The jute sticks of various length and sizes were sent by the sponsor. The sticks received from the sponsor were analyzed for the physical properties of jute sticks. The moisture content and density of the jute sticks were using oven dry method for moisture content and water displacement process for density measurements. The ash content in the jute sticks were measured by taking known weight of the jute stick material in a platinum crucible of 20 ml capacity Ignited the crucible containing the sample for some time using burner till all fumes escapes and then keep it in a muffle furnace at a temperature of 650-700°C for complete charring to ash. After completed cooling the weight is taken. Based on the initial weight taken and the weight obtained after complete charring, the ash content was calculated. The studies revealed the properties as given in Table 1.
Preparation of jute sticks raw material
The jute sticks used in the study were cut into sizes of required dimensions and sent to hammer mill for sizing. Pulverizer available in the institute was utilized to pulverize the hammered particles to get the required size of the particles.
Based on the initial study, it necessitated the physical modification of the jute stick particles to activate the surface for better adhesion. Jute sticks were crushed followed by pulverizing to get the particles of required size for the manufacturing of single layered particle board.
Further the particles were dried to get the moisture content of 3-4% for the manufacture of jute stick particle board. It has been observed that when particles were being reduced to size of 1mm for the face layer the particles were just forming powder. As the bulk density of the jute was very low, Particle yield for core was very less compared to the particle yield of face.
Feeding rate
Chips can be stored in silos for feeding into hammer mill. Where storage system is not provided in some small capacity plant, the feeding into chipper should be synchronized with the capacity of the hammer mill, so that the storage box above the hammer mill is not blocked due to excess material.
Hammer process and optimization of particle size
Since bulk density is low and difficult to get uniform density in Particle. In this stage manually hammered the chopped Jute stick straw of size of 1²-2² length to deform the raw material before feeding to the chipper section.
Optimization of particle size is also required for finding out resin requirement for adequate bonding. As a general rule, more surface area is being generated for thin, slender particles for face from unit weight of wood than that for core.
As a general rule, longer and thinner particles produce a board with high bending strength and higher dimensional stability. Shorter and thicker particles produce a board with lower bending strength, low dimensional stability and higher internal bond strength. The same principle was used while making three layered particle board.
The Jute stick particles sizes were optimized to standard sizes for face < 1 mm and for core particles >1 ≤ 3 mm. The sizing of the particles required hammering/ crushing rather than the usual chipping of particles and then sent to the pulverizer for converting into required size for face and core separately.
Moisture content of jute sick particle
Jute sticks as a raw material is a low-density porous material and dried out rapidly and did not require further drying to chip. Hence this material is below then 20% moisture content and produces higher quantity of powder while processing in mill.
When bigger dimension Jute Sticks raw material are used as raw material, these may be cut to smaller dimension with the help of chopper before feeding into chipper. The parameter in the industrial oven for drying was standardized to bring down the moisture to 3-4%. The moisture content of the particles was analyzed on online moisture meter as higher moisture creates problem while bonding.
Binder: Urea formaldehyde resin
Conventional Urea formaldehyde resin was used for preparation of particle board with Jute stick particle board. For the preparation of resin higher molar ratio of urea/formaldehyde used at initial stage [mole ratio 1:1.72 or weight ratio of urea: formalin = 1:2.25]. 225 parts of formalin is first charged into the reactor. The reactants are allowed to react at pH 8.0 (the pH of formaldehyde was adjusted to 8 by using caustic solution before adding urea and melamine). 90 parts of urea weighed was added to the reactor containing formalin. 10% melamine was also incorporated after the addition of urea. The pH of the final reactant mixture was maintained around 7.5-8.00. The reactant mixture is heated and condensed at 90±2°C for about 90 minutes. Then the pH is reduced to 4.5-5 by using glacial acetic acid and the condensed at 90±2°C until the precipitate is formed (Precipitation is checked by dropping a drop of resin into the beaker containing water). pH is then raised to 7.5 - 8. The resin is cooled and remaining second urea of 10% was added and the resin is cooled to room temperature. The flow properties are checked.
For the present work, both melamine and urea have been used as scavenger to mop free formaldehyde from UF resin. In fact, the first charge is consisted of 90 Kgs. Urea and 10 Kgs. Melamine. 10 Kgs. of urea was used as second urea added after the reaction was arrested. The flow properties of resin are given in Table 2.
Storage of resin
Since resin is the binder for the particles in particle board, it is necessary to use resin of uniform quality to obtain uniform bond quality. It is therefore necessary that the resin in each batch is uniform with respect to viscosity, water tolerance, solid content, pH.
Since all synthetic polymers, which makes the backbone resin, increases its viscosity rapidly as temperature increases, the resin should be made such that it has identical viscosity and be stored at low temperature so that increase in viscosity is negligible.
The flow properties of the glue are being dictated by the viscosity of the resin, it is necessary that resin of uniform viscosity be used. Otherwise, if resin of different consistency is being used, the quantity of resin passing through the nozzle will vary under same condition of pressure and temperature. Storage of resin below 25°C is ideal.
Blending
It is well known that total surface area of the fine particles used as face layer is much larger than that of coarse particles used for core in making three layered particle board. Consequently, finer particles will consume more resin than core particles.
For the present study, a continuous blender has been used. Hence, two separate blenders for face and core have been used. Although fine particles are being used for face and coarse particles are being used for core. Therefore, proper sieves are used to segregate the non-uniform size of particle for face and core layer for uniform distribution of particle. This will not only improve the surface finish but also physical and mechanical properties PB.
Resin uses for face and core particles
100 parts oven dry face particles 12 parts solid resin.
100 parts oven dry core particles 14 parts solid resin.
The adhesive formulation is given in Table 3.
A shaft and shovel type blender are being used for blending resin and additive mix with furnish. The objective of blending is to achieve an even and uniform distribution of resin over the particles. Hence, a central nozzle spray gun is used to mix the glue on to the particles. Accordingly, travel time of particles in blender is adjusted [in minutes] to obtain for uniform mixing.
Mat forming
For the present work, a two-roller mat former has been used. Certainly, it very important part of methodology to assess the uniformity in physical and mechanical properties of final board.
Pre-pressing
A Single daylight Pre-press of platen size 1.4 m × 0.72 m was used for pre-pressing the mat assembly. Pre-pressing was done for time duration of 1 min at a specific pressure of 6 kg/cm
2. The thickness of mat after Pre-pressing was in the range of 40-50 mm for final board thickness of 12 mm.
Hot-pressing
The UF resin was blended with the particles and the adhesive formation have been optimized for making multi layered particle board of density 700-850 kg/m
3. The hot press parameter for manufacturing 3 layered/multilayered particle boards were worked out
i.e., hot press temperature of 165±5°C, specific pressure of 25 kg/cm
2 for 6 minutes in compression cycle and 12 kg/cm
2 for 6 months for curing cycle for a board of 12 mm thickness. The boards were free of any visual defects. The panels were then stabilized for 24-48 hours to attain equilibrium moisture (Fig 1).
After stabilizations the panels were trimmed and cut to sizes for evaluating the physical and mechanical properties as per IS: 3087: Specification for Medium Density Particle Board multi-layered grade 2 (Indian standard 3087, 2005). The properties of the board conform to the requirements of IS: 3087. The same formulations were repeated for checking the consistency in the results and observed that the results obtained were consistent and meets the requirement of grade 2 multilayered medium density particle board as per IS:3087.