Friction and heat transfer coefficients in smooth and rough pipes with dilute polymer solutions

Measurements of friction and heat transfer coefficients were obtained with dilute polymer solutions flowing through electrically heated smooth and rough tubes. The polymer used was "Polyox WSR-301", and tests were performed at concentrations of 10 and 50 parts per million. The rough tubes contained a close-packed, granular type of surface with roughness-height-to-diameter ratios of 0.0138 and 0.0488 respectively. A Prandtl number range of 4.38 to 10.3 was investigated which was obtained by adjusting the bulk temperature of the solution. The Reynolds numbers in the experiments were varied from =10,000 (Pr= 10.3) to 250,000 (Pr= 4.38).

Friction reductions as high as 73% in smooth tubes and 83% in rough tubes were observed, accompanied by an even more drastic heat transfer reduction (as high as 84% in smooth tubes and 93% in rough tubes). The heat transfer coefficients with Polyox can be lower for a rough tube than for a smooth one.

The similarity rules previously developed for heat transfer with a Newtonian fluid were extended to dilute polymer solution pipe flows. A velocity profile similar to the one proposed by Deissler was taken as a model to interpret the friction and heat transfer data in smooth tubes. It was found that the observed results could be explained by assuming that the turbulent diffusivities are reduced in smooth tubes in the vicinity of the wall, which brings about a thickening of the viscous layer. A possible mechanism describing the effect of the polymer additive on rough pipe flow is also discussed.

Judgmental-analytical procedures for adapting tests: Adaptation to Spanish of the Reasoning Tests Battery

Adapting a test between cultures or languages requires taking into account legal, linguistic, metric, and use-related considerations. Significantly more attention has been paid to the methodological aspects involved in the study of metric equivalence than to judgmental-analytical procedures prior to the empirical confirmation stage. However, considering the latter is crucial in the adaptation process. Along these lines, this paper seeks to describe and focus on the relevance of the previous stages, thereby offering a systematization process that comprises ten sections. This approach contributes to ensuring the construction of a test adapted and equivalent in as much as possible to the original. This process is exemplified by means of a Spanish language adaptation of a cognitive test originally designed in Portuguese for the Portuguese population, the Reasoning Test Battery. Copyright (C) 2013, Konrad Lorenz University Foundation. Published by Elsevier Espana, S.L.U.

Advanced Reaction Systems for Hydrogen Production

[EN] This PhD work started in March 2010 with the support of the University of the Basque Country (UPV/EHU) under the program named “Formación de Personal Investigador” at the Chemical and Environmental Engineering Department in the Faculty of Engineering of Bilbao. The major part of the Thesis work was carried out in the mentioned department, as a member of the Sustainable Process Engineering (SuPrEn) research group. In addition, this PhD Thesis includes the research work developed during a period of 6 months at the Institut für Mikrotechnik Mainz GmbH, IMM, in Germany. During the four years of the Thesis, conventional and microreactor systems were tested for several feedstocks renewable and non-renewable, gases and liquids through several reforming processes in order to produce hydrogen. For this purpose, new catalytic formulations which showed high activity, selectivity and stability were design. As a consequence, the PhD work performed allowed the publication of seven scientific articles in peer-reviewed journals. This PhD Thesis is divided into the following six chapters described below. The opportunity of this work is established on the basis of the transition period needed for moving from a petroleum based energy system to a renewable based new one. Consequently, the present global energy scenario was detailed in Chapter 1, and the role of hydrogen as a real alternative in the future energy system was justified based on several outlooks. Therefore, renewable and non-renewable hydrogen production routes were presented, explaining the corresponding benefits and drawbacks. Then, the raw materials used in this Thesis work were described and the most important issues regarding the processes and the characteristics of the catalytic formulations were explained. The introduction chapter finishes by introducing the concepts of decentralized production and process intensification with the use of microreactors. In addition, a small description of these innovative reaction systems and the benefits that entailed their use were also mentioned. In Chapter 2 the main objectives of this Thesis work are summarized. The development of advanced reaction systems for hydrogen rich mixtures production is the main objective. In addition, the use and comparison between two different reaction systems, (fixed bed reactor (FBR) and microreactor), the processing of renewable raw materials, the development of new, active, selective and stable catalytic formulations, and the optimization of the operating conditions were also established as additional partial objectives. Methane and natural gas (NG) steam reforming experimental results obtained when operated with microreactor and FBR systems are presented in Chapter 3. For these experiments nickel-based (Ni/Al2O3 and Ni/MgO) and noble metal-based (Pd/Al2O3 and Pt/Al2O3) catalysts were prepared by wet impregnation and their catalytic activity was measured at several temperatures, from 973 to 1073 K, different S/C ratios, from 1.0 to 2.0, and atmospheric pressure. The Weight Hourly Space Velocity (WHSV) was maintained constant in order to compare the catalytic activity in both reaction systems. The results obtained showed a better performance of the catalysts operating in microreactors. The Ni/MgO catalyst reached the highest hydrogen production yield at 1073 K and steam-to-carbon ratio (S/C) of 1.5 under Steam methane Reforming (SMR) conditions. In addition, this catalyst also showed good activity and stability under NG reforming at S/C=1.0 and 2.0. The Ni/Al2O3 catalyst also showed high activity and good stability and it was the catalyst reaching the highest methane conversion (72.9 %) and H2out/CH4in ratio (2.4) under SMR conditions at 1073 K and S/C=1.0. However, this catalyst suffered from deactivation when it was tested under NG reforming conditions. Regarding the activity measurements carried out with the noble metal-based catalysts in the microreactor systems, they suffered a very quick deactivation, probably because of the effects attributed to carbon deposition, which was detected by Scanning Electron Microscope (SEM). When the FBR was used no catalytic activity was measured with the catalysts under investigation, probably because they were operated at the same WHSV than the microreactors and these WHSVs were too high for FBR system. In Chapter 4 biogas reforming processes were studied. This chapter starts with an introduction explaining the properties of the biogas and the main production routes. Then, the experimental procedure carried out is detailed giving concrete information about the experimental set-up, defining the parameters measured, specifying the characteristics of the reactors used and describing the characterization techniques utilized. Each following section describes the results obtained from activity testing with the different catalysts prepared, which is subsequently summarized: Section 4.3: Biogas reforming processes using γ-Al2O3 based catalysts The activity results obtained by several Ni-based catalysts and a bimetallic Rh-Ni catalyst supported on magnesia or alumina modified with oxides like CeO2 and ZrO2 are presented in this section. In addition, an alumina-based commercial catalyst was tested in order to compare the activity results measured. Four different biogas reforming processes were studied using a FBR: dry reforming (DR), biogas steam reforming (BSR), biogas oxidative reforming (BOR) and tri-reforming (TR). For the BSR process different steam to carbon ratios (S/C) from 1.0 to 3.0, were tested. In the case of BOR process the oxygen-to-methane (O2/CH4) ratio was varied from 0.125 to 0.50. Finally, for TR processes different S/C ratios from 1.0 to 3.0, and O2/CH4 ratios of 0.25 and 0.50 were studied. Then, the catalysts which achieved high activity and stability were impregnated in a microreactor to explore the viability of process intensification. The operation with microreactors was carried out under the best experimental conditions measured in the FBR. In addition, the physicochemical characterization of the fresh and spent catalysts was carried out by Inductively Coupled Plasma Atomic Emission Spectroscopy (ICP-AES), N2 physisorption, H2 chemisorption, Temperature Programmed Reduction (TPR), SEM, X-ray Photoelectron Spectroscopy (XPS) and X-ray powder Diffraction (XRD). Operating with the FBR, conversions close to the ones predicted by thermodynamic calculations were obtained by most of the catalysts tested. The Rh-Ni/Ce-Al2O3 catalyst obtained the highest hydrogen production yield in DR. In BSR process, the Ni/Ce-Al2O3 catalyst achieved the best activity results operating at S/C=1.0. In the case of BOR process, the Ni/Ce-Zr-Al2O3 catalyst showed the highest reactants conversion values operating at O2/CH4=0.25. Finally, in the TR process the Rh-Ni/Ce-Al2O3 catalyst obtained the best results operating at S/C=1.0 and O2/CH4=0.25. Therefore, these three catalysts were selected to be coated onto microchannels in order to test its performance under BOR and TR processes conditions. Although the operation using microreactors was carried out under considerably higher WHSV, similar conversions and yields as the ones measured in FBR were measured. Furthermore, attending to other measurements like Turnover Frequency (TOF) and Hydrogen Productivity (PROD), the values calculated for the catalysts tested in microreactors were one order of magnitude higher. Thus, due to the low dispersion degree measured by H2-chemisorption, the Ni/Ce-Al2O3 catalyst reached the highest TOF and PROD values. Section 4.4: Biogas reforming processes using Zeolites L based catalysts In this section three type of L zeolites, with different morphology and size, were synthesized and used as catalyst support. Then, for each type of L zeolite three nickel monometallic and their homologous Rh-Ni bimetallic catalysts were prepared by the wetness impregnation method. These catalysts were tested using the FBR under DR process and different conditions of BSR (S/C ratio of 1.0 and 2.0), BOR (O2/CH4 ratio of 0.25 and 0.50) and TR processes (at S/C=1.0 and O2/CH4=0.25). The characterization of these catalysts was also carried out by using the same techniques mentioned in the previous section. Very high methane and carbon dioxide conversion values were measured for almost all the catalysts under investigation. The experimental results evidenced the better catalytic behavior of the bimetallic catalysts as compared to the monometallic ones. Comparing the catalysts behavior with regards to their morphology, for the BSR process the Disc catalysts were the most active ones at the lowest S/C ratio tested. On the contrary, the Cylindrical (30–60 nm) catalysts were more active under BOR conditions at O2/CH4=0.25 and TR processes. By the contrary, the Cylindrical (1–3 µm) catalysts showed the worst activity results for both processes. Section 4.5: Biogas reforming processes using Na+ and Cs+ doped Zeolites LTL based catalysts A method for the synthesis of Linde Type L (LTL) zeolite under microwave-assisted hydrothermal conditions and its behavior as a support for heterogeneously catalyzed hydrogen production is described in this section. Then, rhodium and nickel-based bimetallic catalysts were prepared in order to be tested by DR process and BOR process at O2/CH4=0.25. Moreover, the characterization of the catalysts under investigation was also carried out. Higher activities were achieved by the catalysts prepared from the non-doped zeolites, Rh-Ni/D and Rh-Ni/N, as compared to the ones supported on Na+ and Cs+ exchanged supports. However, the differences between them were not very significant. In addition, the Na+ and Cs+ incorporation affected mainly to the Disc catalysts. Comparing the results obtained by these catalysts with the ones studied in the section 4.4, in general worst results were achieved under DR conditions and almost the same results when operated under BOR conditions. In Chapter 5 the ethylene glycol (EG) as feed for syngas production by steam reforming (SR) and oxidative steam reforming (OSR) was studied by using microchannel reactors. The product composition was determined at a S/C of 4.0, reaction temperatures between 625°C and 725°C, atmospheric pressure and Volume Hourly Space Velocities (VHSV) between 100 and 300 NL/(gcath). This work was divided in two sections. The first one corresponds to the introduction of the main and most promising EG production routes. Then, the new experimental procedure is detailed and the information about the experimental set-up and the measured parameters is described. The characterization was carried out using the same techniques as for the previous chapter. Then, the next sections correspond to the catalytic activity and catalysts characterization results. Section 5.3: xRh-cm and xRh-np catalysts for ethylene glycol reforming Initially, catalysts with different rhodium loading, from 1.0 to 5.0 wt. %, and supported on α-Al2O3 were prepared by two different preparation methods (conventional impregnation and separate nanoparticle synthesis). Then, the catalysts were compared regarding their measured activity and selectivity, as well as the characterization results obtained before and after the activity tests carried out. The samples prepared by a conventional impregnation method showed generally higher activity compared to catalysts prepared from Rh nanoparticles. By-product formation of species such as acetaldehyde, ethane and ethylene was detected, regardless if oxygen was added to the feed or not. Among the catalysts tested, the 2.5Rh-cm catalyst was considered the best one. Section 5.4: 2.5Rh-cm catalyst support modification with CeO2 and La2O3 In this part of the Chapter 5, the catalyst showing the best performance in the previous section, the 2.5Rh-Al2O3 catalyst, was selected in order to be improved. Therefore, new Rh based catalysts were designed using α-Al2O3 and being modified this support with different contents of CeO2 or La2O3 oxides. All the catalysts containing additives showed complete conversion and selectivities close to the equilibrium in both SR and OSR processes. In addition, for these catalysts the concentrations measured for the C2H4, CH4, CH3CHO and C2H6 by-products were very low. Finally, the 2.5Rh-20Ce catalyst was selected according to its catalytic activity and characterization results in order to run a stability test, which lasted more than 115 hours under stable operation. The last chapter, Chapter 6, summarizes the main conclusions achieved throughout this Thesis work. Although very high reactant conversions and rich hydrogen mixtures were obtained using a fixed bed reaction system, the use of microreactors improves the key issues, heat and mass transfer limitations, through which the reforming reactions are intensified. Therefore, they seem to be a very interesting and promising alternative for process intensification and decentralized production for remote application.

Pragmatemas e a música no ensino-aprendizagem de inglês como língua adicional em um colégio estadual do RJ: papel na retenção lexical

O presente estudo analisa as contribuições do uso da música e de pragmatemas na retenção lexical por parte de três turmas de inglês como língua adicional em uma escola estadual na cidade de São João de Meriti (RJ). Para tal, constituiu três condições de pesquisa das quais fizeram parte doze alunos na turma 1 (T1); doze alunos na turma 2 (T2); e nove alunos na turma 3 (T3). A turma 1 (T1) participou de práticas pedagógicas com foco na música e sem foco explícito nos pragmatemas presentes na letra; a turma 2 (T2) de práticas pedagógicas com foco na música e nos pragmatemas da letra; e a turma 3 (T3) de práticas pedagógicas voltadas somente para o ensino-aprendizagem dos pragmatemas presentes na letra, sem o suporte da música. Anteriormente à intervenção, foi aplicado um questionário sobre os hábitos sócio-culturais dos participantes visando conhecer suas preferências musicais e perfil de letramento. Para analisar a relação entre o uso da música e de pragmatemas na retenção lexical, foram aplicados um pré-teste antes da intervenção e dois pós-testes com intervalo de 1 mês entre eles. Além disso, o estudo contou com uma entrevista semi-estruturada com os participantes, visando entender a percepção dos mesmos sobre as práticas utilizadas na intervenção. Os achados apontam que houve uma retenção ligeiramente superior nas condições T2 (música e foco nos pragmatemas) e T3 (foco exclusivo nos pragmatemas), com ligeira superioridade para a condição 3. O pragmatema recuperado com maior frequência foi "What's up", fato que pode ser parcialmente explicado pelo fato de ser pronunciado como uma palavra só e pelo número de letras que o representa ortograficamente. Estudos futuros poderão esclarecer se há significância estatística entre as diferenças encontradas assim como melhor explorar como o ensino explícito de unidades lexicais complexas pode contribuir para a retenção desses itens lexicais e consequentemente para o ensino-aprendizagem de línguas adicionais. A intervenção permitiu que os aprendizes passassem a entender que as palavras não ocorrem de modo isolado, mas que sempre caminham junto a outras. Permitiu também que a rotina pedagógica contemplasse a coconstrução do conhecimento, levando os aprendizes a reagir positivamente às práticas utilizadas no ensino de inglês, conforme relatos durante as entrevistas semi-estruturadas. Isso per se já justifica a utilização de práticas semelhantes e ilustra a contribuição do presente estudo

Influência da espessura do filme de cimento na resistência adesiva de pinos de fibra de vidro cimentados em condutos radiculares de dentes humanos

O presente estudo visa avaliar a influência da espessura do filme de cimento sobre a resistência de união de pinos de fibra de vidro em diferentes regiões do conduto radicular (cervical, médio e apical), cimentados com cimento resinoso autoadesivo, com e sem a adição de Rodamina B, por meio do teste de push-out. Quarenta raízes foram incluídas em resina epóxi, submetidas a tratamento endodôntico e obturadas com guta percha e cimento endodôntico sem eugenol. Após sete dias, os condutos foram desobstruídos e aleatoriamente divididos em 4 grupos (n=10), de acordo com as brocas do sistema de pinos de fibra WhitePost DC (FGM) usadas: (G1) broca #2; (G2) broca #3; (G3) broca #4; (G4) broca #2. O preparo foi realizado a uma profundidade de 10 mm. A cimentação foi realizada com o cimento resinoso autoadesivo RelyX U100 (3M ESPE), e apenas nos grupos G1, G2 e G3 uma pequena quantidade de Rodamina B em pó foi usada como corante no cimento. Após uma semana, cada raiz foi seccionada em máquina de corte, obtendo-se 6 fatias de 1 0,1 mm de espessura. Antes do ensaio de push-out, imagens digitais foram obtidas, por meio de um estereomicroscópio, de ambas as faces de cada fatia, para determinação do raio dos pinos e da espessura do filme de cimento. Após o ensaio mecânico, novas imagens foram obtidas para determinação do modo de falha. Para determinar a espessura de cimento, foi desenvolvida uma rotina (macro) no software KS 400. Os dados foram estatisticamente analisados com análise de variância (ANOVA) 2 fatores (influência do diâmetro da broca e influência dos terços) e Kruskal-Wallis (influência da espessura do filme de cimento). Comparações múltiplas foram realizadas com o teste Duncan. Todos os testes foram aplicados com α=0,05. Houve diferenças significantes entre os grupos em relação ao diâmetro da broca (p<0,0001), sendo G2 (14,62 5,15 MPa) > G1 (10,04 5,13 MPa) > G3 (7,68 6,14 MPa). O terço do conduto exerceu influência significativa sobre a resistência adesiva (p<0,0001), sendo os maiores valores obtidos no terço apical. As espessuras do filme de cimento foram estatisticamente diferentes nos grupos. Os maiores valores de espessura de cimento foram obtidos no G3 (248,78 μm), seguido de G2 (185,91 μm) e G1 (110,16 μm), sendo o último estatisticamente semelhante ao G4 (119,99 μm). Os resultados de G1(10,04 5,13 MPa) e G4 (8,89 + 5,18 MPa) foram estatisticamente semelhantes, indicando que a presença da Rodamina B não influencia significativamente na resistência de união. O tipo de falha predominante no G1 foi mista, no G2, adesiva entre pino e cimento, e no G3 e G4, adesiva entre cimento e dentina. O diâmetro da broca influenciou significativamente nos resultados de resistência de união ao teste de push-out. O ligeiro aumento na espessura do filme de cimento promoveu um aumento nos valores de resistência, quando comparado com filmes de cimento muito finos ou muito espessos.

O envolvimento do estresse oxidativo e nitrosativo em modelo de doença pulmonar obstrutiva crônica (DPOC) induzido por elastase

Esse estudo buscou investigar o papel do estresse oxidativo e nitrosativo no enfisema pulmonar induzido por elastase. Foram utilizados camundongos machos C57BL/6 submetidos a dois modelos de indução do enfisema por elastase pancreática suína (PPE): intratraqueal (i.t.) e intranasal (i.n.). No modelo intratraqueal a PPE foi instilada nas doses de 0,05 U ou 0,5 U/camundongo para avaliação temporal do enfisema 7, 14 e 21 dias após instilação de PPE. Em outra etapa, o papel da iNOS foi avaliado através da sua inibição farmacológica por aminoguanidina (AMG) 1% na água de beber ou pela sua exclusão genética em camundongos deficientes em iNOS que tiveram o enfisema induzido por 0,5 U PPE i.t. após 21 dias. No modelo intranasal a dose de PPE foi 3 U/camundongo para avaliação temporal do enfisema (1, 7, 14 e 21 dias após PPE). O papel do estresse oxidativo e nitrosativo foi avaliado com diferentes tratamentos antioxidantes na água de beber: tempol, apocinina+alopurinol, n-acetilcisteína, vitamina C+E, e aminoguanidina durante os 21 dias de indução do enfisema. Os grupos controles foram submetidos à instilação de salina. Lavado broncoalveolar, imunoensaios, análises bioquímicas de estresse oxidativo e ensaios morfométricos foram realizados nos pulmões dos animais. O enfisema foi histologicamente alcançado em 21 dias após 0,5 U PPE i.t., evidenciado pelo aumento do diâmetro alveolar médio Lm e da densidade de volume dos espaços alveolares - Vvair em comparação ao grupo controle. TNF-α foi aumentado em 7 e 14 dias após 0,5 U PPE comparados ao controle, concomitante com a redução de IL-10 nos mesmos períodos, comparados ao controle. O estresse oxidativo foi observado na fase inicial do enfisema, com aumento dos níveis de nitrito, TBARS e superóxido dismutase no grupo 7 dias após 0,5 U PPE (i.t.) quando comparados ao controle ao passo que no modelo intranasal as alterações típicas do estresse foram vistas no grupo 1 dia após 3 U de PPE. Atividade da glutationa peroxidase foi aumentada em todos os grupos PPE (i.t.). A exposição à 0,5 U PPE induziu o aumento da iNOS, eNOS e nitrotirosina, sendo revertido no grupo PPE+AMG. Os animais tratados com AMG 1% e os deficientes em iNOS tiveram o enfisema atenuado histologicamente, mantendo o Lm e o Vvair semelhantes ao grupo controle. Os grupos tratados com n-acetilcisteína e aminoguanidina no modelo i.n. tiveram redução do Lm quando comparados ao grupo PPE. Esses resultados sugerem que as vias de estresse oxidativo e nitrosativo são disparadas pela produção de óxido nítrico via iNOS no enfisema pulmonar. A modulação da iNOS parece uma estratégia promissora no estabelecimento do enfisema pulmonar

Efeito do uso de salbutamol nas propriedades mecânicas do sistema respiratório de indivíduos saudáveis, tabagistas e portadores de doença pulmonar obstrutiva crônica

A doença pulmonar obstrução crônica (DPOC) é caracterizada pela limitação de fluxo parcialmente reversível, classificada por níveis de obstrução pós-broncodilatador. Há várias evidências de que o FEV1 sozinho não é capaz de mostrar a broncodilatação de pacientes com DPOC, mesmo naqueles que apresentam melhora clínica. A técnica de oscilações forçadas (TOF) tem mostrado alta sensibilidade na detecção precoce de alterações mecânicas na DPOC, contudo o efeito broncodilatador na impedância respiratória de pacientes com DPOC ainda não está esclarecido. Objetiva avaliar a utilidade da TOF nos diferentes estágios de obstrução das vias aéreas; (2) avaliar a resposta da impedância respiratória ao salbutamol em indivíduos saudáveis ao exame espirométrico e pacientes com DPOC em diferentes graus de gravidade. Foram avaliados 25 indivíduos saudáveis sem história de tabagismo, 24 tabagistas e 151 pacientes com DPOC classificados em graus I, II, III e IV. Todos os sujeitos foram avaliados pela TOF seguida da espirometria, antes e após o uso do salbutamol spray. As curvas de resistência e reatância demonstraram alteração em todos os estágios de obstrução das vias aéreas após o uso do salbutamol. O grupo de risco apresentou alterações mecânicas semelhantes ao grupo leve (p=ns). Os parâmetros R0, Rm, Csr,din e Z4Hz apresentam desempenho diagnóstico adequado (AUC > 0,85) em todos os estágios de gravidade da doença. Todos os parâmetros de TOF e espirometria apresentaram diminuição após uso do salbutamol. Os indivíduos saudáveis apresentaram uma pequena diminuição comparada aos subgrupos de DPOC. A variação em termos absolutos da ΔZ4Hz e das derivadas da resistência, ΔR0, ΔRm, ΔS, apresentaram variação significativa (p<0,0001, p<0,003; p<0,04; p<0,0002, respectivamente) com o aumento da obstrução brônquica. Nas derivadas da reatância o ΔXm aumentou com a gravidade da doença (p<0,0002). Por outro lado, a ΔCrs,dyn não demonstrou diferença significativa com a gravidade da DPOC. Em termos percentuais os parâmetros da TOF apresentaram variação expressiva em ΔRm% (p<0,02), ΔS% (p<0,02) e ΔXm% (p<0,004) com o aumento da obstrução nas vias aéreas. Por outro lado, ΔR0%, ΔCrs,dyn% e ΔZ4Hz% não variaram entre os estágios da DPOC. A associação entre a broncodilatação nas vias aéreas e a impedância pulmonar foi fraca entre ΔXm vs ΔFVC (r=0,32, p<0,0001) e ΔZ4Hz% vs ΔFEV1% vs ΔFVC% (r=0.28, p<0,0005; r=0,29, p<0,0003, respectivamente). A TOF é útil na avaliação das alterações mecânicas nos diferentes níveis de obstrução das vias aéreas na DPOC. Demonstramos o benefício da medicação broncodilatadora, quantificando a melhora da ventilação através da TOF. A impedância respiratória diminui em todos os estágios da DPOC, o estágio leve melhorou tanto quanto o estágio muito grave. Isto sugere que a medida da impedância pulmonar não é dependente do volume como ocorre na espirometria e que a broncodilatação ocorre em todas as fases da progressão da DPOC.