Polytrimethylene Terephthalate Production - Cost Analysis - PTT E21A

Polytrimethylene Terephthalate Production - Cost Analysis - PTT E21A PDF Author: Intratec
Publisher: Intratec
ISBN:
Category : Business & Economics
Languages : en
Pages : 102

Get Book Here

Book Description
This report presents a cost analysis of Polytrimethylene Terephthalate (PTT) production starting from glucose syrup and terephthalic acid. The process examined combines a process similar to DuPont process for generating propanediol and a process similar to Degussa (now Evonik) process for producing PTT. In this process, a 70 wt% glucose-water syrup is used as raw material. This report was developed based essentially on the following reference(s): Keywords: 1,3-Polypropylene Terephthalate, TPA, Dimethyl Terephthalate, DMT, Bio-PDO, Trimethylene Glycol, PTT, Aerobic Fermentation

Polytrimethylene Terephthalate Production - Cost Analysis - PTT E21A

Polytrimethylene Terephthalate Production - Cost Analysis - PTT E21A PDF Author: Intratec
Publisher: Intratec
ISBN:
Category : Business & Economics
Languages : en
Pages : 102

Get Book Here

Book Description
This report presents a cost analysis of Polytrimethylene Terephthalate (PTT) production starting from glucose syrup and terephthalic acid. The process examined combines a process similar to DuPont process for generating propanediol and a process similar to Degussa (now Evonik) process for producing PTT. In this process, a 70 wt% glucose-water syrup is used as raw material. This report was developed based essentially on the following reference(s): Keywords: 1,3-Polypropylene Terephthalate, TPA, Dimethyl Terephthalate, DMT, Bio-PDO, Trimethylene Glycol, PTT, Aerobic Fermentation

Polytrimethylene Terephthalate Production - Cost Analysis - PTT E11A

Polytrimethylene Terephthalate Production - Cost Analysis - PTT E11A PDF Author: Intratec
Publisher: Intratec
ISBN:
Category : Business & Economics
Languages : en
Pages : 102

Get Book Here

Book Description
This report presents a cost analysis of Polytrimethylene Terephthalate (PTT) production from terephthalic acid and propanediol. The process examined is similar to Degussa (now Evonik) process. This report was developed based essentially on the following reference(s): (1) US Patent 7223830, issued to Zimmer in 2007 (assigned to Lurgi Zimmer GmbH in 2008) (2) EP Patent 0859020, issued to Zimmer and Degussa (now Evonik) in 2006 (3) US Patent 68007, issued to Zimmer and Shell in 2004 (assigned to Lurgi Zimmer GmbH in 2008) Keywords: 1,3-Polypropylene Terephthalate, TPA, PDO, Dimethyl Terephthalate, DMT

Polytrimethylene Terephthalate Production - Cost Analysis - PTT E31B

Polytrimethylene Terephthalate Production - Cost Analysis - PTT E31B PDF Author: Intratec
Publisher: Intratec
ISBN:
Category : Business & Economics
Languages : en
Pages : 102

Get Book Here

Book Description
This report presents a cost analysis of Polytrimethylene Terephthalate (PTT) production starting from raw sugar and terephthalic acid. The process examined combines a process similar to DuPont process for generating propanediol and a process similar to Degussa (now Evonik) process for producing PTT. In this process, raw sugar (sucrose) is diluted and sucrose is hydrolyzed into glucose and fructose (invert sugars). The invert sugars are then fermented to produce Propanediol. This report was developed based essentially on the following reference(s): Keywords: 1,3-Polypropylene Terephthalate, TPA, Dimethyl Terephthalate, DMT, Bio-PDO, Trimethylene Glycol, PTT, Aerobic Fermentation

Polyethylene Terephthalate Production Process - Cost Analysis - PET E11A

Polyethylene Terephthalate Production Process - Cost Analysis - PET E11A PDF Author: Intratec
Publisher: Intratec Solutions
ISBN:
Category : Business & Economics
Languages : en
Pages : 101

Get Book Here

Book Description
This report presents a cost analysis of Polyethylene Terephthalate (PET) production from ethylene glycol and purified terephthalic acid (PTA). The process examined is a typical melt-phase polymerization followed by solid-state polymerization. In this process, initially an oligomer intermediate is produced by the esterification of PTA with ethylene glycol. The oligomer then undergoes a melt-polymerization and a solid-state polymerization, leading to a bottle grade PET. This report was developed based essentially on the following reference(s): (1) "Polyesters, Thermoplastic", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition (2) "Polyesters", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition Keywords: Thermoplastic Polymer, Polyester, High Intrinsic Viscosity, Melt-Phase Polycondensation

Polyethylene Terephthalate Production Process - Cost Analysis - PET E12A

Polyethylene Terephthalate Production Process - Cost Analysis - PET E12A PDF Author: Intratec
Publisher: Intratec Solutions
ISBN:
Category : Business & Economics
Languages : en
Pages : 102

Get Book Here

Book Description
This report presents a cost analysis of Polyethylene Terephthalate (PET) production from ethylene glycol and purified terephthalic acid (PTA). The process examined is similar to Invista NG3 process. In this process, PET oligomers are first polymerized in a melt-phase step, and then passed through a solid-state polymerization step. This report was developed based essentially on the following reference(s): US Patents 5786443 and 5730913, both issued to DuPont in 1998 (both assigned to Invista in 2004) Keywords: Thermoplastic Polymer, Polyester, High Intrinsic Viscosity, Melt-Phase Polycondensation

Polybutylene Terephthalate Production from DMT - Cost Analysis - PBT E11A

Polybutylene Terephthalate Production from DMT - Cost Analysis - PBT E11A PDF Author: Intratec
Publisher: Intratec
ISBN:
Category : Business & Economics
Languages : en
Pages : 102

Get Book Here

Book Description
This report presents a cost analysis of Polybutylene Terephthalate (PBT) production from dimethyl terephthalate (DMT). The process examined is a typical transesterification and polycondensation process. This report was developed based essentially on the following reference(s): Keywords: Polyester, Bishydroxybutyl Terephthalate, HBT, Melt Polymerization, Solid State Polymerization

Medium-Purity Terephthalic Acid Production - Cost Analysis - TPA E11A

Medium-Purity Terephthalic Acid Production - Cost Analysis - TPA E11A PDF Author: Intratec
Publisher: Intratec Solutions
ISBN: 1945324910
Category : Business & Economics
Languages : en
Pages : 52

Get Book Here

Book Description
This report presents a cost analysis of Medium-Purity Terephthalic Acid (MTA) production from p-xylene. The process examined is a typical catalytic oxidation process. In this process, p-xylene is oxidized to Terephthalic Acid. Subsequently, the Terephthalic Acid is crystallized and recovered from the liquor and MTA is obtained as the final product. This report examines one-time costs associated with the construction of a United States-based plant and the continuing costs associated with the daily operation of such a plant. More specifically, it discusses: * Capital Investment, broken down by: - Total fixed capital required, divided in production unit (ISBL); infrastructure (OSBL) and contingency - Alternative perspective on the total fixed capital, divided in direct costs, indirect costs and contingency - Working capital and costs incurred during industrial plant commissioning and start-up * Production cost, broken down by: - Manufacturing variable costs (raw materials, utilities) - Manufacturing fixed costs (maintenance costs, operating charges, plant overhead, local taxes and insurance) - Depreciation and corporate overhead costs * Raw materials consumption, products generation and labor requirements * Process block flow diagram and description of industrial site installations (production unit and infrastructure) This report was developed based essentially on the following reference(s): "Terephthalic Acid, Dimethyl Terephthalate, and Isophthalic Acid", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition Keywords: Para-xylene, TPA, Post-Oxidation Reactor, Mitsubishi, Eastman, Lurgi, Medium Quality, QTA, EPTA

Polyethylene Furanoate Production from Glucose - Cost Analysis - PEF E21A

Polyethylene Furanoate Production from Glucose - Cost Analysis - PEF E21A PDF Author: Intratec
Publisher: Intratec
ISBN:
Category : Business & Economics
Languages : en
Pages : 103

Get Book Here

Book Description
This report presents a cost analysis of Polyethylene Furanoate (PEF) production starting from glucose and monoethylene glycol (MEG). The process examined is similar to the Avantium YXY process, followed by a process that copolymerizes FDCA and MEG. In this process, a 70 wt% glucose-water syrup feed is isomerized to fructose. Then, fructose is converted to methoxy methyl furan (MMF) intermediate, which is oxidized to FDCA. This process generates methyl acetate and methyl levulinate as by-products. The FDCA generated and MEG are polymerized to PEF in two polymerization steps in order to obtain Bottle-Grade PEF. This report was developed based essentially on the following reference(s): (1) US Patent 8519167, issued to Furanix Technologies B.V. in 2013 (2) US Patent 20160024039, issued to Furanix Technologies B.V. in 2016 (3) WO Patent 2015137807, issued to Furanix Technologies in 2015 Keywords: Polyethylene Furanoate, PEF, Green FDCA, Hydroxyl Methyl Furfural, HMF, Purified Terephthalic Acid, Polyethylene 2,5-Furandicarboxylate, MEG

Terephthalic Acid Production from p-Xylene - Cost Analysis - TPA E12A

Terephthalic Acid Production from p-Xylene - Cost Analysis - TPA E12A PDF Author: Intratec
Publisher: Intratec Solutions
ISBN: 1945324112
Category : Business & Economics
Languages : en
Pages : 53

Get Book Here

Book Description
This report presents a cost analysis of Purified Terephthalic Acid (PTA) production from p-xylene. The process examined is a conventional catalytic oxidation process. In this process, p-xylene is oxidized to Terephthalic Acid. The Terephthalic Acid from reaction passes through separation and drying steps and Crude Terephthalic Acid (CTA) is obtained as an intermediate. Subsequently, the CTA is subjected to purification via hydrogenation and PTA is separated as the final product. This report examines one-time costs associated with the construction of a United States-based plant and the continuing costs associated with the daily operation of such a plant. More specifically, it discusses: * Capital Investment, broken down by: - Total fixed capital required, divided in production unit (ISBL); infrastructure (OSBL) and contingency - Alternative perspective on the total fixed capital, divided in direct costs, indirect costs and contingency - Working capital and costs incurred during industrial plant commissioning and start-up * Production cost, broken down by: - Manufacturing variable costs (raw materials, utilities) - Manufacturing fixed costs (maintenance costs, operating charges, plant overhead, local taxes and insurance) - Depreciation and corporate overhead costs * Raw materials consumption, products generation and labor requirements * Process block flow diagram and description of industrial site installations (production unit and infrastructure) This report was developed based essentially on the following reference(s): (1) "Terephthalic Acid, Dimethyl Terephthalate, and Isophthalic Acid", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition; (2) EP Patent 0824653, issued to DuPont in 2000 Keywords: Para-xylene, Paraxylene, TPA, CTA, Hydrogenation, Amoco, Catalytic Oxidation, Acetic Acid, BP, X Technology, PET, Polyethylene Terephthalate, Bromine

Terephthalic Acid Production from p-Xylene - Cost Analysis - TPA E13A

Terephthalic Acid Production from p-Xylene - Cost Analysis - TPA E13A PDF Author: Intratec
Publisher: Intratec Solutions
ISBN: 1945324120
Category : Business & Economics
Languages : en
Pages : 53

Get Book Here

Book Description
This report presents a cost analysis of Purified Terephthalic Acid (PTA) production from p-xylene. The process examined is similar to BP X Technology. In this process, p-xylene is oxidized to Terephthalic Acid. The Terephthalic Acid from reaction is separated as a Crude Terephthalic Acid (CTA) intermediate. The CTA is subjected to hydrogenation and PTA is obtained as the final product. The drying and storage of the CTA intermediate is not necessary in this process. This report examines one-time costs associated with the construction of a United States-based plant and the continuing costs associated with the daily operation of such a plant. More specifically, it discusses: * Capital Investment, broken down by: - Total fixed capital required, divided in production unit (ISBL); infrastructure (OSBL) and contingency - Alternative perspective on the total fixed capital, divided in direct costs, indirect costs and contingency - Working capital and costs incurred during industrial plant commissioning and start-up * Production cost, broken down by: - Manufacturing variable costs (raw materials, utilities) - Manufacturing fixed costs (maintenance costs, operating charges, plant overhead, local taxes and insurance) - Depreciation and corporate overhead costs * Raw materials consumption, products generation and labor requirements * Process block flow diagram and description of industrial site installations (production unit and infrastructure) This report was developed based essentially on the following reference(s): (1) EP Patent 1054855, issued to BP Amoco in 2000; (2) US Patent 20150166452, issued to BP in 2015 Keywords: Para-xylene, Paraxylene, TPA, CTA, Hydrogenation, Amoco, Catalytic Oxidation, Acetic Acid, BP, X Technology, PET, Polyethylene Terephthalate