CN207823021U - A kind of reactor and chemical producing system - Google Patents
A kind of reactor and chemical producing system Download PDFInfo
- Publication number
- CN207823021U CN207823021U CN201721893488.0U CN201721893488U CN207823021U CN 207823021 U CN207823021 U CN 207823021U CN 201721893488 U CN201721893488 U CN 201721893488U CN 207823021 U CN207823021 U CN 207823021U
- Authority
- CN
- China
- Prior art keywords
- temperature
- controller
- reactor
- helix tube
- cylinder
- 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.)
- Active
Links
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
A kind of reactor of the utility model offer and chemical producing system, are related to chemical reaction equipment field.Including：Cylinder, cylinder limit accommodating cavity；Helix tube, helix tube are arranged in accommodating cavity, and the both ends of helix tube are run through cylinder and extended to outside cylinder；And mixing component, mixing component setting are surround in accommodating cavity, and by helix tube.The setting of helix tube can increase heat exchange area when heat exchange occurring in reactor, to the heat transfer effect of enhancing reactor.Mixing component setting is surround in accommodating cavity, and by helix tube, improves the space availability ratio in accommodating cavity.Mixing component by stirring the fluid in accommodating cavity, conduct heat, and achievees the purpose that enhancing reactor heat transfer effect by the convection current to reinforce fluid and spiral tube fluid in accommodating cavity.The enhancing of reactor exchange capability of heat enables reactor preferably controlling reaction temperature, to reduce the generation of side reaction, improves the yield of reaction.
Description
Technical field
The utility model is related to chemical reaction equipment fields, in particular to a kind of reactor and chemical producing system.
Background technology
The heat transfer effect of chemical reaction equipment has strong influence to the control of chemical reaction, for some strongly exothermic changes
If learning the heat that reaction generates cannot be pulled away in time, it is likely that lead to the consequences such as runaway reaction even explosion.For needing
The chemical reaction carried out under specific reaction temperature improves the yield of reaction to reduce the generation of side reaction, needs to realize anti-
Answer being precisely controlled for internal temperature.Therefore, the heat transfer effect for improving reactor is the common of current fine chemistry industry and pharmaceutical industry
Demand.
Utility model content
The purpose of this utility model is to provide a kind of reactors can preferably control with higher exchange capability of heat
Temperature inside system reaction, improves reaction yield.
The another object of the utility model is to provide a kind of chemical producing system, can be changed using reactor is higher
Thermal energy power achievees the purpose that improve production efficiency.
What the embodiments of the present invention were realized in：
A kind of reactor, including：
Cylinder, cylinder limit accommodating cavity；
Helix tube, helix tube are arranged in accommodating cavity, and the both ends of helix tube are run through cylinder and extended to outside cylinder；With
And
Mixing component, mixing component setting are surround in accommodating cavity, and by helix tube.
Further, cylinder is for accommodating heat transferring medium, and helix tube is for accommodating reaction mass.
Further, helix tube is equipped with the first temperature monitor for detecting temperature in helix tube.
Further, cylinder is connected with feed pipe and discharge nozzle.The first control valve, discharge nozzle setting the is arranged in feed pipe
Two control valves.
Further, reactor further includes controller, and the first control valve and the second control valve are electrically-controlled valve.First control
Valve, the second control valve and the first temperature monitor are electrically connected with controller.Controller is for receiving the first temperature monitor
First temperature signal of feedback simultaneously compares the preset temperature of the first temperature signal and controller, and controller is used for according to right
Than the aperture that result adjusts the first control valve and/or the second control valve.
Further, cylinder is connected with heating component, and the heater of heating component is located in accommodating cavity.
Further, reactor further includes controller.Controller is electrical with heating component and the first temperature monitor respectively
Connection.Controller is used to receive the first temperature signal that the first temperature monitor is fed back and by the first temperature signal and controller
Preset temperature is compared, and controller is used to adjust the heating power of heating component according to comparing result.
Further, cylinder is equipped with the second temperature detector for detecting temperature in accommodating cavity.
Further, reactor further includes controller.First temperature monitor, second temperature detector and mixing component are equal
It is electrically connected with controller.Controller is used to receive the first temperature signal of the first temperature monitor feedback, receives second temperature
The second temperature signal of detector feedback, and the first temperature signal and second temperature signal are compared, controller is used for root
The mixing speed of mixing component is adjusted according to comparing result.
Further, reactor further includes controller.Controller is electrical with mixing component and the first temperature monitor respectively
Connection.Controller is used to receive the first temperature signal that the first temperature monitor is fed back and by the first temperature signal and controller
Preset temperature is compared, and controller is used to adjust the mixing speed of mixing component according to comparing result.
A kind of chemical producing system, including：Any one of the above reactor.
The embodiments of the present invention at least have the following advantages that or advantageous effect：
The embodiments of the present invention provide a kind of reactor, which includes mainly cylinder, helix tube and stirring
Component.Wherein, helix tube is arranged in the accommodating cavity limited by cylinder, and the both ends of helix tube are run through cylinder and extended to
Outside cylinder, convenient for helix tube reception and outputting material.The setting of helix tube can increase changing when heat exchange occurring in reactor
Hot area, to the heat transfer effect of enhancing reactor.Mixing component setting is surround in accommodating cavity, and by helix tube, is improved
Space availability ratio in accommodating cavity.Mixing component is by stirring the fluid in accommodating cavity, to reinforce being flowed in accommodating cavity
The convection current of body and spiral tube fluid is conducted heat, and achievees the purpose that enhancing reactor heat transfer effect.Since mixing component is by helix tube
It surround, mixing component enables the fluid with certain rotating speed more uniformly to be contacted with helix tube when stirring, to further
Improve the heat-transfer effect of the inside and outside fluid of helix tube.The enhancing of reactor exchange capability of heat enables reactor preferably to control reaction
Temperature improves the yield of reaction to reduce the generation of side reaction.
The embodiments of the present invention also provide a kind of chemical producing system, including above-mentioned reactor.The Chemical Manufacture system
System achievees the purpose that improve production efficiency and production capacity using the high efficient heat exchanging ability of reactor.
Description of the drawings
It, below will be to required use in embodiment in order to illustrate more clearly of the technical solution of the utility model embodiment
Attached drawing be briefly described, it should be understood that the following drawings illustrates only some embodiments of the utility model, therefore should not be by
Regard the restriction to range as, for those of ordinary skill in the art, without creative efforts, may be used also
To obtain other relevant attached drawings according to these attached drawings.
Fig. 1 is the structural schematic diagram for the reactor that the utility model embodiment 1 provides；
Fig. 2 is the A direction views of Fig. 1；
Fig. 3 is the electrical control structure schematic diagram for the controller that the utility model embodiment 2 provides；
Fig. 4 is the electrical control structure schematic diagram for the controller that the utility model embodiment 3 provides；
Fig. 5 is the electrical control structure schematic diagram for the controller that the utility model embodiment 4 provides；
Fig. 6 is the electrical control structure schematic diagram for the controller that the utility model embodiment 5 provides.
Icon：100- reactors；110- cylinders；112- accommodating cavities；114- feed pipes；116- discharge nozzles；118- expands
Slot；The first temperature monitors of 120-；150- mixing components；152- agitating shafts；154- agitating paddles；170- helix tubes；172- is fed
Section；174- spiral sections；176- discharging sections；178- second temperature detectors；190- heating components；192- heaters；202- first
Solenoid valve；204- second solenoid valves；206- controllers；302- controllers；402- controllers；502- controllers.
Specific implementation mode
It is new below in conjunction with this practicality to keep the purpose, technical scheme and advantage of the utility model embodiment clearer
Attached drawing in type embodiment, the technical scheme in the utility model embodiment is clearly and completely described, it is clear that is retouched
The embodiment stated is the utility model a part of the embodiment, instead of all the embodiments.Usually here described in attached drawing and
The component of the utility model embodiment shown can be arranged and be designed with a variety of different configurations.
Therefore, the detailed description of the embodiments of the present invention to providing in the accompanying drawings is not intended to limit requirement below
The scope of the utility model of protection, but it is merely representative of the selected embodiment of the utility model.Based in the utility model
Embodiment, the every other embodiment that those of ordinary skill in the art are obtained without creative efforts, all
Belong to the range of the utility model protection.
It should be noted that：Similar label and letter indicate similar terms in following attached drawing, therefore, once a certain Xiang Yi
It is defined, then it further need not be defined and explained in subsequent attached drawing in a attached drawing.
In the description of the utility model embodiment, it should be noted that if there is term "upper", "lower", "inner", "outside"
The orientation or positional relationship of equal instructions is to be based on the orientation or positional relationship shown in the drawings or the utility model product uses
When the orientation or positional relationship usually put, be merely for convenience of describing the present invention and simplifying the description, rather than indicate or
It implies that signified device or element must have a particular orientation, with specific azimuth configuration and operation, therefore should not be understood as
Limitations of the present invention.In addition, term " first ", " second " etc. be only used for distinguish description, and should not be understood as instruction or
Imply relative importance.
In the description of the utility model embodiment, it is also necessary to which explanation is unless specifically defined or limited otherwise, if
Appearance term " setting ", " installation ", " connected ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, can also be
It is detachably connected, or is integrally connected；It can be directly connected, can also can be indirectly connected through an intermediary two
Connection inside element.For the ordinary skill in the art, above-mentioned term can be understood in this practicality with concrete condition
Concrete meaning in novel.
Embodiment 1
Fig. 1 is please referred to, Fig. 1 show the structural schematic diagram of reactor 100.The present embodiment provides a kind of reactor 100,
It is mainly used for providing reacting environment and suitable reaction condition for chemical reaction.
Reactor 100 includes cylinder 110, mixing component 150 and helix tube 170.Mixing component 150 and helix tube 170
It is arranged inside cylinder 110, and mixing component 150 is surround by helix tube 170.
Cylinder 110 limits accommodating cavity 112.As shown in Figure 1, helix tube 170 is arranged in accommodating cavity 112, helix tube
170 both ends are run through cylinder 110 and are extended to outside cylinder 110.Mixing component 150 is arranged in accommodating cavity 112, and by spiral shell
Coil 170 is surround.Fig. 2 is please referred to, Fig. 2 show the A direction views of Fig. 1.In the present embodiment, cylinder 110 is cylinder, other realities
Applying the shape of a middle cylinder body 110 can be changed, but when the shape of cylinder 110 is identical as the shape that helix tube 170 is formed, and change
Thermal effect is more preferable.
In the present embodiment, accommodating cavity 112 is for containing heat transferring medium, and helix tube 170 is for containing reaction mass.It can profit
Reaction mass is heated up or cooled down with heat transferring medium, so that reaction mass is under suitable reaction temperature.Helix tube
170 can in a limited space under the conditions of increase heat transferring medium and reaction mass heat exchange area, improve heat exchange efficiency.If reaction
Temperature residing for material is still not ideal enough, can further use mixing component 150 and stir heat transferring medium, enhance heat transferring medium
With the heat convection of reaction mass, to make reaction mass be in more suitably temperature range.Certainly, in other embodiments
Accommodating cavity 112 can be contained to reaction mass, helix tube 170 contains heat transferring medium.
Referring again to Fig. 1, cylinder 110 is also associated with feed pipe 114 and discharge nozzle 116, is convenient for the charging of heat transferring medium
And discharging.The one end of feed pipe 114 far from cylinder 110 is further provided with expansion slot 118, the diameter of expansion slot 118 be more than into
The diameter of expects pipe 114.Expansion slot 118, feed pipe 114, accommodating cavity 112 and discharge nozzle 116 are sequentially communicated.Expansion slot 118
The phenomenon that setting can effectively prevent heat transferring medium heat transferring medium caused by volume expansion to be overflowed from feed pipe 114.
Further, the first temperature monitor 120 can also be installed on cylinder 110.First temperature monitor 120 is used for
Detect the temperature of heat transferring medium in accommodating cavity 112.First temperature monitor 120 can be further disposed at close to helix tube
170 position allows the operator to more accurately understand so that its measurement is close to the temperature of the heat transferring medium of helix tube 170
Exchange heat situation.Operating personnel can judge the temperature of heat transferring medium according to the first temperature signal that the first temperature monitor 120 is fed back
Whether degree is suitable, to judge whether to need to take corresponding measure.For example, if the reaction of known response material is exothermic reaction,
And the testing result of the first temperature monitor 120 shows that heat transferring medium has no heating trend, then illustrates that heat transfer effect is bad at this time,
Unlatching mixing component 150 is needed to be stirred, to enhance heat exchange.In strong exothermal reaction, generally first reaction mass is carried out
Heating, makes reaction mass reach reaction temperature, and reaction mass very exothermic in reaction process later is just needed to anti-at this time
Should quickly it cool down, to reduce side reaction.The lower heat transferring medium of temperature, mixing component 150 can be passed through in temperature-fall period
Stirring be carried out at the same time the cooling that can accelerate to reaction.If the reaction of known response material is the endothermic reaction, and the first temperature
The testing result of detector 120 shows that heat transferring medium has no cooling trend, then illustrates that heat transfer effect is bad at this time, needs to open and stir
It mixes component 150 to be stirred, to enhance heat exchange；Or first temperature monitor 120 testing result show heat exchange medium temperature
Through being less than reaction temperature needed for reaction mass, then needs to increase the flow of heat transferring medium by feed pipe 114 while importing temperature
Higher than the heat transferring medium of reaction temperature, to ensure the origin of heat of reaction mass.
Mixing component 150 includes the agitating shaft 152 being connected with each other and agitating paddle 154, and agitating shaft 152 and agitating paddle 154 are equal
It is surround in accommodating cavity 112, and by helix tube 170.The mixing effect of agitating shaft 152 and agitating paddle 154 can cover
On whole helical lengths of helix tube 170.Agitating paddle 154 is rectangle in the present embodiment.In other embodiment, agitating paddle 154 can
To be other shapes, such as it can be the preferable shape of the mixing effects such as serpentine, spiral shape, anchor slab shape.Such as select spiral
It is band-like, it, will in whipping process if the hand of spiral of spiral shape agitating paddle 154 is identical as the hand of spiral of helix tube 170
The uniformity that heat transferring medium is contacted with helix tube 170 is further increased, to improve the temperature-controllable and temperature of reaction mass
Uniformity.
The rotation of agitating shaft 152 drives agitating paddle 154 to exchange thermal medium and is stirred.The rotation of agitating shaft 152 can be people
Work manual operation is rotated, and can also be driven and be rotated by motor.In order to improve the degree of automation and the life of reactor 100
Efficiency is produced, selects motor that agitating shaft 152 is driven to be rotated in the present embodiment.By the one end of agitating shaft 152 far from agitating paddle 154
It is connected with the output shaft of motor, the rotation of agitating shaft 152 is driven by the rotation of output shaft.
Helix tube 170 includes sequentially connected feed zone 172, spiral section 174 and discharging section 176.Feed zone 172 and go out
Material section 176 runs through cylinder 110 and extends to outside cylinder 110, is convenient for the charging and discharging of reaction mass.It agitating shaft 152 and stirs
Paddle 154 is mixed to be surround by spiral section 174.Discharging section 176 is further fitted with for detecting reaction mass temperature in discharging section 176
Second temperature detector 178.The mounting means of second temperature detector 178 can be directly inserted in discharging section 176.Reaction
Material is mainly reacted in spiral section 174, therefore no matter the reaction is the endothermic reaction or exothermic reaction, reaction mass
When flowing to discharging section 176, the reaction of reaction mass has tended to be steady or has been completed substantially reaction.Therefore, in discharging section 176
Reaction mass temperature is more stablized, and second temperature detector 178 is arranged in discharging section 176 being capable of more accurately reaction response material
Heat exchange situation it is whether good.The testing result fed back by second temperature detector 178, can judge whether to need to reinforce
The heat dissipation of reaction mass or the heating of reaction mass.For example, if the temperature that second temperature detector 178 detects compares reaction mass
Preset temperature it is higher, operating personnel then need to take unlatching to stir or be passed through the measures such as the lower heat transferring medium of temperature；If inspection
Testing temperature is relatively low, then needs that unlatching is taken to stir or be passed through the measures such as the higher heat transferring medium of temperature.
Certainly, in other embodiment, second temperature detector 178 can also be installed on feed zone 172, spiral section 174.
Such as multiple second temperature detectors 178 can be equidistantly installed on spiral section 174, with anti-in comprehensive monitoring spiral section 174
Answer the reaction temperature of material.Key reaction section of the spiral section 174 as reaction mass, the monitoring of internal temperature is to reacting especially
It is important.Second temperature detector 178 can be directly inserted in spiral section 174.
Reactor 100 can further include heating component 190.In the present embodiment, heating component 190 is installed on cylinder
110 bottoms, and the heater 192 of heating component 190 is located in accommodating cavity 112.As shown in Figure 1, heater 192 is positioned at close
One end of 110 bottom of cylinder, agitating shaft 152 are located at one end close to 110 top of cylinder with agitating paddle 154, when reaction mass needs
When heating up, the stirring heat conduction on 110 top of cylinder and 192 heat conduction of heater of lower part act on simultaneously, not only enable reaction mass
It is enough rapidly heated, additionally it is possible to improve the heating uniformity of each position reaction mass in spiral section 174, improve reaction yield.
In the present embodiment, heater 192 can be surround by spiral section 174.The setting is more advantageous to heater 192 to spiral
Section 174 is evenly heated, and the temperature uniformity of reaction mass is improved.Certainly, in other embodiment, the position of heater 192
It can also adjust accordingly.
Heating component 190 includes power supply, to be electrically heated to heater 192.Heater 192 can be Si-Mo rod,
The common heater element such as Elema, ceramic rod.
The operation principle of reactor 100 is：
Can heat transferring medium first be imported by feed pipe 114, so that heat transferring medium is flooded spiral section 174, discharge nozzle 116 can
First to close.Reaction mass is imported by feed zone 172 by certain flow rate, reaction mass will flow to discharging section along spiral section 174
176.Reaction mass will carry out heat exchange after entering spiral section 174 with the heat transferring medium outside spiral section 174.It is examined by the first temperature
The testing result for surveying instrument 120 and second temperature detector 178 takes corresponding measure, improves the control of reaction mass reaction temperature
Precision.
If the temperature detected by second temperature detector 178 is higher than the reaction temperature of preset reaction mass, and first
The temperature that temperature monitor 120 detects can be opened less than the temperature detected by second temperature detector 178, then operating personnel
The rotation of agitating shaft 152 is opened, agitating paddle 154 is stirred, and the convection current for reinforcing reaction mass and heat transferring medium is conducted heat.Or also may be used
To open discharge nozzle 116, and the lower heat transferring medium of temperature is imported by feed pipe 114.
If the temperature detected by second temperature detector 178 is higher than the reaction temperature of preset reaction mass, and first
The temperature that temperature monitor 120 detects is being opened higher than the temperature detected by second temperature detector 178, then operating personnel
While stirring, it is also necessary to open discharge nozzle 116, and the lower heat transferring medium of temperature is imported by feed pipe 114, make accommodating cavity
Fast quick-recovery reaction mass required temperature environment in 112.
If the temperature detected by second temperature detector 178 is less than the reaction temperature of preset reaction mass, and first
The temperature that temperature monitor 120 detects can be opened higher than the temperature detected by second temperature detector 178, then operating personnel
The rotation of agitating shaft 152 is opened, agitating paddle 154 is stirred, and the convection current for reinforcing reaction mass and heat transferring medium is conducted heat.Or also may be used
To open heating component 190, so that heater 192 is exchanged thermal medium and heated, quickly improve the temperature of reaction mass.
If the temperature detected by second temperature detector 178 is less than the reaction temperature of preset reaction mass, and first
The temperature that temperature monitor 120 detects can be opened less than the temperature detected by second temperature detector 178, then operating personnel
Stirring is opened, while opening heating component 190.Or discharge nozzle 116 can also be opened simultaneously, and temperature is imported by feed pipe 114
Higher heat transferring medium, two kinds of heating modes, which are carried out at the same time, makes reaction mass be rapidly heated to preset temperature.
The present embodiment also provides a kind of chemical producing system (not shown), including reactor 100, with higher life
Produce efficiency and production capacity.
Embodiment 2
The present embodiment provides a kind of reactors, and the reactor 100 provided with embodiment 1 is essentially identical, the difference of the two
It is：
Fig. 3 is please referred to, Fig. 3 show the electrical control structure schematic diagram of controller 206.On the reactor of the present embodiment also
Including the first solenoid valve 202, second solenoid valve 204 and controller 206.Certainly, two solenoid valves are intended only as control valve
A kind of selection can also replace two solenoid valves with other kinds of electrically-controlled valve, can realize electric control valve aperture.Other
If manual modulation valve door aperture need to be used in embodiment, two electromagnetism can also be replaced with manual valves such as ball valve, gate valve, butterfly valves
Valve.
First solenoid valve, 202 (not shown in figure 1) is set on feed pipe 114, second solenoid valve is set on discharge nozzle 116
204 (not shown in figure 1)s.Aperture by adjusting the first solenoid valve 202 can adjust the feed rate of heat transferring medium, pass through tune
The aperture of section second solenoid valve 204 can adjust the discharging flow of heat transferring medium.Certainly, feed rate and discharging flow must phases
Matching, otherwise will appear the situation that heat transferring medium is excessive or very few in accommodating cavity 112, is unfavorable for the safety of reactor.
First solenoid valve 202, second solenoid valve 204 and second temperature detector 178 are electrically connected with controller 206.
The preset temperature needed for reaction mass is preset in controller 206.Controller 206 is for receiving second temperature detector 178
The temperature signal of feedback simultaneously compares temperature signal and preset temperature, and controller 206 is used for according to comparing result adjustment the
The aperture of one solenoid valve 202 and/or second solenoid valve 204.
If temperature signal feedback temperature be higher than preset temperature, controller 206 by the first solenoid valve of adjust automatically 202 and/
Or the aperture of second solenoid valve 204, as long as heat transferring medium can be made to increase in the replacement speed on the surface spiral section 174 (see Fig. 1),
It can reach the effect of adjustment reaction mass temperature.For example, the aperture of two solenoid valves can be made to increase, or appropriate increase
The aperture of first solenoid valve 202, the appropriate aperture for reducing second solenoid valve 204.In the case of this kind, dissipated using heat transferring medium
Heat.
If temperature signal feedback temperature be less than preset temperature, controller 206 by the first solenoid valve of adjust automatically 202 and/
Or the aperture of second solenoid valve 204, as long as heat transferring medium can be made to slow down in the replacement speed on the surface spiral section 174 (see Fig. 1),
It can reach the effect of adjustment reaction mass temperature.For example, suitably reducing the aperture of second solenoid valve 204.In the case of this kind, profit
It is heated with heat transferring medium.
The present embodiment also provides a kind of chemical producing system, including above-mentioned reactor, with higher production efficiency and
Production capacity.
Embodiment 3
The present embodiment provides a kind of reactors, and the reactor 100 provided with embodiment 1 is essentially identical, the difference of the two
It is：
Fig. 4 is please referred to, Fig. 4 show the electrical control structure schematic diagram of controller 302.On the reactor of the present embodiment also
Including controller 302.
Controller 302 is electrically connected with heating component 190 (see Fig. 1) and second temperature detector 178 (see Fig. 1) respectively.
The preset temperature needed for reaction mass is preset in controller 302.Controller 302 is for receiving second temperature detector 178
The temperature signal of feedback simultaneously compares temperature signal and preset temperature, and controller 302 is used to be added according to comparing result adjustment
The heating power of hot component 190.
If the temperature of temperature signal feedback is less than preset temperature, controller 302 controls heating component 190 and opens, and root
Suitable heating power is selected according to temperature gap.If heating component 190 has been in open state, controller 302 is according to temperature
Spend the heating power of difference adjustment heating component 190.Temperature gap is bigger, and the heating power needed is bigger.
If the temperature of temperature signal feedback is higher than preset temperature, controller 302 controls heating component 190 and closes or reduce
Heating power.
The present embodiment also provides a kind of chemical producing system, including above-mentioned reactor, with higher production efficiency and
Production capacity.
Embodiment 4
The present embodiment provides a kind of reactors, and the reactor 100 provided with embodiment 1 is essentially identical, the difference of the two
It is：
Fig. 5 is please referred to, Fig. 5 show the electrical control structure schematic diagram of controller 402.On the reactor of the present embodiment also
Including controller 402.
First temperature monitor 120, second temperature detector 178 and mixing component 150 electrically connect with controller 402
It connects.Controller 402 is used to receive the first temperature signal of the first temperature monitor 120 feedback, receives second temperature detector 178
The second temperature signal of feedback, and the first temperature signal and second temperature signal are compared, controller 402 is used for according to right
Than the mixing speed that result adjusts mixing component 150.Controller 402 can be by controlling the rotating speed of motor to control stirring group
The mixing speed of part 150.
If there are difference, controllers 402 for the temperature that the temperature of second temperature signal feedback is fed back with the first temperature signal
The mixing speed of mixing component 150 will be suitably adjusted according to the size of difference, difference is bigger, and mixing speed is bigger, anti-to enhance
The heat transfer effect of device is answered, the heating or cooling of spiral section 174 (see Fig. 1) are accelerated.
The present embodiment also provides a kind of chemical producing system, including above-mentioned reactor, with higher production efficiency and
Production capacity.
Embodiment 5
The present embodiment provides a kind of reactors, and the reactor 100 provided with embodiment 1 is essentially identical, the difference of the two
It is：
Fig. 6 is please referred to, Fig. 6 show the electrical control structure schematic diagram of controller 502.On the reactor of the present embodiment also
Including controller 502.
Controller 502 is electrically connected with mixing component 150 and second temperature detector 178 respectively.In controller 502 in advance
Set the preset temperature needed for reaction mass.Controller 502 is used to receive the temperature signal of the feedback of second temperature detector 178 simultaneously
Temperature signal and preset temperature are compared, controller 502 is used to adjust the stirring speed of mixing component 150 according to comparing result
Degree.
If the temperature of temperature signal feedback is with preset temperature there are difference, controller 502 improves stirring for mixing component 150
Speed is mixed, to accelerate the heating or cooling of spiral section 174 (see Fig. 1).
The present embodiment also provides a kind of chemical producing system, including above-mentioned reactor, with higher production efficiency and
Production capacity.
The preferred embodiment that these are only the utility model, is not intended to limit the utility model, for this field
Technical staff for, various modifications and changes may be made to the present invention.Within the spirit and principle of the utility model,
Any modification, equivalent replacement, improvement and so on should be included within the scope of protection of this utility model.
Claims (13)
1. a kind of reactor, which is characterized in that including：
Cylinder, the cylinder limit accommodating cavity；
Helix tube, the helix tube are arranged in the accommodating cavity, and the both ends of the helix tube are run through the cylinder and prolonged
It extends to outside the cylinder；And
Mixing component, the mixing component setting are surround in the accommodating cavity, and by the helix tube.
2. reactor according to claim 1, it is characterised in that：
The cylinder is for accommodating heat transferring medium, and the helix tube is for accommodating reaction mass.
3. reactor according to claim 1, it is characterised in that：
The helix tube is equipped with the first temperature monitor for detecting temperature in the helix tube.
4. reactor according to claim 3, it is characterised in that：
The helix tube includes sequentially connected feed zone, spiral section and discharging section, and the discharging section is equipped with for detecting
First temperature monitor of temperature, the mixing component are surround by the spiral section in the discharging section.
5. reactor according to claim 3, it is characterised in that：
The cylinder is connected with feed pipe and discharge nozzle, and the first control valve, the discharge nozzle setting second is arranged in the feed pipe
Control valve.
6. reactor according to claim 5, it is characterised in that：
The reactor further includes controller, and first control valve and second control valve are electrically-controlled valve；Described first
Control valve, second control valve and first temperature monitor are electrically connected with the controller, and the controller is used
In the first temperature signal for receiving first temperature monitor feedback and by first temperature signal and the controller
Preset temperature is compared, and the controller is used to adjust first control valve and/or second control according to comparing result
The aperture of valve processed.
7. reactor according to claim 3, it is characterised in that：
The cylinder is connected with heating component, and the heater of the heating component is located in the accommodating cavity.
8. reactor according to claim 7, it is characterised in that；
The reactor further includes controller, and the controller is electric with the heating component and first temperature monitor respectively
Property connection, the controller is used to receive the first temperature signal of first temperature monitor feedback and by first temperature
The preset temperature of signal and the controller is compared, and the controller is used to adjust the heating component according to comparing result
Heating power.
9. reactor according to claim 3, it is characterised in that：
The cylinder is equipped with the second temperature detector for detecting temperature in the accommodating cavity.
10. reactor according to claim 9, it is characterised in that：
The second temperature detector is close to the helix tube.
11. reactor according to claim 9, it is characterised in that：
The reactor further includes controller, first temperature monitor, the second temperature detector and the stirring group
Part is electrically connected with the controller, and the controller is used to receive the first temperature letter of the first temperature monitor feedback
Number, the second temperature signal of the second temperature detector feedback is received, and first temperature signal is warm with described second
Degree signal is compared, and the controller is used to adjust the mixing speed of the mixing component according to comparing result.
12. reactor according to claim 3, it is characterised in that：
The reactor further includes controller, and the controller is electric with the mixing component and first temperature monitor respectively
Property connection, the controller is used to receive the first temperature signal of first temperature monitor feedback and by first temperature
The preset temperature of signal and the controller is compared, and the controller is used to adjust the mixing component according to comparing result
Mixing speed.
13. a kind of chemical producing system, it is characterised in that：
Including such as claim 1-12 any one of them reactor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721893488.0U CN207823021U (en) | 2017-12-28 | 2017-12-28 | A kind of reactor and chemical producing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721893488.0U CN207823021U (en) | 2017-12-28 | 2017-12-28 | A kind of reactor and chemical producing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207823021U true CN207823021U (en) | 2018-09-07 |
Family
ID=63390668
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721893488.0U Active CN207823021U (en) | 2017-12-28 | 2017-12-28 | A kind of reactor and chemical producing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207823021U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107999012A (en) * | 2017-12-28 | 2018-05-08 | 山东豪迈化工技术有限公司 | A kind of reactor and chemical producing system |
| CN110013818A (en) * | 2019-05-22 | 2019-07-16 | 山东豪迈机械制造有限公司 | A kind of agitating shaft and tubular reactor |
| CN111912102A (en) * | 2020-07-08 | 2020-11-10 | 杭州量动自动化设备有限公司 | Fluid heating device using secondary medium and using method thereof |
-
2017
- 2017-12-28 CN CN201721893488.0U patent/CN207823021U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107999012A (en) * | 2017-12-28 | 2018-05-08 | 山东豪迈化工技术有限公司 | A kind of reactor and chemical producing system |
| CN107999012B (en) * | 2017-12-28 | 2024-04-26 | 山东豪迈化工技术有限公司 | Temperature control method of reactor |
| CN110013818A (en) * | 2019-05-22 | 2019-07-16 | 山东豪迈机械制造有限公司 | A kind of agitating shaft and tubular reactor |
| CN111912102A (en) * | 2020-07-08 | 2020-11-10 | 杭州量动自动化设备有限公司 | Fluid heating device using secondary medium and using method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN207823021U (en) | A kind of reactor and chemical producing system | |
| CN107999012A (en) | A kind of reactor and chemical producing system | |
| WO2017197804A1 (en) | Supercritical multifunctional micro-nano colloid preparation device | |
| CN106512909B (en) | A kind of sectional temperature-controlled reactor and its agitating shaft | |
| JP2013151621A (en) | Apparatus and method for synthesizing resin | |
| KR20090010168U (en) | Structure for installing of thermometer measuring device in homo mixer | |
| KR101531859B1 (en) | Agitator capable of heating and cooling liquid material agitated | |
| CN107812469A (en) | Full-automatic magnetic stirring apparatus for chemical experiment | |
| CN203400723U (en) | Heating device of antifoaming agent reaction kettle | |
| CN104492355A (en) | Exothermic reaction device and method for accurately determining temperature in reaction process | |
| CN208537997U (en) | Microwave chemical thermostatic control system | |
| KR101711790B1 (en) | Slushie making device and method | |
| CN207546393U (en) | Heating refrigeration mixing all-in-one machine | |
| CN207307862U (en) | Oiliness polyurethane synthesis system | |
| CN210584697U (en) | Chemical circulating stirrer | |
| CN206642724U (en) | Continuous acylation synthesizes the device of pretilachlor | |
| CN109701475A (en) | A kind of liquid material microwave-ultrasonic coupling processing unit, equipment and application | |
| CN206065349U (en) | A kind of electromagnetic mixing apparatus of semi-solid metal slurry | |
| CN109289600A (en) | A kind of multifunctional mixer of Highgrade integration | |
| CN215087091U (en) | Low-temperature reaction device for preparing graphene oxide | |
| CN104474941A (en) | Stirring tank | |
| CN203227495U (en) | Rotary type combined reaction kettle | |
| CN210573429U (en) | Circulation accuse temperature constant temperature bath | |
| CN106925196A (en) | A kind of microwave heating equipment of High-Sr granite | |
| CN207769700U (en) | Magnetic stirring apparatus for low sticky degree solution |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |