CN205774139U - Water reducer production system - Google Patents
Water reducer production system Download PDFInfo
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- CN205774139U CN205774139U CN201620651015.9U CN201620651015U CN205774139U CN 205774139 U CN205774139 U CN 205774139U CN 201620651015 U CN201620651015 U CN 201620651015U CN 205774139 U CN205774139 U CN 205774139U
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Abstract
The utility model discloses water reducer production system, including reactor and the polycarboxylic acids storage tank, Formaldehyde Tank, acetone storage tank and the sulphite storage tank that are connected with reactor with hydraulic pump by pipeline respectively;The discharging opening of reactor is connected with water reducer storage tank by pipeline;Reactor includes tank body, and the roof of tank body has bar-shaped trough, charging aperture and stirring motor, and the power output shaft of stirring motor is connected with the mixed structure being arranged at tank interior;Mixed structure includes the shaft being connected with power output shaft and installs the stirring support that shaft middle and lower part is shaped as frame;The top of the branch bar of stirring support is installed with a baffle plate, and the lower surface of baffle plate is provided with a pressure transducer;It is provided with a thread segment on branch bar, thread segment is provided with the stirring vane matched with screw thread on it;First-class gauge, hydraulic pump, temperature sensor, pressure transducer, stirring motor and radiator fan are all connected with a control module.
Description
Technical field
This utility model relates to water reducer manufacture field, is specifically related to a kind of water reducer production system.
Background technology
Common additive when water reducer is to prepare concrete, it can reduce water consumption during concrete construction, reduce water
Gray scale, improves concrete strength, shortens concrete curing age, it is ensured that engineering construction progress, makes concrete have the most durable
Property and corrosion resistance.Polycarboxylate water-reducer is at present conventional high efficiency water reducing agent, the naphthalene system diminishing that its working condition is more general
Agent is the harshest, if in polymerization process, monomer polymerization not exclusively, not only has environmental protection hidden danger, and can affect concrete
Performance.
Water reducer mainly with acetone, formaldehyde, sulphite as raw material, sulfonated in stirred tank, condensation and prepare, at present
It is typically provided with a stirring rod in conventional reactor, stirring rod is provided with blade one and realizes the mixing of the solution in tank body,
Owing to the fraction region in reactor can only be stirred by blade, the solution in reactor is caused to be difficult to be fully contacted, from
And extend the response time of formaldehyde and acetone.
Utility model content
For above-mentioned deficiency of the prior art, this utility model provides and a kind of can fill the solution in tank body
Divide the water reducer production system of stirring.
In order to reach foregoing invention purpose, the technical solution adopted in the utility model is:
A kind of water reducer production system is provided to include reactor and pass through what pipeline connected with reactor with hydraulic pump respectively
Polycarboxylic acids storage tank, Formaldehyde Tank, acetone storage tank and sulphite storage tank;The discharging opening of described reactor passes through pipeline and water reducer
Storage tank connects;On the pipeline that described polycarboxylic acids storage tank, Formaldehyde Tank, acetone storage tank and sulphite storage tank are connected with reactor all
It is provided with a first-class gauge;
Reactor includes tank body, and the roof of tank body has bar-shaped trough, charging aperture and stirring motor, the power of stirring motor
Output shaft is connected with the mixed structure being arranged at tank interior;Sidewall and the diapire of tank body are constituted by medial wall and lateral wall,
It is provided with, in the interlayer that medial wall and lateral wall are formed, the electromagnetic heating coil that the solution in tank body is heated;Tank body
Discharging opening and temperature sensor is offered at sidewall adjacent bottom wall;
Mixed structure includes the shaft being connected with power output shaft and is installed on the stirring that shaft middle and lower part is shaped as frame
Support;The top of the branch bar of stirring support is installed with a baffle plate, and the lower surface of baffle plate is provided with a pressure transducer;Branch bar
On be provided with a thread segment, thread segment is provided with the stirring vane matched with screw thread on it;First-class gauge, hydraulic pressure
Pump, temperature sensor, pressure transducer, stirring motor and radiator fan are all connected with a control module.
During enforcement, the preferably sidewall at tank body is provided with multiple for lowering the temperature the solution in tank body at roof
Radiator fan, the sidewall of radiator fan surrounding is installed with a baffle plate installing rack in shaped as frame;Movable peace in bar-shaped trough
Coordinate with baffle plate installing rack equipped with one, when radiator fan does not uses, sealing that radiator fan installing port is sealed gear
Plate.
The beneficial effects of the utility model are: reactor is when being stirred the solution in tank body, and stirring support is right
While solution is stirred, the stirring vane that its bar is installed along with during the rotation of shaft by the lower end of thread segment upwards
Motion realizes rotation;When stirring vane collides pressure transducer, control module controls stirring motor reversion, makes stirring vane
From top to bottom move along thread segment.
This programme Stirring up and down by stirring vane, makes the existing rotation of stirring vane rotate with stirring support again,
Drive stirring support Stirring in conjunction with shaft, it is ensured that being fully contacted of the solution in tank body, thus accelerate formaldehyde
Response time with acetone.
After this programme arranges radiator fan, the heat that formaldehyde and acetone can carry out exothermic reaction generation is discharged rapidly
In tank body, after in tank body, solution reaction completes, and when the temperature in tank body is reduced to the temperature of isothermal holding, can use
The installing port installing radiator fan is sealed by sealing baffle and baffle plate installing rack, to avoid the temperature in tank body less than insulation
Temperature needed for process.
It addition, when the temperature in tank body is less than the temperature of isothermal holding, can start be arranged at tank body medial wall and
Solution in tank body is heated by the electromagnetic heating coil in the interlayer of lateral wall, makes the temperature constant of solution needed for isothermal holding
Temperature requirement.
Accompanying drawing explanation
Fig. 1 is the structural representation of water reducer production system.
Fig. 2 is the structural representation of reactor.
Fig. 3 is the axonometric chart that sealing ring is arranged in sealing baffle.
Wherein, 1, reactor;11, stirring motor;12, tank body;121, sealing baffle;122, sealing ring;123, baffle plate peace
Shelve;124, discharging opening;1241, second gauge;1242, spherical filter net;125, impurities outlet;126, charging aperture;13, dissipate
Hot-air fan;14, electromagnetic heating coil;15, heat-insulation layer;16, temperature sensor;17, transparent window;18, mixed structure;181, gear
Plate;182, pressure transducer;183, thread segment;184, stirring vane;185, shaft;2, polycarboxylic acids storage tank;21, stirring dress
Put;3, pipeline;31, first-class gauge;4, hydraulic pump;5, Formaldehyde Tank;6, acetone storage tank;7, sulphite storage tank;8, diminishing
Agent storage tank.
Detailed description of the invention
Below detailed description of the invention of the present utility model is described, in order to those skilled in the art understand
This utility model, the common skill it should be apparent that this utility model is not limited to the scope of detailed description of the invention, to the art
From the point of view of art personnel, as long as various change limits and in the spirit and scope of the present utility model that determine in appended claim,
These changes are apparent from, and all utilize innovation and creation that this utility model conceives all at the row of protection.
The structural representation of water reducer production system is shown with reference to Fig. 1, Fig. 1;As it is shown in figure 1, this water reducer produces system
The polycarboxylic acids storage tank 2 that including reactor 1 and connected with reactor 1 with hydraulic pump 4 by pipeline 3 respectively, Formaldehyde Tank 5, acetone
Storage tank 6 and sulphite storage tank 7;The discharging opening 124 of described reactor 1 is connected with water reducer storage tank 8 by pipeline 3;Described poly-
It is provided with one on the pipeline 3 that carboxylic acid storage tank 2, Formaldehyde Tank 5, acetone storage tank 6 and sulphite storage tank 7 are connected with reactor 1
First-class gauge 31.
The setting of first-class gauge 31, can be with personnel convenient to operate to polycarboxylic acids storage tank 2, Formaldehyde Tank 5, acetone storage tank 6
Control with accurate with grasping in real time of the solution of sulphite storage tank 7 output.
Polycarboxylic acids storage tank 2 in water reducer production system is provided with the agitating device 21 being stirred its internal solution,
During enforcement, preferably agitating device 21 includes and is arranged on internal dynamic with the motor on polycarboxylic acids storage tank 2 roof of polycarboxylic acids storage tank 2
The stirring rod that power output shaft connects and the stirring blade being arranged in stirring rod.
As in figure 2 it is shown, the reactor 1 in water reducer production system includes tank body 12, the roof of tank body 12 has bar shaped
Groove, charging aperture 126 and stirring motor 11, the power output shaft of stirring motor 11 and the mixed structure 18 being arranged within tank body 12
Connect.
When implementing, the preferably mixed structure 18 of this programme includes the shaft 185 being connected with power output shaft and installs
It is the stirring support of shaped as frame in shaft 185 middle and lower part;The top of the branch bar of stirring support is installed with a baffle plate 181, gear
The lower surface of plate 181 is provided with a pressure transducer 182;It is provided with a thread segment 183 on branch bar, thread segment 183 is installed
There is the stirring vane 184 matched with screw thread on it.
When being stirred the solution in tank body 12, stirring support is while being stirred solution, on its bar
The stirring vane 184 installed realizes rotation along with being moved upward by the lower end of thread segment 183 during the rotation of shaft 185;When stirring
Mixing blade 184 when colliding pressure transducer 182, control module controls stirring motor 11 and inverts, and makes stirring vane 184 along spiral shell
Stricture of vagina section 183 is from top to bottom moved.
This programme Stirring up and down by stirring vane 184, makes the existing rotation of stirring vane 184 again with stirring support
Rotate, drive stirring support Stirring in conjunction with shaft 185, it is ensured that being fully contacted of the solution in tank body 12, thus
Accelerate the response time of formaldehyde and acetone.
Carrying out self-adaptative adjustment for the ease of reactor 1 according to its internal solution temperature, this programme is additionally provided with a control
Molding block, first-class gauge 31, hydraulic pump 4, temperature sensor 16, pressure transducer 182, stirring motor 11 and radiator fan 13
All it is connected with a control module.
Sidewall at tank body 12 is provided with the radiation air that multiple solution in tank body 12 carries out lowering the temperature at roof
Fan 13;After arranging radiator fan 13, the heat that formaldehyde and acetone can carry out exothermic reaction generation discharges tank body 12 rapidly
In.
As it is shown on figure 3, be installed with baffle plate 181 installing rack in shaped as frame on the sidewall of radiator fan 13 surrounding
123;It is movably installed with one when radiator fan 13 does not uses in institute's bar-shaped trough, radiator fan 13 installing port is sealed
Sealing baffle 121;After in tank body 12, solution reaction completes, and when the temperature in tank body 12 is reduced to the temperature of isothermal holding
Time, sealing baffle 121 can be used to seal, the installing port installing radiator fan 13 to keep away with baffle plate 181 installing rack 123
Exempt from the temperature in tank body 12 less than the temperature needed for isothermal holding.
During in order to ensure isothermal holding, the sealing of tank body 12, when implementing, the preferably interior table of baffle plate 181 installing rack 123
Face is provided with a sealing ring 122.After sealing ring 122 is arranged, it can be ensured that between baffle plate 181 installing rack 123 and sealing baffle 121
Sealing.
Referring again to Fig. 2, sidewall and the diapire of tank body 12 are constituted, in medial wall and lateral wall by medial wall and lateral wall
It is provided with, in the interlayer formed, the electromagnetic heating coil 14 that the solution in tank body 12 is heated;The sidewall of tank body 12 is the end of adjacent to
Discharging opening 124 and temperature sensor 16 is offered at wall.
After electromagnetic heating coil 14 is arranged, when the temperature in tank body 12 is less than the temperature of isothermal holding, can start
Solution in tank body 12 is heated by the electromagnetic heating coil 14 being arranged in the medial wall of tank body 12 and lateral wall interlayer, makes solution
Temperature constant temperature requirement needed for isothermal holding.
During enforcement, this programme is preferably enclosed with one layer at the sidewall of tank body 12 and the outer surface of diapire and prevents Electromagnetic Heating line
The heat of circle 14 generation is to the heat-insulation layer 15 of external diffusion.
Due to the solution in reactor 1 reaction time, some impurity can be produced, in order to avoid impurity from discharging opening 124 with
Finished product is discharged together, affects the quality of product;When implementing, this programme is preferably positioned at the end of tank body 12 at discharging opening 124
It is provided with a spherical filter net 1242, the diapire of tank body 12 offers an impurities outlet 125.
For the ease of amount during reactor 1 blowing is accurately controlled, discharging opening 124 is provided with one and controls mould
The second gauge 1241 that block connects.
Belonging to heat release owing to formaldehyde and acetone react, the two can release substantial amounts of heat when reacting, and solution may
There will be the phenomenon of rolling, if the solution participating in reaction in tank body 12 is too much, it is most likely that part solution rolling occurs to dissipating
On Hot-air fan 13, damage radiator fan 13.
In order to solution in tank body 12 is observed by the moment, preferably install one on the sidewall of tank body 12 and be used for observing tank body 12
The transparent window 17 of interior solution reaction situation, is provided with the scale of liquid level in measuring tank body 12 on transparent window 17
Line.
The setting of graduation mark, can facilitate operator to understand the amount of the solution putting into or releasing tank body 12 in time.
In sum, the water reducer production system that this utility model provides is when carrying out water reducer and producing, it is possible to reaction
Solution in still 1 is thoroughly mixed, and makes intensification or heat discharging operation according to the response situation in reactor 1.
Although detailed description of the invention of the present utility model being described in detail in conjunction with accompanying drawing, but should not be construed as right
The restriction of the protection domain of this patent.In the scope described by claims, those skilled in the art are without creative labor
The dynamic various amendments that can make and deformation still belong to the protection domain of this patent.
Claims (6)
1. water reducer production system, it is characterised in that include reactor and connected with reactor with hydraulic pump by pipeline respectively
Polycarboxylic acids storage tank, Formaldehyde Tank, acetone storage tank and sulphite storage tank;The discharging opening of described reactor passes through pipeline and diminishing
Agent storage tank connects;On the pipeline that described polycarboxylic acids storage tank, Formaldehyde Tank, acetone storage tank and sulphite storage tank are connected with reactor
It is provided with a first-class gauge;
Described reactor includes tank body, and the roof of described tank body has bar-shaped trough, charging aperture and stirring motor, described stirring electricity
The power output shaft of machine is connected with the mixed structure being arranged at tank interior;The sidewall of described tank body and diapire by medial wall and
Lateral wall is constituted, and is provided with, in the interlayer that medial wall and lateral wall are formed, the Electromagnetic Heating heating the solution in tank body
Coil;Discharging opening and temperature sensor is offered at the sidewall adjacent bottom wall of described tank body;
Described mixed structure includes the shaft being connected with described power output shaft and to be installed on shaft middle and lower part be shaped as frame
Stirring support;The top of the branch bar of described stirring support is installed with a baffle plate, and the lower surface of described baffle plate is provided with a pressure
Force transducer;It is provided with a thread segment on branch bar, described thread segment is provided with the stirring vane matched with screw thread on it;
Described first-class gauge, hydraulic pump, temperature sensor, pressure transducer, stirring motor and radiator fan all with a control module
Connect.
Water reducer production system the most according to claim 1, it is characterised in that at the sidewall of described tank body at roof
Multiple radiator fan for lowering the temperature the solution in tank body is installed, the sidewall of radiator fan surrounding is installed with
The one baffle plate installing rack in shaped as frame;It is movably installed with in bar-shaped trough and one coordinates with baffle plate installing rack, do not use for radiator fan
Time, the sealing baffle that radiator fan installing port is sealed.
Water reducer production system the most according to claim 2, it is characterised in that the inner surface of described baffle plate installing rack is arranged
There is a sealing ring.
Water reducer production system the most according to claim 1, it is characterised in that described discharging opening is positioned at the end of tank body
It is provided with a spherical filter net, the diapire of described tank body offers an impurities outlet.
Water reducer production system the most according to claim 1, it is characterised in that install one on the sidewall of described tank body and be used for
In observation tank body, the transparent window of solution reaction situation, is provided with the scale of liquid level in measuring tank body on transparent window
Line.
6. according to the arbitrary described water reducer production system of claim 1-5, it is characterised in that at sidewall and the end of described tank body
The outer surface of wall is enclosed with one layer of heat preventing electromagnetic heating coil from producing to the heat-insulation layer of external diffusion.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201620651015.9U CN205774139U (en) | 2016-06-28 | 2016-06-28 | Water reducer production system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201620651015.9U CN205774139U (en) | 2016-06-28 | 2016-06-28 | Water reducer production system |
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Publication Number | Publication Date |
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CN205774139U true CN205774139U (en) | 2016-12-07 |
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CN (1) | CN205774139U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108620012A (en) * | 2018-06-13 | 2018-10-09 | 惠州市强茂化工科技有限公司 | Reaction system for butyl polyacrylate |
-
2016
- 2016-06-28 CN CN201620651015.9U patent/CN205774139U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108620012A (en) * | 2018-06-13 | 2018-10-09 | 惠州市强茂化工科技有限公司 | Reaction system for butyl polyacrylate |
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