WO2005088007A1 - Method for monitoring and controlling a papermaking process - Google Patents

Method for monitoring and controlling a papermaking process Download PDF

Info

Publication number
WO2005088007A1
WO2005088007A1 PCT/FI2005/050078 FI2005050078W WO2005088007A1 WO 2005088007 A1 WO2005088007 A1 WO 2005088007A1 FI 2005050078 W FI2005050078 W FI 2005050078W WO 2005088007 A1 WO2005088007 A1 WO 2005088007A1
Authority
WO
WIPO (PCT)
Prior art keywords
gas
amount
quality
controlling
stock
Prior art date
Application number
PCT/FI2005/050078
Other languages
English (en)
Finnish (fi)
French (fr)
Inventor
Leif Piippola
Tero Jussila
Jouko NIINIMÄKI
Tuomas Stoor
Original Assignee
Metso Paper, Inc.
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 Metso Paper, Inc. filed Critical Metso Paper, Inc.
Priority to AT0903305A priority Critical patent/AT502428B1/de
Priority to DE112005000263T priority patent/DE112005000263T5/de
Publication of WO2005088007A1 publication Critical patent/WO2005088007A1/en

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21DTREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D5/00Purification of the pulp suspension by mechanical means; Apparatus therefor
    • D21D5/26De-aeration of paper stock

Definitions

  • the invention relates to a method for monitoring and controlling a papermaking process.
  • Air and other gases both as dissolved and in gaseous form, occur in the stock and water circulations of a paper or board machine. Air (nitrogen and oxygen) gets into stock in connection with thick stock, circulation waters, pulping and mixing as well as because of leakages in process devices. Gases are also produced in the process as a result of bacterial activity (methane), decomposition (carbon dioxide) of carbonates or other compounds. Gases can cause various kinds of harm. They can, among other things, increase the consumption of energy, hamper the operation of pumps, cause contamination of the process, make the dewatering in the wire section more difficult, and reduce the quality of the paper being manufactured. Attempts are usually made to reduce the drawbacks caused by gases by means of mechanical deaeration and/or by adding deaerating chemicals.
  • An object of the invention is a new way of monitoring and controlling a papermaking process based on measurements made from the process.
  • An object is also a method that provides a more accurate picture than heretofore of the operation of the process, thus facilitating control of the process.
  • the invention is characterized by what is stated in the characterizing part of claim 1.
  • a papermaking process is monitored by measuring the amount and quality of gas from a gas flow discharging from a process device and by controlling the process based on the information obtained.
  • Said process device can be, for example, a deaeration tank, a passive deaeration duct (for example, an OptiAir Flume produced by the applicant), a cyclone, a centrifugal cleaner, a screen, a pulp chest or a water tank, a sampling device or another equivalent process device through which air and gases are removed from the process.
  • the amount of gas is meant the total amount of air and the gases originating from the process.
  • quality of gas is meant, among other things, the proportion of a given gas component in the total amount of gases.
  • the amount and quality of gas is also measured from one or more other material flows.
  • the content of one or more gases present in the process can be measured from a stock and/or water circulation of the process and from gas flows leaving the process.
  • the gas to be measured can be nitrogen, methane, oxygen or carbon dioxide or any other gas present in the process.
  • the gas can be in soluble or gaseous form.
  • deaerator can be controlled based on the amount and quality of gas.
  • deaeration devices are often operated, to be on the safe side, at high capacity because the exact amount of the gases in the process is not generally known.
  • a substantial saving is achieved, for example, because, as a result of the monitoring of gases, the vacuum used in the deaerator can be reduced.
  • An increase in the methane content indicates that anaerobic bacterial activity occurs in the process.
  • An increased carbon dioxide content in turn indicates a change in pH, which has led to the decomposition of carbonate and some other compounds.
  • An increased oxygen or nitrogen content can be an indication of leakages or disturbances in a pump or in another process device in the control of the liquid-level of tanks/chests.
  • the measurement of the amount and quality of gas at several points of the process makes it possible to determine a gas balance in different sections of the process, such as for the short circulation, the long circulation, stock lines, broke lines, etc. This makes it easier to locate the cause of disturbance and to direct corrective action at a right location.
  • the amount and quality of gases is measured at point M10 from a water flow passed from the wire water tank 22 along the line 23 to the deaerator 9.
  • the gas flow discharging from the deaerator 9 is monitored at point M8.
  • the amount and quality of gases is measured at point M9 from the water flow discharging from the deaerator 9.
  • deaerator it is also possible to use deaerators that are based on delay times, such as an OptiAir FlumeTM deaeration duct, a conventional wire pit and/or cyclone.
  • the amount and quality of gases is measured at point Mi l from the wire water flow passed from the wire water tank 22 to the disc filter 27.
  • the gas content and the quality of the gases of the wet broke conducted along the line 28 to the disc filter 27 are monitored at point Ml 2.
  • the gas content and the quality of the gases of the filtrates obtained from the disc filter 27 are monitored at points Ml 3 and M14.
  • the amount and quality of the gas emerging from the deaeration tank 9 can be measured at point M8.
  • the quality of the gas for example, the content of methane or nitrogen changes as a result of increased microbial activity in some preceding process step
  • attempts are made to remedy the problem by controlling the metering of biocide to the process.
  • the data on the amount and quality of gases obtained from the different measurement points M1-M14 can be combined in a desired manner to form a gas balance of the process or a single section thereof.
  • the operation of the deaerator can be controlled based on one or more measurements, so that the vacuum level of the deaerator can be limited to correspond to the actual degasification need.
  • Based on the monitoring of gases it is possible to control the feed amount and location of defoaming chemicals or the quality, amount and feed location of antimicrobial chemicals. In this way, chemicals can be applied where they are most needed and where they are most useful.
  • the measurement of the amount and quality of gas can also be used for monitoring disturbance situations in the process. Monitoring reveals, for example, leakages in pump seals or disturbances in the control of the level in tanks. In that connection, information about a disturbance situation can lead to the initiation of process control or repair action.
  • any methods known in themselves can be used in the measurement of the amount and quality of gas which has dissolved or is in the form of bubbles. These include, for example, ultrasound- or microwave-based methods, an acoustics-based free gas measurement method, a measurement method based on imaging and image processing, volume quantity measurement of gases and gas content measurement based on the compression and expansion of gases.
  • the quality of gas can be measured, among other things, by specific gas sensors and by means of gas chromatography. Quality can also be monitored by measuring the distribution of the gas bubble size or the ratio of dissolved gas and gas in the bubble form by means of a measuring device intended for this purpose.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Paper (AREA)
PCT/FI2005/050078 2004-03-15 2005-03-14 Method for monitoring and controlling a papermaking process WO2005088007A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
AT0903305A AT502428B1 (de) 2004-03-15 2005-03-14 Verfahren zur überwachung und steuerung eines papierherstellungsprozesses
DE112005000263T DE112005000263T5 (de) 2004-03-15 2005-03-14 Verfahren zur Überwachung und Steuerung eines Papierherstellungsprozesses

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI20040395A FI119111B (fi) 2004-03-15 2004-03-15 Menetelmä paperinvalmistusprosessin monitoroimiseksi ja säätämiseksi
FI20040395 2004-03-15

Publications (1)

Publication Number Publication Date
WO2005088007A1 true WO2005088007A1 (en) 2005-09-22

Family

ID=32039416

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/FI2005/050078 WO2005088007A1 (en) 2004-03-15 2005-03-14 Method for monitoring and controlling a papermaking process

Country Status (4)

Country Link
AT (1) AT502428B1 (de)
DE (1) DE112005000263T5 (de)
FI (1) FI119111B (de)
WO (1) WO2005088007A1 (de)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012013407A1 (de) * 2010-07-30 2012-02-02 Voith Patent Gmbh Konstantteil einer maschine zur herstellung einer faserstoffbahn
CN105465102A (zh) * 2015-12-15 2016-04-06 中国航空工业集团公司金城南京机电液压工程研究中心 一种阀套上密封圈和保护圈装配正确性检查装置

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102008056505A1 (de) * 2008-11-08 2010-05-12 Voith Patent Gmbh Konstantteil

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4690634A (en) * 1985-05-31 1987-09-01 Svenska Traforskningsinstitutet Method of measuring dry substance in flue gases
US6124111A (en) * 1997-12-23 2000-09-26 Btg Kalle Inventing Ab, A Corp. Method and an arrangement for measuring the amount/activity of catalase before or in connection with bleaching of preferably cellulose fibres included in a pulp suspension
US20030000670A1 (en) * 2000-01-26 2003-01-02 Michael Schwarz Method for determining a characteristic value for the binding force potential of suspended paper fibers and use of this method
US20030131652A1 (en) * 2002-01-16 2003-07-17 Qingyuan Chen Determination of gas solubility, entrained gas content, and true liquid density in manufacturing processes

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4690634A (en) * 1985-05-31 1987-09-01 Svenska Traforskningsinstitutet Method of measuring dry substance in flue gases
US6124111A (en) * 1997-12-23 2000-09-26 Btg Kalle Inventing Ab, A Corp. Method and an arrangement for measuring the amount/activity of catalase before or in connection with bleaching of preferably cellulose fibres included in a pulp suspension
US20030000670A1 (en) * 2000-01-26 2003-01-02 Michael Schwarz Method for determining a characteristic value for the binding force potential of suspended paper fibers and use of this method
US20030131652A1 (en) * 2002-01-16 2003-07-17 Qingyuan Chen Determination of gas solubility, entrained gas content, and true liquid density in manufacturing processes

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012013407A1 (de) * 2010-07-30 2012-02-02 Voith Patent Gmbh Konstantteil einer maschine zur herstellung einer faserstoffbahn
CN103154362A (zh) * 2010-07-30 2013-06-12 沃依特专利有限责任公司 用于制备纤维幅的机器的进入系统
CN105465102A (zh) * 2015-12-15 2016-04-06 中国航空工业集团公司金城南京机电液压工程研究中心 一种阀套上密封圈和保护圈装配正确性检查装置

Also Published As

Publication number Publication date
FI20040395A (fi) 2005-09-16
AT502428B1 (de) 2008-07-15
DE112005000263T5 (de) 2007-02-15
FI20040395A0 (fi) 2004-03-15
AT502428A2 (de) 2007-03-15
FI119111B (fi) 2008-07-31
AT502428A8 (de) 2007-06-15
AT502428A3 (de) 2008-05-15

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