Stone-ground wood pulp-reinforced polypropylene composites: water uptake and thermal properties

Two of the drawbacks of using natural-based composites in industrial applications are thermal instability and water uptake capacity. In this work, mechanical wood pulp was used to reinforce polypropylene at a level of 20 to 50 wt. %. Composites were mixed by means of a Brabender internal mixer for both non-coupled and coupled formulations. Differential scanning calorimetry (DSC) and thermogravimetric analysis (TGA) were used to determine the thermal properties of the composites. The water uptake behavior was evaluated by immersion of the composites in water until an equilibrium state was reached. Results of water absorption tests revealed that the amount of water absorption was clearly dependent upon the fiber content. The coupled composites showed lower water absorption compared to the uncoupled composites. The incorporation of mechanical wood pulp into the polypropylene matrix produced a clear nucleating effect by increasing the crystallinity degree of the polymer and also increasing the temperature of polymer degradation. The maximum degradation temperature for stone ground wood pulp–reinforced composites was in the range of 330 to 345 ºC

Study and modeling of the desintegration kinetics of coated paper

The disintegration of recovered paper is the first operation in the preparation of recycled pulp. It is known that the defibering process follows a first order kinetics from which it is possible to obtain the disintegration kinetic constant (KD) by means of different ways. The disintegration constant can be obtained from the Somerville index results (%lsv and from the dissipated energy per volume unit (Ss). The %slv is related to the quantity of non-defibrated paper, as a measure of the non-disintegrated fiber residual (percentage of flakes), which is expressed in disintegration time units. In this work, disintegration kinetics from recycled coated paper has been evaluated, working at 20 revise rotor speed and for different fiber consistency (6, 8, 10, 12 and 14%). The results showed that the values of experimental disintegration kinetic constant, Ko, through the analysis of Somerville index, as function of time. Increased, the disintegration time was drastically reduced. The calculation of the disintegration kinetic constant (modelled Ko), extracted from the Rayleigh’s dissipation function, showed a good correlation with the experimental values using the evolution of the Somerville index or with the dissipated energy

Study and modeling of the desintegration kinetics of coated paper

The disintegration of recovered paper is the first operation in the preparation of recycled pulp. It is known that the defibering process follows a first order kinetics from which it is possible to obtain the disintegration kinetic constant (KD) by means of different ways. The disintegration constant can be obtained from the Somerville index results (%lsv and from the dissipated energy per volume unit (Ss). The %slv is related to the quantity of non-defibrated paper, as a measure of the non-disintegrated fiber residual (percentage of flakes), which is expressed in disintegration time units. In this work, disintegration kinetics from recycled coated paper has been evaluated, working at 20 revise rotor speed and for different fiber consistency (6, 8, 10, 12 and 14%). The results showed that the values of experimental disintegration kinetic constant, Ko, through the analysis of Somerville index, as function of time. Increased, the disintegration time was drastically reduced. The calculation of the disintegration kinetic constant (modelled Ko), extracted from the Rayleigh’s dissipation function, showed a good correlation with the experimental values using the evolution of the Somerville index or with the dissipated energy

Study and modeling of the desintegration kinetics of coated paper

The disintegration of recovered paper is the first operation in the preparation of recycled pulp. It is known that the defibering process follows a first order kinetics from which it is possible to obtain the disintegration kinetic constant (KD) by means of different ways. The disintegration constant can be obtained from the Somerville index results (%lsv and from the dissipated energy per volume unit (Ss). The %slv is related to the quantity of non-defibrated paper, as a measure of the non-disintegrated fiber residual (percentage of flakes), which is expressed in disintegration time units. In this work, disintegration kinetics from recycled coated paper has been evaluated, working at 20 revise rotor speed and for different fiber consistency (6, 8, 10, 12 and 14%). The results showed that the values of experimental disintegration kinetic constant, Ko, through the analysis of Somerville index, as function of time. Increased, the disintegration time was drastically reduced. The calculation of the disintegration kinetic constant (modelled Ko), extracted from the Rayleigh’s dissipation function, showed a good correlation with the experimental values using the evolution of the Somerville index or with the dissipated energy

Study and modeling of the desintegration kinetics of coated paper

The disintegration of recovered paper is the first operation in the preparation of recycled pulp. It is known that the defibering process follows a first order kinetics from which it is possible to obtain the disintegration kinetic constant (KD) by means of different ways. The disintegration constant can be obtained from the Somerville index results (%lsv and from the dissipated energy per volume unit (Ss). The %slv is related to the quantity of non-defibrated paper, as a measure of the non-disintegrated fiber residual (percentage of flakes), which is expressed in disintegration time units. In this work, disintegration kinetics from recycled coated paper has been evaluated, working at 20 revise rotor speed and for different fiber consistency (6, 8, 10, 12 and 14%). The results showed that the values of experimental disintegration kinetic constant, Ko, through the analysis of Somerville index, as function of time. Increased, the disintegration time was drastically reduced. The calculation of the disintegration kinetic constant (modelled Ko), extracted from the Rayleigh’s dissipation function, showed a good correlation with the experimental values using the evolution of the Somerville index or with the dissipated energy

Disseny i muntatge d'un sistema de depuració ciclònica per reciclatge de paper

El projecte s’emmarca dins de l’àmbit de la indústria paperera, i dins el procés defabricació del paper es centra concretament amb l’etapa de la depuració ciclònica, una etapa en la qual es pretenen eliminar aquelles partícules sòlides que acompanyen la pasta de paper i que no són desitjables ja que afecten les característiques del paper i el funcionament de la resta d’equips del procés de fabricació. Es presenta una demanda de projecte per part del grup LEPAMAP (Laboratori d’Enginyeria Paperera i Materials Polímers) sobre el disseny d’una instal•lació de depuració ciclònica, mitjançant un hidrocicló, per realitzar activitats de recerca. Un hidrocicló és un equip que separa gràcies a la força centrífuga del flux d’entrada i pel seu disseny amb forma de con invertit. Així doncs, els objectius bàsics d’aquest projecte són dissenyar una instal•lació de depuració adequada per depurar una pasta de paper de possibles contaminants sòlids, la qual cosa implica el disseny d’una bomba centrífuga per impulsar el flux cap a l’interior de l’hidrocicló, dipòsits per emmagatzemar i preparar la suspensió, un agitador per mantenir en tot moment la homogeneïtat de la suspensió i uns dispositius de mesura i control per mesurar i controlar variables com el cabal, la pressió o el volum.El segon objectiu tracta de posar en marxa la instal•lació i comprovar si aquest equip,l’hidrocicló, separa correctament les partícules sòlides del flux de pasta.Paral•lelament s’ha estudiat quins són els equips de depuració més importants a laindústria paperera així com les etapes més importants que formen part del procés de fabricació del paper

Estudi de reactius químics alternatius per al blanqueig de pastes termomecàniques : efecte en les propietats òptiques de les pastes i en la qualitat dels efluents del procés

Aquest estudi s’emmarca en un projecte titulat “Noves possibilitats en el blanqueig en lespastes destintades: Alternatives al blanqueig amb sosa càustica i peròxid d’hidrogen” i estàsubvencionat per diverses empreses europees del sector. La seva realització s’ha dut a termeen el Centre Technique du Papier, a Grenoble, França. L’estudi contempla la realitzaciód’una part del projecte, i té per objecte analitzar els Na2SiO3 modificats, el hidròxid demagnesi (Mg(OH)2) i el hidròxid de calci (Ca(OH)2) per veure si poden actuar com asubstituts del NaOH. Cal intentar aconseguir valors de blancor similars als assolits amb elblanqueig estàndard i millorar substancialment la qualitat de les aigües. Segons el centre derecerca es pot considerar una millora projectable a nivell industrial una reducció de la DQO ide la demanda catiònica a partir d’un 10% a nivell experimental.La pasta que es blanqueja és TMP verge. Els resultats obtinguts a nivell de blancor tambépoden ser considerats aplicables en paper recuperat, prèviament destintat, provenintd’aquest tipus de pasta

Empirical models for predicting the production of wild mushrooms in Scots pine (Pinus sylvestris L.) forests in the Central Pyrenees

Mushroom picking has become a widespread autumn recreational activity in the Central Pyrenees and other regions of Spain. Predictive models that relate mushroom production or fungal species richness with forest stand and site characteristics are not available. This study used mushroom production data from 24 Scots pine plots over 3 years to develop a predictive model that could facilitate forest management decisions when comparing silvicultural options in terms of mushroom production. Mixed modelling was used to model the dependence of mushroom production on stand and site factors. The results showed that productions were greatest when stand basal area was approximately 20 m2 ha-1. Increasing elevation and northern aspect increased total mushroom production as well as the production of edible and marketed mushrooms. Increasing slope decreased productions. Marketed Lactarius spp., the most important group collected in the region, showed similar relationships. The annual variation in mushroom production correlated with autumn rainfall. Mushroom species richness was highest when the total production was highest.

Estudi per a la determinació de la composició òptima d'una barreja de pastes per a la fabricació de paper tripa industrial

El creixent ritme d’exportacions del Brasil, fa que la demanda de papers d’embalatges’incrementi constantment. El material més utilitzat per al transport són les caixes de cartróondulat (OCC). Aquestes caixes, quan se’ls acaba la vida útil, són recuperades per afabricar nou cartró ondulat. El paper de diari, que un cop llegit es converteix en un residu, nos’acostuma a utilitzar per a la fabricació de nous productes paperers, tot i estar fabricat ambfibres de qualitat elevada.Amb la utilització d’aquests materials com a alternativa es disminueix la demanda defibres verges com és el pi, que al Brasil, es troba en una situació crítica a causa de la malagestió de les plantacions.Cal dir que la part pràctica de l’estudi, que consisteix bàsicament en treball de laboratori,ha estat realitzada al Brasil, d’on provenen també les matèries primeres utilitzades. Peraquest motiu, el context de l’estudi està centrat en el mercat, en les necessitats i en larealitat d’aquest país.Aquest projecte té com a objectiu determinar la composició òptima d’una barreja depastes de pi, sisal, retalls i paper de diari, per a la fabricació de paper tripa industrial. Aquestpaper és el que es col•loca, ondulat, enmig de les capes externes del cartró multicapa

Environmental Tax on Products and Services Based on Their Carbon Footprint: A Case Study of the Pulp and Paper Sector

The main aim of this work is to define an environmental tax on products and services based on their carbon footprint. We examine the relevance of conventional life cycle analysis (LCA) and environmentally extended input-output analysis (EIO) as methodological tools to identify emission intensities of products and services on which the tax is based. The short-term price effects of the tax and the policy implications of considering non-GHG are also analyzed. The results from the specific case study on pulp production show that the environmental tax rate based on the LCA approach (1,8%) is higher than both EIO approaches (0,8% for product and 1,4% for industry approach), but they are comparable. Even though LCA is more product specific and provides detailed analysis, EIO would be the more relevant approach to apply economy wide environmental tax. When the environmental tax considers non-GHG emissions instead of only CO2, sectors such as agriculture, mining of coal and extraction of peat, and food exhibit higher environmental tax and price effects. Therefore, it is worthwhile for policy makers to pay attention on the implication of considering only CO2 tax or GHG emissions tax in order for such a policy measure to be effective and meaningful. Keywords: Environmental tax; Life cycle analysis; Environmental input-output analysis.

On the number of limit cycles bifurcating from a non-global degenerated center

Vegeu el resum a l'inici del document del fitxer adjunt

Creating and using a non-dedicated HPC cluster with ParallelKnoppix

This note describes ParallelKnoppix, a bootable CD that allows econometricians with average knowledge of computers to create and begin using a high performance computing cluster for parallel computing in very little time. The computers used may be heterogeneous machines, and clusters of up to 200 nodes are supported. When the cluster is shut down, all machines are in their original state, so their temporary use in the cluster does not interfere with their normal uses. An example shows how a Monte Carlo study of a bootstrap test procedure may be done in parallel. Using a cluster of 20 nodes, the example runs approximately 20 times faster than it does on a single computer.