in kettle body can rotating kettle body, be sufficiently stirred the intrinsic coating raw material of kettle, improve the stirring of coating
Quality, connecting plate is provided with power transmission shaft, and puddler is provided between connecting plate and connecting plate, according to different coating
Raw material selects the puddler of suitable construction, and the intrinsic coating of kettle can be sufficiently stirred, and not only improves the stirring of coating raw material
It quality, can also expand the scope of application of vertical stirred tank, reduce the cost of the more set vertical stirred tanks of manufacture.
Brief description of the drawings
Fig. 1 is the structural representation of the present invention.
In figure：1. bottom plate, 2. risers, 3. kettle bodies, 4. motors, 5. power transmission shafts, 6. puddlers, 7. temperature inductors, 8.
Axle sleeve, 9. connecting shafts, 10. feed pipes, 11. discharge nozzles, 12. thermal medium inlet pipes, 13. thermal medium exit tubes, 14. thermometers, 15. rows
Tracheae, 16. valves, 17. interlayers, 18. power lines, 19. connecting plates, 20. air gauges, 21. bracing pieces, 22. bosses.
Embodiment
The present invention is described in detail below with reference to accompanying drawing.
Embodiment 1：
As shown in Figure 1, a kind of coating stirred tank, including bottom plate 1, riser 2, kettle body 3, motor 4, power transmission shaft 5, puddler 6
With temperature inductor 7, it is characterised in that：Described riser 2 is vertically set on bottom plate 1, and axle sleeve 8 is provided with riser 2,
Connecting shaft 9, feed pipe 10, discharge nozzle 11, thermal medium inlet pipe 12, thermal medium exit tube 13, temperature are provided with described kettle body 3
Meter 14, blast pipe 15, and connecting shaft 9 is arranged in axle sleeve 8, described motor 4 is arranged on kettle body 3, and on motor 4
Power line 18 is provided with, described power transmission shaft 5 is arranged in kettle body 3, and the one end of power transmission shaft 5 is connected with motor 4, and is being driven
Connecting plate 19 is provided with axle 5, described puddler 6 is arranged between connecting plate 19 and connecting plate 19, described temperature sense
Device 7 is arranged on the inwall of kettle body 3, and temperature inductor 7 is connected with thermometer 14, and kettle body 3 is provided with interlayer 17, and
By interlayer 17 and thermal medium inlet pipe 12, thermal medium exit tube 13, can be situated between according to the temperature adjustment heat in coating raw material production process
The thermal medium flow velocity of matter inlet pipe 12, thermal medium exit tube 13, the temperature in kettle body 3 is set to maintain coating raw material reaction preference temperature
Near, the reaction rate of coating raw material can be promoted, the utilization ratio of coating raw material is improved, kettle body 3 is passed through into connecting shaft 9
The structure that can be rotated between riser 2 and riser 2 is arranged to, enables coating rotating kettle sheet while the interior stirring of kettle body 3
Body 3, the coating raw material being sufficiently stirred in kettle body 3, the mixing quality of coating is improved, connecting plate is provided with power transmission shaft 5
19, and puddler 6 is provided between connecting plate 19 and connecting plate 19, stirring for suitable construction is selected according to different coating raw materials
Bar 6 is mixed, the coating in kettle body 3 can be sufficiently stirred, the mixing quality of coating raw material is not only improved, can also expand vertical stir
The scope of application of kettle is mixed, reduces the cost of the more set vertical stirred tanks of manufacture.
The structure that described kettle body 3 is arranged to rotate between riser 2 and riser 2 by connecting shaft 9, makes coating exist
While stirring in kettle body 3 can rotating kettle body 3, the coating raw material being sufficiently stirred in kettle body 3, improve stirring for coating
Mix quality.
Interlayer 17 is provided with described kettle body 3, and interlayer 17 and thermal medium inlet pipe 12, thermal medium exit tube 13 are connected
Connect, can according to temperature adjustment thermal medium inlet pipe 12, the thermal medium flow velocity of thermal medium exit tube 13 in coating raw material production process,
The temperature in kettle body 3 is maintained near coating raw material reaction preference temperature, the reaction rate of coating raw material can be promoted,
Improve the utilization ratio of coating raw material.
Described puddler 6 is arranged to S-shaped structure, and the puddler 6 of suitable construction, energy are selected according to different coating raw materials
It is enough that coating in kettle body 3 is sufficiently stirred, the mixing quality of coating raw material is not only improved, can also expand the suitable of vertical stirred tank
With scope, reduce the manufacture costs for covering vertical stirred tanks more.
Described discharge nozzle 11, thermal medium inlet pipe 12, thermal medium exit tube 13, valve 16 is provided with blast pipe 15, lead to
The flow velocity of the coating raw material after thermal medium and stirring can be controlled by crossing valve 16, improve operating efficiency.
Air gauge 20 is provided with described blast pipe 15, the pressure feelings in kettle body 3 can be shown by air gauge 20
Condition, improve security.
Be provided with bracing piece 21 between described riser 2 and bottom plate 1, by bracing piece 21 improve riser 2 and bottom plate 1 it
Between bonding strength, improve stability of the coating raw material in whipping process.
Be provided with boss 22 between described kettle body 3 and connecting shaft 9, by boss 22 improve kettle body 3 with
Bonding strength between connecting shaft 9, and then improve stability of the kettle body 3 in rotary course.
Described application method comprises the following steps：
First：Check coating stirred tank circuit, pipeline it is whether normal, motor 4, power transmission shaft 5 whether can normal work, stirring
Whether bar 6 is intact；
Second：The coating raw material preference temperature produced as needed, selects suitable thermal medium, and thermal medium is entered by thermal medium
Pipe 12 is inputted to the interlayer 17 of kettle body 3, to carrying out temperature adjustment in kettle body 3, and the real time temperature in kettle body 3 is reflected in
On thermometer 14, the valve 16 on closing discharge nozzle 11, the raw material of coating is added in kettle body 3 by feed pipe 10；
3rd：The power line 18 of motor 4 is connected with external power source, starts motor 4, motor 4 drives power transmission shaft 5 to rotate, and is driven
Axle 5 drives the puddler 6 between connecting plate 19 and connecting plate 19 and connecting plate 19 to rotate, and the coating raw material in kettle body 3 is entered
Row stirring；
4th：In coating raw material production process, according to the temperature value of the display of thermometer 14, regulation thermal medium inlet pipe 12 or heat are situated between
The thermal medium flow velocity of matter outlet pipe 13, make the temperature in kettle body 3 in the range of ± 0.5 DEG C of industrial chemicals preference temperature；
5th：After coating raw material production terminates, motor 4 is closed, opens the valve 16 on discharge nozzle 10, the coating after production is arranged
Go out kettle body 3, discharge the medium in the interlayer 17 of kettle body 3, the coating remained in cleaning kettle body 3, cut off the electricity supply.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all essences in the present invention
All any modification, equivalent and improvement made within refreshing and principle etc., should be included in the scope of the protection.
Part that the present invention does not relate to is same as the prior art or can be realized using prior art.
Claims (9)
1. a kind of coating stirred tank, including bottom plate, riser, kettle body, motor, power transmission shaft, puddler and temperature inductor, it is special
Sign is：Described riser is vertically set on bottom plate, and axle sleeve is provided with riser, the company of being provided with described kettle body
Spindle, feed pipe, discharge nozzle, thermal medium inlet pipe, thermal medium exit tube, thermometer, blast pipe, and connecting shaft is arranged on axle sleeve
Interior, described motor is arranged on kettle body, and power line is provided with motor, and described power transmission shaft is arranged on kettle body
It is interior, by power transmission shaft one end and motor connection, and connecting plate is provided with power transmission shaft, described puddler be arranged on connecting plate with
Between connecting plate, described temperature inductor is arranged in kettle inner body wall, and temperature inductor is connected with thermometer, in kettle
Body is provided with interlayer, the structure that kettle body is arranged to rotate between riser and riser by connecting shaft, coating is existed
While stirring in kettle body can rotating kettle body, be provided with connecting plate on power transmission shaft, and connecting plate and connecting plate it
Between be provided with puddler.
A kind of 2. coating stirred tank according to claim 1, it is characterised in that：Described kettle body is set by connecting shaft
For the structure that can be rotated between riser and riser.
A kind of 3. coating stirred tank according to claim 1, it is characterised in that：Interlayer is provided with described kettle body,
And interlayer is connected with thermal medium inlet pipe, thermal medium exit tube.
A kind of 4. coating stirred tank according to claim 1, it is characterised in that：Described puddler is arranged to S-shaped structure.
A kind of 5. coating stirred tank according to claim 1, it is characterised in that：Described discharge nozzle, thermal medium inlet pipe, heat
Valve is provided with medium outlet pipe, blast pipe.
A kind of 6. coating stirred tank according to claim 1, it is characterised in that：Air pressure is provided with described blast pipe
Table.
A kind of 7. coating stirred tank according to claim 1, it is characterised in that：It is provided between described riser and bottom plate
Bracing piece.
A kind of 8. coating stirred tank according to claim 1, it is characterised in that：Set between described kettle body and connecting shaft
It is equipped with boss.
9. a kind of be applied to a kind of operating method of coating stirred tank as claimed in claim 1, it is characterised in that：Described behaviour
Comprise the following steps as method：
First：Check coating stirred tank circuit, pipeline it is whether normal, motor, power transmission shaft whether can normal work, puddler
It is whether intact；
Second：The coating raw material preference temperature produced as needed, selects suitable thermal medium, and thermal medium is entered by thermal medium
Pipe is inputted to the interlayer of kettle body, and thermometer is reflected in carrying out temperature adjustment in kettle body, and by the intrinsic real time temperature of kettle
On, the valve on closing discharge nozzle, the raw material of coating is added in kettle body by feed pipe；
3rd：The power line of motor is connected with external power source, starts motor, the rotation of motor driven power transmission shaft, power transmission shaft drives
Puddler rotation between connecting plate and connecting plate and connecting plate, is stirred to the intrinsic coating raw material of kettle；
4th：In coating raw material production process, the temperature value that is shown according to thermometer, adjusts thermal medium inlet pipe or thermal medium goes out
The thermal medium flow velocity of pipe, make the intrinsic temperature of kettle in the range of ± 0.5 DEG C of industrial chemicals preference temperature；
5th：After coating raw material production terminates, motor is closed, opens the valve on discharge nozzle, the coating after production is discharged into kettle
Body, the medium in discharge kettle this interlayer body, the coating of residual, cuts off the electricity supply in cleaning kettle body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710619164.6A CN107413259A (en) | 2017-07-26 | 2017-07-26 | A kind of coating stirred tank and its application method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710619164.6A CN107413259A (en) | 2017-07-26 | 2017-07-26 | A kind of coating stirred tank and its application method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107413259A true CN107413259A (en) | 2017-12-01 |
Family
ID=60431276
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710619164.6A Withdrawn CN107413259A (en) | 2017-07-26 | 2017-07-26 | A kind of coating stirred tank and its application method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107413259A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108607447A (en) * | 2018-05-02 | 2018-10-02 | 李赵和 | A kind of printing and dyeing dye stirring device |
| CN108927099A (en) * | 2018-08-01 | 2018-12-04 | 芜湖市三山龙城新材料有限公司 | Reaction kettle suitable for paint process |
| CN108940178A (en) * | 2018-08-01 | 2018-12-07 | 芜湖市三山龙城新材料有限公司 | A kind of paint production reaction kettle |
| CN108940054A (en) * | 2018-08-14 | 2018-12-07 | 周兆平 | Dispersal device suitable for coating processing |
| CN108940055A (en) * | 2018-08-14 | 2018-12-07 | 周兆平 | A kind of dispersing apparatus of coating material production |
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| CN104801222A (en) * | 2014-01-26 | 2015-07-29 | 钱勇 | Intermediate bulk container blender |
| CN205731251U (en) * | 2016-06-25 | 2016-11-30 | 余林岚 | A kind of chemical reaction kettle for anaerobic adhesive processing |
| CN106311120A (en) * | 2016-10-09 | 2017-01-11 | 芜湖瑞德机械科技有限公司 | Reaction kettle for chemical production with temperature adjustment function and operating method of reaction kettle |
| CN106807289A (en) * | 2017-03-27 | 2017-06-09 | 王爽 | A kind of lithium ion cell positive homogenate equipment |
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2017
- 2017-07-26 CN CN201710619164.6A patent/CN107413259A/en not_active Withdrawn
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104801222A (en) * | 2014-01-26 | 2015-07-29 | 钱勇 | Intermediate bulk container blender |
| CN205731251U (en) * | 2016-06-25 | 2016-11-30 | 余林岚 | A kind of chemical reaction kettle for anaerobic adhesive processing |
| CN106311120A (en) * | 2016-10-09 | 2017-01-11 | 芜湖瑞德机械科技有限公司 | Reaction kettle for chemical production with temperature adjustment function and operating method of reaction kettle |
| CN106807289A (en) * | 2017-03-27 | 2017-06-09 | 王爽 | A kind of lithium ion cell positive homogenate equipment |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108607447A (en) * | 2018-05-02 | 2018-10-02 | 李赵和 | A kind of printing and dyeing dye stirring device |
| CN108927099A (en) * | 2018-08-01 | 2018-12-04 | 芜湖市三山龙城新材料有限公司 | Reaction kettle suitable for paint process |
| CN108940178A (en) * | 2018-08-01 | 2018-12-07 | 芜湖市三山龙城新材料有限公司 | A kind of paint production reaction kettle |
| CN108940054A (en) * | 2018-08-14 | 2018-12-07 | 周兆平 | Dispersal device suitable for coating processing |
| CN108940055A (en) * | 2018-08-14 | 2018-12-07 | 周兆平 | A kind of dispersing apparatus of coating material production |
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