Kraft process

Kraft process

The Kraft process (also known as Kraft pulping or sulfate process) describes a technology for conversion of wood into wood pulp consisting of almost pure cellulose fibers. The process entails treatment of wood chips with a mixture of sodium hydroxide and sodium sulfide that break the bonds that link lignin to the cellulose. The process name is derived from German "kraft", meaning "strength/power"; both capitalized and lowercase names ("Kraft process" and "kraft process") appear in the literature, but "kraft" is most commonly used in the pulp and paper industry.


The kraft process was developed by Carl F. Dahl in 1879, and a pulp mill using this technology started (in Sweden) in 1890.cite book |last=Biermann |first=Christopher J. |authorlink= |coauthors= |title=Essentials of Pulping and Papermaking |year=1993 |publisher=Academic Press, Inc. |location=San Diego |isbn=0-12-097360-X] The invention of the recovery boiler by G.H. Tomlinson in the early 1930s, was a milestone in the advancement of the kraft process.cite book |author= E. Sjöström |title= Wood Chemistry: Fundamentals and Applications |publisher= Academic Press|year= 1993] It enabled the recovery and reuse of the inorganic pulping chemicals such that a kraft mill is almost closed-cycle with respect to inorganic chemicals, apart from those used in the bleaching process. For this reason, in the 1940s, the kraft process surpassed the sulfite process as the dominant method for producing wood pulp.

The process

Wood chips are fed into vessels called digesters that are capable of withstanding high pressures. Some digesters operate in a batch manner and some in a continuous process, such as the Kamyr digester. Digesters producing 1,000 tonnes of pulp per day and more are common.cite web |url=] |title=Pollution Prevention Technologies for the BleachedKraft Segment of the U.S. Pulp and Paper Industry (see p 66) |accessdate=2007-09-11 |last=Woodman |first=Jocelyn |coauthors= |date=1993 |work= |publisher=U.S. Environmental Protection Agency] Wood chips and white liquor, a mixture of sodium hydroxide and sodium sulfide, produced in the recovery process, are added to the top of the digester. In a continuous digester the materials are fed at a rate which allows the pulping reaction to be complete by the time the material exit the reactor. Typically delignification requires several hours at 130 to 180 °C (265 to 355 °F). Under these conditions lignin and some hemicellulose degrade to give fragments that are soluble in the strongly basic liquid. The solid pulp (about 50% by weight based on the dry wood chips) is collected and washed. At this point the pulp is quite brown and is known as "brown stock". The combined liquids, known as black liquor (so called because of its color), contain lignin fragments, carbohydrates from the breakdown of hemicellulose, sodium carbonate, sodium sulfate and other inorganic salts.

One of the main chemical reactions that underpin the kraft process is the scission of ether bonds by the nucleophilic sulfide (S2-) or bisulfide (HS-) ions.

Recovery process

The black liquor is concentrated in multiple effect evaporator to 60% or even 80% solids ("heavy black liquor" [cite web|url=|title=Equipment to handle heavy black liquor|accessdate=2007-10-09] ) and burned in the recovery boiler to recover the inorganic chemicals for reuse in the pulping process. Higher solids in the concentrated black liquor increases the energy and chemical efficiency of the recovery cycle, but also gives higher viscosity and precipitation of solids (plugging and fouling of equipment). [cite web |url= |title=Second Critical Solids Black Liquor Scaling |accessdate=2007-10-09 |last=Hsieh |first=Jeffery S. |coauthors=Smith, Jason B. |date= |work= |publisher=Pulp and Paper Engineering, School of Chemical Engineering, Georgia Institute of Technology] [Ref patent
country=US |number=5527427 |status=granted |title=High solids black liquor of reduced viscosity and viscosity reduction method for high solids black liquor |gdate=1996-06-18 |invent1=Mualla Berksoy |invent2=Yaman Boluk |assign1=Optima Specialty Chemicals & Technology Inc
] The combustion is carried out such that sodium sulfate is reduced to sodium sulfide by the organic carbon in the mixture:

:1. Na2SO4 + 2 C → Na2S + 2 CO2

This reaction is similar to Thermo Chemical Sulfato Reduction (TSR) in geochemistry.

The molten salts ("smelt") from the recovery boiler are dissolved in a process water known as weak wash. This process water also known as weak white liquor is composed of all liquors used to wash lime mud and green liquor precipitates and is kept in a tank called weak wash storage tank. The solution of sodium carbonate and sodium sulfide resulted is known as "green liquor". This liquid is mixed with calcium hydroxide to regenerate the white liquor used in the pulping process through an equilibrium reaction (Na2S is shown since it is part of the green liquor, but does not participate in the reaction):

:2. Na2S + Na2CO3 + Ca(OH)2 ←→ Na2S + 2 NaOH + CaCO3

Calcium carbonate precipitates from the white liquor and is recovered and heated in a lime kiln where it is converted to calcium oxide (lime).

:3. CaCO3 → CaO + CO2

Calcium oxide (lime) is reacted with water to regenerate the calcium hydroxide used in Reaction 2:

:4. CaO + H2O → Ca(OH)2

The combination of reactions 1 through 4 form a closed cycle with respect to sodium, sulfur and calcium and is the main concept of the called recausticizing process where sodium carbonate is reacted to regenerate sodium hydroxide.

The recovery boiler also generates high pressure steam which is led to turbogenerators, reducing the steam pressure for the mill use and generating electricity. A modern kraft pulp mill is more than self-sufficient in its electrical generation and normally will provide a net flow of energy to the local electrical grid. [cite web |url= |title=Kraft pulping: Energy consumption and production
accessdate=2007-10-21 |last=Jeffries |first=Tom |coauthors= |date=March 27, 1997 |work= |publisher=University of Wisconsin Biotech Center []
] Additionally, bark and wood residues are often burned in a separate power boiler to generate steam.

Comparison with other pulping processes

Pulp produced by the kraft process is stronger than that made by other pulping processes. Acidic sulfite processes degrade cellulose more than the kraft process, which leads to weaker fibers. Kraft pulping removes most of the lignin present originally in the wood whereas mechanical pulping processes leave most of the lignin in the fibers. The hydrophobic nature of lignin [cite journal |last=Hubbe |first=Martin a. |authorlink=|coauthors=Lucian A. Lucia |year=2007 |month= |title=The "Love-Hate" Relationship Present in Lignocellulosic Materials |journal=BioResources |volume=2 |issue=4 |pages=534–535 |id= |url= |accessdate= 2007-09-15 |quote=|format=Dead link|date=May 2008 ] interferes with the formation of the hydrogen bonds between cellulose (and hemicellulose) in the fibers needed for the strength of paper (strength refers to tensile strength and resistance to tearing).

Kraft pulp is darker than other wood pulps, but it can be bleached to make very white pulp. Fully bleached kraft pulp is used to make high quality paper where strength, whiteness and resistance to yellowing are important.

The kraft process can use a wider range of fiber sources than most other pulping processes. All types of wood, including very resinous types like southern pine [cite web |url= |title=The Southern Pines |accessdate=2007-09-13 |author= |date=1985 |work= |publisher=US Department of Agriculture] , and non-wood species like bamboo and kenaf can be used in the kraft process.


In a modern mill, brownstock (cellulose fibers containing approximately 5% residual lignin), produced by the pulping is first washed to remove some of the dissolved organic material and then further delignified by a variety of bleaching stages. [cite web|url= |title=Environmental Comparison of Bleached Kraft Pulp ManufacturingTechnologies|accessdate=2007-09-28]

In the case of a plant designed to produce pulp to make brown sack paper or linerboard for boxes and packaging, the pulp does not always need to be bleached to a high brightness. Bleaching decreases the mass of pulp produced by about 5%, decreases the strength of the fibers and adds to the cost of manufacture.

Byproducts and emissions

In the case of softwood (conifer) pulping, a soaplike substance is collected from the liquor during evaporation. The soap is acidified to produce tall oil, a source of resin acids, fatty acids and other chemicals. Also turpentine originates from softwood.

Various byproducts containing hydrogen sulfide, methyl mercaptan, dimethyl sulfide, dimethyl disulfide, and other volatile sulfur compounds are the cause of the malodorous air emissions characteristic for pulp mills utilizing the kraft process. Outside the modern mills the odour is perceivable only during disturbance situations, for example when shutting the mill down for maintenance break. This is due to practiced collection and burning of these odorous gases in the recovery boiler along with black liquor. The sulfur dioxide emissions of the kraft pulp mills are much lower than sulfur dioxide emissions from sulfite mills. In modern mills where high dry solids are burned in the recovery boiler hardly any sulfur dioxide leaves the boiler. This is mainly due to higher lower furnace temperature which leads to higher sodium release from the black liquor droplets that can react with sulfur dioxide forming sodium sulfate.

The process effluents are treated in a biological effluent treatment plant, which guarantees that the effluents are not toxic in the recipient.

ee also

*Sulfite process
*Pulp mill
*Wood pulp
*Bleaching of wood pulp


External links

* [ US EPA article on Kraft pulping]
* [ Reference Document on Best Available Techniques in Pulp and Paper Industry by European Commission, 2001]

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