This Section is Currently Under Construction
      
      
       
      
       
      3.  PAPER MAKING 
      PROCESS
      Once the wood has been 
      reduced to pulp it is often made on a machine similar to a Fourdiner into 
      a semi-paper form known as “wet-lap”, for shipping to, or transport 
      around, the paper mill.  The paper mill receives the wet-lap as rolls, 
      bundles, or pallets of  pulp sheets.  The wet-lap usually requires 
      additional refinement and treatment before being used to create the 
      finished paper product.
      3.1 FIBER SLUSHING, 
      BEATING AND REFINING
      The wet lap and any 
      make-up materials, used in creating blends, must be mixed together, 
      repulped, beaten and refined, before it is suitable for making paper.  In 
      rag paper, the wet-lap cottons, and linens are measured by weight and 
      placed in a hydrapulper or digester with water, and “slushed”  back into a 
      pulp mixture. The digester disperses the fibers into the water with 
      minimal fiber damage, by gentle agitation and heated water. After the 
      wet-lap has been returned to pulp, it’s blown out of the digester and fed 
      into a breaking engine.
      The breaking engine and 
      Hollander are the same as discussed in section 2.  The main purpose of  
      beating engine (sometimes referred to as the “Bertram” after it’s 
      manufacturer) is to further breakdown the pulp into separate fibers and 
      filter out of any non-paper-making materials.  The beater roll is kept 
      well off of the bed plate and is gradually lowered ensuring that there are 
      no sheaves (fiber bundles).  After a short period of time in the breaking 
      engine, the pulp is transferred to the Holland beater, where the fiber 
      properties are further developed.
      
      
      Bertram Beater refining the pulp
      In the beater, the 
      outer fiber wall is removed and the fiber’s cells are allowed to swell.  
      At the same time the fiber length is adjusted by adjusting the distance 
      between the blades on the drum and the blades or surface of the bed 
      plate.  As the drum revolves the blades collect fibers on the leading edge 
      of the blade.  As the rotating blades approach the stationary blades the 
      fibers are either sheared or compressed between them, resulting in either 
      frayed or shorter fibers.  While the pulp is in the beater additives can 
      be introduced to alter the properties of  the finished paper.  Some 
      additives, such as clay (aluminum-silicate), Calcium carbonate or Titanium 
      dioxide are introduced to increase opacity and increase brightness; dyes 
      and pigments are added to adjust color and brightness, while Aluminum 
      Sulfate activated rosin and Synthetic Alkaline resins are added for 
      internal sizing.  Internal sizing helps the paper to resist water and ink 
      penetration.
      
      
      Pulp in the Bertram Beater
      After the beater, the 
      pulp is further manipulated by refiners.  Refiners increase the bonding 
      and surface areas of the fibers through a process known as fibrillation.  
      Fibrillation is the fraying of the very fine, threadlike structures, 
      called fibrils, that make up the fiber.  The degree of fraying and the 
      fiber length are determined in the same manner as the Hollander, by the 
      type of blades used, the distance between them, and the time spent in the 
      refiner.  Two main types of refiners are used for this purpose, the 
      conical refiner and the disk refiner.
      The most common types 
      of conical refiners are the Jordan and the Claflin.  Both refiners 
      consists of a stationary conical structure, lined with bars or blades 
      running in the same direction as its axis, and a rotating cone structure 
      called the “plug” which can be moved in or out of the stationary conical 
      structure.  The pulp enters the narrow end of the refiner and is forced 
      out near the large end.
       
      
      
      
      
      
      
      Disk Refiners can be 
      used to further refine stock from a beating engine or in place of it.  
      Disk refiners consist of at least two disk, that have bars or “ribs” 
      across their faces.  They are positioned face to face, so that one disk 
      can rotate, while the other disk is stationary or rotated in the opposite 
      direction.  The refiner can be configured so that four disk are used 
      instead of two, with two of the disk positioned back to back.  The pulp 
      enters either from the center and is discharged out through the perimeter, 
      or enters through the perimeter and is discharged through the center.
       
      
      
      
      
      
      
      
       Increase in refinement results in 
      decreasing fiber length, increase in intra-fiber bond breaking (internal 
      fibrillation), fiber end maceration (external fibrillation).  These 
      processes increase surface, bonding area, and fiber length continuity, 
      which increase the fold, tensile and bursting strength, density, and 
      retention of filler.  The increase in refinement, decreases fiber length, 
      which decreases the tearing strength and increases the paper’s sensitivity 
      to humidity, changes resulting in paper curling and dimension change.  
      Brightness and opacity are also adversely affected by higher levels of 
      refinement.
       Final Screening and 
      Cleaning
      3.2 HAND-MADE 
      PRODUCTION
      Hand-made paper making 
      can be separated into two categories, professional manufacturing and 
      amateur or artistic papermaking.  Professional hand-made production 
      represents the elite of the field.  The finest paper available is produced 
      by the professional hand-made process and requires the highest expertise 
      and skill.  The other category is composed of  the amateur or professional 
      artist who make paper from improvised or small operations, creating sheets 
      for aesthetical purposes.
      Professional hand-made 
      production, although relatively slow, labor intensive, and expensive, 
      produces the finest paper product available.  Because of these reasons 
      only the finest grades of linen and cotton are used.  The “rags” are 
      hand-sorted and pulped in small refining and breaking engines.  After 
      breaking and refining,  the pulp is screened and pumped into head-boxes or 
      stuff-chest, which in turn supply vats.  Three craftsmen, two skilled and 
      one lay, are tasked with forming the sheets of paper.  The skills of the 
      vatman and coucher determine the quality and consistency of the sheet.  To 
      form the paper the vatman uses a wooden frame, covered by a wire screen of 
      either a “woven” or “laid” pattern, called the “mold,” and a deckle.  The 
      deckle keeps the paper pulp from flowing over the edges of the mold.
      
       
      
      
       The exact method of 
      forming paper varies with each vatman, but the basic operation is the 
      same.  The vatman holds the edges of the mold about arms length with the 
      forming wire face up and the surface parallel to the surface of the pulp.  
      The vatman then dips the front of the mold/deckle into the vat submerging 
      approximately 3/4 of the mold/deckle.  The vatman raises the mold/deckle 
      and tilts it back towards himself than away causing a small ripple and 
      evenly distributing the pulp as the water flows through the screen.  He  
      then produces a side to side tilting or shaking motion causing the 
      settling fibers to orient themselves perpendicular to those already 
      settled.  The settling fibers are allowed to “set” and the excess water 
      allowed to drain.  The vatman is finished forming the sheet and places the 
      mold/deckle at an angle for further draining.  After a couple of minutes 
      the coucher takes the drying mold/deckle flips and allows the other side 
      to drain.  The coucher takes the mold/deckle and, while holding it at an 
      almost vertical angle, removes the deckle and places the mold face down 
      onto a felt.  The coucher then positions and places another felt on top of 
      the drying paper sheet.  The top felt must be placed with great care, any 
      surface disturbance will ruin the paper.  After a completed post (stack of 
      sheets) has been formed, the “layman” or “layer” removes the post to the 
      pressing room, where the post is placed into a hydraulic press and pressed 
      with 100 to 150 tons of pressure, removing the excess water.  The layman 
      then removes the sheets and creates another sandwich of paper and felt, 
      this time using felt board.  This pile is placed in press, under slight 
      pressure, overnight.  This is called “exchanging” or “parting” and can be 
      repeated depending on the type of finish desired.  
      Drying Sizing and 
      finishing can be done by hand or by machine depending on the size of the 
      operation and the size of the order.  By hand the paper sheets are hung in 
      drying lofts.  Sizing by hand involves quickly and skillfully skimming 
      sheets through a size vat without stretching the paper, or pooling the 
      size.  In another method sizing is performed by fanning out the sheets in 
      a shallow tank, immersing, draining and pressing.  There are also 
      continuous feeding machines that submerge the sheets through a size vat 
      and then presses and dries the sheets.
      3.3 FOURDRINIER 
      PAPER MACHINE
      The majority of paper 
      is manufactured on the Fourdrinier paper machine.  Nicolas-Louis Robert 
      developed his paper machine under the employment of paper maker Francois 
      Didot and applied for its patent in 1798.  Didot purchased the patent from 
      Robert in payments, but fell behind following confrontations between the 
      two.  Robert took back his patent, but not before Didot had given the 
      plans to his brother-in-law, John Gamble, who owned paper mill in 
      England.  Looking for investors, Gamble interested Henry and Sealy 
      Fourdrinier in the development of the machine.  Under the suggestion of 
      Gamble, the Fourdrinier brothers employed Bryan Donkin to build and 
      perfect the machine at the Frogmore mill, Two Waters, Hertfordshire, 
      England.  Because of a loophole in their patent, the Fourdrinier brothers, 
      like Robert, never received royalties from their machine.  But unlike 
      Robert, who was financially backed by Didot, the Fourdrinier brothers ran 
      into financial difficulty, due to lack of return on their investment.  
      Although they never received any monetary recognition of their efforts the 
      single forming wire machine carries their name.(hunter)
      The Fourdrinier paper 
      making machine is composed of  three main sections: the forming section, 
      the press section, and the dryer section.  A Paper slurry consisting of 
      around 0.5-1.0% fiber, is pumped into a box where it flows out through a 
      slot onto a moving wire belt.  Once on the belt the water is removed by 
      draining and suction, leaving the fibers to form a very wet, and weak 
      paper.  The paper is then pressed, heated, dried, resulting in a 
      continuous roll or “web” which can be further finished as desired or 
      required.
       
      
      
      
      SIMPLE REPRESENTATION OF THE  MODERN 
      FOURDRINIER PAPER MACHINE
 
      
      
      Wet end of a Fourdrinier paper machine.  Head 
      box is near the bottom.  The drying section is towards the back .
      3.3.1  FORMING 
      SECTION
      The forming section of 
      the Fourdrinier constitutes what is called the wet end of the machine and 
      is what the Fourdrinier brothers and their engineer, Donkin, perfected.  
      This section consists of the head box, the forming wire, foils, suction 
      boxes, couch roller, breast roller and dandy roll.
      Pulp is pumped from the 
      machine box through the screens and cleaners to the head box.  The purpose 
      of the head box is to deliver a uniform slurry to the forming wire.  There 
      are several different designs, but all incorporate a method to induce 
      turbulence (deflocculation), while preventing cross currents, which would 
      inhibit the uniformity of the stock.  The simplest design is the gravity 
      fed head box.  It uses height/weight level difference to force the pulp 
      through several baffles and a through a perforated rotating cylinder, 
      before flowing through the apron and slice.  A gravity-fed head box can 
      deliver an eight-inch stock depth at a rate of 400 feet/minute.
       
      
      
      If faster production 
      speeds are required the stock must be fed under pressure.  These machines 
      can operate at speeds greater than 4,000 feet per minute.  The pressurized 
      head boxes are usually hydraulic and the stock is forced through conical 
      injectors, through a perforated plate and through a horizontally split 
      apron and the slice.  The apron height and the slice height, which control 
      the jet of pulp can be independently adjusted by hydraulics. 
       
       
      
      
       
      The pulp flowing onto 
      the forming wire is approximately 0.5-1.0% fibers, with the make-up 
      consisting of water.  As the water is removed from the slurry, the fibers 
      settle onto the surface of a traveling wire, forming a wet mat of paper.  
      Therefore, the main objective of the forming section is the controlled 
      removal of water.  Originally gravity allowed the water to drain through a 
      brass forming wire 60-70 mesh per inch, 40-50 feet length and 70-90 inches 
      in width.  But as production speeds increased, more efficient methods were 
      developed.(Sindall)  The forming wire, now a fine polymer screen with 
      about 65 meshes per inch, carries the paper slurry over table rolls, foils 
      and suction boxes, providing precise control over drainage and agitation 
      control.  As the slurry exits the slice onto the wire, the water starts 
      draining from the suspension. Water jets are positioned over the edges of 
      the forming wire to control the width of web, creating what’s called the 
      deckle edge.  The first fibers forming the mat on the wire are oriented in 
      the direction of the machine; this is the wire side of the paper.  If the 
      rest of the fibers in the slurry were allowed to orient themselves in the 
      same direction, the paper would have poor tear resistance and surface 
      properties.  If gravity was the main method of dehydration, the machine 
      would have to be run at low speeds to overcome the orientation problem, 
      the alternative is to remove the water quickly while the fibers are still 
      agitated from the effects of the headbox. 
       The first set of 
      de-watering elements is a bank of table rolls.  In earlier designs, table 
      rolls were a series of small solid rollers.  If they are used today, they 
      much larger and are used as only the first water removal step.  The 
      rotation of the roll in contact with the covered wire causes a vacuum to 
      form between the two, which pulls the water from the web.
      
      
      Bank of table rolls removing the water 
      from the pulp
      With increasing speeds 
      the table rolls cause problems with paper uniformity and aren’t able to 
      remove enough water before the presses.  Foils have replaced most, if not 
      all of the table rolls.  Foils remove water using a doctor blade on the 
      bottom of the forming wire.  The blade causes a difference in pressures, 
      which draws water from the web behind the blade.  This method allows for 
      more control over the removal process and is not significantly affected by 
      machine speeds.
       
      
      
      
       
      
       Water removal can be further enhanced by 
      placing a vacuum on the foil drainage system.  The foil is essentially the 
      same as that diagrammed above with the addition of vacuum pumps. After the 
      foils, water is further removed using flat suction boxes.  The suction 
      boxes remove the majority of the water, changing the stock consistency 
      from 2% to 20% fiber content.  Above the first couple of suction boxes a 
      skeleton roll covered with wire may ride on the top of the paper mat.  
      This roll called a “dandy roll” compresses the paper, releasing any 
      trapped air and improving the surface.  The dandy roll can be covered with 
      various wire patterns, which may simulate the forming wire and may have 
      recessed or raised elements-designs imparting a watermark onto the paper.  
      In areas where the watermark elements, usually a wire design, are above 
      the surface of the dandy roll, fewer fibers are allowed to settle, and the 
      paper appears light.  If the watermark elements are below the dandy roll 
      surface, more fibers are allowed to settle than in the rest of the paper, 
      and the paper appears darker in these areas.
       
      
      
       
      Dandy 
      Roll
       An alternative to 
      using a dandy roll to create watermarks is the Molette.  The Molette is a 
      rubber stamp roll located before the wet press of the machine.  This type 
      of watermark actually embosses the paper and squeezes the fibers to the 
      edges of the stamp.
       
      3.4  TWIN WIRE 
      MACHINE
      A variation on the 
      Fourdrinier was developed in the 1960’s and employed the use of two 
      forming wire, allowing the paper mat to be dried from both sides 
      simultaneously.
      3.4.1  FORMING 
      SECTION
      The First Twin Wire 
      machines were constructed so that the headbox sprayed a vertical stream 
      between the forming wires at the nip of twin breast rolls.  The paper web 
      was then further drawn vertically, while vacuum boxes operate from both 
      sides.  Newer designs returned to a horizontal feed system with both 
      forming wires traveling horizontally and vacuum boxes drawing suction from 
      below and above the web.  Another variation is the use of a de-watering 
      mat above the suction boxes on a Fourdrinier; this is referred to as a 
      Hybrid Twin Wire Machine.
       
       
      
      
       
       
       
      
      
       
       
      3.5 CYLINDER MOLD 
      MACHINE
      In 1809, in 
      Hertfordshire, England, John Dickinson invented another mechanical method 
      of manufacturing paper, the cylinder mold machine.  Dickinson approached 
      the problem in a slightly different way then Nicholas-Louis Robert.  
      Instead of pouring fibers through the forming wire, his machine dipped the 
      forming wire into a vat, much in the same manner as hand made paper.  This 
      allowed him to create water marks and four-sided deckled edges comparable 
      to hand couched paper.
      The modern cylinder 
      mold machine, also known as “cylinder vat” or “mold made,” is used to make 
      fine bond paper with shadowed watermarks, currency and security papers, 
      art papers, extremely heavy stock, corrugated cardboards, and multi-ply 
      papers.
      3.5.1  FORMING 
      CYLINDER
      The key to the cylinder 
      mold machine is the use of a cylinder wire covered by the forming wire 
      (now called the cylinder blanket or cover), partially submerged in a vat 
      full of pulp.  As the cylinder rotates into the paper stock, the slurry 
      flows onto the surface of the cylinder, and the water flows through the 
      wire cover to the inside of the cylinder where it is discharged.  The 
      fiber mat that accumulates onto the cylinder surface is removed or 
      “couched” by a traveling felt belt.  This traveling felt “the cylinder 
      felt” is sometimes referred to as the forming wire, even though the paper 
      is already formed by the cylinder.  If multiple layer paper is desired, 
      several vats and cylinders can be placed in series with the paper web 
      acting as the cylinder felt for the additional paper mat.  There are two 
      main cylinder vat designs, contraflow and direct flow; and the cylinder 
      felt can be above or below the drying stock.
       
       
      
      
       
       
       
       
      
      
       
      3.6  PRESS SECTION
       
      After the paper has 
      been partially dried while on the forming felts and wires, it still 
      contains vast amounts of water which must be removed to stabilize and 
      strengthen the paper.  The first of these additional drying sections is 
      the press section.  The press section or “wet-press section” contains 
      several drying felts and suction pick-up (vacuum) rolls, which remove 
      water from the paper mat until it reaches about 50%.  Although the paper 
      web can support its own weight, carrier felts support the web, while at 
      the same time removing water from the surface and directing it through a 
      series of vacuum rollers.  The transference of moisture from the web to 
      the felt is enhanced by the nips (the contact points between the rollers) 
      of the rollers, suction boxes, and rollers. 
       
       
      
      
       
       
      
      
 
      3.7  DRYER SECTION
       
      After passing through 
      the press section, water is removed until the consistency of the web is 
      about 5-12 % water.  The removal of water is accomplished by a series of 
      steam heated drums “dryer cans,” which evaporate most of the water from 
      the web.  The web is forced against the dryer cans by the dryer felt (a 
      synthetic material that allows water vapor to pass through without 
      absorption).  As the water vapor leaves the dryer felt it is pushed away 
      by forcing air across the felt.  The dryer cans are usually around 4-5 
      foot in diameter and have highly polished shells.
        
      
      
       
      Dryer 
      Section
      Another type of drying 
      section utilizes a single large highly polished can instead of several 
      smaller cans.  This system, known as a Yankee dryer, is used with light 
      grades of paper, like tissue.
       
      
      
       
      3.8  FINISHING
      After the drying 
      section, the web is subjected to several finishing steps prior to shipping 
      it as a final product. The web can be sized, giving the paper surface 
      resistance, or if other properties are needed, the web can be surface 
      coated.  The web can also be supercalendered giving the surface a very 
      smooth the uniform surface.  In the final stages the web is rewound and 
      slit into two or more rolls and if needed sheeted.
      3.8.1  SIZING
      Sizing imparts 
      resistance to liquids on the paper surface, a property necessary for 
      paper  used for writing or printing.  Without external sizing, ink would 
      bleed and feather.  External or Surface sizing can either be performed on 
      the paper machine or on a stand alone unit. 
       Machine sizing can be 
      performed either by running the web through a size vat or by running the 
      web through a size press.  In the case of the size vat, the web, after 
      exiting the dryer section, is directed down into a vat and through another 
      set of drying cans.   Size presses are located after the between two dryer 
      sections and applies a coat of sizing by transference from rollers and the 
      metering is accomplished by the nip.
      The most common types 
      of sizing consist of pigments and starches, although animal glue and 
      glycerin can also be used (art and banknote papers). 
       
      Spray 
      sizing (starch) applied to the paper
       
      3.8.2  COATING 
      
      Coating paper may be 
      desirable or necessary to improve optical, printing/writing, and/or 
      functional properties.  Functional properties can be for protection form 
      liquids, oils, gases, chemicals, improve adhesion characteristics, improve 
      wear, or some other property.
      Coatings can be 
      classified as aqueous, solvent, high solids, or extrusion, coatings.  
      Aqueous coatings, used for commodity papers, contain water soluble binders 
      and are applied as a liquid.  Common aqueous binders are Casein, Starch, 
      Protein, Acrylics and Polyvinyl Acetates.  Solvent Coatings are used in 
      situations where the binders aren’t soluble in water and are used with 
      specialty papers. High solid and Extrusion coatings are used for 
      specialized papers, where chemical, gas or liquid resistance is 
      necessary.  High solid coatings are applied as a coating of monomers and 
      are polymerized by UV or electron curing.  Extrusion coatings are applied 
      as a molten film of wax or polymer.
      3.8.3  SUPER 
      CALENDERING, COCKLING, AND EMBOSSING
      After the chemical 
      processes have been completed, physical processes, like super calendering, 
      cockling, and embossing, can be used to create the desired surface texture 
      to the paper.  
      Super calendering uses 
      friction and pressure to create a very smooth and glossy paper surface.  
      The super calender consists of a stack of rollers having surfaces 
      alternating between steel and cotton in construction.  There is enough 
      pressure between the steel and cotton rollers to slightly compress the 
      cotton surface causing a drag.  The difference in surface speed on either 
      side of the nip creates friction, which polishes the paper surface.
      
      
      Calendering Rolls
      The cockle finish on 
      many bond writing papers is created by vat sizing the web then subjecting 
      it to high velocity air dryers under high tension, then under low 
      tension.  The finished paper is usually heavily sized and has the 
      characteristic rattle associated with high quality bond paper.
      Embossing is achieved 
      by running the web through an off-line press, where it is subjected to an 
      engraved cylinder.  The concept is similar to the dandyroll, but since the 
      paper fibers cannot be redistributed the surface of the paper is raised or 
      depressed.
      3.8.4  SLITTING, 
      SHEETING, AND SHIPPING
      Once the paper roll 
      (machine log) is reeled from the paper machine it is removed and 
      transferred to a rereeler or a machine winder.  A rereeler unreels the web 
      from the mandrels to create a full log.  During this process any defects 
      can be removed and the web spliced.  A machine winder is similar to the 
      rereeler, but is able to slit the web into multiple, narrower rolls.  
      These rolls can be further finished by supercalendering, embossing, etc., 
      sheeted, or wrapped and shipped.
      
      
      Paper roll at the winder
      If the finished product 
      is sheeted paper, the rewound rolls are transferred to machines known as 
      cutters.  The cutters can slit the web to form multiple narrower webs and 
      cut across the web creating sheets.  The paper rolls are placed onto a 
      stand at one end of the machine.  As the web unwinds it can be slit either 
      adjusting the web width or creating several parallel webs.  After the 
      slitters, the web travels under a revolving knife, which cuts the web into 
      sheets.  After being cut the sheets are jogged through an on-line 
      inspection system which checks caliper and dimensions.  If the sheet does 
      not conform it drops down into a sheeter for recycling as broke.  After 
      the cutters, the paper stacks are placed into guillotine trimmers, where 
      the edges receive their final trim.
      After trimming, 
      paper rolls have inner headers (circular disks) applied to the ends, are 
      wrapped with a heavy moisture resistant paper or plastic and sealed with 
      outer headers.  The sealed rolls are then placed flat, to prevent flat 
      spots from forming, and shipped.  Sheeted paper can be prepared for 
      shipping in various ways depending on the size of the finished product.  
      If the finished sheets are small, such as 8 1/2” X 11,”
      the sheets are stacked in junior cartons, cross 
      stacked on pallets, strapped and wrapped.  Similarly larger sheets can 
      also be carton packaged, strapped and wrapped.  Large orders, such as 
      those for printers, can be bulk packed on skids (slightly different 
      dimensions and design than a pallet), wrapped, and strapped.