Kraft recovery boilers – Principles and practice

This book was created as postgraduate lecture notes for Lappeenranta University of Technology's special course of steam power plants. But as with anything ever written the ideas shown have nurtured for a long time. Parts of these chapters have appeared elsewhere as individual papers or work documents. One of the most helpful episodes have been presentations and discussions during Pohto Operator training seminars. Input from those sessions can be seen in chapter firing. You who run recovery boilers, I salute you. The purpose of this text is to give the reader an overview of recovery boiler operation. Most parts of the recovery boiler operation are common to boilers burning other fuels. The furnace operation differs significantly from operation of other boiler furnaces. Oxygen rich atmosphere is needed to burn fuel efficiently. But the main function of recovery boiler is to reduce spent cooking chemicals. Reduction reactions happen best in oxygen deficient atmosphere. This dual, conflicting nature of recovery furnace makes understanding it so challenging. To understand the processes happening in the recovery furnace one must try to understand the detailed processes that might occur and their limitations. Therefore chapters on materials, corrosion and fouling have been added.

Meesauunin vaipan konepajavalmistus ja laaduntarkastus

Meesauuni on osa sulfaattisellutehdasta ja sen kemikaalikiertoa. Se on pyörivä kaltevaan tasoon asetettu rumpu-uuni, joka voi olla jopa 160 metriä pitkä ja halkaisijaltaan 5,5 metriä. Kalkki on kiertävä apukemikaali, jota käytetään soodakattilalta tulevan viherlipeän muuttamiseen valkolipeäksi. Meesauunin tehtävänä on kierrättää kalkki (CaO) uudelleen käytettäväksi kaustisoinnissa syntyneestä meesasta (CaCO3). Meesauunin vaipan konepajavalmistus on prosessina hyvin yksinkertainen, mutta toleranssivaatimukset ovat hyvin tiukat suhteutettuna meesauunin kokoon. Vaippalohkojen valmistus on siirtynyt halpatyövoiman maihin lähelle loppukäyttäjiä, joten vaatimukset piirustusten laadulle, valmistukselle, ohjeille ja tarkastamiselle ovat lisääntyneet. Uunin vaippa toimitetaan asennuspaikalle useassa lohkossa ja jokainen vaippalohko on tarkastettava ennen toimitusta. Virheellisten vaippalohkojen siirtyminen asennuspaikalle on estettävä. Työn tavoitteena oli parantaa meesauunin vaippalohkojen konepajavalmistuksen laaduntarkastusta. Tässä työssä tutkitaan mittausmenetelmiä vaippalohkojen geometrian mittaamiseen. Tärkeimmät uunin toiminnallisiin ominaisuuksiin vaikuttavat muototoleranssit vaippalohkoille ovat ympyrämäisyys ja keskiviivan suoruus. Virheet näissä toleransseissa aiheuttavat vaurioita uunin muurauksille ja liian suuria kuormituksia tuennoille. Vaippalohkot on mitattava pyöritysrullaston päällä ja konepajan olosuhteissa, mikä aiheuttaa omat haasteensa. Vaippalohkojen suuret massat ja dimensiot aiheuttavat vaippalohkoihin muodonmuutoksia. Muodonmuutokset täytyy olla hallinnassa, mikäli halutaan käyttää CMS-laitteistoja (Coordinate Measuring System). Meesauunin vaippalohkot ovat mitattavissa radiaalimittauksina tai käyttäen CMS-laitteistoja.

Production and partial characterization of lipase from Penicillium verrucosum obtained by submerged fermentation of conventional and industrial media

The growing interest in lipase production is related to the potential biotechnological applications that these enzymes present. Current studies on lipase production by submerged fermentation involve the use of agro-industrial residues aiming at increasing economic attractiveness. Based on these aspects, the objective of this work was to investigate lipase production by Penicillium verrucosum in submerged fermentation using a conventional medium based on peptone, yeast extract, NaCl and olive oil, and an industrial medium based on corn steep liquor, Prodex Lac (yeast hydrolysate), NaCl and olive oil, as well as to characterize the crude enzymatic extracts obtained. Kinetics of lipase production was evaluated and the highest enzymatic activities, of 3.15 and 2.22 U.mL-1, were observed when conventional and industrial media were used, respectively. The enzymatic extract showed optimal activity in the range from 30 to 40 °C and at pH 7.0. Although the industrial medium presents economical advantages over the conventional medium, the presence of agro-industrial residues rich in nitrogen and other important nutrients seemed to contribute to a reduction in lipase activity.

Influência da fermentação e secagem de amêndoas de cacau no teor de compostos fenólicos e na aceitação sensorial

Devido à importância das etapas de fermentação e secagem das sementes de cacau para as características sensoriais dos produtos finais obtidos, bem como para os teores de compostos fenólicos presentes, objetivou-se avaliar a influência do tempo de fermentação e do tipo de secagem de sementes de cacaueiro nos teores de compostos fenólicos, bem como nas características físicas, físico-químicas e sensoriais dos produtos obtidos. Os tempos de fermentação avaliados foram 3 e 7 dias e a secagem foi realizada naturalmente (ao sol) e artificialmente (estufa com circulação de ar a 35 °C). Os teores de compostos fenólicos totais, flavan-3-óis e procianidinas foram quantificados durante a fermentação e ao término da secagem. Constatou-se que grande parte dos compostos fenólicos foi perdida durante a fermentação, sendo que as amêndoas fermentadas por 3 dias apresentaram teores maiores dos compostos fenólicos avaliados. Contudo, observou-se nessa condição uma significativa perda na qualidade sensorial. A secagem natural das amêndoas fermentadas permitiu maior retenção de polifenóis e também melhores resultados sensoriais em relação à secagem artificial. A avaliação sensorial realizada com uma bebida formulada com o liquor obtido dos diferentes tratamentos demonstrou que a amostra fermentada durante 7 dias apresentou as melhores notas sensoriais, sendo que o produto seco naturalmente foi o mais bem avaliado em relação aos demais.

Separation of lignin in Pulp Mill process and its effect on sodium sulphur balance

The aim of this thesis is to define effects of lignin separation process on Pulp mill chemical balance especially on sodium/sulphur-balance. The objective is to develop a simulation model with WinGEMS Process Simulator and use that model to simulate the chemical balances and process changes. The literature part explains what lignin is and how kraft pulp is produced. It also introduces to the methods that can be used to extract lignin from black liquor stream and how those methods affect the pulping process. In experimental part seven different cases are simulated with the created simulation model. The simulations are based on selected reference mill that produces 500 000 tons of bleached air-dried (90 %) pulp per year. The simulations include the chemical balance calculation and the estimated production increase. Based on the simulations the heat load of the recovery boiler can be reduced and the pulp production increased when lignin is extracted. The simulations showed that decreasing the waste acid stream intake from the chlorine dioxide plant is an effective method to control the sulphidity level when about 10 % of lignin is extracted. With higher lignin removal rates the in-mill sulphuric acid production has been discovered to be a better alternative to the sulphidity control.

Mäntyöljyn tislauksen esikäsittely

Raakamäntyöljy on selluteollisuuden sivutuote. Suopa erotetaan mustalipeästä ja palstoitetaan tuottaen siten raakamäntyöljyä. Raakamäntyöljy tislataan tavanomaisesti viiteen pääjakeeseen: rasvahapot, hartsihapot, mäntyöljytisle, esiöljy ja mäntyöljypiki. Näiden jakeiden lisäksi raakamäntyöljyssä on erityisesti mustalipeästä siihen erottuneita epäpuhtauksia, jotka haittaavat raakamäntyöljyn prosessointia. Epäpuhtauksia ovat orgaaniset ja epäorgaaniset yhdisteet, kuten metallit, suolat ja ligniini. Nämä epäpuhtaudet aiheuttavat haitallisia reaktioita prosessissa huonontaen siten lopputuotejakeiden laatua. Tämän lisäksi epäpuhtaudet aiheuttavat saostumia prosessilaitteissa alentaen siten prosessointitehokkuutta. Raakamäntyöljyn esikäsittelyllä tehostetaan tislauksen toimintaa. Työssä esitetään esikäsittelymenetelmistä mm. degumming-menetelmä, laimea happopesu, hiilidioksidikäsittely, valkaisu ja lämpökäsittely. Menetelmien pohjalta valitaan tätä työtä varten yksi menetelmä, jonka pohjalta suunnitellaan kokeellisessa osassa suoritettavat kokeet. Kokeellinen osuus koostuu esikokeista, varsinaisista kokeista ja lisäkokeista. Menetelmän tarkoituksena on saavuttaa epäpuhtauksille 90–95 % reduktioaste. Kokeiden onnistumista tutkitaan analysoimalla alkuperäinen raakamäntyöljy, sekä jokaisen kokeen jälkeen erotetut faasit. Työssä saavutettiin hyvä erotustehokkuus. Alkuperäisen tavoitteen mukaista reduktioastetta ei pystytty määrittämään eri analyysimenetelmien ja niiden analyysituloksissa ilmenneiden eroavaisuuksien vuoksi, mutta lisäkokeiden ansiosta pystyttiin vahvistamaan kyseisen koejärjestelmän optimaalinen poistoaste. Lisäksi työssä havaittiin että esikäsittelytulos on hyvin riippuvainen käsiteltävän raaka-aineen koostumuksesta.

Crowland Municipality : an act for regulating and governing auctioneers, and other persons putting up for sale, goods, wares, and merchandise to the highest or best bidder., 1854

On February 1st, 1854 an act was passed in order to regulate the sale of goods, wares and merchandise. Section I pertained to the fact that any merchant would first obtain a license. Section II deemed that no merchant should sell any wine or spirituous liquors, beer or ale within the municipality of Crowland in any less quantity than 5 gallons or less than 12 bottles in any place other than a House of Public Entertainment without having obtained a license. Section III was in regard to licensing any person who would use a billiard table which was set up for hire or gain. Section IV stated that all sums of money paid by the keepers of Houses of Public Entertainment plus the imperial duty of 2 pound would be payable to the Treasurer of the Municipality of Crowland. Section V was written regarding the continuance of the act to regulate inns, taverns, temperance houses and other Houses of Public Entertainment. Section VI specified that all recesses (not authorized to sell liquor) would pay the sum of 2 pounds. Section VII declared that Peter Benedict was appointed Revenue Inspector of the township and section VIII stated that recess-keepers who took out liquor licenses would be required to pay 6 pounds 5 shillings and for violating this they would pay a penalty. This document was written by Leonard M. Matthews, Township reeve and Alex Reid, clerk.

Letter - Dominion Alliance to Mr. Harry Cowan

A letter from the president of the Dominion Alliance for the Suppression of the Liquor Traffic, Joseph Gibson. The letter is dated November 18th, 1910 and requests "subscription". The request is to add to the campaign fund and the "new fight...voting upon the question of bar-room abolition". The voting is stated to take place in "January next" for about one hundred municipalities in Ontario.

Seagram Museum Collection

The Seagram Museum was opened on May 16th, 1984 by the Honourable William G. Davis, Premier of Ontario. The museum was devoted to the history and technology of the wine and spirit industry. The museum focused on wine-making and distillation, as well as barrel-making and cork manufacturing. The museum was located adjacent to the Seagram Distillery in Waterloo, Ontario. In 1997, the museum closed due to lack of funds.

Alberta Price List No. 3., January 1st, 1925

A price list form for the Alberta Liquor Control Board from 1 January 1925. The price list includes "General Information" in regards to permits for individuals and special permits. The alcohol is then listed by category for pricing: Scotch Whisky, Irish Whisky, Rye Whisky, Bourbon Whisky, Rum, Gin, Brandy, Port, Native Wine, Italian (Type) Wines, Sherry, Claret, Burgundy, White Wine, Sparkling Wine, Vermouth, Cocktails, Liqueurs, Champagne, Bitters, Ale and Stout, Chinese Liquors.

General Price List, Ontario, 1 January 1924

A general price list from the year 1924 for the province of Ontario. The cover of the list reads: "Ontario Government Dispensaries Conducted Under Direction of Board of License Commissioners for Ontario By Authority of The Ontario Temperance Act. General Price List, Dispensaries sell liquor for medicinal, sacramental, scientific and manufacturing purposes only. The sale of liquor for beverage purposes in the Province of Ontario is prohibited by The Ontario Temperance Act. Dispensaries: No.1-154 Wellington Street West, Toronto; No.2-1271 Dundas Street West, Toronto; No.3-29 Charles Street, Hamilton; No.4-425 Talbot Street, London; No.5-30 Sandwich Street West, Windsor; No.6-Golden Lion Block, Kingston; No.7-92 Kent Street, Ottawa; No.8-109 Simpson Street, Fort William."

Newfoundland Price List, 1 June 1928

A price list for Newfoundland by the Board of Liquor Control, St. John's. The list is one page in length and has a few handwritten changes to prices.

Price List - Lawrence A. Wilson Co. Limited, 1916

A price list for Lawrence A. Wilson Co. Limited, 87 James St., Montreal Quebec. It is addressed to The Toronto Hunt, 52 Bay Street, Toronto. There are additional handwritten notes. One of the handwritten notes reads "ck to W. Stephen Haas"

Wiehl & Widmann Price List, August 1903

A price list for Wiehl & Widmann (Wholesale Importers of and Dealers in Wines, Liquors and Mineral Waters). The price list is dated August 1903 and the location of the dealer is New York.

Bulloch, Lade & Co. Order Form, 31 August 1870

An order form for the exportation of scotch pure malt whiskies, distilled by Bulloch, Lade & Co.