Paper Recycling Technology Detailed Part 1

advertisement

Paper Recycling Technology and Science

Dr. Richard A. Venditti

Paper Science and Engineering

Forest Biomaterials Department

North Carolina State University

Lecture:

Paper recycling and technology course introduction and objectives

Dr. Richard Venditti

Faculty member in the Paper Science and

Engineering Program in the Forest Biomaterials

Department at North Carolina State University

PhD in Chemical Engineering, BS in Pulp and

Paper Science and Chemical Engineering

Research areas:

 Paper recycling

Utilization of forest/agricultural materials for new applications

Life cycle analysis

Named a TAPPI Fellow in 2012

Relevant research projects:

– The detection of adhesive contaminants

– The changes in fibers upon recycling

– Automatic sorting of recovered papers

– Flotation deinking surfactants

– Agglomeration deinking

– Screening phenomena and pressure sensitive adhesives

– Deposition of adhesive contaminants

– Neural networks to control deinking operations

– Sludge conversion to bio-ethanol and to biomaterials

Course Outline

The US Paper Recycling Industry

Recovered Paper Grades and Contaminants

Effect of Recycling on Fibers/Paper

Unit Operations

 Pulping, Cleaning, Screening, Washing, Flotation,

Dispersion, Bleaching, …..

Image Analysis, Deinking Chemicals

System Design

Advanced/Additional Topics

Course Activities

Viewing of the Videos of Lectures

Base lectures by Venditti

Guest lectures from industry leaders

Homework assignments

Final Exam

Critical Issues in Recycling:

Going deeper into the recovered paper stream => poor quality material

Meeting paper specifications, which are getting more stringent

Increased demands for recovered paper from emerging countries

Requirements for recycling processes to be environmentally friendly

Requirements for recycling processes to compete with virgin pulps from an economic standpoint

Competition from digital communications

The student after passing this class should be able to address issues in these areas by applying the knowledge developed in this course

Course Student Outcomes:

 After passing this course, the student should have:

 A broad understanding of paper recycling technology and science

 An ability to interpret paper recycling issues correctly.

 An ability to make decisions based on paper recycling concepts to improve paper recycling operations

Lecture:

The US Paper Recycling Industry

Recovered Fiber, not “Wastepaper”

 Learning objectives

 Understand the trends of paper recycling in the industry

 Identify the major categories of recovered fiber what is done with them

Waste Hierarchy

http://www.epa.gov/wastes/nonhaz/municipal/hierarchy.htm

Example: What happens to catalogs?

Source: NCASI

Recycled Fiber Definitions

Secondary Fiber: fibers that have previously been used in a manufacturing process and have been reclaimed as raw material for another process.

Pre-consumer waste: any waste, printed or unprinted, generated in the fabrication or conversion of finished paper. Before use by a consumer as a final end product.

Post-consumer waste: Paper that has passed through the end usage as a consumer product.

Internal broke: off-specification paper that is repulped and used at the same site, not considered secondary fiber.

Recycled Fiber Definitions

 Recovery Rate (RR)

 how much paper is diverted from landfill

RR

=

100 %

Tons of Wastepape r Collected

Tons of Paper Consumed

 Utilization Rate (UR)

 fraction of recycled fibers contained in paper

UR

=

100 %

Tons of Wastepaper Consumed at Mills

Tons of Paper Pro duced

US Paper Recycling Recovery Rate:

1999

Total Paper Consumption: 105 million tons

Total Paper Recovered: 47 million tons

Recovery Rate: = 45%

2004

Total Paper Consumption: 102 million tons

Total Paper Recovered: 50 million tons

Recovery Rate: = 49%

2011

Total Paper Consumption: 79 million tons

Total Paper Recovered: 53 million tons

Recovery Rate: = 66.8%

Source: afandpa.org, 2011

Paper/board Recovery Rate in the US:

53.4%

Record high 66.8% RR.

Paper purchases declined (2.3 million tons) while recovered paper increased 1.3 million tons.

Source: afandpa.org, 2012

Municipal solid waste?

MSW: everyday items that are discarded by the public

Also referred to as trash, or rubbish

Includes packaging, food scraps, grass clippings, sofas, computers, tires and refrigerators, for example.

Does not include industrial, hazardous, or construction waste.

Source of MSW?

 Residential waste (houses and apartments): 55-65% of total MSW generation

 Commercial and institutional locations

(businesses, schools, hospitals..): 35-45%

Municipal Solid Waste Generation (US)

Source: EPA

Municipal Solid Waste Generation, Recycling, and Disposal in the United States: Facts and Figures for 2009

Trends in U.S. Waste Recycling

Adopted from EPA 2011 MSW Facts and Figures

MSW by Material Before Recycling

Source: EPA

Municipal Solid Waste Generation, Recycling, and Disposal in the United States: Facts and Figures for 2009

Products with highest % recovery.

Lead acid batteries, 96%

Corrugated boxes, 85%

Newspapers, 72%

Steel packaging, 69%

Major appliances, 65%

Yard trimmings, 58%

Aluminum cans, 50%

Mixed paper, 45%

Tires, 35%

Glass Containers, 31%

HDPE, milk containers, 29%

PET Bottles, 28%

Source: Wikipedia

Source: EPA

Municipal Solid Waste Generation, Recycling, and Disposal in the United States: Facts and Figures for 2009

Paper leads Packaging Recovery

2009 EPA. afandpa.org, 2012

Recovered and Landfilled Paper

Paper purchases declined (2.3 million tons) while recovered paper increased 1.3 million tons.

Source: afandpa.org, 2012

Where Recovered Paper Goes:

Source: afandpa.org, 2012

Where Recovered Paper Goes:

Use Tons Used

Source: afandpa.org, 2012

Exports and Imports of Recovered Paper

18

16

14

12

10

8

6

4

2

0

1990

Exports

Imports

1992 1994 1996 1998

Year

2000 2002 2004 2006

Recovered Paper Statistical Highlights, 2005 Edition, AF&PA

Recovered Paper Statistical Highlights, 2005 Edition, AF&PA

Major Recovered Paper Groups

Old Corrugated Containers (OCC), also known as corrugated cardboard: Mills use old corrugated containers to make new recycled-content shipping boxes, as well as recycled paperboard for product packaging (cereal boxes, shoe boxes, etc.). POST-CONSUMER

Old Newspapers (ONP): Mills primarily use old newspapers to make new recycled-content newsprint and in recycled paperboard and tissue, among other paper grades.

POST-CONSUMER

Office Printing and Writing Papers: Printing and writing papers collected from offices, businesses and homes. May be sorted to various extents. POST CONSUMER

Mixed paper: Mixed paper is a broad category that often includes items such as discarded mail, telephone books, paperboard, magazines, and catalogs. Mills use mixed paper to produce paperboard and tissue, as a secondary fiber in the production of new paper, or as a raw material in non-paper product such as gypsum wallboard, chipboard, roofing felt, cellulose insulation, and molded pulp products such as egg cartons. POST-CONSUMER

High Grade Deinked Paper: This grade is made of high grade paper such as letterhead, copier paper, envelopes, and printer and convertor scrap that has gone through the printing process. It must first be deinked before it can be reprocessed into high grade paper products such as printing and writing papers or tissue. PRECONSUMER

Pulp substitutes: A high grade paper, pulp substitutes are often shavings and clippings from converting operations at paper mills and print shops. Mills can use pulp substitutes in place of virgin materials to make back into high grade paper products. PRECONSUMER http://www.epa.gov/osw/conserve/materials/paper/basics/grade.htm

Grades of Recovered Paper

Mixed Paper

Super Mixed Paper

Boxboard Cuttings

Mill Wrappers

News

Special News

Special News De-ink Quality

Over-Issue News]

Magazines

Corrugated Containers

Double Sorted Corrugated

New Double-Lined Kraft Corrugated Cuttings

Used Brown Kraft

Mixed Kraft Cuttings

Carrier Stock

New Colored Kraft

Grocery Bag Scrap

Kraft Multi-Wall Bag Scrap

New Brown Kraft Envelope Cuttings

Publication Blanks

Flyleaf Shavings

Coated Soft White Shavings

Hard White Shavings

Hard White Envelope Cuttings

New Colored Envelope Cuttings

Semi Bleached Cuttings

Manila Tabulating Cards

Sorted Office Paper

Sorted Colored Ledger

Manifold Colored Ledger

Sorted White Ledger

Manifold White Ledger

Computer Printout

Coated Book Stock

Coated Groundwood Sections

Printed Bleached Board Cuttings

Misprinted Bleached Board

Unprinted Bleached Board

Mixed Groundwood Shavings

Telephone Directories

White Blank News

Groundwood Computer Printout

#1 Bleached Cup Stock

#2 Printed Bleached Cup Stock

Unprinted Bleached Plate Stock

Printed Bleached Stock

Scrap Specifications Circular, Guidelines for ….Paper Stock…

By: Institute of Scrap Recycling Industries, Inc.

Recovery of OCC

19 MMT used domestically, 8 MMT exported,

Purchases increased 7.2% in 2010, Recovered OCC increased by 11.2%

Source: afandpa.org, 2012

Uses of OCC

19 MMT used domestically, 8 MMT exported,

Purchases increased 7.2% in 2010, Recovered OCC increased by 11.2%

Source: afandpa.org, 2012

Recovery of ONP (mechanical)

Includes ONP, uncoated mechanical, and coated ONP inserts.

7.5% decrease in consumption of ONP

Source: afandpa.org, 2012

Recovery of

ONP

(mechanical)

Source: afandpa.org, 2012

Recovery of Printing Writing Papers

Purchases of PW Papers declined by 5%.

Source: afandpa.org, 2012

Source: AF&PA, 2006 Recovered

Paper Annual Statistics

Recovered Paper Prices,

$/short ton, FOB sellers dock

Recovered Paper Prices, $/ton

Grades

Corrugated Cardboard

Old Newsprint

Box Board

Old Magazines

Mixed Paper

Sorted Office Paper

White Ledger

White Envelope

8

9

64

114

135

LTL

2/08

48

36

33

24

28

104

266

370

TL

2/08

130

108

90

4

8

57

102

121

LTL

2/09

20

18

17

12

25

93

238

331

TL

2/09

55

54

45

TL

1/10

125

100

75

ScrapIndex.com

Lecture:

Introduction to papermaking fibers

The Structure of a

Paper Sheet

Slides courtesy of Med Byrd and Mike Kocurek

The Structure of a

Paper Sheet

Where do papermaking fibers come from?

 Fibers to make paper are produced in a pulping process.

 Pulping: to liberate fibers for papermaking

 Process depends upon the raw material!

Is paper 100% fibers?

 No, the following are also added to paper depending on the grade:

 Starch

Polymers

Inorganic particles: like clay, calcium carbonate, titanium dioxide

Waxes

Coatings

Optical brighteners

Dyes

More…….

Pulping Processes

 For virgin pulps (produced from wood or other plants)

 mechanical pulping

 semi-chemical pulping

 chemical pulping

 For recycled pulps

 repulping of paper in water (like a blender)

So if we start with WOOD?

 Wood is a matrix or composite material, with cellulosic fibers held rigidly in a lignin-hemicellulose matrix

 Since paper is made from individual fibers, they must be liberated from the overall matrix – this is done in the pulping process

What is Pulping ?

Wood – stiff, hard, tough material; useful for building and structures, but useless for papermaking

Fibers – thin, long, flexible, collapsible tubes; perfect for suspending in a water slurry and forming a papermaking

web

Hardwoods and

Softwoods

Softwoods

Longitudinal

Cells

Ray

Cells

Longitudinal cells used

For transport.

Horizontal fibers used for

• Storage (Starch,

Hemicellulose,

Oils, Water)

• Transport across the stem

Fiber ends

Fiber ends

Ray Cells

Volumetric Composition –

Soft wood

91 - 94% Longitudinal Fibers

6 - 9% Ray Cells

Average Fiber Dimensions -

SoftWoods

Region Length Diameter

Redwood NW 6.1

Loblolly Pine S 3.6

Longleaf Pine S 4.9

White Spruce NE

Red Cedar

3.3

NW 3.5

.05-.065

.035-.045

.035-.045

.025-.03

.030-.04

All dimensions in mm

Hardwood

HW and SW Cells

Softwoods Hardwoods

Conduction Springwood Vessels

Support Summerwood Fibers

Storage Ray Cells Ray Cells

a Softwood fiber b,d,e Vessel segments c Hardwood fiber

Average Cell Diameter:

Vessels .020 - .500 mm

Fibers < .020 mm

Cellular Composition

Fibers

Vessels

Parenchyma

Softwood

90%

0%

10%

Hardwood

27-76%

7-55%

5-25%

Hardwood vs Softwood

Softwood and hardwood pulp have different properties and consequently different uses .

Softwood pulp can be made out of pine and spruce. The longfibre pulp:

 reinforcement pulp for improved runnability on the paper machine paper board for strength

The short-fibred hardwood pulp is made from oak, gum. It is used in the manufacture of printing papers.

 enhances printability end use properties (smoothness)

Pulping

Here is a micrograph of wood

Here are two individual fibers glued together with lignin

CLEARLY, to get pulp, at the very least these fibers must be separated somehow

PULP

 This is the industry’s term for the mass that results from the conversion of wood

(or other plant materials) into its individual unit fibers

Types of Pulping

 There are three basic ways to convert wood into a fibrous pulp mass

 The method to use depends on the final paper product desired and how good the quality has to be…..

 But what it ultimately depends upon is: how much lignin do we want to remove? None?

All? And where from?

Where’s the Lignin?

The cell wall has MOST of the lignin in the fiber… but it is distributed over a lot of volume

(low concentration)

The middle lamella (ML) has a small amount of lignin… but it is in a concentrated form to glue the fibers together

Different Wood Pulping Mechanisms

NO LIGNIN

REMOVAL

SOME LIGNIN

REMOVAL

TOTAL LIGNIN

REMOVAL

MECHANICAL

PULPING

SEMI-CHEMICAL

PULPING

CHEMICAL

PULPING

Chemi thermomechanical

(24% lignin)

Semi-chemical

Carbonate or

Chemical Pulping

Direct Heated Batch Digester

Chip Chute

Chip Loading Floor

Chip Pile P

T

Chip Conveyor Belt

Digester Relief

White Liquor

Black Liquor

Digester

T

T

Steam Blow Line

ClO

2

Bleaching Sequence

ClO

2

NaOH

O

2

NaOH

ClO

2

Bleached

Pulp

D (EO) D E D

Unbleached

Pulp

Usually done with multiple stages using different chemicals

ClO

2

= Chlorine Dioxide (D)

NaOH= Sodium Hydroxide (E)

O

2

= Oxygen (O)

Bleach

Towers

A Chemical Pulp Fiber

Long, intact fibers

Few fines

Fiber wall mostly or fully free from lignin; maximum internal bonding possible

Smooth, lignin-free surface -- responds well to refining

Groundwood Process

Debarked logs forced against a revolving abrasive stone

This action grinds the fibers off the log

APPLIED PRESSURE

WOOD

MAGAZINE

SHARPENING

LATHE

FINGER BARS

PULPSTONE

SHOWER

BURR

PIT

WEIR

A Mechanical Pulp Fiber

Most or all of lignin still in wall; interferes with internal bonding

Lots of fines & debris

Cracks and tears in wall

Lignin patches on surface

Surface already fibrillated Fiber cut

SOUTHERN PINE

CHEMICAL PULP

SOUTHERN PINE

MECHANICAL PULP

WITH FINES

Chemical Pulp Sheet

Mechanical

Pulp Sheet

What’s Good About Leaving

Lignin in the Fiber?

 Produces bulky, porous sheets

 Lignin and fines are good lightscatterers; sheets have good opacity

 Lignin permits high filler loading

 Leaving lignin in is good for economics

(yield, capital, operating)

 For low value newsprint, leaving lignin in is good!!!

What’s Bad About Leaving

Lignin in the Fiber?

 Lignin on fiber surface interferes with fiber-fiber bonds

 Lignin inside cell walls inhibits collapsibility and internal bonding

 Lignin makes paper darker, especially degraded lignin like in unbleached kraft

 Lignin absorbs UV light and produces sheet yellowing and premature degradation, example: newsprint

Summary:

Chemical vs. Mechanical Pulps

 Chemical pulping generally delivers longer, stronger, cleaner, brighter pulps with lower opacity and higher cost (if bleached, brown if not bleached)

 Mechanical pulping generally delivers shorter, weaker, dirtier, lower-brightness pulps with great bulk, opacity, and cost

 The worse characteristic of mechanical pulps is they turn yellow with age

Recovered Paper:

Virgin Wood Pulping Process Matters

There are many grades of recovered paper

However, paper is recycled according to its virgin pulping method

Bleached chemical pulps: white (ledgers and others…)

Unbleached chemical pulps: brown (corrugated containers and others…..)

Mechanical pulps: initially grey and yellows (newsprint and others…..)

It should be noted that these groups are used ideally by themselves to produce products

Most grades of paper predominantly consist of one of these fiber types

Very inexpensive paper products use mixes of these (like shoe boxes)

Summary:

Chemical vs. Mechanical Pulps

 Chemical pulps that have been bleached have almost zero lignin, are white and make good printing paper

 (printing and writing papers such as copy paper)

 Chemical pulps that are not bleached are brown and strong

 Used mostly for linerboard

 Mechanical pulps are low value, low cost fibers that yellow,

 reasonable for newsprint and cheap catalogs and directories

Lecture:

Grades of recovered paper

Recycled Fiber Definitions

Virgin Fiber: produced directly from wood in a pulping process

Secondary Fiber: fibers that have previously been produced in a manufacturing process and have been reclaimed as raw material for another process.

Pre-consumer waste: any waste, printed or unprinted, generated in the fabrication or conversion of finished paper.

Before use by a consumer as a final end product.

Post-consumer waste: Paper that has passed through the end usage as a consumer product.

Internal broke: off-specification paper that is repulped and used at the same site, not considered secondary fiber.

Recovered Paper

 There are many grades of recovered paper

 They are characterized mainly (from a practical standpoint) by the paper products that they contain

However, paper is recycled in groups according to its virgin pulping method (scientific)

 Bleached chemical pulps: white, typically mostly HW (short)

Unbleached chemical pulps: brown, typically mostly SW (long)

Mechanical pulps: grey and yellows with time

It should be noted that these groups should optimally be recycled by themselves to produce products

 Most grades of paper predominantly consist of one of these fiber types, but stray amounts of the other types are often present

Recovered paper is recycled into what products?

Printing and writing recovered paper (bleached chemical) recycled into:

Printing and writing

Tissue

Old Corrugated container (unbleached kraft and semi-chemical) recycled into:

 Linerboard and fluted medium

 Tube stock

Old newspapers (mechanical pulps) recycled into:

 Newspapers

Folding cartons

Molded pulp products like egg cartons

Tissue

Mixed papers

 Any low valued product

Why have recovered paper grades?

Type, cost and quality of recovered paper are critically important to the design and operation of a paper recycling mill.

The type of fibers existing in the recovered paper have an enormous effect on the resulting recycled paper properties.

Why have recovered paper grades?

 Recovered paper grades serve:

Classify the various types of recovered paper

Describe the type of paper included in a grade

Specify general quality requirements in the grade

Provide a basis for establishing the market value of a recovered paper grade

The market value of a recovered paper grade depends on:

Optical properties of the fibers contained (brightness, color..)

Types of fibers (chemical fibers, mechanical fibers)

Types of fibers (softwood versus hardwood)

Types of materials applied to the papers (clay coatings, wax, xerographic inks, wet strength agents……)

The presence and amounts of various other types of paper present in the grade

The presence and amount of contaminant s in the grade

Recovered Paper Prices, $/ton

Grades

Corrugated Cardboard

Old Newsprint

Box Board

Old Magazines

Mixed Paper

Sorted Office Paper

White Ledger

White Envelope

8

9

64

114

135

LTL

2/08

48

36

33

24

28

104

266

370

TL

2/08

130

108

90

4

8

57

102

121

LTL

2/09

20

18

17

12

25

93

238

331

TL

2/09

55

54

45

TL

1/10

125

100

75

ScrapIndex.com

The cost of fiber:

The cost of fiber:

Recovered

Paper

Grades

Reference

Guidelines for Paper Stock: PS-2013—Domestic

Transactions Paper Stock: Domestic Transactions

Preamble: These standards and practices apply to paper stock for repulping only and are for use in the United States, Canada, and

Mexico. Transactions may be modified by mutual agreement between

Buyer and Seller.

Basic to the Success of any Buyer-Seller Relationship is an

Atmosphere of “Good Faith.” In keeping with this, the following principles have been established:

Seller must use due diligence to ascertain that shipments consist of properly packed paper stock and that shipments are made during the period specified.

Arbitrary deductions, cancellations and/or rejections by the Buyer are counter to acceptable good trade practices.

Seller shall provide the quality of paper stock agreedupon but shall not be responsible for the use of the paper stock or of the manufactured product.

Scrap Specifications Circular, Guidelines for ….Paper Stock…

By: Institute of Scrap Recycling Industries, Inc.

Guidelines for Paper Stock: The Purchase Agreement

 Quantity

Short tons, 2000 lb

Metric tonnes, 2204.6 lb or 1000 kg

Order complete when +/- 5% is shipped

Grade Specified as in the Guidelines

Packing type specified

 Bales, skids, rolls, pallets, boxes, secure bundles or loose

Pricing and terms

Shipping terms

" FOB shipping point " or "FOB origin" indicates the buyer pays shipping cost and takes responsibility for the goods when the goods leave the seller's premises.

F.O.B. delivered means that the price given to the customer represents all costs needed to delivered the product to the customer's home or business

Shipping instructions

Shipping period

Scrap Specifications Circular, Guidelines for ….Paper Stock…

By: Institute of Scrap Recycling Industries, Inc.

Definitions

Out-throw:

 “all papers that are so manufactured or treated or are in such a form as to be unsuitable for consumption as the grade specified”

Prohibitive Material:

 material in excess of specified maximum make the recovered paper unusable as the grade specified

Any materials that may be damaging to the equipment

Sorted material must be free of food, medical, hazardous waste

Wax, unless agreed to be accepted by the buyer

Scrap Specifications Circular, Guidelines for ….Paper Stock…

By: Institute of Scrap Recycling Industries, Inc.

Example:

 News, De-ink Quality #7. Consists of sorted, fresh newspapers, not sunburned, containing not more than the normal amount of rotogravure and colored sections.

 Prohibitive Materials None Permitted

 Total Outthrows may not exceed ¼ of 1%

Scrap Specifications Circular, Guidelines for ….Paper Stock…

By: Institute of Scrap Recycling Industries, Inc.

Grades: Some mixed grades

Grades: Containing Mechanical

Pulps such as ONP

Grades: Old Magazines, typically recycled with ONP into recycled newsprint , can be both mechanical and chemical fibers tend to have a lot of inorganic material in fillers and coatings

Grades: Unbleached kraft, such as old corrugated containers

Grades: Bleached kraft, called High grades or ledger grades, white paper such as copy paper

Grades: Also called ledger, Bleached kraft, but with colored paper

Grades: Food containers

Grades from Food Applications:

Glossary

Glossary

Lecture:

Common Contaminants in

Recovered Paper

Common Contaminants in Wastepaper

Large Junk

 metals: nuts, screws, foil, cans

 plastics: films, bags, envelopes dirt cloth, yard waste, leather, etc.,

Inks & toners

 Stickies

 Coatings

 Fillers

 Papermaking additives

Common Contaminants in OCC

http://www.ct.gov/dep/cwp/view.asp?A=2714&Q=324858

Printing

 Approximately ½ of all paper produced is printed.

 Printing is constantly changing:

 New inks

 New techniques

 New demands on paper

 Slides courteousy of Joel J. Pawlak,

NCSU.

Inks & Toners

 Primary constituents

 Pigments- colored portion, most often carbon black

 Resins – binds the pigments to the surface of the paper, supplies gloss, resists the pigment from penetrating the paper

 Solvent – makes the ink fluid so it will run on the press

 Additives to provide viscosity, tack, lightfastness, oil resistance, rub resistance

Propel droplets of ink onto paper.

Often made of water, glycol, dyes, or pigments.

Most widely used computer printer and very cheap.

Ink Jet

Image: OKI Printing

Image: PC Tech Guide

Xerography

Commercially important for short run printing.

Toners are thermoplastic resins (water insoluble plastics) with carbon black

Melted onto the sheet

Produces large plastic flakes that are insoluble in water

Then heat to melt the toner to the surface of the paper.

Letter press

 Letterpress- one of the oldest processes

 Ink applied to raised surface only

Flexography

 Flexography –

Flexible letterpress

 Very few requirement for the paper

 Water or solvent

 Usually used for “low quality” applications

– Grocery bags

– Corrugated Container

Four Color Flexo Stack

Flexography

Offset Lithography

 Lithography – Flat surface with ink absorptive and repellant areas.

 Offset means the chemically modified plate doesn’t touch the paper.

 Dominant share of the printing market

Ink Absorptive

Ink Repellant

Lithography

Four color litho print

Lithography

Basic Offset Lithography Printing Press

Rotogravure

Printing

 Gravure

 Ink transported in recesses of printing cylinder

 Highest quality printing process

– Pigment: 27%

– Zinc resonate: 22%

– Toluene: 51%

 Used for high quality printing like currency

Ink in Recesses

Print Plate

Inks & Toners

Type

Simple Letter

Press

Newsprint and

Offset

Component

Pigment +

Mineral Oil

Pirgment +

Soft Resin &

Mineral Oil

Drying System Ink Resin Film Particle Size

(microns)

Absorption into Web

Weak 1-15

2-30 Penetration of

Vehicle into

Web + Resin

Oxidation

Soft Film

Hard Film

Rotogravure Pigment

+Hard Resin &

Solvent

Flexographic Pigment +

UV Cured

Resin & Water

Emulsification

Pigment

+Monomer

Specialty Various

Pgiments and

Rosins

Solvent

Evaporation

Amine

Absorption,

Evaporation

UV

Photopolymeri zation

Heat set or

Other

Hard Film

Water

Resistant Film

Non swelling,

Non saponif.

Hard Film

Hard,

Coherent

Films

2-250

N/A

50-100

40+

End Products

Letterpress

Early

Newsprint

Newsprint,

Books

We Offset,

Letter Press

Magazines,

Catalogues

Newsprint inserts,

Corrugated

High Speed

Coated

Papers

Xerography

Laser Printers

Electronic

Forms

Issues with some inks

 Xerographic inks (toners)

 Small toner particles are melted together to form letters for instance

 After pulping, these can generate large plate like particles (40-400 microns) that can not be floated or screened

 Sometimes have fibers attached or are attached to fibers, are not ink-like

Issues with some inks

 Water based flexographic inks in ONP:

 Disperse in the water system readily but make the water black and unusable

 Are too small (0.3-1 microns) and hydrophillic to be floated

Contaminant Size vs. Removal Efficiency

Stickies

Currently the most challenging problem in paper recycling

Stickies: contaminants in pulp that have the potential to deposit on solid surfaces

Typically organic materials:

Man made stickies: adhesives, coatings…

Natural stickies: pitch, resins..

May deposit on papermachine wires, press felts, dryer fabrics, calendar rolls and cause significant down-time on machine

Are hard to remove in recycling due to often having a neutral density, and an ability to flow and change shape

Stickies

Stickies

Fillers as a Contaminant

Fillers are added to paper to improve brightness, smoothness, and printability

Fillers are cheap

Fillers decrease the strength of paper

Common fillers:

 clay

CaCO3

TiO2

Fillers are washed out of the pulp and lower the overall yield of the recycling process

Fines are characterized as having a length of less than 200 microns, or 0.2 mm, most filler materials are in the 0.1-10 micron range

Fillers are not desirable in some paper products such as tissue paper

Hurt softness

Hurt the creping blade during tissue making

Fillers as a Contaminant

 These are calcium carbonate filler particles of about 0.7 micrometers median size.

Fillers as a Contaminant

 Clay, from Hubbe (left). Clay particles magnified by an electron microscope. drainchem.com.au (right)

Papermaking Additives

 Additives such as starch, gums, retention aids, etc., are lost during recycling and lower yield

 Additives such as dyes can cause the fibers to not make color specifications, this is also a problem with fluorescent dyes

 Wet strength additives cause the paper to be unpulpable in many cases, making the entire paper product unusable and thus, a contaminant

 For instance the wet strength beverage carrier boxes that hold sodas and beers…

Coatings as a Contaminant

 Coatings typically contain inorganic fillers and polymeric binders

 Coating binders can behave as stickies, sometimes termed white pitch

 Coating fillers are washed out of the pulp and lower the overall yield of the recycling process

 Board is often coated with wax

 Wax can cause recycled paper to be weak and slippery

 Wax can deposit on machinery

Coating

Base Stock

Coating

What is coating?

May be any type of fiber.

Must be uniform in the MD and CD.

Low to no water resistance.

Pre-Coat

(optional)

Pre-Coat

(optional)

Coating Formulation

Coating Operations

There are three main components to a coating color:

Water

Pigment

Binder

All but the simplest formulas will have additional components known as additives such as:

Flow modifiers

Colorants

Optical Brighteners

Etc.

Coating Formulation

Coating Operations

Pigments

 Pigments – the major component of the coating color. Usually made up of inorganic particulate material similar to fillers.

 Typical pigments include:

 Clay – most widely used

 Calcium Carbonate – second most widely used

TiO

2

– high brightness, but expensive

Aluminum Oxide – usually used in combination with TiO

2

Contaminant Removal

Contaminant Size vs. Removal Efficiency

Lecture:

Collection, sorting, storage of recovered paper

Collection of Recovered Paper:

Sources

Recovered paper dealers or brokers

Directly from the site of a recovered paper collection drive

From recovered paper collection facilities owned by the recycling paper company

From paper converting facilities

From large office complexes

From stores

From individuals in their private vehicles

Collection of Recovered Paper

Commercial Recycling

Businesses supply recovered paper or board to collectors

Often collectors give businesses a baler for employees to place the paper, and a trailer, only if the volume warrants the investment

The collector and business agree on a contract about volume, pricing and length of contract

Collector picks up the paper

Collection of Recovered Paper

 Typical volumes of OCC produced from different sources: http://www.ct.gov/dep/cwp/view.asp?A=2714&Q=32

4858

Collection of Recovered Paper

Residential Recycling

People put curbside waste out for disposal

Single stream recycling means that all paper, plastics, glass, and metals that can be recycled are put together

Yields of recyclables go up when people don’t have to sort at their house

Municipalities pick up single stream waste streams

Municipalities enter into contracts with material recovery facility

MRF pays for the waste stream

This material is separated for OCC, newspaper, mixed papers

Also recover aluminum, steel, glass, plastics and others

Also produces a residue

Transportation of Recovered Paper

Recovered paper can be transported by truck, barge, container, rail

Recovered paper is typically

Baled

Loose http://www.mass.gov/dep/recycle/approvals/dsconv.pdf

Warehouse Operations Bales:

 ONP bales from municipal waste sorting facility

Warehouse Operations Loose Paper:

 Old newspapers and old magazine warehouse

Example Bale Sizes and Weights

GRADE

No. 6 News

OMG

No. 41 Manifold

White Ledger

Mixed Office

Waste

OCC

SIZE (W H L)

36x48x60 in

30x40x72 in

30x40x72 in

30x36x60 in

30x30x50 in

30x48x60 in

WEIGHT (lb)

2000

1400

1700

1400

1000

1000

Tappi Deinking Short Course, 1995

Storage of Recovered Paper:

Warehouses

 Storage of the paper in a warehouse includes protection from:

 Sunlight

Wetting by rain

Fires

Excessive humidity

Aging (rotation of the inventory)

Animals

Storage of Recovered Paper:

Warehouses

 Rotating the inventory can be important, for example for ONP:

Brightness of pulp decreased by 6% when the paper was aged by 3 years

Tensile strength of the paper decreased by 30-50% when the paper was aged by 3 years

Tappi Deinking Short Course, 1995

Storage of Recovered Paper:

Warehouses

 The size of the warehouse depends on how much inventory must be carried, typically they run from 3-90 days of inventory

 Inventory desired depends on:

Price fluctuations

Nature of contracts entered into

Short and long term supply of recovered paper

Space available for the warehouse

Availability of off-site storage

Average distance of recovered paper transportation

Operating hours for receiving paper

Capital cost of warehouse

Manpower to run warehouse

Cost of operation of the warehouse

Storage of Recovered Paper:

Warehouses

 After the inventory size, other factors determine how big the warehouse must be to store bales:

Height of stacks of bales

Height allowance between top of stacks and sprinklers

Length and width of bale piles

Width of corridors

Other space requirments, such as conveyors, wire cutters, truck docks, locker rooms, offices

Areas for loose paper

Storage of Recovered Paper:

Warehouses

 After the inventory size, other factors determine how big the warehouse must be to store loose paper :

Height of the recovered paper stored within the walled areas

How many walled areas

Length and width of the walled areas

Height allowance between top of piles and sprinklers

Allowance for room to allow vehicles to operate

Other space requirments, such as conveyors, wire cutters, truck docks, locker rooms, offices

Storage of Recovered Paper:

Warehouses

 Prior to use or putting recovered paper into inventory, inspections are sometimes done

 Bale structure

 Visually inspected for appearance of unwanted papers

 Checked for identification tag

 Sometimes broken open and inside inspected, but not often

Storage of Recovered Paper:

Staging for Pulping

 For a batch pulper,

 the required number and type of bales must be assembled to meet the batch requirement

 Often batches are blended, for example ONP and

OMG are added at a definite ratio (OMG assists in brightness and in deinking)

 Strapping wires sometimes must be taken off and cut

 Bales are often broken, providing a better inspection of the paper

 Often want to rotate the inventory

Storage of Recovered Paper:

Staging for Pulping

 For a continuous pulper,

 the proper mix of ages and grades are assembled on a conveyhor

 Wires or straps are cut and removed sometimes

 Bales are often broken, providing a better inspection of the paper

 Often want to rotate the inventory

Warehouse Operations Bales:

Old newspaper and old magazine warehouse

Unloading bales out of a truck

Warehouse Operations Bales:

 Old newspaper and old magazine warehouse

Bales

Bobcat forklift

Bales of Recovered

Paper

Warehouse Operations Bales:

Old newspaper and old magazine warehouse

Moving a Bale

Bales of Recovered

Paper

Warehouse Operations Bales:

 Raw material for a municipal waste sorting facility

Warehouse Operations Bales:

 Bales of old newsprint coming out of a baler at the MRF

Warehouse Operations Bales:

 ONP bales from municipal waste sorting facility

Warehouse Operations Bales:

 Mixed Bales from municipal waste sorting facility

Warehouse Operations Bales:

 Low quality OCC from municipal waste sorting facility

Warehouse Operations Bales:

 OCC from municipal waste sorting facility

Warehouse Operations Bales:

 Low quality mixed waste from municipal waste sorting facility

Recovered OCC bale storage

Recovered OCC bale storage

Bobcat with front clamps

Loading OCC bales on pulp conveyor

Wire bale cutter

Pulp conveyor

Bale falling into pulper

Pulper

Bale falling into pulper

Pulper

Warehouse Operations Loose Paper:

 Old newspapers and old magazine warehouse

Warehouse Operations Loose Paper:

 Old newspapers and old magazine warehouse

Warehouse Operations Loose Paper:

 Old newspapers and old magazine warehouse

Warehouse Operations Loose Paper:

 Pre-consumer old magazines

Warehouse

Operations

Loose Paper:

 Old newspapers and old magazine warehouse

Outdoor storage of bales uncovered:

 ONP Recycling mill in South

Africa

Outdoor storage of bales covered:

 ONP Recycling in Canada

Lecture:

Papermaking fiber types and the effect of recycling on strength properties

Effect of Recycling on Fiber

Properties

 Learning objectives

 Understand how recycling affects chemically pulped fiber

 Understand how recycling affects mechanically pulped (lignin containing) fibers

Different Wood Pulping Mechanisms

NO LIGNIN

REMOVAL

SOME LIGNIN

REMOVAL

TOTAL LIGNIN

REMOVAL

MECHANICAL

PULPING

SEMI-CHEMICAL

PULPING

CHEMICAL

PULPING

Effects of Recycling on Chemical Pulps

 Mechanical damage

 Loss of fines

 Hardening and stiffening (hornification)

 Weakening of bonding

 less fiber conformability

 less absorptive

 loss of hemicellulose

 Decreased cleanliness

Effect of Virgin Chemical

Pulping

Fiber wall structure as in the tree.

Chemical pulping removes lignin from cell wall. The cell wall is swollen with water when refined.

Hornification: Irreversible

A Wet kraft fiber before drying

B 30% consistency (Irreversible processes begin to occur)

C 30-75% consistency

D >75% consistency

Hornification: Irreversible

Never Dried

Fiber

Rewetting

Fiber Swollen

With Water

Dried Collapsed

Fiber - Hornified

Does not Re-swell

Effect of Recycling on Chemical Pulps

Chemically pulped fibers that have never been dried:

 have the ability to swell with water which makes the fibers flexible can be mechanically treated (refining) to increase the swelling and flexibility

The flexible never dried fibers are able to conform in the paper sheet which increases the fiber bonded area making strong paper

When dried, the fibers become rigid, termed hornification

They do not swell on re-wetting as much

They do not bond as well in paper

Effect of Recycling on Chemical Pulps

 Previously dried fibers, upon exposure to water, do not swell and do not become flexible

These rigid fibers break upon refining: causing fines

When paper is made, the rigid fibers do not conform in the paper sheet and the resulting low fiber bonded area produces a weak sheet

Flexible Fibers Stiff fibers

Effects of Recycling on Chemical Pulps

Effect of Recycling on Mechanical Pulps

Wood containing pulps from mechanical pulping processes have lignin (a three-dimensional crosslinked polymer) which makes fiber walls stiff and deters water swelling

The stiff, somewhat round cross section fibers make virgin paper with low fiber bonded area and weak fiber bonds

Therefore, the strength of never dried mechanical pulps is generally lower than of never dried chemical pulps

Recycling may improve properties of mechanical pulps by flatening and flexiblizing the fibers

“Different behavior than chemical pulps on recycling”

Effect of Recycling on Mechanical Pulps

1st Use

80 %

20%

2nd Use

70 %

30%

3rd Use

60 %

40%

Effects of Recycling on Mechanical Pulps

10

9

8

7

6

5

4

3

2

1

0

0

Paper Strength vs. Number of Times Recycled

(Howard and Bichard, 1st Res Forum on Recycling, Oct 1991, CPPA)

Bleached Kraft (Chemical Pulp)

Groundwood (Mechanical Pulp)

1 2 3

Number of Recycles

4 5

Effects of Recycled Fibers on the

Papermaking Process

 Lower freeness: decrease machine speeds or add drainage aid

 Lower paper strength: more sheet breaks

 Low efficiency of chemical additives (fines and anionic trash)

Increased deposits

Decreased cleanliness

Refining of Recycled Fibers

 Because recycled fibers are more brittle, the refining process that is used must be of low intensity in order to avoid too much fiber cutting and fines generation

Lecture:

Basic Paper Recycling process terms

Learning objectives

Understand the following terms

 Moisture Content

 Consistency

 Dissolved solids

 Charge on Pulp

 Yield

 pH

Moisture content (%)

Some slides in this section courtesy of Dr. Med Byrd and Dr. Hasan Jameel at PSE

NCSU

Moisture content (%)

Paper is hygroscopic, meaning it has a natural tendency to absorb

The MC in paper depends on the humidity of the air

The MC in paper depends on the composition of the paper

Ref: The Effect of Moisture on Paper. Helen U.

Kiely, Chief Chemist American Writing Paper

Company, Inc. 1927. The text contained herein was written by Helen U. Kiely, and delivered by

Joseph H. Burgen before the Joint Session,

Connecticut Valley Mill Superintendents and

Printing House Craftsmen, March 5th, 1927.

Consistency

The term consistency, as used in the pulp and paper industry, is defined as the percentage of weight of oven dry fibrous material in stock (pulp and additives) and water

.

It is very similar to % solids, the difference is that % consistency only measures the suspended materials and not the dissolved solids.

Fibers in water: suspended solids

Table salt in water: dissolved solids

When fibers are involved, consistency is the more appropriate term to use.

Consistency

 The definition of consistency may be expressed as:

Stock

• Fibers

• Liquor

• Water

• Dissolved solids

Consistency

When you think about it, knowing the dry fiber content of a given process stream is critical.

 We measure production rate based on dry fiber, not water.

 We dose (charge) chemicals into the process based on dry fiber, not water.

 We calculate the yield of a given process based on dry materials, not water.

 But most of our process streams have both water and fiber !

Consistency

The moisture-free portion of a given sample of pulp or pulp slurry is known as the oven-dry (OD) weight , sometimes known as the bonedry (BD) weight .

It is standard in our industry to use an oven at 105 C to gently dry samples for consistency testing, until they no longer lose weight.

T 240 om-88. The hand sample method consists of manually selecting and weighing a representative sample, removing the water, drying the sample, and weighing the remainder.

• Fibers

Stock • Water

• Liquor

• Dissolved solids

Consistency: Example 1

• A scoop is used to take a sample of pulp slurry from an agitated tank that is known to have 44,000 pounds of total slurry in it.

The contents of the scoop are weighed, and the weight is 385 grams. The sample is put into a beaker and placed in an oven at 105 C overnight, so that all the water is driven off. In the morning, the dry contents of the beaker are weighed, and the weight is 23.2 grams (more properly, 23.2 OD grams).

 A. What is the consistency of the tank contents?

 B. What is the total dry fiber content of the tank?

Consistency Example 1

Part A.

Consistency Example 1

Consistency Example 2

Types of Consistency Sensors

 Pressure Drop

 Mechanical – static or rotating

 Optical

 Microwave

 Sonar

Increasing accuracy

Increasing cost

Pressure Drop

 Locate two pressure taps some distance apart in stock line

 Thicker stock increases friction loss, causing higher pressure drop

 Correlate pressure drop with consistency

 Works only on thicker stock (2-10 % consistency)

Calculated

Consistency

Smart

Controller

P Tap 2

Stock Flow

Tap 1 P

Mechanical -- Static

 As stock gets thicker, drag on items in line gets higher

 Insert wheel, paddle or other linkage into stock flow; attach to strain gauge; correlate drag/strain with consistency

 Good for thick stock

 Newer models very reliable and repeatable

Mechanical -- Rotating

 A small impeller or wheel is driven in the stock stream

 The force required to drive it or the resistance is measured and correlated to consistency

 Reportedly more accurate and less prone to plugging/fouling than the static sensors

Mechanical -- Rotating

Optical

 Most popular method for bleached stock; very accurate

 Polarized light source directed into stock stream; detect how much reflected back

 As consistency rises, reflected light increases

 Works best on bleached stock and thin stock (down to 0.1 % consistency)

Calculated Consistency

Polarized

Light Source

Stock Flow

Detector

Microwave

 New sensor type -- even more accurate than optical, and reportedly more robust

 Works on bleached or unbleached stock

 Not sensitive to filler content

 Works on thicker stock

 Based on attenuation of microwave signal

Microwave Source

Stock Flow

Detector Calculated Consistency

Sonar

 Newest sensor type

 Emitter sends acoustic signal down pipeline

 Based on reflected signal, an amazing amount of information can be gained

 Velocity

 Volumetric flow

 Consistency

 Amount of entrained air

Consistency

Consistency, % Moisture

Content, %

Description

0 – 6 % 100 – 94 % Known as low consistency stock

– slurry behaves like water

Is easily pumped with normal centrifugal pumps.

Where Found

Pulp mill – blow tank, stock lines, screens, washer vats

Paper mill – stock preparation, refining, headbox, after gravity drainage zone on fourdrinier

6 – 18 % 94 – 82 % Known as medium-consistency stock – stock starts to behave more like a solid mush than water

Little to no free liquid drains from it when held in the hand; must be pumped with special pumps

Pulp mill – washer discharge mat, bleaching reaction towers, storage tanks (known, unfortunately, as highdensity storage tanks)

Paper mill – after vacuum zone on fourdrinier

18 % and higher

82 % and lower

Known as high-consistency stock

– stock behaves like a crumbly solid; feels damp

No free liquid can be squeezed out by hand; usually move by conveyor or screw.

Pulp mill – high-consistency oxygen bleaching reactor (if used)

Paper mill – after press section of paper machine (50 %), after dry section of paper machine (95 %)

Relationship between

Moisture Content and Consistency

 Consistency (%) + MC (%) = 100 %

 The Moisture Content of a sample is equal to

(100 % - Consistency, %).

 The Consistency of a sample is equal to

(100 % - Moisture Content, %).

DISSOLVED SOLIDS

Stock

• Fibers

• Liquor

• Water

• Dissolved solids

MASS AND VOLUME IN

PAPERMAKING

• In the paper industry, it is always important that we know how much dry fiber is either contained in a given place (a tank, a batch) or how much is flowing through a pipe or system.

This means that we need to know the MASS of what is in the place or moving past some point in time.

The funny thing is this: we don’t normally measure mass or mass flow rate – it’s much easier for us to measure volume or volumetric flow rate.

We need to learn to convert between volume and mass

Convert Volume to Mass:

EXAMPLE 3

Convert Volume to Mass:

EXAMPLE 3

Convert Volume to Mass:

EXAMPLE 3

Charge on Pulp

Chemicals are added to pulp as a fraction (or percentage) of the oven dry solids in the pulp, which is called a “charge on pulp”

For instance, a deinking chemical might be said to be charged at

2% on pulp

What that means is that the mass of the deinking chemical to add is equal to 0.02*(OD mass of the fiber )

Example, we have 1000 lbs of pulp stock at 10% consistency and we want to charge a bleaching chemical at 5% on pulp, how much of the bleaching chemical do we charge?

Answer,

• the amount of OD fiber is 0.1*1000 lb total pulp stock = or 100 lbs of OD fiber

• If we charge 5% of the bleaching agent then we charge

0.05*100 lbs of OD fiber = 5 lbs of bleaching agent to add

YIELD

Yield is defined as the amount of product that comes out of some process, relative to the amount of material that went into the process.

In the paper industry, yield is ALWAYS defined in terms of moisture-free material going in or out – that is, it is based on dry fiber (oven dry).

Yield is important, because it helps us understand where our raw material is going – how much is lost during screening, how much is dissolved during bleaching, how much is lost during washing, etc.

YIELD EXAMPLE

pH

 pH stands for “potential of hydrogen” and refers to the concentration of hydrogen ions (H + ) in water or whatever liquid is being measured.

 In more everyday terms, pH is a unit of measure for determining if a liquid is acidic or basic (alkaline). Something that is neither acidic nor basic is referred to as neutral.

 You may have encountered the term pH in relation to the water in a fish tank or swimming pool. Bad things can happen when pH levels are either too high or too low.

THE pH SCALE...

 How is pH measured in numbers?

 pH is measured on a scale of 0.0 to 14.0.

Numbers < 7.0 = acidic

Numbers > 7.0 = basic

A pH of 7.0 indicates a neutral liquid pH= -log [H + concentration]

If the amount of H + goes up 10X, the pH only decreases by 1.

The power of the log scale

pH

 Adding acids or bases to water changes its pH.

 Acids lower the pH of water by increasing the

H+ concentration.

 Acid examples: sulfuric acid (H

2

SO

4 acid (HCl), vinegar (acetic acid, CH

3

), hydrochloric

COOH)

Bases raise the pH of water by increasing the

OH- concentration.

 Bases examples: caustic (NaOH, sodium hydroxide), ammonia (NH

3

)

Lecture:

Pulping of recovered paper

Pulping of recovered paper

Definition

Pulper : A device whose main objective is to convert recovered paper into a slurry of well

separated fibers and other waste paper

components.

Pulping of recovered paper

The pulping operation is the first and probably the most critical operation in paper recycling.

Proper pulping is a requirement if unit operations downstream (cleaning, screening, flotation…..) are to be effective.

Incorrect pulping conditions can irreversibly damage fibers making them inappropriate for papermaking uses.

Pulping

Main Function :

Disperse recovered paper into separated fibers.

Several sub-objectives that are also important :

1. Detach contaminants from fibers.

2. Mix paper with water and chemicals at the correct ratios.

3. Maintain contaminants as large as possible to aid subsequent removal processes.

4.

Avoid damage to the fibers (fiber cutting).

5. Removal of large debris from system.

Basic Pulping Categories :

Batch vs. Continuos Pulping

Batch Pulping : The feed recovered paper, water and chemicals are all charged at the beginning of the process and are removed all at once at the end of the process. The batch process is repeated.

Continuos Pulping : The feed recovered paper, water and chemicals are continuously added to the pulper and at the same time, the pulped product is also being continuously removed.

Basic Pulping Categories :

Low vs High Consistency

Consistency (solids) 100 * solids wt solids wt + liquid wt

= % K

Low Consistency Pulping

:

Typically from 3-6 % K. Produces a relatively easily pumpable fluid. The fluid is

“pourable”.

High Consistency Pulping: Typically from 8 - 18 % K. Produces a thick, slurry that will not flow under the influence of gravity alone.

General Parts of a Pulper

1. Wastepaper feed method (conveyor).

2. Pulper tub.

3. Rotor - spinning device for agitation, mechanical energy input

to the system.

4. Baffles - protrusions to assist in mixing and prevent swirling.

5. Dilution water.

6. Pulper exit.

Forces in a Pulper

 Mechanical Forces

These are caused when the fast moving rotor impacts material in the relatively slower body of pulp stock around it.

 Faster rotor speeds cause more intense mechanical forces in the pulper.

Pulper Forces

Hydraulic Forces :

These are caused by the motion of fluid that is caused by the spinning rotor (not by the direct impact of the rotors).

When two adjacent portions of a fluid are moving in different directions ( or at different speeds) a shear force is present. An example in the picture would be at point A.

A

Forces in a Pulper

Attrition

Mechanical shearing forces that occurs between the moving rotor and a static extraction plate near the rotor.

The rotor forces fiber bundles between the rotor and extraction plate. Intense hydraulic forces act to cut the fiber bundles and fibers. This can cause significant damage to fibers.

Used only for low % K pulping because the pulp must be screenable.

Low Consistency Pulping

Consistency from 3 -6 %.

Low profile rotor that rotates at high speeds.

Motion of rotor causes a vortex of pulp stock. The baffles are used to improve mixing.

High mechanical force due to impacts of rotor can damage fiber and break contaminants.

Pulper Types: High Consistency

Typically 8-18 %.

High profile rotor used. The helical screw type rotor is needed to “pull down” the non-fluid like high % K stock, from the top to the bottom of the pulper.

At the high % K, fiber-fiber

(solid-solid) rubbing dominates the forces experienced in the pulper.

Comparison of Low vs High Consistency Pulping

Rotor/ tank volume is much higher for high % K pulping. This is needed to maintain proper motion of non - fluid pulp stock at high % K.

Specific power is higher for high % K due to the higher viscosity pulp stock that must be pulped.

However, the specific power consumption per ton of paper is significantly lower for high % K pulping.This is due to high % K pulping having more tons of fiber for the amount of same pulping volume as a low

% K pulper. Also, the relatively less amount of water at high % K pulping causes less energy to be expended on moving water.

Comparison of Low vs High Consistency Pulping

Rotor speed is slower for high % K, causing less damage to fibers via mechanical forces of rotor.

Attrition forces are not used for high % K pulping. This decreases fiber cutting and contaminant breakage.

RESULTS of above: higher tensile, burst and tear strength for high %K pulping

High consistency pulping includes more fiber to fiber rubbing.

RESULTS of above: This action increases detachment of contaminants from fiber surfaces. The detachment of ink from fibers is especially important for washing and flotation deinking.

Comparison of Low vs High Consistency

Pulping

 Printing and writing grades consist of a high content of fully bleached hardwood and softwood fibers that are susceptible to damage => gentle high consistency pulping is preferred

Further printing and writing grades need ink detachment => high consistency pulping with lots of fiber-fiber rubbing is preferred

OCC recycling, a historically older technology, typically has low consistency pulping because unbleached fibers are less susceptible to damage

Screening and Junk Removal in Pulper

 One of the sub- objectives of pulping is to remove large debris that enters the system.

 Examples of large debris :

wood

wet-strength paper

plastics

 baling wire

nails and bolts

 The removal of debris serves two important functions.

Protects equipment downstream from damage.

Prevents plugging of downstream equipment.

Examples of Debris Removal Methods

Different pulpers have different methods to remove debris, examples of common methods follow.

High Consistency Batch Pulping

HC pulper with Dilution Zone

HC pulper with Detrasher

Low consistency Pulping

Continuos Low consistency pulper with Ragger and junk tower.

Continuos Low consistency pulper with a de-trashing system

High Consistency Batch Pulper with

Dilution Zone

The pulper is designed so that during pulping at 15 -

18% K the pulper volume is only partially full.

At the end of the pulping cycle, dilution water is added to achieve a 5 - 6 % K.

After dilution, accepted stock passes through an extraction plate with holes about 3/4 - 1 inch diameter.

Finally, large debris is flushed from the pulper through a large rejects opening on the side.

High Consistency Batch Pulper with

External Detrasher

The pulper is “full” at high consistency during pulping.

At the end of the pulping dilution water is added at the bottom of the pulper diluting the pulp in the bottom to less than 6 %.

A large opening on the bottom/side of the pulper is used as the exit for the pulper contents.

The pulp and debris are separated by an external detrasher.

Note : There is no extraction plate in the pulper.

Note: drawing not to scale.

Continuos Low Consistency Pulper with

Ragger and Junk Tower

Low consistency continuos pulper typically have an extraction plate that accepts pulped fibers and rejects debris and unpulped flakes.

The extraction plate/ rotor can cause attrition, resulting in fiber cutting.

A junker is used to collect unpulpables such as bolts or rocks.

This debris is thrown out of the pulper into a junk tower where it is removed.

A ragger is also used in many cases to remove bale wire, strings, plastics, etc. The ragger is a continuos “rope” formed by entangled debris. The “rope” is continously pulled out of the pulper and cut into sections and disposed.

Common in OCC mills.

Recovered OCC bale storage

Loading OCC bales on pulper conveyor

Wire bale cutter

Pulper conveyor

Bale falling into pulper

Pulper

Ragger removing debris from the pulper surface

Ragger pulling rejects

out of pulper

Junker Claw

Continuos Low Consistency Pulper with

Ragger and Junk Tower

Low consistency continuos pulper typically have an extraction plate that accepts pulped fibers and rejects debris and unpulped flakes.

The extraction plate/ rotor can cause attrition, resulting in fiber cutting.

A junker is used to collect unpulpables such as bolts or rocks.

This debris is thrown out of the pulper into a junk tower where it is removed.

A ragger is also used in many cases to remove bale wire, strings, plastics, etc. The ragger is a continuos “rope” formed by entangled debris. The “rope” is continously pulled out of the pulper and cut into sections and disposed.

Common in OCC mills.

Example Detrashing Process

recycle

Light rejects

Rotor with screen plate

Heavy rejects

Accepts

Drum Pulping

A continuos, high consistency pulping method.

Most often used for pulping old newsprint.

Consists of an inclined rotating drum 11 -17 rpm through which the paper/ pulp travel down. The drum is very large approximately

10 feet high and 100 feet long.

High Consistency Drum Pulper

Conveyor

High % K

Zone

Screening

Zone

Rejects

Accept

Pulp

Drum Pulping

Two Zones

High Consistency pulping zone

Low consistency pulping zone.

High Consistency Pulping Zone

Paper ,water and chemicals added to ^ 15% K.

Baffles on the walls of the drum lift the paper and drop causing defibering in a gentle manner.

Low Consistency Screening zone

Water is added to dilute stock 3-

4% K.

Pulped fibers pass through 6 mm holes and are accepted from the pulper.

Large rejects continue through the pulper and are4 discharged at the end.

Drum Pulping

Two Zones

High Consistency pulping zone

Low consistency pulping zone.

High Consistency Pulping Zone

Paper ,water and chemicals added to ^ 15% K.

Baffles on the walls of the drum lift the paper and drop causing defibering in a gentle manner.

Low Consistency Screening zone

Water is added to dilute stock 3-4% K.

Pulped fibers pass through 6 mm holes and are accepted from the pulper.

Large rejects continue through the pulper and are4 discharged at the end.

Overview

Rejects

Advantages

Gentle pulping keeps contaminants large and minimizes fiber degradation.

Simple operation that includes screening.

Disadvantages

High capital cost.

Not an aggressive pulping method

(example: cannot pulp wet strength papers).

Drum Pulping

rejects exit

Paper Feed

External Pulping Complementary

Equipment

 Often the pulper is within a loop

 Some operations may send back material to the pulper to be further pulped

 Some operations aid in the removal of large debris

 Other operations add more mechanical action to assist in pulping

High density cleaners

High Density Cleaner: removes large heavy rejects from pulp

Objective: separate large heavy contaminants from fibers to protect downstream equipment from damage and pluggage

How it works: centrifugal forces separate materials mainly due to density/size

Feed

Light weight

Rejects

Detrasher

Heavy

Rejects out the back

Accepts

Example detrashing unit

 Top View

Objective: pulp unpulped pieces of paper/board and separate contaminants using a screen or centrifugal forces to protect downstream equipment from damage and pluggage

Deflakers

Objective: impart mechanical energy to break up flakes of unpulped material.

Pulping Summary

 Several methods to pulp

 Main objective: defiberize

 Secondary Objectives:

 Remove Large Debris

 Detach contaminants

 Not destroy fibers

 Mix

 Final Thought: If pulping is not done properly, subsequent processing steps will be ineffective and product quality will be unacceptable

Lecture:

Screening

Screening

Screening separates contaminants based mainly on size, but also on shape and deformability

Performed by presenting a barrier for large contaminants (slots or holes) that allow fibers to pass through

Screening

0.001 inch = 1 Mil = roughly 25 microns = .025 mm

Modes of Removal

1.

Stiff particles with all 3 dimensions larger than width of slot or diameter of hole are rejected

2.

Stiff particles with one or two dimensions smaller than width/diameter have a probability of rejection.

Rejection Probability, %

100%

50%

0%

1-dimension (rod)< slot size

2-dimension (plate) < slot size

1 2 3 4 5

Number of screen contacts

Screening Types and Conditions

Screen

Type

Screen

Openings, mm

Rotor circumference speed,m/s

20-30

Consistency Range

MC

<6%

Yes

MC

<4.5%

LC

<1.5%

Disk Hole

2-3

Cylindrical Hole

0.8-1.5

Cylindrical Slot

0.1-0.4

10-30

10-30

Yes

Yes Yes

Screening

 Types of perforations

 coarse holes .110 in or 2.7 mm

 fine holes .060 in or 1.52 mm

 coarse slots .010 in or .254 mm

 fine slots .006 in or .152 mm

 Also, the fibers offer a resistance to passage, related to the consistency

Example of Disk Screen

Pressure screen

Pressure Screen Principle to Prevent

Blinding of Screen

The leading edge of the rotating foil accelerates the stock.

The negative pulse under the sweeping foil momentarily reverses the flow, effectively purging the screen openings.

Pressure Screen Flow

Configurations

 Holes

 Slots

 Contoured

Screen Plates

Effect of Reject Rate & Plate

Opening on Screen Cleanliness

Screening Factors

Screening Factors

Screen Performance Variables

 Stock characteristics

 fiber type, debris characteristics, debris level

 Screen design

 flow configuration, plate cleaning mechanism, perforation type (holes or slots), rotor speed

 Operating variables

 stock flow rate (pressure drop across screen), feed consistency, reject rate, screen plate perforation size, stock temperature, dilution flow to screen

Screening

Screen Layout:

Always have cascaded screens to save fiber.

Primary Screen

Accepts

Secondary Screen

Tertiary Screen

Rejects

Open Gravity Screen

Summary Pressure Screen:

Objective: separate large contaminants from fibers

Can act as barrier screen or probability screen

Typically cascaded to save fiber

Typical conditions to promote increased throughput can have negative impact on cleanliness efficiency.

Lecture:

Centrifugal cleaning

Centrifugal Cleaning

 Remove impurities from the pulp stream based mainly on density

 Centrifugal cleaners remove

 metals

 inks

 sand

 bark

 dirt

 etc.,

Centrifugal Cleaning

 Principles of operation

 Centrifugal cleaner uses fluid pressure to create rotational fluid motion in a tapered cylinder

Rotational movement causes denser particles to move to the outside faster than lighter particles

Good fibers carried inward and upward to the accepted stock inlet

Dirt held in the downward current and removed from the bottom

Three Basic Cleaner Types:

High Density Cleaner: separates very large, heavy contaminants such as rocks, staples, glass. Used after pulping (early in the process) to protect downstream equipment. Diameter = 300-700 mm.

Forward Cleaners: separates fine, heavy contaminants such as a sand and inks. Also called cyclones, hydrocyclones, or cleaners. (Described above) Diameter = 70-400 mm

Through Flow Cleaner: separates fine, light contaminants such as glues, adhesives, plastics, foam. Also called light-weight cleaners or reverse cleaners. Diameter = 100-400 mm

Many other variations………….

Types of Cleaners: Functional Differences

 Consistency

 HC cleaner: 2-4.5% K, MC: 1-2, LC: 0.5-1.5

 Centrifugal Acceleration

(acceleration due to gravity =9.8 m/s2)

 HC cleaner: <60 g, MC: <100g, LC: <1000 g

 Reject Rate by mass/stage

 HC cleaner: 0.1-1% , MC: 0.1-1%, LC: 3-30%

Centrifugal Cleaner: Features and Flow

“Bank Arrangement” of Cleaners

Accepts Header

Feed Header

Rejects Header

Several cleaners are piped in parallel fashion.

A single cleaner is not capable of providing enough through put for typical industrial flows.

Forward Cleaners

 Canister

Cleaners

Cleaners Pump

Typical Cleaner “Curve”

Separation Ratio: m(in) – m(acc) / m(in) m= mass flow contaminant

Effective

Separation

Equal

Distribution

Reject Ratio: OD mass flow reject / OD mass flow inlet

Cascade Arrangement of Cleaners

Dilution Water

ACCEPTS

FEED

Primary

Cleaners

Secondary

Cleaners

Dilution Water

Dilution Water

Tertiary

Cleaners

REJECTS

High Density Cleaner

High density cleaners

Rejects

Through Flow Cleaner: removes low density contaminants

Feed

Also note, that reverse cleaners are another type of cleaner used to remove low density contaminants.

Reverse cleaners look like a forward cleaner except the top middle port is the rejects (and is smaller) and the bottom cone tip is the accepts (but is wider), picture not shown here.

Accepts

Thru-flow cleaners

Centrifugal Cleaner Performance Variables

 Stock Characteristics

 fiber type

 contaminant characteristics (size, shape, density), dirt level

 Cleaner Design

 body diameter, feed inlet configuration, accept diameter, cylindrical section height, cone angle, spiral grooves application, reject rate control method (fixed orifice and back pressure)

Parameters Affecting Hydrocyclone

Cleanliness Efficiency

Operating

Variable increase in:

Pressure Difference

Volumetric Flow

Cyclone Diameter

Consistency

Flake Content

Temperature

Reject Rate

Flushing Flow

Cleanliness

Efficiency

Incr/Decr

Incr/Decr

Decrease

Decrease

Decrease

Increase

Increase

Decrease

Sensitivity to

Variable

High

Medium

High

High

Medium

Low

Medium

Medium

Effect of Particle Properties on Separation

Particles with large density differences wrt water are removed more effectively

Particles with density near 1 g/cm 3 may separate from fibers

 Larger particle at same density will be removed more effectively than smaller particle

 Particles of the same density but with favorable hydrodynamic shape (c w

A p

) separate more effectively, eg, a sphere is better than a flat plate, since rejected particles must swim against the main currrent towards the accepts

Fundamentals

Force balance on a single particle in a hydrocyclone axial

F d

F d

F c

F g radial

Radial direction:

Net centrifugal force ↔ Drag force

Axial direction:

Net gravitational force ↔ Drag force

Tangential direction:

– Assume: particles move along with fluid

Fundamentals

 One dimension analysis of single particle

F d F c

(or F g

)

Assume the time for particle to reach its terminal velocity is very brief m

⋅ dU s

= dt

F c

( or F g

)

F d

0

=

F c

( or F g

)

F d

F c

( or F g

)

=

F d

 Particle slip velocity,

U s

= velocity of water – velocity of particle

Net centrifugal force

Drag force

 ρ p u t

2 r

− ρ l u t

2

V p r

=

1

2

ρ l s

2

U A C d

U s

=

2 u t

2 V p r A p

ρ p

− ρ l

ρ l

1

C d for radial direction

C d

= drag coefficient r

= radial position

V p

= volume of particle

ρ ρ l

= density of particle and fluid u t

= tangential velocity of fluid

A p

= projected area of particle

Fundamentals

Why is the slip velocity important ?

For high U s

U s

For low U s

U s

=

2 u t

2 V p r A p

ρ p

− ρ l

ρ l

1

C d

Reject stream

U s

Accept stream

 High u t

(tangential velocity)

High ρ p

(particle density)

 Low C d

(drag coefficient)

Object tends to be rejected

Cleaner Summary

 Several types of cleaners

 Objective: remove high/low density contaminants

 Must reject material to operate effectively

 Several forces/operational variables/particle characteristics that combine to determine effectiveness in removal

Download