PULPING AND BLEACHING
Paper industry uses wide variety raw materials employing different type of pulping and bleaching processes depending on the type of raw materials and requirement of pulp furnish for final paper making. Both unbleached and bleached pulp is produced to meet the requirement of paper. Requirement of bleaching chemicals are also varying depending on the quality of paper and brightness and environmental considerations for cleaner and greener paper. Various steps in pulping and bleaching process is given in Table M-III 2.1. Pulping and bleaching play important role in providing strength to paper depending on fibre length, cellulose content. Commonly used term in pulping is given in Table M-III 2.2.
Table M-III 2.1: Puling and Bleaching Process
Table M-III 2.2: Commonly Used Terms in Pulping
Terms | Description |
White liquor | Cooking Liquor obtained after causticising green liquor containing NaOH, Na2S, and small quantity of Na2CO3 |
Black liquor | Liquor obtained after washing of pulp after cooking which is further concentrated for burning in furnace to recovered chemicals |
Green liquor | Liquor obtained after dissolving smelt from furnace in weak liquor from causticising section |
Active alkali | NaOH +Na2S |
Effective alkali | NaOH+1/2 Na2S |
Total titratable alkai | NaOH +Na2S+Na2CO3 |
Sulphidity | Na2S/Titratable alkali |
Causticity | NaOH/ NaOH +Na2S |
Causticising Efficiency | NaOH/ NaOH +Na2S )] x 100 |
Reduction | Na2S/( Na2SO4 + Na2S ) |
Over all recovery | Recovery ± black liquor stock/ froth liquor consumed |
K.No.(Permangnate | No. of 0.1 N KMnO4 consumed by 1 gm of moisture |
numer) | free pulp. |
Dilution factor (D.F.) | DF = W -E W= Water added per ton of mass E=Water going in pulp per ton of pulp |
Bath Ratio | Wood to liquor ratio |
Consistency | B.D. pulp/ total pulp weight (100gms ) i.e. wt of BD pulp in 100 gm of pulp+ water mixture |
Copper No: | No of milligrams of metallic copper which is reduced from cupric hydroxide to cuprous oxide in alkaline medium by 100 gm of pulp |
Kappa No | 837+.0323*40 ml KMnO4 No. |
Chipping quality plays important role in the overall quality of pulp. Efficiency of debarking process, chip size- length, thickness, uniformity of size, removal of dust and fines are important factors affecting pulping efficiency and quality of pulp. In case of bagasse depithing is very important in overall quality of pulp and paper. In case of agricultural residue size of the straw sand removal of dust also is important. In chipping of bamboo and wood drum chipper and disc chipper are used
KRAFT PULPING PROCESS
Kraft pulping involves Pulping, Washing, Screening, Bleaching. Pulping involves separation of fibre for chemical or mechanical pulping, removal of knots, washing of pulp for recovery of chemical, rejects uncooked material, sand and other foreign material. Bleaching of pulp involves bleaching of washed and screened pulp with bleaching chemicals – chlorine, caustic, hypochlorite, chlorine dioxide, ozone, hydrogen peroxide, sodium hydrosulfite. Conventional used bleaching sequences were (CEHH, CEH, CEHDED, CEDED). Many of the mills in India have also gone for oxygen delignification and newer bleaching sequences.
Cooking of raw material is done batch digester, continuous digester. Spherical batch digester is commonly used for cooking agricultural residues. Cooking liqour used in kraft pulping process is sodium sulphide, sodium carbonate. Cooking cycle may be around 3-5 hr depending of raw material and extend of cooking in batch digester. Typical continuous digester consists of Upper heating zone, upper cooking zone, lower cooking zone, and washing zone. Sequence of operation in coking in digester are chip filling, presetting, liquor charging, heating up and pressure up period, cooking and blowing
Bulk density: 130-150 kg/m3.
Bath ratio: 1:3, Sulphidity 15%
Cooking temp: 170-175 oc.
Pressure:7-7.5 kg/cm2
Temp to rise: 135 oC 2 hr.
Time at: 135-140 oC 2hr.
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1. What is pulping and bleaching in chemical engineering? |
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