CN207970867U - Catalyst spherical carrier molding machine - Google Patents
Catalyst spherical carrier molding machine Download PDFInfo
- Publication number
- CN207970867U CN207970867U CN201820200117.8U CN201820200117U CN207970867U CN 207970867 U CN207970867 U CN 207970867U CN 201820200117 U CN201820200117 U CN 201820200117U CN 207970867 U CN207970867 U CN 207970867U
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- China
- Prior art keywords
- drying chamber
- hose
- spherical carrier
- sewage draining
- draining exit
- 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
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- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Catalysts (AREA)
Abstract
The utility model belongs to catalyst spherical carrier former field, and in particular to a kind of catalyst spherical carrier molding machine, including drop ball device, it is characterised in that：It drips and shaping column is set below ball device, drying chamber is set below shaping column, drying chamber connects compensator with charging pump by hose, and compensator passes through hose and gate valve and shaping column unicom.The utility model is mainly used for the production of colloidal sol balling-up catalyst carrier, and equipment forms closed loop cycle, good seal, no liquid or gas leakage in production process, and environment protecting is good, and production efficiency is high, and product sphericity is high, and spoilage is small.
Description
Technical field
The utility model belongs to catalyst spherical carrier former field, and in particular to a kind of catalyst spherical carrier at
Type device.
Background technology
Currently, chemical industry catalyst spherical carrier gradually starts to prepare using the preparation method of gel micro-ball, gel
The preparation method of microballoon mainly has ultrasonic method, mechanical mixing method, membrane emulsification and injection condensing method etc..Ultrasonic method and mechanical agitation
Method treating capacity is small, it is difficult to for mass producing；Membrane emulsification is difficult to control the more demanding of equipment, operating condition；And it sprays
Condensation method is penetrated although the uniformity of grain size cannot be controlled, operation is relatively easy, can scale amplification, therefore be suitable for industrializing
Using.The equipment that injection condensing method prepares gel micro-ball at present is primarily present poorly sealed, liquid or gas leakage, pollution ring
The problems such as border, spherical shape is fragile, inefficiency.
Utility model content
In view of the above problems, the purpose of this utility model is to provide, a kind of environmental protection, production efficiency is high, product sphericity is high
Catalyst spherical carrier molding machine.
To achieve the above object, the technical solution adopted in the utility model is：Catalyst spherical carrier molding machine, including
Ball device is dripped, shaping column is set below drop ball device, drying chamber is set below shaping column, drying chamber is connected by hose and charging pump
Compensator is connect, compensator is connected to by hose and gate valve with shaping column.Production equipment forms closed loop cycle, good seal, aneroid
Body or gas leakage, environment protecting are good.
It is connected using first flange between the shaping column and drying chamber.
Setting support net inside the drying chamber, asks side off the net that drier coil is arranged, and idler wheel is arranged in bottom；Drying chamber one
Sewage draining exit is arranged close to the position of bottom in side, and sewage draining exit connects ball valve；The first discharge port is arranged in the offside of sewage draining exit, and first goes out
Material mouth level height is higher than sewage draining exit, is connected using second flange between the first discharge port and hose.
In the course of work, catalyst spherical carrier is collected into support on the net, opens the flange on drying chamber, removes drying chamber,
Power supply is connected, drier coil heat drying catalyst spherical carrier is utilized.Catalyst spherical carrier is in static shape during being somebody's turn to do
State, sphericity is complete, is hardly damaged.Multiple drying chamber rotations use, and improve production efficiency.
The charging pump is one kind in diaphragm pump, slush pump, plunger pump, water pump.
Sewage draining exit is arranged in the balance pot bottom, and sewage draining exit connects ball valve；Feed inlet is arranged in side surface upper part, and feed inlet is logical
Hose connection charging pump is crossed, the second discharge port is arranged in side lower, and the second discharge port connects shaping column by hose with gate valve.
Solidify liquid is filled in compensator, charging pump, compensator, shaping column are connected to drying chamber, realize solidify liquid
It recycles, it is cost-effective；The setting of sewage draining exit facilitates the discharge of sediment in solidify liquid.
Compared with prior art, the utility model has the advantages that：
The utility model is used using multiple drying chamber rotations, significantly improves production efficiency, and the sealing of equipment whole process is acyclic
Border is polluted, and solidify liquid recycles, cost-effective, and drying chamber cooperation support net uses, and product sphericity is intact, and spoilage is low.
Description of the drawings
Fig. 1, catalyst spherical carrier forming device structure schematic diagram；
In figure, 1, drop ball device, 2, shaping column, 3, first flange, 4, drying chamber, 5, support net, 6, drier coil, 7, rolling
Wheel, 8, second flange, 9, charging pump, 10, compensator, 11, gate valve, the 12, first discharge port, 13, feed inlet, the 14, second discharging
Mouthful.
Specific implementation mode
The utility model is described further with reference to specific embodiment.
Embodiment 1
As shown in Figure 1, alumina sol catalyst spherical carrier is prepared, the technical solution that embodiment uses：Catalyst spheres
Shaping column 2 is arranged in shape carrier molding machine, including drop ball device 1,1 lower section of drop ball device, and drying chamber 4 is arranged in 2 lower section of shaping column,
Drying chamber 4 connects compensator 10 by hose and charging pump 9, and compensator 10 is connected to by hose and gate valve 11 with shaping column 2.It is raw
It produces equipment and forms closed loop cycle, good seal, no liquid or gas leakage, environment protecting are good.
It is connected using first flange 3 between the shaping column 2 and drying chamber 4.
Drier coil 6 is arranged in the 4 inside setting support net 5 of drying chamber, 5 lower section of support net, and idler wheel 7 is arranged in bottom；It is dry
Sewage draining exit is arranged close to the position of bottom in 4 side of tank, and sewage draining exit connects ball valve；The first discharge port 12 is arranged in the offside of sewage draining exit,
First discharge port, 12 level height is higher than sewage draining exit, is connected using second flange 8 between the first discharge port 12 and hose.
In the course of work, catalyst spherical carrier is collected on support net 5, is opened the flange on drying chamber 4, is removed drying chamber
4, power supply is connected, 6 heat drying catalyst spherical carrier of drier coil is utilized.Catalyst spherical carrier is in static during being somebody's turn to do
State, sphericity is complete, is hardly damaged；Four 4 rotations of drying chamber use, and improve production efficiency.
The charging pump 9 is diaphragm pump.
Sewage draining exit is arranged in 10 bottom of compensator, and sewage draining exit connects ball valve；Feed inlet 13, charging is arranged in side surface upper part
Mouth 13 connects charging pump 9 by hose, and the second discharge port 14 is arranged in side lower, and the second discharge port 14 passes through hose and gate valve 11
Connect shaping column 2.
The acid solidify liquid of filling, charging pump 9, compensator 10, shaping column 2 are connected to drying chamber 4 four in compensator 10, real
Recycling for existing acidity solidify liquid, it is cost-effective；The setting of sewage draining exit facilitates the discharge of sediment in acid solidify liquid.
The present embodiment is used using four 4 rotations of drying chamber, significantly improves production efficiency, and the sealing of equipment whole process is acyclic
Border is polluted, and acid solidify liquid recycles, cost-effective, and the cooperation support net 5 of drying chamber 4 uses, and product sphericity is intact, spoilage
It is low.
Embodiment 2
As shown in Figure 1, silica sol catalyst spherical carrier is prepared, the technical solution that embodiment uses：Catalyst spheres
Shaping column 2 is arranged in shape carrier molding machine, including drop ball device 1,1 lower section of drop ball device, and drying chamber 4 is arranged in 2 lower section of shaping column,
Drying chamber 4 connects compensator 10 by hose and charging pump 9, and compensator 10 is connected to by hose and gate valve 11 with shaping column 2.It is raw
It produces equipment and forms closed loop cycle, good seal, no liquid or gas leakage, environment protecting are good.
It is connected using first flange 3 between the shaping column 2 and drying chamber 4.
Drier coil 6 is arranged in the 4 inside setting support net 5 of drying chamber, 5 lower section of support net, and idler wheel 7 is arranged in bottom；It is dry
Sewage draining exit is arranged close to the position of bottom in 4 side of tank, and sewage draining exit connects ball valve；The first discharge port 12 is arranged in the offside of sewage draining exit,
First discharge port, 12 level height is higher than sewage draining exit, is connected using second flange 8 between the first discharge port 12 and hose.
In the course of work, catalyst spherical carrier is collected on support net 5, is opened the flange on drying chamber 4, is removed drying chamber
4, power supply is connected, 6 heat drying catalyst spherical carrier of drier coil is utilized.Catalyst spherical carrier is in static during being somebody's turn to do
State, sphericity is complete, is hardly damaged；Three 4 rotations of drying chamber use, and improve production efficiency.
The charging pump 9 is plunger pump.
Sewage draining exit is arranged in 10 bottom of compensator, and sewage draining exit connects ball valve；Feed inlet 13, charging is arranged in side surface upper part
Mouth 13 connects charging pump 9 by hose, and the second discharge port 14 is arranged in side lower, and the second discharge port 14 passes through hose and gate valve 11
Connect shaping column 2.
The alkaline-curing liquid of filling, charging pump 9, compensator 10, shaping column 2 are connected to drying chamber 4 four in compensator 10, real
Recycling for existing alkaline-curing liquid, it is cost-effective；The setting of sewage draining exit facilitates the discharge of sediment in alkaline-curing liquid.
The present embodiment is used using three 4 rotations of drying chamber, significantly improves production efficiency, and the sealing of equipment whole process is acyclic
Border is polluted, and alkaline-curing liquid recycles, cost-effective, and the cooperation support net 5 of drying chamber 4 uses, and product sphericity is intact, spoilage
It is low.
Claims (5)
1. catalyst spherical carrier molding machine, including drop ball device (1), it is characterised in that：It is arranged to below drop ball device (1)
Type column (2), shaping column (2) lower section setting drying chamber (4), drying chamber (4) passes through hose and charging pump (9) connects compensator
(10), compensator (10) is connected to by hose and gate valve (11) with shaping column (2).
2. catalyst spherical carrier molding machine according to claim 1, it is characterised in that：The shaping column (2) and
It is connected using first flange (3) between drying chamber (4).
3. catalyst spherical carrier molding machine according to claim 1, it is characterised in that：In the drying chamber (4)
Idler wheel (7) is arranged in portion's setting support net (5), support net (5) lower section setting drier coil (6), bottom；Drying chamber (4) side, the bottom of close to
Sewage draining exit is arranged in the position in portion, and sewage draining exit connects ball valve；The first discharge port (12), the first discharge port is arranged in the offside of sewage draining exit
(12) level height is higher than sewage draining exit, and the first discharge port (12) is connect between hose using second flange (8).
4. catalyst spherical carrier molding machine according to claim 1, it is characterised in that：The charging pump (9) is
One kind in diaphragm pump, slush pump, plunger pump, water pump.
5. catalyst spherical carrier molding machine according to claim 1, it is characterised in that：Described compensator (10) bottom
Sewage draining exit is arranged in portion, and sewage draining exit connects ball valve；Feed inlet (13) is arranged in side surface upper part, and feed inlet (13) is connected by hose and is fed
It pumps (9), the second discharge port (14) is arranged in side lower, and the second discharge port (14) connects shaping column by hose and gate valve (11)
(2)。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820200117.8U CN207970867U (en) | 2018-02-05 | 2018-02-05 | Catalyst spherical carrier molding machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820200117.8U CN207970867U (en) | 2018-02-05 | 2018-02-05 | Catalyst spherical carrier molding machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207970867U true CN207970867U (en) | 2018-10-16 |
Family
ID=63766939
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820200117.8U Expired - Fee Related CN207970867U (en) | 2018-02-05 | 2018-02-05 | Catalyst spherical carrier molding machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207970867U (en) |
-
2018
- 2018-02-05 CN CN201820200117.8U patent/CN207970867U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 255000 Shandong Zibo high tech Zone, Guzhen, Fu Shan village. Co-patentee after: SHANGHAI QIRUN CHEMICAL Co.,Ltd. Patentee after: Shandong qirunyuan New Material Technology Co.,Ltd. Address before: 255000 Shandong Zibo high tech Zone, Guzhen, Fu Shan village. Co-patentee before: SHANGHAI QIRUN CHEMICAL Co.,Ltd. Patentee before: ZIBO RUNYUAN CHEMICAL Co.,Ltd. |
|
| 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: 20181016 Termination date: 20220205 |