CN107379712B - Corrugated paper board production line Intelligent Composite temperature-controlling system - Google Patents

Corrugated paper board production line Intelligent Composite temperature-controlling system Download PDF

Info

Publication number
CN107379712B
CN107379712B CN201710571653.9A CN201710571653A CN107379712B CN 107379712 B CN107379712 B CN 107379712B CN 201710571653 A CN201710571653 A CN 201710571653A CN 107379712 B CN107379712 B CN 107379712B
Authority
CN
China
Prior art keywords
tracheae
pressure
temperature
air inlet
sensor
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
Application number
CN201710571653.9A
Other languages
Chinese (zh)
Other versions
CN107379712A (en
Inventor
陶军
李启坤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sichuan Changhong Electric Co Ltd
Original Assignee
Sichuan Changhong Electric Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sichuan Changhong Electric Co Ltd filed Critical Sichuan Changhong Electric Co Ltd
Priority to CN201710571653.9A priority Critical patent/CN107379712B/en
Publication of CN107379712A publication Critical patent/CN107379712A/en
Application granted granted Critical
Publication of CN107379712B publication Critical patent/CN107379712B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B37/00Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
    • B32B37/06Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the heating method
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B41/00Arrangements for controlling or monitoring lamination processes; Safety arrangements

Abstract

The invention discloses a kind of corrugated paper board production line Intelligent Composite temperature-controlling systems, it includes boiler, single-side machine subelement, Double-plate machine subelement and PLC, the gas outlet of boiler is connected to single-side machine subelement and Double-plate machine subelement respectively by main steam pipe, the air inlet of boiler is connected to single-side machine subelement and Double-plate machine subelement respectively by main air inlet pipe, the steam that boiler generates first passes through main steam pipe and respectively enters single-side machine subelement and Double-plate machine subelement, boiler is back to by main air inlet pipe using after single-side machine subelement and Double-plate machine subelement, corrugated paper board production line Intelligent Composite temperature-controlling system provided by the invention, first pass through internal pipe pressure feedback closed loop, make system quick response, the pressure in each pipeline is set to reach basic settings requirement.Then by temperature feedback closed loop, the steam pressure of links is adjusted again, so that the corrugated board in production process is in most suitable processing temperature always in key position, to improve the processing quality of corrugated board.

Description

Corrugated paper board production line Intelligent Composite temperature-controlling system
Technical field
The present invention relates to corrugated board production technical fields, and in particular to a kind of corrugated paper board production line Intelligent Composite temperature control System.
Background technique
Corrugated paper board production line needs certain high temperature in the production process that body paper is processed into corrugated board, this Temperature generates steam generally by boiler, is provided using the heat of steam.
Traditional corrugated paper board production line, at various locations all without temperature, the detection of pressure, control feedback unit.For Guarantee process conditions required for producing, it can only be using excessively with by the way of vapour.
This will lead to the temperature that the temperature during corrugated board production is higher than fluting medium paper production line, cause to produce The loss of body paper moisture in the process then absorbs water in single-side machine and bond locations, causes the moisture imbalance of each layer body paper, make body paper Become fragile and reduce due ring pressure and resistance to broken ability, generates the deterioration of body paper physical property, cause cardboard out-of-flatness, be easy quick-fried line.
Summary of the invention
The present invention overcomes corrugated paper board production lines in the prior art all to exist at various locations without temperature, pressure detecting The deficiency for reducing corrugated board processing quality provides one kind by pressure, temperature detection, PLC is utilized to control production institute The optimized temperature needed improves the corrugated paper board production line Intelligent Composite temperature-controlling system of production quality.
In order to solve the above technical problems, the invention adopts the following technical scheme:
A kind of corrugated paper board production line Intelligent Composite temperature-controlling system, it includes boiler, single-side machine subelement, two-sided loom list The gas outlet of member and PLC, the boiler are connected to single-side machine subelement and Double-plate machine subelement respectively by main steam pipe, described The air inlet of boiler is connected to single-side machine subelement and Double-plate machine subelement respectively by main air inlet pipe, the steaming that the boiler generates Vapour first passes through main steam pipe and respectively enters single-side machine subelement and Double-plate machine subelement, using single-side machine subelement and Double-plate machine Boiler is back to by main air inlet pipe after subelement;
The single-side machine subelement includes single-side machine, flash tank, facial tissue preheating cylinder and watt paper preheating cylinder, the single-side machine Air inlet is connected to by the first tracheae with main steam pipe, and the first servo valve and drain valve are equipped on first tracheae, described The gas outlet of single-side machine is connected to by the second tracheae with the air inlet of flash tank, and first pressure biography is equipped on second tracheae Sensor and drain valve, the first pressure sensor is for acquiring the second endotracheal pressure F1, the discharge port of the single-side machine First temperature sensor is installed, first temperature sensor is for acquiring single-side machine discharge port position single face corrugated board The gas outlet of temperature T1, the flash tank are connected to by third tracheae and the 4th tracheae with the air inlet of facial tissue preheating cylinder, described The gas outlet of facial tissue preheating cylinder be connected to by the 6th tracheae with main air inlet pipe, the gas outlet of the flash tank pass through third tracheae with 8th tracheae is connected to a watt air inlet for paper preheating cylinder, and the gas outlet of described watt of paper preheating cylinder passes through the 7th tracheae and main air inlet pipe It is connected to, second pressure sensor is installed on the third tracheae, the second pressure sensor is intratracheal for acquiring third Pressure F2, third servo valve and drain valve are installed on the 4th tracheae, third pressure is installed on the 6th tracheae Sensor and drain valve, the third pressure sensor are used to acquire the 6th endotracheal pressure F3, the facial tissue preheating cylinder Discharge port is equipped with second temperature sensor, and the second temperature sensor is used to acquire the folder of facial tissue preheating cylinder discharge port position Insides or in temperature T2 after paper preheating, the 4th servo valve and drain valve, the 7th tracheae are installed on the 8th tracheae On the 4th pressure sensor and drain valve be installed, the 4th pressure sensor for acquiring the 7th endotracheal pressure F4, The discharge port of described watt of paper preheating cylinder is equipped with third temperature sensor, and the third temperature sensor is for acquiring a watt paper preheating Temperature T3 after watt paper preheating of cylinder discharge port position, is also equipped with the first high pressure compensation tracheae by the single-side machine, and described the One high pressure compensation tracheae one end is connected to main steam pipe, and the other end is connected to third tracheae, on the first high pressure compensation tracheae Second servo valve and drain valve are installed, the flash tank also passes through the 5th tracheae and is connected to main air inlet pipe;
The Double-plate machine subelement includes drying tunnel hot plate, flash tank and bonding preheating cylinder, the air inlet of the drying tunnel hot plate It is connected to by the 9th tracheae with main steam pipe, the 5th servo valve and drain valve, the drying tunnel heat is installed on the 9th tracheae The gas outlet of plate is connected to by the tenth tracheae with the air inlet of flash tank, is equipped with the 5th pressure sensor on the tenth tracheae And drain valve, for acquiring the tenth endotracheal pressure F5, the gas outlet of the flash tank passes through the 5th pressure sensor 11st tracheae and the 12nd tracheae are connected to the air inlet of bonding preheating cylinder, and the gas outlet of the bonding preheating cylinder passes through the tenth Three tracheaes are connected to main air inlet pipe, and the 6th pressure sensor, the 6th pressure sensor are equipped on the 11st tracheae 7th servo valve and drain valve be installed for acquiring the 11st endotracheal pressure F6, on the 12nd tracheae, described the 7th pressure sensor and drain valve are installed, the 7th pressure sensor is intratracheal for acquiring the 13rd on 13 tracheaes Pressure F7, the discharge port of the bonding preheating cylinder is equipped with the 4th temperature sensor, and the 4th temperature sensor is for adopting Collection bonds the temperature T4 after the facial tissue preheating of preheating cylinder discharge port position, is equipped with the second high pressure compensation gas by the drying tunnel hot plate Pipe, described second high pressure compensation tracheae one end are connected to main steam pipe, and the other end is connected to the 11st tracheae, second high pressure The 6th servo valve and drain valve are installed on compensation tracheae, the flash tank also passes through the 14th tracheae and is connected to main air inlet pipe;
The PLC respectively with the first servo valve, first pressure sensor, the first temperature sensor, the second servo valve, second Pressure sensor, third servo valve, third pressure sensor, second temperature sensor, the 4th servo valve, the 4th pressure sensing Device, third temperature sensor, the 5th servo valve, the 5th pressure sensor, the 6th servo valve, the 6th pressure sensor, the 7th watch Valve, the 7th pressure sensor and the electrical connection of the 4th temperature sensor are taken, and it is endotracheal default that second is prestored in the PLC The endotracheal preset pressure F2 of pressure F1, the preset temperature T1 of single face corrugated board, third, the 6th endotracheal preset pressure F3, sandwich paper or in preset temperature after preset temperature T2 after paper preheating, the 7th endotracheal preset pressure F4, the preheating of watt paper T3, the tenth endotracheal preset pressure F5, the 11st endotracheal preset pressure F6, the 13rd endotracheal preset pressure F7, Preset temperature T4 after facial tissue preheating, the PLC are used to receive the pressure and temperature of each sensor acquisition, and by received pressure Power and temperature are compared with preset pressure and temperature, and control each servo valve
Further technical solution is that the quantity of the drying tunnel hot plate is three, and the air inlet of three drying tunnel hot plates is equal Be connected to respectively with main steam pipe by the 9th tracheae, the gas outlet of three drying tunnel hot plates pass through the tenth tracheae respectively with flash tank Air inlet connection, and be mounted on the 5th servo valve and drain valve on three the 9th tracheaes, pacify on three the tenth tracheaes Equipped with the 5th pressure sensor and drain valve.
Further technical solution is that the bonding preheating cylinder is three, and the air inlet of three bonding preheating cylinders is logical It crosses the 12nd tracheae to be connected to the 11st tracheae, three bonding preheating cylinder gas outlets pass through the 13rd tracheae and main air inlet pipe connects It is logical, and the 7th servo valve and drain valve are mounted on three the 12nd tracheaes, the is mounted on three the 13rd tracheaes The discharge port of seven pressure sensors and drain valve, three bonding preheating cylinders is mounted on the 4th temperature sensor.
Further technical solution is also to be communicated with gluing preheating device on the 11st tracheae.
Compared with prior art, the beneficial effects of the present invention are:
Corrugated paper board production line Intelligent Composite temperature-controlling system provided by the invention first passes through internal pipe pressure feedback and closes Ring makes system quick response, and the pressure in each pipeline is made to reach basic settings requirement.Then by temperature feedback closed loop, then The steam pressure of secondary adjustment links, makes the corrugated board in production process be in most suitable processing always in key position Temperature, to improve the processing quality of corrugated board.
Detailed description of the invention
Fig. 1 is the structure chart of the corrugated paper board production line Intelligent Composite temperature-controlling system of an embodiment of the present invention.
Fig. 2 is the structure chart of single-side machine subelement in Fig. 1.
Fig. 3 is the structure chart of Double-plate machine subelement in Fig. 1.
As shown, wherein corresponding appended drawing reference title are as follows:
1 boiler, 2 main steam pipes, 3 main air inlet pipes, 4 single-side machine subelements, 41 first tracheaes, 42 first servo valves, 43 is single Face machine, 44 first pressure sensors, 45 second tracheaes, 46 third tracheaes, 47 third servo valves, 48 the 4th tracheaes, 49 the 5th gas Pipe, 410 facial tissue preheating cylinders, 411 third pressure sensors, 412 second temperature sensors, 413 the 6th tracheaes, 414 the 7th tracheaes, 415 third temperature sensors, 416 the 4th pressure sensors, 417 watts of paper preheating cylinders, 418 the 8th tracheaes, 419 the 4th servo valves, 420 second pressure sensors, 421 second servo valves, 422 first temperature sensors, 423 first high pressure compensation tracheaes, 5 return water Machine, 6 Double-plate machine subelements, 61 the 9th tracheaes, 62 the 5th servo valves, 63 second high pressure compensation tracheaes, 64 drying tunnel hot plates, 65 the 5th Pressure sensor, 66 the tenth tracheaes, 67 the 6th servo valves, 68 the 11st tracheaes, 69 the 6th pressure sensors, 610 the 12nd gas Pipe, 611 the 7th servo valves, 612 bonding preheating cylinders, 613 the 7th pressure sensors, 614 the 4th temperature sensors, 615 the 13rd Tracheae, 616 the 14th tracheaes, 7 drain valves, 8 flash tanks.
Specific embodiment
The present invention is further elaborated with reference to the accompanying drawing.
A kind of corrugated paper board production line Intelligent Composite temperature-controlling system as shown in Figs. 1-3, it includes boiler 1, single side loom Unit 4, Double-plate machine subelement 6 and PLC, the gas outlet of boiler 1 by main steam pipe 2 respectively with single-side machine subelement 4 and two-sided Loom unit 6 is connected to, and the air inlet of boiler 1 is connected with single-side machine subelement 4 and Double-plate machine subelement 6 respectively by main air inlet pipe 3 Logical, the steam that boiler 1 generates first passes through main steam pipe 2 and respectively enters single-side machine subelement 4 and Double-plate machine subelement 6, using Boiler 1 is back to by main air inlet pipe 3 after single-side machine subelement 4 and Double-plate machine subelement 6;
Single-side machine subelement includes single-side machine 43, flash tank 8, facial tissue preheating cylinder 410 and watt paper preheating cylinder 417, single-side machine 43 air inlet is connected to by the first tracheae 41 with main steam pipe 2, and the first servo valve 42 and hydrophobic is equipped on the first tracheae 41 Valve 7, the gas outlet of single-side machine 43 are connected to by the second tracheae 45 with the air inlet of flash tank 8, and the is equipped on the second tracheae 45 One pressure sensor 44 and drain valve 7, first pressure sensor 44 are used to acquire the pressure F1 in the second tracheae 45, single-side machine 43 Discharge port the first temperature sensor 422 is installed, the first temperature sensor 422 is for acquiring 43 discharge port position list of single-side machine The gas outlet of the temperature T1 of face corrugated board, flash tank 8 pass through third tracheae 46 and the 4th tracheae 48 and facial tissue preheating cylinder 410 The gas outlet of air inlet connection, facial tissue preheating cylinder 410 is connected to by the 6th tracheae 413 with main air inlet pipe 3, the outlet of flash tank 8 Mouth is connected to by third tracheae 46 and the 8th tracheae 418 with a watt air inlet for paper preheating cylinder 417, the outlet of watt paper preheating cylinder 417 Mouth is connected to by the 7th tracheae 414 with main air inlet pipe 3, and second pressure sensor 420, second pressure are equipped on third tracheae 46 Sensor 420 is used to acquire the pressure F2 in third tracheae 46, is equipped with third servo valve 47 and drain valve on the 4th tracheae 48 7, third pressure sensor 411 and drain valve 7 are installed, third pressure sensor 411 is for acquiring the 6th on the 6th tracheae 413 Pressure F3 in tracheae 413, the discharge port of facial tissue preheating cylinder 410 are equipped with second temperature sensor 412, second temperature sensor 412 for acquire 410 discharge port position of facial tissue preheating cylinder sandwich paper or in temperature T2 after paper preheating, on the 8th tracheae 418 4th servo valve 419 and drain valve 7 are installed, the 4th pressure sensor 416 and drain valve 7 are installed on the 7th tracheae 414, the Four pressure sensors 416 are used to acquire the pressure F4 in the 7th tracheae 414, and the discharge port of watt paper preheating cylinder 417 is equipped with third Temperature sensor 415, after third temperature sensor 415 is used to acquire watt paper preheating of watt 417 discharge port position of paper preheating cylinder Temperature T3 is also equipped with the first high pressure compensation tracheae 423,423 one end of the first high pressure compensation tracheae and main steam by single-side machine 43 Pipe 2 is connected to, and the other end is connected to third tracheae 46, and the second servo valve 421 and hydrophobic is equipped on the first high pressure compensation tracheae 423 Valve 7, flash tank 8 are also connected to by the 5th tracheae 49 with main air inlet pipe 3;
Double-plate machine subelement includes drying tunnel hot plate 64, flash tank 8 and bonding preheating cylinder 612, the air inlet of drying tunnel hot plate 64 It is connected to by the 9th tracheae 61 with main steam pipe 2, the 5th servo valve 62 and drain valve 7, drying tunnel heat is installed on the 9th tracheae 61 The gas outlet of plate 64 is connected to by the tenth tracheae 66 with the air inlet of flash tank 8, and the 5th pressure biography is equipped on the tenth tracheae 66 Sensor 65 and drain valve 7, the 5th pressure sensor 65 are used to acquire the pressure F5 in the tenth tracheae 66, the gas outlet of flash tank 8 It is connected to by the 11st tracheae 68 and the 12nd tracheae 610 with the air inlet of bonding preheating cylinder 612, bonding preheating cylinder 612 goes out Port is connected to by the 13rd tracheae 615 with main air inlet pipe 3, and the 6th pressure sensor 69 is equipped on the 11st tracheae 68, the Six pressure sensors 69 are used to acquire the pressure F6 in the 11st tracheae 68, are equipped with the 7th servo valve on the 12nd tracheae 610 611 and the 7, the 13rd tracheae 615 of drain valve on the 7th pressure sensor 613 and drain valve 7, the 7th pressure sensor are installed 613 for acquiring the pressure F7 in the 13rd tracheae 615, and the discharge port of bonding preheating cylinder 612 is equipped with the 4th temperature sensor 614, the 4th temperature sensor 614 is used to acquire the temperature T4 after the facial tissue preheating of bonding 612 discharge port position of preheating cylinder, drying tunnel Second high pressure compensation tracheae 63 is installed, 63 one end of the second high pressure compensation tracheae is connected to main steam pipe 2, the other end by hot plate 64 It is connected to the 11st tracheae 68, the 6th servo valve 67 and drain valve 7 is installed, flash tank 8 is also on second high pressure compensation tracheae 63 It is connected to by the 14th tracheae 616 with main air inlet pipe 3;
PLC respectively with the first servo valve 42, first pressure sensor 44, the first temperature sensor 422, the second servo valve 421, second pressure sensor 420, third servo valve 47, third pressure sensor 411, second temperature sensor the 412, the 4th are watched Take valve 419, the 4th pressure sensor 416, third temperature sensor 415, the 5th servo valve 62, the 5th pressure sensor 65, Six servo valves 67, the 6th pressure sensor 69, the 7th servo valve 611, the 7th pressure sensor 613 and the 4th temperature sensor 614 electrical connections, and the preset pressure F1 in the second tracheae 45, the preset temperature T1 of single face corrugated board, the are prestored in PLC Preset pressure F2 in three tracheaes 46, the preset pressure F3 in the 6th tracheae 413, sandwich paper or in paper preheating after preset temperature T2, the preset pressure F4 in the 7th tracheae 414, the preset temperature T3 after the preheating of watt paper, the preset pressure F5 in the tenth tracheae 66, Preset pressure F6 in 11st tracheae 68, the preset pressure F7 in the 13rd tracheae 615, the preset temperature after facial tissue preheating T4, PLC are used to receive the pressure and temperature of each sensor acquisition, and by received pressure and temperature and preset pressure and temperature Degree is compared, and controls each servo valve.
The working principle of the invention is specific as follows:
PLC receives the pressure F1 in the second tracheae 45 that first pressure sensor 44 acquires, and will be in the second tracheae 45 Pressure F1 is compared with the preset pressure F1 in the second tracheae 45, if when the pressure F1 in the second tracheae 45 is greater than the second gas When preset pressure F1 in pipe 45, PLC, which controls the first servo valve 42, reduces the vapor volume entered in the first tracheae 41, to make The value of pressure F1 is identical as the value of preset pressure F1 in the second tracheae 45 in second tracheae 45, if the pressure in the second tracheae 45 When power F1 is less than preset pressure F1 in the second tracheae 45, PLC, which controls the first servo valve 42, makes the steaming entered in the first tracheae 41 Tolerance increases, to keep the value of pressure F1 in the second tracheae 45 identical as the value of preset pressure F1 in the second tracheae 45;
PLC receives the pressure F2 in the third tracheae 46 that second pressure sensor 420 acquires, and will be in third tracheae 46 Pressure F2 is compared with the preset pressure F2 in third air inlet pipe 46, if when the pressure F2 in third tracheae 46 is greater than third When preset pressure F2 in air inlet pipe 46, PLC, which controls the second servo valve 421, to be made to enter the endotracheal vapor volume of the first high pressure compensation It reduces, thus keep the value of the pressure F2 in third tracheae 46 identical as the value of preset pressure F2 in third air inlet pipe 46, if When the pressure F2 in third tracheae 46 is less than the preset pressure F2 in third air inlet pipe 46, PLC, which controls the second servo valve 421, to be made Increase into the endotracheal vapor volume of the first high pressure compensation, to make the value and third air inlet pipe of the pressure F2 in third tracheae 46 The value of preset pressure F2 in 46 is identical;
PLC receives the pressure F3 in the 6th tracheae 413 that third pressure sensor 411 acquires, and will be in the 6th tracheae 413 Pressure F3 be compared with the preset pressure F3 in the 6th tracheae 413, if the pressure F3 in the 6th tracheae 413 is greater than the When preset pressure F3 in six tracheaes 413, PLC control third servo valve 47 reduces the vapor volume entered in the 4th tracheae 48, To keep the value of the pressure F3 in the 6th tracheae 413 identical as the value of preset pressure F3 in the 6th tracheae 413, if when the 6th When pressure F3 in tracheae 413 is less than preset pressure F3 in the 6th tracheae 413, PLC control third servo valve 47 makes to enter the Vapor volume in four tracheaes 48 increases, thus the value and the default pressure in the 6th tracheae 413 that make the pressure F3 in the 6th tracheae 413 The value of power F3 is identical;
PLC receives the pressure F4 in the 7th tracheae 414 of the 4th pressure sensor 416 acquisition, and will be in the 7th tracheae 414 Pressure F4 be compared with the preset pressure F4 in the 7th tracheae 414, if the pressure F4 in the 7th tracheae 414 is greater than the When preset pressure F4 in seven tracheaes 414, PLC, which controls the 4th servo valve 419, subtracts the vapor volume entered in the 8th tracheae 418 It is few, to keep the value of the pressure F4 in the 7th tracheae 414 identical as the value of preset pressure F4 in the 7th tracheae 414, if worked as When pressure F4 in 7th tracheae 414 is less than preset pressure F4 in the 7th tracheae 414, PLC control the 4th servo valve 419 make into The vapor volume entered in the 8th tracheae 418 increases, to make in value and the 7th tracheae 414 of the pressure F4 in the 7th tracheae 414 The value of preset pressure F4 is identical;
PLC receives the pressure F5 in the tenth tracheae 66 of the 5th pressure sensor 65 acquisition, and will be in the tenth tracheae 66 Pressure F5 is compared with the preset pressure F5 in the tenth tracheae 66, if when the pressure F5 in the tenth tracheae 66 is greater than the tenth gas When preset pressure F5 in pipe 66, PLC, which controls the 5th servo valve 62, reduces the vapor volume entered in the 9th tracheae 61, to make The value of pressure F5 in tenth tracheae 66 is identical as the value of preset pressure F5 in the tenth tracheae 66, if when in the tenth tracheae 66 Pressure F5 less than preset pressure F5 in the tenth tracheae 66 when, PLC, which controls the 5th servo valve 62, to be made to enter in the 9th tracheae 61 Vapor volume increase, to make the value phase of the value of the pressure F5 in the tenth tracheae 66 with the preset pressure F5 in the tenth tracheae 66 Together;
PLC receives the pressure F6 in the 11st tracheae 68 of the 6th pressure sensor 69 acquisition, and by the 11st tracheae 68 Interior pressure F6 is compared with the preset pressure F6 in the 11st tracheae 68, if the pressure F6 in the 11st tracheae 68 is big When preset pressure F6 in the 11st tracheae 68, PLC, which controls the 6th servo valve 67, to be made to enter in the second high pressure compensation tracheae 63 Vapor volume reduce, thus make the pressure F6 in the 11st tracheae 68 value and the 11st tracheae 68 in preset pressure F6 value It is identical, if when the pressure F6 in the 11st tracheae 68 is less than preset pressure F6 in the 11st tracheae 68, PLC control the 6th Servo valve 67 increases the vapor volume entered in the second high pressure compensation tracheae 63, to make the pressure F6's in the 11st tracheae 68 It is worth identical as the value of preset pressure F6 in the 11st tracheae 68;
PLC receives the pressure F7 in the 13rd tracheae 615 of the 7th pressure sensor 613 acquisition, and by the 13rd tracheae Pressure F7 in 615 is compared with the preset pressure F7 in the 13rd tracheae 615, if when the pressure in the 13rd tracheae 615 When power F7 is greater than the preset pressure F7 in the 13rd tracheae 615, PLC, which controls the 7th servo valve 611, to be made to enter the 12nd tracheae 610 Interior vapor volume is reduced, thus the value for making the pressure F7 in the 13rd tracheae 615 and the preset pressure F7 in the 13rd tracheae 615 Value it is identical, if when the pressure F7 in the 13rd tracheae 615 is less than preset pressure F7 in the 13rd tracheae 615, PLC control Making the 7th servo valve 611 increases the vapor volume entered in the 12nd tracheae 610, to make the pressure in the 13rd tracheae 615 The value of F7 is identical as the value of preset pressure F7 in the 13rd tracheae 615;
PLC receives the temperature T1 of the 43 discharge port position single face corrugated board of single-side machine of the first temperature sensor 422 acquisition, And be compared the temperature T1 of 43 discharge port position single face corrugated board of single-side machine with the preset temperature T1 of single face corrugated board, If when the temperature T1 of 43 discharge port position single face corrugated board of single-side machine is greater than the preset temperature T1, PLC of single face corrugated board Controlling the first servo valve 42 reduces the vapor volume entered in the first tracheae 41, due to the reduction of vapor volume, so making single-side machine The temperature of 43 processing reduces accordingly, so that it is single to be equal to the value of the temperature T1 of 43 discharge port position single face corrugated board of single-side machine The value of the preset temperature T1 of face corrugated board, if the temperature T1 when 43 discharge port position single face corrugated board of single-side machine is less than list The preset temperature T1 of face corrugated board, PLC, which controls the first servo valve 42, increases the vapor volume entered in the first tracheae 41, due to The increase of vapor volume, so the temperature for processing single-side machine 43 accordingly increases, to make 43 discharge port position single side of single-side machine The value of the temperature T1 of corrugated board is equal to the value of the preset temperature T1 of single face corrugated board;
PLC receive second temperature sensor 412 acquire the sandwich paper of 410 discharge port position of facial tissue preheating cylinder or in paper preheat Temperature T2 afterwards, and by the sandwich paper of 410 discharge port position of facial tissue preheating cylinder or in paper preheating after temperature T2 and sandwich paper or in Paper preheating after preset temperature T2 be compared, if when the sandwich paper of 410 discharge port position of facial tissue preheating cylinder or in paper preheating after Temperature T2 be greater than sandwich paper or in preset temperature T2 after paper preheating, PLC control third servo valve 47 makes to enter the 4th tracheae Vapor volume in 48 is reduced, due to the reduction of vapor volume, so the temperature for processing facial tissue preheating cylinder 410 reduces accordingly, from And make the sandwich paper of 410 discharge port position of facial tissue preheating cylinder or in paper preheating after temperature T2 value be equal to sandwich paper or in paper preheat The value of preset temperature T2 afterwards, if when the sandwich paper of 410 discharge port position of facial tissue preheating cylinder or in paper preheat after temperature T2 it is small In sandwich paper or in preset temperature T2 after paper preheating, PLC control third servo valve 47 makes the steam entered in the 4th tracheae 48 Amount increases, due to the increase of vapor volume, so the temperature for processing facial tissue preheating cylinder 410 increases accordingly, to keep facial tissue pre- The sandwich paper of hot 410 discharge port position of cylinder or in temperature T2 after paper preheating value be equal to sandwich paper or in default temperature after paper preheating Spend the value of T2;
PLC receives the temperature after 417 discharge port position watt paper of watt paper preheating cylinder preheating that third temperature sensor 415 acquires T3, and the temperature T3 and preset temperature T3 after watt paper preheating after the preheating of 417 discharge port position watt paper of watt paper preheating cylinder is carried out Compare, if the temperature T3 after preheating of 417 discharge port position watt paper of watt paper preheating cylinder is greater than the preset temperature after watt paper preheating T3, PLC, which control the 4th servo valve 419, reduces the vapor volume entered in the 8th tracheae 418, due to the reduction of vapor volume, so The temperature for processing watt paper preheating cylinder 417 reduces accordingly, thus after preheating 417 discharge port position watt paper of watt paper preheating cylinder The value of temperature T3 is equal to the value of the preset temperature T3 after watt paper preheating, if when 417 discharge port position watt paper of watt paper preheating cylinder is pre- Temperature T3 after heat is less than the preset temperature T3 after watt paper preheating, and PLC, which controls the 4th servo valve 419, to be made to enter the 8th tracheae 418 Interior vapor volume increases, due to the increase of vapor volume, so the temperature for processing watt paper preheating cylinder 417 accordingly increases, thus The value of temperature T3 after preheating 417 discharge port position watt paper of watt paper preheating cylinder is equal to the preset temperature T3's after watt paper preheating Value;
PLC receives the temperature after bonding 612 discharge port position facial tissue of the preheating cylinder preheating of the 4th temperature sensor 614 acquisition T4, and the temperature T4 after 612 discharge port position facial tissue of preheating cylinder preheats and the preset temperature T4 progress after facial tissue preheating will be bonded Compare, if temperature T4 after bonding the preheating of 612 discharge port position facial tissue of preheating cylinder is greater than the preset temperature after facial tissue preheats T4, PLC, which control the 7th servo valve 611, reduces the vapor volume entered in the 12nd tracheae 610, due to the reduction of vapor volume, institute So that the temperature that bonding preheating cylinder 612 is processed reduces accordingly, to make after bonding the preheating of 612 discharge port position facial tissue of preheating cylinder Temperature T4 value be equal to facial tissue preheating after preset temperature T4 value, if when bonding 612 discharge port position facial tissue of preheating cylinder Temperature T4 after preheating is greater than the preset temperature T4 after facial tissue preheating, and PLC, which controls the 7th servo valve 611, to be made to enter the 12nd tracheae Vapor volume in 610 increases, due to the increase of vapor volume, so the temperature for bonding the processing of preheating cylinder 612 is accordingly increased, from And the preset temperature T4 for being equal to the value for bonding the temperature T4 after the preheating of 612 discharge port position facial tissue of preheating cylinder after facial tissue preheating Value;
Corrugated paper board production line intelligence is formed by PLC, servo valve and pressure sensor cooperating first in the present embodiment Pressure feedback closed loop in the compound temperature-controlling system of energy is steamed by pressure feedback closed loop to realize and enter in each pipeline of control The size of tolerance, so that the pressure in each pipeline be made to be attained by the preset pressure of production requirement;
Secondly as different brackets, different grammes per square metre, the body paper performance of different suppliers have the characteristics that it is respective, to equipment Adaptability and requirement also have certain difference, along with the humidity in Various Seasonal temperature and air is all in continuous variation, pressure Force feedback closed loop can only meet product quality requirement to a certain extent, and what is had a direct impact to quality of corrugated is former In paper paper, sandwich paper, watt paper or facial tissue crucial Working position temperature, so, in the present embodiment by PLC, servo valve and Temperature sensor cooperating forms corrugated paper board production line and intelligently meets the temperature feedback closed loop in temperature-controlling system, passes through temperature Feedback closed loop controls single-side machine, facial tissue preheating cylinder, watt paper preheating cylinder, the amount into steam for bonding preheating cylinder, so that control is each The temperature of a working cell makes the temperature of the body paper of each unit discharge port meet preset processing temperature, thus raising watt The processing quality of corrugated paper board.
The above specific embodiment is described in detail for the essence of the present invention, but can not be to protection scope of the present invention It is limited, it should be apparent that, under the inspiration of the present invention, those of ordinary skill in the art can also carry out many improvement And modification, it should be noted that these improvement and modification are all fallen within the scope of the claims of the present invention.

Claims (4)

1. a kind of corrugated paper board production line Intelligent Composite temperature-controlling system, which is characterized in that it includes boiler (1), single side loom list First (4), Double-plate machine subelement (6) and PLC, the gas outlet of the boiler (1) by main steam pipe (2) respectively with single side loom list First (4) are connected to Double-plate machine subelement (6), the air inlet of the boiler (1) pass through main air inlet pipe (3) respectively with single side loom list First (4) are connected to Double-plate machine subelement (6), and the steam that the boiler (1) generates first passes through main steam pipe (2) and respectively enters single side Loom unit (4) and Double-plate machine subelement (6), using single-side machine subelement (4) and Double-plate machine subelement (6) afterwards by it is main into Tracheae (3) is back to boiler (1);
The single-side machine subelement (4) includes single-side machine (43), flash tank (8), facial tissue preheating cylinder (410) and watt paper preheating cylinder (417), the air inlet of the single-side machine (43) is connected to by the first tracheae (41) with main steam pipe (2), first tracheae (41) the first servo valve (42) and drain valve (7) are installed, the gas outlet of the single-side machine (43) passes through the second tracheae (45) on It is connected to the air inlet of flash tank (8), first pressure sensor (44) and drain valve is installed on second tracheae (45) (7), the first pressure sensor (44) is used to acquire the pressure F1 in the second tracheae (45), the discharging of the single-side machine (43) Mouth is equipped with the first temperature sensor (422), and first temperature sensor (422) is for acquiring single-side machine (43) discharge port position Set the temperature T1 of single face corrugated board, the gas outlet of the flash tank (8) by third tracheae (46) and the 4th tracheae (48) and The air inlet of facial tissue preheating cylinder (410) is connected to, and the gas outlet of the facial tissue preheating cylinder (410) passes through the 6th tracheae (413) and master The gas outlet of air inlet pipe (3) connection, the flash tank (8) is preheated by third tracheae (46) and the 8th tracheae (418) with watt paper The air inlet of cylinder (417) is connected to, and the gas outlet of described watt of paper preheating cylinder (417) passes through the 7th tracheae (414) and main air inlet pipe (3) It is connected to, is equipped with second pressure sensor (420) on the third tracheae (46), the second pressure sensor (420) is used for The pressure F2 in third tracheae (46) is acquired, third servo valve (47) and drain valve (7) are installed on the 4th tracheae (48), Third pressure sensor (411) and drain valve (7), the third pressure sensor are installed on the 6th tracheae (413) (411) for acquiring the pressure F3 in the 6th tracheae (413), the discharge port of the facial tissue preheating cylinder (410) is equipped with the second temperature It spends sensor (412), the second temperature sensor (412) is for acquiring the sandwich of facial tissue preheating cylinder (410) discharge port position Paper or in temperature T2 after paper preheating, the 4th servo valve (419) and drain valve (7), institute are installed on the 8th tracheae (418) It states and the 4th pressure sensor (416) and drain valve (7) is installed on the 7th tracheae (414), the 4th pressure sensor (416) For acquiring the pressure F4 in the 7th tracheae (414), the discharge port of described watt of paper preheating cylinder (417) is equipped with third temperature sensing Device (415), after the third temperature sensor (415) is used to acquire watt paper preheating of watt paper preheating cylinder (417) discharge port position Temperature T3, is also equipped with the first high pressure compensation tracheae (423), the first high pressure compensation tracheae by the single-side machine (43) (423) one end is connected to main steam pipe (2), and the other end is connected to third tracheae (46), the first high pressure compensation tracheae (423) On the second servo valve (421) and drain valve (7) be installed, the flash tank (8) also passes through the 5th tracheae (49) and main air inlet pipe (3) it is connected to;
The Double-plate machine subelement (6) includes drying tunnel hot plate (64), flash tank (8) and bonding preheating cylinder (612), the drying tunnel heat The air inlet of plate (64) is connected to by the 9th tracheae (61) with main steam pipe (2), is equipped with the 5th on the 9th tracheae (61) Servo valve (62) and drain valve (7), the gas outlet of the drying tunnel hot plate (64) by the tenth tracheae (66) and flash tank (8) into Port is connected to, and the 5th pressure sensor (65) and drain valve (7) are equipped on the tenth tracheae (66), and the 5th pressure passes Sensor (65) is used to acquire the pressure F5 in the tenth tracheae (66), and the gas outlet of the flash tank (8) passes through the 11st tracheae (68) it is connected to the 12nd tracheae (610) with the air inlet of bonding preheating cylinder (612), the outlet of bonding preheating cylinder (612) Mouth is connected to by the 13rd tracheae (615) with main air inlet pipe (3), is equipped with the 6th pressure sensing on the 11st tracheae (68) Device (69), the 6th pressure sensor (69) are used to acquire the pressure F6 in the 11st tracheae (68), the 12nd tracheae (610) the 7th servo valve (611) and drain valve (7) are installed on, the 7th pressure biography is installed on the 13rd tracheae (615) Sensor (613) and drain valve (7), the 7th pressure sensor (613) are used to acquire the pressure in the 13rd tracheae (615) The discharge port of F7, bonding preheating cylinder (612) are equipped with the 4th temperature sensor (614), the 4th temperature sensor (614) the temperature T4 after the facial tissue preheating for acquiring bonding preheating cylinder (612) discharge port position, the drying tunnel hot plate (64) are other Second high pressure compensation tracheae (63) is installed, the second high pressure compensation tracheae (63) one end is connected to main steam pipe (2), another End is connected to the 11st tracheae (68), is equipped with the 6th servo valve (67) and drain valve on the second high pressure compensation tracheae (63) (7), the flash tank (8) is also connected to by the 14th tracheae (616) with main air inlet pipe (3);
The PLC is watched with the first servo valve (42), first pressure sensor (44), the first temperature sensor (422), second respectively Take valve (421), second pressure sensor (420), third servo valve (47), third pressure sensor (411), second temperature sensing Device (412), the 4th servo valve (419), the 4th pressure sensor (416), third temperature sensor (415), the 5th servo valve (62), the 5th pressure sensor (65), the 6th servo valve (67), the 6th pressure sensor (69), the 7th servo valve (611), Seven pressure sensors (613) and the electrical connection of the 4th temperature sensor (614), and the second tracheae (45) are prestored in the PLC Preset temperature T1, the preset pressure F2 in third tracheae (46), the 6th tracheae of interior preset pressure F1, single face corrugated board (413) preset pressure F3, sandwich paper in or in the preset temperature T2 after paper preheating, the preset pressure in the 7th tracheae (414) Preset temperature T3, the preset pressure F5 in the tenth tracheae (66), the default pressure in the 11st tracheae (68) after F4, watt paper preheating Power F6, the preset pressure F7 in the 13rd tracheae (615), the preset temperature T4 after facial tissue preheating, the PLC are each for receiving The pressure and temperature of sensor acquisition, and received pressure and temperature is compared with preset pressure and temperature, and controls Each servo valve.
2. corrugated paper board production line Intelligent Composite temperature-controlling system according to claim 1, it is characterised in that the drying tunnel heat The quantity of plate (64) be three, the air inlet of three drying tunnel hot plates (64) pass through the 9th tracheae (61) respectively with main steam pipe (2) it is connected to, the gas outlet of three drying tunnel hot plates (64) passes through the tenth tracheae (66) and connects respectively with the air inlet of flash tank (8) It is logical, and the 5th servo valve (62) and drain valve (7) are mounted on three the 9th tracheaes (61), on three the tenth tracheaes (66) It is mounted on the 5th pressure sensor (65) and drain valve (7).
3. corrugated paper board production line Intelligent Composite temperature-controlling system according to claim 1, it is characterised in that the bonding is pre- Hot cylinder (612) is three, and the air inlet of three bondings preheating cylinder (612) passes through the 12nd tracheae (610) and the 11st tracheae (68) it being connected to, the gas outlet of three bondings preheating cylinder (612) passes through the 13rd tracheae (615) and is connected to main air inlet pipe (3), and And the 7th servo valve (611) and drain valve (7) are mounted on three the 12nd tracheaes (610), three the 13rd tracheaes (615) On be mounted on the 7th pressure sensor (613) and drain valve (7), the discharge ports of three bondings preheating cylinder (612) are mounted on 4th temperature sensor (614).
4. corrugated paper board production line Intelligent Composite temperature-controlling system according to claim 1, it is characterised in that the described 11st Tracheae is also communicated with gluing preheating device on (68).
CN201710571653.9A 2017-07-13 2017-07-13 Corrugated paper board production line Intelligent Composite temperature-controlling system Active CN107379712B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710571653.9A CN107379712B (en) 2017-07-13 2017-07-13 Corrugated paper board production line Intelligent Composite temperature-controlling system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710571653.9A CN107379712B (en) 2017-07-13 2017-07-13 Corrugated paper board production line Intelligent Composite temperature-controlling system

Publications (2)

Publication Number Publication Date
CN107379712A CN107379712A (en) 2017-11-24
CN107379712B true CN107379712B (en) 2019-07-19

Family

ID=60339500

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710571653.9A Active CN107379712B (en) 2017-07-13 2017-07-13 Corrugated paper board production line Intelligent Composite temperature-controlling system

Country Status (1)

Country Link
CN (1) CN107379712B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109283869B (en) * 2018-09-03 2021-04-06 南通达成包装制品有限公司 Corrugated board production control system
CN109094116A (en) * 2018-09-20 2018-12-28 青岛立合环保科技有限公司 A kind of corrugated paper board production line temperature control system
CN110281594A (en) * 2019-07-26 2019-09-27 临沂兴华包装有限公司 High speed corrugated board wire temperature production method and vapour system
CN110820398B (en) * 2019-10-23 2022-07-08 浙江荣晟环保纸业股份有限公司 Production system of dampproofing corrugated paper that intelligent degree is high

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201264390Y (en) * 2008-08-04 2009-07-01 唐蕾 Single layer corrugated paper jointing heating automatic control device for corrugated production line
CN202898901U (en) * 2012-10-23 2013-04-24 福建省文松彩印有限公司 Energy-saving emission-reducing corrugated board heating system
CN106042460A (en) * 2016-07-26 2016-10-26 昆山鸣朋纸业有限公司 Corrugated paper board production line
CN106903931A (en) * 2017-02-24 2017-06-30 浙江大胜达包装股份有限公司 Steam ladder utilizes system on corrugated paper production line

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201264390Y (en) * 2008-08-04 2009-07-01 唐蕾 Single layer corrugated paper jointing heating automatic control device for corrugated production line
CN202898901U (en) * 2012-10-23 2013-04-24 福建省文松彩印有限公司 Energy-saving emission-reducing corrugated board heating system
CN106042460A (en) * 2016-07-26 2016-10-26 昆山鸣朋纸业有限公司 Corrugated paper board production line
CN106903931A (en) * 2017-02-24 2017-06-30 浙江大胜达包装股份有限公司 Steam ladder utilizes system on corrugated paper production line

Also Published As

Publication number Publication date
CN107379712A (en) 2017-11-24

Similar Documents

Publication Publication Date Title
CN107379712B (en) Corrugated paper board production line Intelligent Composite temperature-controlling system
CA2996396C (en) Coupled system and method for the separation and drying of moist fine particle coal
CN105494608B (en) A kind of dewatering vegetable sectional drying box
CN103938483A (en) Paper humidifying device on paper making machine
CN106195995A (en) A kind of heating power jet pump height adds steam-supplying system
CN205388229U (en) Corrugated paper production facility steam system
CN204693042U (en) The high-pressure natural gas depressurized system that a kind of heat supply is not delayed
CN104548888B (en) A kind of filter press squeezing, percolation gas drying and preheating device and its implementation
CN206970994U (en) Corrugated paper board production line steam gradient utilization system
CN204469509U (en) A kind of filter press squeezing, percolation gas drying and preheating device
CN1721617B (en) Steam generation apparatus and vapor iron using the same
CN216994048U (en) Novel vehicle-mounted fuel type steam box device
CN206426616U (en) Hot plate heating system is used in a kind of corrugated paper production
CN103924474B (en) A kind of paper humidifying equipment
CN106567234A (en) Integrated heating and steam generator and dryer having the same
CN207669939U (en) Energy-saving clean module laminating machine
CN207044862U (en) Corrugated paper board production line intelligence drainage control system
CN204569884U (en) A kind of Wort boiling system of reusable edible secondary steam
CN209944003U (en) Dual steam energy-saving system for corrugated paper production line
CN204648192U (en) A kind of temperature difference water inlet waste heat circulation boiler
CN208671388U (en) Electrode boiler high temperature circulation hot-water heating system expands moisturizing exhaust apparatus with level pressure
CN210374710U (en) Heat exchanger
CN105599359A (en) Constant-temperature constant-pressure intelligent control system for steam of corrugated board
CN106642047A (en) Corrugated paper board production line steam cycle system
CN204790616U (en) Corrugated container board drying tunnel system of adjusting temperature

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
EE01 Entry into force of recordation of patent licensing contract

Application publication date: 20171124

Assignee: Sichuan Honglin Packaging Technology Co.,Ltd.

Assignor: SICHUAN CHANGHONG ELECTRIC Co.,Ltd.

Contract record no.: X2023980043951

Denomination of invention: Intelligent composite temperature control system for corrugated cardboard production line

Granted publication date: 20190719

License type: Common License

Record date: 20231027

EE01 Entry into force of recordation of patent licensing contract