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This report presents the economics of SBR production from n-butane and styrene. In this process, 1,3-Butadiene is initially produced from n-butane via a dehydrogenation process that is similar to Lummus Catadiene. Then, styrene and butadiene are polymerized via a typical cold emulsion process for generating a non-oil extended, non-staining grade of emulsion SBR (similar to 1502).
This report presents the economics of SBR production starting from butadiene and styrene. The analysis encompasses a plant located in the United States, employing a typical cold emulsion process for generating a non-oil extended, non-staining grade of emulsion SBR (similar to 1502). In this process, an emulsion comprising water, styrene and butadiene is polymerized into a latex, which is then coagulated to form the SBR.
This report presents the economics of high solids content SBR Latex production starting from butadiene and styrene. The analysis, based on a plant located in the United States, approaches a typical cold emulsion process. For generating a high solids latex with high butadiene content, the obtained low solids latex is further concentrated after polymerization.
This report targets SBR Latex production in the United States via a typical cold emulsion polymerization process. The main product generated is a low solids content SBR Latex with high styrene content.
This report presents the economics of SBR production from n-butane and styrene. In this process, 1,3-Butadiene is initially produced from n-butane via a dehydrogenation process that is similar to Lummus Catadiene. Then, styrene and butadiene are polymerized via a typical continuous solution process for producing a solution SBR grade.
This report presents the economics of SBR production starting from butadiene and styrene in the United States. It approaches a continuous process for producing a solution SBR grade. In this process, the anionic copolymerization of styrene and butadiene is carried out in the presence of cyclohexane solvent.