WebMay 1, 2024 · The pulp and paper sector currently plays important part in the world's economy. In this paper, we present a review of pulping technologies to convert logs or wood chips and non-woody materials into pulp for use in papermaking which consist of mechanical, chemical and semi-mechanical. WebAnthraquinone and Polysulfide - Applicability foe Use in Pulp Mill Operations / 253 Deal, H., TAPPI 1996 Pulping Conference Proceedings , TAPPI PRESS, Atlanta, p. 73 Sulfide Profiling for Increased Kraft Pulping Selectivity / 261 Jiang, J.E. and Herschmiller, D.W., TAPPI 1996 Pulping Conference Proceedings, TAPPI PRESS, Atlanta, p.311
Pulp and paper industry: An overview on pulping technologies, …
WebMay 1, 2024 · The pulp and paper sector currently plays important part in the world's economy. In this paper, we present a review of pulping technologies to convert logs or … WebB. Calculation of the H-factor. The brief results of calculating the H-factor as a means of expressing cooking temperature and time duration as a single variable during the kraft pulping are presented in Table 2. The greater value of H-factor level implies the more severe intense kraft cooking condition, and vice versa. machine disc rotors
Kraft pulping of softwood chips with mild hot water pre-hydrolysis …
WebMay 16, 2024 · Depending on the fiber type, chemical pulping can be conducted in either a 25-liter vertical batch digester, a 25-liter rotating digester, a 500-liter Continuously Stirred Tank Reactor (CSTR) or a 2500-liter vertical batch digester. Each digester is computer controlled to allow precise temperature ramps and controlled H-factor pulping. WebThe pulping results are shown in Table 4. For an increase in delignification level (kappa reduction), a raising of the alkali charge and also of the H factor were necessary. In this work, the rise in the H factor was achieved by increasing the maximum cooking temperature, while the time was the same in all experiments. WebKraft pulping is considered as most dominant process to obtain lignin from the lignocellulosic biomass. In pulping process via kraft method, aqueous sodium hydroxide along with sulfides at a temperature range of 423–453 K for 2 h to separate lignin from the cellulose under high pH condition [2]. machine dispenser candy