CN208850666U - A kind of tobacco cutting secondary charging make-up water supply control system - Google Patents
A kind of tobacco cutting secondary charging make-up water supply control system Download PDFInfo
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- CN208850666U CN208850666U CN201821512432.0U CN201821512432U CN208850666U CN 208850666 U CN208850666 U CN 208850666U CN 201821512432 U CN201821512432 U CN 201821512432U CN 208850666 U CN208850666 U CN 208850666U
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Abstract
A kind of tobacco cutting secondary charging make-up water supply control system, it is characterized by: devising two independent charging water pipes after former pipeline is come out from flowmeter, newly-increased Pneumatic three-way valve one, Pneumatic three-way valve two, Pneumatic three-way valve five, dual-medium nozzle A, B can form two independent charging water pipes with the stainless steel tube pipeline that links together;Pneumatic three-way valve one, Pneumatic three-way valve for feed liquid conduit head tank second is that switch;Pneumatic three-way valve is fifth is that production and the switching of pre-filled pipeline.Moisturizing devise quantitative water compensating and in proportion moisturizing meet different process requirement;It realizes and the dual circuit of Feed lines is selected in production, energy flexible Application, pipeline switching can be carried out by such as encountering equipment fault in production, realize in production not fracture;It can guarantee equipment continuous production and tobacco leaf formulation integrality.
Description
Technical field
The utility model belongs to technical field of tobacco, and material can be real during secondary punishment in advance during tobacco leaf production
Water but also Loading Control System more particularly to a kind of tobacco cutting secondary charging make-up water supply control system can now be added.
Background technique
During cigarette primary processing, secondary charging is one of the key link of technology for making tobacco threds process.Existing secondary charging is set
Standby is to set feed ratio according to cigarette product, and feed liquid is accurately uniformly mixed and is fitted in blade, technology for making tobacco threds requirement is met.State
The drawbacks of feed way that interior current secondary charging uses, which can only meet, equally to feed or adds water, and the two cannot be simultaneously.It is now full
Sufficient product processes diversification and requires proposition that can feed and can add in secondary charging equipment the different of product processing technique
Water realizes quantitative watering simultaneously and adds the handoff functionality of water function and batch can and Feed lines in proportion.Carrying out secondary moisturizing
Also practical stability dries the moisture before silk in journey, to realize that the stabilization of cut-tobacco drier slab temperatures plays a key effect.Add to realize
This function of work diversification need to redesign pipe-line system and control system.The pipe-line system of general charging (feeding) equipment domestic at present
It is as follows with the working principle of control system:
Pipe-line system: pipe-line system includes water supply pipe, steam pipework, Feed lines and pneumatics pipeline.Feed lines: by
Agitator, solenoid valve, filter, gear pump, flowmeter, thermometer, pressure gauge, the composition such as dual-medium nozzle.For to material
Charging.Charging (feeding) equipment work: pre-filled first, feed liquid is from agitator by solenoid valve, and filter, gear pump operation is feed liquid
Indentation Feed lines are returned in agitator by triple valve.Feed liquid is always in Feed lines cycle operation when pre-filled.Work as material
Triple valve commutation feed liquid enters dual-medium nozzle after into feed rollers, while steam valve opens atomization feed liquid and sprays into roller to object
Material injection.It is domestic at present there was only a set of Feed lines in Feed lines design, moisturizing is carried out while being unable to satisfy charging.
Feed machine control system, and the control principle of country's charger is that electronic scale send the supplied materials flow signal measured at present
To after electric-control system processing, gained setting feeding quantity is compared with the practical feeding quantity that mass flowmenter is examined after handling
Frequency converter output frequency is controlled, to change charge pump motor speed, the flow tracking electronic scale for the feed liquid for exporting pump measures leaf
Piece flow and calculate theoretical feeding quantity, reach the automatic control to feed in proportion.Existing control program can only control charging
It can not achieve the logic switch for moisturizing accurately being controlled and being controlled charging water pipe.It in summary will be to Feed lines and program
It redesigns.
Utility model content
The purpose of this utility model is to be realized by providing a set of new property pipe-line system and new control program in secondary punishment in advance
When can feed, while also can moisturizing.It can also feed, one is selected in both moisturizings.
Pipe-line system technical solution is as follows: (1) increasing Pneumatic three-way valve one, five He of Pneumatic three-way valve two and Pneumatic three-way valve newly
Feed return pipe and connecting line.The circuit A(B) is linked into A(B) batch can composition A(B) pipeline independent loop.It is described increased
Device meets charging moisturizing requirement.One routing batch can A, Pneumatic two-way valve one, Pneumatic two-way valve two, A pump, A flowmeter, pneumatic three
Port valve five, A pipeline, Pneumatic three-way valve one, Pneumatic three-way valve two, dual-medium nozzle A are constituted.Another way is by batch can B, the first two-way
Valve, the second two-port valve, B pump, B flowmeter, Pneumatic three-way valve six, Pneumatic three-way valve three, Pneumatic three-way valve four, dual-medium nozzle B
It constitutes.Two independent pipelines are constituted in this way.
A kind of tobacco cutting secondary charging make-up water supply control system, it is characterised in that: batch can A by the first pipeline/A pipeline with
Pneumatic three-way valve five connects, be connected on the first pipeline Pneumatic two-way valve one, Pneumatic two-way valve two, filter, A pump, pressure gauge,
A flowmeter, the first triple valve, dual-medium nozzle A a port are connect by pipeline with Pneumatic three-way valve five, dual-medium nozzle A
Another port is connect by pipeline with steam;Pneumatic three-way valve five is connect by A pipeline with sewage draining exit, is connected on loop pipe A
Pneumatic three-way valve one, Pneumatic three-way valve two;Piping connection between one end and filter and A pump of first bypass two-port valve, separately
Piping connection between one end and A flowmeter and the first triple valve, first triple valve one end are connect with metering sample tap;
Batch can B is connect by the second pipeline/B pipeline with Pneumatic three-way valve six, be connected on the second pipeline the first two-port valve,
Second two-port valve, filter, B pump, pressure gauge, B flowmeter, the second triple valve, dual-medium nozzle B a port by pipeline with
Pneumatic three-way valve six connects, and the another port dual-medium nozzle B is connect by pipeline with steam;Pneumatic three-way valve six passes through B pipeline
It is connect with sewage draining exit, Pneumatic three-way valve three, Pneumatic three-way valve four is connected on B pipeline;One end of second bypass two-port valve and mistake
Piping connection between filter and B pump, the piping connection between the other end and B flowmeter and the second triple valve, the second triple valve
One end is connect with metering sample tap;
One one end of Pneumatic three-way valve is connect with Pneumatic three-way valve three, batch can A respectively by pipeline, two one end of Pneumatic three-way valve
It is connect respectively with Pneumatic three-way valve four, batch can B by pipeline.
Wherein, compressed air is connect by third pipeline with third triple valve one end, be connected on third pipeline two-port valve,
Filter, pressure reduction control valve, flow control valve;
Water source is connect by the 4th pipeline with third triple valve one end, and two-port valve, pressure release control are connected on the 4th pipeline
Valve, flow control valve, pressure-control valve, the other both ends of third triple valve respectively with the first pipeline/A pipeline, the second pipeline/B
Piping connection;
Steam is connect by the first branched pipe with batch can B, and two-port valve, pressure-control valve, pressure are connected on the first branched pipe
Power table, steam are connect by second branched pipe with batch can A, and two-port valve, pressure-control valve, pressure are connected in second branched pipe
Table, steam are connect by third branched pipe with the condensation mouth of a river, and steam passes through the 4th branched pipe and the 4th piping connection, the 4th pipeline
On be connected with two-port valve, flow control valve, pressure gauge;
Agitating device is provided in batch can A, batch can B, agitating device includes motor, drive shaft, is provided with one in drive shaft
A or multiple agitator arms, batch can A, the periphery batch can B are provided with temperature control device, for controlling temperature in batch can A, batch can B.
It further include control system, touch screen, operation button, control system includes PID module, feedback proportional module, operation
Module.
Optionally, the pneumatic T-type triple-valve body is stainless steel 304 material.
Optionally, the Feed lines are stainless steel 304 material.
The opening and closing of newly-increased Pneumatic three-way valve need to be controlled by pneumatics pipeline from the above mentioned, and the pneumatics valve island of charger have it is pre-
It leaves a blank pressure electromagnetic valve.The control Pneumatic three-way valve pneumatic tube added is connected to pneumatics valve island module and carries out logic control.
Compared with prior art, the utility model has the advantage that
1, the utility model tobacco cutting secondary charging method for supplementing water meets the diversity requirements of production technology.Preferably
It solves to be different product, different formulations offer can feed can also moisturizing selection scheme.
2, moisturizing devise quantitative water compensating and in proportion moisturizing meet different process requirement.
3, it realizes and the dual circuit of Feed lines is selected in production, energy flexible Application such as encounters equipment in production
Failure can carry out pipeline switching, realize in production not fracture.It can guarantee equipment continuous production and tobacco leaf formulation integrality.
4, moisturizing proportionality coefficient and feedback moisturizing proportionality coefficient energy flexible modulation rate of water make-up are set in parameter list, reaches technique
It is required that.
5, accurate moisturizing accurately calculate realize dry silk before moisture stabilization, to realize cut-tobacco drier slab temperatures
Stabilization play a key effect.Secondary moisturizing is to qualification rate 100%, cpk value > 1%.
Detailed description of the invention
Fig. 1 is the part piping diagram connecting in the utility model with dual-medium nozzle A, dual-medium nozzle B;
Fig. 2 is the utility model pipeline integrated connection figure;
Fig. 3 is the utility model moisturizing A tank control logic figure;
Fig. 4 is the utility model moisturizing B tank control logic figure;
Fig. 5 is the pre-filled moisturizing PID control schematic diagram of the utility model;
Fig. 6 is the utility model quantitative water compensating PID control schematic diagram;
Fig. 7 is the utility model moisturizing PID control schematic diagram in proportion.
In figure: 1, the first two-port valve, the 2, second two-port valve, 3, Pneumatic two-way valve one, 4, Pneumatic two-way valve two, 5, pneumatic three
Port valve one, 6, Pneumatic three-way valve two, 7, Pneumatic three-way valve three, 8, Pneumatic three-way valve four, 9, Pneumatic three-way valve five, 10, pneumatic three
Port valve six, 11, dual-medium nozzle A, 12, dual-medium nozzle B, 13, A pipeline, 14, B pipeline, 15, batch can A, 16, batch can B, 17,
Compressed air, 18, steam, 19, water source, 20, A flowmeter, 21, A pump, 22, B flowmeter, 23, B pump, the 24, first triple valve,
25, the second triple valve, 26, third triple valve, the 27, first bypass two-port valve, the 28, second bypass two-port valve.
Specific embodiment
The embodiments of the present invention is described in detail with reference to the accompanying drawing.
It is as shown in Figs. 1-2: a kind of novel Feed lines design pipeline connecting figure.The charging water pipe includes batch can A15,
Batch can B16, A pump 21, B pump 23, A flowmeter 20, B flowmeter 22, dual-medium nozzle A11, dual-medium nozzle B12, Pneumatic three-way
Valve, Pneumatic two-way valve, the composition such as three-way connection.1: changing pipeline: devising two after former pipeline is come out from flowmeter and independently add
Expect water pipe.Newly-increased Pneumatic three-way type valve 1, Pneumatic three-way valve 26, Pneumatic three-way valve 59, dual-medium nozzle A11 and double
Medium nozzle B12 can form two independent charging water pipes with the stainless steel tube pipeline that links together.Pneumatic three-way valve
One 5, Pneumatic three-way valve 26 is for the switching of feed liquid conduit head tank.Pneumatic three-way valve 59 is that production and pre-filled pipeline are cut
It changes.Specifically: a routing feed pot A15, Pneumatic two-way valve 1, Pneumatic two-way valve 24, A pump 21, A flowmeter 20, pneumatic three
Port valve 59, A pipeline, Pneumatic three-way valve 1, Pneumatic three-way valve 26, dual-medium nozzle A11 are constituted.Another way feed pot B16,
First two-port valve 1, the second two-port valve 2, B pump 23, B flowmeter 22, Pneumatic three-way valve 6 10, Pneumatic three-way valve 37, Pneumatic three-way
Valve 48, dual-medium nozzle B12 are constituted.As shown in Figs. 1-2.
Specifically: batch can A15 is connect by the first pipeline/A pipeline 13 with Pneumatic three-way valve 59, connected on the first pipeline/
It is connected with Pneumatic two-way valve 1, Pneumatic two-way valve 24, filter, A in turn and pumps 21, pressure gauge, A flowmeter 20, the first threeway
Valve 24,11 a port of dual-medium nozzle A are connect by pipeline with Pneumatic three-way valve 59,11 another port dual-medium nozzle A
It is connect by pipeline with steam 18;Pneumatic three-way valve 59 is connect by A pipeline 13 with sewage draining exit, is connected in turn on A pipeline 13
Pneumatic three-way valve 1, Pneumatic three-way valve 26;Pipeline between one end and filter and A pump 21 of first bypass two-port valve 27 connects
It connects, the piping connection between the other end and A flowmeter 20 and the first triple valve 24,24 one end of the first triple valve and metering sample tap
Connection.
Batch can B16 is connect by the second pipeline/B pipeline 14 with Pneumatic three-way valve 6 10, connect/is successively connected on the second pipeline
It is connected to the first two-port valve 1, the second two-port valve 2, filter, B and pumps 23, pressure gauge, B flowmeter 22, the second triple valve 25, double media
12 a port of nozzle B connect by pipeline with Pneumatic three-way valve 6 10,12 another port dual-medium nozzle B pass through pipeline and
Steam 18 connects;Pneumatic three-way valve 6 10 is connect by B pipeline 14 with sewage draining exit, is connected with Pneumatic three-way valve in turn on B pipeline
37, Pneumatic three-way valve 48;Piping connection between one end and filter and B pump 23 of second bypass two-port valve 28, the other end
With the piping connection between B flowmeter 22 and the second triple valve 25,25 one end of the second triple valve is connect with metering sample tap.
One 5 one end of Pneumatic three-way valve is connect with Pneumatic three-way valve 37, batch can A15 respectively by pipeline, Pneumatic three-way valve two
6 one end are connect with Pneumatic three-way valve 48, batch can B16 respectively by pipeline.
Compressed air 17 is connect by third pipeline with 26 one end of third triple valve, is connected/is sequentially connected on third pipeline
There are two-port valve, filter, pressure reduction control valve, flow control valve.
Water source 19 is connect by the 4th pipeline with 26 one end of third triple valve, connected on the 4th pipeline/it is connected with two in turn
Port valve, unloading pressure control valve, flow control valve, pressure-control valve, the other both ends of third triple valve 26 respectively with the first pipeline/A
Pipeline 13, the second pipeline/B pipeline 14 connect.
Steam is connect by the first branched pipe with batch can B16, be connected on the first branched pipe two-port valve, pressure-control valve,
Pressure gauge etc., steam are connect by second branched pipe with batch can A15, be connected in second branched pipe two-port valve, pressure-control valve,
Pressure gauge etc., steam are connect by third branched pipe with the condensation mouth of a river, and steam passes through the 4th branched pipe and the 4th piping connection, the
Two-port valve, flow control valve, pressure gauge etc. are connected on four pipelines.
Agitating device is provided in batch can A15, batch can B16, agitating device includes motor, drive shaft, is arranged in drive shaft
There are one or more agitator arms, batch can A15, the periphery batch can B16 are provided with temperature control device, for controlling batch can A15, batch can
Temperature in B16.Batch can periphery is provided with the liquid level sensor of numerical display type, for showing, observing liquid level;The electricity of agitating device
Machine is variable ratio frequency changer speed regulating motor, and the operating status and revolving speed of agitating device can be according to the use states of batch can, such as whether discharging, liquid
The running speed of the adjustings control agitating device such as position height, temperature level.
All valves are preferably electromagnetic type control valve, can also partially be electromagnetic type control valve in pipeline, partially mechanically to control
Valve processed.
It is required to write valve logic control program and moisturizing control program according to control:
In control touch screen picture addition such as lower button and control parameter:
A.1 it needs to make quantitative watering in touch screen with Tia according to system control and adds water by control touch screen in proportion
Button selection.
A.2 it is needed to add water select button in touch screen production A pipeline 13 plus water and B pipeline 14 with Tia according to system control,
The charging of A pipeline 13 and the charging select button of B pipeline 14.Its function is that B pipeline 14 may be selected while selection A pipeline 13 plus water
Charging is controlled, and A pipeline 13 may be selected while selecting B pipeline 14 plus water and feed.Pipeline when two kinds of different feed liquid additions
It cannot switch.Pipeline selection can be carried out according to practical condition when selecting A pipeline 13 plus water, A pipeline 13 may be selected and also select
B pipeline 14 is selected, it can be to the switching of pipeline in pre-filled and production.It can also be according to practical life when selecting B pipeline 14 plus water
It produces situation and carries out pipeline selection, A pipeline 13 may be selected and also select B pipeline 14, it can be to the switching of pipeline in pre-filled and production.
Realize batch can two-way choice and the two-way choice of pipeline.
A.3 it is needed to increase by 13 moisturizing proportionality coefficient ka value of A pipeline in touch panel device parameter list with Tia according to system control
Moisturizing ratio value ka1 is fed back with A pipeline 13;14 moisturizing proportionality coefficient kb value of B pipeline and B pipeline 14 feed back moisturizing ratio value kb1;
Moisture content of outlet setting value M3;The pre-filled setting value C1 of 13 moisturizing of A pipeline, the pre-filled setting value C2. of 14 moisturizing of B pipeline
A.4 program is required to run charging control program when selection has charging according to control;Moisturizing journey is run when having moisturizing
Sequence.Both of which feeds sometimes, and moisturizing program is run simultaneously.
Pneumatic operated valve is controlled by charger pneumatics valve island.According to production by row's selection batch can, Feed lines, choosing when tool application
Water pipe is selected, control logic such as Fig. 3,4: in work, feed pot and selection charging or water pipe being selected according to production requirement.
According to blade total amount and plus or moisturizing material ratio adds the charging liquid of appropriate weight or batch can is added in water.Production before to charger into
Row preheating, and to the pre-filled of pipeline.Program is by automatic running when charger is run.
Moisturizing control principle when pre-filled and production:
(1) the pre-filled control of moisturizing is carried out before blade feeds intake:
Selected according to actual process, system program is by A pipeline 13, the pre-filled numerical value C1(C2 of B pipeline 14) it is used as moisturizing stream
Amount setting value and A pipeline 13,14 actual flow meter instantaneous flow value YA(B of B pipeline) it carries out PID arithmetic and adjusts to obtain charging pumping frequency
Rate, closed-loop control when formation one is pre-filled.The pre-filled setting value C1 of 13 moisturizing of this example A pipeline is 40kg/h;B pipeline 14
The pre-filled setting value C2 of moisturizing is 40kg/h.
(2) moisturizing control is carried out when blade produces:
The blade instantaneous flow generated when blade material flows through weighing belt carries out blade instantaneous flow by program flat
Blade instantaneous flow smooth value Q is calculated in cunning;Blade generates entrance moisture value and to entrance moisture when passing through entrance Moisture Meter
Value carries out smoothing computation and obtains entrance moisture value smooth value M1, and blade is by producing saliva score value and to out when moisture content of outlet instrument
Saliva score value carries out smoothing computation and obtains moisture content of outlet value smooth value M2.
When it is implemented, selecting quantitative water compensating according to the condition of production and in proportion moisturizing button, program will be by select buttons
Situation carries out logic control.Moisturizing will carry out calculating control by following working principle.This example blade instantaneous flow 3000kg/h;
Entrance moisture 17.5%;Moisture content of outlet setting 19.0%.Moisturizing Proportional coefficient K a(b);Moisturizing ratio calculations are fed back according to reality
The condition of production is set.This example is 13 moisturizing Proportional coefficient K a0.6 of A pipeline;A pipeline 13 feeds back moisturizing ratio calculations
ka10.05.
Accurate moisturizing calculation formula:
B.1 quantitative watering calculation formula is carried out according to blade mass flow:
A(B) pipeline quantitative water compensating setting value F1=(weighing belt instantaneous flow smooth value Q × moisturizing Proportional coefficient K a(b))/
100
B.2 A(B) moisturizing definite value F2 calculates step to pipeline in proportion:
C1: moisture difference N1=(moisture content of outlet smooth value M2.- entrance moisture smooth value M1)/100-moisture content of outlet are flat
Sliding value M2.
C2: rate of water make-up N2=N1 × weighing belt instantaneous flow smooth value Q × moisturizing proportionality coefficient k+ theory amount of water F3
C3: by calculate saliva set up separately definite value M3 and practical moisture content of outlet smooth value M2.PID operation obtained it is program-controlled
Amount cv value W1 processed
C4: theoretical amount of water F3=process control amount cv value W1 × feedback moisturizing ratio calculations k1
C5: rate of water make-up N2 with actual flow meter flow through instantaneous value YA(B) carry out PID adjust operation control obtain charge pump fortune
Line frequency, moisturizing closed-loop control when forming production.
Field Production Data table (moisturizing in proportion):
Technological parameter | Maximum value | Minimum value | Average value | Qualification rate | Standard deviation | CPK |
Secondary discharging moisture | 19.12 | 18.77 | 18.97 | 100 | 0.06 | 2.84 |
Secondary feeds moisture | 18.61 | 17.44 | 18.20 | 99.81 | 0.11 | 1.19 |
Above embodiment is the explanation to the utility model, is not the restriction to the utility model, it is possible to understand that not
These embodiments can be carried out with a variety of variations, modification, replacement in the case where being detached from the principles of the present invention and spirit and become
Type, the protection scope of the utility model are defined by the appended claims and the equivalents thereof.
Claims (4)
1. a kind of tobacco cutting secondary charging make-up water supply control system, it is characterised in that: batch can A(15) pass through the first pipeline/A pipeline
(13) it is connect with Pneumatic three-way valve five (9), Pneumatic two-way valve one (3), Pneumatic two-way valve two (4), mistake is connected on the first pipeline
Filter, A pump (21), pressure gauge, A flowmeter (20), the first triple valve (24), dual-medium nozzle A(11) a port passes through pipe
Road is connect with Pneumatic three-way valve five (9), and (11) another port dual-medium nozzle A is connect by pipeline with steam (18);Pneumatic three
Port valve five (9) is connect by A pipeline (13) with sewage draining exit, and Pneumatic three-way valve one (5), Pneumatic three-way valve two are connected on A pipeline
(6);Piping connection between one end and filter and A pump (21) of first bypass two-port valve (27), the other end and A flowmeter
(20) piping connection between the first triple valve (24), the first triple valve (24) one end are connect with metering sample tap;
Batch can B(16) it is connect with Pneumatic three-way valve six (10) by the second pipeline/B pipeline (14), the is connected on the second pipeline
One two-port valve (1), the second two-port valve (2), filter, B pump (23), pressure gauge, B flowmeter (22), the second triple valve (25), double
Medium nozzle B(12) a port connect by pipeline with Pneumatic three-way valve six (10), dual-medium nozzle B (12) another port
It is connect by pipeline with steam (18);Pneumatic three-way valve six (10) is connect by B pipeline (14) with sewage draining exit, on B pipeline (14)
It is connected with Pneumatic three-way valve three (7), Pneumatic three-way valve four (8);One end of second bypass two-port valve (28) and filter and B pump
(23) piping connection between, the piping connection between the other end and B flowmeter (22) and the second triple valve (25), the second threeway
Valve (25) one end is connect with metering sample tap;
Pneumatic three-way valve one (5) one end by pipeline respectively with Pneumatic three-way valve three (7), batch can A(15) connect, Pneumatic three-way valve
Two (6) one end by pipeline respectively with Pneumatic three-way valve four (8), batch can B(16) connect.
2. a kind of tobacco cutting secondary charging make-up water supply control system according to claim 1, compressed air (17) passes through third
Pipeline is connect with third triple valve (26) one end, and two-port valve, filter, pressure reduction control valve, flow control are connected on third pipeline
Valve processed;
Water source (19) is connect by the 4th pipeline with third triple valve (26) one end, is connected with two-port valve, pressure release on the 4th pipeline
Control valve, flow control valve, pressure-control valve, the other both ends of third triple valve (26) respectively with the first pipeline/A pipeline
(13), the second pipeline/B pipeline (14) connection;
Steam (18) is connect by the first branched pipe with batch can B(16), and two-port valve, pressure control are connected on the first branched pipe
Valve, pressure gauge, steam (18) are connect by second branched pipe with batch can A(15), and two-port valve, pressure are connected in second branched pipe
Control valve, pressure gauge, steam are connect by third branched pipe with the condensation mouth of a river, and steam is connected by the 4th branched pipe and the 4th pipeline
It connects, is connected with two-port valve, flow control valve, pressure gauge on the 4th pipeline;
Batch can A(15), batch can B(16) in be provided with agitating device, agitating device includes motor, drive shaft, is arranged in drive shaft
Have one or more agitator arms, batch can A(15), batch can B(16) periphery is provided with temperature control device, for controlling batch can A(15),
Batch can B(16) interior temperature.
3. a kind of tobacco cutting secondary charging make-up water supply control system according to claim 1 further includes control system, touches
Screen, operation button, control system includes PID module, feedback proportional module, computing module.
4. a kind of tobacco cutting secondary charging make-up water supply control system according to claim 1, each Pneumatic three-way valve material is not
Become rusty steel 304 or 316 materials, and each connecting line material is stainless steel 304 or 316 materials.
Priority Applications (1)
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CN201821512432.0U CN208850666U (en) | 2018-09-17 | 2018-09-17 | A kind of tobacco cutting secondary charging make-up water supply control system |
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CN201821512432.0U CN208850666U (en) | 2018-09-17 | 2018-09-17 | A kind of tobacco cutting secondary charging make-up water supply control system |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN110427061A (en) * | 2019-08-01 | 2019-11-08 | 北京新长征天高智机科技有限公司 | A kind of control system and method for tobacco production |
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2018
- 2018-09-17 CN CN201821512432.0U patent/CN208850666U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110427061A (en) * | 2019-08-01 | 2019-11-08 | 北京新长征天高智机科技有限公司 | A kind of control system and method for tobacco production |
CN110427061B (en) * | 2019-08-01 | 2021-07-13 | 北京新长征天高智机科技有限公司 | Control system and method for tobacco production |
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