CN207671697U - A kind of production system of smectite powder - Google Patents
A kind of production system of smectite powder Download PDFInfo
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- CN207671697U CN207671697U CN201721646861.2U CN201721646861U CN207671697U CN 207671697 U CN207671697 U CN 207671697U CN 201721646861 U CN201721646861 U CN 201721646861U CN 207671697 U CN207671697 U CN 207671697U
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Abstract
The utility model discloses a kind of production systems of smectite powder, belong to smectite powder technical field.The production system of the utility model includes original soil processing unit, purifying modified device, separation drying unit, crushing packing device and wastewater treatment equipment；Original soil processing unit, purifying modified device, separation drying unit and crushing packing device be sequentially communicated, wastewater treatment equipment respectively by pipeline and detach drying unit and purifying modified device connection, to form waste water circulation loop；The operation system structure compact and reasonable, industrial operability is strong, and using effect is good.
Description
Technical field
The utility model is related to smectite powder technical fields, and in particular to a kind of production system of smectite powder
System.
Background technology
Organic montmorillonite powder is a kind of compound of inorganic mineral and organic matter, in all kinds of organic solvents, oils, liquid
Gel can be formed in resin, and there is good thickening property, thixotropy, suspension stability, high-temperature stability, lubricity, film forming,
Water resistance and chemical stability, therefore it is widely used in the industry such as coating, paint, printing ink, aviation, metallurgy, chemical fibre, oil.It is applying
In terms of material, organic montmorillonite powder is corrosion-resistant, wear-resisting, anti-for having in metal anti-corrosive paint generally as anti-settling agent, thickener
Salt water contamination, is not easy the features such as wet at shock resistance；In terms of textile industry, the dye of the main synthetic fabrics of organic montmorillonite powder
Color auxiliary agent；In terms of high speed printing ink, the consistency of ink, viscosity and control permeability are adjusted as needed；High gentle
In terms of consistent lubricant, organic montmorillonite powder is used in particular for preparing the Hmp grease for being suitable for high temperature and continuously running operation for a long time；
In oil base drilling fluid, organic clay is oleophylic colloid most basic in drilling fluid, organic clay be the system that can be improved viscosity and
Shearing force, and the filter loss of system can be reduced, therefore organic clay is essential additive, preparative in oil base drilling fluid
The excellent organic clay of energy is the premise for preparing high-performance oil-based drilling fluid.
Natural smectite powder has larger specific surface area and ion exchange capacity, since its surface silica structure has pole
The hydrolysis of strong hydrophily and interlayer cation, therefore the ability of non-modified original soil absorption organic matter is poor.As having at present
One of the method for modifying of machine montmorillonite powder, dry method are that aqueous na-montmorillonite powder and organic stearic acid and aliphatic ester is direct
Mixing is uniformly mixed, and squeezes, the organic montmorillonite powder containing certain moisture is made.Dry process is simple, but since dry method is usual
It need to squeeze or be carried out under the melting temperature of organic modifiers, energy consumption is big, and can not ensure the homogeneity of products obtained therefrom and steady
It is qualitative.
Therefore it provides a kind of performance is uniform, stablize and the production system of the smectite powder of saving energy consumption is this practicality
The problem of novel urgent need to resolve.
Utility model content
For overcome the deficiencies in the prior art, the purpose of this utility model is to provide a kind of productions of smectite powder
System, the operation system structure compact and reasonable of the utility model, industrial operability is strong, and using effect is good.
To solve the above problems, technical solution used by the utility model is as follows：
A kind of production system of smectite powder comprising original soil processing unit, purifying modified device, separation drying dress
It sets, crushing packing device and wastewater treatment equipment；The original soil processing unit, purifying modified device, separation drying unit and powder
Broken packing device is sequentially communicated, the original soil processing unit to original soil after screening and packing by pipeline by feedstock transportation extremely
Sodium modification is carried out in the purifying modified device, modified organic montmorillonite powder is dried by pipeline to the separation
Washing is detached and is dried in device, is dispensed finally by grinding is crushed in pipeline to the crushing packing device；Institute
It states wastewater treatment equipment and drying unit and the connection of purifying modified device is detached with described by pipeline respectively, to form waste water cycle
Circuit.
Preferably, the original soil processing unit includes original soil storage pool, the first screening machine, the first deduster and packing of weighing
Device；The original soil storage pool is connected to by conveyer with the feeding mouth of first screening machine, the discharging of first screening machine
Mouth is connected to the feeding mouth of the dispenser of weighing；The air intake vent of the air outlet of first screening machine and first deduster
By gas phase pipeline connection, the first air-introduced machine is connected on the air outlet of first deduster, first deduster goes out
Material mouth is arranged in the upper end of the dispenser of weighing；The original soil dispensed is delivered to institute by the dispenser of weighing by conveyer
It states in purifying modified device.
Preferably, the purifying modified device includes pulping tank, natridization reaction device, hydrocyclone, modified-reaction device, changes
Property agent feed pot；The feeding mouth of the pulping tank is connected to the original soil processing unit, the discharge port of the pulping tank with it is described
The feeding mouth of natridization reaction device is connected to, and the discharge port of the natridization reaction device is connected to the hydrocyclone, the waterpower rotation
The top of stream device is connected to by the pipeline with pump with the modified-reaction device, the bottom of the modified-reaction device by pipeline and
The pipeline connection with pump, the modifying agent feed pot are connected to the modified-reaction device；The modified-reaction device and institute
State separation drying unit connection.
Preferably, the separation drying unit includes solid-liquid separator and dryer, the feeding end of the solid-liquid separator
It is connected to the purifying modified device, the liquid discharge end of the solid-liquid separator is connected to the wastewater treatment equipment, described
The solids exit end of solid-liquid separator is connected to the dryer；The crushing packing device include grinder, the second screening machine,
Second deduster and packaging unit, the grinder are connected to the discharge port of the dryer, the top of the grinder and institute
The top connection of the second screening machine is stated, the top of second screening machine is connected to second deduster, second screening
The bottom of machine and the second deduster is connected to by pipeline with the packaging unit respectively.
Preferably, the wastewater treatment equipment includes header tank, recovery pond and clear water reserviors；The header tank is detached with described
Drying unit is connected to, and the entrance of the recovery pond is connected to the header tank, and the outlet of the recovery pond connects with the clear water reserviors
Logical, the clear water reserviors are connected to the purifying modified device.
Compared with prior art, the beneficial effects of the utility model are：
The production system technique of smectite powder described in the utility model is continuous, method is simple, industrial operability
By force, reaction more fully, speed faster, modified effect it is more preferable, it is environmentally friendly, realize the zero-emission of waste water.
Description of the drawings
Fig. 1 is the structural schematic diagram of the production system of smectite powder described in the utility model；
Drawing reference numeral explanation：1, original soil processing unit；11, original soil storage pool；12, the first screening machine；13, the first dedusting
Device；14, it weighs dispenser；15, the first air-introduced machine；2, purifying modified device；21, pulping tank；22, natridization reaction device；23, waterpower
Cyclone；24, modified-reaction device；25, modifying agent feed pot；3, drying unit is detached；31, solid-liquid separator；32, dryer；
4, crushing packing device；41, grinder；42, the second screening machine；43, the second deduster；44, packaging unit；5, wastewater treatment fills
It sets；51, header tank；52, recovery pond；53, clear water reserviors；6, steam unit；7, the second air-introduced machine.
Specific implementation mode
The utility model is described in further detail with reference to the accompanying drawings and detailed description.
As shown in Figure 1, being a kind of production system of smectite powder described in the utility model comprising original soil processing
Device 1, purifying modified device 2, separation drying unit 3, crushing packing device 4 and wastewater treatment equipment 5.Original soil processing unit 1,
Purifying modified device 2, separation drying unit 3 and crushing packing device 4 are sequentially communicated, and original soil processing unit 1 is to original soil through sieving
After choosing and packing natridization reaction and modified-reaction will be carried out by pipeline in feedstock transportation to purifying modified device 2, it is modified
Organic montmorillonite powder is detached and is dried by washing in pipeline to separation drying unit 3, finally by pipeline to powder
It crushes, grind, pack in broken packing device 4, obtain organic montmorillonite powder finished product；Wastewater treatment equipment 5 passes through pipe respectively
Road is connected to drying unit 3 and purifying modified device 2 is detached, to form cycling utilization of wastewater circuit.
Specifically, original soil processing unit 1 includes original soil storage pool 11, the first screening machine 12, the first deduster 13 and weighs
Dispenser 14.Original soil storage pool 11 is connected to by conveyer with the feeding mouth of the first screening machine 12, the discharging of the first screening machine 12
Mouth is connected to the feeding mouth for dispenser 14 of weighing；The air intake vent of the air outlet of first screening machine 12 and the first deduster 13 passes through gas
Phase pipeline connection is connected with the first air-introduced machine 15, the discharge port setting of the first deduster 13 on the air outlet of the first deduster 13
In the upper end for weighing dispenser 14；The original soil dispensed is delivered to purifying modified device 2 by dispenser 14 of weighing by conveyer
In.The course of work of original soil processing unit 1 is as follows：Natural smectite powder is stored in original soil storage pool 11, passes through conveyer
Natural smectite powder is delivered in the first screening machine 12 and is sieved, the first screening machine 12 includes multiple Screen assemblies,
The outlet discharge of the original soil of the middle and low grade screened component bottom when passing through first Screen assemblies, high-grade original soil are conveyed
To in next Screen assemblies, then original soil is reached through remaining Screen assemblies in dispenser 14 of weighing, and original soil dust is in air inducing
Air outlet through the first screening machine 12 under the action of machine, which is delivered in deduster, to be dusted, and original soil dust is under deduster effect
It falls into weighing dispenser 14, the original soil for being screened out dispenses in dispenser 14 of weighing according to specific weight.
Specifically, purifying modified device 2 includes pulping tank 21, natridization reaction device 22, hydrocyclone 23, modified-reaction device
24, modifying agent feed pot 25.The feeding mouth of pulping tank 21 is connected to original soil processing unit 1, the discharge port and sodium of pulping tank 21
The feeding mouth of reactor 22 is connected to, and the discharge port of natridization reaction device 22 is connected to hydrocyclone 23, the top of hydrocyclone 23
End is connected to by the pipeline with pump with modified-reaction device 24, and the bottom of modified-reaction device 24 passes through pipeline and the pipeline with pump
Connection, modifying agent feed pot 25 are connected to modified-reaction device 24；Modified-reaction device 24 is connected to drying unit 3 is detached.Purification changes
The course of work of property device 2 is as follows：It is anti-to be delivered to sodium after stirring evenly for the original soil dispensed stirring pulping in pulping tank 21
Answer and natrium carbonicum calcinatum is added in device 22 carries out natridization reaction, the montmorillonite powder after sodium enter in hydrocyclone 23 carry out from
The heart, the montmorillonite powder particle for keeping grain size larger are passed through by the smaller montmorillonite powder particle of the bottom discharge of hydrocyclone 23, grain size
It is modified reaction, modifying agent feed pot in the modified-reaction device 24 that the pipeline at 23 top of hydrocyclone enters in subsequent processing
Modifying agent is added to be stirred with montmorillonite powder particle in modified-reaction device 24 and mixes by 25, and material is made to mix in the horizontal
It is even；In order to further react fully, the mixture in modified-reaction device 24 flows back into the top of modified-reaction device 24 by pipeline
Portion continues to be stirred, and so that material is uniformly mixed in the longitudinal direction, reacts abundant.
Specifically, separation drying unit 3 include solid-liquid separator 31 and dryer 32, the feeding end of solid-liquid separator 31 with
Purifying modified device 2 is connected to, and the liquid discharge end of solid-liquid separator 31 is connected to wastewater treatment equipment 5, solid-liquid separator 31
Solids exit end is connected to dryer 32；Crushing packing device 4 includes grinder 41, the second screening machine 42, the second deduster 43
With packaging unit 44, grinder 41 is connected to the discharge port of dryer 32, the top at the top of grinder 41 and the second screening machine 42
Portion is connected to, and the top of the second screening machine 42 is connected to the second deduster 43, the bottom of the second screening machine 42 and the second deduster 43
It is connected to respectively with packaging unit 44 by pipeline.By smectite powder made from purifying modified device 2 under the action of pump
It is transported in solid-liquid separator 31 and carries out washing separation, the waste water after separation is flowed into wastewater treatment equipment 5 through pipeline and carried out
It recycles；Solid enters after being dried in dryer 32 is ground to required fineness in grinder 41, subsequently into second
Sizing screening is carried out in screening machine 42, is finally dispensed to get smectite powder finished product in packaging unit 44.
Wastewater treatment equipment 5 includes header tank 51, recovery pond 52 and clear water reserviors 53；Header tank 51 with detach drying unit 3
Connection, the entrance of recovery pond 52 are connected to header tank 51, and the outlet of recovery pond 52 is connected to clear water reserviors 53, clear water reserviors 53 and purification
Reforming apparatus 2 is connected to.Waste water is collected in after the outflow of solid-liquid separator 31 in header tank 51, is then flowed into recovery pond 52 and is carried out
Purified treatment is delivered in clear water reserviors 53 by pump after up to standard and is stored, then passes through the pipeline with pump to purifying modified device 2
Zero-emission is realized in middle reuse.
Production system described in the utility model further includes steam unit 6, which is added by pipeline and modifying agent
Batch can 25 is connected to so that the modifying agent atomization in modifying agent feed pot 25 so that modifying agent reacts more abundant with base slurry；The steaming
Vapour device 6 is connected to by pipeline with dryer 32, and institute's calorific requirement is provided for baking operation；Further, dryer 32 passes through pipe
Road is connected with the second air-introduced machine 7, comes to drain steam from dryer 32.
The above embodiment is only preferred embodiments of the present invention, cannot be protected with this to limit the utility model
Range, the variation of any unsubstantiality that those skilled in the art is done on the basis of the utility model and replacing belongs to
In the utility model range claimed.
Claims (5)
1. a kind of production system of smectite powder, it is characterised in that：Including original soil processing unit, purifying modified device, divide
From drying unit, crushing packing device and wastewater treatment equipment；The original soil processing unit, purifying modified device, separation drying
Device and crushing packing device are sequentially communicated, and the original soil processing unit will be former by pipeline after screening and packing to original soil
Material is delivered in the purifying modified device and carries out sodium modification, and modified organic montmorillonite powder is by pipeline to described
Washing is detached and is dried in separation drying unit, finally by crushing grinding in pipeline to the crushing packing device
Packing；The wastewater treatment equipment detaches drying unit and the connection of purifying modified device by pipeline with described respectively, to be formed
Waste water circulation loop.
2. the production system of smectite powder according to claim 1, it is characterised in that：The original soil processing unit packet
Include original soil storage pool, the first screening machine, the first deduster and dispenser of weighing；The original soil storage pool by conveyer with it is described
The feeding mouth of first screening machine is connected to, and the discharge port of first screening machine is connected to the feeding mouth of the dispenser of weighing；Institute
The air intake vent of the air outlet of the first screening machine and first deduster is stated by gas phase pipeline connection, first deduster
The first air-introduced machine is connected on air outlet, the discharge port of first deduster is arranged in the upper end of the dispenser of weighing；Institute
Dispenser of weighing is stated the original soil dispensed is delivered in the purifying modified device by conveyer.
3. the production system of smectite powder according to claim 1, it is characterised in that：The purifying modified device packet
Include pulping tank, natridization reaction device, hydrocyclone, modified-reaction device, modifying agent feed pot；The feeding mouth of the pulping tank and institute
The connection of original soil processing unit is stated, the discharge port of the pulping tank is connected to the feeding mouth of the natridization reaction device, and the sodium is anti-
The discharge port of device is answered to be connected to the hydrocyclone, the top of the hydrocyclone is changed by the pipeline with pump with described
Property reactor connection, the bottom of the modified-reaction device is connected to described with the pipeline pumped by pipeline, and the modifying agent adds
Batch can is connected to the modified-reaction device；The modified-reaction device detaches drying unit connection with described.
4. the production system of smectite powder according to claim 1, it is characterised in that：The separation drying unit packet
Solid-liquid separator and dryer are included, the feeding end of the solid-liquid separator is connected to the purifying modified device, the solid-liquid point
Liquid discharge end from device is connected to the wastewater treatment equipment, solids exit end and the dryer of the solid-liquid separator
Connection；The crushing packing device includes grinder, the second screening machine, the second deduster and packaging unit, the grinder with
The discharge port of the dryer is connected to, and the top of the grinder is connected to the top of second screening machine, second sieve
The top of extension set is connected to second deduster, the bottom of second screening machine and the second deduster respectively by pipeline with
The packaging unit connection.
5. the production system of smectite powder according to claim 1, it is characterised in that：The wastewater treatment equipment packet
Include header tank, recovery pond and clear water reserviors；The header tank detaches drying unit connection, the entrance of the recovery pond and institute with described
Header tank connection is stated, the outlet of the recovery pond is connected to the clear water reserviors, and the clear water reserviors connect with the purifying modified device
It is logical.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721646861.2U CN207671697U (en) | 2017-11-30 | 2017-11-30 | A kind of production system of smectite powder |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201721646861.2U CN207671697U (en) | 2017-11-30 | 2017-11-30 | A kind of production system of smectite powder |
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| CN207671697U true CN207671697U (en) | 2018-07-31 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107857279A (en) * | 2017-11-30 | 2018-03-30 | 联技精细材料(珠海)有限公司 | The production method and its system of a kind of smectite powder |
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- 2017-11-30 CN CN201721646861.2U patent/CN207671697U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107857279A (en) * | 2017-11-30 | 2018-03-30 | 联技精细材料(珠海)有限公司 | The production method and its system of a kind of smectite powder |
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