with at least one layer of cellulosic non woven viscose or lyocell or the like 1 or 2 prepared by the process described above presence or absence of either of the layers 1 or 2 may be decided upon the desired performance of the composite structure the structure may then be consolidated by known methods pulp preferred for use for making the solution is soft wood pulp having high alpha cellulose content 89 93 and low semi cellulose content dp degree of polymerization of the pulp is in the range of 600 to 1100 preferred range would be 700 to 1000 cellulose concentration to achieve a spin able solution can be in the range of 5 to 28 preferably 7 to 20 most preferred values of the cellulose concentration are 10 to 15 nmmo n methyl morpholine n oxide as available in the market is of 50 concentration has to be pre concentrated to 77 prior to dissolution of cellulose by conventional distillation process blending of small pieces of pulp with pre concentrated solvent is carried out at about 100 u00b0 c in a double blade sigma mixer where in vacuum of 400 mm hg is applied after duration of 1 5 hours a homogeneous solution is obtained which is allowed to cool down to solid condition other methods available for making cellulose solutions on a continuous basis are available like use of high shear blender thin film device or a devolatalizing type counter.