Uuttoprosessin suunnittelu

Teknologian kehitys ja prosessien tiukempi valvonta ovat alentaneet selluteollisuuden häviöitä tehden prosesseista suljetumpia. Valitettavasti nämä edistysaskeleet teknologiassa ovat lisänneet prosessiin kuulumattomien yhdisteiden määrää kemikaalien talteenottokierrossa. Näistä kemikaaleista haitallisimpia ovat kloridi- ja kaliumyhdisteet, jotka tulevat prosessiin raaka-aineiden ja prosessikemikaalien mukana. Kloridi ja kalium muodostavat emäksisissä liuoksissa epäorgaanisia liukoisia yhdisteitä, jotka rikastuvat lipeäkiertoon. Soodakattilassa kloridien läsnäolo alentaa tuhkan sulamislämpötilaa sekä tarttumispistettä, lisää korroosiota ja saostumien muodostumista kattilan pinnalle. Nämä seuraukset voivat vähentää vuosituotantoa ja nostaa korjauskustannuksia. Kaliumin ja kloridin rikastumista talteenottokiertoon voidaan estää poistamalla ne prosessista. Prosessiin kuulumattomat yhdisteet tulisi poistaa talteenottoprosessista ja säilyttää samalla korkea kemikaalien talteenottoprosentti. Koska kaliumin ja kloridin rikastumiskertoimet soodakattilan tuhkassa ovat korkeita, on tuhkan käsittely tehokasta. Kloridin ja kaliumin poistoon on kehitetty menetelmiä, joilla voidaan vähentää hyödyllisten kemikaalien häviöitä. Näitä menetelmiä ovat uutto, ioninvaihto, elektrodialyysi, jäähdytyskiteytys ja haihdutuskiteytys. Menetelmissä tuhka jaetaan kloridi- ja kaliumpitoiseen osaan ja natriumsulfaattipitoiseen osaan. Kloridi ja kalium poistetaan prosessista ja loput palautetaan lipeäkiertoon. Kloridin ja kaliumin poistoa tuhkasta tutkittiin uuttamalla tuhkaa vedellä. Parhaissa käyttöolosuhteissa natriumsulfaatin liukoisuus veteen on huomattavasti alhaisempi kuin kaliumkloridin liukoisuus veteen. Optimaalinen uuttolämpötila ja tuhka-vesisuhde määritettiin siten, että kloridi- ja kaliumpitoisuudet suodoksessa olivat mahdollisimman korkeat sekä natriumin ja muiden anioneiden pitoisuudet suodoksessa mahdollisimman alhaiset. Saatuja tuloksia käytettiin jatkuvatoimisen uuttoprosessin suunnittelussa.

Lipeäkierron kemiallisesti parhaat käytännöt

Diplomityön tavoitteena oli kartoittaa kemiallisesti parhaita käytäntöjä sellutehtaiden kemikaalien talteenottoprosessissa. Kirjallisuudesta ei löytynyt lipeäkiertoon liittyvää kemiallista tietoutta. Laiteteknisten ratkaisujen kautta yritettiin saada selville parhaat käytännöt. Teoriaosassa on myös käsitelty lipeäkierrossa esiintyvien vierasaineiden lähteitä, rikastumista ja poistumista prosessista. Työ tehtiin Stora Enson Suomessa sijaitseville tehtaille. Kokeellisessa osassa on suoritettu tehtailta saadun materiaalin perusteella tunnuslukujen laskentaa sekä PCA-analyysin teko. Työssä tarkastelualueena on lipeäkierto liuottajasta meesauuniin. Kaukopäässä on käytössä lipeäkierrossa kaksi lipeälinjaa ja muilla tehtailla vain yksi. Saatujen tunnuslukujen perusteella tehtaille on annettu pisteitä nollasta viiteen. Viisi pistettä on saanut parhaan arvon saanut tehdas ja nolla pistettä kaukana parhaasta arvosta olevat. Tunnuslukuja on valittu 14 ja edellä esitetyllä tavalla pisteytettynä on parhaaksi tehtaaksi saatu Kaukopään 1-lipeälinja ja huonoin on Kemijärvi. Huomioitavaa on Kaukopään 2-lipeälinjan sijoittuminen vasta neljänneksi, vaikka lipeälinjoilla on valkolipeän ja meesan käsittelyssä yhteiset syöttösäiliöt. PCA-analyysin perusteella havaittiin, että kuukausikeskiarvoja käytettäessä tulokset tasoittuvat verrattuna päiväarvoilla tehtyyn analyysiin. Analyysi osoittaa, että tehtailla lipeäkierto ei ole täysin hallinnassa. Tämä ilmenee suurina objektien liikkeinä kuvissa. Päiväarvoilla analyysi tehtiin vain Oulun tehtaalle. Tarkastelussa valittiin kuukauden mittainen ajanjakso niin hyvää kuin huonoakin jaksoa. Mallien selitysasteista voidaan nähdä eroja hyvän ja huonon jakson välillä. Tämä ilmenee niin, että hyvän jakson mallin selitysaste on korkeampi kuin huonon jakson. Objektien sijoittuminen kuvissa on myös erilainen. Hyvän jakson aikana objektit ovat pieninä ryhminä, kun huonon jakson objektit ovat hajonneet yksittäisiksi arvoiksi ja päivien väliset erot ovat suuret.

Polysulfidiprosessi sulfaattisellutehtaassa

Kandidaatintyön tavoitteena on kartoittaa merkittävimmät muutokset sellutehtaalla siirryttäessä sulfaattimassan valmistuksesta polysulfidiselluprosessiin. Työssä esitellään sulfaattisellun valmistusprosessi ja polysulfidin vaatimat muutokset selluprosessissa erityisesti höyrynkulutuksen kannalta. Sellutehtaan höyrynkulutusta ja sen mahdollisia muutoksia tarkastellaan suhteessa tehtaan selluntuotantoon. Tutkimus tehdään tutustuen dokumenttilähteisiin sekä erityisesti hankkimalla lisätietoa ja käytännön näkemystä asiantuntijahaastatteluista. Työssä käytetään esimerkkinä tyypillistä modernia sellutehdasta, jonka perusteella tarkasteltavat osaprosessit ovat valikoituneet. Sulfaattiprosessiin tehtävät muutokset käsittävät keittolipeän muuttamisen polysulfidipitoiseksi, polysulfidin valmistusprosessin (MOXY) sekä keiton muuttamisen siten, että polysulfidin vaikutus voidaan maksimoida. Polysulfidiprosessi vaikuttaa merkittävästi lipeäkiertoon, keittämöön sekä kuivauskoneeseen. Muilla osastoilla ominaishöyrynkulutuksen odotetaan pysyvän tavanomaista sulfaattiprosessia vastaavalla tasolla. Höyrynkulutuksella on huomattava merkitys modernin sellutehtaan tuotanto- ja kustannustehokkuuteen, sillä säästetyllä ylijäämähöyryllä voidaan tuottaa myyntisähköä. Uusiutuvan energian tuottajana ja ympäristövastuullisena toimijana sellutehtaiden on järkevää pyrkiä vähentämään omaa höyrynkulutustaan ja lisäämään sitä kautta sähköntuotantoaan.

Polysulfidiprosessin vaikutukset höyrynkulutukseen sulfaattisellutehtaassa

Diplomityön tavoitteena on kartoittaa höyrynkulutuksen merkittävimmät muutokset sellutehtaalla siirryttäessä sulfaattimassan valmistuksesta polysulfidiselluprosessiin. Työssä esitellään sulfaattisellun valmistusprosessi ja polysulfidin vaatimat muutokset selluprosessissa erityisesti höyrynkulutuksen kannalta. Sellutehtaan höyrynkulutusta ja sen mahdollisia sekä todennettuja muutoksia tarkastellaan suhteessa tehtaan selluntuotantoon. Diplomityössä analysoidaan muutoksiin johtaneita syitä ja erityisesti peilataan niitä ennalta odotettuihin muutoksiin, joita kandidaatintyö ”Polysulfidiprosessi sulfaattisellutehtaassa” (Szepaniak 2014) esitti kirjallisuuden pohjalta. Tutkimus tehdään tutustuen dokumenttilähteisiin sekä erityisesti hankkimalla lisätietoa ja käytännön näkemystä asiantuntijahaastatteluista. Työssä käytetään esimerkkinä tyypillistä modernia sellutehdasta, jonka perusteella tarkasteltavat osaprosessit ovat valikoituneet. Tutkimustulosten perusteella esitetään jatkotutkimus- ja kehityskohteita. Sulfaattiprosessiin tehtävät muutokset käsittävät keittolipeän muuttamisen polysulfidipitoiseksi, polysulfidin valmistusprosessin (MOXY) sekä keiton muuttamisen siten, että polysulfidin vaikutus voidaan maksimoida. Polysulfidiprosessi vaikuttaa merkittävästi lipeäkiertoon ja keittämöön. Keittämön höyrynkulutus kasvaa, haihduttamon kuorma vähenee ja soodakattilan lämmöntuotanto heikkenee. Muilla osastoilla ominaishöyrynkulutuksen muutokset ovat tilastollisesti merkityksettömiä. Höyrynkulutuksella on huomattava merkitys modernin sellutehtaan tuotanto- ja kustannustehokkuuteen, sillä säästetyllä ylijäämähöyryllä voidaan tuottaa myyntisähköä. Uusiutuvan energian tuottajana ja ympäristövastuullisena toimijana sellutehtaiden on järkevää pyrkiä vähentämään omaa höyrynkulutustaan ja lisäämään sitä kautta sähköntuotantoaan.

Black liquor gasification combined cycle with CO2 capture-Technical and economic analysis

Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

Behavior of black liquor nitrogen in combustion : formation of cyanate

The Kraft pulping process is the dominant chemical pulping process in the world. Roughly 195 million metric tons of black liquor are produced annually as a by-product from the Kraft pulping process. Black liquor consists of spent cooking chemicals and dissolved organics from the wood and can contain up to 0.15 wt% nitrogen on dry solids basis. The cooking chemicals from black liquor are recovered in a chemical recovery cycle. Water is evaporated in the first stage of the chemical recovery cycle, so the black liquor has a dry solids content of 65-85% prior to combustion. During combustion of black liquor, a portion of the black liquor nitrogen is volatilized, finally forming N2 or NO. The rest of the nitrogen remains in the char as char nitrogen. During char conversion, fixed carbon is burned off leaving the pulping chemicals as smelt, and the char nitrogen forms mostly smelt nitrogen (cyanate, OCN-). Smelt exits the recovery boiler and is dissolved in water. The cyanate from smelt decomposes in the presence of water, forming NH3, which causes nitrogen emissions from the rest of the chemical recovery cycle. This thesis had two focuses: firstly, to determine how the nitrogen chemistry in the recovery boiler is affected by modification of black liquor; and secondly, to find out what causes cyanate formation during thermal conversion, and which parameters affect cyanate formation and decomposition during thermal conversion of black liquor. The fate of added biosludge nitrogen in chemical recovery was determined in Paper I. The added biosludge increased the nitrogen content of black liquor. At the pulp mill, the added biosludge did not increase the NO formation in the recovery boiler, but instead increased the amount of cyanate in green liquor. The increased cyanate caused more NH3 formation, which increased the NCG boiler’s NO emissions. Laboratory-scale experiments showed an increase in both NO and cyanate formation after biosludge addition. Black liquor can be modified, for example by addition of a solid biomass to increase the energy density of black liquor, or by separation of lignin from black liquor by precipitation. The precipitated lignin can be utilized in the production of green chemicals or as a fuel. In Papers II and III, laboratory-scale experiments were conducted to determine the impact of black liquor modification on NO and cyanate formation. Removal of lignin from black liquor reduced the nitrogen content of the black liquor. In most cases NO and cyanate formation decreased with increasing lignin removal; the exception was NO formation from lignin lean soda liquors. The addition of biomass to black liquor resulted in a higher nitrogen content fuel mixture, due to the higher nitrogen content of biomass compared to black liquor. More NO and cyanate were formed from the fuel mixtures than from pure black liquor. The increased amount of formed cyanate led to the hypothesis that black liquor is catalytically active and converts a portion of the nitrogen in the mixed fuel to cyanate. The mechanism behind cyanate formation during thermal conversion of black liquor was not clear before this thesis. Paper IV studies the cyanate formation of alkali metal loaded fuels during gasification in a CO2 atmosphere. The salts K2CO3, Na2CO3, and K2SO4 all promoted char nitrogen to cyanate conversion during gasification, while KCl and CaCO3 did not. It is now assumed that cyanate is formed when alkali metal carbonate or an active intermediate of alkali metal carbonate (e.g. -CO2K) reacts with the char nitrogen forming cyanate. By testing different fuels (bark, peat, and coal), each of which had a different form of organic nitrogen, it was concluded that the form of organic nitrogen in char also has an impact on cyanate formation. Cyanate can be formed during pyrolysis of black liquor, but at temperatures 900°C or above, the formed cyanate will decompose. Cyanate formation in gasifying conditions with different levels of CO2 in the atmosphere was also studied. Most of the char nitrogen was converted to cyanate during gasification at 800-900°C in 13-50% CO2 in N2, and only 5% of the initial fuel nitrogen was converted to NO during char conversion. The formed smelt cyanate was stable at 800°C 13% CO2, while it decomposed at 900°C 13% CO2. The cyanate decomposition was faster at higher temperatures and in oxygen-containing atmospheres than in an inert atmosphere. The presence of CO2 in oxygencontaining atmospheres slowed down the decomposition of cyanate. This work will provide new information on how modification of black liquor affects the nitrogen chemistry during thermal conversion of black liquor and what causes cyanate formation during thermal conversion of black liquor. The formation and decomposition of cyanate was studied in order to provide new data, which would be useful in modeling of nitrogen chemistry in the recovery boiler.

Economic and technical feasibility study of a combined-cycle cogeneration system associated with cellulose plants

In this paper, is presented an economical and technical feasibility study of a combined cycle cogeneration system proposed to be used in a pulp plant located in Brazil, where around 95% of country's pulp production is done by the use of Kraft Process. This process allows the use of black liquor and other by-products as fuel. This study is based upon actual data from a pulp plant with a daily production of 1000 tons., that generates part of the energy demanded by the process in a conventional cogeneration system with condensing steam turbine and two extractions. The addition of a gas turbine was studied to compare electricity production level and its related costs between original system and the new one, considering that the former can use industrial by-products and firewood as fuel, when required. Several parameters related to electric generation systems operation and production costs were studied. The use of natural gas in the combined cycle, in comparison with the use of firewood in the conventional system was studied. The advantages of natural gas fuel are highlighted. The surplus availability and the electricity generation costs are presented as a function of pulp and black liquor production.

Use of stable-isotope probing, full-cycle rRNA analysis, and fluorescence in situ hybridization-microautoradiography to study a methanol-fed denitrifying microbial community

A denitrifying microbial consortium was enriched in an anoxically operated, methanol-fed sequencing batch reactor (SBR) fed with a mineral salts medium containing methanol as the sole carbon source and nitrate as the electron acceptor. The SBR was inoculated with sludge from a biological nutrient removal activated sludge plant exhibiting good denitrification. The SBR denitrification rate improved from less than 0.02 mg of NO3-.N mg of mixed-liquor volatile suspended solids (MLVSS)(-1) h(-1) to a steady-state value of 0.06 mg of NO3-.N mg of MLVSS-1 h(-1) over a 7-month operational period. At this time, the enriched microbial community was subjected to stable-isotope probing (SIP) with [C-13] methanol to biomark the DNA of the denitrifiers. The extracted [C-13]DNA and [C-12]DNA from the SIP experiment were separately subjected to full-cycle rRNA analysis. The dominant 16S rRNA gene phylotype (group A clones) in the [C-13]DNA clone library was closely related to those of the obligate methylotrophs Methylobacillus and Methylophilus in the order Methylophilales of the Betaproteobacteria (96 to 97% sequence identities), while the most abundant clone groups in the [C-12]DNA clone library mostly belonged to the family Saprospiraceae in the Bacteroidetes phylum. Oligonucleotide probes for use in fluorescence in situ hybridization (FISH) were designed to specifically target the group A clones and Methylophilales (probes DEN67 and MET1216, respectively) and the Saprospiraceae clones (probe SAP553). Application of these probes to the SBR biomass over the enrichment period demonstrated a strong correlation between the level of SBR denitrification and relative abundance of DEN67-targeted bacteria in the SBR community. By contrast, there was no correlation between the denitrification rate and the relative abundances of the well-known denitrifying genera Hyphomicrobium and Paracoccus or the Saprospiraceae clones visualized by FISH in the SBR biomass. FISH combined with microautoradiography independently confirmed that the DEN67-targeted cells were the dominant bacterial group capable of anoxic [C-14] methanol uptake in the enriched biomass. The well-known denitrification lag period in the methanol-fed SBR was shown to coincide with a lag phase in growth of the DEN67-targeted denitrifying population. We conclude that Methylophilales bacteria are the dominant denitrifiers in our SBR system and likely are important denitrifiers in full-scale methanol-fed denitrifying sludges.

Efficient and stable nitritation and denitritation of ammonium-rich sludge dewatering liquor using an SBR with continuous loading

Separate treatment of dewatering liquor from anaerobic sludge digestion significantly reduces the nitrogen load of the main stream and improves overall nitrogen elimination. Such ammonium-rich wastewater is particularly suited to be treated by high rate processes which achieve a rapid elimination of nitrogen with a minimal COD requirement. Processes whereby ammonium is oxidised to nitrite only (nitritation) followed by denitritation with carbon addition can achieve this. Nitrogen removal by nitritation/denitritation was optimised using a novel SBR operation with continuous dewatering liquor addition. Efficient and robust nitrogen elimination was obtained at a total hydraulic retention time of 1 day via the nitrite pathway. Around 85-90% nitrogen removal was achieved at an ammonium loading rate of 1.2 g NH4+-N m(-3) d(-1). Ethanol was used as electron donor for denitritation at a ratio of 2.2gCODg(-1) N removed. Conventional nitritation/denitritation with rapid addition of the dewatering liquor at the beginning of the cycle often resulted in considerable nitric oxide (NO) accumulation during the anoxic phase possibly leading to unstable denitritation. Some NO production was still observed in the novel continuous mode, but denitritation was never seriously affected. Thus, process stability can be increased and the high specific reaction rates as well as the continuous feeding result in decreased reactor size for full-scale operation. (c) 2006 Elsevier Ltd. All rights reserved.

Interplay Between Cell Growth And Cell Cycle In Plants.

The growth of organs and whole plants depends on both cell growth and cell-cycle progression, but the interaction between both processes is poorly understood. In plants, the balance between growth and cell-cycle progression requires coordinated regulation of four different processes: macromolecular synthesis (cytoplasmic growth), turgor-driven cell-wall extension, mitotic cycle, and endocycle. Potential feedbacks between these processes include a cell-size checkpoint operating before DNA synthesis and a link between DNA contents and maximum cell size. In addition, key intercellular signals and growth regulatory genes appear to target at the same time cell-cycle and cell-growth functions. For example, auxin, gibberellin, and brassinosteroid all have parallel links to cell-cycle progression (through S-phase Cyclin D-CDK and the anaphase-promoting complex) and cell-wall functions (through cell-wall extensibility or microtubule dynamics). Another intercellular signal mediated by microtubule dynamics is the mechanical stress caused by growth of interconnected cells. Superimposed on developmental controls, sugar signalling through the TOR pathway has recently emerged as a central control point linking cytoplasmic growth, cell-cycle and cell-wall functions. Recent progress in quantitative imaging and computational modelling will facilitate analysis of the multiple interconnections between plant cell growth and cell cycle and ultimately will be required for the predictive manipulation of plant growth.

Screening The Life Cycle Of Schistosoma Mansoni Using High-resolution Mass Spectrometry.

Schistosomiasis is a common tropical disease caused by Schistosoma species Schistosomiasis' pathogenesis is known to vary according to the worms' strain. Moreover, high parasitical virulence is directly related to eggs release and granulomatous inflammation in the host's organs. This virulence might be influenced by different classes of molecules, such as lipids. Therefore, better understanding of the metabolic profile of these organisms is necessary, especially for an increased potential of unraveling strain virulence mechanisms and resistance to existing treatments. In this report, direct-infusion electrospray high-resolution mass spectrometry (ESI(+)-HRMS) along with the lipidomic platform were employed to rapidly characterize and differentiate two Brazilian S. mansoni strains (BH and SE) in three stages of their life cycle: eggs, miracidia and cercariae, with samples from experimental animals (Swiss/SPF mice). Furthermore, urine samples of the infected and uninfected mice were analyzed to assess the possibility of direct diagnosis. All samples were differentiated using multivariate data analysis, PCA, which helped electing markers from distinct lipid classes; phospholipids, diacylglycerols and triacylglycerols, for example, clearly presented different intensities in some stages and strains, as well as in urine samples. This indicates that biochemical characterization of S. mansoni may help narrowing-down the investigation of new therapeutic targets according to strain composition and aggressiveness of disease. Interestingly, lipid profile of infected mice urine varies when compared to control samples, indicating that direct diagnosis of schistosomiasis from urine may be feasible.

Polymorphisms Of Cell Cycle Control Genes Influence The Development Of Sporadic Medullary Thyroid Carcinoma.

The role of key cell cycle regulation genes such as, CDKN1B, CDKN2A, CDKN2B, and CDKN2C in sporadic medullary thyroid carcinoma (s-MTC) is still largely unknown. In order to evaluate the influence of inherited polymorphisms of these genes on the pathogenesis of s-MTC, we used TaqMan SNP genotyping to examine 45 s-MTC patients carefully matched with 98 controls. A multivariate logistic regression analysis demonstrated that CDKN1B and CDKN2A genes were related to s-MTC susceptibility. The rs2066827*GT+GG CDKN1B genotype was more frequent in s-MTC patients (62.22%) than in controls (40.21%), increasing the susceptibility to s-MTC (OR=2.47; 95% CI=1.048-5.833; P=0.038). By contrast, the rs11515*CG+GG of CDKN2A gene was more frequent in the controls (32.65%) than in patients (15.56%), reducing the risk for s-MTC (OR=0.174; 95% CI=0.048-0.627; P=0.0075). A stepwise regression analysis indicated that two genotypes together could explain 11% of the total s-MTC risk. In addition, a relationship was found between disease progression and the presence of alterations in the CDKN1A (rs1801270), CDKN2C (rs12885), and CDKN2B (rs1063192) genes. WT rs1801270 CDKN1A patients presented extrathyroidal tumor extension more frequently (92%) than polymorphic CDKN1A rs1801270 patients (50%; P=0.0376). Patients with the WT CDKN2C gene (rs12885) presented larger tumors (2.9±1.8 cm) than polymorphic patients (1.5±0.7 cm; P=0.0324). On the other hand, patients with the polymorphic CDKN2B gene (rs1063192) presented distant metastases (36.3%; P=0.0261). In summary, we demonstrated that CDKN1B and CDKN2A genes are associated with susceptibility, whereas the inherited genetic profile of CDKN1A, CDKN2B, and CDKN2C is associated with aggressive features of tumors. This study suggests that profiling cell cycle genes may help define the risk and characterize s-MTC aggressiveness.

Glycosaminoglycan distribution in the rat uterine cervix during the estrous cycle

OBJECTIVE: To analyze the amount of glycosaminoglycans in the uterine cervix during each phase of the rat estrous cycle. DESIGN: Based on vaginal smears, forty female, regularly cycling rats were divided into four groups (n = 10 for each group): GI - proestrous, GII - estrous, GIII - metaestrous and GIV - diestrous. Animals were sacrificed at each phase of the cycle, and the cervix was immediately removed and submitted to biochemical extraction and determination of sulfated glycosaminoglycans and hyaluronic acid. The results were analyzed by ANOVA followed by the Bonferroni post-hoc test. RESULTS: The uterine cervix had the highest amount of total sulfated glycosaminoglycans and dermatan sulfate during the estrous phase (8.90 ± 0.55 mg/g of cetonic extract, p<0.001; and 8.86 ± 0.57 mg/g of cetonic extract, p<0.001). In addition, there was more heparan sulfate at the cervix during the proestrous phase (0.185 ± 0.03 mg/g of cetonic extract) than during any other phase (p<0.001). There were no significant changes in the concentration of hyaluronic acid in the uterine cervix during the estrous cycle. CONCLUSION: Our data suggest that the amount of total sulfated glycosaminoglycans may be influenced by hormonal fluctuations related to the estrous cycle, with dermatan sulfate and heparan sulfate being the glycosaminoglycans most sensitive to hormonal change.

Survival, population pize, and gonotrophic cycle duration of Nyssomyia neivai (Diptera: Psychodidae) at an endemic area of American Cutaneous Leishmaniasis in Southeastern Brazil

The survival, absolute population size, gonotrophic cycle duration, and temporal and spatial abundance of Nyssomyia neivai (Pinto) were studied in a rural area endemic for American cutaneous leishmaniasis (ACL) in Conchal, Sõo Paulo State, southeastern Brazil, using mark-release-recapture techniques and by monitoring population fluctuation. The monthly abundance exhibited a unimodal pattern, with forest and domicile habitats having the highest relative abundances. A total of 1,873 males and 3,557 females were marked and released during the six experiments, of which 4.1-13.0 per cent of males and 4.1-11.8 per cent of females were recaptured. Daily survivorship estimated from the decline in recaptures per day was 0.681 for males and 0.667 for females. Gonotrophic cycle duration was estimated to be 4.0 d. Absolute population size was calculated using the Lincoln Index and ranged from 861 to 4,612 males and from 2,187 to 19,739 females. The low proportion of females that reach the age when they are potentially infective suggests that N. neivai has a low biological capacity to serve as a vector and that factors such as high biting rates and opportunistic feeding behavior would be needed to enable Leishmania (Viannia) braziliensis Vianna transmission. This agreed with the epidemiological pattern of ACL in southeastern Brazil that is characterized by low incidence, with isolated cases acquired principally within domiciliary habitats

LIFE CYCLE AND POPULATION STRUCTURE OF AEGLA PAULENSIS (DECAPODA: ANOMURA: AEGLIDAE)

We describe growth, longevity, sex ratio, reproductive period, and recruitment of Aegla paulensis from Jaragua Stale Park, Sao Paulo, Brazil (23 degrees 27'27.9 '' S; 46 degrees 45'32.3 '' W). The population was sampled monthly (September 2007 through August 2009) with the aid of traps. Over five thousand individuals were captured, sexed, measured (carapace length = CL) and inspected for reproductive traits (females only), and then released back to the sampling site. The pattern of the reproductive cycle was strongly seasonal (austral mid autumn through late winter), with a single recruitment pulse per year. The obtained von Bertalanffy growth equations were CL = 21.25[1-e(-0.041(t + 1.250))] and CL = 16.52[1-e(-0.049(t + 1.823))] for males and females, respectively. Males (mean CL +/- SD = 11.86 +/- 2.79 mm) attain larger sizes than females (mean CL +/- SD = 10.84 +/- 2.36 mm). Aegla paulensis reproduces twice during an estimated life span of 40.2 months for females and 33.9 months for males. Temporal variation of sex ratio showed a distinctive pattern characterized by a sequence of three distinct periods that repeated from one year to another, and which suggested that a behavioral component influence the proportion of sex in adult specimens sampled with traps during reproductive and non-reproductive periods.