Composites product; a pultrusion continuous method for manufacturing thereof

Abstract

The composite pultruded products either in “I” profile or “Plate” profile of higher cross sectional area where said products consisting essentially synthetic polyester felts as core impregnated with a resin system comprises of at least one resin, curing system comprising a curing agent and an accelerator, a filler, a thinner, pigment or any other additives; encapsulated between bi-directionally and/or uni-directionally oriented synthetic fabric selected from polyester, carbon, aramid, glass, basalt and mixtures thereof impregnated with said resin system are provided. In another composite pultruded products either in “I” profile or “Plate” profile of higher cross sectional area where said products consisting of plank of short fibers bagasse premixed with the said resin system as core is enclosed between the synthetic polyester felts impregnated with the resin system which is further enclosed between bi-directionally and/or uni-directionally oriented synthetic fabric selected from polyester, carbon, aramid, glass, basalt and mixtures thereof impregnated with the resin system. The system and method for the preparation of said composite pultruded products are also illustrated herein. These products lead to a significant reduction in weight and reduction in density with higher stiffness and bending strength. The present composite products are encapsulated by fabrics in the peripheral area bringing more integrity uniformity of synthetic polyester felt materials. This leads to a significant cost reduction without sacrificing much tensile strength.

Claims

1. A composite pultruded product consisting essentially of: 10 to 50% by volume synthetic polyester felts as a core; 10 to 30% by volume bi-directionally and/or uni-directionally oriented synthetic fabric selected from polyester, carbon, aramid, glass, basalt, and mixtures thereof, wherein the felts are encapsulated between the fabric; and 40 to 60% by volume of a resin system impregnating the felts and the fabric, wherein the composite product is either I profiled or Plate profiled.

2. The product of claim 1, wherein the synthetic polyester felts are needle punched mat of polyester felts having weight 400 to 1000 GSM.

3. The product of claim 1, wherein the resin system includes a resin and a curing system including a curing agent and at least one of an accelerator, filler, thinner, and pigment.

4. The product of claim 3, wherein the resin is one of, a thermosetting resin selected from unsaturated polyester, epoxy, polyurethane, phenolic resins, and mixtures thereof, a thermoplastic resin selected from polyethylene, polypropylene, acrylonitrile-butadiene-styrene, polyacetal, polyamide, polyimide, saturated polyester resins, and mixtures thereof, and a mixture thereof.

5. A composite pultruded product consisting essentially of: plank of bagasse fibers as a core; synthetic polyester felts, wherein the plank of bagasse fibers are encapsulated between the felts; bi-directionally and/or uni-directionally oriented synthetic fabric selected from polyester, carbon, aramid, glass, basalt, and mixtures thereof, wherein the felts are enclosed between the fabric; and; a resin system mixed in the bagasse fibers and impregnating the felts and the fabric, wherein the composite product is either I profiled or Plate profiled.

6. The product of claim 5, wherein the product comprises 10 to 40% by volume the synthetic polyester felts, 5 to 10% by volume the synthetic fabric, 10 to 30% by volume the bagasse fibers, and 40 to 60% by volume the resin system.

7. The product of claim 5, wherein the synthetic polyester felts are needle punched mat of polyester felts having weight 400 to 1000 GSM.

8. The product of claim 5, wherein the bagasse fibers are premixed with the resin system in equal volumes.

9. The product of claim 5, wherein the resin system includes a resin and a curing system including a curing agent and at least one of an accelerator, filler, thinner, and pigment.

10. The product of claim 9, wherein the resin is one of, a thermosetting resin selected from unsaturated polyester, epoxy, polyurethane, phenolic resins, and mixtures thereof, a thermoplastic resin selected from polyethylene, polypropylene, acrylonitrile-butadiene-styrene, polyacetal, polyamide, polyimide, saturated polyester resins, and mixtures thereof, and a mixture thereof.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1A illustrates a plate profiled bio-composite pultruded product having coextruded bagasse as core encapsulated with synthetic polyester felt which is further encapsulated with glass fabrics; FIG. 1B illustrates a plate profiled bio-composite pultruded product having synthetic polyester felt as core encapsulated with glass fabrics; and FIG. 1C illustrates a plate profiled bio-composite pultruded product having synthetic polyester felt as core encapsulated with polyester fabrics.

(2) FIG. 2A illustrates an “I” profiled bio-composite pultruded product having coextruded bagasse as core encapsulated with synthetic polyester felt which is further encapsulated with glass fabrics; FIG. 2B illustrates an “I” profiled bio-composite pultruded product having synthetic polyester felt as core encapsulated with glass fabrics; and FIG. 2C illustrates an “I” profiled bio-composite pultruded product having synthetic polyester felt as core encapsulated with polyester fabrics.

(3) FIG. 3 illustrates a pultrusion apparatus for continuous production of a composite pultruded product; particularly “Plate” or “I” profiled as shown in FIG. 1B and FIG. 1C and FIG. 2B and FIG. 2C.

(4) FIG. 4 illustrates a pultrusion apparatus for continuous production of a composite pultruded product; particularly “Plate” or “I” profiled as shown in FIG. 1A and FIG. 2A.

DETAILED DESCRIPTION

(5) The present invention as described below, it is to be understood that this invention is not limited to particular embodiments, drawings, methodologies and materials described, as these may vary as per the person skilled in the art. It is also to be understood that the terminology used in the description is for the purpose of describing the particular embodiments only, and is not intended to limit the scope of the present invention.

(6) Before the present invention is described, it is to be understood that unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. Further, it is to be understood that the present invention is not limited to the methodologies and materials similar or equivalent to those described herein can be used in the practice or testing of the present invention, the preferred methods and materials are described, as these may vary within the specification indicated. Unless stated to the contrary, any use of the words such as “including,” “containing,” “comprising,” “having” and the like, means “including without limitation” shall not be construed to limit any general statement that it follows to the specific or similar items or matters immediately following it. Embodiments of the invention are not mutually exclusive, but may be implemented in various combinations. The described embodiments of the invention and the disclosed examples are given for the purpose of illustration rather than limitation of the invention as set forth the appended claims. Further the terms disclosed embodiments are merely exemplary methods of the invention, which may be embodied in various forms.

(7) It is also to be understood that the terms “a”, “an”, “the” and like are words for the sake of convenience and are not to be construed as limiting terms. Moreover, it will be understood that the illustrations are for the purpose of describing a particular exemplary embodiment of the invention and are not limited to the invention thereto.

(8) The term “fibres” or “fibre” or “fabric” or “fabrics” are interchangeable and intends to cover single as well as plural fibre or fabric.

(9) The term “Composite” may be read as “Bio-composite” in the specification where composite product comprises bagasse as one of the constituent.

(10) According to one of the embodiments of the invention, there is provided composite pultruded product consisting essentially synthetic polyester felt as core impregnated with a resin system, enclosed between bi-directionally and/or uni-directionally oriented synthetic fabric selected from polyester, carbon, aramid, glass, basalt and mixtures thereof impregnated with a resin system;

(11) said bio-composite product is either in “Plate” profile [FIG. 1 (B) or (C)] or “I” profile [FIG. 2 (B) or (C)].

(12) Preferably, the product comprises 10 to 50% by vol. of synthetic polyester felt, 10 to 30% by vol. of synthetic fabric and 40 to 60% by vol. of resin system.

(13) According to another embodiment of the invention there is provided another composite pultruded product consisting essentially plank of short fibers bagasse premixed with a resin system as core encapsulated between a synthetic polyester felt impregnated with the resin system which is further encapsulated between bi-directionally and/or uni-directionally oriented synthetic fabric selected from polyester, carbon, aramid, glass, basalt and mixtures thereof impregnated with the resin system;

(14) said composite product is either in “Plate” profile [FIG. 1 (A)] or “I” profile[FIG. 2 (A)].

(15) Preferably, the product comprises 10 to 40% by vol. of synthetic polyester felt, 5 to 10% by vol. of synthetic fabric, 10 to 30% by vol. of bagasse short fibres and 40 to 60% by vol. of resin system.

(16) Typically, the bagasse fibres are premixed with the resin system prior to extrusion in equal proportion.

(17) The resin system used for impregnation of natural fibers or synthetic felt/fabric, comprise of at least a resin, curing system comprising curing agent and accelerator, filler, thinner, pigment or any other additives.

(18) Particularly, the resin used in the resin system is either a thermosetting resin selected from unsaturated polyester, epoxy, polyurethane, phenolic resins and mixture thereof or a thermoplastic resin selected from polyethylene, polypropylene, acrylonitrile-butadiene-styrene, polyacetal, polyamide, polyimide, saturated polyester resins and mixtures thereof.

(19) Particularly, the curing agent used in the resin system is selected from methyl ethyl ketone peroxide, cumene hydroperoxide, t-butyl hydroperoxide, benzoyl peroxide, and/or hydrogen peroxide.

(20) Particularly, the accelerators used in the resin system is selected from cobalt naphthenate and/or cobalt octoate.

(21) Particularly, the filler used in the resin system is calcium carbonate.

(22) Particularly, thinner is methanol.

(23) Two types of resin systems are used in the present invention.

(24) First type of the resin system comprises at least 100 parts per hundred (pph) of resin and at least 20 pph of Thinner. Particularly, the resin system comprises 100 pph of phenol formaldehyde resin and 20 pph of methanol.

(25) Second type of the resin system comprises at least 100 pph of resin, at least 1.7 pph of curing system, at least 2 pph of filler, and at least 10 pph of thinner. Particularly, the resin system comprises 100 pph of polyester, 1.7 pph of curing system comprising 0.2 pph of cobalt octoate and 1.5 pph of benzoyl peroxide, 2 pph of calcium carbonate and 10 pph of methanol.

(26) The synthetic polyester felt used in the composite products is in the form of needle punched mat having weight in the range of 400 to 1000 GSM. The needle punched mat of synthetic polyester felt is prepared from waste PET bottles to reduce the cost of production.

(27) Synthetic polyester felt is required to be passed through IR heater for dehumidification so as to enhance resin affinity.

(28) The core of the products may include coextruded bagasse plank or bagasse mixed with resin system and further coextruded into plank or natural fibers including mat impregnated with the resin system. However, use of combination of bagasse along with natural fibers including mat with or without the resin system should be considered within the scope of the invention.

DETAILED DESCRIPTION OF THE ACCOMPANYING DRAWINGS

(29) FIG. 1(A) illustrates sectional view of Plate profiled composite product (100), where coextruded bagasse plank (101) as core encapsulated with synthetic polyester felt (102), which is further encapsulated with glass fabrics (103).

(30) FIG. 1(B) illustrates sectional view of Plate profiled composite product (104), where synthetic polyester felt (105) as core which is encapsulated with glass fabrics (106).

(31) FIG. 1(C) illustrates sectional view Plate profiled composite product (107), where synthetic polyester felt (108) as core which is encapsulated with polyester fabrics (109).

(32) FIG. 2(A) illustrates sectional view of “I” profiled composite product (110), where coextruded bagasse plank (111) as core encapsulated with synthetic polyester felt (112), which is further encapsulated with glass fabrics (113).

(33) FIG. 2(B) illustrates sectional view of “I” profiled composite product (114), where synthetic polyester felt (115) as core which is encapsulated with glass fabrics (116).

(34) FIG. 2(C) illustrates sectional view of “I” profiled composite product (117), where synthetic polyester felt (118) as core which is encapsulated with polyester fabrics (119).

(35) The pultrusion system for continuous production of composite pultruded products of the invention is illustrated in FIG. 3.

(36) In the FIG. 3, roller stands are used in place of conventionally used creel stand. Roller stand occupies less space as compared to creel stand.

(37) The pultrusion system for continuous production of composite pultruded products of the invention comprises:

(38) a roller stand (4) provided with at least three roller means (1, 2, 3) to feed at least one synthetic polyester felt and at least two synthetic fibres;

(39) a heating means (5), preferably IR heater, said IR heater is in close proximity to roller means (1, 2, 3) of roller stands (4) so as to pass synthetic polyester felt and synthetic fibres through it to reduce moisture from thereof;

(40) an enclosed resin bath (6) provided with a resin storage and charging unit (8) and preforming die (7) enclosed in it; said resin storage and charging unit adapted to provide resin system for impregnation of the fibres to said resin bath (6), and said preforming die (7) having die cavity about longitudinal axis and tapering at end so as to squeeze fibres impregnated with resin; said resin bath is in close proximity to said IR heater (5) so as to pass synthetic polyester felt and synthetic fibres through said resin bath followed by said preforming die cavity (7);

(41) heating means (9), preferably heating plates provided to said preforming die (7) to encapsulate along its length; said die (7) being activable to heat to transfer a precured preform of squeezed resin impregnated fibres to further location;

(42) a pultrusion die (10) provided in close proximity to said preforming die (7) so as to pass said precured preform of squeezed resin impregnated fibres through it;

(43) heating means (11), preferably heating plates provided to said pultrusion die (10) to encapsulate along its length; said die (10) being activable to heat to transfer a cured pultruded bio-composite product to further location; and

(44) an external pultrusion puller (12) provided at the end of the system to pull said cured pultruded bio-composite product from said pultrusion die (10);

(45) said cured pultruded composite product consisting essentially synthetic polyester felt impregnated with said resin system as core encapsulated between bi-directionally and/or uni-directionally oriented synthetic fabric impregnated with said resin system;

(46) said composite product is either in “I” profile [FIG. 1 (B) or (C)] or “Plate” profile [FIG. 2 (B) or (C)].

(47) The step of reducing moisture by passing natural or synthetic fibres or fabric or mat through IR heater enhances affinity of the mats, fibres or fabrics towards the resin system. The ability of the mats, fibres or fabrics to readily absorb resin is essential for production of the composite products.

(48) Typically, the synthetic polyester felt or synthetic fabric is passed through IR heater (5) by maintaining speed of 2 to 6 meter per hour of fibres/fabric/mat in it. After passing through IR heater, the natural fibre or synthetic fabric has 3 to 4% moisture.

(49) Typically, the precured preform obtained from preforming die (7) is squeezed mats, fibres or fabrics which are at least 40% impregnated with the resin system.

(50) Typically, the preforming die (7) having cavity designed to be adapted “I” profile or “Plate” profile.

(51) Typically, “I” profiled die having cavity adapted to have dimension of 20 mm thick of I beam of flange with width 70 mm and height of 120 mm.

(52) Typically, “Plate” profiled die having cavity adapted to have dimension of 8-16 mm thick and 600-1200 mm width.

(53) Typically, the preforming die (7) is maintained at temperature in the range of 70 to 90° C. by using heating mean (9).

(54) Typically, the pultrusion die (10) having cylindrical cavity die adapted to process precured “I” profiled or “Plate” profiled preform through it.

(55) Typically, the pultrusion die (10) is maintained at temperature in the range of 160 to 180° C. by using heating mean (11).

(56) Typically, the synthetic polyester felt and the synthetic fabric is passed at speed of 2 to 6 meter per hour through enclosed resin bath (6) for the impregnation of synthetic polyester felt and the synthetic fabric.

(57) Typically, the resin impregnated felt or fabric is passed at speed of 2 to 6 meter per hour through the preforming die (7) to obtain precured “I” profiled or “Plate” profiled preform.

(58) Typically the precured “I” profiled or “Plate” profiled preform is passed at speed of 2 to 6 meter per hour through the pultrusion die (10) to obtain cured “I” profiled or “Plate” profiled preform.

(59) According to still another embodiment of the invention, there is provided a continuous pultrusion method for production of the composite pultruded products of the invention by using the system of the invention as illustrated in FIG. 3.

(60) In this method, 10 to 50% by vol. of synthetic polyester felt are provided by roller mean (2) and 10 to 30% by vol. of synthetic fabric selected from polyester, carbon, aramid, glass, basalt and mixtures thereof are provided by roller means (1 and 3). These felts/fibres/fabrics are passed through IR heater (5) at speed of 2 to 6 meter per hour to reduce moisture from thereof. These felts/fibres/fabrics are impregnated by passing them at speed of 2 to 6 meter per hour through the resin bath (6) comprising a resin system followed by passing them at speed of 2 to 6 meter per hour through a preforming die (7) under heating at temperature in the range of 70 to 90° C. by using heating means (9) to obtain a precured preform of squeezed felts/fibres/fabrics impregnated with the said resin system. The precured preform of squeezed fibres impregnated with the resin system is transferred from the said die (7) to pultrusion die (10); die (7) is activable to heat to transfer said precured preform to pultrusion die (10). The said precured preform is passed at speed of 2 to 6 meter per hour through pultrusion die (10) under heating at temperature in the range of 160 to 180° C. using heating means (11) to obtain a cured pultruded hybrid composite product. The said die (10) being activable to heat to transfer and expel said cured pultruded composite product. The said cured pultruded composite product is pulled by external pultrusion puller (12).

(61) Typically, the precured preform of squeezed felts/fibres/fabrics impregnated with the resin system obtained from preforming die (7) is either “I” profiled or “Plate” profiled.

(62) The above described system and corresponding continuous pultrusion method is used to produce the said pultruded composite product consisting essentially synthetic polyester felt impregnated with the resin system as core encapsulated between bi-directionally and uni-directionally oriented synthetic fabric impregnated with the resin system;

(63) said composite products are either “I” profiled [see FIG. 1 (B) or (C)] or “Plate” profiled [see FIG. 2 (B) or (C)].

(64) Preferably, the product comprises 10 to 50% by vol. of synthetic polyester felt, 10 to 30% by vol. of synthetic fabric and 40 to 60% by vol. of resin system.

(65) Preferably, the synthetic polyester felt used is preferably unsaturated polyester felt, more preferably needle punched mat prepared from waste PET bottles having weight 400 to 1000 GSM.

(66) Preferably, said synthetic fabric having a moisture content of 5% or less, weight of 100 to 600 gm/m2 and tensile strength of 400 to 500 MPa. Preferably, the synthetic fabric is preferably glass fabric.

(67) The resin system used for impregnation of synthetic polyester or synthetic fabric, comprise of at least a resin, curing system comprising curing agent and accelerator, filler, thinner, pigment or any other additives.

(68) Particularly, the resin used in the resin system is either a thermosetting resin selected from unsaturated polyester, epoxy, polyurethane, phenolic resins and mixture thereof or a thermoplastic resin selected from polyethylene, polypropylene, acrylonitrile-butadiene-styrene, polyacetal, polyamide, polyimide, saturated polyester resins and mixtures thereof.

(69) Particularly, the curing agent used in the resin system is selected from methyl ethyl ketone peroxide, cumene hydroperoxide, t-butyl hydroperoxide, benzoyl peroxide, and/or hydrogen peroxide.

(70) Particularly, the accelerators used in the resin system is selected from cobalt naphthenate and/or cobalt octoate.

(71) Particularly, the filler used in the resin system is calcium carbonate.

(72) Particularly, the thinner is methanol.

(73) Typically, two types of resin systems used in the present invention.

(74) First type of the resin system comprises at least 100 parts per hundred (pph) of resin and at least 20 pph of thinner. Particularly, the resin system comprises 100 pph of phenol formaldehyde resin and 20 pph of methanol (as thinner).

(75) Second type of the resin system comprises at least 100 pph of resin, at least 1.7 pph of curing system, at least 2 pph of filler, and at least 10 pph of thinner.

(76) Particularly, the resin system comprises 100 pph of polyester, 1.7 pph of curing system comprising 0.2 pph of cobalt octoate and 1.5 pph of benzoyl peroxide, 2 pph of calcium carbonate (filler) and 10 pph of methanol (thinner).

(77) Another pultrusion system for continuous production of another composite pultruded product of the invention is illustrated in FIG. 4.

(78) In the FIG. 4, the system comprising:

(79) at least two roller stands (13 and 14), each roller stand provided with at least two roller means (15,16) and (17, 18) to feed synthetic polyester felt and synthetic fabric;

(80) heating means (19, 20), preferably IR heater; said IR heater (19, 20) is in close proximity to said each roller means (15,16) and (17, 18) so as to pass felts/fibres/fabrics through the heater to reduce moisture from thereof;

(81) enclosed resin baths (21, 22) containing resin system for impregnation of the felts/fibres/fabrics in close proximity to said each IR heater (19, 20); said each resin bath (21, 22) provided with preforming die “A” (23, 24) enclosed in it respectively; and said preforming die “A” (23, 24) having die cavity about longitudinal axis which is tapering at end so as to squeeze felts/fibres/fabrics impregnated with the resin system; pressurising means (25, 26) provided to said preforming die “A” (23, 24) to encapsulate said die “A” (23, 24) along its length; said die “A” (23, 24) being activable to pressure to transfer said squeezed resin impregnated felts/fibres/fabrics to further location;

(82) a screw extruder (28) comprising a barrel (29) connected to hooper (30) at one end, screw (31) along its longitudinal axis and pressure means (32) along its longitudinal axis; said hooper provides means for supplying short fibres of bagasse to produce a bagasse plank;

(83) a preforming die “B” (27) in close proximity to said screw extruder (28) as well as said preforming dies “A” (23, 24) to enable to pass a bagasse plank from said extruder (28) and squeezed resin impregnated felts/fibres/fabrics from said die “A” (23, 24) for further processing to form a precured preform; said preforming die “B” (27) having long cylindrical cavity about longitudinal axis with tapering end;

(84) heating means (33) provided to encapsulate said preforming die “B” (27) along its length; said die “B” (27) being activable to heat to transfer said precured preform to further location;

(85) a pultrusion die (34) in close proximity to said preforming die “B” (27); said pultrusion die (34) having slit die with uniform dimension along its length to process precured preform further;

(86) heating means (35) provided to encapsulate said pultrusion die (34) along its length; said pultrusion die (34) being activable to heat to cure preform and transfer to expel cured pultruded bio-composite products to further location; and

(87) external pultrusion puller (36) for pulling out said cured bio-composite pultruded product;

(88) said pultruded composite product consisting plank of short fibers bagasse premixed with resin system as core encapsulated between the synthetic polyester felts impregnated with the resin system which is further encapsulated between bi-directionally and uni-directionally oriented synthetic fabric selected from polyester, carbon, aramid, glass, basalt and mixtures thereof impregnated with the resin system;

(89) said composite product is either “I” profiled [FIG. 1 (A)] or “Plate” profiled [FIG. 2 (A)].

(90) The step of reducing moisture enhances affinity of the felts/fibres/fabrics towards the resin system. The ability of the felts/fibres/fabrics to readily absorb resin is essential for production of the composite products. The resin system used in the invention consists of a resin, a curing system comprising curing agent and an accelerator, a pigment, filler, thinner or any other additives for impregnation of the felts/fibres/fabrics. The said hooper provides means for supplying short fibers of bagasse. The said preforming die “B” (27) having a cavity about longitudinal axis and tapering at end and said pultrusion die (34) having slit die with uniform dimension along its length. Thus, the precured preform obtained is squeezed felts/fibres/fabrics which are at least 40% impregnated with the resin system.

(91) Typically, the synthetic polyester felts or synthetic fabrics are passed through IR heaters (19, 20) by maintaining speed of 2 to 6 meter per hour of felts/fibres/fabrics in it. After passing through IR heater, the felts/fibres/fabrics have 3 to 4% moisture.

(92) Typically, the preforming die “A” (23, 24) having cavity about longitudinal axis which is tapering at end so as to remove excess resin system and obtain said resin system impregnated squeezed felts/fibres/fabrics.

(93) Typically, the preforming die “A” (23, 24) is activable under pressure using pressurizing means (25,26) to transfer squeezed resin impregnated felts/fibres/fabrics to said preforming die “B” (27).

(94) Typically, preforming die “B” (27) having cavity designed to be adapted “I” profile or “Plate” profile.

(95) Typically, “I” profiled die having cavity adapted to have dimension of 20 mm thick I beam of flange with width 70 mm and height of 100 to 120 mm.

(96) Typically, “Plate” profiled die having cavity adapted to have dimension of 8 to 16 mm thick, 600 to 1200 mm of width.

(97) Typically, the preforming die “B” (27) is maintained at temperature in the range of 70 to 90° C. by using heating means (35).

(98) Typically, the pultrusion die (34) having cylindrical cavity die adapted to process “I” profiled or “Plate” profiled precured preform through it.

(99) Typically, the pultrusion die (34) is maintained at temperature in the range of 160 to 180° C. by using heating means (36).

(100) Typically, the felts/fibres/fabrics are passed at speed 2 to 6 meter per hour through enclosed resin baths (21, 22) to obtain impregnated fibres with the resin system.

(101) Typically, the squeezed impregnated felts/fibres/fabrics are passed at speed 2 to 6 meter per hour through the preforming die “A” (23, 24) to obtain squeezed felts/fibres/fabrics impregnated with the resin system.

(102) Typically, the squeezed impregnated felts/fibres/fabrics and bagasse plank are passed at speed 2 to 6 meter per hour through the preforming die “B” (27) to obtain said precured preform.

(103) Typically, the said precured preform passed at speed 2 to 6 meter per hour through the pultrusion die (34) to obtain cured hybrid pultruded composite product.

(104) According to another additional embodiment of the invention, there is provided another continuous pultrusion method for production of another composite pultruded product of the invention by using system of the invention as illustrated in FIG. 4.

(105) In this method, 10 to 40% by vol. of synthetic polyester felts are provided from roller mean (16 and 17) and 5 to 10% by vol. of synthetic fabric selected from polyester, carbon, aramid, glass, basalt and mixtures thereof is provided from roller mean (15 and 18). These felts/fibres/fabrics are passed through IR heater (19, 20) at speed of 2 to 6 meter per hour to reduce moisture from thereof. After reducing the moisture, the said felts/fibres/fabrics are impregnated by passing them at speed of 2 to 6 meter per hour through resin bath (21, 22) comprising resin system consisting of at least a resin, a curing agent, an accelerator, pigment or any other additives. These impregnated felts/fibres/fabrics with the resin system are passed at speed of 2 to 6 meter per hour through preforming die “A” (23, 24) under pressure using pressurising means (25,26) to obtain squeezed felts/fibres/fabrics impregnated with the resin system. The squeezed felts/fibres/fabrics impregnated with resin system are transferred to preforming die “B” (27).

(106) A plank from short fibres of bagasse is prepared by extruding short fibres of bagasse premixed with a resin system using the screw extruder (28) comprises supplying 10 to 30% by vol. of short fibres of bagasse premixed with a resin system in equal proportion through a hooper (30) to a barrel (29) having a screw (31) along its longitudinal axis and extruding it a at rotational speed of 20-30 RPM with 10 L/D ratio into plank. The extruded bagasse plank is transferred from the screw extruder (28) to a preforming die “B” (27). The extruded bagasse plank and two squeezed fibres impregnated with resin system are passed at speed of 2 to 6 meter per hour through the said preforming die “B” (27) under heating at temperature in the range of 70 to 90° C. using heating means (33), said two squeezed felts/fibres/fabrics are positioned above and below the extruded bagasse plank so as to encapsulate the bagasse plank between the synthetic polyester felts impregnated with the resin system which is further encapsulated by bi-directionally and/or uni-directionally oriented synthetic fabric selected from polyester, carbon, aramid, glass, basalt and mixtures thereof impregnated with the resin system and obtain precured preform of encapsulated composite product.

(107) The precured preform of encapsulated composite product is finally passed at speed of 2 to 6 meter per hour through pultrusion die (34) under heating at temperature in the range of 160 to 180° C. using heating means (35) so as to obtain cured composite pultruded product and expel it as it is activable under heating.

(108) The cured pultruded composite product is pulled out by external pultrusion puller (36).

(109) The said cured pultruded composite product obtained by using the above-mentioned system and the above-mentioned method consisting plank of short fibers bagasse premixed with a resin system as core encapsulated between the synthetic polyester felts impregnated with the resin system which is further encapsulated between bi-directionally and/or uni-directionally oriented synthetic fabric selected from polyester, carbon, aramid, glass, basalt and mixtures thereof impregnated with the resin system. The said composite product is either “I” profiled [FIG. 1 (A)] or “Plate” profiled [FIG. 2 (A)].

(110) Preferably, the product comprises 10 to 40% by vol. of synthetic polyester felt, 5 to 10% by vol. of synthetic fabric, 10 to 30% by vol. of bagasse short fibres and 40 to 60% by vol. of resin system.

(111) The synthetic polyester felt used in the composite products of the invention is in the form of needle punched mat having weight in the range of 400 to 1000 GSM. The needle punched mat of synthetic polyester felt is prepared from waste PET bottles to reduce the cost of production.

(112) PET beverage bottles are converted into fibers and different production techniques are available for the same. Thus, the following production technique should be considered to be exemplary, and not limiting, as long as resulting to PET derived polyester fibers. The exemplary fiber production technique is based on pelletizing the PET bottles, melting the pellets to generate molten polyester, and passing the molten polyester through a screen or grating having predefined pore sizes (the pore sizes control the diameter of the resulting individual polyester fibers). The polyester fibers are cut to the desired length. The polyester fibers are carded (also referred to as combing) to align the individual fibers. The aligned fibers are then used to generate the PET derived polyester fiber based non-woven mat by needle punching. In some embodiments, some amount of recycled synthetic fibers from other sources (such as shredded carpet, textiles, and clothing) can be added to the PET derived polyester fiber. In an exemplary embodiment, the PET derived polyester fiber is formed into a mat weighing about 400 to about 1000 GSM. The needle punched mat of synthetic polyester felt have following properties namely; Mass (ASTM D 5261) 1000 GSM; Tensile Strength (Wide Width) (ASTM D 4595) 40 KN/m; Elongation (ASTM D 4595) 55%; Grab Tensile Strength (ASTM D 4632) 1850 N; Grab Tensile Elongation (ASTM D 4632) >55%; CBR (ASTM D 6241) 4500 N; Opening Size (O90) (ASTM D 4751) 60 Microns; Thickness 4 mm; and Trap Tear (ASTM D 4533) 950 N.

(113) Preferably, said synthetic fabric having a moisture content of 5% or less, weight of 100 to 600 gm/m2, and tensile strength of 400 to 500 MPa.

(114) Preferably, the synthetic fabric is selected from bi-directionally and/or uni-directionally oriented synthetic fabric selected from polyester, carbon, aramid, glass, basalt and mixtures thereof; more preferably glass fabric.

(115) The resin system used for impregnation of felts/fibres/fabrics, comprise of at least a resin, curing system comprising curing agent and accelerator, filler, thinner, pigment or any other additives.

(116) Particularly, the resin used in the resin system is either a thermosetting resin selected from unsaturated polyester, epoxy, polyurethane, phenolic resins and mixture thereof or a thermoplastic resin selected from polyethylene, polypropylene, acrylonitrile-butadiene-styrene, polyacetal, polyamide, polyimide, saturated polyester resins and mixtures thereof.

(117) Particularly, the curing agent used in the resin system is selected from methyl ethyl ketone peroxide, cumene hydroperoxide, t-butyl hydroperoxide, benzoyl peroxide, and/or hydrogen peroxide.

(118) Particularly, the accelerators used in the resin system is selected from cobalt naphthenate and/or cobalt octoate.

(119) Particularly, the filler used in the resin system is calcium carbonate.

(120) Particularly, the thinner is methanol.

(121) Two types of resin systems are used in the present invention.

(122) First type of the resin system comprises at least 100 parts per hundred (pph) of resin and at least 20 pph of thinner.

(123) Particularly, the resin system comprises 100 pph of phenol formaldehyde resin and 20 pph of methanol (thinner).

(124) Second type of the resin system comprises at least 100 pph of resin, at least 1.7 pph of curing system, at least 2 pph of filler, and at least 10 pph of thinner.

(125) Particularly, the resin system comprises 100 pph of polyester, 1.7 pph of curing system comprising 1 pph tertiary butyl perbenzoate; 0.2 pph of cobalt octoate and 1.5 pph of benzoyl peroxide, 2 pph of calcium carbonate (filler) and 10 pph of methanol (thinner).

(126) Particularly, another resin system comprises 100 pph of unsaturated polyester resins (Aropol), 1.7 pph of curing system comprising 1 pph tertiary butyl perbenzoate; 0.2 pph of cobalt octoate and 1.5 pph of benzoyl peroxide, 2 pph of calcium carbonate (filler) and 10 pph of methanol (thinner).

(127) Typically, the bagasse fibres are premixed with the resin system prior to extrusion in equal proportion.

(128) Typically, bale form bagasse is crushed to form smaller particle size bagasse, followed by moisture reduction by passing through IR heater to reduce the moisture to 3 to 4% and then premixed with said resin system in equal proportion to be used in the present invention.

(129) The post forming die may be heated and may be incorporated in the puller mechanism or may be separate. Alternatively one or more of the felts/fibres/fabrics supplied to the pultrusion die may be pre-impregnated with resin in bath. Bath may be located either before or after former.

(130) Thus, pultrusion systems for continuous production of composite pultruded products of the invention eliminates wastage of material due to spilling of raw material during the manufacture thus making it clean, cost effective and efficient. The preforming die of the system is specially designed to have a cavity about longitudinal axis with a shape of either “I” or “Plate” profile and tapering at end so as to overcome the limitation of feeding impregnated reinforcing felts/fibres/fabrics into intricate die. The present system has roller stand instead of creel stand for feeding felts/fibres/fabrics which uses less space as compared to conventional creel stand. Thus, the current method reduces manufacturing cost, reduces environmental impact and improves composite products, which can be used as efficient structural beam or plate or panel in a modular structure. The composite products of the invention have uniform property and overcome limitation of conventional overdesigned thin and thick glass reinforced composites products. Also said products are with improved low ratio of weight to strength as well as said products are with improved, thicker and wider profiles and plates products. The said products with improved bio-based hybrid advanced composites, thereby having more fatigue life than the conventional natural fibre composites. The products of the invention have more impact/tensile/bending strength than the conventional composites products. Thus, said products eliminates use of conventional glass roving and overcomes the limitation of jamming of glass roving in resin bath. The present invention increase uniformity of the property and the strength of bagasse pultruded products by encapsulating the peripheral areas by synthetic fabrics more accurately glass fabrics and polyester fabrics or in combination thereof.

(131) The present invention is described in the examples given below; further these are provided only to illustrate the invention and therefore should not be construed to limit the scope of the invention.

Example 1

(132) A Product “Plate” Profiled

(133) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 20% unidirectional glass fabric, 24% synthetic polyester felt (need to use specific trade name), and 56% resin system, all measured by volume.

(134) The needle punched mat prepared from PET bottles having weight of 1000 g/m2. (manufactured by CAPITOL Non Oven Private Ltd).

(135) 24% by vol. of synthetic polyester felt was provided by roller mean (2) and 20% by vol. of unidirectional glass fabric of 200 g/m2 was provided by roller means (1 and 3). These felts/fabrics were passed through IR heater (5) at speed 4 meter per hour to reduce moisture to 3 to 4%. These felts/fabrics were impregnated by passing them at speed 4 meter per hour through the resin bath (6) comprising a resin system consisting of 100 part phenol formaldehyde (68 to 72% resole type phenol formaldehyde in water supplied by Shivam polymer Pvt. Ltd.) and 20 parts methanol. The impregnated fabrics and felts were passed through a preforming die (7) having cavity of plate profile of dimension i.e. 8 mm thick and 1000 mm width at speed 4 meter per hour and at temperature 80° C. to obtain a precured “Plate” profile resin squeezed preform. This precured preform was further passed through the pultrusion die (10) at speed 4 meter per hour and at temperature 170° C. using heating means (11) to obtain a cured pultruded composite product of “Plate” profiled. “Plate” profiled pultruded bio-composite product from the said pultrusion die (10) was pulled out with the help of an external pultrusion puller (12).

Example 2

(136) B Product “Plate” Profiled

(137) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 15% unidirectional glass fabric, 35% synthetic polyester felts, and 50% resin system, all measured by volume by following same method as described in Example 1.

Example 3

(138) C Product “Plate” Profiled

(139) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 10% unidirectional glass fabric, 45% synthetic polyester felts, and 45% resin system, all measured by volume by following same method as described in Example 1.

Example 4

(140) D Product “Plate” Profiled

(141) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 20% bidirectional glass fabric, 24% synthetic polyester felts, and 56% resin system, all measured by volume by following same method as described in Example 1.

Example 5

(142) E Product “Plate” Profiled

(143) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 15% bidirectional glass fabric, 35% synthetic polyester felts, and 50% resin system, all measured by volume by following same method as described in Example 1.

Example 6

(144) F product “Plate” profiled

(145) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 10% bidirectional glass fabric, 45% synthetic polyester felts, and 45% resin system, all measured by volume by following same method as described in Example 1.

Example 7

(146) G Product “Plate” Profiled

(147) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 30% polyester fabric, 14% synthetic polyester felts, and 56% resin system, all measured by volume by following same method as described in Example 1.

Example 8

(148) H Product “Plate” Profiled

(149) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 25% polyester fabric, 25% synthetic polyester felts, and 50% resin system, all measured by volume by following same method as described in Example 1.

Example 9

(150) I Product “Plate” Profiled

(151) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 20% polyester fabric, 35% synthetic polyester felts, and 45% resin system, all measured by volume by following same method as described in Example 1.

(152) The Plate profiled composite products prepared according to examples 1 to 9 were analyzed for its density, modulus of elasticity, modulus of rupture and impact strength and the results of the same are tabulated in Table 2.

(153) TABLE-US-00002 TABLE 2 Volume % Modulus Modulus Synthetic Synthetic Bio- of of Fabrics Polyester Resin composite Density Elasticity Rupture Impact Fabrics Type Reinforcement Felts system product kg/m.sup.3 GPa MPa Strength Unidirectional 20 24 56 A 1,750 26.0 392 75 Glass 15 35 50 B 1,680 30.0 395 68 Fabric 15 45 45 C 1,680 32.5 380 59 Bidirectional 20 24 56 D 1,750 25.4 419 78 Glass 15 35 50 E 1,520 30.8 408 79 Fabric 10 45 45 F 1,420 35.5 312 69 Polyester 30 14 56 G 1,680 24.5 350 65 Fabrics 25 25 50 H 1,580 30.0 335 64 20 35 45 I 1,520 31.2 310 60

(154) These composite pultruded products obtained according to examples 1 to 9, wherein increasing synthetic polyester felt amount and reducing synthetic fabric leads to significant reduction in density as well as in weight. This also leads to a significant reduction of cost. The present composite products are encapsulated by fabrics in the peripheral area thus bringing more integrity uniformity of synthetic polyester felts materials further increasing stiffness of the product.

Example 10

(155) J Product “Plate” Profiled

(156) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 20% unidirectional glass fabric, 24% synthetic polyester felt (need to use specific trade name), and 56% resin system, all measured by volume following same method as described in Example 1 except resin system used here comprises 100 pph of unsaturated polyester resins (Aropol); 1.7 pph of curing system comprising 1 pph tertiary butyl perbenzoate; 0.2 pph of cobalt octoate and 1.5 pph of benzoyl peroxide; 2 pph of calcium carbonate (filler) and 10 pph of methanol (thinner).

Example 11

(157) K Product “Plate” Profiled

(158) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 15% unidirectional glass fabric, 35% synthetic polyester felts, and 50% resin system, all measured by volume by following same method as described in Example 2 except resin system used here comprises 100 pph of unsaturated polyester resins (Aropol); 1.7 pph of curing system comprising 1 pph tertiary butyl perbenzoate; 0.2 pph of cobalt octoate and 1.5 pph of benzoyl peroxide; 2 pph of calcium carbonate (filler) and 10 pph of methanol (thinner).

Example 12

(159) L Product “Plate” Profiled

(160) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 10% unidirectional glass fabric, 45% synthetic polyester felts, and 45% resin system, all measured by volume by following same method as described in Example 3 except resin system used here comprises 100 pph of unsaturated polyester resins (Aropol); 1.7 pph of curing system comprising 1 pph tertiary butyl perbenzoate; 0.2 pph of cobalt octoate and 1.5 pph of benzoyl peroxide; 2 pph of calcium carbonate (filler) and 10 pph of methanol (thinner).

Example 13

(161) M Product “Plate” Profiled

(162) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 20% bidirectional glass fabric, 24% synthetic polyester felts, and 56% resin system, all measured by volume by following same method as described in Example 4 except resin system used here comprises 100 pph of unsaturated polyester resins (Aropol); 1.7 pph of curing system comprising 1 pph tertiary butyl perbenzoate; 0.2 pph of cobalt octoate and 1.5 pph of benzoyl peroxide; 2 pph of calcium carbonate (filler) and 10 pph of methanol (thinner).

Example 14

(163) N Product “Plate” Profiled

(164) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 15% bidirectional glass fabric, 35% synthetic polyester felts, and 50% resin system, all measured by volume by following same method as described in Example 5 except resin system used here comprises 100 pph of unsaturated polyester resins (Aropol); 1.7 pph of curing system comprising 1 pph tertiary butyl perbenzoate; 0.2 pph of cobalt octoate and 1.5 pph of benzoyl peroxide; 2 pph of calcium carbonate (filler) and 10 pph of methanol (thinner).

Example 15

(165) O Product “Plate” Profiled

(166) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 10% bidirectional glass fabric, 45% synthetic polyester felts, and 45% resin system, all measured by volume by following same method as described in Example 6 except resin system used here comprises 100 pph of unsaturated polyester resins (Aropol); 1.7 pph of curing system comprising 1 pph tertiary butyl perbenzoate; 0.2 pph of cobalt octoate and 1.5 pph of benzoyl peroxide; 2 pph of calcium carbonate (filler) and 10 pph of methanol (thinner).

Example 16

(167) P Product “Plate” Profiled

(168) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 30% polyester fabric, 14% synthetic polyester felts, and 56% resin system, all measured by volume by following same method as described in Example 7 except resin system used here comprises 100 pph of unsaturated polyester resins (Aropol); 1.7 pph of curing system comprising 1 pph tertiary butyl perbenzoate; 0.2 pph of cobalt octoate and 1.5 pph of benzoyl peroxide; 2 pph of calcium carbonate (filler) and 10 pph of methanol (thinner).

Example 17

(169) Q Product “Plate” Profiled

(170) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 25% polyester fabric, 25% synthetic polyester felts, and 50% resin system, all measured by volume by following same method as described in Example 8 except resin system used here comprises 100 pph of unsaturated polyester resins (Aropol); 1.7 pph of curing system comprising 1 pph tertiary butyl perbenzoate; 0.2 pph of cobalt octoate and 1.5 pph of benzoyl peroxide; 2 pph of calcium carbonate (filler) and 10 pph of methanol (thinner).

Example 18

(171) R Product “Plate” Profiled

(172) “Plate” profiled flat pultruded product having a cross section 8×1000 mm was made with 20% polyester fabric, 35% synthetic polyester felts, and 45% resin system, all measured by volume by following same method as described in Example 9 except resin system used here comprises 100 pph of unsaturated polyester resins (Aropol); 1.7 pph of curing system comprising 1 pph tertiary butyl perbenzoate; 0.2 pph of cobalt octoate and 1.5 pph of benzoyl peroxide; 2 pph of calcium carbonate (filler) and 10 pph of methanol (thinner).

(173) The Plate profiled biocomposite products prepared according to examples 11 to 18 were analyzed for its density, modulus of elasticity, modulus of rupture and impact strength and the results of the same are tabulated in Table 3.

(174) TABLE-US-00003 TABLE 3 Volume % Modulus Modulus Synthetic Synthetic Bio- of of Fabrics Polyester Resin composite Density Elasticity Rupture Impact Fabrics Type Reinforcement Felts system product kg/m.sup.3 GPa MPa Strength Unidirectional 20 24 56 J 1,710 24.0 392 75 Glass 15 35 50 K 1,620 29.0 395 68 Fabric 15 45 45 L 1,630 32.5 380 59 Bidirectional 20 24 56 M 1,720 20.4 419 78 Glass 15 35 50 N 1,500 29.8 408 79 Fabric 10 45 45 O 1,400 35.5 312 69 Polyester 30 14 56 P 1,600 24.5 350 65 Fabrics 25 25 50 Q 1,530 29.0 335 64 20 35 45 R 1,500 26.2 310 60

(175) These composite pultruded products obtained according to examples 10 to 18, wherein increasing synthetic polyester felt amount and reducing synthetic fabric leads to significant reduction in density as well as weight. This also leads to a significant reduction of cost. The present composite products are encapsulated by fabrics in the peripheral area thus bringing more integrity uniformity of synthetic polyester felts materials further increasing stiffness of the product.

Example 19

(176) AA Biocomposite Product “I” Profiled

(177) “I” profiled flat pultruded product having dimension of 20 mm thick of I beam of flange with width of 70 mm and height of 120 mm was made with 10% unidirectional glass fabric, 30% of bagasse; 14% synthetic polyester felt, and 46% resin system, all measured by volume.

(178) The needle punched mat prepared from PET bottles having weight of 1000 g/m2. (manufactured by CAPITOL Non Oven Private Ltd).

(179) 14% by vol. of synthetic polyester felts was provided from roller means (16 and 17) and 10% by vol. of unidirectional glass fabric (200 g/m.sup.2) was provided from roller mean (15 and 18). These felts/fabrics were passed through IR heater (19, 20) at speed of 4 meter per hour to reduce moisture (3 to 4%). After moisture reduction, the said felts/fabrics were impregnated by passing through resin bath (21, 22) comprising resin system consisting of 100 parts of polyester (82% by vol. of unsaturated polyester in styrene supplied by Satyen Polymers Pvt. Ltd), 0.2 parts of cobalt octoate, 1.5 parts of Benzyl Peroxide, 2 parts of Calcium Carbonate, and 10 parts of methanol. These impregnated felts/fabrics with the resin system were passed at speed of 4 meter per hour through preforming die “A” (23, 24) under pressure using pressurising means (25,26) to obtain squeezed felts/fabrics impregnated with the resin system. The squeezed resin impregnated felts/fabrics was transferred to preforming die “B” (27).

(180) A plank of 15 mm thick and 1800 g/m.sup.2 basis weight was prepared from short fibres of bagasse by extruding 30% by vol. of short fibres of bagasse premixed with the resin system (i.e. 100 parts of Polyester (82% by vol. of unsaturated polyester in styrene supplied by Satyen Polymers Pvt. Ltd), 0.2 parts of cobalt octoate, 1.5 parts of Benzyl Peroxide, 2 parts of Calcium Carbonate, and 10 parts of methanol) in equal proportion using the screw extruder (28) comprises supplying short fibres of bagasse through a hooper (30) to a barrel (29) having a screw (31) along its longitudinal axis and extruding it at rotational speed of 20-30 RPM with 10 L/D ratio into plank. The extruded bagasse plank was transferred from the screw extruder (28) to a preforming die “B” (27).

(181) The extruded bagasse plank and two squeezed felts/fabrics impregnated with resin system were passed at speed of 4 meter per hour through the said preforming die “B” (27), having dimension of 20 mm thick of I beam of flange with width 70 mm and height of 120 mm, under heating at temperature 80° C. using heating means (33), said two squeezed felts and fabrics were positioned above and below the extruded bagasse plank so as to encapsulate the bagasse plank between the synthetic polyester felts impregnated with the resin system which was further encapsulated by bi-directionally oriented E-glass fabric impregnated with the resin system and obtain precured “I” profiled preform of encapsulated bio-composite product.

(182) The precured “I” profiled preform was finally passed at speed of 4 meter per hour through pultrusion die (34) under heating at temperature 170° C. using heating means (35) so as to obtain cured “I” profiled bio-composite pultruded product and expel it as it was activable under heating. The cured pultruded bio-composite product was pulled out by external pultrusion puller (36).

Example 20

(183) AB Biocomposite Product “I” Profiled

(184) “I” profiled flat pultruded product having dimension of 20 mm thick of I beam of flange with width 70 mm and height of 120 mm was made with 10% of bidirectional glass fabric, 25% of bagasse, 15% of synthetic polyester felt, and 50% of resin system, all measured by volume by following same method as described in Example 19 except replacing unidirectional glass fabric with bidirectional glass fabric.

Example 21

(185) AC Biocomposite Product “I” Profiled

(186) “I” profiled flat pultruded product having dimension of 20 mm thick of I beam of flange with width 70 mm and height of 120 mm was made with 10% of Basalt fabric, 15% of bagasse, 25% synthetic polyester felts, and 50% of resin system, all measured by volume by following same method as described in Example 19 except replacing unidirectional glass fabric with Basalt fabric.

Example 22

(187) AD Biocomposite Product “I” Profiled

(188) “I” profiled flat pultruded product having dimension of 20 mm thick of I beam of flange with width 70 mm and height of 120 mm was made with 10% of polyester fabric, 20% of bagasse, 14% of synthetic polyester felts, and 56% of resin system, all measured by volume by following same method as described in Example 19 except replacing unidirectional glass fabric with polyester fabric.

Example 23

(189) AE Biocomposite Product “I” Profiled

(190) “I” profiled flat pultruded product having dimension of 20 mm thick of I beam of flange with width 70 mm and height of 120 mm was made with 10% of aramid fabric, 25% of bagasse, 15% of synthetic polyester, and 50% resin system, all measured by volume by following same method as described in Example 19 except replacing unidirectional glass fabric with Aramid fabric.

Example 24

(191) AF Biocomposite Product “I” Profiled

(192) “I” profiled flat pultruded product having dimension of 20 mm thick of I beam of flange with width 70 mm and height of 120 mm was made with 10% of Carbon fabric, 10% of bagasse, 35% of synthetic polyester, and 45% of resin system, all measured by volume by following same method as described in Example 19 except replacing unidirectional glass fabric with Carbon fabric.

(193) “I” profiled biocomposite products prepared according to examples 19 to 24 were analyzed for its density, modulus of elasticity, modulus of rupture and impact strength and the results of the same are tabulated in Table 4.

(194) TABLE-US-00004 TABLE 4 Volume % Modulus Modulus Synthetic Bio- of of polyester Polyester composite Density Elasticity Rupture Impact Fabrics Type Bagasse felts Resin product kg/m.sup.3 GPa MPa Strength Unidirectional 30 14 46 AA 1,700 20.0 500 60 Glass fabric 10% V/V Bidirectional 25 15 50 AB 1,580 20.0 608 76 glass fabric 10% V/V Basalt 15 25 50 AC 1,480 22.5 669 76 10% V/V Polyester 20 14 56 AD 1,700 10.4 371 50 10% V/V Aramid 25 15 50 AE 1,410 20.8 328 57 10% V/V Carbon 10 35 45 AF 1,310 30.5 652 76.7 10% V/V

(195) These bio-composite pultruded products obtained according to examples 19 to 24 leads to significant reduction in weight as well as in density because of incorporation of bagasse as a core. This also leads to a significant cost reduction. The glass fabric was distributed at top and bottom over synthetic polyester felts which is covering preformed bagasse at the center part of the product. The present bio-composite products are encapsulated by fabrics in the peripheral area bringing more integrity uniformity of synthetic polyester felts materials further increasing stiffness and tensile strength.

(196) The products of examples 15 and 24 were tested for their allow BM, allow SF, E, EI and tensile strength and the results of the same were tabulated in the table 4. The same test were carried out on 12 mm thick conventional Plywood and H-16 Convention H Beam and the results of the same were tabulated in the table 5.

(197) TABLE-US-00005 TABLE 5 Plywood 8 mm thick 12 mm Thick of plywood H Beam Conventional product of Conventional Product of Sr. No. Property Unit Plywood example 15 H-16 example 24  1. Allow BM kNm 0.20 0.21 3.0 3.48 2 Allow SF kN 6.16 17.92 6.0 63.33 3 E N/mm.sup.2 6700/3600  9424/19424 14000 19424 4 EI kN-m.sup.2 1.1 1.402 145 151.00 5 Tensile Strength N/mm.sup.2 32.5/22.5 75.3/28.4 — —

(198) According to the comparative results of products of examples 15 and 24 and conventional products as described in Table 5, the products of the invention have superior performance over the conventional one.

(199) It has been found that the composite products of the present invention is hybrid products with substantial technical advancements. The current invention has following advantages:

(200) 1. Low cost;

(201) 2. Easy processing system;

(202) 3. High toughening strength i.e. High Impact strength;

(203) 4. High Isotropic strength than conventional natural fibre composites;

(204) 5. Less fatigue (i.e. more durable);

(205) 6. Good tensile strength;

(206) 7. Comparable strength as that of glass fibre composites; and

(207) 8. Utilizes 40% waste materials and hence eco-friendly.

(208) The results illustrated in all five tables unequivocally establish the superior traits of composite products prepared in accordance with the present invention as compared to conventional composite product. The products of the invention with technical advancement are used as shuttering Plywood and I and Plate beam for civil application.