The microstructure of polyolefins determines their macroscopic properties. Consequently, it is essential to predict how polymerization conditions will affect polyolefin microstructure. The most important microstructural distributions of ethylene/alfa-olefin copolymers made with coordination catalysts are their molecular weight (MWD), chemical composition (CCD), and comonomer sequence length (CSLD). Several mathematical models have been developed to predict these microstructural distributions; reliable techniques to estimate parameters for these models, however, are still poorly developed, especially for catalysts that have multiple site types, such as heterogeneous Ziegler-Natta complexes. Most commercial polyolefins are made with heterogeneous Ziegler-Natta catalysts, which make polyolefins with broad MWD, CCD, and CSLD. This behavior is attributed to the presence of several active site types, leading to a final product that can be seen as a blend of polymers made on the different catalyst site types. The main objective of this project is to develop a methodology to estimate the most important parameters needed to describe the microstructure of ethylene/alfa-olefin copolymers made with these multiple site-type catalysts. To accomplish this objective, we developed the Integrated Deconvolution Estimation Model (IDEM). IDEM estimates ethylene/alf-olefin reactivity ratios for each site type in two-steps. In the first step, the copolymer MWD, measured by high-temperature gel permeation chromatography, is deconvoluted into several Flory’s most probable distributions to determine the number of site types and the weight fractions of copolymer made on each of them. In the second estimation step, the model uses the MWD deconvolution information to fit the copolymer triad distributions measured by 13C NMR and estimate the reactivity ratios per site type. This is the first time that MWD and triad distribution information is integrated to estimate the reactivity ratio per site type of multiple site-type catalysts used to make ethylene/alfa-olefin copolymers. IDEM was applied to two sets of ethylene-co-1-butene copolymers made with a commercial Ziegler-Natta catalyst, covering a wide range of 1-butene fractions. In the first set of samples (EBH), hydrogen was used as a chain transfer agent, whereas it was absent in the second set (EB). Comparison of the reactivity ratio estimates for the sets of samples permitted the quantification of the hydrogen effect on the reactivity ratios of the different site types present in the Ziegler-Natta catalyst used in this thesis. Since 13C NMR it is an essential analytical step in IDEM, triad distributions for the EB and EBH copolymers were measured in two different laboratories (Department of Chemistry at the University of Waterloo, and Dow Chemical Research Center at Freeport, Texas). IDEM was applied to both set of triad measurements to find out the effect of interlaboratory 13C NMR analysis on reactivity ratio estimation.

The microstructure of polyolefins determines their macroscopic properties. Consequently, it is essential to predict how polymerization conditions will affect polyolefin microstructure. The most important microstructural distributions of ethylene/alfa-olefin copolymers made with coordination catalysts are their molecular weight (MWD), chemical composition (CCD), and comonomer sequence length (CSLD). Several mathematical models have been developed to predict these microstructural distributions; reliable techniques to estimate parameters for these models, however, are still poorly developed, especially for catalysts that have multiple site types, such as heterogeneous Ziegler-Natta complexes. Most commercial polyolefins are made with heterogeneous Ziegler-Natta catalysts, which make polyolefins with broad MWD, CCD, and CSLD. This behavior is attributed to the presence of several active site types, leading to a final product that can be seen as a blend of polymers made on the different catalyst site types. The main objective of this project is to develop a methodology to estimate the most important parameters needed to describe the microstructure of ethylene/alfa-olefin copolymers made with these multiple site-type catalysts. To accomplish this objective, we developed the Integrated Deconvolution Estimation Model (IDEM). IDEM estimates ethylene/alf-olefin reactivity ratios for each site type in two-steps. In the first step, the copolymer MWD, measured by high-temperature gel permeation chromatography, is deconvoluted into several Flory’s most probable distributions to determine the number of site types and the weight fractions of copolymer made on each of them. In the second estimation step, the model uses the MWD deconvolution information to fit the copolymer triad distributions measured by 13C NMR and estimate the reactivity ratios per site type. This is the first time that MWD and triad distribution information is integrated to estimate the reactivity ratio per site type of multiple site-type catalysts used to make ethylene/alfa-olefin copolymers. IDEM was applied to two sets of ethylene-co-1-butene copolymers made with a commercial Ziegler-Natta catalyst, covering a wide range of 1-butene fractions. In the first set of samples (EBH), hydrogen was used as a chain transfer agent, whereas it was absent in the second set (EB). Comparison of the reactivity ratio estimates for the sets of samples permitted the quantification of the hydrogen effect on the reactivity ratios of the different site types present in the Ziegler-Natta catalyst used in this thesis. Since 13C NMR it is an essential analytical step in IDEM, triad distributions for the EB and EBH copolymers were measured in two different laboratories (Department of Chemistry at the University of Waterloo, and Dow Chemical Research Center at Freeport, Texas). IDEM was applied to both set of triad measurements to find out the effect of interlaboratory 13C NMR analysis on reactivity ratio estimation.

Doctor of Philosophy / Department of Grain Science and Industry / Finlay I. MacRitchie / Novel genetic materials were used to deduce gluten protein composition-functionality relationships. The Pegaso bread wheat near-isogenic lines (NILs) included addition, variation and/or deletion of major loci coding for HMW-GS, LMW-GS and gliadins. The waxy wheat lines (Svevo and N11 set) included wild, partial and complete waxy lines. Triticale translocations include 1R.1D and 1A.1D lines (GDS7, Trim, Rhino and Rigel sets) with HMW-GS 5+10 and 2+12. The main goal of the study was to establish the usefulness of NILs as appropriate materials to investigate the structure-function relationships of wheat proteins and to evaluate the performance of unique triticale translocations and waxy wheat lines. Effect of genetic variation on phytochemical (phenolic acid and policosanol) contents was also studied. Innovative methods like MALLS, Lab-on-a-chip and micro (10 g) baking were utilized along with traditional analytical methods. Results confirmed the potential of using NILs in understanding the effects of certain proteins coded at specific loci that might often be targeted in breeding programs. Removal of expected chain terminators at Gli-1/Gli-2 loci causes a shift in MWD to higher values, reflected in higher UPP and dough strength. Lines with HMW-GS 5+10 were clearly separated from 2+12 lines in terms of dough strength and UPP. The present study obtained evidence that modified ω-gliadins acts as chain terminators and cause reduction of protein polymer size and thus shifts in MWD. Marked differences in terms of milling characteristics, protein composition and ultimately in end-use functionality were observed with various waxy wheat null lines. Loaf volumes with waxy wheat flour alone were higher than a 50% blend with commercial wheat; however, breads were unacceptable to consumers in all aspects. Poor milling quality, very low mixing times with low bread loaf volumes were typical of all the triticales studied. However, translocation of the HMW-GS from wheat chromosome 1D increased dough strength, particularly the HMW-GS 5+10. Among the phytochemicals studied, double nulls at Gli-1 loci of Pegaso NILs had the highest total policosanols and total phenolic acid contents.Slight variation to wheat phenolic acid composition and contents were observed with waxy wheat and triticale lines.

A distribuição de pesos moleculares (DPM) de um polímero afeta as propriedades mecânicas, térmicas e reológicas do material. Além disso, a análise em tempo real de uma reação de polimerização é uma tarefa complicada e, consequentemente, os procedimentos de controle devem ser baseados em valores gerados pelos modelos. Por isso, é extremamente importante ter dados confiáveis sobre distribuições de pesos moleculares, melhorar a eficiência dos métodos existentes e desenvolver novos métodos capazes de prever as heterogeneidades das reações de polimerização. Experimentalmente, a DPM pode ser obtida usando técnicas como a cromatografia de permeação em gel. Para predizer a DPM, vários métodos foram desenvolvidos nas ultimas décadas. Um dos principais é o dos momentos estatísticos, baseado em conceitos puramente estatísticos, que não conseguem descrever completamente a DPM. Além disso, as aproximações com método de Galerkin usam polinômios ortogonais - no caso especifico polinômios de Laguerre - cujos coeficientes são calculados empregando os momentos estatísticos e a distribuição é gerada resolvendo um número de equações definido pelo usuário, relacionado à precisão desejada. Enfim, o método das funções geradoras de probabilidades foi utilizado para prever as DPMs, porém necessitando uma inversão da transformada de Laplace, que introduz problemas numéricos nem sempre possíveis de serem resolvidos. No presente trabalho, o sistema rigoroso de equações diferenciais ordinárias foi resolvido, com objetivo de reduzir as imprecisões e as limitações introduzidas pelas aproximações. Obter diretamente a DPM completa requer a resolução de um sistema contendo cerca de 2Nmax até 3Nmax equações diferenciais ordinárias rígidas, tarefa que há alguns anos era inviável devido a limitações relacionadas à capacidade de cálculo. Foi modelada a DPM para uma reação de polimerização radicalar livre de estireno e de metacrilato de metila. Um interesse especial foi dado à taxa de terminação que é, no momento, um dos temas mais investigados em polimerização por radicais livres. Os resultados das simulações foram comparados com dados experimentais tirados de reatores convencionais e, subsequentemente, com dados experimentais provenientes de um millireactor não convencional. / It is well known that the molecular weight distribution (MWD) of a synthetic polymer affects its mechanical, thermal and rheological properties. Furthermore, the on-line analysis for polymerization reaction is a difficult task and, consequently, the control procedures must rely on values given by models. As such, it is extremely important to have reliable data on the MWD, improve the efficiency of existing methods and develop new ones to predict the heterogeneities of polymerization reactions. Experimentally, the MWD can be obtained using techniques such as Gel Permeation Chromatography (GPC). To predict the MWD, many methods have been developed over the last decades. One of the main methods is the statistical moment treatment, which is based on a pure statistical concept and do not describe the whole MWD. Moreover, Galerkin approximation uses orthogonal polynomials -in general Laguerre polynomials- whose coefficients are calculated exploiting the statistical moment definition and the distribution is generated by solving a user-defined number of equations based on the desired precision. Finally, probability-generating functions that have been used to predict MWDs require Laplace transforms inversions, introducing numerical issues that must be bypassed and are not always solvable. It has been decided to base the approach without adopting any of these methods but directly solving the rigorous ordinary differential equation (ODE) system in order to reduce the inaccuracies and the limitations introduced by approximations. The direct obtention of the MWD requires the resolution of a system containing approximately 2Nmax up to 3Nmax stiff ODE equations that, a few years ago, was unfeasible due computational time limitations. The MWDs for a free radical styrene polymerization system and a methyl methacrylate system have been modeled. A special focus was given to the termination rate constant, which is, at the present, one of the most investigated topics in free radical polymerization. The results of the simulations were compared to experimental data taken from conventional reactors and, subsequently, to experimental data coming from an unconventional millireactor.

A distribuição de pesos moleculares (DPM) de um polímero afeta as propriedades mecânicas, térmicas e reológicas do material. Além disso, a análise em tempo real de uma reação de polimerização é uma tarefa complicada e, consequentemente, os procedimentos de controle devem ser baseados em valores gerados pelos modelos. Por isso, é extremamente importante ter dados confiáveis sobre distribuições de pesos moleculares, melhorar a eficiência dos métodos existentes e desenvolver novos métodos capazes de prever as heterogeneidades das reações de polimerização. Experimentalmente, a DPM pode ser obtida usando técnicas como a cromatografia de permeação em gel. Para predizer a DPM, vários métodos foram desenvolvidos nas ultimas décadas. Um dos principais é o dos momentos estatísticos, baseado em conceitos puramente estatísticos, que não conseguem descrever completamente a DPM. Além disso, as aproximações com método de Galerkin usam polinômios ortogonais - no caso especifico polinômios de Laguerre - cujos coeficientes são calculados empregando os momentos estatísticos e a distribuição é gerada resolvendo um número de equações definido pelo usuário, relacionado à precisão desejada. Enfim, o método das funções geradoras de probabilidades foi utilizado para prever as DPMs, porém necessitando uma inversão da transformada de Laplace, que introduz problemas numéricos nem sempre possíveis de serem resolvidos. No presente trabalho, o sistema rigoroso de equações diferenciais ordinárias foi resolvido, com objetivo de reduzir as imprecisões e as limitações introduzidas pelas aproximações. Obter diretamente a DPM completa requer a resolução de um sistema contendo cerca de 2Nmax até 3Nmax equações diferenciais ordinárias rígidas, tarefa que há alguns anos era inviável devido a limitações relacionadas à capacidade de cálculo. Foi modelada a DPM para uma reação de polimerização radicalar livre de estireno e de metacrilato de metila. Um interesse especial foi dado à taxa de terminação que é, no momento, um dos temas mais investigados em polimerização por radicais livres. Os resultados das simulações foram comparados com dados experimentais tirados de reatores convencionais e, subsequentemente, com dados experimentais provenientes de um millireactor não convencional. / It is well known that the molecular weight distribution (MWD) of a synthetic polymer affects its mechanical, thermal and rheological properties. Furthermore, the on-line analysis for polymerization reaction is a difficult task and, consequently, the control procedures must rely on values given by models. As such, it is extremely important to have reliable data on the MWD, improve the efficiency of existing methods and develop new ones to predict the heterogeneities of polymerization reactions. Experimentally, the MWD can be obtained using techniques such as Gel Permeation Chromatography (GPC). To predict the MWD, many methods have been developed over the last decades. One of the main methods is the statistical moment treatment, which is based on a pure statistical concept and do not describe the whole MWD. Moreover, Galerkin approximation uses orthogonal polynomials -in general Laguerre polynomials- whose coefficients are calculated exploiting the statistical moment definition and the distribution is generated by solving a user-defined number of equations based on the desired precision. Finally, probability-generating functions that have been used to predict MWDs require Laplace transforms inversions, introducing numerical issues that must be bypassed and are not always solvable. It has been decided to base the approach without adopting any of these methods but directly solving the rigorous ordinary differential equation (ODE) system in order to reduce the inaccuracies and the limitations introduced by approximations. The direct obtention of the MWD requires the resolution of a system containing approximately 2Nmax up to 3Nmax stiff ODE equations that, a few years ago, was unfeasible due computational time limitations. The MWDs for a free radical styrene polymerization system and a methyl methacrylate system have been modeled. A special focus was given to the termination rate constant, which is, at the present, one of the most investigated topics in free radical polymerization. The results of the simulations were compared to experimental data taken from conventional reactors and, subsequently, to experimental data coming from an unconventional millireactor.

O impacto da oxidação com ozônio na transformação de compostos orgânicos de elevada massa molar (HMW) para o aumento da biodegradabilidade dos efluentes da indústria de celulose e papel foi investigado sob diferentes doses de ozônio. Os experimentos foram realizados utilizando-se os efluentes primário e de extração alcalina de duas indústrias de celulose sob dois valores iniciais de pH (12 e 7). Utilizou-se um reator em escala de laboratório equipado com um difusor de bolhas finas para a aplicação do ozônio. Os resultados revelaram o potencial da aplicação de ozônio como uma etapa de tratamento anterior ao processo biológico convencional. Para o efluente primário, a aplicação de 0,70 mg\'O IND.3\'/mL efluente elevou a razão DBO5/DQO de 0,18 para 0,35 e foi alcançada uma remoção de cor na ordem de 87%. Para o efluente de extração alcalina da indústria Howe Sound, a razão DBO5/DQO foi elevada de 0,07 para 0,15 (pH inicial 12) e para 0,20 (pH inicial 7) e obteve-se uma remoção de cor por volta de 44% com a aplicação de 0,80 mg\'O IND.3\'/mL efluente. Para o efluente de extração alcalina da indústria Catalyst Paper, obteve-se uma remoção de cor por volta de 78% e a razão DBO5/DQO foi elevada de 0,07 para 0,16 após a aplicação de uma dose de ozônio de 0,80 mg\'O IND.3\'/mL efluente. Essas modificações foram alcançadas por uma redução nas frações de elevada massa molar durante a aplicação de ozônio. Para o efluente primário, observou-se uma elevada redução da faixa de maior massa molecular ( > 2kDa) após a aplicação de 0,72 mg\'O IND.3\'/mL efluente. Alcançaram-se 85% e 61% de remoção da faixa superior a 5 kDa para os efluentes de extração alcalina da indústria Howe Sound sob pH inicial 7 e 12, respectivamente, com a aplicação de cerca de 0,72 mg\'O IND.3\'/mL efluente. A faixa de maior massa molar ( > 10 kDa) dos efluentes de extração alcalina da indústria Catalyst Paper foi removida com a aplicação de aproximadamente 0,80 mg \'O IND.3\'/mL efluente. O papel do ozônio molecular disponível sob pH neutro parece ser de fundamental importância quando o objetivo é a redução dos compostos de elevada massa molecular. / The impact of ozone oxidation in transforming high molecular weight (HMW) organic compounds in order to improve the biodegradability of pulp and paper effluents was investigated under different ozone doses. The experiments were conducted uppon a primary treated effluent and an alkaline bleach plant effluent taken from two pulp mills. The effluents were investigated under different initial pH (7 and 12). Ozone was applied using a semi-batch reactor equipped with fine bubble diffuser. The results showed the potential for using ozone as a pre-treatment to the conventional biological process. Applying 0.70 mg\'O IND.3\'/mLww to the primary treated effluent enhanced the ratio of BOD5/COD was from 0.18 to 0.35 and decreased the colour by 87%. The ratio of BOD5/COD was increased from 0.07 to 0.15 (initial pH 12) and to 0.20 (initial pH 7) and colour was reduced by 44% after applying 0.80 mg\'O IND.3\'/mLww to the alkaline bleach effluent from Howe Sound\'s mill. A similar behavior was observed after 0.80 mg\'O IND.3\'/mLww was applied to the alkaline bleach effluent from Catalyst\'s mill. The ratio of BOD5/COD was increased from 0.07 to 0.16 and the effluent colour decreased by 78%. These changes were primarily driven by reductions of the HMW fractions of the effluent during ozonation. Organics with molecular range higher than 2 kDa were completely removed from the primary treated effluent. Aproximately 85% and 61% of the organics higher than 5 kDa were removed from the Howe Sound\'s alkaline bleach effluent under initial pH 7 and 12, respectively, after applying 0.72 mg\'O IND.3\'/mLww. Organic compounds with molecular weight higher than 10 kDa were completely removed from the Catalyst\'s alkaline bleach effluent after applying 0.80 mg\'O IND.3\'/mLww. Molecular ozone available under neutral conditions seems to play an important role when the removal of the high molecular weight organic compounds is the main objective.

No description available.

Characterization of cellulose by its molecular weight distribution is afforded after polymeranalogeous dissolution. Additionally, a molecular dispersion of the polymer is a prerequisite. Common processes are dissolution of cellulose in dimethylacetamide-lithiumchloride, nitration and carbanilation. Degradation of the polysaccharide chains can occur in each of the mentioned processes. It is shown that degradation in pyridine occurs via beta-elimination at carbonyl groups along the cellulose chains. Carbanilierung in DMSO is much more pronounced. It comprises oxidation along the Pfitzner-Moffatt-mechanism and subsequent beta-elimination at the thus formed carbonyl-groups. This was elucidated with model systems and by investigation of the carbanilation in different media. Carbonyl groups of cellulose are masked through reaction with phenylisocyanate. This was shown with model. Therefore, the determination of carbonyl groups in cellulose-tricarbanilates is not possible. The separation of low-molecular weight byproducts was optimised. The influence of pretreatment and preactivation of cellulose-samples on the completeness of the conversion was studied. A standard protocol for the carbanilation of cellulose is provided. / Cellulose wird u.a. durch ihre Molmassenverteilung charakterisiert, deren Ermittlung ein polymeranaloges Verfahren zur molekulardispersen Auflösung des Polymers erfordert. Hierfür sind die Direktlösung, die Nitrierung und die Carbanilierung in Gebrauch. Bei allen Prozessen kann es zum Abbau der Polysaccharidketten kommen, wobei diesen Prozessen wenig Beachtung geschenkt wurde. In der Arbeit wird gezeigt, daß der Abbau bei der Carbanilierung in Pyridin durch Beta-Eliminierung an vorhandenen Carbonylgruppen erfolgt. Die Carbanilierung in DMSO fällt stets stärker aus als bei Einsatz von Pyridin und umfasst die Prozesse Oxidation nach dem Pfitzner-Moffatt-Mechanismus und anschließende Beta-Eliminierung an den neu gebildeten Carbonylgruppen. Dies wird durch Untersuchungen an Modellsystemen und am Polymer herausgearbeitet. Carbonylgruppen an Cellulose werden durch die Umsetzung mit Phenylisocyanat maskiert, was an Modellverbindungen gezeigt wurde (Bildung von Endioldicarbanilaten und carbanilierten Halbacetalen). Ihre Bestimmung in Cellulosecarbanilaten ist daher nicht möglich. Die Abtrennung von niedermolekularen Nebenprodukten der Umsetzung wurde optimiert. Der Einfluss der Vorbehandlung und Voraktivierung von Celluloseproben auf die Vollständigkeit der Umsetzung wurde eingehend untersucht. Es wird ein Standardverfahren zur Carbanilierung von Cellulose angegeben.

No description available.

O impacto da oxidação com ozônio na transformação de compostos orgânicos de elevada massa molar (HMW) para o aumento da biodegradabilidade dos efluentes da indústria de celulose e papel foi investigado sob diferentes doses de ozônio. Os experimentos foram realizados utilizando-se os efluentes primário e de extração alcalina de duas indústrias de celulose sob dois valores iniciais de pH (12 e 7). Utilizou-se um reator em escala de laboratório equipado com um difusor de bolhas finas para a aplicação do ozônio. Os resultados revelaram o potencial da aplicação de ozônio como uma etapa de tratamento anterior ao processo biológico convencional. Para o efluente primário, a aplicação de 0,70 mg\'O IND.3\'/mL efluente elevou a razão DBO5/DQO de 0,18 para 0,35 e foi alcançada uma remoção de cor na ordem de 87%. Para o efluente de extração alcalina da indústria Howe Sound, a razão DBO5/DQO foi elevada de 0,07 para 0,15 (pH inicial 12) e para 0,20 (pH inicial 7) e obteve-se uma remoção de cor por volta de 44% com a aplicação de 0,80 mg\'O IND.3\'/mL efluente. Para o efluente de extração alcalina da indústria Catalyst Paper, obteve-se uma remoção de cor por volta de 78% e a razão DBO5/DQO foi elevada de 0,07 para 0,16 após a aplicação de uma dose de ozônio de 0,80 mg\'O IND.3\'/mL efluente. Essas modificações foram alcançadas por uma redução nas frações de elevada massa molar durante a aplicação de ozônio. Para o efluente primário, observou-se uma elevada redução da faixa de maior massa molecular ( > 2kDa) após a aplicação de 0,72 mg\'O IND.3\'/mL efluente. Alcançaram-se 85% e 61% de remoção da faixa superior a 5 kDa para os efluentes de extração alcalina da indústria Howe Sound sob pH inicial 7 e 12, respectivamente, com a aplicação de cerca de 0,72 mg\'O IND.3\'/mL efluente. A faixa de maior massa molar ( > 10 kDa) dos efluentes de extração alcalina da indústria Catalyst Paper foi removida com a aplicação de aproximadamente 0,80 mg \'O IND.3\'/mL efluente. O papel do ozônio molecular disponível sob pH neutro parece ser de fundamental importância quando o objetivo é a redução dos compostos de elevada massa molecular. / The impact of ozone oxidation in transforming high molecular weight (HMW) organic compounds in order to improve the biodegradability of pulp and paper effluents was investigated under different ozone doses. The experiments were conducted uppon a primary treated effluent and an alkaline bleach plant effluent taken from two pulp mills. The effluents were investigated under different initial pH (7 and 12). Ozone was applied using a semi-batch reactor equipped with fine bubble diffuser. The results showed the potential for using ozone as a pre-treatment to the conventional biological process. Applying 0.70 mg\'O IND.3\'/mLww to the primary treated effluent enhanced the ratio of BOD5/COD was from 0.18 to 0.35 and decreased the colour by 87%. The ratio of BOD5/COD was increased from 0.07 to 0.15 (initial pH 12) and to 0.20 (initial pH 7) and colour was reduced by 44% after applying 0.80 mg\'O IND.3\'/mLww to the alkaline bleach effluent from Howe Sound\'s mill. A similar behavior was observed after 0.80 mg\'O IND.3\'/mLww was applied to the alkaline bleach effluent from Catalyst\'s mill. The ratio of BOD5/COD was increased from 0.07 to 0.16 and the effluent colour decreased by 78%. These changes were primarily driven by reductions of the HMW fractions of the effluent during ozonation. Organics with molecular range higher than 2 kDa were completely removed from the primary treated effluent. Aproximately 85% and 61% of the organics higher than 5 kDa were removed from the Howe Sound\'s alkaline bleach effluent under initial pH 7 and 12, respectively, after applying 0.72 mg\'O IND.3\'/mLww. Organic compounds with molecular weight higher than 10 kDa were completely removed from the Catalyst\'s alkaline bleach effluent after applying 0.80 mg\'O IND.3\'/mLww. Molecular ozone available under neutral conditions seems to play an important role when the removal of the high molecular weight organic compounds is the main objective.