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

Investigations on ecofriendly de-inking agents for paper recycling

School of Environmental Studies, Cochin University of Science and Technology

The Chemical Mechanism of a Brown-Rot Decay Mimtic System and its Application in Paper Recycling Processes

This work is aimed at improving our current knowledge of the non-enzymatic inecl~anisins involved in brown-rot decay, as well as the exploration of potential applications of a brown-rot mimetic model system in paper recycling processes. The study was divided into two parts. The first part focussed on the chemical mechanisms involved in chelation and reduction of iron by a low molecular weight chelator (isolated from the brown-rot fungus Gloeophyllz~m tmbeum) and its model compound 2,3- dihydroxybenzoic acid (2,3-DHBA). Chelation as well as free radical generation mediated by this system were studied by ESR measurement. The results indicate that the effects of the chelator/iron ratio, the pH, and other reaction parameters on hydroxyl radical generation by a Fenton type system could be determined using ESR spin-trapping techniques. The results also support the hypothesis that superoxide radicals are involved in the chelator-mediated Fenton process. In the second part of the study, the effect of a chelator-mediated Fenton system for the improvement of deinking efficiency and the n~odification of fiber and paper properties was studied. For the deinking study, copy paper was laser printed with an identical standard pattern. Then repulping and flotation operations were performed to remove ink particles. Under properly controlled deinking conditions, the chelator mediated treatment (CMT) resulted in a reduction in dirt count over that of conventional deinking procedures with no significant loss of pulp strength. To study the effect of the chelator system treatment on the quality of pulp with different fines content, a fully bleached hardwood kraft pulp was beaten to different freeness levels and treated with the chelator-mediated free radical system. The result shows that virgin fiber and heavily beaten fiber respond differently to the free radical treatment. Unbeaten fibers become more flexible and easier to collapse after free radical treatment, while beaten fibers show a reduction in fines and small materials after mild free radical treatment.

Office recycling program guide.

Shipping list no.: 93-0060-P.

Local solid waste and recycling officials directory /

Description based on: [1994]; title from cover.

Wastepaper collection and recycled paper procurement update of March 1990 /

At head of title: Report to the Eighty-Sixth General Assembly on the Wastepaper collection and recycled paper procurement update of March 1990.

Separating paper at the waste source for recycling /

"This report (SW-128) was prepared for the Office of Solid Waste Management Programs by Stephen Lingle"--Page 2 of cover.

The Costs of Municipal Curbside Recycling and Waste Collection

This paper estimates cost functions for both municipal solid waste collection and disposal services and curbside recycling programs. Cost data are obtained from a national survey of randomly selected municipalities. Results suggest, perhaps unsurprisingly, that both marginal and average costs of recycling systems exceed those of waste collection and disposal systems. Economies of scale are estimated for all observed quantities of waste collection and disposal. Economies of scale for recycling disappear at high levels of recycling - marginal and average cost curves for recycling take on the usual U-shape. Waste and recycling costs are also estimated as functions of factor costs and program attributes.

Level monitoring system for waste oil containers: an EPS@ISEP project

Waste oil recycling companies play a very important role in our society. Competition among companies is tough and process optimization is essential for survival. By equipping oil containers with a level monitoring system that periodically reports the level and alerts when it reaches the preset threshold, the oil recycling companies are able to streamline the oil collection process and, thus, reduce the operation costs while maintaining the quality of service. This paper describes the development of this level monitoring system by a team of four students from different engineering backgrounds and nationalities. The team conducted a study of the state of the art, draw marketing and sustainable development plans and, finally, designed and implemented a prototype that continuously measures the container content level and sends an alert message as soon as it reaches the preset capacity.

Carbon footprint of recycled paper

Industrial production of pulp and paper is an intensive consumer of energy, natural resources, and chemicals that result in a big carbon footprint of the final product. At present companies and industries aspire to calculate their gas emissions into the atmosphere in order to afterwards reduce atmospheric contamination. One of the approaches allowing to increase carbon burden from the pulp and paper manufacture is paper recycling. The general purpose of the current paper is to establish methods of quantifying and minimizing the carbon footprint of paper. The first target of this research is to derive a mathematical relationship between virgin fibre requirements with respect to the amount of recycled paper used in the pulp. One more purpose is to establish a model to be used to clarify the contribution of recycling and transportation to decreasing carbon dioxide emissions. For this study sensitivity analysis is used to investigate the robustness of obtained results. The results of the present study show that an increasing of recycling rate does not always lead to minimizing the carbon footprint. Additionally, we derived that transportation of waste paper throughout distances longer than 5800 km has no sense because the use of that paper will only increase carbon dioxide emissions and it is better to reject recycling at all. Finally, we designed the model for organization of a new supply chain of paper product to a customer. The models were implemented as reusable MATLAB frameworks.

Aspectes físics i químics del destintatge de paper revista mitjançant tensioactius catiònics

En una tesi anterior (Puig, 2004) es varen estudiar els aspectes mecànics vinculats al desfibratge i als consums energètics associats al procés de desintegració per acabar quantificant les forces implicades en el procés d'individualització dels components de diferents paperots. Aquest estudi, ha permès conèixer les condicions de desintegració que condueixen a un mínim consum energètic, aspecte complementari al reciclatge i destintatge del paperot però molt important per aconseguir un procés realment sostenible. Degut als requeriments del mercat, hi ha un altre aspecte o vessant realment important com és l'eliminació de tinta. Aquest procés, malgrat la complexitat industrial, es pot reduir o simplificar en dues etapes: la desintegració i la flotació. Ambdues, per raons d'eficàcia i condicionades pels agents químics que s'utilitzen, es realitzen en medi fortament alcalí (entorn d'un pH a 12). Aquest fet, genera una forta contaminació (DQO elevada) i per tant, és un procés poc respectuós amb el medi ambient. Els factors que condicionen treballar en medi alcalí són principalment, el despreniment de la tinta del suport, clarament accelerat en medi bàsic i fonamental per un bon destintatge i la utilització de tensioactius aniònics. Aquests tensioactius són sensibles al pH i la seva eficàcia disminueix en medi neutre o quasi neutre. Atès el que s'ha exposat, s'ha plantejat aquesta tesi que porta per títol "Aspectes Físics i Químics del Destintatge de Paper Revista mitjançant Tensioactius Catiònics", com un estudi del procés de destintatge de paper revista recuperat parant especial atenció a les variables físico-químiques i mecàniques del procés i a la seva influència en el despreniment i fragmentació de la tinta, així com en el procés d'eliminació de la tinta per flotació per tal d'avaluar la viabilitat d'un procés de destintatge en medi neutre enfront del destintatge alcalí convencional. S'ha utilitzat, com a paperot a destintar, el paper revista ja que aquest tipus de paper representa un percentatge elevat del paper recuperat a la Unió Europea. A més, aquest tipus de paper és utilitzat habitualment en les plantes de destintatge industrials per millorar les propietats de les suspensions destintades de paper de diari. La utilització de tensioactius catiònics és deguda a que la seva activitat no es veu afectada pel pH de la suspensió. Així, durant la comparació dels processos de destintatge en medi neutre i en medi alcalí, les eficàcies dels processos no es veuran influenciades pel grau d'ionització del tensioactiu. Donada l'absència d'estudis sobre la influència de les variables del procés en les mesures de concentració efectiva de tinta residual (ERIC) i ja que s'ha emprat aquest paràmetre per avaluar el despreniment i fragmentació de la tinta durant l'etapa de desintegració. En primer lloc, s'ha plantejat un estudi fonamental de la influència que poden tenir les variables del procés (granulometria, concentració de tinta i tipus de suport) en aquest paràmetre. Pel que fa a l'etapa de flotació, s'estudiarà l'efectivitat d'aquesta etapa, posant especial atenció a la capacitat del tensioactiu per eliminar tota la tinta despresa en l'etapa de desintegració. A més, donada la poca informació bibliogràfica referida als mecanismes de flotació amb tensioactius catiònics i la influència que té l'adsorció d'aquests agents per part de la suspensió paperera en l'etapa de flotació, s'ha dut a terme un estudi de l'adsorció dels tensioactius catiònics per part dels components d'una suspensió paperera. Per tant, la tesi realitzada té com a objectius:  Estudi fonamental de les mesures de ERIC (concentració efectiva de tinta residual) amb suports específics.  Estudi de la desintegració en medi neutre i comparació amb la desintegració clàssica.  Modelització del desfibratge de paperot a l'etapa de desintegració.  Estudi de l'eliminació de tinta per flotació en medi neutre i comparació amb la flotació clàssica.  Estudi del mecanisme d'adsorció de tensioactius en suspensions de cel·lulosa sintètica i de paperot.