Relevant bibliographies by topics / Nimoy

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Academic literature on the topic 'Nimoy'

Author: Grafiati
Published: 4 June 2021
Last updated: 30 January 2023

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Journal articles on the topic "Nimoy"

1

Bush, Elizabeth. "Fascinating: The Life of Leonard Nimoy by Richard Michelson." Bulletin of the Center for Children's Books 70, no. 3 (2016): 140. http://dx.doi.org/10.1353/bcc.2016.0908.

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2

Picard, Anne-Marie. "Travestissement et paternité : la masculinité remade in the USA." Articles divers 1, no. 1-2 (February 23, 2011): 114–31. http://dx.doi.org/10.7202/1000994ar.

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Les films Trois hommes et un couffin de Coline Serreau et Three Men and a Baby de Leonard Nimoy sont analysés ici de façon comparative. L’auteure explique la façon dont la version américaine fait une « re-vision » du regard attendri que Serreau portait sur les nouveaux hommes nés des mouvements et des analyses féministes. La nouvelle masculinté (non phallique) illustrée dans le film français est totalement abolie et remplacée par l’idéologie patriarcale américaine.
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Zhang, Jing Cheng, Hai Bin Yu, Jun Nan, Shan Geng, Xiao Guo Li, Xiao Long Qu, Yu Lin Shi, Yu Ting Zhang, and Hong Guang Liu. "Synthesis and Hydrodesulfurization Performance of NiMo Sulfide Catalysts Supported on γ-Al2O3." Advanced Materials Research 781-784 (September 2013): 304–7. http://dx.doi.org/10.4028/www.scientific.net/amr.781-784.304.

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This work presents the synthesis and hydrodesulfurization performance of NiMo sulfide catalysts supported on γ-Al2O3 during the hydrodesulfurization (HDS) of dibenzothiophene (DBT). The catalysts were synthesized by the co-impregnation method using an atomic ratio of Ni=Ni/(Ni+Mo)=0.5. The materials were characterized by N2 physisorption, XRD and HRTEM. This catalyst exhibited the larger pore size and high specific surface area, as well as better morphological properties. The catalytic activity was evaluated using a high-pressure batch reactor at 280 °C and 3.0 MPa. The catalytic activity during HDS-DBT indicated that the NiMoS/γ-Al2O3 catalyst was better than that NiMoS/γ-Al2O3 catalyst. the NiMoS/γ-Al2O3 catalyst exhibits higher DDS selectivity (3.0) than NiMo/γ-Al2O3 catalyst (2.55).
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Puello-Polo, Esneyder, Yina Pájaro, and Edgar Márquez. "Effect of the Gallium and Vanadium on the Dibenzothiophene Hydrodesulfurization and Naphthalene Hydrogenation Activities Using Sulfided NiMo-V2O5/Al2O3-Ga2O3." Catalysts 10, no. 8 (August 7, 2020): 894. http://dx.doi.org/10.3390/catal10080894.

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The effect of Ga and V as support-modifier and promoter of NiMoV/Al2O3-Ga2O3 catalyst on hydrogenation (HYD) and hydrodesulfurization (HDS) activities was studied. The catalysts were characterized by elemental analysis, textural properties, XRD, XPS, EDS elemental mapping and High-resolution transmission electron microscopy (HRTEM). The chemical analyses by X-ray Fluorescence (XRF) and CHNS-O elemental analysis showed results for all compounds in agreement, within experimental accuracy, according to stoichiometric values proposed to Mo/Ni = 6 and (V+Ni)/(V+Ni+Mo) = 0.35. The sol-gel synthesis method increased the surface area by incorporation of Ga3+ ions into the Al2O3 forming Ga-O-Al bonding; whereas the impregnation synthesis method leads to decrease by blocking of alumina pores, as follows NiMoV/Al-Ga(1%-I) < NiMoV/Al-Ga(1%-SG) < NiMo/Al2O3 < Al2O3-Ga2O3(1%-I) < Al2O3-Ga2O3(1%-SG) < Al2O3, propitiating Dp-BJH between 6.18 and 7.89 nm. XRD confirmed a bulk structure typical of (NH4)4[NiMo6O24H6]•5H2O and XPS the presence at the surface of Mo4+, Mo6+, NixSy, Ni2+, Ga3+ and V5+ species, respectively. The EDS elemental mapping confirmed that Ni, Mo, Al, Ga, V and S are well-distributed on Al2O3-Ga2O3(1%-SG) support. The HRTEM analysis shows that the length and stacking distribution of MoS2 crystallites varied from 5.07 to 5.94 nm and 2.74 to 3.58 with synthesis method (SG to I). The results of the characterization sulfided catalysts showed that the synthesis method via impregnation induced largest presence of gallium on the surface influencing the dispersion V5+ species, this effect improves the dispersion of the MoS2 phase and increasing the number of active sites, which correlates well with the dibenzothiophene HDS and naphthalene HYD activities. The dibenzothiophene HDS activities with overall pseudo-first-order rate constants’ values (kHDS) from 1.65 to 7.07 L/(h·mol·m2) follow the order: NiMoV-S/Al-Ga(1%-I) < NiMo-S/Al2O3 < NiMoV-S/Al-Ga(1%-SG), whereas the rate constants’ values (k) of naphthalene HYD from 0.022 to 2.23 L/(h·mol·m2) as follow: NiMoV-S/Al-Ga(1%-SG) < NiMo-S/Al2O3 < NiMoV-S/Al-Ga(1%-I). We consider that Ga and V act as structural promoters in the NiMo catalysts supported on Al2O3 that allows the largest generation of BRIM sites for HYD and CUS sites for DDS.
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Nuzhdin, Alexey, Galina Bukhtiyarova, Aleksander Porsin, Igor Prosvirin, Irina Deliy, Vladimir Volodin, Evgeny Gerasimov, Evgeniya Vlasova, and Valerii Bukhtiyarov. "Effect of Mono-, Di-, and Triethylene Glycol on the Activity of Phosphate-Doped NiMo/Al2O3 Hydrotreating Catalysts." Catalysts 9, no. 1 (January 17, 2019): 96. http://dx.doi.org/10.3390/catal9010096.

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The effect of glycols on the catalytic properties of phosphate-doped NiMo/Al2O3 catalysts in the hydrotreating of straight-run gas oil (SRGO) was studied. The NiMo(P)/Al2O3 catalysts were prepared using ethylene glycol (EG), diethylene glycol (DEG), and triethylene glycol (TEG) as additives. The organic agent was introduced into the aqueous impregnation solution obtained by the dissolving of MoO3 in H3PO4 solution, followed by Ni(OH)2 addition. The Raman and UV–Vis studies show that the impregnation solution contains diphosphopentamolybdate HxP2Mo5O23(6−x)− and Ni(H2O)62+, and that these ions are not affected by the presence of glycols. When the impregnation solution comes in contact with the γ-Al2O3 surface, HxP2Mo5O23(6−x)− is decomposed completely. The catalysts were characterized by Raman spectroscopy, low-temperature N2 adsorption, X-ray photoelectron spectroscopy, and transmission electron microscopy. It is shown that the sulfide catalysts prepared with glycols display higher activity in the hydrotreating of straight-run gas oil than the NiMoP/Al2O3 catalyst prepared without the additive. The hydrodesulfurization and hydrodenitrogenation activities depend on the glycol type and are decreased in the following order: NiMoP-DEG/Al2O3 > NiMoP-EG/Al2O3 > NiMoP-TEG/Al2O3 > NiMoP/Al2O3. The higher activity of NiMoP-DEG/Al2O3 can be explained with the higher dispersion of molybdenum on the surface of the catalyst in the sulfide state.
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Liu, Ying, Huan Zhang, Cong Ma, and Nan Sun. "Modified Nimo Nanoparticles for Efficient Catalytic Hydrogen Generation from Hydrous Hydrazine." Catalysts 9, no. 7 (July 10, 2019): 596. http://dx.doi.org/10.3390/catal9070596.

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Precious metal-free NiMoM (M = Pr2O3, Cu2O) catalysts have been synthesized through a simple coreduction method, without any surfactant or support material, and characterized using X-ray diffraction (XRD), transmission electron microscopy (TEM), and X-ray photoelectron spectroscopy (XPS). The resultant Pr2O3- or Cu2O-modified NiMo catalysts exhibit different structures, which is due to a difference in the synergistic effects of NiMo and the modifying elements. NiMoPr2O3 has an amorphous structure, with low crystallinity and uniform particle dispersion, while NiMo@Cu2O adopts the core–shell structure, where the core and shell are synergistic with each other to promote electron transfer efficiency. The support material-free nanocatalysts Ni9Mo1(Pr2O3)0.375 and Ni4Mo@Cu2O are both highly efficient compared with bimetallic NiMo catalysts, in terms of hydrogen generation from hydrous hydrazine (N2H4·H2O) at 343 K, with total turnover frequencies (TOFs) of 62 h−1 and 71.4 h−1, respectively. Their corresponding activation energies (Ea) were determined to be 43.24 kJ mol−1 and 46.47 kJ mol−1, respectively. This is the first report on the use of Pr-modified NiMo and core–shell NiMo@Cu2O catalysts, and these results may be used to promote the effective application of noble metal-free nanocatalysts for hydrogen production from hydrous hydrazine.
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James, S. W., K. A. Bullock, S. E. Gygax, B. A. Kraynack, R. A. Matura, J. A. MacLeod, K. K. McNeal, et al. "nimO, an Aspergillus gene related to budding yeast Dbf4, is required for DNA synthesis and mitotic checkpoint control." Journal of Cell Science 112, no. 9 (May 1, 1999): 1313–24. http://dx.doi.org/10.1242/jcs.112.9.1313.

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The nimO predicted protein of Aspergillus nidulans is related structurally and functionally to Dbf4p, the regulatory subunit of Cdc7p kinase in budding yeast. nimOp and Dbf4p are most similar in their C-termini, which contain a PEST motif and a novel, short-looped Cys2-His2 zinc finger-like motif. DNA labelling and reciprocal shift assays using ts-lethal nimO18 mutants showed that nimO is required for initiation of DNA synthesis and for efficient progression through S phase. nimO18 mutants abrogated a cell cycle checkpoint linking S and M phases by segregating their unreplicated chromatin. This checkpoint defect did not interfere with other checkpoints monitoring spindle assembly and DNA damage (dimer lesions), but did prevent activation of a DNA replication checkpoint. The division of unreplicated chromatin was accelerated in cells lacking a component of the anaphase-promoting complex (bimEAPC1), consistent with the involvement of nimO and APC/C in separate checkpoint pathways. A nimO deletion conferred DNA synthesis and checkpoint defects similar to nimO18. Inducible nimO alleles lacking as many as 244 C-terminal amino acids supported hyphal growth, but not asexual development, when overexpressed in a ts-lethal nimO18 strain. However, the truncated alleles could not rescue a nimO deletion, indicating that the C terminus is essential and suggesting some type of interaction among nimO polypeptides.
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Yan, Jiawei, Zhidong Wei, Meiqi Xu, Zhi Jiang, and Wenfeng Shangguan. "Polyoxometalate Template-Based Synthetic Strategy to Prepare Ni, Mo Co-Doped CdS for Efficient Photocatalytic Hydrogen Evolution from Water Splitting." Catalysts 10, no. 12 (December 17, 2020): 1478. http://dx.doi.org/10.3390/catal10121478.

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In this work, a novel polyoxometalate template-based strategy was applied to construct the bi-metal-doped CdS photocatalysts. NiMo6 polyoxometalate template precursor was applied for the preparation of Ni, Mo co-doped CdS photocatalysts (NiMo-CdS). The structures of the materials were explored by XRD, SEM, HRTEM, HAADF, element mapping, XPS, Raman spectrum and UV-vis DRS. Moreover, the results of the UV-vis spectrum showed that NiMo-CdS exhibited an enhanced performance on light absorption. The results of photocatalytic hydrogen evolution from water splitting demonstrated that the NiMo-CdS showed higher efficiency on hydrogen evolution than noble-metal Pt-doped CdS. The reason could be ascribed to the enhanced light absorption ability and charge separation after Ni and Mo were introduced, which could also act as co-catalysts. The apparent quantum yield (AQY) efficiency could reach 42% at 365 nm. This work proposed a novel and inexpensive method to synthesize the bi-metal (Ni, Mo) decorated CdS photocatalysts for efficient hydrogen evolution from water splitting.
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Polo Hernández, Andrés, Esneyder Puello polo, and Carlos Diaz. "Influencia del Ce en la hidrodesulfuración de tiofeno utilizando precursores catalíticos de heteropolioxomolibdatos de níquel tipo Anderson soportados sobre alúmina/Influence of Ce in the thiophene hydrodesulfurization using catalytic precursor of alumina." Prospectiva 15, no. 1 (February 22, 2017): 74–82. http://dx.doi.org/10.15665/rp.v15i1.755.

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El efecto del soporte modificado con cerio en precursores catalíticos de NiMo tipo Anderson sobre la hidrodesulfuración de tiofeno fue investigada. Los sólidos fueron caracterizados por área específica (SBET), difracción de rayos X (DRX) y espectroscopía infrarroja (FTIR). El soporte modificado con cerio se impregnó con una solución acuosa del heteropolioxomolibdato tipo Anderson de Ni. La presencia de (NH4)4[NiMo6O24H6]•5H2O y alúmina en fases gamma y gibbsita se verificó por DRX, mientras que el FTIR permitió asignar las características vibracionales de la estructura tipo Anderson, debido a los estiramientos y flexiones de los grupos funcionales presentes. Los soportes γ-Al2O3, γ-Al2O3-Ce y Ce/γ-Al2O3 mostraron mayor área específica (149-66 m2/g) que los precursores catalíticos NiMo6/γ-Al2O3, NiMo6/γ-Al2O3-Ce y NiMo6-Ce/γ-Al2O3 (76-36 m2/g). Los catalizadores provenientes de alúminas modificadas con cerio presentaron mayor actividad HDS que los obtenidos con alúmina no modificada, lo cual está asociado a la formación de mayor número de sitios activos.
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Puello polo, Esneyder, Melissa Romero Baños, and Jayson Fals Fals. "Precursores catalíticos de polioxometalatos tipo Anderson-Evans de FeMo, CoMo y NiMo soportados sobre zeolita β para la hidrodesulfuración de tiofeno/Catalytic precursors of β zeolite supported Anderson–Evans type FeMo, CoMo and NiMo polyoxometalates..." Prospectiva 16, no. 1 (December 5, 2017): 34–40. http://dx.doi.org/10.15665/rp.v16i1.1298.

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Precursores catalíticos de polioxometalatos de FeMo, CoMo y NiMo tipo Anderson-Evans soportados sobre zeolita β en la hidrodesulfuración de tiofeno fue investigada. Los sólidos fueron caracterizados por análisis elemental (ICP plasma), área específica (SBET), difracción de rayos X (DRX) y espectroscopía infrarroja (FTIR). El soporte se impregnó con una solución acuosa del heteropolioxomolibdatos tipo Anderson-Evans de FeMo, CoMo y NiMo. El análisis elemental de Fe, Co, Ni y Mo dio resultados de acuerdo con la exactitud experimental de las relaciones atómicas nominales para cada precursor. La presencia de zeolita β, (NH4)3[FeMo6O24H6]•7H2O, (NH4)3[CoMo6O24H6]•7H2O y (NH4)4[NiMo6O24H6]•5H2O se verificó por DRX, mientras que el FTIR permitió asignar los estiramientos y flexiones de los grupos funcionales presentes en la estructura del heteropolioxomolibdato Anderson-Evans y la zeolita β. Los precursores catalíticos FeMo6/zeolita β, CoMo6/zeolita β y NiMo6/zeolita β mostraron mayor área específica (204-268 m2/g) que los heteropolioxomolibdatos tipo Anderson-Evans (1-3 m2/g). Los catalizadores provenientes de heteropolioxometalatos tipo Anderson-Evans de FeMo, CoMo y NiMo soportados en zeolita β presentaron mayor actividad HDS que los precursores no soportados (FeMo6/zeolita β y CoMo6/zeolita β), lo cual está asociado a la formación de mayor número de sitios activos.
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Dissertations / Theses on the topic "Nimoy"

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Baudon, Alain. "Hydrocraquage d'hydrocarbures modèles sur catalyseurs industriels NiMoS." Poitiers, 1996. http://www.theses.fr/1996POIT2302.

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L'hydrocraquage des charges petrolieres est un des procedes de conversion de l'industrie du raffinage qui, par sa grande flexibilite, permet d'orienter sa production en fonction de la demande du marche. Il permet d'obtenir aisement le produit recherche (essence, gazole, kerosene), meme a partir de charges refractaires au craquage, comme les charges riches en polyaromatiques. L'objectif de ce travail etait d'etudier la transformation de differents types d'hydrocarbures representatifs des charges a traiter (paraffines, naphtenes, aromatiques) dans des conditions proches de celles utilisees dans les unites industrielles (reacteur dynamique sous pression elevee d'hydrogene, presence de composes soufres et azotes). Le catalyseur utilise pour cette etude est lui aussi de type industriel, a base de sulfures de nickel et de molybdene deposes sur une alumine et associes a une zeolithe y protonique. La principale conclusion de cette etude est donc que la transformation des differents hydrocarbures se produit toujours essentiellement par un mecanisme bifonctionnel, conduisant a des produits d'isomerisation et de craquage. La structure de l'hydrocarbure ne modifie que les vitesses des differentes reactions, y compris celle de la formation de coke, et par consequent la selectivite de l'hydrocraquage. La structure de l'hydrocarbure semble egalement jouer un role important au niveau de la cinetique de la reaction. En effet, les equations cinetiques utilisees pour decrire la transformation des n-alcanes ne semblent pas adaptees a la transformation des naphtenes, et encore moins a celle des naphteno-aromatiques. Enfin, la methode utilisee pour presulfurer le catalyseur influe considerablement sur son activite ulterieure en hydrocraquage. Une sulfuration en absence d'hydrocarbure (par h#2s/h#2) conduit a une meilleure formation de la phase sulfure, et par consequent a une activite hydrogenante plus forte du catalyseur. La sulfuration en presence d'un hydrocarbure (dimethyldisulfure en solution dans le n-heptane ou le n-decane) conduit a un cokage des sites acides du catalyseur
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CABRAL, Rucilana Patrícia Bezerra. "Síntese e avaliação de NiMo/Beta e NiMo/SAPO-5 no hidrocraqueamento do cumeno com piridina." Universidade Federal de Campina Grande, 2008. http://dspace.sti.ufcg.edu.br:8080/jspui/handle/riufcg/1695.

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Submitted by Maria Medeiros (maria.dilva1@ufcg.edu.br) on 2018-09-12T14:38:14Z No. of bitstreams: 1 RUCILANA PATRÍCIA BEZERRA CABRAL - TESE (PPGEP) 2008.pdf: 6571244 bytes, checksum: d2b524bd924cc294214a4507138e3b56 (MD5)
Made available in DSpace on 2018-09-12T14:38:14Z (GMT). No. of bitstreams: 1 RUCILANA PATRÍCIA BEZERRA CABRAL - TESE (PPGEP) 2008.pdf: 6571244 bytes, checksum: d2b524bd924cc294214a4507138e3b56 (MD5) Previous issue date: 2008-07-06
Devido ao aumento na produção de óleo pesado, a indústria do refino voltou-se para os processos de hidrocraqueamento (HCC) que fornecem combustíveis básicos e leves atendendo as exigências da sociedade moderna. O processo HCC é realizado, geralmente, sob temperaturas e pressões elevadas na presença do hidrogênio e de um catalisador de hidrocraqueamento. As cargas de petróleo brasileiras inevitavelmente contêm muitas impurezas, como os compostos orgânicos nitrogenados. Estes compostos de nitrogênio presentes nas cargas de hidrocraqueamento atuam como venenos temporários dos catalisadores, resultando numa diminuição de atividade destes catalisadores. Normalmente, os catalisadores de HCC compreendem de um suporte ácido mais um componente hidrogenante selecionado do Grupo VIB e do grupo VIII da Tabela periódica dos Elementos, na forma de óxido ou sulfeto. Zeólita Beta e SAPO-5 foram propostos para serem usados como suportes ácidos. A respeito do componente hidrogenante, a combinação de metais usados, expressada como óxidos, foi NiO-MoO3. Uma série de catalisadores NiMo suportados em Zeólita Beta e SAPO-5, de diferentes composições, foram preparados por impregnação seqüencial úmida dos materiais utilizando soluções aquosas precursoras de Ni(NO3)2.6H2O e (NH4)6 Mo7O24. 4H2O. Os suportes e catalisadores foram analisados pelas técnicas: Difração de raios-X (DRX), Espectrometria de Emissão Atômica de Plasma Acoplado Induzido (ICPAES), Adsorção Física de N2 pelo método BET, Redução com Temperatura Programada (RTP), Microscopia Eletrônica de Transmissão (MET), Espectroscopia no Infravermelho de piridina adsorvida (IV), Espectroscopia de Refletância Difusa (DRS) e Espectroscopia de Ressonância Magnética Nuclear (RMN). Os catalisadores NiMo sulfetados foram avaliados usando um reator tubular de fluxo contínuo, no hidrocraqueamento do cumeno na presença e ausência de piridina. Foi verificado que os catalisadores suportados em zeólita Beta promoveram maiores conversões que os suportados em SAPO-5, principalmente o que usou zeólita Beta (Si/Al=8,2) com 4%NiO e 15%MoO3. A presença da piridina foi prejudicial à performance de todos os catalisadores, inclusive para os padrões cedidos pelo CENPES.
Due to the increasing of the heavier crude oil feedstocks production, the oil refining industry has turned to hydrocracking (HCK) processes to provide the lighter basic fuels which modern society demands. The HCK process is generally carried out under high temperatures and pressures in the presence of the hydrogen and a HCK catalyst. The feedstocks of the Brazilian crudes inevitably contain many impurities, such as organic nitrogen compounds. These nitrogen compounds present in the feeds of hydrocracking process act as, temporary poisons to the catalysts, thereby decreasing the catalyst activity. Usually, hydrocracking catalysts comprise of an acidic support plus a hydrogenating component selected from the Group VIB metals and Group VIII metals of the Periodic Table of the Elements, in their oxide or sulfide form. Beta zeolite and SAPO-5 are proposed as acidic support materials for hydrocracking. Regarding the hydrogenation component the combination of the metals used in the form of oxides, was NiO-MoO3. A series of NiMo catalysts supported on Beta zeolite and SAPO-5, of different compositions, were prepared by sequential incipient wetness impregnation of the materials with aqueous solutions of Ni(NO3)2 . 6H2O and (NH4)6 Mo7O24.4H2O. The supports and catalysts were analyzed by several techniques such as: X-ray diffraction (XRD), plasma-emission spectrometry (ICP-AES), N2 physical adsorption by BET method, temperature programmed reduction (TPR), transmission electronic microscopy (TEM), infrared spectroscopy of adsorbed pyridine (IR), diffuse reflectance spectroscopy (DRS) and nuclear magnetic resonance (NMR) spectroscopy. The sulfide NiMo catalysts were evaluated using a continuous-flow tubular reactor by the cumene hydrocracking in the presence and absence of pyridine. It was verified that the NiMo catalysts based on Beta zeolite produced the highest cumene conversion than those based on SAPO-5, particularly the one with Beta zeolite (Si/Al=8,2) containing 4%NiO and 15%MoO3. The presence of nitrogen as pyridine was detrimental for the performance of all catalysts, including the standards one, supplied for the CENPES.
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Valentini, Laura. "Essays on environmental policy, plant location and financial liability." Thesis, University of Southampton, 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.313192.

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Alamoudi, Majed. "Hydrodesulphurization of dibenzothiophene using carbon supported NiMoS catalysts." Thesis, University of British Columbia, 2016. http://hdl.handle.net/2429/57541.

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Hydrodesulphurization (HDS) is the major process used to remove S from crude oil feedstocks in order to improve fuel quality and meet environmental regulations. The goal of this study was to determine if petroleum coke (petcoke), derived from Alberta oilsands, could be converted into a useful catalyst support. Hence the HDS activity and selectivity of nickel molybdenum sulfided catalysts supported on activated carbon (NiMoS/AC), petroleum coke (NiMoS/PC) and conventional alumina (NiMo/γ-Al₂O₃) have been compared using dibenzothiophene (DBT) as a model reactant. The reactions were carried out in a novel slurry-phase batch microreactor at different reaction times (30-120 min) and temperatures (588-638 K) and a fixed H2 pressure (4.8 MPa). The results showed that NiMoS/PC had higher activity towards the HDS of DBT when compared with NiMoS/AC, although the catalysts had very similar product selectivities. The highest activity for DBT HDS, corresponding to 90% DBT conversion, occurred at 638 K for the NiMoS/AC catalyst and at 623K for the NiMoS/PC catalyst. The reaction proceeded by two pathways: the direct desulphurization (DDS) reaction route and the hydrogenation (HYD) reaction route. The power law pseudo 1st-order kinetic model was applied to the HDS of DBT. The estimated kinetic parameters showed similar magnitudes for the HYD versus the DDS routes over both catalysts, whereas the DDS pathway had higher apparent activation energy compared to the HYD route for both catalysts.
Applied Science, Faculty of
Chemical and Biological Engineering, Department of
Graduate
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5

Steffel, Jennifer Elaine. "Storming the suburban fortress : understanding the NIMBY phenomenon." Thesis, McGill University, 1995. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=23704.

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The ubiquitous settlement pattern of the American suburb is in fact a carefully constructed reality. Because the vision of the home in the suburbs is very deeply rooted, any development which is considered threatening to this image is met with a defensive reaction. Too often, however, when these NIMBY ("Not In My Back Yard") sentiments are permitted to dictate what is acceptable in a community, housing affordable to low- and moderate-income households is purposely excluded.
This thesis explores the processes by which discriminatory NIMBY sentiments are realized as legal development regulations in contemporary suburbs. The historic evolution of the suburbs and the psychological foundations behind their typical characteristics are presented as the sources of a suburban value structure which esteems NIMBY. Suburban governments are mandated to represent their constituents' values, but exclusionary development controls are a complex product of constituent demands, fiscal constraints, and constitutional limits.
This analysis reveals that legislative responsibility often bows to political weakness. NIMBY groups use political pressure to manipulate municipal governments into using their vast discretionary powers over development as a weapon for exclusion. In response to either political or fiscal motivations, legislators pressure planners to validate discriminatory legislative agendas with their plans, thus undermining their abilities to guide growth effectively. Although the process of development regulation is well-grounded in historic and legal precedents, when legislation is used for discriminatory ends, citizens' civil and property rights are jeopardized. This thesis explains how regulations such as zoning ordinances can be used for exclusion when municipal government disregards its mandate to be the guardian of the general welfare.
Increased awareness of both the motivations and the manifestations of the NIMBY phenomenon may enable individuals as well as lawmakers to create a more equitable suburbia.
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Boatwright, Jessica Ann. "Siting Community Wind Farms: An Investigation of NIMBY." Thesis, Virginia Tech, 2013. http://hdl.handle.net/10919/23750.

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Wind energy is expanding rapidly in the United States as the nation\'s energy policy objectives increasingly focus on renewables. Public opinion polls show that a majority of Americans support wind energy development but actual wind farm projects often face intense local opposition. This dichotomy between general support for wind energy but opposition towards siting a project nearby is often attributed to the not-in-my-backyard (NIMBY) phenomenon. In this study we employ a discrete choice experiment to investigate public preferences for different characteristics of a local wind farm. We investigate NIMBY by first controlling for characteristics that might cause local opposition, such as seeing or hearing a wind farm from home, and then after considering these effects of a wind farm we examine whether people who favor wind energy display NIMBY resistance. Finally, we estimate compensation requirements for siting a wind farm within sight or sound of someone\'s home. Results show that people who somewhat favor wind energy do display NIMBY attitudes since they are predisposed to vote against local wind development even after controlling whether they would see and hear the wind farm from their homes. We do not detect NIMBY attitudes among people who strongly favor wind energy because they have a positive disposition towards local wind farms. Our results suggest that if an incentive program is in place from the onset of a wind development project it could offset NIMBY reactions to specific projects.
Master of Science
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Bolehovský, Petr. "Vliv umístění zařízení na nakládání s odpady na regionální rozvoj a síla vlivu NIMBY efektu ("not in my backyard")." Master's thesis, Vysoká škola ekonomická v Praze, 2011. http://www.nusl.cz/ntk/nusl-72752.

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NIMBY is widely used acronym for people's unwilingness to house noxious facilities in their immediate neighborhood. People feel that they are somewhat and they expect to be compensated for this. Goal of this thesis is to evaluate influence of monetary compensations on people's willingness to accept these facilities. Evaluates effects of Crowding Theory, extristic and intristic motivations on willingness to accept these facilities. Used method was qualitative analysis in form of controlled interviews with key stakeholders (mayor and town citizens). Author tries to evaluate if the NIMBY effect is the main reason for generally bad acceptance of this facilities. This thesis explores the NIMBY effect on construction of one of these facilities in town Chotíkov with a view on the gradual development of view throughout the population of this town.
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Sörensen, Jimmie. "NIMBY eller YIMBY? : Upplands Väsbys vindkraft i Ockelbo kommun." Thesis, Stockholms universitet, Institutionen för naturgeografi och kvartärgeologi (INK), 2014. http://urn.kb.se/resolve?urn=urn:nbn:se:su:diva-104621.

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Syftet med denna uppsats är att undersöka den lokala uppfattningen i Ockelbo gentemot etableringen av en vindkraftspark i näromgivningen samt vad som ligger bakom Upplands Väsbys val att bygga ett vindkraftverk på annan ort. Resultaten visar att NIMBY-åsikter inte ligger bakom Upplands Väsbys val samt att attityden som återges bland de boende och kommuntjänstemännen i Ockelbo kommun präglas av en positiv inställning mot vindkraftsetableringen i deras närmiljö. Den positiva inställningen grundar sig främst på utbetalningen av bygdepengen samt att vindkraften symboliserar och innebär miljövänlig energi.
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Joffres, Benoît. "Synthèse de bio-liquide de seconde génération par hydroliquéfaction catalytique de la lignine." Thesis, Lyon 1, 2013. http://www.theses.fr/2013LYO10223.

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Actuellement, la transformation de la biomasse en bio-carburant ou molécules pour l'industrie chimique fait l'objet de nombreuses recherches. La lignine, en tant que coproduit de l'industrie papetière et de l'éthanol cellulosique, est une ressource des plus disponibles qui pourait être utilisée pour la production d'aromatiques ou de composés phénoliques. Cependant, cette macromolécule constituée d'unités propylphénoliques liées par des liaisons éthers nécessite d'être dépolymérisée. Ce travail porte sur la compréhension des mécanismes de liquéfaction par hydroconversion catalytique d'une lignine de paille de blé extraite par un procédé papetier à la soude. Dans un premier temps, nous avons mené une caractérisation poussée de cette lignine à l'aide de diverses techniques qui nous a permis de proposer une structure modèle. Ensuite, nous avons mis en place un mode opératoire de conversion et un protocole de récupération des produits. La réaction est réalisée en réacteur semi-ouvert à 350°C en présence d'H2 (8MPa), d'un solvant donneur d'hydrogène (tétraline) et d'un catalyseur d'hydrotraitement NiMoP/Al2O3 sulfuré. Les produits se répartissent en une phase liquide (liquéfiat), une phase gaz, une lignine résiduelle et des solides non-solubles dans le THF. Un taux de conversion a été défini comme le rendement en produits non-solides et les valeurs maximales atteintes sont de 81% pds après 28h de réaction avec un excellent bilan matière. Les fractions récupérées ont ensuite été caractérisées en détail avec des techniques d'analyse adaptées. Grâce à ce protocole d'analyse, nous avons pu observer que le solvant permet d'éviter la formation de solides et que le catalyseur intervient principalement sur l'hydrodésoxygénation et l'hydrogénation des molécules issues de la dépolymérisation de la charge. Enfin, nous avons suivis la réaction au cours du temps, ce qui nous a permis de présenter une ébauche de schéma réactionnel. Les premières étapes de conversion sont la décarboxylation, l'hydrogénolyse des OH aliphatiques et la rupture des liaisons éthers entre les unités élémentaires de la lignine, qui entraînent sa dépolymérisation. Puis des processus plus lent se produisent comme l'élimination des groupes méthoxy, principalement par déméthylation suivi de déshydroxylation. Ainsi, les principaux produits obtenus sont des composés phénoliques et des composés désoxygénés
Nowadays, the transformation of lignocellulosic biomass is deeply investigated in order to provide biofuels and chemicals. Lignin, a by-product of pulp and bio-ethanol industry, is an available resource which could be used for the production of aromatic and phenolic compounds. However, this macromolecule mainly made of propylphenolic units linked by ether functions needs to be depolymerized. This work focuses on the study of liquefaction mechanisms by catalytic hydroconversion of wheat straw lignin extracted by a soda pulping. In the first part of this study, an in-depth characterization of this lignin was carried out using techniques. A structure of our lignin was proposed as a result. Then, a procedure was developed to perform the catalytic hydroconversion and recover the products. Catalytic experiments were carried out in a semi-batch reactor at 350°C, using H2 (8 MPa), a hydrogen donor solvent (tetralin) and a sulfide NiMoP/Al2O3 catalyst. The recovered products were separated into a liquid phase, gases, a lignin residue and THF insoluble solids. A conversion of 81 wt% of lignin into non-solid products was reached after 28h of reaction with an excellent mass balance. The characterization of the different fractions was carried out using techniques. Thanks to this protocol, we were able to point out the role of the H-donor solvent for preventing solid formation as well as the role of the catalyst for hydrodeoxygenation and hydrogenation of the depolymerized products. Finally, the catalytic hydroconversion of the lignin was carried out with the different residence times, which helps understanding the transformations occurring during the conversion. At the beginning of the reaction, we observed decarboxylation, hydrogenolysis of aliphatic OH and cleavage of ether linkages between the phenolic units of the lignin. Then, we observed elimination of methoxy groups, mainly by demethylation followed by dehydroxylation. Finally, the main products obtained during the reaction were phenolic and deoxygenated compounds such as aromatics, naphthenes and alkanes
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Novotná, Miroslava. "NIMBY efekt: Postoj obyvatel v případě plánované výstavby bioplynové stanice." Master's thesis, Vysoká škola ekonomická v Praze, 2012. http://www.nusl.cz/ntk/nusl-125010.

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The aim of the thesis is a research of the "Not In My Back Yard" effect, a negative attitude of local people to a construction of a new and potentially dangerous project in their vicinity. The thesis quantifies strength of the NIMBY effect in Městec Králové, a town where a biogas plant is planned to be constructed. The hypothesis is that the strength of the NIMBY effect is higher for the people who live in a higher proximity to a planned construction than for the people who do not.The hypothesis is evaluated based on data gained by an own survey conducted among residents of the town.Quantification of the NIMBY effect is more frequently a subject of research of foreign studies; empirical studies of biogas plants are rather rare. From this reason I have implemented a study of population of Městec Králové and tried to prove whether presence of the "Not In My Back Yard" effect can be indicated.
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Books on the topic "Nimoy"

1

Micklos, John. Leonard Nimoy: A star's trek. Minneapolis, Minn: Dillon Press, 1988.

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My incredibly wonderful, miserable life: An anti-memoir. New York: Pocket Books, 2015.

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Kobylet͡sʹkyĭ, I͡Ulian. Nimby: [virshi]. Lʹviv: Ukraïnsʹki Tekhnolohiï, 1999.

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Aquino, Corazon Cojuangco. Ninoy and Cory. Manila: Cory Aquino, 2001.

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Rofer, Francisco. Sino nimos españoles. Me xico, D.F: Editores Mexicanos Unidos, 1992.

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The NIMBY factor. New York: St. Martin's Press, 1992.

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Slaying the NIMBY dragon. New Brunswick, U.S.A: Transaction Publishers, 1998.

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Ninoy: The willing martyr. [Philippines]: Isaiah Books, 1986.

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Johari, Allama Talib. Harf-e-nimo. Lahore: Mawra Publishers, 2002.

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1965-, Stygryt, ed. Los dioses de Nimo: Chi ndi enwere na nimo. Paterna, Valencia: Ecir, 2007.

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Book chapters on the topic "Nimoy"

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Bitonti, Alberto. "NIMBY." In The Palgrave Encyclopedia of Interest Groups, Lobbying and Public Affairs, 916–18. Cham: Springer International Publishing, 2022. http://dx.doi.org/10.1007/978-3-030-44556-0_142.

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Bitonti, Alberto. "NIMBY." In The Palgrave Encyclopedia of Interest Groups, Lobbying and Public Affairs, 1–3. Cham: Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-13895-0_142-1.

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Horstkorte, Rüdiger, Bettina Büttner, Kaya Bork, Navdeep Sahota, Sarah Sabir, Laura O’Regan, Joelle Blot, et al. "NimO (Aspergillus)." In Encyclopedia of Signaling Molecules, 1228. New York, NY: Springer New York, 2012. http://dx.doi.org/10.1007/978-1-4419-0461-4_100926.

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Chung, Shan Shan. "Collective Versus Self-interests: What Is Behind NIMBY?" In Land and Housing Controversies in Hong Kong, 145–67. Singapore: Springer Singapore, 2020. http://dx.doi.org/10.1007/978-981-15-5266-3_8.

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Menzl, Marcus. "Nimby-Proteste – Ausdruck neu erwachten Partizipationsinteresses oder eines zerfallenden Gemeinwesens?" In Stadt und soziale Bewegungen, 65–81. Wiesbaden: Springer Fachmedien Wiesbaden, 2014. http://dx.doi.org/10.1007/978-3-658-01398-1_4.

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Scally, Corianne Payton, and J. Rosie Tighe. "Democracy in action? NIMBY as impediment to equitable affordable housing siting." In The Affordable Housing Reader, 337–54. 2nd ed. London: Routledge, 2022. http://dx.doi.org/10.4324/9780429299377-30.

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Magnani, Natalia. "Civil Society and Conflicts Over Renewable Energies Beyond the NIMBY Syndrome." In Understanding the Energy Transition, 27–52. Cham: Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-83481-4_3.

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Kollo, Lauri, Jüri Pirso, and Kristjan Juhani. "Effect of Sinter/HIP Technology on Properties of TiC-NiMo Cermets." In Progress in Powder Metallurgy, 1169–72. Stafa: Trans Tech Publications Ltd., 2007. http://dx.doi.org/10.4028/0-87849-419-7.1169.

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Hubbard, Phil. "NIMBY." In International Encyclopedia of Human Geography, 403–7. Elsevier, 2009. http://dx.doi.org/10.1016/b978-0-08-102295-5.10019-8.

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Hubbard, P. "NIMBY." In International Encyclopedia of Human Geography, 444–49. Elsevier, 2009. http://dx.doi.org/10.1016/b978-008044910-4.01068-3.

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Conference papers on the topic "Nimoy"

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Nepomnyashchiy, A. A., E. A. Buluchevskiy, T. R. Karpova, and A. V. Lavrenov. "Hydrodeoxygenation of sunflower oil over NiMoS/MoO3-Al2O3 and NiMoS/P2O5-Al2O3 catalysts." In 21ST CENTURY: CHEMISTRY TO LIFE. AIP Publishing, 2019. http://dx.doi.org/10.1063/1.5122951.

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Tian, P., and S. J. Chen. "Discussion on NIMBY Phenomena and Governance Strategies." In 2015 International Conference on Social Science, Education Management and Sports Education. Paris, France: Atlantis Press, 2015. http://dx.doi.org/10.2991/ssemse-15.2015.244.

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Ling, Qiang, Jian Cai, Shuidi Wang, and Huiyou Zhao. "Electroless NiMoP Thin Film Deposition on Si/SiO2." In 2007 8th International Conference on Electronic Packaging Technology. IEEE, 2007. http://dx.doi.org/10.1109/icept.2007.4441459.

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Gu, Yong, Lie Zhang, Zhengdu Wang, and Yangyang Zheng. "Bi-level planning model for NIMBY facility location problem." In 2017 36th Chinese Control Conference (CCC). IEEE, 2017. http://dx.doi.org/10.23919/chicc.2017.8028549.

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Kobayashi, Takako, Takeo Kondo, Yuji Miura, Kazukiyo Yamamoto, and Wataru Miyazaki. "An Attitude Survey on the Establishment of Offshore BSL-4 Facility as a NIMBY." In ASME 2010 29th International Conference on Ocean, Offshore and Arctic Engineering. ASMEDC, 2010. http://dx.doi.org/10.1115/omae2010-20603.

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We conducted a pilot attitude survey about attitude towards NIMBY (not in my back yard) facility with the students who major in ocean engineering and environmental engineering as subjects. The results found the following: facilities that are most often considered NIMBYs are a nuclear power plant, an industrial waste disposal facility, followed by a bio-research institute; if a NIMBY is established more than 50 km apart from the subjects’ residential area, its presence becomes acceptable; the degree of rejection lessens in the order of an isolated, uninhabited island, on a desert, and a submarine location. Also, the results showed that the best merit of building a BSL-4 facility offshore is that it can be relocated to another location if necessary. As a conclusion, a BSL-4 facility is most likely to be accepted to the local residents if it is built on a floating construction 50 km offshore, allowing to move to another location if necessary.
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Salleh, Abdul Hakim, Mohd Sanusi S. Ahamad, Mohd Suffian Yusoff, and Hamidi Abdul Aziz. "Multiple criteria landfill site selection method incorporating the NIMBY factors." In PROCEEDINGS OF THE INTERNATIONAL CONFERENCE OF GLOBAL NETWORK FOR INNOVATIVE TECHNOLOGY AND AWAM INTERNATIONAL CONFERENCE IN CIVIL ENGINEERING (IGNITE-AICCE’17): Sustainable Technology And Practice For Infrastructure and Community Resilience. Author(s), 2017. http://dx.doi.org/10.1063/1.5005759.

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MELLO, M. D., J. A. VILLETH, F. A. BRAGGIO, J. L. ZOTIN, and M. A. P. da SILVA. "HIDRODESSULFURIZAÇÃO DE DIBENZOTIOFENO E 4,6-DIMETILDIBENZOTIOFENO EM CATALISADOR NiMoP/Al2O3." In XX Congresso Brasileiro de Engenharia Química. São Paulo: Editora Edgard Blücher, 2015. http://dx.doi.org/10.5151/chemeng-cobeq2014-1381-19568-155546.

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NUGRAHANINGTYAS, KHOIRINA DWI, DIAN MARUTO WIDJONARKO, WEGA TRI SUNARYANTI, and TRIYONO. "PREPARATION AND CHARACTERIZATION OF NIMO/ACTIVE NATURAL ZEOLITE CATALYSTS." In Proceedings of the International Conference on CBEE 2009. WORLD SCIENTIFIC, 2009. http://dx.doi.org/10.1142/9789814295048_0035.

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Ghoreishi, S. M., and M. Alibouri. "Synthesis of NiMo/Al2O3 nanocatalyst via supercritical fluid technology." In 2010 International Conference on Enabling Science and Nanotechnology (ESciNano). IEEE, 2010. http://dx.doi.org/10.1109/escinano.2010.5701060.

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Almeida, Antonio V. "Wastewater Rehabilitation in a NIMBY Environment: The Lake Arlington Wastewater Interceptor." In Pipeline Division Specialty Conference 2006. Reston, VA: American Society of Civil Engineers, 2006. http://dx.doi.org/10.1061/40854(211)93.

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Reports on the topic "Nimoy"

1

Levinson, Arik. NIMBY Taxes Matter: State Taxes and Interstate Hazardous Waste Shipments. Cambridge, MA: National Bureau of Economic Research, December 1997. http://dx.doi.org/10.3386/w6314.

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Bobrick, Micheal C. A Reasoned Response to Nimby Opposition to Incineration of Chemical Weapon Stockpiles. Fort Belvoir, VA: Defense Technical Information Center, April 1993. http://dx.doi.org/10.21236/ada456582.

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Comolli, A. G., E. S. Johanson, S. V. Panvelker, G. A. Popper, and R. H. Stalzer. Two-stage, close coupled catalytic liquefaction of coal. [Catalysts: FeOOH and NiMo]. Office of Scientific and Technical Information (OSTI), October 1991. http://dx.doi.org/10.2172/5899665.

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Lacetera, Nicola, and Mario Macis. Moral NIMBY-ism? Understanding Societal Support for Monetary Compensation to Plasma Donors in Canada. Cambridge, MA: National Bureau of Economic Research, May 2018. http://dx.doi.org/10.3386/w24572.

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Chaturvedi, S., J. A. Rodriguez, J. C. Hanson, A. Albornoz, and J. L. Brito. Properties of pure and sulfided NiMoO{sub 4} and CoMoO{sub 4} catalysts: TPR, XANES and time-resolved XRD studies. Office of Scientific and Technical Information (OSTI), December 1998. http://dx.doi.org/10.2172/555287.

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