AU739537B2 - Process for the production of cellulose paper pulps by biodelignification of vegetable masses - Google Patents

Description

K< j r -1- P/00/011 Regulation 3.2

AUSTRALIA

Patents Act 1990

SUBSTITUTE

COMPLETE SPECIFICATION STANDARD PATENT Invention Title: PROCESS FOR THE PRODUCTION OF CELLULOSE PAPER PULPS BY BIODELIGNIFICATION OF VEGETABLE MASSES a. a a a The following statement is a full description of this invention, including the best method of performing it known to us: GH REF: P25078-A:DAA:RK lA

DESCRIPTION

The present invention relates to a process for the production of cellulose pulps starting from cultured vegetable biomasses (treespecies, textile plants, etc.), with special reference to kenaf (Hibiscus cannabinus) or residues from other agriculturalindustrial productions such as cereal straws, maize stalks, and the like.

The present invention also relates to the apparatus suitable to realise said process, as well as the vegetable biomasses produced from kenaf and textile plants in general.

"Textile fibre plants" and more simply "textile plants", even though they belong to different 15 botanical genuses and species, have a stem formed by two main fractions,. quite distinct and easily separable from -one- .,another:' external cortical fibres (bast fibres) which constitute the real textile part characterised by aggregates of long 20 and flexible fibres with a high content of cellulose and a low content of lignin, and the internal part (core or wood), constituted by aggregates of very short and rigid fibres.

Cortical fibres have good general characteristics, while the fibres of the internal part, on the contrary, have a the poor characteristics.

The ratio between cortical fibres and fibres of f, 2 the wood part is generally 1:2, and they can be separated from one another by means of mechanical systems.

Among the plants that belong to the "textile fibre" group, the most common are: kenaf, hemp, flax, cotton (for the stem part), jute, ramie, roselle (Hibiscus sabdarifa), etc.

Kenaf, in particular, is an annual plant of probable Asian origin, that grows quickly (3-4 months), needs no particular cultivation practises and can grow also on poor soils and with relatively low rainfall; at present it is cultivated in many regions of the world for the utilisation of *the cortical part for textile purposes (sacks, ropes, 15 etc.). Given its high productivity (up to 20 t/ha of dry matter), in the last years several attempts have been made at utilising kenaf also as a potential 9 source of row material for.paper making.

The production of cellulose pulp for paper industry 9* 20 is a process that utilises mainly arboreal species from specialised cultivations. Wood, reduced to dimensions of about 30-40 mm and a thickness of about 5-7 mm, is treated at high temperature and pressure with suitable mixes of chemical reagents that selectively attack lignin and hemicellulose macromolecules, rendering them soluble. Pulps coming from this first treatment, commonly called "coo- 3 king", are called "raw pulps"; they still contain partly modified lignin and are more or less Havanabrown coloured.

Raw pulps may be directly used to produce papers for packing or other industrial uses. However, if pulps should be used for fine and very fine papers (culture-papers, white papers, writing and printing papers and the like), raw pulps must be submitted to further chemical-physical treatments suitable to eliminate almost entire lylignin molecules and coloured molecules in general; this second operation is commonly referred to as "bleaching".

For this process, rapid growth ligneous plants are mainly used, which, with the help of chemical substances (alkali or acids), in condition of high pressure and temperature, are selectively delignified to obtain pulps containing cellulose and other components of lignocellulose. LThese pulps are then submitted to mechanical and chemical-physical trea- 20 tments, in order to complete the removal of lignin and hemicellulose residual components, and utilised thereafter for paper production. Such paper making i* processes are characterised by a high consumption of thermal and mechanical energy and an as much high use of chemical reagents that are found, at the end of the process, in the fabrication waters mixed with the organic substances dissolved by cooking (refluents).

Refluents must be treated in satellite plants comparable, for size and complexity, to the same paper mills; because of the absolute need of treating refluents, running production units with a production power of less than 150,000 t/year is uneconomic and prevents therefore a cellulose production in countries, such as Italy, that have no large areas to be assigned to these productions.

The same holds good for countries whose internal paper consumptions are lower than the aforesaid quantities, as are generally emergent countries.

Fabrication yields, expressed as pulp quantity obtained compared to the starting material, vary within a wide range that depends especially on the quantity of 15 chemical reagents used, from a minimum amount of for bleached chemical pulps used in the fabrication of fine and very fine papers, to about for pulps produced utilising' only mechanical energy (however, such pulps have poor resistance and durability and are used especially for newspapers).

9* An approximate classification of pulps, based on the intrinsic qualities of pulps and fabrication yields, may be the following: Bleached chemical pulps 40-50% yield Raw chemical pulps 45-60% yield Semi-chemical pulps 70-75% yield Semi-mechanical pulps 75-85% yield Mechanical and thermomechanical pulps 85-93% yield Recently, many economic, ecological and market reasons have spurred an active interest for the setting up of new technologies for the production of cellulose pulps, which technologies, besides allowing to run small and little pollutant production units because of the use of lesser amounts of chemical products, may profitably use raw materials other than the traditional arboreal species, and in particular annual plants and vegetable residues coming from other agricultural-industrial workings. Among said technologies, the thermomechanical process used in the preparation of cellulose pulps is worthy mentioning, as this process provides several non negligible advantages, among which the high yields 15 and the production of effluents having a polluting charge markedly lower than that obtained by the use of conventional chemical processes.

In the beginning, the use of new technologies was on the colonisation of the material by fungi having a high .4 20 ligninolythic activity Ander, Eriksson, K.E.L., Svensk Papperstid. 78:641 (1975), but such approach was not applicable because of many drawbacks due to the high weight losses of the material, ascribable to mycelium metabolism, and especially to the length of the treatment period, which seemed incompatible with paper production cycles [Samuelsson, L. Mjoberg, Hartler, Vallander, L. and Eriks- 6 son,K.E.L., Svensk Papperstid. 83:221 (1980); Eriksson, Vallander, L. Svensk Papperstid., 85(6):33 (1982), even though said processes seemed to have giid results as concerns energy saving Myers, Leatham, Wegner, T.H., TAPPI J. 71(5):105 (1988]) and improvement in strength characteristics of paper layers.

Such difficulties have oriented research towards the development of applications based on the use of enzymes suitable for lignocellulose degradation. Said enzymes are produced by organisms that can utilise lignocellulose residues, in particular fungi responsible for wood butt rot, or more generically wood saprophyte mycelia, of which some thousands species are S. 15 known. In particular, the discovery of an enzyme, lignin peroxidase, involved in lignin degradation, has polarised the attention of many people on the development of applications based on its utilisation [Arbeloa, de Leseleuc, Goma, Pommier, J.C., 20 TAPPI J. 75(3):215 (1992)]. Afterwards, also these applications have been downsized by several evidences; in particular, the extreme fragility of this enzyme, the necessity of adding hydrogen peroxide to ensure S working, and the necessity of utilising it in combination with other enzymes, such as xylanase and betakylosidase, to obtain substantial results [Viikari, L., Ranua, Kantelinen, Sundqvist, Linko, M.

'L

7 Proceed. 3rd Int. Symp. on Biotechnol. in the Pulp and Paper Ind., 67 (1986)].

It is an advantage that in one or more forms of this invention, a process may be provided for the production of cellulose paper pulps allowing to use as raw materials both the conventional raw materials such as arboreal species and annual plants especially cultivated, such as textile plants, kenaf and the like, and also waste material, such as cereal straws, maize stalks, and the like.

It is a further advantage that in another form there may be provided a process for the production of paper pulps from vegetable biomasses, essentially by 1 biodelignification, that is highly selective with regard 15 to the attack of lignocellulose copolymers, that may be realised according to a continuous process, with high o .yields, that gives constant and reproducible results, and a S that allows a limited use of reagents and produces no toxic and/or heavily polluting substances and/or 20 substances of difficult and expensive disposal.

These and related advantages which will be clearly understood from the following description, may be achieved by a process for the production of cellulose paper pulps from vegetable masses, which process, according to the present invention, comprises the following stages: sterilisation at a temperature higher than 120XC of a mass suitable to form the culture medium; S:25078A 8 mixing of said sterilised mass, inoculated with an inoculum in a dosed quantity, with heated and sterile water, in an amount such as to bring said inoculated mass to the wished temperature and concentration; conditioning and reaction under stirring of said inoculated mass in a controlled atmosphere of CO 2 and 02 and in a sterile environment, at controlled temperature and pH, for a period comprised between 20 and 300 hours, with production of suitable enzyme mixes; elementarisation of the mass containing said enzyme mixes and soaking up of the same with an extraction fluid, such as water, with formation of a suspension; extraction of the enzymes present in said extraction fluid through pressing and backwashing of said 15 suspension, obtaining an extract of enzymes, and separation of the exhausted solid resulting from said pressing; elementarisation, separation, cleaning and selection of vegetable ;materials for the production of said 20 cellulose paper pulp, obtaining a vegetable mass and a vegetable waste material; compacting of said vegetable mass to eliminate the air contained in said mass and to reduce its volume; mixing of said compact mass with said enzyme extracts in dosed quantity and possibly with heated water, in order to obtain a vegetable mass with a solid content comprised between 10 and 50% by weight; 'r t.

9 conditioning and reaction under stirring of said vegetable mass, mixed with said enzymes in a controlled atmosphere of CO 2 and 02, with controlled temperature and pH for a period comprised between 5 and hours and subsequent washing with water, obtaining a washed cellulose paper pulp with a low content of residual modified lignin and a washing fluid containing the soluble substances originally contained in said vegetable material together with the substances solubilised by the biological attack; possible cooking and bleaching treatment of said washed cellulose pulp; purification and disposal of said washing fluid.

More particularly, said vegetable material for the 15 production of cellulose paper pulp is constituted of a annual cultivated plants, such as kenaf (Hybiscus cannabinus), hemp, flax, cotton, various stems and the like, and/or agricultural-industrial residues, such as cereal straws (wheat, barley, rye, rice), maize stalks, 20 etc.

Advantageously, said inoculum is constituted of edible ligninolythic mushrooms, such as "Lentinus edodes", "Pleurotus eryngii", "Pleurotus sajor caju", extracts thereof and/or liquid, semisolid or solid culture media thereof.

Different species of mushrooms such as: Laetiporus sulphureus, Pleurotus ostreatus, Pleurotus sajor-caju, Pleurotus eringii, Coprinus stercorarius, Stropharia ferrii, Lentinus edodes, Trichoderma koningii, Trichotecium roseum, Penicillium sp., etc., have been inoculated on wheat straw, maize stalks, stumps of Eucalyptus camaldulensis and kenaf stems (Hibiscus cannabinus).

Such mushrooms may also be grown in artificial conditions, either on solid media (solid state fermentation) or liquid media (submerged fermentation) in order to obtain the production of such exocellular enzymes [Giovannozzi-Sermanni, G.Porri, A. Chimicaoggi 3,15-19 (1989); Giovannozzi-Sermanni et al., AgroFoof Ind. HiTech 39 (1992)].

In conditions of optimum ratio between one another, 15 such exoenzymes may be utilised for selective biodelignification. Generally, said enzymes are produced by selected fungus cultures, so that the activity of the enzymes produced .by the same are as high as possible with regard to lignins and hemicelluloses and as low 20 as possible with regard to celluloses.

In the solid state, they may be obtained by means of an especially designed batch bioreactor which allows to obtain controlled growth conditions, to obtain the mix of exaenzymes in a rigorously reproducible manner [Giovannozzi-Sermanni et al., Chimicaoggi 3:55 (1987)].

The preparation of the enzyme cocktail may be carried out using the already mentioned solid state 11 fermentation technique; among other things, this technique allows to utilise as fungus culture medium the vegetable wastes derived from the dry cleaning of the vegetable intended for the fabrication of cellulose pulps or other vegetable waste biomass.

As has been said, the delignification process subject matter of this invention satisfies some basic requirements, such as: degradation uniformity of the lignocellulose biomass, process velocity, result reproducibility, biodegradation efficiency, mycelium growth optimisation, attack selectivity of lignocellulose copolymers, absence of toxic compound of fungus-origin, such as aflatoxins, in refluents, possibility of carrying on a continuous production of the enzyme 15 mix, possibility of carrying on the biodelignification process utilising a continuous enzymatic mixes process.

The process subject matter of the present invention is illustrated hereunder with reference to the 9*9 20 amended drawings appended by way of nonlimiting illu- 9* stration of the same process wherein: Figure 1 shows schematically the enzyme production cycle, while Figure 2 shows, always schematically, the biological treatment cycle, Preparation of the enzyme mix (Figure 1) Sterilisation at a temperature higher than of 120 0 C of the 12 biomass which will form the culture medium. Sterilisation, according to the present invention, is carried out in the dry phase by means of injections of middle pressure (100-150 kPa) vapour overheated at 200-300 0 C, at the bottom of a continuous-working cylindrical tower 1. The vegetable to be sterilised is fed in the upper part of tower 1 and extracted at the base after an average permanence of about minutes at the chosen temperature; extraction is through a system of mobile screws 2 (of the living bottom bin type) or another system allowing its dosage at the following working station. The dosed material falls into a mixing and transport tilting screw 3 at whose base the inoculum is 15 added as well as a quantity of hot and sterile.

water from tank 4, sufficient to bring the vegetable mass to the wished concentration and temperature; large diameter screw 3, having a very contained angular velocity, transports the 99* 20 material to the reaction chamber 5, where, in an atmosphere of C0 2 0 2 ,controlled pH and temperature, the production of the enzyme takes place. From the moment of the inlet in the sterilisation tower 1 to the end of the reaction chamber 5, the plant is air-tight and the vegetable material is kept out of the contact with the air, to prevent possible infections, etc.

The handling of the biomass in the reaction chamber is performed by a set of tilting axis screws 6 which perform the functions of mixing and handling the fermenting vegetable bed, transporting the biomass from inlet to outlet of the reaction chamber, intimate insertion in the reaction mass of instruments suitable to measure the conditions of temperature, pH, etc. of thermostating (heating, cooling) of the fermenting mass, injection of possible pH corrective solutions, or anyhow solutions useful for the process.

To be in condition of carrying out all these operations, the set of screws is mounted on trolley 7 of a bridge crane that allows its 15 traverse according to the two axes of the :reaction chamber; the feed of the material is regulated by the traverse modulable speed of trolley 7 and by the tilt of the axis of screws 6 (0 to 45 degrees), while stirring up is regulated by 20 the rotation modulable speed of the same screws.

The permanence time in the reaction chamber 5 is from 24 to 240 hours and at the end of the period establis- •coo hed the vegetable, as a consequence of the effect of the traverse movement performed by the screws, has reached the outlet of the reaction chamber from where it is sent on to a hydraulic pulper 8 which elementarises and soaks it up with the enzyme 14 extraction fluid, generally water.

Such suspension undergoes a double pressing and backwashing which extracts the enzyme almost completely; the enzyme is sent on directly, according to a continuous method, to the treatment of the vegetable to be transformed into paper pulp, while the exhausted material resulting from the pressing gets out of the biological cycle and may be utilised to produce compost or the like.

Biodelignification process (Figure 2) The vegetable material to be utilised for the production of cellulose pulps is elementarised in a hammer mill 9 continuously fed by a rotary hopper; the treatment of hammer mill 9 has also the function a 15 of breaking the possible knots of stems and pulverising leaves, twigs still attached to the vegetable, pith, and removing bast from wood of textile plants, making possible, if so wished, the subsequent separation.

20 It follows a pneumatic transport which feed a rotating a.* tumbler 10 provided with reels and counter reels which has the function of removing the undesirable parts and of separating, if so whished, bast from wood.

The clean and possibly selected vegetable is fed to a rotor-compactor 11 whose function is to stably reduce the volume of the vegetable mass and to eliminate a great part of the air contained within the latter. This material is fed to a mixing and transport tilting screw 12, at whose base the suspension of the -enzyme obtained as said hereinabove and possibly hot water are added, so as to bring the concentration of the vegetable mass to a percent of to In such process conditions, the vegetable masses which, however compacted, keep the form memory, quickly and easily absorb the enzyme mix, which, acting in rapid and a capillary way, increases time and quantity efficiency of biodelignification.

The screw transports the material into a reaction chamber 13 with a controlled atmosphere, quite similar, as concerns the working principle, to the just *f S" 15 described one for the production of the enzyme and provided with a set of adjustable axis screws 14 mounted on trolley 15; the biological treatment has a duration comprised between 6 and 24 hours.

Preferably, the coils ofhandling screws are hollow 20 with internal circulation of thermostated fluids; the metal structure of screws may carry the various sensors of the control instruments and homogeneously distribute in the reaction mass fluids for pH correc- 0 tion or anyhow useful for the good outcome of the reaction.

At the end of the biological stage, the material is extracted and passed on to a multi-stage backwashing plant; the washing fluid contains all the soluble substances that were contained at the start in the vegetable and also those that have been solubilised by the biological attack; its BOD and COD content is about 4000 6000 ppm and, given the partial degradation of the dissolved organic molecules, its purification is usually possible by a simple chemicalphysical treatment followed by a suitable biological treatment.

Washed pulps have a content of residual modified lignin of about 6-10% in the case of bast of textile plants, and the possible subsequent cooking treatments may be less aggressive than those generally used for the same pulps not biologicalally 0o0 15 treated (generally, to arrive at the complete elementarisation of fibres, a mild alkaline treatment in an oxidising environment suffices).

Pulp production operations have been carried out, using the same vegetable material, without and with ee prior biological treatment, to be in condition of compare and quantify advantages and benefits brought about by the technology subject matter of the present invention.

The characteristics of biotreated pulps referred to not biotreated pulps with comparable dripping show that: the percent of reagent and the mechanical energy necessary to arrive at a given dripping of fibres is always lower for the biotreated material, which means that, during the biological treatment the lignin fraction undergoes a deep disgregating action. In the case of kenaf bast, it was even possible to obtain the elementarisation of fibres without any chemical help and the mechanical energy used resulted to be less than half the one necessary in conventional treatments; the process total yields are markedly higher for pulps obtained with a prior biotreatment.

This, besides being an important economic factor, confirms the great selectivity and efficaciousness of the biological attack.

The process subject matter of the present invention *i is suitable for the treatment of traditional raw materials (arboreal species) as well as of especially cultivated annual plants (textile plants with special reference to kenaf), and of waste biomasses (cereal straws, maize stalks, etc.). Through the setting up and mutual harmonisation of the biologi- *cal, biochemical and technological components with more than positive results, this process allows: optimisation of mycelium growth processes, attack selectivity on lignocellulose polymers, reproducibility of results, biodegradation efficiency velocity of biological processes fully in keeping with industrial times, possibility of continuous operation with fully automated plants and cycles, absence of toxic compounds of fungus-origin.

Concerning the process aspect, several steps have been set up consisting of the following main points: mechanical pre-treatment of stems of annual plants (cotton, flax, Graminae straws, stalks, kenaf, etc.), to separate bast from xylem, without compromising the fibre length, loading of the vegetable in the inside of a rotary or continuous bioreactor, addition of a hexocellular enzym cocktail to S 15 lignecellulose material, mix incubation at variable temperatures and for a variable period of time, .e washing of the material biotreated for the production of cellulose pulp and the fabrication of paper, utilising a thermomechanical treatment.

In the following some examples are given of produc- :.tion of cellulose pulps obtained from annual plants and in particular kenaf bast and wood and agricultural residues (wheat straw and maize stalks).

According to the present invention, all the operations concerning the production of the enzyme are carried out according to a continuous method and 19 therefore the running of the enzyme production plant can be fully automated with extreme easiness. At the same time, the storing time and quantity which would need particular cares especially as concerns preservation temperature is reduced to a minimum.

The biological treatment with enzymes of the vegetable to be transformed into cellulose pulp, besides being modulable and selective with regard to lignins and/or hemicelluloses takes place at very contained temperatures and therefore in conditions that cause the possible polycondensations of the lignin macromolecules that hinder the subsequent operations of transformation into pulp and of bleaching to be extremely limited.

The biological attack of the material to be used for .:the production of cellulose takes place in reaction chambers like those used for the production of the enzyme according to a likewise continuous and relatie e vely quick process, easily adjustable and automatically S 20 controllable for all the mass being worked.

It is also worthy stressing that the prior biological treatment allows to utilise, in the subsequent transformation into pulp, mild treatments (mechanical, thermal, chemical), with ensuing remarkable saving of mechanical and thermal energy and of chemical reagents; also the global costs of industrial installation and the running costs are much reduced compared to those of conventional plants. Besides, as the biological activity is extremely selective, the yields of pulp production obtainable through the biological treatment are on the average higher with respect to conventional yields, and the selectivity of biological attack involes a lower hydrolysis of cellulose chains with ensuing improvement of all the mechanical characteristics of the pulps produced and especially of the tearing index that is the most required characteristic for almost all the types of paper.

In keeping with the greater global yield of transformation into pulps and the reduced use of reagents, -the content of organic and inorganic substances of refluents it markedly reduced, which 15 causes the purification of the same to be less expensive.

For particular vegetables (such as the bast of *kenaf and other textile plants), for whose transformation into paper pulps the biological treatment alone 20 followed by an appropriate mechanical treatment may suffice, the industrial plant and its running may be particularly simple and little expensive; also the treatment of refluents might be limited to a simple e e chemical-physical treatment followed by a particularly accurate biological treatment.

The whole without adversely affecting in any way the physical-mechanical and optical qualities of the producible pulps. Besides, the simplicity of the biological-mechanical treatment alone, and the contained cost of the plants for the transformation into paper pulp that can be used for some particular types of vegetable allow the running of small size plants like those that might be installed in countries that do not have large areas to be allocated for paper production.

EXAMPLE 1 Kenaf bast, suitably chopped up in such a way as not to jeopardise fibre length, was treated with an enzyme mix obtained by growing the mushroom Lentinus edodes in liquid medium.

Such mix was added to the solid medium, adopting the 15 5:1 volume/weight ratio, and the whole was allowed to incubate at 40xC for 24 hours in a fermenter. The mix was characterised by the presence of enzyme activities involved in the degradation of the polymers of the vegetable wall, except for cellulases, that may play an unwished role in such applications.

At the end of the incubation, the material was pressed and submitted to the thermomechanical process.

Such pre-treatment of a semi-industrial type (400 kg/h) allowed to consistently reduce pulp dripping, which is an important parameter in paper industry, as it is an indirect measure of water retention by the same pulp. As a consequence a reduction in the same positively affects paper production time. Pulp yield did not undergo significant reduction compared to control. Another consequence of biotreatment was an increase in some properties of strength of the obtained layer compared to untreated control, in particular the values of ultimate length and burst index were higher than the control by 36 and 45% respectively.

Besides, using a peroxide bleach, a degree of whiteness was obtained that was greatly improved with respect to control.

Table 1 biotreated control dripping 25 density 0.38 0.56 traction index 34.0 25.0 tearing index 6.2 4.1 :I burst index 2.8 IRB (degree of 75 whiteness) EXAMPLE 2 In this case, an enzyme preparation was used that had been obtained by hydraulically pressing the lignocellulose material (wheat straw) colonised by the Lentinus edodes mushroom. Said preparation contained an activity spectrum wider than that of the preparation obtained from fluid culture of the same mushroom, and was in particular characterised by the presence of celluloselythic enzymes and a higher manganesedependent and hemicellulosic peroxidase activity, with respect to the extract utilised in Example 1.

Kenaf bast was treated in the same conditions of Example 1, except for the treatment time which was halved (12 hours). Such reduction, allowed by a greater volumetric activity of the individual enzymes contained in the mix (in particular laccase, tyrosinase, Mn-peroxidase and endoxylanase, esterase, oxygenase, etc.), was also adopted to prevent unwished effects due to the presence of celluloselythic activities that could jeopardise the integrity of the fibres. The chemical quantitative analysis of wall polymers of biologically treated samples compared 15 to control, showed a reduction in lignin content of about 10-12% and a marked reduction of the hemicellulose fraction, while cellulose appeared to be unalterated. Also in this case, a substantial .reduction in dripping was noticed as well as an in- 20 crease with respect to controls in the ultimate length and the burst index (Table 2).

Table 2 biotreated control Sdripping 28 37 density 0.42 0.60 traction index 41 28 tearing index 5.8 3.9 burst index 2.8 1.8 IRB (degree of 77 62 whiteness) EXAMPLE 3 An enzyme preparation obtained by growing for seven days the mushroom Pleurotus eryngii according to the submerged cultivation method was utilised to treat maize stalks. The preparation was added to the material to be treated according to a 1:6 weight/volume ratio, and the whole was allowed to incubate for 24 hours at 50xC. The analysis of the fibrous composition of the material showed that the cellulose and hemicellulose contents were unchanged with respect to the control, while lignin content was reduced by 15 10%. Such material was submitted to the thermomechanical process. The pulp yield was not significantly reduced, while its dripping was markedly reduced compared to control..

Burst index appeared to have improved with respect to 20 control as well as ultimate length. (Table 3).

Table 3 biotreated control dripping 27 37 density 0.45 0.52 traction index 35 27 tearing index 4.5 3.2 burst index 2.9 2.2 IRB (degree of 62 48 whiteness) EXAMPLE 4 The repetition of the biotreatment described for Exampie 3 with the same extract diluted 10 times in water allowed to obtain results comparable to those of the preceding example, suggesting the possibility of reducing the concentration of biocatalysts in such process. (Table 4).

Table 4

S..

S..

S

S

S

dripping density traction index tearing index burst index IRB (degree of whiteness) biotreated 25 0.42 39 5.2 3.0 65 control 42 0.66 28 2.8 2.3 51 25A In the claims which follow and in the preceding description of the invention, except where the context requires otherwise due to express language or necessary implication, the words "comprises" and "comprising" are used in the sense of "includes" and "including", i.e. the features specified may be associated with further features in various embodiments of the invention.

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Claims (4)

1. A process for the production of cellulose paper pulps from vegetable masses, characterised in that it comprises the following stages: sterilisation at a temperature in excess of 120xC of a mass suitable to form the culture medium; mixing of said sterilised and dosed mass with a dosed inoculum and heated and sterile water, in such a quantity as to bring said inoculated mass to the wished temperature and concentration; conditioning and reaction under stirring of said inoculated mass in a controlled atmosphere of C02 and 02 and sterile environment with controlled temperatu- re and pH for a period of time comprised between 20 and 300 hours, with production of suitable enzyme mixes; elementarisation of the mass containing said enzy- mes and soaking up of the same with an extraction fluid such as water, with formation of a suspension; extraction of the enzymes included in said extraction fluid by pressing and backwashing said suspension, obtaining an enzyme extract and separation of the exhausted solid resulting from said pressing; elementarisation, separation, cleaning and selection of vegetable material for the production of said cellulose paper pulp, obtaining a useful vegetable mass and waste material; compacting of said useful mass to eliminate air included in said mass and to reduce its volume; mixing of said compacted mass with said enzyme extracts in dosed quantity and possibly with heated water, so as to obtain a vegetable mass having a solid content comprised between 10 and 50% by weight; conditioning and reaction under stirring of said vegetable mass mixed with said enzymes in a controlled atmosphere of C02 and 02 with controlled temperature and pH for a time comprised between 5 and 50 hours and subsequent washing with water, obtaining a washed cellulose paper pulp with a low content of residual modified lignin and a washing fluid containing the soluble substances that were contained at the start in 15 said vegetable material together with the substances *solubilised by the biological attack; possible cooking and bleaching treatment of said washed cellulose pulp; S- purification and disposal of said washing fluid. .20 2. Process according to claim 1, characterised in that said vegetable material for the production of cellulose :i: paper pulp is constituted by cultivated annual plants, such as kenaf (Hybiscus cannabinus), hemp, flax, cotton and various stems and/or agricultural-industrial resi- dues, such as cereal straws, maize stalks.

3. Process according to claim 1, characterised in that said inoculum is constituted of edible ligninolythic mushrooms, such as "Lentinus edodes", "Pleurotus eryn- gii", "Pleurotus sajor-caju", extracts thereof and/or fluid, semisolid or solid culture medium thereof.

4. Process according to claim 1, characterised in that said sterilisation is carried out in the dry phase through injection of medium pressure vapour, of about

100-150 kPa, overheated at 200-300xC, for a period of time of about 20-60 min. Process according to claim 1, characterised in that said mass suitable to form said culture medium is constituted of said waste material or of material obtained from the cleaning and selection of said vegetable material and/or little valuable waste vegeta- ble residues. 15 6. Process according to claim 1, characterised in that said elementarisation of said mass containing said enzyme mixes is carried out by a mechanical-hydraulic action in water. 7. Process according to claim 1, characterised in that 20 the stages necessary to obtain said enzyme extract and/or the stages necessary to obtain said washed cellulose paper pulps are carried out according to a continuous method and can be automated. 8. Process according to claim 1, characterised in that it takes place at low temperature and therefore in conditions such as to markedly reduce the possibility of polycondensation of lignin macromolecules that hinder the possible cooking and bleaching operations. 9. An apparatus to realise the process for the produc- tion of cellulose paper pulps from biological masses according to claim 1, characterised in that it compri- ses: a tower for the sterilisation of the mass suitable to form the culture medium; -a first screw for mixing said sterilised mass with the inoculum and handling of the same in a sterile environment; a first conditioning and reaction chamber provided with means suitable for mixing and handling the inoculated mass in a sterile environment and control- led atmosphere of C02 and 02, with controlled tempera- 15 ture and pH; a hydraulic pulper for the elementarisation of the mass and its soaking up with the suspensions of enzyme S: mixes; S- a hammer mill for the elementarisation of the vegeta- 20 ble material, to break up the knots of the stems and pulverise the leaves, detach bast from wood, etc.; a rotating tumbler provided with reels and counter reels for separating the various fractions; a rotor compactor to reduce the volume of the vege- table mass and to remove the greatest part of the air contained in the same; -a second screw for mixing said compacted vegetable mass with the extracts containing the enzymes and possibly with water for its handling in a sterile environment; a second conditioning and reaction chamber provided with means suitable for the mixing and handling of the vegetable mass mixed with the enzymes in a sterile environment and controlled atmosphere of C02 and 02, with controlled temperature and pH; apparatuses of a known type for cooking and bleaching cellulose pulps, as well as for the dispo- sal of refluents. Apparatus according to claim 9, characterised in that said first and/or said second screws are provided with hollow coils, with internal circulation 15 of thermostatic fluids, and also with sensors for the *00 various control instruments, as well as means suitable .o ~to homogeneously distribute in said sterilised mass S.. .g 0 and/or said compacted vegetable mass suitable pH S• correctives and/or various additives. 11. Apparatus according to claim 9, characterised in that said first and said second conditioning and reac- e tion chambers are provided with tilting axis screws translatable along all the surface of the chamber by means of a bridge crane or the like, and adjustable as concerns the tilt angle, rotation speed, and traverse speed, so as to keep in constant movement the reaction mass and to control the reaction progress and speed, as well as the permanence time of the reacting masses in said chambers. 12. Cellulose paper pulps obtained from cultivated annual plants such as kenaf (Hybiscus cannabinus), hemp, flax, cotton and various stems and/or agricultu- ral-industrial residues, such as cereal straws and maize stalks. 13. A process for the production of cellulose paper from vegetable masses substantially as herein described with reference to any one of Figures 1 or 2 or Examples 1 to 4, excluding comparative or control processes. 14. Apparatus for the production of cellulose paper from vegetable masses substantially as herein 15 described with reference to the accompanying drawings. g. Dated this 31st day of July 1997 20 CONSIGLIO NAZIONALE DELLE RICERCHE and UNIVERSITA' DEGLI STUDI DELLA e. a TUSCIA DIPARTIMENTO DI AGROBIOLOGIA E AGROCHIMICA By their Patent Attorney GRIFFITH HACK too•