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Hydrocarbon resin production and consumption

HR industrial production began in the United States when in 1920, using as a raw material some coke-chemical fractions, the early products of this category were obtained [315]. In 1927, Neville Cindu Ltd. was one of the largest HR manufacturers [316,317]. Indene-coumaronic resins were marketed in France by HGD (Huiles, Goudrons et Derives) in 1927. [Pg.223]

The first LMWPB was produced on an industrial scale in 1925 in Germany under the trade name Plastikator 32 [318]. In the United States products of this category were obtained in 1950 [318]. [Pg.223]

The year 1938 marked the start of terpenic resin production [319], while in 1940, the United States produced the first aromatic HRs using petroleum fractions as raw materials. Europe s aromatic HR production lagged to 1964 [320,321]. [Pg.223]

Mixed and cycloaliphatic copolymeric resins were achieved in the period between 1960 and 1970 [322]. Thus, in 1965, the main types of HRs were already known and commercialized, with a remarkable production capacity. [Pg.223]

For total HRs, one sees that it was the United States alone that in 1950 produced 50,000 t/year, after which the yield volume continually increased to reach 90,000 t/year in 1957, 130,000 in 1963, and approximately 160,000 t/year in 1968. Although petroleum aromatic fractions were used as raw materials to obtain HRs as late as 1940, it was only after 10 years that these fractions covered two-thirds of the whole HR yield volume. Further development of this industry was exclusively based on petroleum-origin raw materials. [Pg.223]


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