Calcium carbonate dries activation integral device
Technical field
The utility model relates to a kind of production equipment of activated Calcium carbonate, specifically a kind of dry activation one of calcium carbonate
Body device.
Background technique
Activated Calcium carbonate is a kind of high-grade filler with high filler loading capacity, and loading is 2 ~ 5 times of ordinary calcium carbonate,
And it is strong with the intermolecular affinity of rubber, plastics, oil factor is low, whiteness is high, ductility is high, thus be widely used in rubber,
Plastics, plastic-steel door and window, PVC cable material, high grade paint, tubing, tire, sole, polyvinyl blow molding, sealing joint strip, glass steel
The industries such as product, cable packaging cloth, papermaking, building materials, ink, daily-use chemical industry, weaving, feed, food additives.
Currently, the production of domestic activated Calcium carbonate is usually to be heated to the calcium carbonate serosity that carbonization is completed in activation equipment
Activator is added in required activation temperature (80 ~ 90 DEG C), and calcium carbonate serosity and activator stir in activation equipment by High Temperature And Velocity
Mix generation activated Calcium carbonate.The production method energy consumption is big, complicated for operation, production process is discontinuous, at high cost.
Utility model content
The purpose of this utility model is just to provide a kind of dry activation integral device of calcium carbonate, living to solve existing calcium carbonate
Change Process Energy and consumes problem big, complicated for operation, at high cost.
The utility model is realized in this way:
A kind of dry activation integral device of calcium carbonate, is atomized including drying machine, the activator being arranged in the drying machine
Device, the storage tank to store activator, the activator delivery pipe that is connected between the storage tank and the activator atomizer with
And the conveying metering pump in the activator delivery pipe is set;The activator atomizer includes that several branch pipes and setting are being propped up
Several atomizers on pipe, the branch pipe are connected to the activator delivery pipe, and the inlet of the atomizer passes through company
Adapter tube is connected to branch pipe.
The drying machine is double blades drying machine, and the activator atomizer is arranged by mounting rack in double blades drying machine
Casing top cover on, and be located at drying machine body dryer section top.
The mounting rack is the rectangular frame being welded by several cross bars and several vertical hack levers, and branch pipe setting is being installed
On the hack lever of frame.
The drying machine is tray drier, and the activator atomizer is arranged in tray drier body middle and upper part
Basin try to get to the heart of a matter on face.
The branch pipe includes allotment pipe and ring pipe, and one end of each allotment pipe converges at one, is provided at the convergence
Distribution plate, distribution plate are connected with the end of activator delivery pipe, and the other end of each allotment pipe is connected to ring pipe respectively, atomization spray
Head is evenly arranged on ring pipe.
The utility model by activated Calcium carbonate production process activation procedure with drying process is ingenious is combined together, energy
The problem of enough efficiently solving calcium carbonate serosity activation energy consumption height, Batch Process, low efficiency, complex process, realizes production
Serialization, significantly reduces production energy consumption at energy-saving, simplifies activating process, has saved activating cost.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of integrated device described in embodiment 1.
Fig. 2 is the structural schematic diagram of activator atomizer described in embodiment 1.
Fig. 3 is the structural schematic diagram of integrated device described in embodiment 2.
Fig. 4 is the structural schematic diagram of activator atomizer described in embodiment 2.
In figure: 1, drying machine, 2, activator atomizer, 3, storage tank, 4, conveying metering pump, 5, activator delivery pipe, 6, machine
Shell, 7, live spindle, 8, feed inlet, 9, discharge port, 10, moisture exhausting port, 11, mounting rack, 12, branch pipe, 13, connecting tube, 14, mist
Change spray head, 15, basin, 16, distribution plate, 17, allotment pipe, 18, ring pipe.
Specific embodiment
Embodiment 1
As shown in Figure 1 and 2, the utility model include double blades drying machine 1, the activator atomizer 2 being arranged at the top of it,
Activator storage tank 3, conveying metering pump 4 and activator delivery pipe 5.
Double blades drying machine 1 includes pedestal, the casing 6 being set on the base, two rotations being disposed side by side on inside casing 6
Several blades and the driver for turning main shaft 7, being arranged in live spindle 7.Charging is equipped in the upper body of 6 one end of casing
Mouth 8 is equipped with discharge port 9 in the lower case of 6 other end of casing, moisture exhausting port 10 is additionally provided on casing 6.In casing 6
Two sides and bottom are provided with collet, to be passed through thermal medium.Live spindle 7 extends transversely through casing 6, and inner hollow, one end is set
There is thermal medium inlet, the other end is equipped with thermal medium outlet, and blade is arranged on the lateral wall of live spindle 7.Driver and rotation
Main shaft 7 is sequentially connected, to drive live spindle 7 to rotate.The leading portion (part for closing on feed inlet 8) of double blades drying machine 1
For preheating section, back segment is dryer section, and preheating section accounts for the 1/4 of body total length.
The top of the dryer section of rotating twin-screw dryer, including mounting rack 11, several branch pipes 12 is arranged in activator atomizer 2
With atomizer 14.Mounting rack 11 is the rectangular frame being welded by several cross bars and several vertical hack levers, is fixedly mounted on
On the casing top cover of double blades drying machine 1, and the live spindle 7 of its cross bar (frame body length direction) and double blades drying machine 1
In parallel.Branch pipe 12 is arranged on the hack lever of mounting rack 11, and each branch pipe 12 is connected to activator delivery pipe 5 respectively, atomizer 14
The lower section of branch pipe 12 is set, and inlet is connected to by connecting tube 13 with branch pipe 12.Activator delivery pipe 5 and activator storage tank
3 connections, conveying metering pump 4 are arranged in activator delivery pipe 5, to the activator conveying that will be stored in activator storage tank 3
To each branch pipe 12, and then enter atomizer 14.
When production, the calcium carbonate filter cake from a upper process is entered inside casing 6 by feed inlet 8, meanwhile, thermal medium is divided to two
Road enters in drying machine 1, enters in collet all the way, another way enters in live spindle 7.In the preheating section of double blades drying machine 1
In, the temperature of calcium carbonate material is increased to 80 DEG C.When material is run to the lower section of activator atomizer 2, starting conveying metering
Pump 4, the activator in storage tank 3 is pumped out, through each branch pipe 12, is sent to atomizer 14.The activation sprayed through atomizer 14
Agent is mixed with calcium carbonate material, and the heating of thermal medium and live spindle 7(are with blade in body) stirring action under, complete dry
Dry and activation procedure.Thermal medium by heat exchange drains into recovery system, the activated carbon obtained after the completion of activation is dry through outlet
Sour calcium enters next process through discharge port 9, and the dry wet tail gas generated is discharged through moisture exhausting port 10.
Embodiment 2
As shown in Figures 3 and 4, the utility model include Continuous disc drying machine 1, activator atomizer 2, activator storage tank 3,
Convey metering pump 4 and activator delivery pipe 5.
Continuous disc drying machine 1 includes casing 6, is equipped with feed inlet 8 at the top of casing 6, and bottom is equipped with discharge port 9,
Moisture exhausting port 10 is additionally provided on casing 6.Live spindle 7, several basins 15 are internally provided with and for being passed through heat in casing 6
The heating tube of medium.Basin 15 divides for deep bid and shallow bid, and deep bid and shallow bid are alternately distributed along 7 length direction of live spindle.Rotation
Turn main shaft 7 and driver is sequentially connected, several rake arms is provided in live spindle 7, if being respectively arranged in each rake arms
Dry harrowing leaf.When live spindle 7 rotates, rake arms and rake leaf is driven to rotate on basin 15, basin 15 and shell keep opposite
It is static.
The trying to get to the heart of a matter on face of first piece of basin of the dryer section of Continuous disc drying machine 1 is arranged in activator atomizer 2, and
Cylindric body relative to drying machine 1 is set for the eccentric.Activator atomizer 2 include activator distribution plate 16, allotment pipe 17,
Ring pipe 18 and several atomizers 14, allotment pipe 17 are connected between distribution plate 16 and ring pipe 18 (allotment pipe and annular
Pipe is referred to as branch pipe), atomizer 14 is arranged on ring pipe 18, the top of distribution plate 16 and the end of activator delivery pipe 5
It is connected, the inlet of atomizer 14 is connected to by connecting tube 13 with ring pipe 18.Activator delivery pipe 5 and activator storage tank 3
Connection, conveying metering pump 4 is arranged in activator delivery pipe 5, the activator being stored in activator storage tank 3 to be delivered to
In distribution plate 16, the allocated distribution of disk 16 to each allotment pipe 17, and then each atomizer 14 is entered by ring pipe 18.
When production, the calcium carbonate filter cake from a upper process is entered inside casing 6 by feed inlet 8, meanwhile, thermal medium is through adding
Heat pipe enters in basin 15, calcium carbonate material tray drier 1 preheating section pre-heating temperature elevation to 80 DEG C.When material comes downwards to
When activator 2 lower section of atomizer, start delivery pump, the activator in batch can is pumped out, the allocated disk 16 and each branch pipe 12, send to
Atomizer 14.The activator sprayed through atomizer 14 is mixed with calcium carbonate material, in body the heating of thermal medium and
Live spindle 7(is with rake arms and rake leaf) stirring action under, complete dry and activation procedure.Thermal medium by heat exchange is through going out
Mouth drains into recovery system, and the activated Calcium carbonate obtained after the completion of activation is dry enters next process through discharge port 9, dry to generate
Wet tail gas be discharged through moisture exhausting port 10.