CN207823007U - Automatic-temperature water-reducing agent process units - Google Patents
Automatic-temperature water-reducing agent process units Download PDFInfo
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- CN207823007U CN207823007U CN201721620886.5U CN201721620886U CN207823007U CN 207823007 U CN207823007 U CN 207823007U CN 201721620886 U CN201721620886 U CN 201721620886U CN 207823007 U CN207823007 U CN 207823007U
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- reaction chamber
- inductor
- reducing agent
- temperature
- process units
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Abstract
The utility model discloses Automatic-temperature water-reducing agent process units, it includes reaction chamber (1), and the first feeder sleeve (2) and the second feeder sleeve (3) are provided at the top of reaction chamber (1)；Flow inductor A (4), solenoid valve A (5), flow inductor B (6) and solenoid valve B (7) are respectively arranged on two feeder sleeves；Reaction chamber (1) bottom is provided with discharge nozzle (8), and discharge nozzle (8) is equipped with baiting valve (9)；It is provided with heating layer (10) in reaction chamber (1) side wall, temperature inductor (11) is provided with outside heating layer (10)；Fixed frame (12) is installed outside reaction chamber (1), motor (13) is installed on fixed frame (12)；It is connected with agitating shaft (14) on motor (13), stirring rod (15) is provided on agitating shaft (14)；It is provided with PLC controller (16) outside reaction chamber (1).The utility model can not only improve temperature control efficiency, also have the advantages that the probability of error is small and easy to operate.
Description
Technical field
The utility model is related to a kind of water-reducing agents to produce temperature regulating device, especially Automatic-temperature water-reducing agent process units.
Background technology
In water-reducing agent production process, requirement of the different links to the temperature of reaction is different, and some existing productions are set
Standby generally use water circulation control system realizes the control to temperature, but such efficiency is very low；And the height of temperature mostly by
Artificial to be completed to control, operate trouble, and the probability in operating process there are error is larger.Therefore, existing water-reducing agent
Production equipment has that temperature control is less efficient and the temperature control probability of error is larger.
Utility model content
The purpose of the utility model is to provide a kind of Automatic-temperature water-reducing agent process units.The utility model is not only
Temperature control efficiency can be improved, also has the advantages that the probability of error is low.
The technical solution of the utility model：A.T.C type water-reducing agent process units, it is characterised in that：Including reaction
Case, reaction chamber top are provided with the first feeder sleeve and the second feeder sleeve；Flow inductor A, flow are provided on first feeder sleeve
Solenoid valve A is equipped with below inductor A；It is provided with flow inductor B on second feeder sleeve, electromagnetism is equipped with below flow inductor B
Valve B；Reaction chamber bottom is provided with discharge nozzle, and discharge nozzle is equipped with baiting valve；Heating layer, heating layer are provided in reaction chamber side wall
It is provided with temperature inductor outside；Fixed frame is installed outside reaction chamber, motor is installed on fixed frame；It is connected on motor
Agitating shaft, stirring rod is provided on agitating shaft, and agitating shaft is arranged inside reaction chamber；PLC controller is provided with outside reaction chamber.
In A.T.C type water-reducing agent process units above-mentioned, there is lattice coil inside the heating layer, coil with
Temperature inductor connects；The outside of heating layer is provided with thermal insulation layer.
In A.T.C type water-reducing agent process units above-mentioned, the PLC controller is provided with multiple input end, often
A input terminal is correspondingly provided with output end.
In A.T.C type water-reducing agent process units above-mentioned, the reaction chamber is equipped with venthole.
In A.T.C type water-reducing agent process units above-mentioned, glass electrode and reference are provided on the agitating shaft
Electrode, two electrodes are connected with inductor.
In A.T.C type water-reducing agent process units above-mentioned, the input terminal of the solenoid valve A, solenoid valve B it is defeated
The input terminal for entering end and coil is connect with a output end in PLC controller respectively；Output end, the stream of the flow inductor A
The output end of the output end of inductor B, the output end of temperature inductor and inductor is measured respectively at a input in PLC controller
End connection.
Compared with prior art, the utility model improves existing temperature regulating device, by installing flow on feeder sleeve
Inductor and solenoid valve, to control the raw material for flowing into reaction chamber；By the way that heating layer, heating layer connection are arranged in reaction chamber side wall
There is temperature inductor, to realize the real-time monitoring to temperature, improves temperature control efficiency；In outside, setting PLC controller is come in fact simultaneously
Now to the automation control of temperature and flow, simplicity operation reduces the probability of error.In addition, passing through the ring in heating layer heating layer
It is wound with coil, using electromagnetic inductive heating principle, the purpose of heating is realized by being powered to coil；By in the outer of heating layer
Portion is provided with thermal insulation layer, to reduce the loss of heat；By being provided with glass electrode and reference electrode, two electricity on agitating shaft
Pole is connected with inductor, to detect the pH value inside reaction chamber in real time；By PLC controller come electromagnetic valve for adjusting A and solenoid valve
B flows into make material stablize.Therefore, the utility model can not only improve temperature control efficiency, also have the probability of error small and operation
Convenient advantage.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the partial enlarged view at A in Fig. 1；
Fig. 3 is the line graph of PLC controller and element.
Label in attached drawing be：1- reaction chambers, the first feeder sleeves of 2-, the second feeder sleeves of 3-, 4- flow inductors A, 5- electricity
Magnet valve A, 6- flow inductor B, 7- solenoid valve B, 8- discharge nozzle, 9- baiting valves, 10- heating layers, 11- temperature inductors, 12- are solid
Determine frame, 13- motors, 14- agitating shafts, 15- stirring rods, 16-PLC controllers, 17- coils, 18- thermal insulation layers, 19- ventholes,
20- glass electrodes, 21- reference electrodes, 22- inductors.
Specific implementation mode
The utility model is further described with reference to the accompanying drawings and examples, but is not intended as to the utility model
The foundation of limitation.
Embodiment.A.T.C type water-reducing agent process units is constituted as shown in Figures 1 to 3, including reaction chamber 1, reaction
1 top of case is provided with the first feeder sleeve 2 and the second feeder sleeve 3；Flow inductor A4, flow sense are provided on first feeder sleeve 2
It answers and is equipped with solenoid valve A5 below device A4；It is provided with flow inductor B6 on second feeder sleeve 3, electricity is equipped with below flow inductor B6
Magnet valve B7；1 bottom of reaction chamber is provided with discharge nozzle 8, and discharge nozzle 8 is equipped with baiting valve 9；It is provided with heating in 1 side wall of reaction chamber
Layer 10, heating layer 10 are provided with temperature inductor 11 outside；Fixed frame 12 is installed outside reaction chamber 1, is pacified on fixed frame 12
Equipped with motor 13；It is connected with agitating shaft 14 on motor 13, stirring rod 15 is provided on agitating shaft 14, the setting of agitating shaft 15 is being reacted
Inside case 1；PLC controller 16 is provided with outside reaction chamber 1.
There are lattice coil 17, coil 17 to be connect with temperature inductor 11 inside the heating layer 10；The outside of heating layer 10
It is provided with thermal insulation layer 18；The PLC controller 16 is provided with multiple input end, and each input terminal is correspondingly provided with output end；It is described
Reaction chamber 1 is equipped with venthole 19；Glass electrode 20 and reference electrode 21, two electrode connections are provided on the agitating shaft 14
There is inductor 22；The input terminal of the input terminal of the solenoid valve A5, the input terminal of solenoid valve B7 and coil 17 is controlled with PLC respectively
3 output ends connection on device 16；The output end of the flow inductor A4, the output end and temperature sense of flow inductor B6
The output end of device 11 is connected respectively at 3 input terminals in PLC controller 16.
Operation principle：Open PLC controller 16 and motor 13, coil 17 is powered, PLC controller 16 control solenoid valve A5 and
Solenoid valve B7 is opened, and first step raw material enters reaction chamber 1 by the first feeder sleeve 2；Motor 13 drives agitating shaft 14 to rotate, stirring
Axis 14 drives the rotation of stirring rod 15 to stir raw material；Flow inductor A4 monitors the flow of 2 inner material of the first feeder sleeve in real time
And PLC controller 16 is sent a signal to by input terminal, PLC controller 16 is sent out by the signal received from output end Y119
Go out to adjust signal, to adjust the size that solenoid valve A5 is closed in real time；Temperature inductor 11 detects the temperature in reaction chamber 1 in real time,
And PLC controller 16 is sent a signal to by input terminal X324, PLC controller 16 is by the analysis comparison to signal, from output
End Y321 send out signal, come change on coil 17 by electric current, ensure reaction chamber 1 in temperature be maintained at suitable range
In, the exhaust gas generated in reaction process can be discharged from gas outlet 19；After reaching the time of first step reaction, PLC controller 16
First control solenoid valve A5 is closed, then adjusts the electric current in coil 17, waits for that the temperature signal that temperature sensor 11 transmits reaches second
After walking the temperature needed, the unlatching of solenoid valve B7 is controlled by output end Y220, and the raw material that second step reacts is made to enter reaction chamber 1
It is interior, carry out next step reaction；Equally flow inductor B6 is sent out by input terminal X223 to PLC controller 16 during reaction
The number of delivering letters, temperature inductor 11 send signal by input terminal X324 to PLC controller 16, and PLC controller 16 passes through analysis pair
Than receiving signal, corresponding element is adjusted by corresponding output end；Equal second steps after reaction, control by PLC
Device 16 processed controls solenoid valve B7 and closes again, adjusts electric current in coil 17, waits for that the temperature that temperature inductor 11 detects reaches next
After the desired value for walking reaction temperature, solenoid valve A5 or solenoid valve B7 is opened, carries out next step reaction；Appeal step is repeated, is waited until
It is all to close motor 13 and PLC controller 16 after reaction, baiting valve 9 is opened, so that product is flowed out from discharge nozzle 8, waits products
After having flowed, baiting valve 9 is closed, all working terminates.
In a whole reaction process, glass electrode 20 and reference electrode 21 on agitating shaft 14 form a primary battery,
It is connect with inductor 22, inductor 22 sent data to PLC controller 16 every 5 minutes automatic storage one-shot measurement data；
PLC controller 16 can analyze the data that comparison receives, and when data value exceeds setting value, PLC controller 16 can send out alarm
Signal and stop signal, control solenoid valve A5, solenoid valve B7 and coil 17 are closed.
Claims (5)
1. Automatic-temperature water-reducing agent process units, it is characterised in that：The is provided with including reaction chamber (1), at the top of reaction chamber (1)
One feeder sleeve (2) and the second feeder sleeve (3)；Flow inductor A (4), flow inductor A (4) are provided on first feeder sleeve (2)
Lower section is equipped with solenoid valve A (5)；It is provided with flow inductor B (6) on second feeder sleeve (3), is equipped with below flow inductor B (6)
Solenoid valve B (7)；Reaction chamber (1) bottom is provided with discharge nozzle (8), and discharge nozzle (8) is equipped with baiting valve (9)；Reaction chamber (1) side
It is provided with heating layer (10) in wall, temperature inductor (11) is provided with outside heating layer (10)；Fixation is installed outside reaction chamber (1)
Frame (12) is equipped with motor (13) on fixed frame (12)；Agitating shaft (14) is connected on motor (13), on agitating shaft (14)
It is provided with stirring rod (15), agitating shaft (14) setting is internal in reaction chamber (1)；It is provided with PLC controller outside reaction chamber (1)
(16)；Glass electrode (20) and reference electrode (21) are provided on the agitating shaft (14), two electrodes are connected with inductor
(22)。
2. Automatic-temperature water-reducing agent process units according to claim 1, it is characterised in that：In the heating layer (10)
Portion has lattice coil (17), coil (17) to be connect with temperature inductor (11)；The outside of heating layer (10) is provided with thermal insulation layer
(18)。
3. Automatic-temperature water-reducing agent process units according to claim 1, it is characterised in that：The PLC controller
(16) it is provided with multiple input end, each input terminal is correspondingly provided with output end.
4. Automatic-temperature water-reducing agent process units according to claim 1, it is characterised in that：On the reaction chamber (1)
Equipped with venthole (19).
5. the Automatic-temperature water-reducing agent process units according to any requirement in Claims 1-4, it is characterised in that：Institute
State the input terminal of the input terminal of (5) solenoid valve A, the input terminal of solenoid valve B (7) and coil (17) respectively with PLC controller (16)
On 4 output ends connection；The output end of the flow inductor A (4), output end, the temperature sense of flow inductor B (6)
The output end of device (11) and the output end of inductor (22) are connect with 4 input terminals in PLC controller (16) respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721620886.5U CN207823007U (en) | 2017-11-29 | 2017-11-29 | Automatic-temperature water-reducing agent process units |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721620886.5U CN207823007U (en) | 2017-11-29 | 2017-11-29 | Automatic-temperature water-reducing agent process units |
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| CN207823007U true CN207823007U (en) | 2018-09-07 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107754747A (en) * | 2017-11-29 | 2018-03-06 | 浙江大东吴集团建设新材料有限公司 | A kind of Automatic-temperature water reducer process units |
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2017
- 2017-11-29 CN CN201721620886.5U patent/CN207823007U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107754747A (en) * | 2017-11-29 | 2018-03-06 | 浙江大东吴集团建设新材料有限公司 | A kind of Automatic-temperature water reducer process units |
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