Thematische Bibliographien / Bleaching technology

Inhaltsverzeichnis

  1. Zeitschriftenartikel
  2. Dissertationen
  3. Bücher
  4. Buchteile
  5. Konferenzberichte

Auswahl der wissenschaftlichen Literatur zum Thema „Bleaching technology“

Autor: Grafiati
Veröffentlicht am 28. Juni 2021
Zuletzt aktualisiert am 17. Februar 2022

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Zeitschriftenartikel zum Thema "Bleaching technology"

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Rounsaville, Jeff. „Ozone Bleaching. Ozone Technology for Pulp Bleaching Applications.“ JAPAN TAPPI JOURNAL 51, Nr. 5 (1997): 738–43. http://dx.doi.org/10.2524/jtappij.51.738.

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Shen, De Jun. „Oak Veneer Bleaching Technology“. Advanced Materials Research 430-432 (Januar 2012): 1219–22. http://dx.doi.org/10.4028/www.scientific.net/amr.430-432.1219.

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oak veneer furniture with bleach treatment process, and by orthogonal test method of oak veneer bleaching factors were analyzed to determine the bleaching process parameters, that is a certain quality and a certain fraction of the mass fraction of sodium hypochlorite oxalic acid composition of oxidized bleach treatment is better.
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Kawakami, Chiaki, Kenji Matsumoto, Olavi Pikka und Aki Vilpponen. „Ozone Bleaching. Recent Bleaching Technology with Ozone and Ahlstage.“ JAPAN TAPPI JOURNAL 51, Nr. 5 (1997): 751–61. http://dx.doi.org/10.2524/jtappij.51.751.

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4

Li, Zhijiang, Tianru Yu und Lichao Yu. „Study on the scouring-bleaching technology of Xinjiang scutched flax“. Journal of Engineered Fibers and Fabrics 15 (Januar 2020): 155892502095765. http://dx.doi.org/10.1177/1558925020957650.

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This study explored and improved the optimal scouring-bleaching process of Xinjiang scutched flax, based on its characteristics and the scouring-bleaching process of existing mature flax. The physical properties, such as length, strength, split degree and fineness, and the chemical composition of Xinjiang scutched flax, such as the content of cellulose, lipowax, pectin, hemicellulose, water-soluble matter, lignin, etc., were measured and analyzed. The approximate range of bleaching process parameters was determined referring to the existing general flax scouring-bleaching process. Thirdly, the orthogonal experiment of three factors and three levels interaction is designed, and the optimal scouring-bleaching process scheme is obtained after analysis and verification.
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Kirkpatrick, Neil. „Biological Bleaching of Wood Pulps – A Viable Chlorine-Free Bleaching Technology?“ Water Science and Technology 24, Nr. 3-4 (01.08.1991): 75–79. http://dx.doi.org/10.2166/wst.1991.0464.

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Biobleaching of wood pulp is bleaching caused by the activity of certain microorganisms. The term “biobleaching” is sometimes also used to describe enzymatic bleaching. In both cases, the aim is to effect bleaching without the use of chlorine, thus minimising the discharge of potentially toxic and mutagenic chlorinated organics in bleach plant effluents. In this paper, the current status of biobleaching research is reviewed and factors necessitating further investigation before biobleaching might be viable on a commercial basis are highlighted.
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Ragnar, Martinr, und Kenji Umemura. „COMPACT BLEACHING™“. JAPAN TAPPI JOURNAL 60, Nr. 2 (2006): 191–96. http://dx.doi.org/10.2524/jtappij.60.191.

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Koshitsuka, Tetsuo. „Foundation of Recycled Pulp Bleaching Technology.“ JAPAN TAPPI JOURNAL 56, Nr. 7 (2002): 963–75. http://dx.doi.org/10.2524/jtappij.56.963.

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Dairaku, Toshio, und Yutaka Araki. „Modern Technology of Kraft Pulp Bleaching.“ JAPAN TAPPI JOURNAL 45, Nr. 11 (1991): 1208–18. http://dx.doi.org/10.2524/jtappij.45.1208.

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Khakimova, Firdaves Kharisovna, Konstantin Andreyevich Sinyayev und Ruslan Eduardovich. „DEVELOPMENT OF TECHNOLOGY FOR PRODUCTION OF DISSOLVING WOOD PULP“. chemistry of plant raw material, Nr. 2 (10.06.2020): 333–43. http://dx.doi.org/10.14258/jcprm.2020026677.

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The work is devoted to the study of possibility and expediency of ECF bleaching for semi-chemical pulp with production of dissolving pulp, which is very popular in Russia and in the world. Production of dissolving wood pulp is important to replace cotton pulp obtained from imported raw materials. The conditions of bleaching and alkali treatment of sulfite pulp are investigated. CA dissolving pulp grade P was produced. To this end, new environmentally reliable short bleaching and alkali treatment schemes of sulfite pulp have been developed using only two oxidizing reagents: hydrogen peroxide and sodium chlorite. The bleaching schemes are based on the ECF technology developed earlier by the authors. Bleached dissolving pulp CA grade P was obtained according to all proposed schemes, including the shortened scheme Pa–E–Ch1–HAT–Ch2–A; pulp with increased yield was obtained due to good selectivity of the used chemicals under the developed conditions of delignification and bleaching, which contributes to the economy of wood. The possibility of obtaining pulp for viscose according to the above scheme is also shown. The results of studies have shown the possibility of obtaining wood pulp CA grade P from these raw materials by TCF technology with the use for delignification and bleaching (after alkali treatment) of hydrogen peroxide in an acidic and traditional alkaline medium, respectively.
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Gavora, J., A. Terenová und P. Jankovič. „Mutagenicity of pulp bleaching wastewater depends on bleaching technology (chlorine vs. ozone)“. Mutation Research/Environmental Mutagenesis and Related Subjects 271, Nr. 2 (1992): 183. http://dx.doi.org/10.1016/0165-1161(92)91249-q.

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Dissertationen zum Thema "Bleaching technology"

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Kouřil, Čeněk. „Úprava bělící technologie při výrobě buničiny z jednoletých rostlin“. Master's thesis, Vysoké učení technické v Brně. Fakulta strojního inženýrství, 2021. http://www.nusl.cz/ntk/nusl-442846.

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Diplomová práce se zabývá bělícím procesem při výrobě papíru. Hlavním cílem práce je zhodnotit současný stav bělící technologie ve firmě OP Papírna, s.r.o. a navrhnout úpravu, která povede k větší efektivitě této technologie. K vyřešení zadání byla provedena rešerše technologických principů bělení a dále provedeny laboratorní experimenty s cílem najít vhodné řešení. Přínos experimentů byl podpořen technologickými výpočty. Výsledky experimentů ukázaly, že současný stav bělící technologie lze několika způsoby zefektivnit. Bylo ukázáno, že podané návrhy mají potenciál velkých ekonomických i chemických úspor. Čtenáři práce se dostane základního přehledu technologie výroby buničiny a papíru se zaměřením na bělící proces a získá znalost jeho bilančních výpočtů.
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Rosing, Trina. „Using Structure-from-Motion Technology to Compare Coral Coverage on Restored vs. Unrestored Reefs“. Wittenberg University Honors Theses / OhioLINK, 2021. http://rave.ohiolink.edu/etdc/view?acc_num=wuhonors1623948204369104.

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Djerdjouri, Nour-Eddine. „Hydrogen peroxide delignification in a biomimetic system based on manganese peroxidase“. Diss., Available online, Georgia Institute of Technology, 2005, 2003. http://etd.gatech.edu/theses/available/ipstetd-1017/.

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Rabelo, Marcos Sousa. „Tecnologias avançadas para pré-branqueamento de polpa kraft de eucalipto“. Universidade Federal de Viçosa, 2006. http://locus.ufv.br/handle/123456789/573.

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The EFC bleaching with the current technologies, based on the chlorine dioxide use represents the second greatest cost in the eucalyptus kraft pulp bleaching (US$ 25-30/t), being the wood the first (US$ 40-80/t). On the other hand, the bleaching reagents offer, typically chlorine dioxide, has been a limiting factor for the production increase in many old industrial units since the units capacity generating this reagent can only be increased by its complete substitution. Besides, the bleaching effluent with the chlorine dioxide is of difficult re-circulation in the chemical recovery. Pulp bleaching alternative technologies, which minimize the use of chlorine dioxide are, therefore, very welcome. The focus of the investigations searching for alternative reagents have been based on the pulp pre-bleaching, i.e., in the two stages of the bleaching sequence, aiming at using less chlorine dioxide and lower the number of kappa pulp that follows the bleaching phase. The practical industrial experience in Brazil shows that the kappa number, after the wood cooking and delignification with oxygen, varies from 9 to 11. The subsequent pulp bleaching with this level of kappa number requires from 33 to 44kg of active chlorine per pulp ton, that is, about 4kg of chlorine per kappa number unit. Therefore, the main objective of this study was to investigate alternatives, which allowed, not only the specific chlorine dioxide consume reduction but also, and mainly, the kappa pulp number reduction that follows to the bleaching phase. Such alternatives included: (1) increase in the delignification efficiency with oxygen by the use of additives and optimization of the operational variables; (2) substitution of the acid stage and/or first de-oxidation stage by a peroxide acid catalyzed with molybdenum salts (PMo) or other salts; (3) industrial evaluation of the PMo stage in a PMoZDP sequence; and (4) NaOH substitution by Mg(OH)2 in the P and Ep stages of the AZDP, a/(Ze)DP and D*(Ep)D bleaching sequences. These objectives accomplishments resulted in the four chapters of this work. The MgSO4 use in the oxygen delignification and the application of the most severe alkali conditions (25kg/t) and of the temperature (115oC) allow the kappa pulp number reduction to values of 9,0, thus reducing the bleaching cost by the Oa/(Ze)DP sequence, without pulp quality loss. The substitution of the sequence AZDP acid stage by the peroxide acetic stage (produced from the glucose pentacetate), also reduced the kappa of the bleaching start, with the bleaching time reduction. The peroxide acid catalyzed with molybdenum (PMo) use in substitution of the acid stage (A) reduced substantially the kappa of the bleaching start, having also reduced the bleaching total cost by the AZDP sequence in R$2,13/t of pulp. Such results were confirmed in a trial mill in a 1200t/day plant without pulp quality loss and the bleaching effluent. The best conditions to operate the PMo stage were: temperature 90-95OC; pH 3,5; 2 hours; 0,1kg/t molybdenum and; 5kg/t hydrogen peroxide. The principal effect of the kappa reduction observed in the PMo stage occurred through the hexenuronic acid removal from the pulp. That the substitution of 25% of the sodium hydroxide and 100% of magnesium sulphate used in the Ep stage by the Mg(OH)2 was demonstrated to be possible without significant damage to the viscosity and brightness of the pulp bleached by the D*(Ep)D sequence
O branqueamento ECF com as tecnologias atuais, à base de dióxido de cloro representa o segundo maior custo de produção de polpa kraft branqueada de eucalipto (US$ 25-30/t), sendo a madeira o primeiro (US$ 40-80/t). Por outro lado, a oferta de reagentes de branqueamento, tipicamente dióxido de cloro, tem sido fator limitante para o aumento da produção de muitas unidades industriais antigas, já que a capacidade de unidades geradoras desse reagente só pode ser aumentada pela sua completa substituição. Além disso, o efluente do branqueamento com dióxido de cloro é de difícil recirculação no sistema de recuperação química da fábrica. Tecnologias alternativas de branqueamento de polpa que minimizem o uso de dióxido de cloro são, portanto, muito bem-vindas. O foco das investigações em busca de reagentes alternativos tem sido na fase de pré-branqueamento da polpa, i.e., nos dois primeiros estágios da seqüência de branqueamento, visando a utilizar menos dióxido de cloro e baixar o número kappa da polpa que segue para a fase de alvejamento. A experiência prática industrial no Brasil demonstra que o número kappa da polpa, após cozimento da madeira e deslignificação com oxigênio, varia de 9 a 11. O branqueamento subseqüente da polpa com esse nível de número kappa requer de 36 a 44kg de cloro ativo por tonelada de polpa, ou seja, cerca de 4kg de cloro ativo por unidade de número kappa. Portanto, o principal objetivo deste estudo foi investigar alternativas que permitissem não só reduzir o consumo específico de dióxido de cloro, mas, principalmente, reduzir o número kappa da polpa que segue para a fase de alvejamento Tais alternativas incluíram: (1) aumento da eficiência de deslignificação com oxigênio pelo uso de aditivos e otimização de variáveis operacionais; (2) substituição do estágio ácido e/ou primeiro estágio de dioxidação por um estágio de peróxido ácido catalisado com sais de molibdênio (PMo) ou outros sais; (3) avaliação industrial do estágio PMo numa seqüência PMoZDP; e (4) substituição do NaOH por Mg(OH)2 nos estágios P e Ep das seqüências de branqueamento AZDP, a/(Ze)DP e D*(Ep)D. O cumprimento desses objetivos resultou nos quatro capítulos deste trabalho. Foi concluído que o uso do MgSO4 na deslignificação com oxigênio associados à aplicação de condições mais severas de álcali (25kg/t) e temperatura (115ºC) permitem reduzir o número kappa da polpa para valores abaixo de 9,0, diminuindo o custo do branqueamento pela seqüência Oa/(Ze)DP, sem prejuízo para a qualidade da polpa. A substituição do estágio ácido da seqüência AZDP, pelo estágio de peroxiacético (produzido a partir do pentacetato de glicose), também reduziu o kappa de entrada do alvejamento. A utilização do estágio de peróxido ácido catalisado com molibdênio (PMo) em substituição ao estágio ácido (A) reduziu o kappa de entrada do alvejamento substancialmente, tendo reduzido também o custo total do branqueamento pela seqüência AZDP em R$2,13/t de polpa. Tais resultados foram confirmados em teste industrial numa planta de 1200t/dia, sem prejuízo para a qualidade da polpa e do efluente de branqueamento. As melhores condições para operar o estágio PMo foram: temperatura 90-95ºC; pH 3,5; 2 horas; 0,1kg/t molibdênio; e 5kg/t peróxido de hidrogênio. O principal efeito da redução do kappa observado no estágio PMo ocorreu pela remoção de ácidos hexenourônicos da polpa. Foi demonstrado ser possível substituir 25% do hidróxido de sódio e 100% do sulfato de magnésio utilizados no estágio Ep pelo Mg(OH)2, sem danos significativos para a viscosidade e alvura da polpa branqueada pela seqüência D*(Ep)D
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Ndangui, Chancelle Betty. „Production et caractérisation de farine de patate douce (Ipomoeabatatas.Lam) : optimisation de la technologie de panification“. Thesis, Université de Lorraine, 2015. http://www.theses.fr/2015LORR0059/document.

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La patate douce est un tubercule appartenant à l'ordre des polémoniales et à la famille des convolvulacées. Il contient de l’amidon, qui est l’élément principal, des dextrines, du ß-carotène, puis d’autres éléments nutritifs en quantités variables. L’objectif de la thèse a été de valoriser la patate douce sous forme de farines et de mettre en évidence les potentialités technologiques de ces farines. Deux études complémentaires ont été réalisées au cours de ce travail de thèse, la première concerne l’étude de l’impact des prétraitements thermiques et chimiques sur les propriétés physicochimiques, thermiques, rhéologiques et fonctionnelles des farines issues de patates douces ayant : TPD (tranche de patate douce non prétraitée), TPDCaCl2 (tranche de patate douce prétraitée au CaCl2) et enfin TPDB (tranche de patate douce prétraitée par blanchiment). Il en résulte une légère augmentation de la teneur en sucres réducteurs dans les farines TPDCaCl2 par rapport aux farines TPDB et TPD. Cependant, la valeur de L* (luminance) dans la farine TPDB était inférieure à celles des farines TPDCaCl2 et TPD. La teneur en calcium était relativement élevée dans la farine TPDCaCl2 (120,6 mg/100g) par rapport aux farines TPD et TPDB (respectivement, 77,8 et 67,6 mg/100g). Les valeurs d’enthalpie de gélatinisation et de module élastique (G’) étaient supérieures dans la farine TPDCaCl2. La capacité de gonflement était élevée dans les farines blanchies. Il a également été constaté une légère augmentation de la constante d'énergie de liaison d'eau du modèle BET dans les farines traitées au CaCl2 et une augmentation marquée pour les farines blanchies. De cette étude, on déduit que les farines traitées au CaCl2 possèdent les propriétés physicochimiques les plus intéressantes pour une application en panification et dans la formulation alimentaire. Dans une seconde étude, les essais de panification ont été réalisés avec différents taux d’incorporation à la farine de blé (0, 10, 15, 20, 25 et 30 %) des farines de patate douce traitées au CaCl2 afin de déterminer le taux d’incorporation optimal permettant de réaliser un compromis entre l’amélioration des propriétés nutritionnelles et la diminution des propriétés rhéologiques de la pâte à pain, suite à l’incorporation de farine de patate douce. Les paramètres texturaux des pâtes ont été déterminés. Il en résulte une diminution de la cohésion, la valeur de a* (échelle de couleurs rouge-vert) a augmenté avec l’augmentation du taux de substitution, contrairement aux valeurs de la luminance L* qui ont diminué. Finalement, la farine de patate douce pouvait être incorporée dans une formulation de panification jusqu’à 25 % sans dépréciation notable des qualités organosensorielles des pains
Sweet potato is an edible tuber belonging to the order of Solanales and Convolvulaceae family. It contains starch, which is the main component, dextrins, ß-carotene, and other nutrients in varying amounts. The thesis aimed promoting the use of sweet potato as flour by highlighting its nutritional potential. Two complementary studies were carried out in this thesis work, the first concerned the study of the impact of thermal and chemical pretreatments on physicochemical, thermal, rheological, and functional properties of sweet potatoes flours obtained after different pretreatments : TPD (unpretreated sweet potato slices), TPDCaCl2 (CaCl2- pretreated sweet potato slices) and finally TPDB (bleached sweet potato slices). These results show a slight increase in reducing sugar content in TPDCaCl2flour compared to TPDB and TPD flours. However, the value of L* (luminance) in the TPDB flour was below the ones ofTPDCaCl2 and TPD flours. The calcium content was relatively high in TPDCaCl2 flour (120.6 mg / 100 g) compared to TPD and TPDB flours (respectively, 77.8 and 67.6 mg / 100g). The gelatinization enthalpy and elastic modulus (G’) were higher in the TPDCaCl2 flour. The swelling capacity was high in bleached flour. It was also noticed a slight increase in the water binding energy constant of the BET model in CaCl2-pretreated and blanched. In this study, it was deduced that the flours pretreated with CaCl2 have physicochemical properties interesting for bakery and food formulation applications. In the second part of the thesis study, baking tests were carried out with different levels of incorporation to wheat flour (0, 10, 15, 20, 25 and 30 %) of the CaCl2-pretreated sweet potato flour in order to determine the optimal incorporation level allowing the compromise between improved nutritional properties and the decreased rheological properties of the dough, due to the sweet potato flour incorporation. Textural parameters of doughs were determined. This resulted in a decrease in cohesion and an increase in the value of a* (red - green color scale) with increasing the degree of substitution, in contrast to the luminance L * values which felt. Finally, sweet potato flour could be incorporated into a bread formulation up to 25 % without significant impairment of sensory organic qualities of bread
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Bücher zum Thema "Bleaching technology"

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Bleaching technology for chemical and mechanical pulps. San Francisco: Miller Freeman, 1991.

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L, Patrick Ken, Hrsg. Bleaching technology for chemical and mechanical pulps. San Francisco, CA: Miller Freeman, 1991.

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Assessment of Bleaching Technology and Emission Control in the Pulp and Paper Industry. International Institute for Environment and Development, 1996.

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Patrick, Ken L. Advances in Bleaching Technology: Low Aox Technologies for Chemical and Recycled Fibers (Pulp & Paper Technical Insight Series). Backbeat Books, 1997.

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Forbes, R. J. Studies in Ancient Technology: The Fibres and Fabrics of Antiquity - Washing, Bleaching, Fulling and Felting - Dyes and Dyeing - Spinning - Sewing , Basketry ... and Weaving (Studies in Ancient Technology). Brill Academic Publishers, 1997.

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1940-, Turoski Victor, American Chemical Society. Division of Environmental Chemistry und American Chemical Society Meeting, Hrsg. Chlorine and chlorine compounds in the paper industry: Developed from a symposium sponsored by the Division of Environmental Chemistry at the 210th National Meeting of the American Chemical Society, Chicago, Illinois, August 20-24, 1995. Chelsea, Mich: Ann Arbor Press, 1997.

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A Novel Green Treatment for Textiles Sustainability. CRC Press, 2012.

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Buchteile zum Thema "Bleaching technology"

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Renders, A. „Recycled fibre bleaching“. In Technology of Paper Recycling, 157–79. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-1328-1_5.

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Ngu, L. N., und F. A. A. Twaiq. „Investigation into Alternative for Bleaching Earth in Palm Oil Processing“. In Developments in Sustainable Chemical and Bioprocess Technology, 303–10. Boston, MA: Springer US, 2013. http://dx.doi.org/10.1007/978-1-4614-6208-8_36.

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Afonso, M. D., und M. N. Pinho. „Treatment of Bleaching Effluents by Pressure - Driven Membrane Processes — A Review“. In Membrane Technology: Applications to Industrial Wastewater Treatment, 63–79. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0211-7_5.

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„10. Bleaching of Pulp“. In Pulping Chemistry and Technology, 239–76. De Gruyter, 2009. http://dx.doi.org/10.1515/9783110213423.239.

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Levene, Raphael. „Wool Bleaching“. In Handbook of Fiber Science and Technology: Volume I Chemical Processing of Fibers and Fabrics, 305–37. Routledge, 2018. http://dx.doi.org/10.1201/9780203719275-4.

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Hintz, H. L. „Paper: Pulping and Bleaching“. In Encyclopedia of Materials: Science and Technology, 6707–11. Elsevier, 2001. http://dx.doi.org/10.1016/b0-08-043152-6/01187-6.

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„9. Chemistry of Bleaching of Chemical Pulp“. In Pulping Chemistry and Technology, 201–38. De Gruyter, 2009. http://dx.doi.org/10.1515/9783110213423.201.

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Atalla, R. H., R. S. Reiner, C. J. Houtman und E. L. Springer. „PULPING | New Technology in Pulping and Bleaching“. In Encyclopedia of Forest Sciences, 918–24. Elsevier, 2004. http://dx.doi.org/10.1016/b0-12-145160-7/00141-1.

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„11. Production of Bleaching Chemicals at the Mill“. In Pulping Chemistry and Technology, 277–96. De Gruyter, 2009. http://dx.doi.org/10.1515/9783110213423.277.

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Lewin, Menachem. „Bleaching of Cellulosic and Synthetic Fabrics“. In Handbook of Fiber Science and Technology: Volume I Chemical Processing of Fibers and Fabrics, 91–256. Routledge, 2018. http://dx.doi.org/10.1201/9780203719275-2.

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Konferenzberichte zum Thema "Bleaching technology"

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Liu, Shuchang, Oleg Mitrofanov und Ajay Nahata. „Transmission bleaching and coupling crossover in a split tapered aperture“. In CLEO: Applications and Technology. Washington, D.C.: OSA, 2014. http://dx.doi.org/10.1364/cleo_at.2014.jth2a.65.

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Cui Shuling. „Qualitative analysis and substitution of bleaching catalyst promor“. In 2014 IEEE Workshop on Advanced Research and Technology in Industry Applications (WARTIA). IEEE, 2014. http://dx.doi.org/10.1109/wartia.2014.6976202.

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Sharma, G., I. Al-Naib, H. Hafez, R. Morandotti und T. Ozaki. „Absorption Bleaching in Silicon via High-Power Terahertz Pulses: Carrier Dependence“. In CLEO: Applications and Technology. Washington, D.C.: OSA, 2012. http://dx.doi.org/10.1364/cleo_at.2012.jw2a.46.

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Ding, Mingjie, Shuen Wei, Yanhua Luo und Gang-Ding Peng. „Reversible Photo-Bleaching Effect in Bi/Er Co-Doped Optical Fiber“. In Australian Conference on Optical Fibre Technology. Washington, D.C.: OSA, 2016. http://dx.doi.org/10.1364/acoft.2016.ath2c.3.

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Roozkhosh, Shahin, und Renato Mancuso. „The Potential of Programmable Logic in the Middle: Cache Bleaching“. In 2020 IEEE Real-Time and Embedded Technology and Applications Symposium (RTAS). IEEE, 2020. http://dx.doi.org/10.1109/rtas48715.2020.00006.

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Huang, Gang, Junhua Wang, Fengchun Dong und Yongtang Jia. „Application of activators for hydrogen peroxide bleaching at low temperature“. In 2nd International Conference on Electronic and Mechanical Engineering and Information Technology. Paris, France: Atlantis Press, 2012. http://dx.doi.org/10.2991/emeit.2012.344.

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Koerner, R., M. Oehme, M. Gollhofer, K. Kostecki, M. Schmid, S. Bechler, D. Widmann, E. Kasper und J. Schulze. „Optical bleaching in electrical pumped n-doped Ge on Si optical devices“. In 2014 7th International Silicon-Germanium Technology and Device Meeting (ISTDM). IEEE, 2014. http://dx.doi.org/10.1109/istdm.2014.6874655.

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Liu, De'an, Liren Liu, Liyong Ren, Changhe Zhou und Guangao Li. „Bleaching effect in LiNbO 3 :Fe:Cu crystals and its application for nonvolatile holographic storage“. In International Symposium on Optical Science and Technology, herausgegeben von Francis T. S. Yu und Ruyan Guo. SPIE, 2002. http://dx.doi.org/10.1117/12.452617.

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Sirisinha, Pawin, Jessada Pakotiprapha, Karyn Viseshakul, Panigarn Katekaew, Teerakiat Kerdcharoen und Tanthip Eamsa-ard. „Detection of Na2S2O4 bleaching agent contaminated in bean sprout using an electronic nose“. In 2020 12th International Conference on Knowledge and Smart Technology (KST). IEEE, 2020. http://dx.doi.org/10.1109/kst48564.2020.9059375.

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Mierczyk, Zygmunt, Zygmunt Frukacz und Jaroslaw Kisielewski. „Influence of charge state of chromium ions on the bleaching dynamics of YAG:Cr4+ nonlinear absorbers“. In Laser Technology V, herausgegeben von Wieslaw L. Wolinski und Michal Malinowski. SPIE, 1997. http://dx.doi.org/10.1117/12.280489.

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