Roles of keratins in intestinal health and disease

Intermediate filament keratins (K) play a pivotal role in protein targeting and epithelialcytoprotection from stress as evidenced by keratin mutations predisposing to human liver and skin diseases and possibly inflammatory bowel disease (IBD). The K8-null (K8-/-) mice exhibit colonic phenotype similar to IBD and marked spontaneous colitis, epithelial hyperproliferation, decreased apoptosis, mistargeting of proteins leading to defective ion transport and diarrhea. The K8-heterozygote (K8+/-) mouse colon appears normal but displays a defective sodium (Na+) and chloride (Cl-) transport similar to, but milder than K8-/-. Characterization of K8+/- colon revealed ~50% less keratins (K7, K8, K19, K20) compared to K8 wild type (K8+/+). A similar ~50% decrease was seen in K8+/- mRNA levels as compared to K8+/+, while the mRNA levels for the other keratins were unaltered. K8+/- keratins were arranged in a normal colonic crypt expression pattern, except K7 which was expressed at the top of crypts in contrast to K8+/+. The K8+/- colon showed mild hyperplasia but no signs of inflammation and no resistance to apoptosis. Experimental colitis induced by using different concentrations of dextran sulphate sodium (DSS) showed that K8+/- mice are slightly more sensitive to induced colitis and showed a delayed recovery compared to K8+/+. Hence, the K8+/- mouse with less keratins and without inflammation, provided a novel model to study direct molecular mechanisms of keratins in intestinal homeostasis and ion transport. Different candidate ion transporters for a possible role in altered ion transport seen in the K8-/- and K8+/- mouse colon were evaluated. Besides normal levels of CFTR, PAT-1 and NHE-3, DRA mRNA levels were decreased 3-4-fold and DRA protein nearly entirely lost in K8-/- caecum, distal and proximal colon compared to K8+/+. In K8+/- mice, DRA mRNA levels were unaltered while decreased DRA protein level and patchy distribution was detected particularly in the proximal colon and as compared to K8+/+. DRA was similarly decreased when K8 was knocked-down in Caco-2 cells, confirming that K8 levels modulate DRA levels in an inflammation-independent manner. The dramatic loss of DRA in colon and caecum of K8-/- mice was responsible for the chloride transport defect. The milder ion transport in K8+/- colon might be related to DRA suggesting a role for K8 in regulation of DRA expression and targeting. The current study demonstrates the importance of keratins in stress protection and cell signaling. Furthermore, we have also successfully developed a novel, simple, fast, cost effective, non-invasive in vivo imaging method for the early diagnosis of murine colitis with specificity for both genetic and experimental colitis. The said modality provides continuous measurements of reactive oxygen and nitrogen species (RONS) and minimizes the use of an increased number of experimental animals by using a luminal derivative chemiluminescent probe, L-012 which provides a cost-effective tool to study the level and longitudinal progression of colitis.

Production of magnesium carbonates from serpentinites for CO2 mineral sequestration : optimisation towards industrial application

Global warming is one of the most alarming problems of this century. Initial scepticism concerning its validity is currently dwarfed by the intensification of extreme weather events whilst the gradual arising level of anthropogenic CO2 is pointed out as its main driver. Most of the greenhouse gas (GHG) emissions come from large point sources (heat and power production and industrial processes) and the continued use of fossil fuels requires quick and effective measures to meet the world’s energy demand whilst (at least) stabilizing CO2 atmospheric levels. The framework known as Carbon Capture and Storage (CCS) – or Carbon Capture Utilization and Storage (CCUS) – comprises a portfolio of technologies applicable to large‐scale GHG sources for preventing CO2 from entering the atmosphere. Amongst them, CO2 capture and mineralisation (CCM) presents the highest potential for CO2 sequestration as the predicted carbon storage capacity (as mineral carbonates) far exceeds the estimated levels of the worldwide identified fossil fuel reserves. The work presented in this thesis aims at taking a step forward to the deployment of an energy/cost effective process for simultaneous capture and storage of CO2 in the form of thermodynamically stable and environmentally friendly solid carbonates. R&D work on the process considered here began in 2007 at Åbo Akademi University in Finland. It involves the processing of magnesium silicate minerals with recyclable ammonium salts for extraction of magnesium at ambient pressure and 400‐440⁰C, followed by aqueous precipitation of magnesium in the form of hydroxide, Mg(OH)2, and finally Mg(OH)2 carbonation in a pressurised fluidized bed reactor at ~510⁰C and ~20 bar PCO2 to produce high purity MgCO3. Rock material taken from the Hitura nickel mine, Finland, and serpentinite collected from Bragança, Portugal, were tested for magnesium extraction with both ammonium sulphate and bisulphate (AS and ABS) for determination of optimal operation parameters, primarily: reaction time, reactor type and presence of moisture. Typical efficiencies range from 50 to 80% of magnesium extraction at 350‐450⁰C. In general ABS performs better than AS showing comparable efficiencies at lower temperature and reaction times. The best experimental results so far obtained include 80% magnesium extraction with ABS at 450⁰C in a laboratory scale rotary kiln and 70% Mg(OH)2 carbonation in the PFB at 500⁰C, 20 bar CO2 pressure for 15 minutes. The extraction reaction with ammonium salts is not at all selective towards magnesium. Other elements like iron, nickel, chromium, copper, etc., are also co‐extracted. Their separation, recovery and valorisation are addressed as well and found to be of great importance. The assessment of the exergetic performance of the process was carried out using Aspen Plus® software and pinch analysis technology. The choice of fluxing agent and its recovery method have a decisive sway in the performance of the process: AS is recovered by crystallisation and in general the whole process requires more exergy (2.48–5.09 GJ/tCO2sequestered) than ABS (2.48–4.47 GJ/tCO2sequestered) when ABS is recovered by thermal decomposition. However, the corrosive nature of molten ABS and operational problems inherent to thermal regeneration of ABS prohibit this route. Regeneration of ABS through addition of H2SO4 to AS (followed by crystallisation) results in an overall negative exergy balance (mainly at the expense of low grade heat) but will flood the system with sulphates. Although the ÅA route is still energy intensive, its performance is comparable to conventional CO2 capture methods using alkanolamine solvents. An energy‐neutral process is dependent on the availability and quality of nearby waste heat and economic viability might be achieved with: magnesium extraction and carbonation levels ≥ 90%, the processing of CO2‐containing flue gases (eliminating the expensive capture step) and production of marketable products.

Mineraalien rikastusprosessin vesijalanjälki

Mineraalien rikastamiseen käytetään useita fysikaalisia ja kemiallisia menetelmiä. Prosessi sisältää malmin hienonnuksen, rikastuksen ja lopuksi vedenpoistamisen rikastelietteestä. Malmin rikastamiseen käytetään muun muassa vaahdotusta, liuotusta, magneettista rikastusta ja tiheyseroihin perustuvia rikastusmenetelmiä. Rikastuslietteestä voidaan poistaa vettä sakeuttamalla ja suodattamalla. Rikastusprosessin ympäristövaikutuksia voidaan arvioida laskemalla tuotteen vesijalanjälki, joka kertoo valmistamiseen kulutetun veden määrän. Tässä kirjallisuustyössä esiteltiin mineraalien käsittelymenetelmiä sekä prosessijätevesien puhdistusmenetelmiä. Kirjallisuuslähteiden pohjalta selvitettiin Pyhäsalmen kaivoksella valmistetun kuparianodin vesijalanjälki sekä esitettiin menetelmiä, joilla prosessiin tarvittavan raakaveden kulutusta voitaisiin vähentää. Pyhäsalmella kuparirikasteesta valmistetun kuparianodin vesijalanjälki on 240 litraa H2O ekvivalenttia tuotettua tonnia kohden. Pyhäsalmen prosessin raakaveden kulutusta voidaan vähentää lisäämällä sisäistä vedenkierrätystä. Kalsiumsulfaatin saostuminen putkiin ja pumppuihin on ilmentynyt ongelmaksi vedenkierrätyksen lisäämisessä. Kalsiumsulfaattia voidaan erottaa vedestä membraaneihin, ioninvaihtoon ja sähkökemiaan perustuvilla tekniikoilla. Vaihtoehdossa, jossa johdetaan kaikista kolmesta vaahdotuksesta saatavat rikastuslietteen ja rikastushiekan sakeutuksien ylitteet sekä suodatuksien suodosvedet samaan vedenkäsittelyyn voidaan kattaa arviolta noin 65 % koko veden tarpeesta. Raakavettä säästetään vuodessa 3,4 Mm^3 ja samalla rikastushiekka-altaiden tarvittava koko pienenee, joka vähentää ympäristöriskejä.

Metalli-ionin ja hapon erotus toisistaan kalvosuodatuksella

Työn tarkoituksena oli kuparin ja hapon erottaminen toisistaan malliaineliuoksesta membraanitekniikalla. Kaivannaisteollisuudessa happoja käytetään metalleiden liuottamiseen. Lisäksi happamia jätevesiä syntyy sulfidikaivoksissa, sadeveden liuottaessa metalleja. Raskasmetallit ovat erittäin myrkyllistä vesieliöille. Työn tavoitteena oli saada happo ja metalli hyödynnettävään muotoon. Työn kokeellisessa osassa vertailtiin kahta polymeeristä ja keraamista membraania hapon ja metallin erotuksessa. Mittauksissa käytetyt membraanit olivat: AMS Technologies A-3012 ja A-3014 sekä Inopor ® Type SKR. Syöttöliuos sisälsi kuparisulfaattia ja rikkihappoa. Suodatukset tehtiin 30 ºC lämpötilassa useissa paineissa ja pH-arvoissa. Polymeeristen membraanien suodatusnäytteistä saadut retentiot kuparille olivat vastaavia aikaisempien tutkimusten tuloksien kanssa. A-3012 kalvon kuparin retentio oli 95 % ja A-3014 kalvolle kuparin retentio oli 90 %. Lisäksi mittausten korkeimmissa pH-arvoissa (2,9-2,3) happo konsentroitui permeaattiin. Polymeerisillä membraaneilla ei ollut merkkejä kalvon likaantumisesta tai hajoamisesta. Keraamisella membraanilla mitatut tulokset eivät olleet vastaavia aikaisempien tutkimusten tuloksien kanssa. Kuparin retentio olivat 2 ja 20 prosentin välillä, eikä liuoksen pH eronnut syötön ja permeaatin välillä. Tulosten perusteella molemmat tutkitut polymeeriset membraanit soveltuvat kuparin erottamiseen happamasta liuoksesta. Mittauksissa käytetty keraaminen membraani ei sovellu tähän tehtävään.