CN105839439A - Automatic control system for drum pulper - Google Patents

Automatic control system for drum pulper Download PDF

Info

Publication number
CN105839439A
CN105839439A CN201610220736.9A CN201610220736A CN105839439A CN 105839439 A CN105839439 A CN 105839439A CN 201610220736 A CN201610220736 A CN 201610220736A CN 105839439 A CN105839439 A CN 105839439A
Authority
CN
China
Prior art keywords
rotary drum
water
automatic control
highly concentrated
size degradation
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.)
Granted
Application number
CN201610220736.9A
Other languages
Chinese (zh)
Other versions
CN105839439B (en
Inventor
殷宪文
刘志伟
荣继东
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.)
Nine Dragons Paper Hebei Co ltd
Original Assignee
HEBEI YONGXIN PAPER 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 HEBEI YONGXIN PAPER Co Ltd filed Critical HEBEI YONGXIN PAPER Co Ltd
Priority to CN201610220736.9A priority Critical patent/CN105839439B/en
Publication of CN105839439A publication Critical patent/CN105839439A/en
Application granted granted Critical
Publication of CN105839439B publication Critical patent/CN105839439B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment
    • D21B1/04Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • D21B1/30Defibrating by other means
    • D21B1/34Kneading or mixing; Pulpers
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment
    • D21B1/04Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • D21B1/30Defibrating by other means
    • D21B1/32Defibrating by other means of waste paper
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment
    • D21B1/04Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • D21B1/30Defibrating by other means
    • D21B1/34Kneading or mixing; Pulpers
    • D21B1/345Pulpers
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/64Paper recycling

Landscapes

  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Mechanical Engineering (AREA)
  • Paper (AREA)

Abstract

The invention discloses an automatic control system for a drum pulper. The automatic control system comprises a conveying system, a pulping system, a high-concentration deslagging system, a water system and a slag discharging system, wherein the conveying system is connected with the pulping system, the pulping system is connected with the high-concentration deslagging system and the slag discharging system, and the water system is connected with the pulping system and the high-concentration deslagging system. The automatic control system has the beneficial effects as follows: the constituent systems can be taken as a whole and started simultaneously, or each constituent system can be started independently, and different control can be performed according to different requirements, so that the cost is saved.

Description

A kind of rotary drum pulping machine automatic control system
Technical field
The present invention relates to rotary drum pulping machine control system improve, particularly a kind of rotary drum pulping machine is certainly Autocontrol system.
Background technology
General rotary drum pulping machine control system, it is impossible to simultaneously starting as an entirety While, also the system of each composition is individually started, thus enter according to different demands The control that row is different, production cost is high, and dilution water flow, shower water flowed fluctuation are relatively big, and draw The concentration change that rises, the current of electric change problem such as greatly, waste water resource, automatization level is low.
Summary of the invention
The invention aims to solve the problems referred to above, devise a kind of rotary drum pulping machine automatic Control system.
Realizing above-mentioned purpose the technical scheme is that, a kind of rotary drum pulping machine automatically controls and is System, including induction system, size degradation system, highly concentrated slag removing system, water system, dreg removing system, Wherein,
Described induction system is connected with described size degradation system, and described size degradation system is respectively with described Highly concentrated slag removing system is connected with described dreg removing system, described water system respectively with described size degradation system System is connected with described highly concentrated slag removing system,
Described induction system includes that carrier bar input equipment and nucleon claim;
Described size degradation system includes high-voltage motor, lubricating oil station, reductor and rotary drum body apparatus;
Described highly concentrated slag removing system includes one section of scummer, two-stage nitration scummer and collection slag ladle;
Described water system is made up of dilution water, shower water, sealing water, cooling water;
Described dreg removing system is carried slag device by four and forms,
Described input system arrives rotary drum body by three chain of stations triggers, after pulping, enters Slurry enters HC Cleaner, and waste material enters scarfing cinder sieving department by four slag extracting machines.
In described waste paper feed conveying system, according to the requirement of yield, automatically calculate chain board motor Rotating speed.
Described size degradation system, according to the requirement of yield, automatically controls dilution water flow, spray water flow Amount.
Described highly concentrated slag removing system, according to rotary drum liquid level, one section of scummer relay pump rotating speed, is carried out Automatically control good slurry flow, motor speed.
Described highly concentrated slag removing system is carried out according to discharging pump, dilution water pump operation, collection slag ladle automatically Deslagging.
Described water system, according to outlet pressure, the setting of liquid level, automatically controls, works as nucleon The measured value claimed is more than 10Kg/min during certain value, and dilution water flow, shower water flow are controlled automatically System.
Described dreg removing system, according to rotary drum liquid level 0-100%, one section of scummer relay pump rotating speed, enters Row automatically controls.
Utilizing the rotary drum pulping machine automatic control system that technical scheme makes, rotary drum is broken Pulp grinder automatic control system both can start as an entirety simultaneously, it is also possible to each The system of composition individually starts, and can carry out different control according to different demands, can With cost-effective, steady production, it is to avoid the waste of water resource, automaticity is high.
Accompanying drawing explanation
Fig. 1 is the structural representation of rotary drum pulping machine automatic control system of the present invention;
In figure, 1, induction system;2, size degradation system;3, highly concentrated slag removing system;4, water system;5、 Dreg removing system.
Detailed description of the invention
Below in conjunction with the accompanying drawings the present invention is specifically described, as it is shown in figure 1, a kind of rotary drum is broken Pulp grinder automatic control system, including induction system (1), size degradation system (2), highly concentrated slagging-off System (3), water system (4), dreg removing system (5), wherein, described induction system (1) Being connected with described size degradation system (2), described size degradation system (2) highly concentrated is removed with described respectively Slag system (3) is connected with described dreg removing system (5), described water system () respectively with institute State size degradation system (2) to be connected with described highly concentrated slag removing system (3), described induction system (1) Claim including carrier bar input equipment and nucleon;Described size degradation system (2) includes high-voltage motor, lubrication Petrol station, reductor and rotary drum body apparatus;Described highly concentrated slag removing system (3) includes one section of slagging-off Device, two-stage nitration scummer and collection slag ladle;Described water system (4) is by dilution water, shower water, close Water shutoff, cooling water form;Described dreg removing system (5) is carried slag device by four and forms, Described input system arrives rotary drum body by three chain of stations triggers, after pulping, enters slurry Entering HC Cleaner, waste material enters scarfing cinder sieving department by four slag extracting machines;Described waste paper In feed conveying system (1), according to the requirement of yield, automatically calculate carrier bar motor speed;Institute State the size degradation system (2) requirement according to yield, automatically control dilution water flow, shower water flow; Described highly concentrated slag removing system (3), according to rotary drum liquid level, one section of scummer relay pump rotating speed, is carried out Automatically control good slurry flow, motor speed;Described highly concentrated slag removing system (3) basis Discharging pump, dilution water pump operation, collection slag ladle carries out automatic discharge;Described water system (4) basis Outlet pressure, the setting of liquid level, automatically control, and the measured value claimed when nucleon is more than certain 10Kg/min during value, dilution water flow, shower water flow automatically control;Described dreg removing system (5) According to rotary drum liquid level 0-100%, one section of scummer relay pump rotating speed, automatically control.
The feature of the technical program is, including induction system, size degradation system, highly concentrated slag removing system, Water system, dreg removing system, wherein, described induction system is connected with described size degradation system, institute State size degradation system to be connected with described dreg removing system with described highly concentrated slag removing system respectively, described water System is connected with described size degradation system and described highly concentrated slag removing system respectively, described induction system Claim including carrier bar input equipment and nucleon;Described size degradation system include high-voltage motor, lubricating oil station, Reductor and rotary drum body apparatus;Described highly concentrated slag removing system includes that one section of scummer, two-stage nitration remove Slag device and collection slag ladle;Described water system is by dilution water, shower water, sealing water, cooling water group Become;Described dreg removing system is carried slag device by four and forms, and described input system passes through three Chain of stations trigger arrives rotary drum body, after pulping, enters slurry and enters HC Cleaner, useless Expect to enter scarfing cinder sieving department by four slag extracting machines;Rotary drum pulping machine automatic control system both may be used To start as an entirety simultaneously, it is also possible to the system of each composition is individually opened Dynamic, different control can be carried out according to different demands, can be cost-effective.
In the technical program, when whole system automatically controls, only when all of fortune When row condition is met, just can carry out equipment and just can start, now rotary drum pulping machine is existing Field has acoustic-optic alarm and reports to the police, and on-the-spot operator is carried out safety instruction: will Open rotary drum.Starting in 30 seconds, motor carries out group and starts, if do not started in 30 seconds, Then need to restart.
In the technical program, boot sequence: HC Cleaner system, water system, deslagging system System, size degradation system, induction system.
In the technical program, during the startup of each motor, there is delay function, only when one After electric motor starting, next motor just starts, it is to avoid when starting, load is the biggest simultaneously.
In the technical program, all of frequency conversion equipment has an initial starting value when starting, After motor runs the regular hour, just can automatically control according to external setting-up value.
In the technical program, setting according to yield, chain board motor, according to yield, calculates automatically Go out rotating speed.When the measured value that nucleon claims is more than certain value, dilution water flow, shower water flow Automatically control.
In the technical program, according to rotary drum liquid level, one section of scummer relay pump rotating speed, carry out Automatically control.
In the technical program, according to outlet pressure, dilution water pump, feeding spraying pump, discharging pump, Two-stage nitration HC Cleaner enters stock pump, two-stage nitration HC Cleaner relay pump automatically controls.
In the technical program, according to discharging pump, dilution water pump operation, collection slag ladle is carried out automatically Deslagging.
In the technical program, enter stock pump run according to dilution water pump, two-stage nitration HC Cleaner, Two two-stage nitration HC Cleaners carry out automatic discharge.
In the technical program, 2-3 second valve opening door before rotary drum mair motor starts premise, leans on out Mouth end dilution water valve is to open after rotary drum starts now again, so needs a timing due to valve event Between, it is to avoid running pulp.
In the technical program, adding vapours need to be chain with front end dilution water flow, when flow is low The mandatory closedown of valve when 500l/min (no matter being manual or automatic mode).Avoid steaming Vapour enters pipeline.
In the technical program, dump chest agitator is chain with liquid level, in automatic mode, reaches Open to when starting liquid level, stop during less than low liquid level.
In the technical program, each equipment is automatically stopped according to different chain conditions.
In the technical program, rotary drum input system has a filtering set-up function, the most permissible Avoiding owing to feeding is uneven, the dilution water flow, the shower water flowed fluctuation that cause are relatively big, and The concentration change that causes, the current of electric change problem such as greatly, can be with steady production.
In the technical program, there is the regular hour owing to waste paper enters Di Nong district from highly concentrated district, After shower water flow can run according to rotary drum, set delay time, then automatically control, keep away Exempt from the waste of water resource.
In the technical program, when rotary drum runs, feed system stops, due to Di Nong district still Slurry, shower water is had to remain a need for work, setting value when at this moment system can be run automatically according to feeding Automatically controlling the flow of shower water, automaticity is high.
In the technical program, dilute water valve when rotary drum orderly closedown leaves again and should force to reach stop Aperture before rotary drum.
In the technical program, when rotary drum runs, can automatically calculate the yield of yesterday, yesterday The yield of they each teams and groups, the yield of today, the yield of each teams and groups today, the yield of this month, The yield of last month.
Technique scheme only embodies the optimal technical scheme of technical solution of the present invention, this technology Some variations that some of which part may be made by the technical staff in field all embody this Bright principle, within belonging to protection scope of the present invention.

Claims (7)

1. a rotary drum pulping machine automatic control system, it is characterised in that include induction system (1), Size degradation system (2), highly concentrated slag removing system (3), water system (4), dreg removing system (5), Wherein,
Described induction system (1) is connected with described size degradation system (2), described size degradation system (2) it is connected with described dreg removing system (5) with described highly concentrated slag removing system (3) respectively, institute State water system () respectively with described size degradation system (2) and described highly concentrated slag removing system (3) phase Connect,
Described induction system (1) includes that carrier bar input equipment and nucleon claim;
Described size degradation system (2) includes high-voltage motor, lubricating oil station, reductor and rotary drum body Device;
Described highly concentrated slag removing system (3) includes one section of scummer, two-stage nitration scummer and collection slag ladle;
Described water system (4) is made up of dilution water, shower water, sealing water, cooling water;
Described dreg removing system (5) is carried slag device by four and forms,
Described input system arrives rotary drum body by three chain of stations triggers, after pulping, enters Slurry enters HC Cleaner, and waste material enters scarfing cinder sieving department by four slag extracting machines.
Rotary drum pulping machine automatic control system the most according to claim 1, it is characterised in that In described waste paper feed conveying system (1), according to the requirement of yield, automatically calculate chain board motor Rotating speed.
Rotary drum pulping machine automatic control system the most according to claim 1, it is characterised in that Described size degradation system (2), according to the requirement of yield, automatically controls dilution water flow, spray water flow Amount.
Rotary drum pulping machine automatic control system the most according to claim 1, it is characterised in that Described highly concentrated slag removing system (3), according to rotary drum liquid level, one section of scummer relay pump rotating speed, is carried out Automatically control good slurry flow, motor speed.
Rotary drum pulping machine automatic control system the most according to claim 1, it is characterised in that Described highly concentrated slag removing system (3) is carried out according to discharging pump, dilution water pump operation, collection slag ladle automatically Deslagging.
Rotary drum pulping machine automatic control system the most according to claim 1, it is characterised in that Described water system (4), according to outlet pressure, the setting of liquid level, automatically controls, works as nucleon The measured value claimed is more than 10Kg/min during certain value, and dilution water flow, shower water flow are controlled automatically System.
Rotary drum pulping machine automatic control system the most according to claim 1, it is characterised in that Described dreg removing system (5), according to rotary drum liquid level 0-100%, one section of scummer relay pump rotating speed, enters Row automatically controls.
CN201610220736.9A 2016-04-08 2016-04-08 A kind of rotary drum pulping machine automatic control system Expired - Fee Related CN105839439B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610220736.9A CN105839439B (en) 2016-04-08 2016-04-08 A kind of rotary drum pulping machine automatic control system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610220736.9A CN105839439B (en) 2016-04-08 2016-04-08 A kind of rotary drum pulping machine automatic control system

Publications (2)

Publication Number Publication Date
CN105839439A true CN105839439A (en) 2016-08-10
CN105839439B CN105839439B (en) 2017-09-05

Family

ID=56597967

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610220736.9A Expired - Fee Related CN105839439B (en) 2016-04-08 2016-04-08 A kind of rotary drum pulping machine automatic control system

Country Status (1)

Country Link
CN (1) CN105839439B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020181885A1 (en) * 2019-03-08 2020-09-17 浙江景兴纸业股份有限公司 Pulping method for household paper

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101831825A (en) * 2010-03-25 2010-09-15 吉林晨鸣纸业有限责任公司 Improved production method of waste paper deinking pulp
CN102154868A (en) * 2011-01-18 2011-08-17 维达纸业(江门)有限公司 Automatic frequency conversion pulping system in household paper manufacturing process
CN102733215A (en) * 2012-07-17 2012-10-17 广东理文造纸有限公司 System for papermaking pulping
CN203498699U (en) * 2013-08-26 2014-03-26 徐州天元纸业有限公司 Mechanical device for producing art paperboard pulp by taking recycled waste newspaper as raw material

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101831825A (en) * 2010-03-25 2010-09-15 吉林晨鸣纸业有限责任公司 Improved production method of waste paper deinking pulp
CN102154868A (en) * 2011-01-18 2011-08-17 维达纸业(江门)有限公司 Automatic frequency conversion pulping system in household paper manufacturing process
CN102733215A (en) * 2012-07-17 2012-10-17 广东理文造纸有限公司 System for papermaking pulping
CN203498699U (en) * 2013-08-26 2014-03-26 徐州天元纸业有限公司 Mechanical device for producing art paperboard pulp by taking recycled waste newspaper as raw material

Non-Patent Citations (5)

* Cited by examiner, † Cited by third party
Title
刘山: "水力碎浆机自动控制系统改造", 《中华纸业》 *
周耘: "碎浆机清渣系统设备的改造", 《中国造纸》 *
朱光云: "年产6万吨高档生活用纸项目的研究", 《陕西科技大学硕士学位论文》 *
王雄波: "一条现代化废纸脱墨生产线的设备配置", 《造纸科学与技术》 *
赵博等: "基于S7_200PLC的新型转鼓碎浆机控制系统", 《中华纸业》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020181885A1 (en) * 2019-03-08 2020-09-17 浙江景兴纸业股份有限公司 Pulping method for household paper

Also Published As

Publication number Publication date
CN105839439B (en) 2017-09-05

Similar Documents

Publication Publication Date Title
CN104478122A (en) Method for solid-liquid separation of waste incineration fly ash water washing slurry
CN105839439A (en) Automatic control system for drum pulper
CN107096647A (en) A kind of oily crumb centrifugal separator
CN208483599U (en) A kind of CNC milling machine chip chip removal mechanism
EP3147276B1 (en) Method for processing acetic acid solvent in oxidising unit of pta industrial apparatus
CN110562907B (en) Automatic control system for unloading tank car light oil by using rotary piston pump and control method thereof
CN104984837A (en) Continuous ore discharge type centrifuge
CN202151590U (en) Spherical cobalt hydroxide cleaning device
CN205587158U (en) Full -automatic deoiling machine
CN103041630A (en) Solid-liquid separating, washing and drying integrated device
CN205307983U (en) Sizing material dross removal mechanism
CN109093520B (en) Multi-wire saw liquid supply system magnetic mud separation device
CN203828058U (en) Rubbing plate blockage automatic cleaning device
CN104437899A (en) Blanking device for centrifuge
CN109606853B (en) Automatic processing system and method for double-row synchronous line shutdown materials
CN204320498U (en) A kind of centrifuge blanking device
CN205973759U (en) Conveyor is prepared to polyester thick liquids
CN204523205U (en) A kind of spiral material washing machine
CN204866162U (en) Drum -type magnetic separator
CN110834061A (en) Multifunctional automatic oil removal online device
CN110482274A (en) A kind of tobacco cutting production line removal of impurities conveying device and its control method
CN110274251A (en) A kind of exhaust of oil processing system
CN220738004U (en) Self-cleaning system of fly ash washing centrifuge free of external water supplementing
CN2634149Y (en) High speed pump automatic startor for propylene raw material
CN220496640U (en) Horizontal decanter centrifuge cleaning device

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CP01 Change in the name or title of a patent holder

Address after: 063500 Luannan Tangshan City County of Hebei Province Chengguan West Road No. 88

Patentee after: NINE DRAGONS PAPER (HEBEI) CO.,LTD.

Address before: 063500 Luannan Tangshan City County of Hebei Province Chengguan West Road No. 88

Patentee before: HEBEI YONGXIN PAPER INDUSTRY CO.,LTD.

CP01 Change in the name or title of a patent holder
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170905

CF01 Termination of patent right due to non-payment of annual fee