2
A Royal Event for Board and Packaging Papers
In early May 2001, under the motto “ahead, Voith Paper invited the manufacturers of board and packaging papers to Vienna to exchange their experiences and opinions.
The list of the more than 400 partici- pants reads like the ‘Who’s Who’ of the board and packaging paper industry: The author: Over 250 top international managers Nicole Schnait, from the board and packaging paper Paper Machines Board and Packaging sector, as well as representatives of institutes, technical universities and representatives from the media had accepted the invitation to come to Vienna. A total of 40 countries were represented – from Australia to Canada, from Japan to Chile. Otto Heissenberger, President of the Board and Packaging 3 Paper Machine Division, and Dr. Hermut Kormann, Lunch was served in the newly renovated President of J.M. Voith Aktien- roof foyer of Vienna’s Hofburg Palace. gesellschaft, Heidenheim.
Vienna’s Hofburg Palace provided a royal setting for the conference. In former times, the Hofburg Palace was the emperors’ winter residence. Today it houses the offices of the Austrian Federal President, the Spanish Riding School, the National Library, several museums and a modern conference centre. More than 350 guests from 40 countries attended the conference held in the ‘Großer Redoutensaal’. 4
On the evening before the conference, Otto Heissenberger, President of the Board and Packaging Paper Machine Division, welcomed the guests at a reception held at the Ferstel Palace. The evening’s entertainment was an 5 experience enjoyed by everyone. In the A ‘gemutlich’ evening at a ‘Heuriger’ with relaxing atmosphere, many attendees The spouses’ programme included a visit to typical ‘Schrammel’ folk music is an absolute also found the time to discuss future the imperial apartments in the Hofburg and the must in Vienna. plans and projects. Porcelain Manufactory Augarten.
Three years had passed since the last What are the possibilities of multi-ply SAICA 3 in Spain, the fastest paper ma- “ahead Customer Conference was held in and multi-layer concepts, when are chine for corrugating medium, constantly 1998, focusing for the first time on the such concepts used today and what reports new speed world records. The topic of board and packaging papers – advantages do they offer for the pro- new production line for gypsum-grade and it was time for an update. duction of certain board or packaging paperboard, Lawton, Oklahoma, USA, is paper grades? the world’s first paper machine fitted with two gap formers. The fact that the Many investments were made by Voith What can be done to follow the trend shoe press technology has also gained a Paper during these three years, mainly towards higher speeds and lower basis firm foothold in the production of board to strengthen its process competence. weights of packaging papers? What was demonstrated by a report on the Today, papermakers have to re-think and are the possibilities to boost produc- BM 3 rebuild at Mayr-Melnhof, Frohn- optimize their complete production tion while enhancing quality when leiten, Austria. process to assure that their products are producing board? geared to market requirements at opti- mum cost effectiveness. How do investment cost and operating The guests’ expectations were high, and cost correlate, and how can a the participants this year were twice as machine’s total cost be minimized? many as during the “ahead 1998 Confer- Some changes were clearly visible, such ence. The numerous positive reactions, as the acquisition of the Scapa group, The papers focused both on concepts for the pleasant atmosphere during the con- which considerably strengthened the new production lines and on possible ference and the fact that the large confer- Voith Paper Service Division and made upgrading through rebuilds. Moreover, ence room was packed full until the last Voith Fabrics one of the major manufac- several “smart solutions” were present- paper was read, showed that the Vienna turers of paper machine clothing. ed, allowing the papermaker to achieve conference was worth visiting. lasting improvements in machine perfor- mance with small investment budgets In other areas, such as research and de- and minimum amortization times. In closing, a small, but unique, thank- velopment, Voith Paper has also focused you gift was presented. Each participant on strengthening its process compe- received a ‘take-away’ paper machine. tence. The following topics were inter- Highlighted on the agenda were the pa- The simple design, ab- linked throughout each paper being pre- pers on new reference plants. During solutely maintenance- sented at the “ahead 2001 Conference: “ahead 1998, several new components free and environ- and machine concepts specifically devel- mentally friend- oped for board and packaging papers had ly, was received How do the raw materials used, the been presented, such as the gap formers, with great enthu- stock preparation equipment, the DuoFormer™ Base and DuoFormer™ Top. siasm. paper machine components and fol- This time, five customers demonstrated lowing process stages interact with how these concepts had successfully “ahead on the Internet: one another during operation of a been put into practice, giving current fig- All papers and the best photos of the conference board or packaging paper production ures to substantiate their reports. can be found on the “ahead homepage: line and how can such interaction be Simply download at: www.ahead.voithpaper.com utilized to achieve an optimum The papers presented at the conference can also be requested from: product? Some of the production lines discussed Ms Sigrid Hrebacka, Fax: +43 27 42 8 06 25 48 have revolutionized the industry: PM 9 at E-mail: [email protected] 6
Our guests’ opinions
Ing. product. It was a highlight for me not Henk Lingbeek only in technical respects, but also be- SCA Packaging De cause it focused on the tasks of our Pekka Mauranen Hoop, Netherlands product. KCL, Finland
It was an excellent conference, and what ... Whether I will come again? Yes, of I come from the Finnish research insti- I liked especially – I also attended the course, we already agreed yesterday that, tute KCL and have to admire your team. conference three years ago – was the if things go on like this, Voith can hold Listening to all of the papers about the combination of topics: not only technical such a meeting every week! different products, I realize how deep issues, but also some dealing with mar- their expertise is in this field. keting, final products, Voith Paper's phi- losophy and organization. I think Voith has done extensive theoreti- cal research and development work and has applied the results in practice on the pilot machine and in customers’ mills… Peter Reichler Amcor Australasia, ...Of course, the location is very impres- Australia sive, this imperial palace...
Dipl. Ing. (FH) I think it was a very impressive confer- ...I think it's a world-class conference! Manfred Stemmer ence, you have picked a beautiful loca- Cascades Arnsberg tion, even the weather is impressive. GmbH, Germany What pleased me more than anything else was the quality of the presentation and My general impression is a very positive the information provided... one, we gained new ideas and thoughts, and moreover, it was a good opportunity ... It was very pleasing that the informa- to talk with many colleagues. tion was prepared in a way that even the non-technical people, such as myself, T.S. Ong What impressed me most was the profes- could understand... Genting Sanyen, sionalism of the presentations. Malaysia ... The paper on investment and operating ...An important thing is that people with cost yesterday and of course the two pre- The conference was well organized, and I practical experience were present, report- sentations of the new mills in Turkey and think the topics were well chosen, partic- ing about their experiences... SAICA were most interesting!… ularly on the first day. The quality of the papers, in general, was good – ’they were ...What I also liked very much, as I come ...I do have to express my appreciation of presented by many of the young people. I from the folding boxboard sector myself, the Voith team – they have done a fabu- think there is a bright future ahead be- was the first paper giving entirely new lous job! cause Voith is capable of renewing itself aspects of the publicity value of our with these young specialists... News FROM StoffaufbereitungTHE DIVISIONS 7
Stock preparation – the key to ensure the productivity of newsprint and SC paper machines
The Federal Republic of Germany holds What is the present situation in the use a top position in Europe with regard to of recovered papers in the field of graphi- the use of secondary fibers for the man- cal papers? ufacture of paper and board products. The rate of utilisation of recovered Fig. 1 shows the relative recovered paper paper is presently 62%. For Germany, contents for the most important graphi- this ratio is expected to be increased cal, wood-containing paper grades. The further, which will lead to a further abscissa in this diagram represents the reduction in fresh fiber usage. quality whereas the ordinate stands for The author: the price achieved with these products. Harald Selder, The red field describes the average, rela- Fiber Systems tive recovered paper content used in It is known that the largest quantities of these products. recovered paper are used in the field of packaging papers. In this product sector, Today, the standard newsprint paper is signs of maximization have already be- usually made from 100% deinked pulp come apparent, so that in this sector no (DIP). The same applies for upgraded increase in the use of recovered paper newsprint. In the SC paper sector, 40% is to be expected. A higher percentage of secondary fibers are used on average, can therefore only be achieved by raising and for LWC papers, approximately 25%. the secondary fiber usage for graphical A similar percentage is also used for the papers. high-grade coated papers. 8
Fig. 1: Content of deinked pulp in wood-containing printing papers.
Fig. 2: Number and relative weight of advertising inserts in newspapers.
Weight of inserts *Relative weight = x 100 Overall weight (newspaper + inserts)
Fig. 3: Trend in paper grades used for magazines and change in inorganic content of DIP. German deinking furnish: 50% ONP, 50% OMG.
1 Recovered paper: share of 70%. In Japan, statutory regula- 100 quality and availability tions limit the advertising space in daily HWC newspapers, which explains this high MWC The recovered paper grade, which is percentage of inserts. 75 LWC available in sufficient quantities in Ger- many and of satisfactory quality unifor- Such a high share of inserts is not to be MFC mity, suitable for the higher-quality, expected in Europe. However, a further STIN 50
Price graphical papers, is the deinking furnish. increase in the number of advertising in- SC serts in daily papers is to be reckoned SIN This deinking furnish is collected in the with. Local and regional advertising is not 25 IN form of a household collection grade by of interest as yet for the electronic media, Rel. content of deinked pulp [%] NEWS the recovered paper trade, and it‘s then and it will remain a domain of print ad- separated into brown and white paper vertising for now and the near future. Quality fractions in sorting plants. Another change can be noted for the 2 30 80 The resulting white paper fraction con- magazine paper grade. Approximately sists of approximately 50% old newspa- 15 years ago, the principal paper grade 70 25 pers and 50% magazines and is supplied for magazine production was LWC paper. Japan 60 to the paper mills as deinking furnish. Today, the predominant paper grades Japan 20 The paper composition of this deinking used for magazines in Germany are the 50 furnish is subject to continuous change, SC paper grades suitable for roto-gravure 15 40 which the stock preparation engineers printing, as can be seen from Fig. 3. have to take into consideration. In this About 70% of the magazines published 30 10 Germany article, we will point out the most essen- in Germany are presently printed on SC 20 tial changes in the deinking furnish com- papers. Germany 5 position, which have an influence on the Number of inserts 10 Relativ weight* [%] deinkability and the DIP quality. This situation must be expected to 0 0 change again. The reason is the new gen- Today, the daily newspapers include ap- eration LWC papers. These papers are 3 proximately 2-5 advertising inserts per coated and calendered in an online 100 50 paper. These inserts are in most cases process. In this way, production costs printed on SC and LWC papers. The can considerably be reduced. In addition, 80 40 printing process is mostly sheet-fed off- the quality of these papers is equivalent SCA Papers set with integrated heat-set drying. Due or even superior to that of the corre- 60 30 to this heat-set treatment, many prob- sponding SC papers. Consequently, there lems have to be reckoned with when it will be more LWC papers in the deinking Ash content comes to deinking. The quantitative share furnish in the future. 40 20 of these inserts is approximately 10-20% LWC Papers of each newspaper, as shown in Fig. 2. From Fig. 3, it is also obvious that a con- Relative content [%] Relative 20 10 stant rise in ash content can be noted in In Japanese daily newspapers up to 30 the deinking furnish. This rise is the 0 0 Content of anorganic substances [%] inserts per distributed paper can be result of continuously increasing ash 1985 1990 1995 2000 2005 found. In this case, the inserts have a contents in LWC and SC papers, and on Fiber Systems 9
– Higher final – Runability product requirements – Productivity – Quality decrease of recovered paper Fig. 4: Runnability- and productivity-related 4 – Reduction of fresh variables. water consumption Fig. 5: Simplified block diagramm of analyzed system. the other hand of rising ash contents in 5 analysis focused on establishing the standard newsprint papers. Drum pulper change in the macro and micro stickies area. For reasons of completeness, the Drum chest Along with the higher percentage of mag- development of the chemical oxygen de- azines in the deinking furnish, more ad- Coarse screening mand and the anion-charged substances
hesive glue and more hotmelts are auto- Loop I was also established. matically fed into the stock preparation Flotation I systems. These substances are the Fine screening For the macro stickies determination, the sources of the macro stickies, which will pick-up method, developed by Voith Sul- Thickening I cause many upsets on the paper machine zer was used. And, the micro stickies if not sufficiently removed. In addition, were determined with the laser optical Disperging I large quantities of coating binders and particle counting method developed by coating additives are included in the Flotation II BASF. coated papers. It is from these sub- Thickening II stances that the micro stickies originate Loop II In the following section, a thorough de- resulting in serious runnability and avail- Make up scription is given of the results obtained ability problems on the paper machines water from PM regarding the macro and micro sticky be- if their removal is not satisfactory. This haviour. Disperging II H2O2 situation will require systematic counter- NaOH measures in the future (Fig. 4). Bleach tower Results In addition to the usual targets of optical brightness and cleanliness, which are preparation systems with regard to the Macro stickies aimed at in the stock preparation separation of detrimental substances. For The first reduction in macro stickies process, the separation of detrimental this reason, the results of a detrimental worth mentioning occurs in coarse substances in the recovered paper must substances analysis will first of all be screening, as shown in figure 6. In flota- also be increasingly considered in the fu- presented. tion I, no macro stickies are removed. ture. As fresh water usage in paper pro- With 85% removal efficiency, fine screen- duction is reduced, this subject becomes The system chosen for the analysis ing is by far the most effective process even more important. The remainder of (Fig. 5) consists of a 2-loop process for module. A further reduction in macro this article describes solutions for the the production of DIP for SCB papers. stickies can be noted in both disperging control of detrimental substances in the The first process loop includes the drum systems. stock preparation system. The control pulper, coarse screening, flotation I, fine strategies are integrated with plans for screening, thickening and disperging I. The total sticky loading was reduced from optimizing paper machine operation. The second process loop contains flota- 11510 mm2/kg b.d. to 192 mm2/kg b.d. tion II, thickening and disperging II. Dis- which corresponds to a total reduction of perging II is combined with peroxide 98.3%. Process modules for controlling bleaching. No process water cleaning is detrimental substances connected, neither in the first nor in the Micro stickies second process loop. Only the make-up The change in micro stickies area in each In order to be able to fight detrimental water from the paper machine, which is process step presents a completely dif- substances effectively, it is necessary to carried over to the stock preparation, is ferent picture from that of the macro define those modules integrated in stock run through a microflotation. The system stickies. The screens do practically noth- 10
After pulping 10 = inlet coarse screening 11510 4.71*10
Inlet flotation I 4000 1.02*1010 After flotation I 4849 10 = inlet fine screening 8.44*10 Fig. 6: Change in macro stickies area in the analyzed deinking system. After fine screening 725 9.19*1010 Fig. 7: Change in number of micro stickies in the After thickening I 10 analyzed deinking system. (MC+HC) 1180 3.78*10 Fig. 8: Effectiveness of stock prep process units After disperging I 600 4.23*1010 in removing substances detrimental to runnability and productivity. Inlet flotation II 436 9.77*1010 Fig. 9: MultiScreen fine screen optimized for macro stickies removal. After flotation II 10 520 6.32*10 Rotor – Multiple blades After thickening II 10 – Adequate pressure pulses 580 3.01*10 Screen basket – C-bar™ technology After bleach tower 10 330 3.43*10 – High precision of slot width Housing Headbox PM 192 6.26*1010 – Conical design – Fishmouth accept discharge 10 10 0 4000 8000 12000 0 4*10 8*10 Macro stickies area [mm2/kg b.d.] Number of micro stickies [n/kg b.d.] ing in terms of micro sticky removal. 67Whereas the flotation blocks possess a 8 Process blocks Macro stickies Micro stickies COD Cationic demand considerable separation ability. A high re- Coarse screening moval efficiency is produced in the thick- Flotation I ening stages. But, the low micro sticky Fine screening level after the thickening processes can- Thickening I not be maintained due to the highly cont- Disperging I aminated process water that is subse- Flotation II quently used for dilution. At this point it Thickening II becomes noticeable that microflotation is Disperging II needed for cleaning the process water No influence Low improvement Medium improvem. High improvem. (Fig. 7).
9 Rotor Fig. 8 summarizes the efficiency of the in- dividual process modules used in the stock preparation system with regard to the separation of the investigated group of detrimental substances.
The most effective process module with Inlet Screen basket regard to macro sticky separation is fine screening. Voith Paper Fiber Systems recognized the importance of fine screen- ing for the macro sticky removal at an early stage and now offers a most effec- tive machine – the MultiScreen. This screen (Fig. 9) is completely optimized Reject Housing from “head to foot”.
Micro sticky control is most effective in the flotation blocks and in microflotation used for water cleaning. However, there Dilution water Accept will always be some residual micro sticky load carried over to the paper machine. Fiber Systems 11
11502% 1300 Fig. 10: Correlation between build up of 1100 detrimental substances in the PM white water. absorption efficiency and fresh water usage. 0% 900 Fig. 11: Effect of hydrophobic micro stickies 10% 700 concentration in the process water loop on paper machine availability. 500 25% Change in Fig. 12: Strategy for control of detrimental 300 50% 75% Absorbtion efficiency substances.
detrimental substance [%] Process units relevant to macro stickies 100 100% Source: BASF Process units relevant to micro stickies 071421 Process units relevant to COD Process units relevant to cat. demand. Fresh water l/kg paper 10
In this case, the carried over micro sticky 11 Feed quantity of micro stickies Collapse situation = load is to be bound to the fibers by > rejected quantity renew process water means of fixing agents so that the left- over microstickies go out with the fin- ished paper. The correlation between absorption efficiency and changes in con- centration dependent upon fresh water usage is shown in Fig. 10. It can be noted that a 50% absorption efficiency is re- quired for maintaining a stable micro sticky concentration in the white water Concentration of hydrophobic circuit (Fig. 10). micro stickies in process water
Feed quantity of micro stickies = rejected quantity Machine uptime If more micro stickies are fed to the pa- per machine than can be absorbed by the 12 fiber material, the concentration in the white water circuit will continuously rise. Eventually, a critical concentration is Stock preparation Paper machine reached where slight changes in tempera- ture and pH-value will induce the forma- tion of macro stickies due to displace- ments in solubility. With a further in- crease in concentration, a collapse situa- Minimization of tion will be evoked. The paper machine Mikro- flotation I carry over must be shut down and the process water exchanged. This kind of situation will Mikro- flotation II considerably impair paper machine avail- ability (Fig. 11). Flotation I Fine screening Coarse screening Thickening I Thickening Thickening II Disperging I Flotation II Summary and recommendations Disperging II Optimum reduction in Fixing of residual detrimental substances detrimental substances to the fibre and removal with the paper In order to ensure the runnability and availability of high-speed newsprint and SC paper machines, it is absolutely nec- detrimental substances by a correspond- Consequently, deposits and contamina- essary to control the level of detrimental ing module arrangement and by opti- tions of felts and screens can be elimi- substances. There is a continuously in- mized process water management and nated. Another advantage of this control creasing load of detrimental substances, cleaning. The aim should always be to strategy is the much reduced usage of and countermeasures must be taken to keep the carry over of detrimental sub- process chemicals during the manufac- fight this. Detrimental substances are stances to the paper machine as low as turing process. Fixing agents should only combatted most efficiently in the stock possible (Fig. 12). This way, high con- be used after the reduction in detrimental preparation systems. The system supplier centrations of detrimental substances in substances in the stock preparation sys- can decisively help to reduce the load of paper machine circuits can be avoided. tem has been optimized. 12
New EcoMizer™ – Product A new cleaner concept establishes itself
Hydrocyclones for the separation of specifically heavy and/or light contami- nants have been used in the paper industry for about 50 years. After some significant innovations in the first decades, the development of hydro- cyclones came to a relative standstill in the recent past. Consequently, the difficulties with these machines have The author: remained the same. The new EcoMizer Wolfgang Mannes development now offers a solution to Fiber Systems many of these problems. Fiber Systems 13
Fig. 1: Distribution of axial velocities in a hydrocyclone (result of numerical simulation using the finite volume method).
Fig. 2: Backflow of thickened, contaminated suspension in the vortex center.
Fig. 3: EcoMizer™-Cleaner – Flow conditions at the rejects outlet.
Thickening behavior as a basic problem large influence on the viscosity – the 1 vax (m/s) more energy is required for this. 9.65 Most problems with hydrocyclones can be contributed to an elementary cause – In the hydrocyclone, energy is fed in with 6.89 the tendency of the fibres suspension to the incoming suspension only and dis- thicken in the rejects. If this tendency is tributed downwards in the hydrocyclone 4.12 not correctly assessed when designing a by the axial flow running along the cylin- 1.36 cleaner plant, stock consistency increas- der and cone walls (Fig. 1). This energy es in the final stages of a cleaner plant distribution depends on the volumetric -1.39 will lead to operating problems and/or distribution of the inlet flow into the ac- excessive fibre losses. cept and reject flows. -4.16
However, apart from the uncertainty in The lower the volumetric reject dis- -6.92 the design of cleaner plants, fibre thick- charge, the less energy reaches the bot- ening also limits the possible operating tom cone area. At the same time, the 2 conditions. A hydrocyclone only func- stock consistency, and thus the viscosity Cleaner cone tions with the use of fibres while their of the suspension, are at its highest in fluidation caused by rotation is guaran- the bottom cone area due to the thicken- teed. If the rotation in the cone comes ing effect of the hydrocyclone. Therefore, to a standstill, the cleaner becomes with low reject rates, failure of the re- clogged. The restriction at the cone noz- ferred to rotary motion may occur and Backflow zle or a re-routing of the rejects on the consequently lead to clogging of the cone end to a radial or tangential outlet, cleaner. Nozzle will not allow any “pressing through” of the fibres. The consumption of the kinetic energy in the cone area is further intensified by an This phenomena of rotation failure actu- additional phenomenon. As can be seen ally is the most common cause for oper- in Fig. 2, the basic pattern of a downward ating problems on the hydrocyclone, flow along the cone wall and an upward whereas clogging due to individual, or back-flow in the vortex centre is also 3 large-size contaminants is rather an ex- present at the reject outlet. ception in the low consistency range. With this backflow, the thickened reject stock is returned to the cone where it fur- Break-down of rotation and return flows ther increases the consumption of kinetic energy. In addition, contaminants, which What causes the rotation in a hydrocy- were already separated, are once more clone to break down? Since a fibre sus- entrained upwards and in the worst case, pension is a viscous medium, it must be may even reach the accepts. constantly fed with energy in order to maintain the rotation in the cleaner. The more viscous the medium – as is known, the stock consistency of fibres has a very 14
Fig. 4: Problems with classical concepts for rejects dilution.
4 Low addition of High addition of Distribution dilution water dilution water of axial velocity
upwards
downwards
Contaminants settle back Danger of backflushing to the cone wall the contaminants
The EcoMizer™ concept In conventional concepts to decrease the near the cone wall, where the contami- reject stock consistency, the filtrate is nants are concentrated, are not affected The newly developed EcoMizer concept usually added tangentially in the lower at all by to the addition of dilution water, offers a solution for these two problem cone area (Fig. 4). Although fibre recov- which also facilitates the dosage of the areas. The concept was derived from the ery is thus fundamentally possible, with water quantity. fact that the basic flow pattern in the hy- an excessive dosage of filtrate there is a dro-cyclone cannot be influenced. This is great risk that contaminants, already con- Finally, the energy demand for adding the a consequence of the geometry and the centrated in the cone wall area, will be di- filtrate is considerably lower than when it usual distribution of the volumetric inlet verted to the vortex center at the point is carried out via the cone wall. Depend- flow in a hydrocyclone. However, the where the filtrate is fed in. If these conta- ing on the pressure ratios in the hydrocy- decisive idea is to “replace” the thickened minants reach an area with an upward di- clone, even a vacuum may exist in the reject stock in the central return flow in rected axial speed, flushing back of cont- vortex centre, so that the flushing water the lower cone by a clean filtrate or white aminants into the accepts may occur. is sucked in from the outside without any water added from the outside (Fig. 3). This risk particularly exists for contami- pressure. Thus, on the one hand, dirt is prevented nants which are difficult to separate, from being sucked upwards once again. such as dirt specks, since their specific In conclusion, it is possible with the On the other hand, the injected filtrate weight differs only slightly from that of EcoMizer concept to decrease the stock will mix in the cone with the surrounding fibres. consistencies in the reject outlet area suspension, so that the stock consisten- without any negative effect on separation cy of the surrounding suspension will With the EcoMizer concept, however, the efficiency. On the contrary, due to the also be decreased. addition of the filtrate is distributed over fact that the thickened reject stock is pre- a comparatively large volume, actually vented from flowing back in the vortex the entire lower cone area. Thus, it can centre, and because of the lower stock Comparison with traditional concepts be dosed much better. consistencies, the rotational speeds in the lower cone remain high and the trac- This type of dilution water addition has Furthermore, addition of filtrate is started tive forces acting on contaminants re- several advantages compared to previous in the centre of the cleaner and from main low. This means efficiency may concepts. there continues outwards. The layers even be improved in certain cases. Fiber Systems 15
Accepts
Fig. 5: Advantages of the new EcoMizer cleaner concept. Inlet
5 of the rejects, the stock consistency in Higher operational reliability at lower reject rates the bottom cone area still remains lower than with conventional cleaners. With Reduced number of cleaning stages (2-3 in stock preparation, higher inlet stock consistencies, new max. 4 in the approach flow) possibilities result concerning the Savings with respect to space require- arrangement of fine cleaning and slotted ments and additional investment costs for screening in recycled paper stock prepa- pumps and drives, piping and control ration systems. equipment