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Kraft process

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210:. Air remaining in chips at the beginning of liquor impregnation is trapped within the chips. The impregnation can be done before or after the chips enter the digester and is normally done below 100 °C (212 °F). The cooking liquors consist of a mixture of white liquor, water in chips, condensed steam and weak black liquor. In the impregnation, cooking liquor penetrates into the capillary structure of the chips and low temperature chemical reactions with the wood begin. A good impregnation is important to get a homogeneous cook and low rejects. About 40–60% of all alkali consumption, in the continuous process, occurs in the impregnation zone. 42: 2407: 742: 131: 2417: 243: 1184: 432:. A modern kraft pulp mill is more than self-sufficient in its electrical generation and normally will provide a net flow of energy which can be used by an associated paper mill or sold to neighboring industries or communities through to the local electrical grid. Additionally, bark and wood residues are often burned in a separate power boiler to generate steam. 31: 824:
Pulp mills are almost always located near large bodies of water due to their substantial demand for water. Delignification of chemical pulps releases considerable amounts of organic material into the environment, particularly into rivers or lakes. The wastewater effluent can also be a major source of
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The brownstock from the blowing goes to the washing stages where the used cooking liquors are separated from the cellulose fibers. Normally a pulp mill has 3-5 washing stages in series. Washing stages are also placed after oxygen delignification and between the bleaching stages as well. Pulp washers
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to recover the inorganic chemicals for reuse in the pulping process. Higher solids in the concentrated black liquor increases the energy and chemical efficiency of the recovery cycle, but also gives higher viscosity and precipitation of solids (plugging and fouling of equipment). During combustion,
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In the case of a plant designed to produce pulp to make brown sack paper or linerboard for boxes and packaging, the pulp does not always need to be bleached to a high brightness. Bleaching decreases the mass of pulp produced by about 5%, decreases the strength of the fibers and adds to the cost of
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emissions of kraft-pulp mills are much lower than those from sulfite mills. In the ambient air outside a typical modern kraft-pulp mill, the sulfur-dioxide odour is perceivable only during disturbance situations, for example when the mill is shut down for a maintenance break, or when an extended
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is the measure of the amount of water used in washing compared with the theoretical amount required to displace the liquor from the thickened pulp. Lower dilution factor reduces energy consumption, while higher dilution factor normally gives cleaner pulp. Thorough washing of the pulp reduces the
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The wood chips are then cooked in pressurized digesters. Some digesters operate in a batch manner and some in a continuous process. Digesters producing 1,000 tonnes or more of pulp per day are common, with the largest producing more than 3,500 tonnes per day. Typically, delignification requires
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by G. H. Tomlinson in the early 1930s was a milestone in the advancement of the kraft process. It enabled the recovery and reuse of the inorganic pulping chemicals such that a kraft mill is a nearly closed-cycle process with respect to inorganic chemicals, apart from those used in the bleaching
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Hoffman, E., Guernsey, J. R., Walker, T. R., Kim, J. S., Sherren, K., & Andreou, P. (2017). Pilot study investigating ambient air toxics emissions near a Canadian kraft pulp and paper facility in Pictou County, Nova Scotia. Environmental Science and Pollution Research, 24(25),
105:. The technology entails several steps, both mechanical and chemical. It is the dominant method for producing paper. In some situations, the process has been controversial because kraft plants can release odorous products and in some situations produce substantial liquid 1530:
Hoffman, E., Bernier, M., Blotnicky, B., Golden, P. G., Janes, J., Kader, A., ... & Walker, T. R. (2015). Assessment of public perception and environmental compliance at a pulp and paper facility: a Canadian case study. Environmental monitoring and assessment, 187(12),
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Hoffman, E., Bernier, M., Blotnicky, B., Golden, P. G., Janes, J., Kader, A., ... & Walker, T. R. (2015). Assessment of public perception and environmental compliance at a pulp and paper facility: a Canadian case study. Environmental Monitoring and Assessment, 187(12),
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Hoffman, E., Lyons, J., Boxall, J., Robertson, C., Lake, C. B., & Walker, T. R. (2017). Spatiotemporal assessment (quarter century) of pulp mill metal (loid) contaminated sediment to inform remediation decisions. Environmental monitoring and assessment, 189(6),
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Hoffman, E., Lyons, J., Boxall, J., Robertson, C., Lake, C. B., & Walker, T. R. (2017). Spatiotemporal assessment (quarter century) of pulp mill metal (loid) contaminated sediment to inform remediation decisions. Environmental Monitoring and Assessment, 189(6),
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The fiber containing shives and knots are separated from the rest of the reject and reprocessed either in a refiner or is sent back to the digester. The content of knots is typically 0.5–3.0% of the digester output, while the shives content is about 0.1–1.0%.
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power outage occurs. Control of odours is achieved through the collection and burning of these odorous gases in the recovery boiler alongside the black liquor. In modern mills, where well-dried solids are burned in the recovery boiler, hardly any
519:(screens) and centrifugal cleaning. The sieves are normally set up in a multistage cascade operation because considerable amounts of good fibres can go to the reject stream when trying to achieve maximum purity in the accept flow. 479:
The finished cooked wood chips are blown to a collection tank called a blow tank that operates at atmospheric pressure. This releases a lot of steam and volatiles. The volatiles are condensed and collected; in the case of northern
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precipitates. The resulting solution of sodium carbonate and sodium sulfide is known as "green liquor". The green liquor's eponymous green colour arises from the presence of colloidal iron sulfide. This liquid is then mixed with
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In a modern mill, brownstock (cellulose fibers containing approximately 5% residual lignin) produced by the pulping is first washed to remove some of the dissolved organic material and then further delignified by a variety of
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Kraft pulp is darker than other wood pulps, but it can be bleached to make very white pulp. Fully bleached kraft pulp is used to make high-quality paper where strength, whiteness, and resistance to yellowing are important.
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The molten salts ("smelt") from the recovery boiler are dissolved in a process water known as "weak wash". This process water, also known as "weak white liquor" is composed of all liquors used to wash lime mud and
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degrade cellulose more than the kraft process, which leads to weaker fibers. Kraft pulping removes most of the lignin present originally in the wood whereas mechanical pulping processes leave most of the
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Although recovery boilers using G.H. Tomlinson's invention have been in general use since the early 1930s, attempts have been made to find a more efficient process for the recovery of cooking chemicals.
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degrade to give fragments that are soluble in the strongly basic liquid. The solid pulp (about 50% by weight of the dry wood chips) is collected and washed. At this point the pulp is known as
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leaves the boiler. At high boiler temperatures, the sodium released from the black liquor droplets reacts with sulfur dioxide, thereby effectively scavenging it by forming odourless
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of the soap layer formed on top of the liquor storage tanks. From pines the average yield of turpentine is 5–10 kg/t pulp and of crude tall oil is 30–50 kg/t pulp.
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The combination of reactions 1 through 4 form a closed cycle with respect to sodium, sulfur and calcium and is the main concept of the so-called recausticizing process where
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used in pulp production are 12–25 millimetres (0.47–0.98 in) long and 2–10 millimetres (0.079–0.394 in) thick. The chips normally first enter the
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The kraft process can use a wider range of fiber sources than most other pulping processes. All types of wood, including very resinous types like southern
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The recovery boiler also generates high pressure steam which is fed to turbogenerators, reducing the steam pressure for the mill use and generating
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soap. The availability of these is strongly dependent on wood species, growth conditions, storage time of logs and chips, and the mill's process.
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Both capitalized and lowercase spelling ("Kraft process" and "kraft process") appear in the literature, but "kraft" is most commonly used in the
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between the stages such that the pulp moves in the opposite direction to the flow of washing waters. Several processes are involved:
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Pulp and Paper Circle provides industry-related information (especially kraft mills) to pulp and paper engineers and technologists.
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can be added in the soap separation to speed up and improve the separation of soap from the used cooking liquors by flocculation.
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and maintains a high effective sulfur ratio (sulfidity), an important determiner of the strength of the paper. Acidic
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because of its color. The combined liquids, known as black liquor (because of its color), contain lignin fragments,
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remove foam and speed up the production process. Drainage of washing equipment is improved and gives cleaner pulp.
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Rudolf Patt et al. "Paper and Pulp" in Ullmann's Encyclopedia of Industrial Chemistry 2002 Wiley-VCH, Weinheim.
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The weak black liquor is further evaporated to 65% or even 80% solids ("heavy black liquor") and burned in the
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Joint Textbook Committee of the Paper Industry (1969). Macdonald, Ronald Gordon; Franklin, John N. (eds.).
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in solution, to regenerate the white liquor used in the pulping process through an equilibrium reaction (Na
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between cellulose (and hemicellulose) in the fibers needed for the strength of paper (strength refers to
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One of the main chemical reactions that underpin the kraft process is the scission of ether bonds by the
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Reference Document on Best Available Techniques in Pulp and Paper Industry by European Commission, 2001
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fix finely dispersed potential deposits to the fibers and thereby transport them out of the process.
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around two hours at 170 to 176 °C (338 to 349 °F). Under digesting conditions, lignin and
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Calcium oxide (lime) is reacted with water to regenerate the calcium hydroxide used in Reaction 2:
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Giddings, J.F.; Roll, D.R.; Cappellino, C.A.; Day, M.; Nardone, R.A. (2008). "12.12.4.". In
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S is shown since it is part of the green liquor, but does not participate in the reaction):
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Screening of the pulp after pulping is a process whereby the pulp is separated from large
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may be used to improve impregnation of the wood chips with the cooking liquors.
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Anthraquinone Pulping. A TAPPI Press Anthology of Published Papers, 1977-1996
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compounds are the cause of the malodorous air emissions characteristic for
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The excess black liquor contains about 15% solids and is concentrated in a
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process. For this reason, in the 1940s, the kraft process superseded the
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Pulp produced by the kraft process is stronger than that made by other
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precipitates from the white liquor and is recovered and heated in a
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was issued in 1884, and a pulp mill using this technology began in
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keep the system cleaner and reduce the need for maintenance stops.
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Process chemicals are added to improve the production process:
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Pulp and Paper Manufacture, vol. 1 : The Pulping of Wood
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agents. The process effluents can be treated in a biological
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is the pulp. The material separated from the pulp is called
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are the most extractive-rich woods. The raw turpentine is
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to sodium sulfide by the organic carbon in the mixture:
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Papermaking science and Technology: 6. Chemical Pulping
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The main byproducts of kraft pulping are crude sulfate
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net reaction in depolymerization of lignin by SH (Ar =
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nature of lignin interferes with the formation of the
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The screening section consists of different types of
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A precursor of the kraft process was used during the
1424:. US Department of Agriculture. 1985. Archived from 1378: 825:pollution, containing lignins from the trees, high 1243:"Kraft pulping: Energy consumption and production" 1073:. U.S. Environmental Protection Agency. p. 66 1009: 849:, which can substantially reduce their toxicity. 769:and is distilled off the digester, while the raw 112:The process name is derived from the German word 2433: 1554:Gullichsen, Johan; Carl-Johan Fogelholm (2000). 1488:Journal of the Air Pollution Control Association 1146: 289:off. The collected soap is further processed to 177:as the dominant method for producing wood pulp. 564:Several types of washing equipment are in use: 626:is used as a digester additive. It works as a 142:in England. The kraft process was invented by 1610: 1202:; Messina, J.; Cooper, P.; Heald, C. (eds.). 1191: 1149:"Second Critical Solids Black Liquor Scaling" 1042:Wood Chemistry: Fundamentals and Applications 1447: 1445: 1039: 730: 1672: 1617: 1603: 1379:Hubbe, Martin a.; Lucian A. Lucia (2007). 1396: 198:where they are wetted and preheated with 27:Process of converting wood into wood pulp 1442: 1240: 1123:"Equipment to handle heavy black liquor" 1007: 740: 241: 129: 40: 29: 1451: 1208:(4th ed.). New York: McGraw Hill. 1068: 679:Comparison with other pulping processes 14: 2434: 1477: 1035: 1033: 1003: 1001: 999: 1598: 1349:"Tall Oil and Tall Oil Soap Recovery" 1322: 1012:Essentials of Pulping and Papermaking 231:from the breakdown of hemicellulose, 2416: 607: 1147:Hsieh, Jeffery S.; Smith, Jason B. 1030: 996: 272: 24: 1547: 1062: 1016:. San Diego: Academic Press, Inc. 727:can be used in the kraft process. 93:, that breaks the bonds that link 25: 2473: 1573: 1008:Biermann, Christopher J. (1993). 808:utilizing the kraft process. The 285:soap rises to the surface and is 61:) is a process for conversion of 2415: 2406: 2405: 1241:Jeffries, Tom (March 27, 1997). 330:thermochemical sulfate reduction 69:, which consists of almost pure 1585:US EPA article on kraft pulping 1534: 1524: 1514: 1471: 1452:Stenius, Per, ed. (2000). "2". 1411: 1372: 1341: 1316: 1285: 1260: 1234: 1172: 1140: 1115: 185: 1500:10.1080/00022470.1962.10468107 1084: 980:. Vol. 1 (2nd ed.). 967: 954: 938: 928: 918: 784:Various byproducts containing 180: 168:in 1890. The invention of the 73:fibres, the main component of 45:Woodchips for paper production 13: 1: 2232:Environmental impact of paper 950:10.1002/14356007.a18_545.pub4 912: 745:Forchem tall oil refinery in 737:Environmental impact of paper 504:, dirt and other debris. The 122:produced using this process. 1478:Hansen, G. A. (1962). "Odor 773:is separated from the spent 719:, and non-wood species like 708:and resistance to tearing). 584: 491: 484:this consists mainly of raw 328:This reaction is similar to 7: 1398:10.15376/biores.2.4.534-535 852: 239:and other inorganic salts. 10: 2478: 2179:Surface chemistry of paper 1682:(Zuo Bo/Tso Po/Tso Tzǔ-yi) 734: 588: 526: 474: 279:multiple effect evaporator 213: 125: 2401: 2340: 2285: 2197: 2154: 2113: 1758: 1728: 1698: 1649: 1632: 1624: 1454:Forest Products Chemistry 1092:"Basics of Kraft Pulping" 1069:Woodman, Jocelyn (1993). 421:is reacted to regenerate 383:where it is converted to 1711:Friedrich Gottlob Keller 1558:. Finland: Tappi Press. 1327:. Atlanta: TAPPI Press. 1323:Goyal, Gopal C. (1997). 847:effluent treatment plant 831:dissolved organic carbon 827:biological oxygen demand 731:Byproducts and emissions 557:chemical oxygen demand ( 2452:Pulp and paper industry 2227:Elemental chlorine free 2184:Units of paper quantity 962:pulp and paper industry 449:entrained flow gasifier 2207:Bleaching of wood pulp 1180:US granted 5527427 750: 591:Bleaching of wood pulp 255: 135: 46: 38: 2126:Corrugated fiberboard 1883:Electrical insulation 1736:Thomas Francis Carter 1249:on September 28, 2011 800:, and other volatile 744: 735:Further information: 571:Atmospheric diffusers 245: 134:A roll of kraft paper 133: 44: 33: 1484:in a Kraft Pulp Mill 1419:"The Southern Pines" 1040:E. Sjöström (1993). 841:, heavy metals, and 451:successfully at its 696:in the fibers. The 616:Impregnation aids. 574:Vacuum drum washers 534:countercurrent flow 161:U.S. patent 296,935 35:International Paper 2447:Chemical processes 1268:"Chemrec web site" 833:(DOC), along with 798:dimethyl disulfide 751: 568:Pressure diffusers 301:sodium sulfate is 256: 136: 47: 39: 37:: Kraft paper mill 2429: 2428: 1754: 1753: 1746:Tsien Tsuen-hsuin 1724: 1723: 1694: 1693: 1637:Paper engineering 689:sulfite processes 685:pulping processes 666:complexing agents 658:Dispersing agents 608:Process chemicals 444:first generation 377:Calcium carbonate 347:calcium hydroxide 332:in geochemistry. 16:(Redirected from 2469: 2419: 2418: 2409: 2408: 2393:Beverage cartons 2383:Watercolor paper 2242:Hollander beater 1726: 1725: 1696: 1695: 1670: 1669: 1619: 1612: 1605: 1596: 1595: 1569: 1542: 1538: 1532: 1528: 1522: 1518: 1512: 1511: 1482:Fallout Control 1475: 1469: 1467: 1449: 1440: 1439: 1437: 1436: 1430: 1423: 1415: 1409: 1408: 1406: 1405: 1400: 1376: 1370: 1369: 1367: 1366: 1360: 1354:. 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2474: 2463: 2460: 2458: 2455: 2453: 2450: 2448: 2445: 2443: 2440: 2439: 2437: 2422: 2414: 2412: 2404: 2403: 2400: 2394: 2391: 2389: 2386: 2384: 2381: 2379: 2376: 2374: 2371: 2369: 2366: 2364: 2361: 2359: 2356: 2354: 2351: 2349: 2346: 2345: 2343: 2339: 2331: 2328: 2327: 2326: 2323: 2319: 2318:United States 2316: 2314: 2311: 2309: 2306: 2304: 2301: 2299: 2296: 2295: 2294: 2291: 2290: 2288: 2284: 2278: 2275: 2273: 2270: 2268: 2265: 2263: 2260: 2258: 2257:Paper machine 2255: 2253: 2250: 2248: 2247:Kraft process 2245: 2243: 2240: 2238: 2235: 2233: 2230: 2228: 2225: 2223: 2220: 2218: 2215: 2213: 2210: 2208: 2205: 2204: 2202: 2196: 2190: 2187: 2185: 2182: 2180: 2177: 2175: 2172: 2170: 2167: 2165: 2162: 2161: 2159: 2157: 2153: 2147: 2144: 2142: 2139: 2137: 2134: 2132: 2129: 2127: 2124: 2122: 2119: 2118: 2116: 2112: 2106: 2103: 2101: 2098: 2096: 2093: 2091: 2088: 2086: 2083: 2081: 2078: 2076: 2073: 2071: 2068: 2066: 2063: 2061: 2058: 2056: 2053: 2051: 2048: 2046: 2043: 2041: 2038: 2036: 2033: 2031: 2028: 2026: 2023: 2021: 2018: 2016: 2013: 2011: 2008: 2006: 2003: 2001: 1998: 1996: 1993: 1991: 1988: 1986: 1983: 1981: 1978: 1976: 1973: 1971: 1968: 1966: 1963: 1961: 1958: 1956: 1953: 1951: 1948: 1946: 1943: 1939: 1936: 1935: 1934: 1931: 1929: 1926: 1924: 1921: 1919: 1916: 1914: 1911: 1909: 1906: 1904: 1901: 1899: 1896: 1894: 1891: 1889: 1886: 1884: 1881: 1879: 1876: 1874: 1871: 1869: 1866: 1864: 1861: 1859: 1856: 1852: 1849: 1848: 1847: 1844: 1842: 1839: 1837: 1834: 1832: 1829: 1827: 1824: 1822: 1819: 1817: 1814: 1812: 1809: 1807: 1804: 1802: 1799: 1797: 1794: 1792: 1789: 1787: 1784: 1782: 1779: 1777: 1774: 1772: 1769: 1767: 1764: 1763: 1761: 1757: 1747: 1744: 1742: 1739: 1737: 1734: 1733: 1731: 1727: 1717: 1714: 1712: 1709: 1707: 1704: 1703: 1701: 1697: 1687: 1684: 1681: 1678: 1677: 1675: 1671: 1665: 1662: 1660: 1657: 1656: 1654: 1652: 1648: 1642: 1638: 1635: 1634: 1631: 1627: 1620: 1615: 1613: 1608: 1606: 1601: 1600: 1597: 1591: 1588: 1586: 1583: 1581: 1578: 1577: 1567: 1565:952-5216-06-3 1561: 1557: 1552: 1551: 1537: 1527: 1517: 1509: 1505: 1501: 1497: 1493: 1489: 1485: 1481: 1474: 1465: 1463:952-5216-03-9 1459: 1455: 1448: 1446: 1431:on 2007-07-09 1427: 1420: 1414: 1399: 1394: 1390: 1386: 1382: 1375: 1361:on 2012-03-05 1357: 1350: 1344: 1336: 1334:0-89852-340-0 1330: 1326: 1319: 1305:on 2004-12-18 1301: 1294: 1288: 1274:on 2012-07-09 1273: 1269: 1263: 1248: 1244: 1237: 1221: 1217: 1215:9780071460446 1211: 1207: 1206: 1205:Pump Handbook 1201: 1194: 1181: 1175: 1161:on 2011-08-31 1157: 1150: 1143: 1129:on 2005-04-20 1128: 1124: 1118: 1104:on 2021-10-23 1100: 1093: 1087: 1072: 1065: 1057: 1055:0-12-647480-X 1051: 1047: 1043: 1036: 1034: 1025: 1023:0-12-097360-X 1019: 1014: 1013: 1004: 1002: 1000: 991: 987: 983: 979: 978: 970: 963: 957: 951: 947: 941: 931: 921: 917: 907: 904: 902: 899: 897: 894: 892: 889: 887: 884: 882: 879: 877: 874: 872: 869: 866: 865:Johan Richter 863: 861: 858: 857: 850: 848: 844: 840: 836: 832: 828: 822: 820: 816: 811: 807: 803: 799: 795: 791: 787: 782: 780: 776: 772: 768: 764: 760: 756: 748: 743: 738: 728: 726: 722: 718: 713: 709: 707: 703: 699: 695: 690: 686: 673: 670: 667: 663: 659: 656: 653: 650: 647: 643: 640: 637:and reducing 636: 633:by oxidizing 632: 629: 625: 624:Anthraquinone 622: 619: 615: 614: 613: 605: 604:manufacture. 601: 599: 592: 579: 576: 573: 570: 567: 566: 565: 562: 560: 555: 551: 547: 543: 539: 535: 524: 520: 518: 513: 511: 507: 503: 499: 489: 487: 483: 472: 470: 466: 462: 458: 454: 450: 447: 443: 439: 433: 431: 426: 424: 420: 405: 404: 403: 390: 389: 388: 386: 385:calcium oxide 382: 378: 356: 355: 354: 348: 344: 343:calcium oxide 339: 333: 331: 308: 307: 306: 304: 299: 294: 292: 288: 284: 280: 270: 268: 264: 261: 253: 249: 244: 240: 238: 234: 230: 229:carbohydrates 226: 222: 221:hemicellulose 211: 209: 205: 201: 197: 193: 178: 176: 171: 167: 162: 157: 153: 149: 145: 141: 132: 123: 121: 117: 116: 110: 108: 104: 100: 99:hemicellulose 96: 92: 89:S), known as 84: 80: 76: 72: 68: 64: 60: 56: 55:kraft pulping 52: 51:kraft process 43: 36: 32: 19: 18:Kraft pulping 2358:Papier-mâché 2353:Paper towels 2272:Soda pulping 2246: 2189:Wet strength 1990:Photographic 1863:Cotton (rag) 1836:Construction 1555: 1536: 1526: 1521:20685-20698. 1516: 1491: 1487: 1483: 1479: 1473: 1453: 1433:. Retrieved 1426:the original 1413: 1402:. Retrieved 1388: 1385:BioResources 1384: 1374: 1363:. Retrieved 1356:the original 1343: 1324: 1318: 1307:. Retrieved 1300:the original 1287: 1276:. Retrieved 1272:the original 1262: 1251:. Retrieved 1247:the original 1236: 1226:February 21, 1224:. Retrieved 1220:the original 1204: 1200:Karassik, I. 1193: 1174: 1163:. Retrieved 1156:the original 1142: 1131:. Retrieved 1127:the original 1117: 1106:. Retrieved 1099:the original 1086: 1075:. Retrieved 1064: 1041: 1011: 976: 969: 956: 940: 930: 920: 901:Soda pulping 871:Kappa number 823: 783: 775:black liquor 752: 714: 710: 682: 662:detackifiers 611: 602: 594: 580:Wash presses 563: 553: 546:displacement 530: 521: 514: 509: 505: 495: 478: 446:black liquor 438:Weyerhaeuser 434: 427: 416: 401: 375: 338:green liquor 334: 327: 295: 276: 260:nucleophilic 257: 224: 217: 208:white liquor 195: 189: 186:Impregnation 144:Carl F. Dahl 137: 113: 111: 91:white liquor 81:(NaOH), and 58: 54: 50: 48: 2442:Papermaking 2388:Paper money 2348:Lined paper 2267:Papermaking 2200:and process 2198:Manufacture 2174:Paper sizes 1903:Greaseproof 1888:Genkō yōshi 1741:Dard Hunter 1673:Originators 1641:Papermaking 982:McGraw Hill 876:Kraft paper 779:decantation 698:hydrophobic 618:Surfactants 430:electricity 269:(HS) ions. 225:brown stock 196:presteaming 181:The process 146:in 1879 in 120:kraft paper 2436:Categories 2325:Paper mill 2252:Organosolv 2131:Fiber crop 2121:China clay 2080:Waterproof 1980:Paperboard 1858:Correction 1851:Carbonless 1699:Developers 1435:2007-09-13 1404:2015-02-03 1365:2008-12-19 1309:2007-09-28 1278:2011-01-07 1253:2007-10-21 1165:2007-10-09 1133:2007-10-09 1108:2021-10-23 1077:2022-02-06 913:References 881:Organosolv 829:(BOD) and 821:crystals. 806:pulp mills 755:turpentine 749:, Finland. 538:thickening 486:turpentine 410:O → Ca(OH) 406:4. CaO + H 395:→ CaO + CO 317:+ 2 C → Na 192:wood chips 2378:Notebooks 2363:Cardboard 2146:Wood pulp 2114:Materials 2090:Wood-free 2065:Wallpaper 2060:Tree-free 2000:Red rosin 1985:Parchment 1970:Onionskin 1965:Newsprint 1826:Cartridge 1821:Cardstock 1816:Cardboard 1766:Acid-free 990:867778880 906:Wood pulp 896:Pulp mill 843:chelating 839:chlorates 652:Defoamers 635:cellulose 598:bleaching 585:Bleaching 550:diffusion 492:Screening 482:softwoods 463:plant in 455:plant in 381:lime kiln 267:bisulfide 103:cellulose 71:cellulose 67:wood pulp 2411:Category 2368:Clothing 2286:Industry 2222:Deinking 2212:Calender 2169:Grammage 2055:Transfer 2020:Security 1893:Glassine 1796:Blotting 1771:Air-laid 1729:Scholars 1508:13904415 860:H-factor 853:See also 835:alcohols 767:volatile 759:tall oil 631:catalyst 600:stages. 542:dilution 453:New Bern 387:(lime). 365:+ Ca(OH) 321:S + 2 CO 291:tall oil 254:groups). 2421:Commons 2373:Tissues 2164:Density 2141:Papyrus 2100:Writing 2050:Tracing 2040:Thermal 2015:Scritta 2010:Rolling 1975:Origami 1938:Butcher 1873:Display 1841:Contact 1806:Bristol 1781:Asphalt 1686:Damjing 1680:Cai Lun 1651:History 527:Washing 475:Blowing 442:Chemrec 391:3. CaCO 303:reduced 287:skimmed 265:(S) or 263:sulfide 214:Cooking 190:Common 156:Germany 152:Prussia 126:History 2303:Europe 2298:Canada 2045:Tissue 1955:Manila 1928:Korean 1923:Ingres 1918:Inkjet 1831:Coated 1811:Carbon 1786:Banana 1562:  1506:  1460:  1331:  1212:  1186:  1052:  1020:  988:  802:sulfur 721:bamboo 694:lignin 639:lignin 552:. The 517:sieves 510:reject 506:accept 498:shives 469:Sweden 250:, R = 166:Sweden 148:Danzig 107:wastes 101:, and 95:lignin 2313:Japan 2308:India 2075:Wasli 2070:Washi 2030:Stone 1960:Mummy 1950:Lokta 1933:Kraft 1913:India 1898:Graph 1868:Crêpe 1791:Bible 1776:Amate 1759:Types 1626:Paper 1429:(PDF) 1422:(PDF) 1359:(PDF) 1352:(PDF) 1303:(PDF) 1296:(PDF) 1159:(PDF) 1152:(PDF) 1102:(PDF) 1095:(PDF) 886:Paper 763:Pines 747:Rauma 725:kenaf 628:redox 502:knots 465:Piteå 357:2. Na 309:1. Na 283:rosin 252:alkyl 204:black 200:steam 115:Kraft 75:paper 65:into 2341:Uses 2330:List 2105:Xuan 2095:Wove 2025:Seed 2005:Rice 1945:Laid 1908:Hemp 1846:Copy 1801:Bond 1560:ISBN 1541:257. 1531:766. 1504:PMID 1458:ISBN 1329:ISBN 1228:2013 1210:ISBN 1050:ISBN 1018:ISBN 986:OCLC 935:766. 925:257. 771:soap 757:and 723:and 717:pine 664:and 548:and 532:use 248:aryl 206:and 63:wood 49:The 2085:Wax 2035:Tar 1496:doi 1486:". 1480:and 1393:doi 946:doi 777:by 644:An 561:). 559:COD 85:(Na 57:or 2438:: 1878:Dó 1639:/ 1502:. 1492:12 1490:. 1444:^ 1387:. 1383:. 1048:. 1044:. 1032:^ 998:^ 984:. 837:, 796:, 792:, 788:, 660:, 544:, 540:/ 512:. 500:, 488:. 471:. 467:, 425:. 361:CO 313:SO 235:, 158:. 154:, 150:, 109:. 97:, 1618:e 1611:t 1604:v 1568:. 1510:. 1498:: 1468:. 1466:. 1438:. 1407:. 1395:: 1389:2 1368:. 1337:. 1312:. 1281:. 1256:. 1230:. 1168:. 1136:. 1111:. 1080:. 1058:. 1026:. 992:. 964:. 948:: 412:2 408:2 397:2 393:3 371:3 367:2 363:3 359:2 351:2 323:2 319:2 315:4 311:2 87:2 20:)

Index

Kraft pulping

International Paper

wood
wood pulp
cellulose
paper
sodium hydroxide
sodium sulfide
white liquor
lignin
hemicellulose
cellulose
wastes
Kraft
kraft paper

Napoleonic Wars
Carl F. Dahl
Danzig
Prussia
Germany
U.S. patent 296,935
Sweden
recovery boiler
sulfite process
wood chips
steam
black

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