Activated Carbon by Potassium Carbonate Activation from Pine Sawdust ( Pinus montezumae Lamb.)

2020 ◽  
Vol 43 (9) ◽  
pp. 1716-1725
Author(s):  
Francisco Márquez-Montesino ◽  
Neil Torres-Figueredo ◽  
Adela Lemus-Santana ◽  
Fernando Trejo
Fuel ◽  
1983 ◽  
Vol 62 (2) ◽  
pp. 221-225 ◽  
Author(s):  
Freek Kapteijn ◽  
Jacob A. Moulijn

2019 ◽  
Vol 21 (5) ◽  
pp. 2382-2388
Author(s):  
Wenliang Zhu ◽  
Kohei Okada ◽  
Zhong Li ◽  
Jiliang Zhu ◽  
Elia Marin ◽  
...  

Percolative composites consisting of potassium carbonate dispersed in polyvinylidene fluoride (PVDF) polymeric matrix have shown high dielectric constant and electrical conductivity due to the formation of chemically activated carbon interfaces in the composite.


1984 ◽  
Vol 49 (3) ◽  
pp. 592-596 ◽  
Author(s):  
Libor Červený ◽  
Nguyen Thi Thanh ◽  
Vlastimil Růžička

The competitive catalytic hydrogenation of 2-octyne and 1-heptene in methanol has been studied on catalysts 3% Pd on activated carbon and Pd black, modified with ammonium chloride, potassium chloride, potassium carbonate, or calcium carbonate. The rates of hydrogenation of the two substrates and the rate of isomerization of 1-heptene have been determined. The effect of inorganic salts on the activity and selectivity of the catalysts is discussed.


2011 ◽  
Vol 704-705 ◽  
pp. 517-522 ◽  
Author(s):  
Xiao Juan Jin ◽  
Zhi Ming Yu ◽  
Gao Jiang Yan ◽  
Wu Yu

Activated carbons were prepared through chemical activation of lignin from straw pulping precursor using potassium carbonate as the chemical agent. Effects of activated temperature, K2CO3/lignin ratio and the activated time on the yield, Iodine number of activated carbon were investigated. Experimental results indicated that the optimum conditions were as follow: activated temperature 800°C, K3CO3(40% concentration) /lignin ratio 5: l, activated time 50min. These conditions allowed us to obtain a BET surface area of 1104 m2/g, including the external or non-microporous surface of 417 m2/g,Amount of methylene blue adsorption, Iodine number and the yield of activated carbon prepared under optimum conditions were 10.6mL/0.lg,1310 mg/g and 19.75%, respectively.


2021 ◽  
Vol 57 (2) ◽  
pp. 106-113
Author(s):  
A.Zh. Yerman ◽  
◽  
A.A. Atchabarovа ◽  
K.K. Kishibaev ◽  
◽  
...  

This article presents the optimal results of new sorbents for the sorption separation of nickel and cadmium ions based on waste of plant raw materials of the Republic of Kazakhstan - pine sawdust. To obtain activated carbon, pine sawdust based on plant waste was subjected to thermal treatment by carbonization methods at a temperature of 600-800 ° C and hydrothermal 220-260 ° C. Further, to increase the specific surface area, the samples after heat treatment were activated with hot water vapor at a temperature of 800-850 ° C for 1 hour. As a result of steam-gas activation, combustion of unstructured carbon and an increase in pores on the surface of activated carbon occur. In addition, the main physicochemical characteristics, sorption properties of the obtained activated carbon (specific surface area, m2 /g, fraction of pore volume, cm3 /g, average pore size, nm, sorption capacity by the amount of iodine,%) are considered. Also, the obtained sorption materials were studied in the process of sorption of nickel and cadmium ions from model solutions in a static mode. The optimal parameters of the sorption process were determined, at which the highest degree of extraction of nickel and cadmium ions is achieved: pH, phase contact time, ratio of solid and liquid phases. The recovery rate of cadmium and nickel ions in the static regime was more than 95% for cadmium and nickel. Keywords: activated carbon, sorbent, sorption, plant waste, nickel ion, cadmium ion


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