927 resultados para bladder washing


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Every adherent eukaryotic cell exerts appreciable traction forces upon its substrate. Moreover, every resident cell within the heart, great vessels, bladder, gut or lung routinely experiences large periodic stretches. As an acute response to such stretches the cytoskeleton can stiffen, increase traction forces and reinforce, as reported by some, or can soften and fluidize, as reported more recently by our laboratory, but in any given circumstance it remains unknown which response might prevail or why. Using a novel nanotechnology, we show here that in loading conditions expected in most physiological circumstances the localized reinforcement response fails to scale up to the level of homogeneous cell stretch; fluidization trumps reinforcement. Whereas the reinforcement response is known to be mediated by upstream mechanosensing and downstream signaling, results presented here show the fluidization response to be altogether novel: it is a direct physical effect of mechanical force acting upon a structural lattice that is soft and fragile. Cytoskeletal softness and fragility, we argue, is consistent with early evolutionary adaptations of the eukaryotic cell to material properties of a soft inert microenvironment.

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Pelvic lipomatosis is a rare disorder where fat tissue deposition is observed in spaces of the pelvic area, causing extrinsic compression of the bladder, rectum and blood vessels. In the present report, the authors describe the case of a 48-year-old male patient presenting low back pain, dysuria and pollakiuria. Findings at excretory urography, computed tomography and magnetic resonance imaging are described.

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The issue of how contractility and adhesion are related to cell shape and migration pattern remains largely unresolved. In this paper we report that Gleevec (Imatinib), an Abl family kinase inhibitor, produces a profound change in the shape and migration of rat bladder tumor cells (NBTII) plated on collagen-coated substrates. Cells treated with Gleevec adopt a highly spread D-shape and migrate more rapidly with greater persistence. Accompanying this more spread state is an increase in integrin-mediated adhesion coupled with increases in the size and number of discrete adhesions. In addition, both total internal reflection fluorescence microscopy (TIRFM) and interference reflection microscopy (IRM) revealed a band of small punctate adhesions with rapid turnover near the cell leading margin. These changes led to an increase in global cell-substrate adhesion strength, as assessed by laminar flow experiments. Gleevec-treated cells have greater RhoA activity which, via myosin activation, led to an increase in the magnitude of total traction force applied to the substrate. These chemical and physical alterations upon Gleevec treatment produce the dramatic change in morphology and migration that is observed.

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Tämä työ suoritettiin UPM- Kymmene Oyj:n Tervasaaren tehtaan PK 5:llä. PK 5 valmistaa tarrantaustapaperia. Tämän työn tarkoituksena oli löytää eri keinoja paperin puhtauden parantamiseksi. Puhtaamman paperin valmistaminen parantaa paperikoneen kilpailukykyä kilpailijoihinsa nähden sekä vähentää asiakasvalituskustannuksia. Työn kirjallinen osa koostuu kolmesta suuremmasta kokonaisuudesta, joiden tarkoituksena on luoda teoriapohjaa kokeellisen osan suoritusta varten. Kirjallisuusosan pääpaino on kohdistettu PK 5:llä esiintyviin saostumanaiheuttajiin, kuten uuteaineisiin, ASA- liimaan ja mikrobeihin. Tarkemmassa tarkastelussa on kirjallisuusosassa myös painelajittelu ja pyörrepuhdistus. Kokeellisessa osassa suoritettiin PK 5:n prosessissa syntyvien epäpuhtauksien karakterisointi. Suurimmat saostuman aiheuttajat analyysien perusteella olivat puuperäiset uuteaineet ja ASA- liima. Epäorgaanisista aineista päällystyskomponenttina toimiva kaoliini ja sellun mukana tuleva pihkatalkki esiintyi useimpien saostumien komponentteina. Selvityksessä havaittiin, että prosessille vieraita aineita ei löydetty muista, kuin kalanteroidusta paperista analysoiduista tummista täplistä. Tummista täplistä analysoitu styreenin alkuperä voi selittyä mm. prosessiin päässeellä kumilla tai muovilla. PK 5:n prosessissa selvityksen mukaan silikonipohjainen vaahdonestoaine aiheuttaa erittäin suuria tummia saostumia, joten sen pääsy prosessiin tulee estää sellutehtaalla tarkoin. Epäpuhtauksien määrä on suurin PK 5:n prosessissa hylkylinjassa ja lyhyessä kierrossa. Hylyn painelajittelu poistaa hyvin roskia syöttömassasta. Hylyn lajittelun toisen portaan lajittimen rejektin roskapitoisuus on suhteellisen suuri. Rejektin ohjaaminen ulos prosessista vähentää roskaisuuden rikastumista prosessiin. Sakeamassalajittelun sijoittaminen PK 5:n konekyypin jälkeen vähentää roskien päätymistä paperiin. Hylyn painelajittelun ja PP- laitoksen rejektin ohjaaminen sakeamassalajittelun toiseen portaaseen vähentäisi priimakuitutappiota ja roskien määrää käytetyissä massoissa. Seisokin aikaisen putkilinjojen pesujen lopputulos parani huomattavasti BA- pesuaineen käyttöönoton jälkeen. Kyseisen pesuaine soveltuu liuottamaan putkistosta mm. PK 5:llä esiintyvät uuteaine- ja ASA- saostumat. BSA- sellun pH- säädön lopettamisella oli suuri vähentävä vaikutus tummien täplien esiintymistiheyteen. pH- säädössä BSA- tornin pohjalaimennukseen annosteltu lipeä edesauttoi tummien saostumien syntymistä saippuoiden uuteaineita.

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Diplomityön tarkoituksena oli tutkia ja kehittää menetelmä arvometallien kuten kuparin, sinkin, koboltin ja nikkelin talteenottoon metallikloridiliuoksesta. Tavoitteena oli valita taloudellisin ja ympäristöystävällisin menetelmä, jolla saadaan nämä arvometallit myyntituotteiksi. Lisäksi puhdistetun prosessiveden tuli täyttää asetetut tavoitteet. Kirjallisuustyön perusteella laskettiin viidelle eri prosessivaihtoehdolle ainetaseet HSC Sim 6.0 ohjelmalla, joka on HSC Chemistry-pohjainen prosessien simulointi- ja mallinnusohjelma. Kaikissa vaihtoehdoissa oli ensimmäisenä prosessiosana kuparin, sinkin, koboltin ja nikkelin sulfidisaostus ja sakan pesu. Sulfidisaostusta seurasi vaihtoehtoisesti joko 1) hapetus hapella ja hydroksidisaostus, 2) hapetus vetyperoksidilla ja hydroksidisaostus, 3) pelkkä hydroksidisaostus, 4) hapetus SO2/O2-kaasuseoksella ja hydroksidisaostus tai 5) karbonaattisaostus. Taselaskennan perusteella valittiin kokeelliseen osaan tutkittavat prosessivaihtoehdot, jotka olivat sulfidisaostus, hydroksidisaostus, SO2/O2- hapetus ja hydroksidisaostus sekä karbonaattisaostus. Kokeissa arvometallit saatiin talteenotettua sulfidisaostuksella selektiivisimmin lämpötilassa 55 °C ja pH:ssa 4. Näissä olosuhteissa reagenssin kulutus verrattaessa muihin tehtyihin sulfidisaostuksiin oli pienin. Sakka laskeutui ja suotautui hyvin. Loppusakan sisältämien metallien (kupari, sinkki ja koboltti) pitoisuudet olivat korkeimmat. Myös nikkelin määrä oli suuri. Mangaani ja rauta saatiin talteenotettua selektiivisimmin karbonaattisaostuksella lämpötilassa 65 °C. Sakka sisälsi eniten mangaania. Sakka laskeutui ja suotautui hyvin. Tällä menetelmällä puhdistetun prosessiveden laatu täytti asetetut tavoitteet.

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Well-ordered Georgia kaolinite (Kga-1b) obtained from the source Clay Repository of the Clay Minerals Society (USA) was intercalated with urea using grinding procedures. To achieve complete intercalation 20% of urea (in weight) was used, producing Al2Si2O5(OH)4 (N2H4CO)0,86 with an interplanar basal spacing of 1,08nm. After washing with water under ultrasound stirring at 363K, urea was completely removed and kaolinite was partially exfoliated. After drying under air, the material was converted to hydrated kaolinite with the composition Al2Si2O5(OH)4 (H2O)0,64 and an interplanar basal spacing of 0,84nm. In this compound, water molecules positioned between the layers of the silicate can be removed after calcination at 573K, regenerating structurally disordered kaolinite.

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The xerogel p-anisidinepropylsilica was obtained. This solid presents some residual paraffin and also a small fraction of high organofunctionalized material that was leached in polar solvent. The xerogel purification could be achieved by exhaustively washing with hexane and dichloromethane solvents, or submitting the xerogel to thermal treatment up to 300 ºC, in vacuum. The resulting purified xerogel material present an appreciable thermal stability and resistance to leaching by solvents.

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Well-ordered kaolinite from the Brazilian Amazon Region (State of Pará) was initially reacted at 60 °C with a water dimethylsulfoxide mixture. After washing and characterisation, the resulting material was washed several times with methanol and in the final step with water. The water molecules displace the previously dimethylsulfoxide intercalated molecules and two different hydrated kaolinites were obtained. An unstable phase characterized by an interplanar basal distance of 0,996 nm that after drying collapse to the stable 0,844 nm hydrated kaolinite. The dehydration of the sample to disordered kaolinite was accompanied by Powder X-ray Diffractometry, thermal analysis (simultaneous TG and DSC) and FTIR spectroscopy.

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In this thesis, cleaning of ceramic filter plates clogged by iron oxides was studied. Oxalic acid is considered as the most effective cleaning agent for the plates fouled by iron oxides, but when using oxalic acid, sparingly soluble calcium oxalate may be formed and it can blind the filter media. Suitability of another chemical for cleaning the plates clogged by iron oxides was studied in this thesis. The literature part was mostly about the properties of the chemical, about its reactions, industrial uses, safety issues etc. In the experimental part, the efficiency of the chemical for cleaning of the ceramic plates clogged by iron oxides was studied. Two kinds of plates were used in the experiments; the others were clogged by hematite and the others by magnetite. Both soaking and flow-through experiments were done. A suitable concentration, pH and temperature were tried to find in the experiments. Also the effect of ultrasound was studied. The efficiency of the cleaning was examined by measuring the permeability of the plates during the experiments. ICP-OES analysis was performed for determining the amount of dissolved iron in the washing solution. Some experiments were also done with oxalic acid. The results from the oxalic acid experiments were compared to the results from the experiments with the other chemical. In the experiments with the other chemical, the permeability increased more and the amounts of dissolved iron were larger. According to the results from the experiments, the method of application of the washing solutions had an impact on the washing results.

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Mekaanisen massan peroksidivalkaisussa on perinteisesti käytetty kahta kompleksinmuodostajaa, jotka ovat dietyleenitriamiinipentaetikkahappo (DTPA) ja etyleenidiamiinipentaetikkahappo (EDTA). Kompleksinmuodostajat saavat aikaan hyvän kelatointituloksen muodostamalla valkaisulle haitallisten metalli-ionien kanssa kompleksin ja estäen näin metalli-ionien valkaisutulosta huonontavan vaikutuksen. Perinteiset kompleksinmuodostajat DTPA ja EDTA eivät kuitenkaan ole biohajoavia ja niiden epäillään irrottavan metalleja vesistöjen sedimenteistä. Työssä selvitettiin kolmen eri biohajoavan kompleksinmuodostajan valkaisuteho verrattuna perinteisiin kompleksinmuodostajiin. Laboratoriossa suoritetut pesukokeet osoittivat, että mikään biohajoava kompleksinmuodostaja ei saavuttanut samaa pesutehoa kuin perinteiset kompleksinmuodostajat. Valkaisukokeet kuitenkin osoittivat, että biohajoava kompleksinmuodostaja ISA pääsi hyvin lähelle perinteisten kompleksinmuodostajien valkaisutuloksia suoritettaessa valkaisu siten, että massa esipestään kompleksinmuodostajalla ja sen jälkeen valkaistaan vakiokemikaaliannoksella alkalina ollessa natriumhydroksidi. Kaksi muuta biohajoavaa kompleksinmuodostajaa, ISA+EDDS ja HAS, eivät saavuttaneet samaa tasoa. HAS toimi kyllä stabilaattorina, muttei pystynyt nostamaan massan vaaleutta.

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This work shows some laboratory waste management developed in order to recover some elements or to prepare the waste for a correct final disposal. The 25 elements chosen cover basically all chemical behaviors found for the metals in the Periodic Table. The treatments adopted were based on the classical behavior in aqueous solution (wet chemistry) but an important condition for a full success was the previous knowledge of the qualitative composition of the wastes treated. Some general trends were found: the final liquid waste was always saline and normally presented a higher volume than the original waste; most original wastes were acid in nature; steps such as solid-liquid separation, washing, evaporating and calcining were currently performed. This work was also a very good experience in chemistry in solution for students and showed them the need of treating wastes for a better environment.

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In this technical note, we describe the construction of a low-cost computer controlled device for layer-by-layer film fabrication. The software allows to control multiple material deposition, washing and drying steps and the time for each operation. To test the device, we produced and characterized self-assembled films of conductive polymers by alternating poly(o-methoxyaniline) (POMA) and poly(3-thiophene acetic acid) (PTAA) via the layer-by-layer technique.

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In this work the application of the photo-Fenton process for the treatment of washing water of herbicide containers using solar energy was studied. The influence of the H2O2 concentration and the iron source on the degradation of tebuthiuron and diuron was investigated. The degradation efficiency was strongly affected by the iron source. Using ferrioxalate, total mineralization of diuron and tebuthiuron was obtained either for the individual compounds or for a mixture containing both herbicides, while when using Fe(NO3)3, the maximum mineralization reached for both herbicides was only 50%.

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A simple, fast and low-cost methodology was optimized, seeking preparation of a crude pig liver esterase (PLE) concentrate. Basically, the method consisted of the following steps: liver homogenization, acetone washing, enzyme extraction and purification/concentration. Starting from 1 kg of fresh liver more than 200 kU of PLE suspension were obtained after 8 hours, at an estimated cost of US$0.21/kU. The PLE concentrate thus obtained was stable, showing 96-100% of the initial activity after 7 months in refrigerator at 4°C.

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A comparison between silica by acid leaching of rice husk (RH) and silica obtained from thermal treatment of rice husk ash (RHA) is presented. The best leaching results were obtained using 10% hydrochloric acid followed by washing with water. The alternative method, calcination of RHA at 700 ºC for 6 h followed by grinding for 80 min, was more effective. Silica obtained from RH was about 97% amorphous, had a 17.37 µm mean particle size, and a specific surface area of 296 m²/g. On the other hand, for silica obtained from RHA the values were about 95% amorphous material 0.68 µm, and 81 m²/g.