Volume, dry weight, and kraft pulping of fertilized balsam fir from Nova Scotia

1980 ◽  
Vol 10 (3) ◽  
pp. 362-366
Author(s):  
K. Hunt ◽  
V. R. Timmer ◽  
W. G. Warren
Keyword(s):  
Nova Scotia ◽  
Dry Weight ◽  
Kraft Pulping ◽  
Balsam Fir ◽  
Pulp Yield ◽  
Stem Wood ◽  
Breast Height ◽  
Weight Density ◽  
Growth Decline ◽  
Precise Testing

Volume, dry weight, density, and kraft pulping data were obtained from control and fertilized, mature balsam fir (Abiesbalsamea (L.) Mill.) from Nova Scotia. Fertilization treatments consisted of 450 kg N/ha; 450 kg N and 112 kg P/ha; and 450 kg N, 112 kg P, and 112 kg K/ha, plus the untreated control. Samples were taken at three height positions in trees: stump, breast height, and mid-stem. Wood laid down for 5 years after treatment was separated from wood laid down for 5 years before treatment, and its density determined before being pulped by the kraft process.Fertilization significantly increased volume and dry weight increment and reversed patterns of growth decline during the response period. Any effect specifically due to phosphorous or potassium fertilization over that of nitrogen could not be detected with certainty. Wood density was reduced by N and NP applications; however, pulp yield was unaffected by the fertilization treatments. The need for tree equivalence prior to treatment is stressed for more precise testing of differences.

Kraft Pulping and Specific Gravity in the Uppermost Stem of Fertilized Balsam Fir

1975 ◽  
Vol 5 (3) ◽  
pp. 399-402 ◽  
Author(s):  
J. D. Gagnon ◽  
K. Hunt
Keyword(s):  
Specific Gravity ◽  
Boreal Forest ◽  
Kraft Pulping ◽  
Balsam Fir ◽  
Pulp Yield ◽  
Kraft Process ◽  
Forest Region ◽  
The Mean ◽  
Boreal Forest Region

Samples of five pairs of fertilized and non-fertilized 60-year-old natural balsam fir (Abiesbalsamea (L.) Mill.) growing in the Quebec boreal forest region were pulped by the kraft process and the specific gravity was measured. Analyses carried out 7 years after treatment on the last seven terminal internodes revealed the mean pulp yield of trees fertilized exceeded that of non-fertilized by 7%, while the mean specific gravity was about 6% lower.

Factors Influencing the Weight of Black Spruce and Balsam Fir Stems

1972 ◽  
Vol 2 (4) ◽  
pp. 427-433 ◽  
Author(s):  
S. M. Pnevmaticos ◽  
T. A. Jaeger ◽  
E. Perem
Keyword(s):  
Moisture Content ◽  
Black Spruce ◽  
Stem Bark ◽  
Balsam Fir ◽  
Regression Equations ◽  
Green Density ◽  
Stem Wood ◽  
Independent Variables ◽  
Breast Height ◽  
Factors Influencing

The factors influencing green weight of black spruce and balsam fir stems were investigated. It was found that for black spruce stems, moisture content and sapwood content could be predicted by the age and height of the tree. For balsam fir, however, it was difficult to establish meaningful correlations. Stem bark volume was well correlated for both species with diameter at breast height. Regression equations for stem green density with different combinations of independent variables estimated at breast height were developed; it was found that breast height specific gravity and moisture content were the most important variables in predicting stem green density. Stem wood volume was very well correlated with stem weight immediately after felling.

Near-neutral pre-extraction of hemicelluloses and subsequent kraft pulping of southern mixed hardwoods

TAPPI Journal ◽  
2011 ◽  
Vol 10 (1) ◽  
pp. 7-15 ◽  
Author(s):  
SUNG-HOON YOON ◽  
MEHMET SEFIK TUNC ◽  
ADRIAAN VAN HEININGEN
Keyword(s):  
Dry Weight ◽  
Kraft Pulping ◽  
Weight Basis ◽  
Alkaline Solutions ◽  
Pulp Yield ◽  
Kraft Pulps ◽  
Alkaline Ph ◽  
Green Liquor ◽  
Kraft Cooking ◽  
High Alkali

Southern mixed hardwood chips were extracted with alkaline solutions at different chemical charges, times (45-110 min), and temperatures (125°C-160°C). At high alkali charges (10% and 20% sodium hydroxide [NaOH] as sodium oxide [Na2O]), the extract was strongly alkaline (pH about 13) and 17%-40% of the wood was dissolved. Subsequent kraft cooking of the extracted chips yielded 5%-7% less pulp than that of control kraft pulps. However, at reduced alkali charge, just sufficient to approximately neutralize the acids released during pre-extraction, the pulp yield (on original wood) after subsequent kraft pulping was not affected. In this case, about 5%-10% of the wood substance is removed during pre-extraction with 3% NaOH or 3% green liquor (+0.05% anthraquinone) at 140°C and 160°C for 60, 90, and 110 min. The green liquor extract obtained after 110 min at 160°C contained 2.1% (oven-dry weight basis) of sugars, 2.1% acetic acid, and 1.6% lignin accounting for 64% of the wood weight loss. Kraft pulping of the pre-extracted wood chips performed at 12% effective alkali charge showed significantly improved delignification rates and approximately the same or slightly higher yield than the kraft control at 15% effective alkali. The near-neutral green liquor+anthraquinone pre-extraction kraft pulps showed lower refining response but higher tear resistance and similar tensile strength compared to control kraft pulps.

Biomass and nutrient removals by conventional and whole-tree clear-cutting of a red spruce – balsam fir stand in central Nova Scotia

1981 ◽  
Vol 11 (2) ◽  
pp. 250-258 ◽  
Author(s):  
B. Freedman ◽  
R. Morash ◽  
A. J. Hanson
Keyword(s):  
Nova Scotia ◽  
Biomass Yield ◽  
Dry Weight ◽  
Red Spruce ◽  
Balsam Fir ◽  
Soil Horizons ◽  
Clear Cut ◽  
Clear Cutting ◽  
Total Pool ◽  
Whole Tree

Data are presented of biomass and nutrient removals by conventional and whole-tree clear-cutting of 0.5-ha blocks of an all-aged Picearubens – Abiesbalsamea stand in central Nova Scotia. The biomass yield from the conventional clear-cut plot was 105 200 kg dry weight•ha−1, and the removals of N, P, K, Ca, and Mg were 98.2, 16.3, 91.7, 180.9, and 17.0 kg•ha−1 respectively. Biomass removals from the whole-tree clear-cut plot were 152 500 kg dry weight•ha−1, and the removals of N, P, K, Ca, and Mg were 239.1, 35.2, 132.6, 336.5, and 36.9 kg•ha−1, respectively. These removals of N, P, K, Ca, and Mg from the whole-tree harvested plot, expressed as percentages of the quantities of these nutrients in the "total" pool within the exploitable soil horizons, were 5.0, 2.8, 1.0, 5.9, and 2.1%, respectively. However, when these removals were expressed relative to the quantities in the "available" soil pools, they were much larger, i.e., 500, 34, 184, 306, and 95% for N, P, K, Ca, and Mg, respectively.

Polysulfide-borohydride modification of southern pine alkaline pulping integrated with hydrothermal pre-extraction of hemicelluloses

TAPPI Journal ◽  
2011 ◽  
Vol 10 (7) ◽  
pp. 9-16
Author(s):  
SUNG-HOON YOON ◽  
HARRY CULLINAN ◽  
GOPAL A. KRISHNAGOPALAN
Keyword(s):  
Loblolly Pine ◽  
Sodium Borohydride ◽  
Kraft Pulping ◽  
Hot Water ◽  
Pulp Yield ◽  
Paper Strength ◽  
Southern Pine ◽  
Two Stage ◽  
Simultaneous Treatment ◽  
Process Modification

We studied three process modifications to investigate their effects on the property and yield recovery capabilities of kraft pulping integrated with hemicellulose pre-extraction of southern pine. Loblolly pine chips were pre-extracted with hot water until the sugar extraction yield reached the targeted value of 10% and then subjected to conventional and modified kraft pulping. Modification included polysulfide pretreatment; polysulfide-sodium borohydride dual pretreatment, and polysulfide followed by polysulfide-sodium borohydride dual pretreatment two-stage pretreatments prior to kraft pulping. In the first modification, about 5% of the lost pulp yield (total 7%) caused by hemicellulose pre-extraction could be recovered with 15%-20% polysulfide pretreatment. Complete recovery (7%) was achieved with simultaneous pretreatment using 15% polysulfide and 0.5% sodium borohydride with 0.1% anthraquinone in polysulfide-sodium borohydride dual pretreatment. Two-stage pretreatment using recycled 15% polysulfide followed by simultaneous treatment of 6% polysulfide and 0.4%–0.5% sodium borohydride with 0.1% anthraquinone also achieved 100% yield recovery. Continuous recycling of 15% polysulfide employed in the two-stage process modification maintained its yield protection efficiency in a repeated recycling cycle. No significant changes in paper strength were found in handsheets prepared from the three process modifications, except for a minor reduction in tear strength.

Prehydrolysis kraft pulping of jute cutting and caddis mixture for rayon production

TAPPI Journal ◽  
2019 ◽  
Vol 18 (5) ◽  
pp. 287-293 ◽  
Author(s):  
JANNATUN NAYEEM ◽  
M. SARWAR JAHAN ◽  
RAZIA SULTANA POPY ◽  
M. NASHIR UDDIN ◽  
M.A. QUAIYYUM
Keyword(s):  
Kraft Pulping ◽  
Kappa Number ◽  
Pulp Yield ◽  
Solid Residue ◽  
Rayon Production ◽  
Kraft Cooking ◽  
Prehydrolysis Kraft

Jute cutting, jute caddis, and cutting-caddis mixtures were prehydrolyzed by varying time and temperature to get about 90% prehydrolyzed yield. At the conditions of 170°C for 60 min of prehydrolysis, the yield for 100% jute cutting was 76.3%, while the same for jute caddis was only 67.9%. But with prehydrolysis at 150°C for 60 min, the yield was 90% for jute cutting, where 49.94% of original pentosan was dissolved and prehydrolysis of jute caddis at 140°C in 60 min yielded 86.4% solid residue. Jute cutting-caddis mixed prehydrolysis was done at 140°C for 30 min and yielded 92% solid residue for 50:50 cutting-caddis mixtures, where pentosan dissolution was only 29%. Prehydrolyzed jute cutting, jute caddis, and cutting-caddis mixtures were subsequently kraft cooked. Pulp yield was only 40.9% for 100% jute cutting prehydrolyzed at 170°C for 60 min, which was 10.9% lower than the prehydrolysis at 140°C. For jute cutting-caddis mixed prehydrolysis at 140°C for 45 min followed by kraft cooking, pulp yield decreased by 3.3% from the 100% cutting to 50% caddis in the mixture, but 75% caddis in the mixture decreased pulp yield by 6.7%. The kappa number 50:50 cutting-caddis mixture was only 11.3. Pulp bleachability improved with increasing jute cutting proportion in the cutting-caddis mixture pulp.

Coumarin Content and Physicochemical Profile of Mikania laevigata Extracts

2004 ◽  
Vol 59 (3-4) ◽  
pp. 197-200 ◽  
Author(s):  
Maique W. Biavatti ◽  
Cesar A. Koerich ◽  
Carlos H. Henck ◽  
Enderson Zucatelli ◽  
Fernanda H. Martineli ◽  
...  
Keyword(s):  
Efficient Method ◽  
Extraction Method ◽  
Dry Weight ◽  
Southern Brazil ◽  
Weight Density ◽  
Ethanol Content ◽  
Mikania Laevigata ◽  
Method Of Extraction

The ‘guaco’ lianous herb Mikania laevigata, which is widespread in Southern Brazil, is traditionally used to treat bronchitis, asthma and cough. This work investigates the influence of the extraction method, solvent:drug ratio, ethanol proportion, harvest season (summer or winter) and solvent heating on the physicochemical profile of the extracts (dry weight, density, pH) and the coumarin (1,2-benzopyrone) content determined by LC. Among the results obtained, it is observed that higher ethanol content increases the amount of coumarin in the extract. Leaves harvested in summer also produce an extract with a high coumarin yield. The most efficient method of extraction is percolation, independent of the solvent used.

Kraft pulping and bleaching of Eichhornia crassipes (Mart.) Solms (water hyacinth)

BioResources ◽  
2020 ◽  
Vol 15 (4) ◽  
pp. 9243-9264
Author(s):  
Luis Fernando Pintor-Ibarra ◽  
José de Jesús Rivera-Prado ◽  
Sarai Ramos-Vargas ◽  
Teófilo Escoto-García ◽  
Nancy Eloisa Rodríguez-Olalde ◽  
...  
Keyword(s):  
Water Hyacinth ◽  
Eichhornia Crassipes ◽  
Kraft Pulping ◽  
Kappa Number ◽  
Pulp Yield ◽  
Inorganic Elements ◽  
Wood Fibers ◽  
Pulp Bleaching ◽  
Cellulosic Pulp ◽  
Unbleached Pulp

Eichhornia crassipes (water hyacinth) was pulped by means of a kraft pulping process with reagent loads of 10 and 20% on a dry matter basis to determine yield, rejects, kappa number, and ash. Fiber classification, brightness, opacity, and viscosity were measured in the brown pulp. Bleaching was performed by means of an O1O2D1(PO)D2HD3 sequence. Yield, kappa number, pH, ash, brightness, opacity, and viscosity were evaluated in the bleached pulp. Finally, a microanalysis of inorganic elements was carried out in both the bleached and unbleached pulp ash. The highest kraft pulp yield was 26.4%, with a 10% reagent load at 120 °C and 30 minutes cooking. It was determined that E. crassipes cellulosic pulp contains large amounts of fines. Results of the bleaching sequence indicate low brightness (58.0 %) and low viscosity (6.43 cP). The most abundant inorganic elements in the ash of both bleached and unbleached pulp were Ca, Mg, P, and Si. These results suggest that E. crassipes biomass might complement cellulosic fibers in pulping processes of low yield, such as the wood fibers used to produce handmade paper.

Application of Chelating Agents as Cooking Aids in Bamboo Pulping

2013 ◽  
Vol 750-752 ◽  
pp. 1520-1523
Author(s):  
Hong Xia Gao ◽  
Wen Hua He ◽  
Xiu Qiong Guan ◽  
Chun Liu ◽  
Bo Yuan
Keyword(s):  
Phosphonic Acid ◽  
Chelating Agents ◽  
Kraft Pulping ◽  
Kappa Number ◽  
Pulp Yield ◽  
Diethylene Triamine ◽  
Bamboo Pulp ◽  
Kraft Cooking ◽  
Pulp Strength

The effect of chelating agents Diethylene Triamine Penta Methylene Phosphonic Acid in bamboo kraft cooking was studied. The results show that the bamboo pulp yield was 49.52% when DTPMPA dosage is 0.4%, at the same time the Kappa number was lower. With the increasing of DTPMPA dosage in bamboo kraft pulping, the bamboo pulp strength was increased.

scholarly journals Chemical characteristics and Kraft pulping of tension wood from Eucalyptus globulus labill

2012 ◽  
Vol 36 (6) ◽  
pp. 1163-1172 ◽  
Author(s):  
María Graciela Aguayo ◽  
Regis Teixeira Mendonça ◽  
Paulina Martínez ◽  
Jaime Rodríguez ◽  
Miguel Pereira
Keyword(s):  
Eucalyptus Globulus ◽  
Lignin Content ◽  
Strength Properties ◽  
Kraft Pulping ◽  
Pulp Yield ◽  
Chemical Characteristics ◽  
Kraft Pulps ◽  
Opposite Wood ◽  
Alkali Consumption ◽  
Pulp Strength

Tension (TW) and opposite wood (OW) of Eucalyptus globulus trees were analyzed for its chemical characteristics and Kraft pulp production. Lignin content was 16% lower and contained 32% more syringyl units in TW than in OW. The increase in syringyl units favoured the formation of β-O-4 bonds that was also higher in TW than in OW (84% vs. 64%, respectively). The effect of these wood features was evaluated in the production of Kraft pulps from both types of wood. At kappa number 16, Kraft pulps obtained from TW demanded less active alkali in delignification and presented slightly higher or similar pulp yield than pulps made with OW. Fiber length, coarseness and intrinsic viscosity were also higher in tension than in opposite pulps. When pulps where refined to 30°SR, TW pulps needed 18% more revolutions in the PFI mill to achieve the same beating degree than OW pulps. Strength properties (tensile, tear and burst indexes) were slightly higher or similar in tension as compared with opposite wood pulps. After an OD0(EO)D1 bleaching sequence, both pulps achieved up to 89% ISO brightness. Bleached pulps from TW presented higher viscosity and low amount of hexenuronic acids than pulps from OW. Results showed that TW presented high xylans and low lignin content that caused a decrease in alkali consumption, increase pulp strength properties and similar bleaching performance as compared with pulps from OW.

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