Refining process for production of refined palm-pressed fibre oil

Abstract ALLEGHENY LUDLUM E-BRITE 26-1 ALLOY is a low-carbon, low-nitrogen ferritic stainless steel made by a vacuum refining process. It provides: (1) Excellent resistance to pitting and crevice corrosion in chloride-containing environments, (2) Excellent resistance to chloride stress-corrosion cracking, (3) Resistance to intergranular corrosion, (4) Resistance to a wide variety of corrosive environments, and (5) Improved toughness and ductility after welding. Its applications include equipment for handling caustic, organic acids, nitric acid, bleach solutions, urea and chloride containing cooling waters. This datasheet provides information on composition, physical properties, microstructure, hardness, and tensile properties as well as fracture toughness. It also includes information on low temperature performance and corrosion resistance as well as forming, heat treating, machining, and joining. Filing Code: SS-360. Producer or source: Allegheny Ludlum Corporation.

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Extra colour removal in a refinery

Sugar Industry ◽

10.36961/si12200 ◽

2011 ◽

pp. 718-725 ◽

Cited By ~ 1

Author(s):

Laura Diego ◽

Fernando Martín ◽

Marta G de Quevedo ◽

Jaime Sagristá

Keyword(s):

Refining Process ◽

Ion Exchange Resins ◽

Colour Removal ◽

Precipitated Calcium Carbonate ◽

Sodium Bisulphite ◽

Powdered Carbon ◽

Raw Sugar ◽

Sugar Refinery ◽

Exchange Resins ◽

Main Factor

The main factor affecting the raw sugar refining process is certainly “colour”. The higher colour removal, the higher is the obtained sugar yield. Therefore, colour removal is the main goal throughout the process. In a conventional sugar refinery colour is removed in the purification and decolorisation steps – the second one is normally done using ion-exchange resins – but there are some other ways of colour removal such as adding some colour removing agents (powdered carbon, sodium bisulphite, PCC [precipitated calcium carbonate]). In this article the pilot plant results of experiments of increasing colour removal in the refining process are described, such as PCC addition, 3rd carbonatation (re-purification), hydrogen peroxide addition, powdered carbon addition, sodium bisulphite addition and crystallization improvements. The good results achieved in some of these trials led to perform some industrial trials, the results of wich are summarized in this article as well.

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A circulating ventilation system to concentrate pollutants and reduce exhaust volumes: Case studies with experiments and numerical simulation for the rubber refining process

Journal of Building Engineering ◽

10.1016/j.jobe.2020.101984 ◽

2020 ◽

pp. 101984

Author(s):

Lingjie Zeng ◽

Guodong Liu ◽

Jun Gao ◽

Bowen Du ◽

Lipeng Lv ◽

...

Keyword(s):

Numerical Simulation ◽

Case Studies ◽

Ventilation System ◽

Refining Process

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Numerical simulation analysis on solute redistribution of In–1 wt% Sn alloy during multipass vertical zone refining process

Journal of Crystal Growth ◽

10.1016/j.jcrysgro.2021.126156 ◽

2021 ◽

Vol 565 ◽

pp. 126156

Author(s):

Mingxu Li ◽

Qingle Tian ◽

Meizhen Wu ◽

Jubo Peng ◽

Jiatao Zhang ◽

...

Keyword(s):

Numerical Simulation ◽

Simulation Analysis ◽

Refining Process ◽

Zone Refining ◽

Solute Redistribution ◽

Vertical Zone

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Separation of Sn, Sb, Bi, and Cu from Tin Anode Slime by Solvent Extraction and Chemical Precipitation

Metals ◽

10.3390/met11030515 ◽

2021 ◽

Vol 11 (3) ◽

pp. 515

Author(s):

Wei-Sheng Chen ◽

Shota Mesaki ◽

Cheng-Han Lee

Keyword(s):

Solvent Extraction ◽

Liquid Phase ◽

Ph Value ◽

Chemical Precipitation ◽

Extraction Process ◽

Refining Process ◽

Anode Slime ◽

Electrolytic Refining ◽

Precipitation Procedure ◽

Tin Anode

Tin anode slime is a by-product of the tin electrolytic refining process. This study investigated a route to separate Sn, Sb, Bi, and Cu from tin anode slime after leaching with hydrochloric acid. In the solvent extraction process with tributyl phosphate, Sb and Sn were extracted into the organic phase. Bi and Cu were unextracted and remained in the liquid phase. In the stripping experiment, Sb and Sn were stripped and separated with HCl and HNO3. Bi and Cu in the aqueous phase were also separated with chemical precipitation procedure by controlling pH value. The purities of Sn, Sb, Cu solution and the Bi-containing solid were 96.25%, 83.65%, 97.51%, and 92.1%. The recovery rates of Sn, Sb, Cu, and Bi were 76.2%, 67.1%, and 96.2% and 92.4%.

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