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  • About
  • The Global ETD Search service is a free service for researchers to find electronic theses and dissertations. This service is provided by the Networked Digital Library of Theses and Dissertations.
    Our metadata is collected from universities around the world. If you manage a university/consortium/country archive and want to be added, details can be found on the NDLTD website.
1

Investigation of Single and Double Network Gels by Maximum Bubble Pressure Rheology

Chen, Yan January 2014 (has links)
No description available.
2

Dynamická tenziometrie ve výzkumu biokoloidů / Dynamic tensiometry of biocolloids

Kulilová, Pavlína January 2008 (has links)
Hyaluronová kyselina je v současné době velmi významná biomolekula používaná v medicíně a kosmetice, a její výzkum je důležitý pro další budoucí použití. Zaměření této práce je studování povrchových vlastností hyaluronové kyseliny, jejích hydrofobních derivátů a roztoků SDS pro srovnání, za použití tenziometrie. Tyto sloučeniny byly zkoumány ve vodě a v roztocích ve formě sodné soli. Sledované vzorky byly měřeny dvěmi metodami v různých koncentračních rozmezích při laboratorní teplotě pomocí nového BPA-800P bublinového tenziometeru. Byly navrženy takové experimenty, aby se zjistily využitelné možnosti tohoto přístroje pro další výzkum. Výsledky práce ukazují rozdílnosti jednotlivých povrchově aktivních látek v závislosti na jejich koncentraci a použitém prostředí. Hyaluronová kyselina nevykazuje povrchovou aktivitu, zatímco její deriváty a SDS ano.
3

[pt] MODELO TERMODINÂMICO PARA ELV DO SISTEMA ÁGUA - MDEA: MODELOS DE PENG-ROBINSON E UNIQUAC / [en] THERMODYNAMIC MODEL FOR VLE WATER - MDEA SYSTEM: PENGROBINSON AND UNIQUAC MODELS

PEDRO HENRIQUE DE LIMA RIPPER MOREIRA 27 September 2023 (has links)
[pt] A determinação de parâmetros de interação precisos para equações de estado (EdE) em sistemas aquosos de aminas são cruciais para desenvolver modelos termodinâmicos em processos da engenharia química. O sistema binário de Nmetildietanolamina (MDEA) e água na purificação do biogás foi avaliado usando as abordagens 𝜑 – 𝜑 e 𝛾 – 𝜑, EdE de Peng–Robinson clássico com a regra de mistura não aleatória e EdE Peng–Robinson com a regra de mistura Wong-Sandler, para otimizar o fator acêntrico, ω, de componentes puros, e os parâmetros de interação binária, 𝑘𝑖𝑗. Os parâmetros de interação 𝑢𝑖𝑗 das EdE que incorporam o modelo UNIQUAC, como a abordagem γ – φ e a regra de mistura de Wong-Sandler também foram otimizados. Esses parâmetros foram avaliados usando um algoritmo de pressão de bolha reativa, codificação MATLAB e minimização de funções objetivas relacionadas ao desvio médio absoluto, AAD, entre dados experimentais e calculados em diferentes temperaturas. Os ω calculados de água, CO2 e MDEA foram 0,3275, 0,2039 e 1,0133, respectivamente, com AAD inferior aos valores da literatura. A abordagem 𝜑 − 𝜑 com EdE clássica de Peng–Robinson com regra de mistura Wong– Sandler foi mais adequada para o binário MDEA – H2O, resultando em 𝑢12 0 = −234.2841, 𝑢12 𝑇 = 1.0499, 𝑢21 0 = 266.4326, 𝑢21 𝑇 = 0.1966, 𝑘𝑖𝑗 = −0.0715, com pressão de vapor AAD% = 6,57% e composição AAD% = 17,51%. Devido à natureza altamente não ideal do sistema binário CO2 – H2O, nem as abordagens φ – φ ou γ – φ usando as EdE selecionadas resultaram em diagramas precisos de pressão de ponto de bolha para o equilíbrio vapor – líquido (VLE). / [en] Determining interaction parameter for equations of state (EOS) of water – amines systems are crucial to develop accurate models in chemical engineering processes. The binary system of N-methyldiethanolamine (MDEA) and water in biogas purification was evaluated using both φ – φ and γ – φ approaches, classic Peng–Robinson with the empirical “non-random” mixing rule and Peng–Robinson with the Wong-Sandler mixing rule EOS to optimize pure components acentric factor, ω, and binary interaction parameters, 𝑘𝑖𝑗. The interaction parameters 𝑢𝑖𝑗 from EOS that incorporate UNIQUAC model, such as γ – φ approach and Wong-Sandler mixing rule were optimized as well. These parameters were evaluated using a bubble pressure algorithm, MATLAB coding and minimization of objective functions related to absolute average deviation, AAD, between experimental and calculated data at different temperatures. The calculated ω of water, CO2 and MDEA were 0.3275, 0.2039 and 1.0133 respectively with lower AAD than literature values. The 𝜑−𝜑 approach classic Peng–Robinson with Wong – Sandler mixing rule EOS was better suited for the MDEA – H2O binary, resulting in as 𝑢120=−234.2841, 𝑢12𝑇=1.0499, 𝑢210=266.4326, 𝑢21𝑇=0.1966, 𝑘𝑖𝑗=−0.0715, with vapor pressure AAD% = 6.57% and composition AAD% = 17.51%. Due to the highly non-ideal nature of the CO2 – H2O binary system, neither φ – φ or γ – φ approaches using the selected EOS resulted in accurate vapor – liquid equilibrium (VLE) bubble point pressure diagrams.

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