Reduction of emerging micropollutants, organic matter, nutrients and salinity from real wastewater by combined MBR–NF/RO treatment

To study the possibility of producing better water quality from municipal wastewater, a membrane bioreactor (MBR) pilot plant with flat sheet (FS) and hollow fiber (HF) membranes coupled with another pilot plant equipped with nanofiltration (NF)/reverse osmosis (RO) membranes were operated to treat municipal wastewater from the wastewater treatment plant (WWTP) Rincón de León, Alicante (Spain). This study was focused on improving the quality of the permeate obtained from the MBR process when complemented by NF or RO stages with respect to salinity, organic matter and nutrients. Furthermore, the removal efficiencies of 10 EMPs were evaluated, comparing the reductions achieved between the wastewater treatment by MBR (adsorption to sludge and biodegradation) and the later treatment using NF or RO (mainly size exclusion). The results showed that the high quality of water was obtained which is appropriate for reuse with salinity removal efficiencies higher than 97%, 96% for total organic carbon (TOC), 91% for nitrates View the MathML sourceNO3- and 99% for total phosphorous (TP). High removal efficiencies were obtained for the majority of the analyzed EMP compounds.

Low-temperature isothermal Rankine cycle for desalination

In brackish groundwater desalination, high recovery ratio (of fresh water from saline feed) is desired to minimise concentrate reject. To this effect, previous studies have developed a batch reverse osmosis (RO) desalination system, DesaLink, which proposed to expand steam in a reciprocating piston cylinder and transmit the driving force through a linkage crank mechanism to pressurise batches of saline water (recirculating) in a water piston cylinder unto RO membranes. However, steam is largely disadvantaged at operation from low temperature (< 150oC) thermal sources; and organic working fluids are more viable, though, the obtainable thermal cycle efficiencies are generally low with low temperatures. Consequently, this thesis proposed to investigate the use of organic working fluid Rankine cycle (ORC) with isothermal expansion, to drive the DesaLink machine, at improved thermal efficiency from low temperature thermal sources. Following a review of the methods of achieving isothermal expansion, ‘liquid flooded expansion’ and ‘expansion chamber surface heating’ were identified as potential alternative methods. Preliminary experimental comparative analysis of variants of the heated expansion chamber technique of effecting isothermal expansion favoured a heated plain wall technique, and as such was adopted for further optimisation and development. Further, an optimised isothermal ORC engine was built and tested at < 95oC heat source temperature, with R245fa working fluid – which was selected from 16 working fluids that were analysed for isothermal operation. Upon satisfactory performance of the test engine, a larger (10 times) version was built and coupled to drive the DesaLink system. Operating the integrated ORC-RO DesaLink system, gave freshwater (approximately 500 ppm) production of about 12 litres per hour (from 4000 ppm feed water) at a recovery ratio of about 0.7 and specific energy consumption of 0.34 kWh/m3; and at a thermal efficiency of 7.7%. Theoretical models characterising the operation and performance of the integrated system was developed and utilised to access the potential field performance of the system, when powered by two different thermal energy sources – solar and industrial bakery waste heat – as case studies.

Application of Nanofiltration to the Treatment of Acid mine Drainage Waters

This study investigated the separation of uranium and other elements in high concentrations from acid mine waters at Caldas Uranium Mining, in the southeast of Brazil, using nanofiltration membranes. Nanofiltrarion is widely used in water treatment due to the lower energy requirements and higher yields than reverse osmosis. Separation characteristics are dependent on both the molecular size and charge of the dissolved species in the feed solution as well as membrane properties. In this investigation the potential of nanofiltration to removed dissolved species like uranium from acid mine water drainage was measured. Two composite aromatic polyamide commercially membranes of FilmTec/Dow were tested and it found that uranium rejections of greater than 90% and also showed potential for the separation of aluminum and manganese.

Betalain rich functional extract with reduced salts and nitrate content from red beetroot (Beta vulgaris L.) using membrane separation technology

An initial laboratory-scale evaluation of separation characteristics of membranes with nominal molecular weight cut-offs (NMWCO) ranging from 30 kD down to 0.5 kD indicated effective separation of betalains in the 0.5 kD region. Subsequent pilot-level trials using 1 kD, loose reverse osmosis (LRO) and reverse osmosis (RO) spiral-wound membranes showed LRO membrane to be very efficient with up to 96% salt and 47% other dissolved solids removed while retaining majority of the pigment (∼98%) in the betalain rich extract (BRE). The total betalain content in the BRE increased up to 46%, the highest recovery reported so far at pilot scale level. Interestingly, more than 95% of the nitrates were removed from the BRE after the three diafiltrations. These studies indicate that membrane technology is the most efficient technique to produce BRE with highly reduced amounts of salts and nitrate content.

A test of the ash-free dry weight technique on the developmental stages of Patiriella spp. (Echinodermata : Asteroidea)

Determination of the ash-free dry weight (AFDW) of marine specimens requires samples to be rinsed, soaked, and centrifuged. Problems associated with this technique were examined with the developmental stages of seastar species (Patiriella) with different modes of development. The influence of three rinsing solutions (ammonium formate [AF], filtered seawater [FSW], and reverse osmosis water [RO]) was assessed. The hypothesis that the AFDW technique is a measure of organic material was addressed by drying inorganic salts. Developmental stages of Patiriella calcar rinsed in FSW were twice as heavy as those rinsed in RO or AE indicating that samples should be rinsed in RO or AF before weighing. Soaking treatments had a significant effect on the AFDW of samples of P. calcar (planktonic developer), indicating that the rinsing period should be brief. Zygotes of Patiriella re gularis (planktonic developer) were significantly heavier than ova or gastrulae, regardless of treatment. In contrast, there were no significant differences in the AFDW of any stages or treatments of Patiriella exigua (benthic developer). This may be due to the presence of a modified fertilization envelope, which protects these benthic embryos. Inorganic salts with water of crystallization and FSW lost 20-75% and 14% of their dry weight, respectively, after ashing. We propose that salt ions may retain water, which does not evaporate during drying but is lost during ashing, resulting in the overestimation of sample AFDW. If a similar process occurs in the developmental stages of marine invertebrates, changes in the intracellular ionic composition through development may result in inaccurate estimates of biomass.

Estudo da cinética e influência dos métodos de secagem sobre as propriedades físico-químicas de soro de leite

O soro de leite é um subproduto da fabricação do queijo, seja por acidificação ou por processo enzimático. Em condições ideais, a caseína do leite se agrega formando um gel, que posteriormente cortado, induz a separação e liberação do soro. É utilizado de diversas formas em toda a indústria alimentícia, possui rica composição em lactose, sais minerais e proteínas. A desidratação é um dos principais processos utilizados para beneficiamento e transformação do soro. Diante disto, o objetivo deste trabalho foi avaliar a influência dos métodos de secagem: liofilização, leito de espuma (nas temperaturas de 40, 50, 60, 70 e 80ºC) e spray-dryer (nas temperaturas de 55, 60, 65, 70 e 75ºC), sobre as características de umidade, proteína, cor e solubilidade do soro, bem como estudar o seu processo de secagem. O soro foi obtido e desidratado após concentração por osmose reversa, testando 11 tratamentos, em 3 repetições, utilizando um delineamento inteiramente casualizado. Os resultados demonstraram que o modelo matemático que melhor se ajustou foi o modelo de Page, apresentado um coeficiente de determinação ajustado acima de 0,98 e erro padrão da regressão em todas as temperaturas abaixo de 0,04 para o método por leito de espuma. Para o método de liofilização os respectivos valores foram 0,9975 e 0,01612. A partir disso, pode-se elaborar um modelo matemático generalizado, apresentando um coeficiente de determinação igual a 0,9888. No caso do leito de espuma, observou-se que à medida que se aumenta a temperatura do ar de secagem, o tempo de secagem diminui e os valores do coeficiente de difusão efetiva aumentam. Porém, a redução no tempo de secagem entre os intervalos de temperatura, diminui com o aumento da mesma. A energia de ativação para a difusão no processo de secagem do soro foi de 26,650 kJ/mol e para todas as avaliações físico-químicas e tecnológicas, a análise de variância apresentou um valor de F significativo (p<0,05), indicando que há pelo menos um contraste entre as médias dos tratamentos que é significativo.

Recuperação parcial da água de lavagem dos filtros utilizados no tratamento da água de piscinas de uso público

Mestrado em Engenharia Química. Ramo optimização energética na indústria química

Dialyse et écologie: est-il possible de faire mieux à l'avenir [Dialysis and ecology: can we do better in the future?].

Development of dialysis has saved the lives of many patients. However, haemodialysis and peritoneal dialysis are very demanding in resources such as water and electricity, and generate a large amount of waste. In this article, we will review the environmental aspects of dialysis. Different solutions will be discussed, such as recycling of water discharged during reverse osmosis, the integration of solar energy, recycling of waste plastics, and the use of other techniques such as sorbent dialysis. In a world where natural resources are precious and where global warming is a major problem, it is important that not only dialysis, but all branches of medicine become more attentive to ecology.

Bioelectrochemical Treatment of Contaminated Groundwater

To remove these pollutants from groundwater, different technologies can be used. Currently, the Environmental Protection Agency (EPA) considers ion exchange, reverse osmosis and reverse electrodialysis to be effective methods for the decrease of their concentrations, below their limit in drinking water. These technologies have some drawbacks, such as low selectivity towards the target pollutant, high energy or chemicals requirements, and the generation of waste brine (pollutants are separated from water, not treated), which require an additional treatment. Bio Electro Chemical Systems (BES) could fill this niche

Voimalaitoksen palamisilman esilämmittimen sisäpuolisen korroosion hallinta pinta-aktiivisten amiinien avulla

Useat voimalaitokset käyttävät hiiliteräksistä valmistettuja palamisilman esilämmittimiä, joissa höyrykattilan palamisilmaa lämmitetään matalapainehöyryllä. Joissakin tapauksissa esilämmittimet ovat kärsineet sisäpuolisen korroosion aiheuttamista putkirikoista. Tämän työn tavoitteena oli selvittää korroosiovaurioiden aiheuttajat ja tarkastella eri keinoja uusien korroosiovaurioiden ehkäisemiseksi. Keskeisimpänä uusien vaurioiden ehkäisykeinona tarkastellaan pinta-aktiivisia amiineja sisältäviä höyrykattilan jälkiannostelukemikaaliseoksia, joista tarkemman tarkastelun kohteena on kaupallinen Helamin 90 H Turb- kemikaaliseos. Pääasialliseksi korroosion aiheuttajaksi on usein epäilty höyryn sisältämää hiilidioksidia. Uusimpien näkemysten mukaan orgaaniset hapot, pääasiassa etikka- ja muurahaishappo ovat kuitenkin hiilidioksidia voimakkaampia korroosion aiheuttajia ilmanesilämmittimissä. Orgaaniset hapot väkevöityvät höyryn lauhtumisen alkaessa muodostuviin lauhdepisaroihin ja alentavat pH-tasoa radikaalisti. pH-tason aleneminen nopeuttaa metallipintoja suojaavan magnetiitin liukenemista ja vaikeuttaa myös sen uusiutumista. Orgaanisia happoja ja hiilidioksidia muodostuu orgaanisten aineiden osittaisessa hajoamisessa höyrykattilan vesi-höyrypiirissä. Pääasialliset orgaanisten aineiden lähteet ovat lisäveden mukana kattilaan kulkeutuva luonnon orgaaninen aines ja käytetyt orgaaniset jälkiannostelukemikaalit. Orgaanisten aineiden kuormaa voidaan pienentää parantamalla lisäveden valmistusprosessin orgaanisten aineiden erotustehokkuutta esimerkiksi käänteisosmoosilla. Mikäli lisäveden laadun parantaminen ei ole järkevästi toteutettavissa, voidaan orgaanisten jälkiannostelukemikaalien oikeanlaisella käytöllä neutraloida orgaanisten happojen vaikutus ilmanesilämmittimissä. Tehokkaimmaksi korroosion hillitsijäksi suoritettujen mittausten perusteella osoittautuivat kemikaaliseokset, jotka sisältävät alkaloivien amiinien lisäksi kalvoa muodostavaa pinta-aktiivista amiinia.

Lannoitetehtaan prosessivesien käsittelyvaihtoehtojen soveltuvuuden arviointi

Phosphorus and nitrogen cause eutrophication of water bodies, causing severe damage to the ecosystem. Eutrophication of the waters causes oxygen depletion, which in turn increases fish mortality, releasing toxins in waters. The released toxins can cause damage to animals and humans, which is the reason in many countries to set emission limits for waste water. Nutrients exist naturally, but due to human activities there is high nutrient leaching to water bodies. Human activity is one of the main reasons to the eutrophication. The aim of this thesis was to estimate the suitability of different water treatment options for Yara Finland’s fertilizer plant’s process waters in Siilinjärvi. The fertilizer plant process waters are high concentrate and especially nitrogen concentrations are high, which bring challenge to the treatment. At the theoretical part was investigated conventional and as well advanced wastewater treatment methods like reverse osmosis, adsorption and ion exchange. Beside different treatment methods corporate environmental requirements, responsibility and strategies were researched. At the empirical part of the thesis the goal was to find out possibil-ities to intensify the efficiency of purification at lamella clarifier with chemical precipitation. In addition possibility to use already existing chemical purifying plant for process waters was estimated. As a result of the research Yara has a possibility to intensify lamella clarifier’s action by addi-tion of calcium hydroxide and thus to obtain the phosphorus and fluorine to precipitate out of the water. But in practice this would be too expensive. It is possible to eliminate nitrogen compounds by adsorption or ammonia stripping, both methods requires additional testing. It is possible to process waters in chemical purifying plant, if ammonium nitrogen has been reduced before. Reverse osmosis is possible to exploit for the phosphoric acid plant’s waters.

Comparison of sustainability of technologies for water desalination

The aim of this work is to perform an in-depth overview on the sustainability of several major commercialized technologies for water desalination and to identify the challenges and propose suggestions for the development of water desalination technologies. The overview of those technologies mainly focuses on the sustainability from the viewpoint of total capital investment, total product cost, energy consumption and global warming index. Additionally, a systematic sustainability assessment methodology has been introduced to validate the assessment process. Conclusions are:1) Reverse osmosis desalination (RO) plants are better than multi-stage flash distillation (MSF) desalination plants and multiple-effect distillation (MED) desalination plants from the viewpoint of energy consumption, global warming index and total production cost; 2)Though energy intensive, MSF plants and MED plants secure their advantages over RO plants by lower total capital investment, wider applicability and purer water desalted and they are still likely to flourish in energy-rich area;3) Water production stage and wastewater disposal stage are the two stages during which most pollutant gases are emitted. The water production stage alone contributes approximately 80~90% of the total pollutant gases emission during its life cycle; 4)The total capital cost per m3 desalted water decreases remarkably with the increasing of plant capacity. The differences between the capital cost per m3 desalted water of RO and other desalination plants will decrease as the capacity increases; 5) It is found that utilities costs serve as the major part of the total product cost, and they account for 91.16%, 85.55% and 71.26% of the total product cost for MSF, MED and RO plants, respectively; 6) The absolute superiority of given technology depends on the actual social-economic situation (energy prices, social policies, technology advancements).

Ravinnepitoisen teollisen jäteveden tuotteistaminen

Tässä työssä selvitettiin ravinnepitoisen jäteveden väkevöintiä erityisesti ammoniumtypen ja orgaanisten happojen osalta. Konsentrointiin käytettiin pääasiassa käänteisosmoosia sekä haihdutusta, mutta myös nanosuodatusta tutkittiin. Jätevesi oli Honkajoki Oy:n lauhdevettä. Kirjallisuusosassa esiteltiin Honkajoki Oy:n toimintaa, membraanierotus-prosesseja, lihantuotannossa syntyvän jätteen ominaisuuksia sekä sen puhdistamista. Keskeisimmät suodatukset tehtiin DOW FILMTEC SW30HR -membraanilla, ja käytetty laitteisto oli DSS LabStak M20. Suodatuksia tehtiin eri pH-olosuhteissa typen ja orgaanisten happojen erottumisen kannalta optimaalisten olosuhteiden löytämiseksi. Lisäksi tutkittiin, kuinka puhtaaksi permeaatti voidaan saada uudelleensuodatuksen avulla. Työssä käytettiin myös haihdutusta lauhteen väkevöintiin. Ammoniumtypen konsentroituminen suodatuksissa oli tehokkainta pH:n ollessa 7 tai sen alle. Kaksivaiheisella suodatuksella permeaatin laatu alitti selvästi Karvianjokeen laskettaville jätevesille asetetut laatu- ja kuormitusrajat. Yhdistämällä suodatus- ja haihdutusprosessit, pystyttiin valmistamaan liuosta, jonka ammoniumtyppipitoisuus oli noin 7,6 %. Tuolloin suodatus tehtiin pH 7:ssä ja haihdutus pH 3:ssa rotavaporilla 26 mbar paineessa ja 50 °C lämpötilassa. Syöttöliuoksen tilavuuden alenema oli noin 65-kertainen. Haihdutuksessa muodostuneessa lauhteessa oli paljon orgaanisia happoja ja käytännössä ei lainkaan ammoniumtyppeä. Tuotejakeita saatiin siten kaksi kappaletta: ammoniumtyppijae ja orgaanisia happoja sisältävä jae.

Maximizing of water recovery in nanofiltration of mine process waters by using antiscalants

Reverse osmosis and nanofiltration are among the most effective and widely used desalination and water softening technologies. They can also be used to treat mining wastewaters and are capable of producing water of extremely high purity, regardless of the high concentrations of toxic heavy metals and extreme pH and salinity. However, challenges with recovering the salts and metals from mining wastewaters in exploitable form, as well as problems with scaling still limit the process efficiency and the ratio of purified water recoverable from process waters. To address the problem of membrane scaling caused by calcium sulfate, batch filtration experiments with the Desal-5 DL nanofiltration membrane, three commercial antiscalants and actual mine process water from a copper mine were performed. The aim of these experiments was to find process conditions where maximum water recovery would be achieved before significant scaling or irreversible membrane fouling would occur and to further improve water recovery by addition of antiscalants. Water recovery of 70 % was reached with the experimental setups by optimizing process conditions. PC-504T antiscaling agent was determined to be the most effective of the three antiscalants used and the addition of 5 ppm of PC-504T allowed the water recovery to be further increased from 70 % to 85 % before major scaling was observed. In these conditions 92 % calcium rejection was achieved.

Kartonkikoneen tuoreveden käytön vähentäminen kemiallisesti puhdistettua jätevesikirkastetta hyödyntäen

Tämän diplomityön tarkoituksena oli tutkia mahdollisuutta hyödyntää kemiallisesti puh-distettua jätevettä prosessivetenä. Vedensäästöpotentiaalin perusteella tutkimuskohteeksi valittiin kartonkikone 4. Tutkimuksen tavoite oli tuoreveden käytön ja jätevesipäästöjen vähentäminen Stora Enso Imatran tehtailla. Työn kirjallisuusosa keskittyy kemialliseen jätevedenkäsittelyyn, kartonkikoneen veden käyttöön ja prosessiveden laatuun vaikuttaviin tekijöihin. Työn kokeellisessa osassa laa-dittiin vesitase tuoreveden käyttökohteiden ja veden tarpeen määrittämiseksi. Kemialli-sesti puhdistetun jäteveden ja prosessiveden ominaisuudet määritettiin, jotta saatiin sel-ville ne ominaisuudet, jotka voisivat estää jätevesikirkasteen hyötykäytön. Laboratoriomääritykset osoittivat, että hyötykäytön esteenä ovat jätevesikirkasteen kiin-toaine-, sulfaatti- ja karbonaattipitoisuus sekä mikrobitaso ja väri. Metallien ja suolaionien haittavaikutusten selvittäminen vaatii lisätutkimusta. Lisäpuhdistusmenetelmien avulla, kuten käänteisosmoosi, jätevesikirkasteen laatu saataisiin vastaamaan prosessiveden tasoa ja hyötykäyttö olisi mahdollista myös kartonkikone 4:n ulkopuolella.