UNSATURATED POLYESTER RESIN (20 MT PER DAY OUTPUT)

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Polyester resins are unsaturated synthetic resins formed by the reaction of dibasic organic acids and polyhydric alcohols. Maleic Anhydride is a commonly used raw material with diacid functionality. Polyester resins are used in sheet moulding compound, bulk moulding compound and the toner of laser printers. Wall panels fabricated from polyester resins reinforced with fiberglass so-called fiberglass reinforced plastic (FRP) are typically used in restaurants, kitchens, restrooms and other areas that require washable low-maintenance walls. They are also used extensively in Cured-in-place pipe applications. Departments of Transportation in the USA also specify them for use as overlays on roads and bridges. In this application they are known as PCO Polyester Concrete Overlays. These are usually based on isophthalic acid and cut with styrene at high levels usually up to 50%.

Unsaturated polyesters are condensation polymers formed by the reaction of polyols (also known as polyhydric alcohols), organic compounds with multiple alcohol or hydroxy functional groups, with saturated or unsaturated dibasic acids. Typical polyols used are glycols such as ethylene glycol; acids used are phthalic acid, isophthalic acid and maleic acid. Water, a by-product of esterification reactions, is continuously removed, driving the reaction to completion. The use of unsaturated polyesters and additives such as styrene lowers the viscosity of the resin. The initially liquid resin is converted to a solid by cross-linking chains. This is done by creating free radicals at unsaturated bonds, which propagate in a chain reaction to other unsaturated bonds in adjacent molecules, linking them in the process. The initial free radicals are induced by adding a compound that easily decomposes into free radicals. This compound is usually and incorrectly known as the catalyst. Initiator is the more correct term. Substances used are generally organic peroxides such as benzoyl peroxide or methyl ethyl ketone peroxide.
Polyester resins are thermosetting and, as with other resins, cure exothermically. The use of excessive initiator especially with a catalyst present can, therefore, cause charring or even ignition during the curing process. Excessive catalyst may also cause the product to fracture or form a rubbery material.

Polyester resins are the most widely used resin systems, particularly in the marine industry. By far the majority of dinghies, yachts and workboats built in composites make use of this resin system.

Polyester resins such as these are of the ‘unsaturated’ type. Unsaturated polyester resin is a thermoset, capable of being cured from a liquid or solid state when subject to the right conditions. It is usual to refer to unsaturated polyester resins as ‘polyester resins’, or simply as ‘polyesters’. There is a whole range of polyesters made from different acids, glycols and monomers, all having varying properties.

There are two principle types of polyester resin used as standard laminating systems in the composites industry. Orthophthalic polyester resin is the standard economic resin used by many people. Isophthalic polyester resin is now becoming the preferred material in industries such as marine where its superior water resistance is desirable.

The figure below shows the idealized chemical structure of typical polyester. Note the positions of the ester groups (CO – O – C) and the reactive sites (C* = C*) within the molecular chain.

Most polyester resins are viscous, pale coloured liquids consisting of a solution of polyester in a monomer which is usually styrene. The addition of styrene in amounts of up to 50% helps to make the resin easier to handle by reducing its viscosity. The styrene also performs the vital function of enabling the resin to cure from a liquid to a solid by ‘cross-linking’ the molecular chains of the polyester, without the evolution of any by-products. These resins can therefore be moulded without the use of pressure and are called ‘contact’ or ‘low pressure’ resins. Polyester resins have a limited storage life as they will set or ‘gel’ on their own over a long period of time. Often small quantities of inhibitor are added during the resin manufacture to slow this gelling action.

For use in moulding, a polyester resin requires the addition of several ancillary products. These products are generally:

• Catalyst
• Accelerator
• Additives: Thixotropic; Pigment; Filler; Chemical/fire resistance

A manufacturer may supply the resin in its basic form or with any of the above additives already included. Resins can be formulated to the moulder’s requirements ready simply for the addition of the catalyst prior to moulding. As has been mentioned, given enough time an unsaturated polyester resin will set by itself. This rate of polymerisation is too slow for practical purposes and therefore catalysts and accelerators are used to achieve the polymerisation of the resin within a practical time period. Catalysts are added to the resin system shortly before use to initiate the polymerisation reaction. The catalyst does not take part in the chemical reaction but simply activates the process. An accelerator is added to the catalysed resin to enable the reaction to proceed at workshop temperature and/or at a greater rate. Since accelerators have little influence on the resin in the absence of a catalyst they are sometimes added to the resin by the polyester manufacturer to create a ‘pre-accelerated’ resin.

The molecular chains of the polyester can be represented as follows, where ‘B’ indicates the reactive sites in the molecule.

With the addition of styrene ‘S ‘, and in the presence of a catalyst, the styrene cross-links the polymer chains at each of the reactive sites to form a highly complex three-dimensional network as follows:

The polyester resin is then said to be ‘cured’. It is now a chemically resistant (and usually) hard solid. The cross-linking or curing process is called ‘polymerization’. It is a non-reversible chemical reaction. The ‘side-by-side’ nature of this cross-linking of the molecular chains tends to means that polyester laminates suffer from brittleness when shock loadings are applied.

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Description

INTRODUCTION
RAW MATERIAL
COMPONENTS OF POLYESTER RESINS
TYPES OF POLYESTER RESINS
SATURATED POLYESTER RESIN
UNSATURATED POLYESTER RESIN
FIRE RESISTANT POLYESTER RESIN
ELECTRICAL RESISTANT POLYESTER RESIN
LOW STYRENE EMISSION POLYESTER RESIN
ISOPHTHALIC POLYESTER RESINS FOR FIBERGLASS FABRICATIONS
THE DIFFERENT POLYESTER RESINS
CHARACTERISTICS AND BENEFITS OF POLYESTER RESIN
PERFORMANCE CHARACTERISTICS
SUGGESTED USE
RECOMENDED CATALYST
TYPICAL LIQUID RESIN PROPERTIES
TYPICAL CAST UNFILLED RESIN PROPERTIES
ADVANTAGE OF POLYESTER RESIN
POLYESTER RESIN OFFERS THE FOLLOWING ADVANTAGES:
PROPERTIES OF ISOPHTHALIC POLYESTER RESIN AND ORTHOPHTHALIC POLYESTER RESIN
PROPERTIES AND USES
A. FORMULATION DEPENDENT PROPERTIES
B. REACTION DEPENDENT PROPERTIES
CHARACTERISTIC OF JET UNDER THE CONDITIONS OF CURE: CURED
RESIN PROPERTIES:
PHYSICAL PROPERTIES OF CURED RESIN:
ELECTRICAL PROPERTIES OF CURED RESIN:
B.I.S. SPECIFICATIONS
MARKET OVERVIEW OF UNSATURATED POLYESTER RESIN
WORLD CONSUMPTION OF UNSATURATED POLYESTER RESINS – 2018
GLOBAL UNSATURATED POLYESTER RESIN MARKET SHARE,
BY END USE, 2019 (%)
GLOBAL UNSATURATED POLYESTER RESINS: MARKET TAXONOMY
BY PRODUCT TYPE
BY END-USER INDUSTRY
CONSUMPTION OF UNSATURATED POLYESTER RESIN
TOP FIVE EXPORT DESTINATIONS OF UNSATURATED POLYESTER RESIN
UNSATURATED POLYESTER RESIN
MANUFACTURING PROCESS OF UNSATURATED POLYESTER RESIN
REACTION
PROCESS FLOW DIAGRAM
MANUFACTURING PROCESS OF UNSATURATED POLYESTER RESIN
(USING POLYETHYLENE TEREPHTHALATE AS MAIN RAW MATERIAL)
PROCESS FLOW DIAGRAM
PROCESS IN DETAILS
PROCESS DETAILS
BLENDING OPERATION:
PACKAGING:
CHEMISTRY OF UNSATURATED POLYESTER RESIN
TECHNICAL DETAILS OF UNSATURATED POLYESTER RESIN MANUFACTURE
REACTION MECHANISM
THE CURING OF UNSATURATED POLYESTER RESINS
MONOMERS
THE POLYMERISATION PROCESS
FIG.: STRUCTURE OF METHYL ETHYL KETONE PEROXIDE
SYNTHESIS OF ISOPHTHALATE UPR
FORMULATION OF ISOPHTHALATE UPR
POLYESTER RESIN (FOR REINFORCED PLASTICS) G. P. GRADE
FORMULATION:-
PROPERTIES OF (REINFORCED GRADE POLYESTER RESIN)
POLYESTER RESIN (LAMINATE GRADE):-
FORMULATION – 1
PROCESS OF MANUFACTURING OF POLYESTER RESIN (LAMINATE GRADE)
POLYESTER VARNISH PREPARATION:-
MANUFACTURING PROCESS OF POLYESTER RESIN (ELECTRICAL GRADE)
POLYESTER G:-
POLYESTER VARISH:-
UNSATURATED POLYESTER RESINS
RAW MATERIALS
USING PHTHALIC ANHYDRIDE AS A MAIN RAW MATERIAL
USING POLYETHYLENE TEREPHTHALATE AS A MAIN RAW MATERIAL
TECHNICAL DATA SHEET OF ORTHOPHTHALIC POLYESTER RESIN
PHYSICAL PROPERTIES:
APPLICATION:
PACKING AND SHELF-LIFE:
SUPPLIERS OF PLANT AND MACHINERIES (GLOBAL)
SUPPLIERS OF RAW MATERIALS (GLOBAL)
SUPPLIERS OF COMPLETE PLANT AND EQUIPMENTS FOR UNSATURATED
POLYESTER RESINS
SUPPLIERS OF REACTORS
SUPPLIERS OF MIXERS
SUPPLIERS OF STORAGE TANK/ REACTION VESSELS
SUPPLIERS OF BOILER
SUPPLIERS OF LABORATORY EQUIPMENTS/LABORATORY TESTING
EQUIPMENTS
SUPPLIERS OF RAW MATERIALS
SUPPLIERS OF POLYPROPYLENE GLYCOL
SUPPLIERS OF PHTHALIC ANHYDRIDE
SUPPLIERS OF MALEIC ANHYDRIDE
SUPPLIERS OF POLYETHYLENE GLYCOL
SUPPLIERS OF STYRENE MONOMER
SUPPLIERS OF ANTIFOAMING AGENTS
SUPPLIERS OF STABILIZERS
PLANT LAYOUT

APPENDIX – A:

01. PLANT ECONOMICS
02. LAND & BUILDING
03. PLANT AND MACHINERY
04. OTHER FIXED ASSESTS
05. FIXED CAPITAL
06. RAW MATERIAL
07. SALARY AND WAGES
08. UTILITIES AND OVERHEADS
09. TOTAL WORKING CAPITAL
10. TOTAL CAPITAL INVESTMENT
11. COST OF PRODUCTION
12. TURN OVER/ANNUM
13. BREAK EVEN POINT
14. RESOURCES FOR FINANCE
15. INSTALMENT PAYABLE IN 5 YEARS
16. DEPRECIATION CHART FOR 5 YEARS
17. PROFIT ANALYSIS FOR 5 YEARS
18. PROJECTED BALANCE SHEET FOR (5 YEARS)

Additional information

Plant Capacity

20 MT/Day

Land & Building

(4000 sq.mt.)

Plant & Machinery

US$ 201428

Rate of Return

24$

Break Even Point

47%