Tumor targeting with newly designed biparatopic antibodies directed against two different epitopes of the carcinoembryonic antigen (CEA).

In an attempt to improve tumor targeting and tumor retention time of monoclonal antibodies (MAbs), we prepared biparatopic antibodies (BpAbs) having the capability of binding 2 different non-overlapping epitopes on the same target antigen molecule, namely, the carcinoembryonic antigen (CEA). Six BpAbs were constructed by coupling 2 different Fab' fragments from 4 different specific anti-CEA MAbs recognizing 4 CEA epitopes (Gold 1-4). Demonstration of the double paratopic binding of these antibodies for CEA was confirmed in vitro by inhibition radioimmunoassay and cross-inhibition analysis by surface plasmon resonance (SPR; BIACORE) technology. Using the latter technique, the affinity constants for CEA immobilized onto the sensor chip were found to range from 0.37 to 1.54 x 10(9) M(-1) for the 4 parental F(ab')2 fragments and from 1.88 to 10.14 x 10(9) M(-1) for the BpAbs, demonstrating the advantage of biparatopic binding over conventional F(ab')2 binding. The Ka improvement was particularly high for BpAb F6/35A7 and BpAb F6/B17 with a 9.5- and 8.1-fold increase, respectively, as compared with the parental F(ab')2. In vivo, the 6 BpAbs were compared with their 2 respective parental F(ab')2 by injection of 131I-BpAb/125I-F(ab')2 parental fragments into nude mice xenografted with the human colon carcinoma T380. Dissection 72 hr post-injection demonstrated that BpAb B17/CE25 and BpAb F6/B17 gave higher tumor uptake than that of their parental F(ab')2. This finding is particularly interesting for BpAb F6/B17, which compared favorably with the F6 F(ab')2, one of the best parental F(ab')2 fragments used in our study.

Korkeavaaleuksisen PGW-massan valmistaminen

Työssä haettiin optimaalista valkaisukemikaalien annostelusuhdetta mahdollisimman vaalean massan valmistamiseksi. Tarkoituksena oli myös selvittää käytettävän tehdasprosessin pullonkauloja ja esittää vaihtoehtoja prosessin kehittämiseksi. Kirjallisuusosassa tutustuttiin mekaanisen massan peroksidivalkaisuun ja erilaisiin prosessimalleihin sen suorittamiseksi. Kirjallisuudesta saatuja lähtötietoja sovellettiin sitten ensin laboratorio- ja laajemmin tehdaskokein käytäntöön. Laboratoriokokeissa haettiin optimaalista lipeäannosta vakioperoksidiannoksella. Lisäksi selvitettiin lämpötilan ja viipymäajan vaikutusta valkaisutulokseen. Tuloksista oli todettavissa, että sekä lämpötilan että lipeäannoksen kasvattaminen kiihdyttää valkaisureaktiota. Korkeammassa lämpötilassa tarvittava lipeäannos on pienempi. Lyhyellä viipymäajalla ja matalammalla lämpötilalla saavutetaan hyviä tuloksia vain suurella lipeäannoksella. Suurempaa silikaattiannosta käytettäessä valkaisun jälkeen mitattu loppupH oli korkeampi ja jäännösperoksidin määrä hieman suurempi kuin referenssipisteessä. Vaaleudessa ei merkittävää muutosta näkynyt. Yleisesti laboratoriokokeiden tulokset vastasivat kirjallisuudessa esitettyjä tuloksia. Tehdaskokeet suoritettiin kahdella peroksidiannoksella. Kummallekin peroksidiannokselle haettiin optimaalinen lipeäannos. Lisäksi seurattiin silikaattiannoksen vaikutusta syntyvään vaaleuteen. Varsinaisten kokeiden lisäksi suoritettiin lyhyt maksimivaaleuskoe suurella peroksidiannoksella käyttäen kahta eri lipeäannosta. Suurin mitattu vaaleus oli 79,3 % ISO. Peroksidiannoksella 2,5 % saavutettiin noin 14 ISO-yksikön vaaleudennousu, ja annoksella 3 % vaaleudennousu oli noin 16 yksikköä. Tehdaskokeiden aikana kokeiltiin myös kemikaalien laimennusveden määrän vaikutusta vaaleuteen. Veden määrän vähetessä valkaisusakeus nousi ja vaaleus parani. Hiomon nykyprosessille laadittiin aine- ja energiatase. Taseet tehtiin myös prosessille, jossa nykyvalkaisimoon on lisätty valkaistun massan pesu ja jäännöskemikaalien kierrätys. Taseiden tarkoituksena oli selvittää virtaavien jakeiden määriä ja prosessin energiatasapainoa eri tilanteissa. Massan puhtauden paranemista pesun aikana tarkasteltiin laskennallisesti. Tämän työn aikana kävi selväksi, että oikeilla valkaisukemikaalisuhteilla pystytään valmistamaan vaaleaa massaa. Viipymäaikaa lisäämällä valkaisuun saisi lisää tehoa, mutta vain tunnin viipymäajalla päästään jo hyviin tuloksiin. Vaaleusheittoja aiheuttavat valkaistavan massan lähtövaaleuden, sakeuden ja lämpötilan muutokset. Lisäksi viipymäajan muutokset aiheuttavat huojuntaa saavutettavaan loppuvaaleuteen.

Minimibiolietetuottoinen aktiivilieteprosessi massateollisuuden peroksidipitoisten jätevesien puhdistuksessa

Työ on tehty USF Aquaflow Oy:lle osana Cleantech 2000-projektia. USF Aquaflow Oy on suunnitellut minimibiolietetuottoisen reaktorin, MBP-reaktorin, toimivaksi osana aktiivilieteprosessia. Työn tavoitteena oli selvittää MBP-reaktorin toimintaa massateollisuuden peroksidipitoisilla jätevesillä. Pääpaino asetettiin MBP-reaktorin mikrobiologian tutkimiseen. Aktiivilieteprosessissa syntyvä bioliete on yksi metsäteollisuuden merkittävimmistä sivuainevirroista, jonka tuotantoa pyritään vähentämään ja käsiteltävyyttä parantamaan. MBP-reaktori aktiivilieteprosessissa vähentää koko prosessin lietteentuottoa, nostaa lietteen kuiva-ainepitoisuutta ja vähentää näin lietteen vaatimaa jatkokäsittelyn tarvetta. Työssä tutkittiin kahdella erilaisella jätevesijakeella peroksidin vaikutusta MBP-reaktorin COD-reduktioon, kiintoaineen kasvuun, lietteentuottoon ja mikrobiologiaan eri pituisilla viiveillä. MBP-reaktorin viive on suunniteltu aktiivilieteprosessin ilmastusaltaan viivettä huomattavasti lyhyemmäksi. Työn tuloksien perusteella lyhyellä viiveellä MBP-reaktorissa käynnistyy tehokas bakteeritoiminta, joka kuluttaa jäteveden COD:ta. Sellutehtaan jätevesille MBP-reaktorin toiminta on heikompaa kuin termomekaanisen massanvalmistuksen jätevesillä, johtuen sellun valmistuksessa käytetyistä kemikaaleista. Jätevedenpuhdistamon lietteen määrän vähentäminen on tällä hetkellä metsäteollisuuden tehtailla tärkeä jatkotutkimuksia vaativa kohde. MBP-reaktorin toiminnan takaamiseksi osana aktiivilieteprosessia tulisi jatkotutkimuksia suorittaa eri tyyppisille jätevesijakeille ja tarkkailla useampien kemikaalien vaikutusta reaktorin mikrobiologiaan, COD-reduktioon ja lietteentuottoon.

Stabilization of the ionic form of weak acid cation exchange resins

Weak acid cation exchange (WAC) resins are used in the chromatographic separation of betaine from vinasse, a by-product of sugar industry. The ionic form of the resin determines the elution time of betaine. When a WAC-resin is in hydrogen form, the retention time of betaine is the longest and betaine elutes as the last component of vi-nasse from the chromatographic column. If the feed solution contains salts and its pH is not acidic enough to keep the resin undissociated, the ionic form of the hydrogen form resin starts to alter. Vinasse contains salts and its pH is around 5, it also contains weak acids. To keep the metal ion content (Na/H ratio) of the resin low enough to ensure successful separation of betaine, acid has to be added to either eluent (water) or vinasse. The aim of the present work was to examine by laboratory experiments which option requires less acid. Also the retention mechanism of betaine was investigated by measuring retention volumes of acetic acid and choline in different Na/H ratios of the resin. It was found that the resulting ionic form of the resin is the same regardless of whether the regeneration acid is added to the eluent or the feed solution (vinasse). Be-sides the salt concentration and the pH of vinasse, also the concentration of weak acids in the feed affects the resulting ionic form of the resin. The more buffering capacity vinasse has, the more acid is required to keep the ionic form of the resin desired. Vinasse was found to be quite strong buffer solution, which means relatively high amounts of acid are required to prevent the Na/H ratio from increasing too much. It is known that the retention volume of betaine decreases significantly, when the Na/H ratio increases. This is assumed to occur, because the amount of hydrogen bonds between the carboxylic groups of betaine and the resin decreases. Same behavior was not found with acetic acid. Choline has the same molecular structure as betaine, but instead of carboxylic group it has hydroxide group. The retention volume of choline increased as the Na/H ratio of the resin increased, because of the ion exchange reaction between choline cation and dissociated carboxylic group of the resin. Since the retention behavior of choline on the resin is opposite to the behavior of be-taine, the strong affinity of betaine towards hydrogen form WAC-resin has to be based on its carboxylic group. It is probable that the quaternary ammonium groups also affect the behavior of the carboxylic groups of betaine, causing them to form hydrogen bonds with the carboxylic groups of the resin.

Identificação de componentes de óleos voláteis: Análise espectroscópica de misturas de sesquiterpenos

This paper describes a chromatographic method to fractionate volatile oils and to identify their sesquiterpenic constituents. The fractionation process includes flash chromatography over silica gel and chromatography over silica gel/AgNO3, utilising pentane, CH2Cl2 and/or acetone as eluents. GC chromatograms were obtained in order to get the relative percentage of each constituent in the volatile oils, to get the retention time value of them as well as to analyse and combine the fractions eluted from the columns. Such procedure afford mixtures of sesquiterpenes which are analysed by GC/MS, 13C and ¹H NMR.

Avaliação da salinização de açudes no semi-árido brasileiro por ICP-AES

The salt accumulation process in some reservoirs of regular and irregular use (from 10 to 50 years of constrution), located in the Southeast of Bahia State was evaluated. Inductively coupled plasma atomic emission spectrometry was used to evaluate the concentrations of Na, K, Ca and Mg in water samples from inside and upstream of the reservoirs. The results showed that for reservoirs of irregular use, the salt accumulation, indicated by the tracer Na, increases with the age of the reservoirs, however for the reservoirs of regular use the hydraulic retention time is the main parameter.

Estudo do coeficiente de partição octanol-água de bifenilas policloradas (PCBs) utilizando parâmetros topológicos

A model based on chemical structure was developed for the accurate prediction of octanol/water partition coefficient (K OW) of polychlorinated biphenyls (PCBs), which are molecules of environmental interest. Partial least squares (PLS) was used to build the regression model. Topological indices were used as molecular descriptors. Variable selection was performed by Hierarchical Cluster Analysis (HCA). In the modeling process, the experimental K OW measured for 30 PCBs by thin-layer chromatography - retention time (TLC-RT) has been used. The developed model (Q² = 0,990 and r² = 0,994) was used to estimate the log K OW values for the 179 PCB congeners whose K OW data have not yet been measured by TLC-RT method. The results showed that topological indices can be very useful to predict the K OW.

Bioenergiaa ja ravinteita kasvi- ja eläinperäisistä sivuainevirroista Parikkalassa

Euroopan unionissa pyritään lisäämään uusiutuvien energialähteiden käyttöä. Tämän työn tavoitteena oli selvittää Parikkalan kunnan alueella muodostuvat biomassat sekä tutkia niiden hyötykäyttömahdollisuuksia sähkön, lämmön sekä lannoitteiden tuotannossa. Käsiteltäviä biomassoja ovat eläintilojen lietteet ja lannat, biojätteet ja yhdyskuntalietteet, vesistöjen kunnostuksessa syntyvät biomassat sekä peltobiomassat ja metsäbiomassa. Mädätyksen kannalta olennaisinta on materiaalien kosteus ja haihtuvan orgaanisen aineksen pitoisuus sekä siitä saatava biokaasumäärä. Poltossa polttoaineen kuiva-aineen lämpöarvo ja kosteus määrittelevät saadun hyödyn. Kompostoinnissa on tärkeää huolehtia riittävästä ilman saannista ja riittävästä viipymäajasta. Hyödynnettäessä biokaasua sähkön ja lämmön yhteistuotannossa on tärkeää löytää hyötykäyttö myös muodostuvalle lämmölle. Poltosta saatavan tuhkan hyötykäyttö onnistuu metsälannoitteena, kun poltetaan turvetta tai puuta. Kompostia voidaan hyödyntää maanparannusaineena. Parikkalan alueella tarkasteltiin biomassojen nykyistä ja mahdollista tulevaa hyötykäyttöä. Tarkastelu tehtiin skenaarioiden avulla. Skenaarioihin kuuluvat mädätyksen ja polton maksimipotentiaalit sekä keskitetyn ja hajautetun käsittelyn skenaariot. Alueelta on saatavissa paljon biomassoja, joista massaltaan suurin on eläintilojen lannat. Alueella on hankaluutena löytää sopiva kulutuskohde biokaasusta tuotetulle lämmölle, mutta sopivana kohteena voisi toimia alueella oleva suuri sikala tai lämpökeskukset.

Degradação de corantes reativos pelo sistema ferro metálico/peróxido de hidrogênio

In this work the degradation of aqueous solutions of reactive azo-dyes is reported using a combined reductive/advanced oxidative process based in the H2O2/zero-valent iron system. At optimized experimental conditions (pH 7, H2O2 100 mg L-1, iron 7 g L-1) and using a continuous system containing commercial iron wool, the process afforded almost total discolorization of aqueous solutions of three reactive azo-dyes (reactive orange 16, reactive black 5 and brilliant yellow 3G-P) at a hydraulic retention time of 2.5 min. At these conditions the hydrogen peroxide is almost totally consumed while the released total soluble iron reaches a concentration compatible with the current Brazilian legislation (15 mg L-1).

Active sulphide mine tailings impoundments as sources of contaminated drainage: controlling factors, methods of characterisation and geochemical constraints for mitigation

Low quality mine drainage from tailings facilities persists as one of the most significant global environmental concerns related to sulphide mining. Due to the large variation in geological and environmental conditions at mine sites, universal approaches to the management of mine drainage are not always applicable. Instead, site-specific knowledge of the geochemical behaviour of waste materials is required for the design and closure of the facilities. In this thesis, tailings-derived water contamination and factors causing the pollution were investigated in two coeval active sulphide mine sites in Finland: the Hitura Ni mine and the Luikonlahti Cu-Zn-Co-Ni mine and talc processing plant. A hydrogeochemical study was performed to characterise the tailingsderived water pollution at Hitura. Geochemical changes in the Hitura tailings were evaluated with a detailed mineralogical and geochemical investigation (solid-phase speciation, acid mine drainage potential, pore water chemistry) and using a spatial assessment to identify the mechanisms of water contamination. A similar spatial investigation, applying selective extractions, was carried out in the Luikonlahti tailings area for comparative purposes (Hitura low-sulphide tailings vs. Luikonlahti sulphide-rich tailings). At both sites, hydrogeochemistry of tailings seepage waters was further characterised to examine the net results of the processes observed within the impoundments and to identify constraints for water treatment. At Luikonlahti, annual and seasonal variation in effluent quality was evaluated based on a four-year monitoring period. Observations pertinent to future assessment and mine drainage prevention from existing and future tailings facilities were presented based on the results. A combination of hydrogeochemical approaches provided a means to delineate the tailings-derived neutral mine drainage at Hitura. Tailings effluents with elevated Ni, SO₄ ^2- and Fe content had dispersed to the surrounding aquifer through a levelled-out esker and underneath the seepage collection ditches. In future mines, this could be avoided with additional basal liners in tailings impoundments where the permeability of the underlying Quaternary deposits is inadequate, and with sufficiently deep ditches. Based on the studies, extensive sulphide oxidation with subsequent metal release may already initiate during active tailings disposal. The intensity and onset of oxidation depended on e.g. the Fe sulphide content of the tailings, water saturation level, and time of exposure of fresh sulphide grains. Continuous disposal decreased sulphide weathering in the surface of low-sulphide tailings, but oxidation initiated if they were left uncovered after disposal ceased. In the sulphide-rich tailings, delayed burial of the unsaturated tailings had resulted in thick oxidized layers, despite the continuous operation. Sulphide weathering and contaminant release occurred also in the border zones. Based on the results, the prevention of sulphide oxidation should already be considered in the planning of tailings disposal, taking into account the border zones. Moreover, even lowsulphide tailings should be covered without delay after active disposal ceases. The quality of tailings effluents showed wide variation within a single impoundment and between the two different types of tailings facilities assessed. The affecting factors included source materials, the intensity of weathering of tailings and embankment materials along the seepage flow path, inputs from the process waters, the water retention time in tailings, and climatic seasonality. In addition, modifications to the tailings impoundment may markedly change the effluent quality. The wide variation in the tailings effluent quality poses challenges for treatment design. The final decision on water management requires quantification of the spatial and seasonal fluctuation at the site, taking into account changes resulting from the eventual closure of the impoundment. Overall, comprehensive hydrogeochemical mapping was deemed essential in the identification of critical contaminants and their sources at mine sites. Mineralogical analysis, selective extractions, and pore water analysis were a good combination of methods for studying the weathering of tailings and in evaluating metal mobility from the facilities. Selective extractions with visual observations and pH measurements of tailings solids were, nevertheless, adequate in describing the spatial distribution of sulphide oxidation in tailings impoundments. Seepage water chemistry provided additional data on geochemical processes in tailings and was necessary for defining constraints for water treatment.

Water circulations for effective bleaching of high-brightness mechanical pulps

The amount of water available is usually restricted, which leads to a situation where a complete understanding of the process, including water circulations and the influence of water components, is essential. The main aim of this thesis was to clarify the possibilities for the efficient use of residual peroxide by means of water circulation rearrangements. Rearranging water circulations and the reduction of water usage may cause new problems, such as metal induced peroxide decomposition that needs to be addressed. This thesis introduces theoretical methods of water circulations to combine two variables; effective utilization of residual peroxide and avoiding manganese in the alkaline peroxide bleaching stage. Results are mainly based on laboratory and mill site experiments concerning the utilization of residual peroxide. A simulation model (BALAS) was used to evaluate the manganese contents and residual peroxide doses. It was shown that with optimum recirculation of residual peroxide the brightness can be improved or chemical costs can be decreased. From the scientific perspective, it was also very important to discover that recycled peroxide was more effective pre-bleaching agent compared to fresh peroxide. This can be due to the organic acids i.e. per acetic acid in wash press filtrate that have been formed in alkaline bleaching stage. Even short retention time was adequate and the activation of residual peroxide using sodium hydroxide was not necessary. There are several possibilities for using residual peroxide in practice regarding bleaching. A typical modern mechanical pulping process line consist of defibering, screening, a disc filter, a bleach press, high consistency (HC) peroxide bleaching and a wash press. Furthermore there usually is not a particular medium consistency (MC) pre-bleaching stage that includes additional thickening equipment. The most advisable way to utilize residual peroxide in this kind of process is to recycle the wash press filtrate to the dilution of disc filter pulp (low MC pre-bleaching stage). An arrangement such as this would be beneficial in terms of the reduced convection of manganese to the alkaline bleaching stage. Manganese originates from wood material and will be removed to the water phase already in the early stages of the process. Recycling residual peroxide prior to the disc filter is not recommended because of low consistencies. Regarding water circulations, the novel point of view is that, it would be beneficial to divide water circulations into two sections and the critical location for the division is the disc filter. Both of these two sections have their own priority. Section one before the disc filter: manganese removal. Section two after the disc filter: brightening of pulp. This division can be carried out if the disc filter pulp is diluted only by wash press filtrate before the MC storage tower. The situation is even better if there is an additional press after the disc filter, which will improve the consistency of the pulp. This has a significant effect on the peroxide concentration in the MC pre-bleaching stage. In terms of manganese content, it is essential to avoid the use of disc filter filtrate in the bleach press and wash press showers. An additional cut-off press would also be beneficial for manganese removal. As a combination of higher initial brightness and lower manganese content, the typical brightness increase varies between approximately 0.5 and 1% ISO units after the alkaline peroxide bleaching stage. This improvement does not seem to be remarkable, but as it is generally known, the final brightness unit is the most expensive and difficult to achieve. The estimation of cost savings is not unambiguous. For example in GW/TMP mill case 0.6% ISO units higher final brightness gave 10% savings in the costs of bleaching chemicals. With an hypothetical 200 000 ton annual production, this means that the mill could save in the costs of bleaching chemicals more than 400 000 euros per year. In general, it can be said that there were no differences between the behavior of different types of processes (GW, PGW, TMP and BCTMP). The enhancement of recycling gave a similar response in all cases. However, we have to remember that the utilization of residual peroxide in older mills depends a great deal on the process equipment, the amount of water available and existing pipeline connections. In summary, it can be said that processes are individual and the same solutions cannot be applied to all cases.

Otimização e validação intralaboratorial de método para análise de resíduos de cloranfenicol em leite caprino por cromatografia gasosa com detecção por captura de elétrons (CG/DCE)

The presence of chloramphenicol residues in goat milk can cause toxic effects in the population. The present work consists of the optimization and validation of analytical methodology for determination of chloramphenicol residues in goat milk by GC/ECD. The extraction was made with ethyl acetate and the clean-up with SPE-C18. The identification was made by comparison of retention time and GC/MS, and the quantification by external standard. The method was selective, linearity (0.998), precise (5.8-13.4%), exact (69.87-73.71%) and robust. The LOD and LOQ of method were 0.030 and 0.10 μg/kg, respectively. The method was efficiently for analysis of chloramphenicol in goat milk.

Determinação de 2,5-hexanodiona em urina empregando cromatografia líquida de alta eficiência, após derivatização com 2,4-dinitrofenil-hidrazina

A method for quantifying urinary 2,5-hexanedione was optimized and validated. Urine samples were hydrolyzed and derivatized with 2,4-dinitrophenylhydrazine. The analyte was separated in a high performance liquid chromatography system with a diode array detector, using a C18 column (150 x 4.6 mm, p.d. 5 µm) and a mobile phase composed of phosphate buffer pH 2.3:acetonitrile (40:60, v/v), at a flow rate of 1 mL/min. The chromatograms were monitored at 334 nm. Retention time was 7.3 minutes. Main validation parameters were: coefficient of determination: 0.9994, accuracy: 96 to 107%; intra-assay precision (RSD): 3.08 to 6.72%; inter-assay precision (RSD): 2.54 to 8.17% and limit of quantitation of 0.19 µg/mL.

Desenvolvimento de metodologia para avaliar remoção de estrogênios em estações de tratamento de esgotos

The present research aimed to study the parameters that affect the determination of estrogens in sewage upon the use of SPE and determination by using gas chromatography mass spectrometry (GC/MS). The study evaluated the stabilization pond technology with regard to estrogens removal. The results showed that the methodology was able to identify and quantify the estrogens E1, E2, E2-17A and EE2 in sewage. Moreover, the estrogens sometimes were not removed in the stabilization pond, showing that even the high hydraulic retention time (HRT) and high sunlight intensity were not enough to degrade these compounds completely during load peaks.

Kaasun dispergoituminen tehdasmittakaavaisessa keskisakean massan sekoittimessa

Työn tarkoituksena oli selvittää Proto 10 kemikaalisekoittimen kyky dispergoida kaasua keskisakean valkaistun mäntysellun joukkoon. Työssä käytettiin kuvantamistekniikkaa, jonka avulla pystyttiin näkemään sekoittimen ja putkiston sisälle sekoitustapahtuman aikana. Muodostunutta dispersiota tarkasteltiin kolmesta kuvauspisteestä, joista yksi sijaitsi sekoittimen pesässä ja kaksi putkistossa sekoittimen jälkeen. Työssä verrattiin myös laboratoriosekoittimella saatuja tuloksia teollisen mittakaavan sekoittimella saatuihin tuloksiin, sekä määritettiin tarvittava pinta-aktiivisen aineen konsentraatio, jolla saavutettiin ruskeaa massaa vastaava vaahtoaminen. Työn kokeellinen osuus koostui kolmesta osasta. Ensimmäisessä vaiheessa tutkittiin ruskeasta mänty- ja koivumassasta lingotun suodoksen vaahtoamista ja verrattiin sitä vedellä ja pesuaineella saatavaan vaahtoon. Toisessa vaiheessa suoritettiin referenssiajot laboratoriosekoittimen ja teollisen mittakaavan sekoittimen vertailua varten Quantum Mark IV laboratoriosekoittimella. Kolmannessa vaiheessa tutkittiin Proto 10 sekoittimen kykyä dispergoida kaasua mäntysellun joukkoon eri pyörimisnopeuksilla ja virtaamilla. Työn tuloksien perusteella energiankäytön kannalta paras pyörimisnopeus Proto 10 sekoittimelle on 1500 min-1. Nostamalla kierrosnopeutta yli tämän ei saavutettu merkittävää parannusta dispersion laadussa varsinkaan suuremmilla virtaamilla. Virtaamalla todettiin olevan suuri merkitys sekoitustulokseen. Laboratoriosekoittimella tehtyjen kokeiden todettiin vastaavan parhaiten teollisen mittakaavan tuloksia pyörimisnopeudella 1200 min-1.