NOx storage-reduction characteristics of Ba-based lean NOx trap catalysts subjected to simulated road aging

In order to study the effect of washcoat composition on lean NOx trap (LNT) aging characteristics, fully formulated monolithic LNT catalysts containing varying amounts of La-stabilized CeO2 (5 wt% La2O3) or CeO2-ZrO2 (Ce:Zr = 70:30) were subjected to accelerated aging on a bench reactor. Subsequent catalyst evaluation revealed that aging resulted in deterioration of the NOx storage, NOx release and NOx reduction functions, whereas the observation of lean phase NO2 slip for all of the aged catalysts indicated that LNT performance was not limited by the kinetics of NO oxidation. After aging, all of the catalysts showed increased selectivity to NH3 in the temperature range 250–450 °C. TEM, H2 chemisorption, XPS and elemental analysis data revealed two main changes which can explain the degradation in LNT performance. First, residual sulfur in the catalysts, present as BaSO4, decreased catalyst NOx storage capacity. Second, sintering of the precious metals in the washcoat was observed, which can be expected to decrease the rate of NOx reduction. Additionally, sintering is hypothesized to result in segregation of the precious metal and Ba phases, resulting in less efficient NOx spillover from Pt to Ba during NOx adsorption, as well as decreased rates of reductant spillover from Pt to Ba and reverse NOx spillover during catalyst regeneration. Spectacular improvement in LNT durability was observed for catalysts containing CeO2 or CeO2-ZrO2 relative to their non-ceria containing analog. This was attributed to (i) the ability of ceria to participate in NOx storage/reduction as a supplement to the main Ba NOx storage component; (ii) the fact that Pt and CeO2(-ZrO2) are not subject to phase segregation; and (iii) the ability of ceria to trap sulfur, resulting in decreased sulfur accumulation on the Ba component.

NOx storage and reduction over copper-based catalysts. Part 2: Ce0.8M0.2Oδ supports (M = Zr, La, Ce, Pr or Nd)

5% copper catalysts with Ce0.8M0.2Oδ supports (M = Zr, La, Ce, Pr or Nd) have been studied by rapid-scan operando DRIFTS for NOx Storage and Reduction (NSR) with high frequency (30 s) CO, H2 and 50%CO + 50%H2 micropulses. In the absence of reductant pulses, below 200–250 °C NOx was stored on the catalysts as nitrite and nitro groups, and above this temperature nitrates were the main species identified. The thermal stability of the NOx species stored on the catalysts depended on the acid/basic character of the dopant (M more acidic = NOx stored less stable ⇒ Zr4+ < none < Nd3+ < Pr3+ < La3+ ⇐ M more basic = NOx stored more stable). Catalysts regeneration was more efficient with H2 than with CO, and the CO + H2 mixture presented an intermediate behavior, but with smaller differences among the series of catalyst than observed using CO alone. N2 is the main NOx reduction product upon H2 regeneration. The highest NOx removal in NSR experiments performed at 400 °C with CO + H2 pulses was achieved with the catalyst with the most basic dopant (CuO/Ce0.8La0.2Oδ) while the poorest performing catalyst was that with the most acidic dopant (CuO/Ce0.8Zr0.2Oδ). The poor performance of CuO/Ce0.8Zr0.2Oδ in NSR experiments with CO pulses was attributed to its lower oxidation capacity compared to the other catalysts.

Sviluppi di catalizzatori per l'abbattimento di NOx in presenza di ossigeno

Il traffico veicolare è la principale fonte antropogenica di NOx, idrocarburi (HC) e CO e, dato che la sostituzione dei motori a combustione interna con sistemi alternativi appare ancora lontana nel tempo, lo sviluppo di sistemi in grado di limitare al massimo le emissioni di questi mezzi di trasporto riveste un’importanza fondamentale. Sfortunatamente non esiste un rapporto ottimale aria/combustibile che permetta di avere basse emissioni, mentre la massima potenza ottenibile dal motore corrisponde alle condizioni di elevata formazione di CO e HC. Gli attuali sistemi di abbattimento permettono il controllo delle emissioni da sorgenti mobili tramite una centralina che collega il sistema di iniezione del motore e la concentrazione di ossigeno del sistema catalitico (posto nella marmitta) in modo da controllare il rapporto aria/combustibile (Fig. 1). Le marmitte catalitiche per motori a benzina utilizzano catalizzatori “three way” a base di Pt/Rh supportati su ossidi (allumina, zirconia e ceria), che, dovendo operare con un rapporto quasi stechiometrico combustibile/comburente, comportano una minore efficienza del motore e consumi maggiori del 20-30% rispetto alla combustione in eccesso di ossigeno. Inoltre, questa tecnologia non può essere utilizzata nei motori diesel, che lavorano in eccesso di ossigeno ed utilizzano carburanti con un tenore di zolfo relativamente elevato. In questi ultimi anni è cresciuto l’interesse per il controllo delle emissioni di NOx da fonti veicolari, con particolare attenzione alla riduzione catalitica in presenza di un eccesso di ossigeno, cioè in condizioni di combustione magra. Uno sviluppo recente è rappresentato dai catalizzatori tipo “Toyota” che sono basati sul concetto di accumulo e riduzione (storage/reduction), nei quali l’NO viene ossidato ed accumulato sul catalizzatore come nitrato in condizioni di eccesso di ossigeno. Modificando poi per brevi periodi di tempo le condizioni di alimentazione da ossidanti (aria/combustibile > 14,7 p/p) a riducenti (aria/combustibile < 14,7 p/p) il nitrato immagazzinato viene ridotto a N2 e H2O. Questi catalizzatori sono però molto sensibili alla presenza di zolfo e non possono essere utilizzati con i carburanti diesel attualmente in commercio. Obiettivo di questo lavoro di tesi è stato quello di ottimizzare e migliorare la comprensione del meccanismo di reazione dei catalizzatori “storage-reduction” per l’abbattimento degli NOx nelle emissioni di autoveicoli in presenza di un eccesso di ossigeno. In particolare lo studio è stato focalizzato dapprima sulle proprietà del Pt, fase attiva nei processi di storage-reduction, in funzione del tipo di precursore e sulle proprietà e composizione della fase di accumulo (Ba, Mg ed una loro miscela equimolare) e del supporto (γ-Al2O3 o Mg(Al)O). Lo studio è stato inizialmente focalizzato sulle proprietà dei precursori del Pt, fase attiva nei processi di storage-reduction, sulla composizione della fase di accumulo (Ba, Mg ed una loro miscela equimolare) e del supporto (γ-Al2O3 o Mg(Al)O). E’ stata effettuata una dettagliata caratterizzazione chimico-fisica dei materiali preparati tramite analisi a raggi X (XRD), area superficiale, porosimetria, analisi di dispersione metallica, analisi in riduzione e/o ossidazione in programmata di temperatura (TPR-O), che ha permesso una migliore comprensione delle proprietà dei catalizzatori. Vista la complessità delle miscele gassose reali, sono state utilizzate, nelle prove catalitiche di laboratorio, alcune miscele più semplici, che tuttavia potessero rappresentare in maniera significativa le condizioni reali di esercizio. Il comportamento dei catalizzatori è stato studiato utilizzando differenti miscele sintetiche, con composizioni che permettessero di comprendere meglio il meccanismo. L’intervallo di temperatura in cui si è operato è compreso tra 200-450°C. Al fine di migliorare i catalizzatori, per aumentarne la resistenza alla disattivazione da zolfo, sono state effettuate prove alimentando in continuo SO2 per verificare la resistenza alla disattivazione in funzione della composizione del catalizzatore. I principali risultati conseguiti possono essere così riassunti: A. Caratteristiche Fisiche. Dall’analisi XRD si osserva che l’impregnazione con Pt(NH3)2(NO2)2 o con la sospensione nanoparticellare in DEG, non modifica le proprietà chimico-fisiche del supporto, con l’eccezione del campione con sospensione nanoparticellare impregnata su ossido misto per il quale si è osservata sia la segregazione del Pt, sia la presenza di composti carboniosi sulla superficie. Viceversa l’impregnazione con Ba porta ad una significativa diminuzione dell’area superficiale e della porosità. B. Caratteristiche Chimiche. L’analisi di dispersione metallica, tramite il chemiassorbimento di H2, mostra per i catalizzatori impregnati con Pt nanoparticellare, una bassa dispersione metallica e di conseguenza elevate dimensioni delle particelle di Pt. I campioni impregnati con Pt(NH3)2(NO2)2 presentano una migliore dispersione. Infine dalle analisi TPR-O si è osservato che: Maggiore è la dispersione del metallo nobile maggiore è la sua interazione con il supporto, L’aumento della temperatura di riduzione del PtOx è proporzionale alla quantità dei metalli alcalino terrosi, C. Precursore Metallo Nobile. Nelle prove di attività catalitica, con cicli ossidanti e riducenti continui in presenza ed in assenza di CO2, i catalizzatori con Pt nanoparticellare mostrano una minore attività catalitica, specie in presenza di un competitore come la CO2. Al contrario i catalizzatori ottenuti per impregnazione con la soluzione acquosa di Pt(NH3)2(NO2)2 presentano un’ottima attività catalitica, stabile nel tempo, e sono meno influenzabili dalla presenza di CO2. D. Resistenza all’avvelenamento da SO2. Il catalizzatore di riferimento, 17Ba1Pt/γAl2O3, mostra un effetto di avvelenamento con formazione di solfati più stabili che sul sistema Ba-Mg; difatti il campione non recupera i valori iniziali di attività se non dopo molti cicli di rigenerazione e temperature superiori ai 300°C. Per questi catalizzatori l’avvelenamento da SO2 sembra essere di tipo reversibile, anche se a temperature e condizioni più favorevoli per il 1.5Mg8.5Ba-1Pt/γAl2O3. E. Capacità di Accumulo e Rigenerabilità. Tramite questo tipo di prova è stato possibile ipotizzare e verificare il meccanismo della riduzione. I catalizzatori ottenuti per impregnazione con la soluzione acquosa di Pt(NH3)2(NO2)2 hanno mostrato un’elevata capacità di accumulo. Questa è maggiore per il campione bimetallico (Ba-Mg) a T < 300°C, mentre per il riferimento è maggiore per T > 300°C. Per ambedue i catalizzatori è evidente la formazione di ammoniaca, che potrebbe essere utilizzata come un indice che la riduzione dei nitrati accumulati è arrivata al termine e che il tempo ottimale per la riduzione è stato raggiunto o superato. Per evitare la formazione di NH3, sul catalizzatore di riferimento, è stata variata la concentrazione del riducente e la temperatura in modo da permettere alle specie adsorbite sulla superficie e nel bulk di poter raggiungere il Pt prima che l’ambiente diventi troppo riducente e quindi meno selettivo. La presenza di CO2 riduce fortemente la formazione di NH3; probabilmente perché la CO2, occupando i siti degli elementi alcalino-terrosi lontani dal Pt, impedisce ai nitriti/nitrati o all’H2 attivato di percorrere “elevate” distanze prima di reagire, aumentando così le possibilità di una riduzione più breve e più selettiva. F. Tempo di Riduzione. Si è migliorata la comprensione del ruolo svolto dalla concentrazione dell’agente riducente e dell’effetto della durata della fase riducente. Una durata troppo breve porta, nel lungo periodo, alla saturazione dei siti attivi, un eccesso alla formazione di NH3 Attraverso queste ultime prove è stato possibile formulare un meccanismo di reazione, in particolare della fase riducente. G. Meccanismo di Riduzione. La mobilità dei reagenti, nitriti/nitrati o H2 attivato è un elemento fondamentale nel meccanismo della riduzione. La vicinanza tra i siti di accumulo e quelli redox è determinante per il tipo di prodotti che si possono ottenere. La diminuzione della concentrazione del riducente o l’aumento della temperatura concede maggiore tempo o energia alle specie adsorbite sulla superficie o nel bulk per migrare e reagire prima che l’ambiente diventi troppo riducente e quindi meno selettivo.

Nitrogen Oxides Reduction Possibilities at Pulp Mill and Power Plant

Tutkimuksen tarkoituksena oli selvittää typenoksidien vähennysmahdollisuudet Stora Enson Varkauden tehtaiden sellutehtaalla ja voimalaitoksella. Tutkimuksessa käsiteltiin tehdasalueen suurimpia typenoksidien päästölähteitä: soodakattilaa, meesauunia, kuorikattilaa, öljykattilaa ja muovi-alumiinijakeen kaasutuslaitosta. Tutkimuksessa selvitettiin typenoksidipäästöjen syntymekanismit ja erilaisiin polttotekniikoihin soveltuvat typenoksidien vähennystekniikat. Varkauden tehtaiden typenoksidien vuosipäästö vuonna 2001 oli 836 tonnia. Kansallinen lainsäädäntö, kansainväliset sopimukset sekä paras käytettävissä oleva tekniikka (BAT) huomioiden selvitettiin kuhunkin kohteeseen parhaiten soveltuvat ratkaisut. Tutkimuksen perusteella laadittiin toimenpideohjelma, joka määrittelee suositeltavan toteutusjärjestyksen typenoksidien vähennystoimenpiteille. Toimenpideohjelman tärkeimpinä kriteereinä pidettiin vuonna 2004 tulevan uuden ympäristöluvan arvioituja luparajoja sekä toimenpiteiden kustannustehokkuutta. Toteutusjärjestyksessä ensimmäiseksi valittiin koeajojakson järjestäminen ajon optimoimiseksi kiertopetikattilalla ja toiseksi meesauunin ajon optimointi jatkuvatoimisen NOx-analysaattorin avulla. Seuraaviksi toimenpiteiksi ehdotettiin vertikaali-ilmajärjestelmän käyttöönottoa soodakattilalla sekä SNCR-järjestelmän asennusta kuorikattilalle. Saavutettava NOx-vähennys tulisi olemaan 10 – 45 % ja hinta 30 – 3573 EUR vähennettyä NOx-tonnia kohti. Tutkimuksen osana Ilmatieteen laitoksella teetetyn typenoksidien leviämisselvityksen mukaan Stora Enson tehtaiden NOx-päästöjen vaikutus Varkauden ilmanlaatuun on hyvin pieni. Suurin osa NOx-päästöistä aiheutuu liikenteestä.

Reduction of nitrogen oxide emissions in lime kiln

Different nitrogen oxide removal technologies for rotary lime kiln are studied in this thesis, the main focus being in commercial technologies. Post-combustion methods are investigated in more detail as potential possible NOx removal with combustion methods in rotary lime kiln is more limited or primary methods are already in use. However, secondary methods as NOx scrubber, SNCR or SCR technologies are not listed as the Best Available Technologies defined by European Union. BAT technologies for NOx removal in lime kiln are (1) Optimised combustion and combustion control, (2) Good mixing of fuel and air, (3) Low-NOx burner and (4) Fuel selection/low-N fuel. SNCR method is the most suitable technique for NOx removal in lime kiln when NOx removal from 50 % to 70 % is required in case primary methods are already in use or cannot be applied. In higher removal cases ammonia slip is an issue in SNCR. By using SCR better NOx reduction can be achieved but issues with catalyst materials are expected to arise because of the dust and sulphur dioxide which leads to catalyst poison formation in lower flue gas temperatures. NOx scrubbing has potential when simultaneous NOx and SO2 removal is required. The challenge is that NO cannot be scrubbed directly, but once it is oxidized to NO2 or further scrubbing can be performed as the solubility of NO2 is higher. Commercial installations have not been made regarding SNCR, SCR or NOx scrubbing regarding rotary lime kiln. For SNCR and SCR the closest references come from cement industry.

Adaptación de una central térmica de carbón a la Directiva de Emisiones Industriales

El proyecto que se presenta a continuación recoge la adaptación de una Central Térmica de carbón al cumplimiento de la DIRECTIVA 2010/75/UE DEL PARLAMENTO EUROPEO Y DEL CONSEJO de 24 de noviembre de 2010 sobre las emisiones industriales. La Central sobre la que se realiza el proyecto tiene un grupo térmico de carbón suscritico refrigerado por agua, con una potencia a plena carga de 350 MWe y de 190 MWe a mínimo técnico. Genera 1 090 t/h de vapor a 540 °C y 168 kg/cm2 funcionando a plena carga. Actualmente las emisiones de NOx son de 650 mg/m3, (condiciones normales, seco, 6 % O2). El objeto del proyecto es reducir estas emisiones a un valor máximo de 200 mg/m3 en las mismas condiciones. El proyecto analiza detalladamente las condiciones actuales de operación de la instalación en cuanto a combustible utilizado, horas de funcionamiento, condiciones climáticas y producción. Se analiza así mismo, todas las técnicas disponibles en mercado para la reducción del NOx, diferenciando entre medidas primarias (actúan sobre los efectos de formación) y secundarias (limpieza de gases). Las medidas primarias ya están implementadas en la central, por tanto, el proyecto plantea la reducción con medidas secundarias. De las medidas secundarias analizadas se ha seleccionado la instalación de un Reactor de Reducción Selectiva Catalítica (Reactor SCR). Tras un análisis de los diferentes reactores y catalizadores disponibles se ha seleccionado un reactor de configuración High-dust, una disposición de catalizador en 3 capas más 1, cuyos componentes están basados en óxidos metálicos (TiO2, V2O5, WO3) y estructura laminar. Se ha buscado la instalación del reactor para operar a una temperatura inferior a 450 °C. Como agente reductor se ha seleccionado NH3 a una dilución del 24,5 %. El proyecto recoge también el diseño de todo el sistema de almacenamiento, evaporación, dilución e inyección de amoniaco. El resultado del proyecto garantiza una concentración en los gases de salida por la chimenea inferior 180 mg/m3(n) de NOx. La reducción del NOx a los límites establecidos, tienen un coste por MWh neto generado para la central, trabajando 60 % a plena carga y 40 % a mínimo técnico y una amortización de 10 años, de 4,10 €/MWh. ABSTRACT The following project shows the compliance adjustment of a coal-fired power station to the 2010/75/EU Directive of the European Parliament and Council 24th November 2010 on industrial emissions. The project is based on a power station with a subcritical thermal coal unit, cooled with water, with a maximum power of 350 MWe and a technical minimum of 190 MWe. It produces 1 090 t/h of steam at 540 ° C and 168 kg/cm2 operating under full load. Currently, NOx emissions are 650 mg / m3 (normal conditions, dry, 6% O2). The project aims to reduce these emissions to a maximum value of 200 mg / m3 under the same conditions. The project analyses in detail the current operating conditions of the system in terms of fuel used, hours of operation, climatic conditions and production. In addition, it also analyses every available technique of NOx reduction on the market, distinguishing between primary (acting on the effects of formation) and secondary measures (gas cleaning). Primary measures are already implemented in the plant, thus proposing reduction with secondary measures. Among the secondary measures analyzed, it has been selected to install a Selective Catalytic Reduction Reactor (SCR Reactor). Having researched the different reactors and catalysts available, for the reactor has been selected High-dust configuration, an arrangement of catalyst in 3 layers plus 1, whose components are based on metal oxides (TiO2, V2O5, WO3) and laminar structure. The reactor has been sought facility to operate at a temperature below 450 ° C. NH3 diluted to 24,5 % has been selected as reducing agent. The project also includes the design of the entire storage system, evaporation, dilution and ammonia injection. The results of the project ensure a gas concentration in the lower chimney exit below 180 mg / m3(n) NOx. The reduction of NOx to the established limits has a cost per net MWh generated in the plant, working at 60% of full load and at 40% of technical minimum, with an amortization of 10 years, 4,10 € / MWh.

The Effect of Nutrient-Rich Effluents from Shrimp Farming on Mangrove Soil Carbon Storage and Geochemistry Under Semi-Arid Climate Conditions in Northern Brazil

A semi-arid mangrove estuary system in the northeast Brazilian coast (Ceará state) was selected for this study to (i) evaluate the impact of shrimp farm nutrient-rich wastewater effluents on the soil geochemistry and organic carbon (OC) storage and (ii) estimate the total amount of OC stored in mangrove soils (0–40 cm). Wastewater-affected mangrove forests were referred to as WAM and undisturbed areas as Non-WAM. Redox conditions and OC content were statistically correlated (P < 0.05) with seasonality and type of land use (WAM vs. Non-WAM). Eh values were from anoxic to oxic conditions in the wet season (from − 5 to 68 mV in WAM and from < 40 to > 400 mV in Non-WAM soils) and significantly higher (from 66 to 411 mV) in the dry season (P < 0.01). OC contents (0–40 cm soil depth) were significantly higher (P < 0.01) in the wet season than the dry season, and higher in Non-WAM soils than in WAM soils (values of 8.1 and 6.7 kg m− 2 in the wet and dry seasons, respectively, for Non-WAM, and values of 3.8 and 2.9 kg m− 2 in the wet and dry seasons, respectively, for WAM soils; P < 0.01). Iron partitioning was significantly dependent (P < 0.05) on type of land use, with a smaller degree of pyritization and lower Fe-pyrite presence in WAM soils compared to Non-WAM soils. Basal respiration of soil sediments was significantly influenced (P < 0.01) by type of land use with highest CO2 flux rates measured in the WAM soils (mean values of 0.20 mg CO2 h− 1–g− 1 C vs. 0.04 mg CO2 h− 1–g− 1 C). The OC storage reduction in WAM soils was potentially caused (i) by an increase in microbial activity induced by loading of nutrient-rich effluents and (ii) by an increase of strong electron acceptors [e.g., NO3−] that promote a decrease in pyrite concentration and hence a reduction in soil OC burial. The current estimated OC stored in mangrove soils (0–40 cm) in the state of Ceará is approximately 1 million t.

Síndrome de apneia hipopneia obstrutiva do sono e óxido nítrico : que relação ?

RESUMO: A síndrome de apneia hipopneia obstrutiva do sono (SAHOS), pela sua prevalência e consequências clínicas, nomeadamente as de natureza cardiovascular, é actualmente considerada um problema de saúde pública. A patogénese da doença cardiovascular na SAHOS não está ainda completamente estabelecida, mas parece ser multifactorial, envolvendo diversos mecanismos que incluem a hiperactividade do sistema nervoso simpático, a disfunção endotelial, a activação selectiva de vias inflamatórias, o stress oxidativo vascular e a disfunção metabólica. A terapêutica com CPAP diminui grandemente o risco de eventos cardiovasculares fatais e não fatais. O CPAP está inequivocamente indicado para o tratamento da SAHOS grave, no entanto, não é consensual a sua utilização nos doentes com SAHOS ligeira/moderada sem hipersonolência diurna associada. Tendo em conta este facto, é fundamental que as indicações terapêuticas do CPAP nestes doentes tenham uma relação custo-eficácia favorável. Assim, dado o posicionamento do estado da arte relativamente ao estudo da disfunção endotelial e da activação do sistema nervoso simpático estar centrada maioritariamente nos doentes com SAHOS grave, desenvolvemos este estudo com o objectivo de comparar os níveis plasmáticos de nitratos, os níveis de catecolaminas urinárias e os valores de pressão arterial nos doentes com SAHOS ligeira/moderada e grave e avaliar a resposta destes parâmetros ao tratamento com CPAP durante um mês. Realizámos um estudo prospectivo, incidindo sobre uma população de 67 doentes do sexo masculino com o diagnóstico de SAHOS (36 com SAHOS ligeira/moderada e 31com SAHOS grave). O protocolo consistia em 3 visitas: antes da terapêutica com CPAP (visita 1), uma semana após CPAP (visita 2) e um mês após CPAP (visita 3). Nas visitas 1 e 3, eram submetidos a três colheitas de sangue às 11 pm, 4 am e 7 am para doseamento dos nitratos plasmáticos e na visita 2 apenas às 7 am. Nas visitas 1 e 3 era também efectuada uma colheita de urina de 24 horas para o doseamento das catecolaminas urinárias e eram submetidos a uma monitorização ambulatória da pressão arterial de 24 horas (MAPA). Foi ainda estudado um grupo controlo de 30 indivíduos do sexo masculino não fumadores sem patologia conhecida e sem evidência de SAHOS. Antes da terapêutica com CPAP, verificou-se uma diminuição significativa dos níveis de nitratos ao longo da noite quer nos doentes com SAHOS ligeira/moderada, quer nos doentes com SAHOS grave. No entanto, esta redução diferia nos 2 grupos de doentes, sendo significativamente superior nos doentes com SAHOS grave (27,6±20,1% vs 16,5±18,5%; p<0,05). Após um mês de tratamento com CPAP, verificou-se um aumento significativo dos valores de nitratos plasmáticos apenas nos doentes com SAHOS grave, mantendo-se os níveis de nitratos elevados ao longo da noite, já não existindo o decréscimo desses valores ao longo da mesma. Os valores de noradrenalina basais eram significativamente superiores nos doentes com SAHOS grave comparativamente com os doentes com SAHOS ligeira/moderada (73,9±30,1μg/24h vs 48,5±19,91μg/24h; p<0,05). Após um mês de terapêutica com CPAP, apenas se verificou uma redução significativa nos valores da noradrenalina nos doentes com SAHOS grave (73,9±30,1μg/24h para 55,4±21,8 μg/24h; p<0,05). Os doentes com SAHOS grave apresentaram valores de pressão arterial mais elevados do que os doentes com SAHOS ligeira/moderada, nomeadamente no que diz respeito aos valores de pressão arterial média, sistólica média de 24 horas, diurna e nocturna e diastólica média de 24 horas, diurna e nocturna. Após um mês de terapêutica com CPAP, verificou-se uma redução significativa dos valores tensionais apenas nos doentescom SAHOS grave, para a pressão média (-2,32+5,0; p=0,005), para a sistólica média de 24 horas (-4,0+7,9mmHg; p=0,009), para a pressão sistólica diurna (-4,3+8,8mmHg; p=0,01), para a pressão sistólica nocturna (-5,1+9,0mmHg; p=0,005), para a pressão diastólica média de 24 horas (-2,7+5,8mmHg; p=0,016), para a pressão diastólica diurna (-3,2+6,3mmHg; p=0,009) e para a pressão diastólica nocturna (-2,5+7,0mmHg; p=0,04). Os níveis tensionais dos doentes com SAHOS grave após CPAP atingiram valores semelhantes aos dos doentes com SAHOS ligeira/moderada, relativamente a todos os parâmetros avaliados no MAPA. Este estudo demonstrou que antes do tratamento com CPAP, existe uma redução dos níveis de nitratos ao longo da noite não só nos doentes com SAHOS grave mas também nos doentes com SAHOS ligeira/moderada. No entanto, a terapêutica com CPAP leva a um aumento significativo dos valores de nitratos plasmáticos apenas nos doentes com SAHOS grave, mantendo-se os níveis de nitratos elevados ao longo da noite, já não existindo o decréscimo desses valores ao longo da mesma. O tratamento com CPAP durante um mês, apenas reduz os níveis de noradrenalina urinária e os valores de pressão arterial nos doentes com SAHOS grave.------------ ABSTRACT: In severe obstructive sleep apnea (OSA) reduced circulating nitrate, increased levels of urinary norepinephrine (U-NE) and changes in systemic blood pressure (BP) have been described and are reverted by Continuous Positive Airway Pressure (CPAP). However, the consequences of mild/moderate OSA on these parameters and the CPAP effect upon them are not well known. We aimed to: 1) compare the levels of plasma nitrate (NOx) and U-NE of mild/moderate and severe male OSA patients 2) compare BP in these patient groups; and 3) determine whether CPAP improves sympathetic dysfunction, nitrate deficiency and BP in these patients. This prospective study was carried out in 67 consecutive OSA patients (36 mild/moderate and 31 severe patients) and NOx (11 pm, 4 am, 7 am), 24-h U-NE and ambulatory blood pressure monitoring were obtained before and after 4 weeks of CPAP. Baseline: NOx levels showed a significant decrease (p<0.001) during the night in both groups of patients. The U-NE and BP were significantly higher in the severe group. Post CPAP: After one month of CPAP, there was a significant increase of NOx, a reduction of U-NE and BP only in severe patients. This study shows that in contrast to severe OSA patients, those with mild/moderate OSA, which have lower values of BP and U-NE at baseline, do not benefit from a 4 weeks CPAP treatment as measured by plasma nitrate, 24-h U-NE levels and BP.

Metsäteollisuusintegraatin ympäristövaikutukset

Diplomityön tavoitteena oli selvittää Stora Enso Oyj Imatran tehtaiden ympäristövaikutuksia. Tarkastelu toteutettiin kahdella lähestymistavalla. Elinkaariarvioinnilla tarkasteltiin Imatran tehtaiden kartonki- ja paperituotannon elinkaaren aikaisia ympäristövaikutuksia. Elinkaariarvioinnin lisäksi tarkasteltiin Imatran tehtaiden aiheuttamia paikallisia ympäristövaikutuksia. Paikallisten vaikutusten arviointi perustui ensisijaisesti toiminnasta aiheutuvien päästöjen ja lainsäädännöllisesti ympäristön tilalle asetettujen vaatimusten ja tavoitetasojen vertailuun. Lisäksi työssä tehtiin arvio Imatran tehtaiden typenoksidipäästöjen vähentämisestä aiheutuvista kustannuksista. Työn teoriaosiossa tarkasteltiin elinkaariarvioinnin pääperiaatteita, paikallisten ympäristövaikutusten arviointiperusteita sekä yleisellä tasolla typenoksidipäästöjen vähentämistekniikoita. Elinkaariarvioinnissa ympäristövaikutuksiltaan merkittävimmiksi elinkaarivaiheiksi osoit-tautuivat paperin ja kartongin tuotantovaihe sekä kuljetukset. Paikallisten vaikutusten arvioinnissa todettiin tehtaiden jätevesien aiheuttavan lievää rehevöitymistä lähivaikutusalueella. Terveys- ja viihtyvyysvaikutuksista melu ja haju todettiin merkittävimmiksi. Työssä tarkastellut typenoksidipäästöjen vähentämismenetelmät osoittautuivat kalliiksi ja investoinneilla saavutetut ympäristöhyödyt vähäisiksi.

The effect of environmentally differentiated port fees to shipping companies’ environmental investments

The pressure has grown to develop cost-effective emission reduction strategies in the Baltic Sea. The forthcoming stringent regulations of the International Maritime Organization for reducing harmful emissions of shipping in the Baltic Sea are causing increasing expenses for the operators. A market-based attitude towards pricing of economic incentives could be seen as a new approach for a successful application for the additional emission reduction of nitrogen oxides (NOx). In this study the aim is to understand the phenomenon of environmentally differentiated port fees and its effects on shipping companies’ emission reduction investments. The goal is to examine empirically the real-life effects of the possible environmental differentiated port fee system and the effect of environmentally differentiated port fees on NOx reduction investments in the Baltic Sea. The research approach of this study is nomothetical. In this study research questions are answered by analyzing the broad database of the Baltic Sea fleet. Also the framework of theory is confirmed and plays an important role in analyzing the research problem. Existing investment costs of NOx emission reduction technology to ship owners are estimated and compared to investment costs with granted discounts added to the cash flows. The statistical analysis in this study is descriptive. The major statistic examination of this study is the calculation of the net present values of investments with different port fee scenarios. This is done to investigate if the NOx technology investments could be economically reasonable. Based on calculations it is clear that the effect of environmentally differentiated port fees is not adequate to compensate the total investment costs for NOx reduction. If the investment decision is made only with profitability considerations, sources will prefer to emission abatement as long as incomes from the given subsidy exceeds their abatement costs. Despite of the results, evidence was found that shipping companies are nevertheless willing to invest on voluntary emission abatement technology. In that case, investment decision could be made with criteria of, for example, sustainable strategy or brand image. Combined fairway and port fee system or governmental regulations and recommendation could also function as additional incentives to compensate the investment costs. Also, the results imply that the use of NPV is not necessarily the best method to evaluate environmental investments. If the calculations would be done with more environmental methods the results would probably be different.

Using biomass-based fuels including pyrolysis liquids for power and CHP production

The use of biomass-derived liquids (in short: bioliquids) instead of solid biomass can help overcome some of the barriers hindering a wider use of biomass in smaller-scale CHP systems. Relevant bioliquids included biodiesel, vegetable oils as well straight and upgraded pyrolysis oil. In this joint EU-Russian research project Bioliquids-CHP prime movers (engines and turbines) will be developed and modified so that these can run efficiently on bioliquids. At the same time, bioliquids will be upgraded and blended in order to facilitate their use in prime movers. Preliminary results with regard to bioliquid selection, production, and characterisation; the selection and modification of a micro gas turbine; and the development of engines and components are discussed. The research also covers NOx emission reduction and control and an assessment of the benefits and economics of bioliquids-based CHP systems in EU and Russian markets.

Development of a Predictive Control Function for a Plug-in Hybrid Electric Vehicle with Electrically-heated Catalyst

This master thesis work is focused on the development of a predictive EHC control function for a diesel plug-in hybrid electric vehicle equipped with a EURO 7 compliant exhaust aftertreatment system (EATS), with the purpose of showing the advantages provided by the implementation of a predictive control strategy with respect to a rule-based one. A preliminary step will be the definition of an accurate powertrain and EATS physical model, starting from already existing and validated applications. Then, a rule-based control strategy managing the torque split between the electric motor (EM) and the internal combustion engine (ICE) will be developed and calibrated, with the main target of limiting tailpipe NOx emission by taking into account EM and ICE operating conditions together with EATS conversion efficiency. The information available from vehicle connectivity will be used to reconstruct the future driving scenario, also referred to as electronic horizon (eHorizon), and in particular to predict ICE first start. Based on this knowledge, an EATS pre-heating phase can be planned to avoid low pollutant conversion efficiencies, thus preventing high NOx emission due to engine cold start. Consequently, the final NOx emission over the complete driving cycle will be strongly reduced, allowing to comply with the limits potentially set by the incoming EURO 7 regulation. Moreover, given the same NOx emission target, the gain achieved thanks to the implementation of an EHC predictive control function will allow to consider a simplified EATS layout, thus reducing the related manufacturing cost. The promising results achieved in terms of NOx emission reduction show the effectiveness of the application of a predictive control strategy focused on EATS thermal management and highlight the potential of a complete integration and parallel development of involved vehicle physical systems, control software and connectivity data management.

Selective catalytic reduction of nitrogen oxides with ammonia in forced unsteady state reactors - Case based reasoning and mathematical model simulation reasoning

The application of forced unsteady-state reactors in case of selective catalytic reduction of nitrogen oxides (NOx) with ammonia (NH3) is sustained by the fact that favorable temperature and composition distributions which cannot be achieved in any steady-state regime can be obtained by means of unsteady-state operations. In a normal way of operation the low exothermicity of the selective catalytic reduction (SCR) reaction (usually carried out in the range of 280-350°C) is not enough to maintain by itself the chemical reaction. A normal mode of operation usually requires supply of supplementary heat increasing in this way the overall process operation cost. Through forced unsteady-state operation, the main advantage that can be obtained when exothermic reactions take place is the possibility of trapping, beside the ammonia, the moving heat wave inside the catalytic bed. The unsteady state-operation enables the exploitation of the thermal storage capacity of the catalyticbed. The catalytic bed acts as a regenerative heat exchanger allowing auto-thermal behaviour when the adiabatic temperature rise is low. Finding the optimum reactor configuration, employing the most suitable operation model and identifying the reactor behavior are highly important steps in order to configure a proper device for industrial applications. The Reverse Flow Reactor (RFR) - a forced unsteady state reactor - corresponds to the above mentioned characteristics and may be employed as an efficient device for the treatment of dilute pollutant mixtures. As a main disadvantage, beside its advantages, the RFR presents the 'wash out' phenomena. This phenomenon represents emissions of unconverted reactants at every switch of the flow direction. As a consequence our attention was focused on finding an alternative reactor configuration for RFR which is not affected by the incontrollable emissions of unconverted reactants. In this respect the Reactor Network (RN) was investigated. Its configuration consists of several reactors connected in a closed sequence, simulating a moving bed by changing the reactants feeding position. In the RN the flow direction is maintained in the same way ensuring uniformcatalyst exploitation and in the same time the 'wash out' phenomena is annulated. The simulated moving bed (SMB) can operate in transient mode giving practically constant exit concentration and high conversion levels. The main advantage of the reactor network operation is emphasizedby the possibility to obtain auto-thermal behavior with nearly uniformcatalyst utilization. However, the reactor network presents only a small range of switching times which allow to reach and to maintain an ignited state. Even so a proper study of the complex behavior of the RN may give the necessary information to overcome all the difficulties that can appear in the RN operation. The unsteady-state reactors complexity arises from the fact that these reactor types are characterized by short contact times and complex interaction between heat and mass transportphenomena. Such complex interactions can give rise to a remarkable complex dynamic behavior characterized by a set of spatial-temporal patterns, chaotic changes in concentration and traveling waves of heat or chemical reactivity. The main efforts of the current research studies concern the improvement of contact modalities between reactants, the possibility of thermal wave storage inside the reactor and the improvement of the kinetic activity of the catalyst used. Paying attention to the above mentioned aspects is important when higher activity even at low feeding temperatures and low emissions of unconverted reactants are the main operation concerns. Also, the prediction of the reactor pseudo or steady-state performance (regarding the conversion, selectivity and thermal behavior) and the dynamicreactor response during exploitation are important aspects in finding the optimal control strategy for the forced unsteady state catalytic tubular reactors. The design of an adapted reactor requires knowledge about the influence of its operating conditions on the overall process performance and a precise evaluation of the operating parameters rage for which a sustained dynamic behavior is obtained. An apriori estimation of the system parameters result in diminution of the computational efforts. Usually the convergence of unsteady state reactor systems requires integration over hundreds of cycles depending on the initial guess of the parameter values. The investigation of various operation models and thermal transfer strategies give reliable means to obtain recuperative and regenerative devices which are capable to maintain an auto-thermal behavior in case of low exothermic reactions. In the present research work a gradual analysis of the SCR of NOx with ammonia process in forced unsteady-state reactors was realized. The investigation covers the presentationof the general problematic related to the effect of noxious emissions in the environment, the analysis of the suitable catalysts types for the process, the mathematical analysis approach for modeling and finding the system solutions and the experimental investigation of the device found to be more suitable for the present process. In order to gain information about the forced unsteady state reactor design, operation, important system parameters and their values, mathematical description, mathematicalmethod for solving systems of partial differential equations and other specific aspects, in a fast and easy way, and a case based reasoning (CBR) approach has been used. This approach, using the experience of past similarproblems and their adapted solutions, may provide a method for gaining informations and solutions for new problems related to the forced unsteady state reactors technology. As a consequence a CBR system was implemented and a corresponding tool was developed. Further on, grooving up the hypothesis of isothermal operation, the investigation by means of numerical simulation of the feasibility of the SCR of NOx with ammonia in the RFRand in the RN with variable feeding position was realized. The hypothesis of non-isothermal operation was taken into account because in our opinion ifa commercial catalyst is considered, is not possible to modify the chemical activity and its adsorptive capacity to improve the operation butis possible to change the operation regime. In order to identify the most suitable device for the unsteady state reduction of NOx with ammonia, considering the perspective of recuperative and regenerative devices, a comparative analysis of the above mentioned two devices performance was realized. The assumption of isothermal conditions in the beginningof the forced unsteadystate investigation allowed the simplification of the analysis enabling to focus on the impact of the conditions and mode of operation on the dynamic features caused by the trapping of one reactant in the reactor, without considering the impact of thermal effect on overall reactor performance. The non-isothermal system approach has been investigated in order to point out the important influence of the thermal effect on overall reactor performance, studying the possibility of RFR and RN utilization as recuperative and regenerative devices and the possibility of achieving a sustained auto-thermal behavior in case of lowexothermic reaction of SCR of NOx with ammonia and low temperature gasfeeding. Beside the influence of the thermal effect, the influence of the principal operating parameters, as switching time, inlet flow rate and initial catalyst temperature have been stressed. This analysis is important not only because it allows a comparison between the two devices and optimisation of the operation, but also the switching time is the main operating parameter. An appropriate choice of this parameter enables the fulfilment of the process constraints. The level of the conversions achieved, the more uniform temperature profiles, the uniformity ofcatalyst exploitation and the much simpler mode of operation imposed the RN as a much more suitable device for SCR of NOx with ammonia, in usual operation and also in the perspective of control strategy implementation. Theoretical simplified models have also been proposed in order to describe the forced unsteady state reactors performance and to estimate their internal temperature and concentration profiles. The general idea was to extend the study of catalytic reactor dynamics taking into account the perspectives that haven't been analyzed yet. The experimental investigation ofRN revealed a good agreement between the data obtained by model simulation and the ones obtained experimentally.

The real-time optimisation of DNO owned storage devices on the LV network for peak reduction

Energy storage is a potential alternative to conventional network reinforcementof the low voltage (LV) distribution network to ensure the grid’s infrastructure remainswithin its operating constraints. This paper presents a study on the control of such storagedevices, owned by distribution network operators. A deterministic model predictive control (MPC) controller and a stochastic receding horizon controller (SRHC) are presented, wherethe objective is to achieve the greatest peak reduction in demand, for a given storagedevice specification, taking into account the high level of uncertainty in the prediction of LV demand. The algorithms presented in this paper are compared to a standard set-pointcontroller and bench marked against a control algorithm with a perfect forecast. A specificcase study, using storage on the LV network, is presented, and the results of each algorithmare compared. A comprehensive analysis is then carried out simulating a large number of LV networks of varying numbers of households. The results show that the performance of each algorithm is dependent on the number of aggregated households. However, on a typical aggregation, the novel SRHC algorithm presented in this paper is shown to outperform each of the comparable storage control techniques.