SOLUBILISATION AND HYDROLYSIS OF CELLULOSE-CONTAINING MATERIALS

Abstract: A process for the solubilisation and/or hydrolysis of a cellulose-containing material wherein the material is con­ tacted with hydrogen chloride, water and calcium chloride to produce a reaction mixture of specified composition. Prefer­ ably the process is used to convert wood pulp or paper into syrups containing glucose.

Description: Solubilisation and hydrolysis of cellulose-containing materials This invention relates to a process for the solubilisation and hydrolysis of cellulose-containing materials. Cellulose-containing materials are derived originally from plants and generally contain, in addition to cellulose, hemi-cellulose and lignin. Cellulose is a polymer, the chain units of which are essentially all derived from glucose. Hemicellulose is a polymer the chain units of which are derived from various sugars, mninly glucose and xylose but with other sugar units occurring depending upon the source of the cellulose. Cellulose occurs in both crystalline and amorphous forms, the crystalline form being more common. hydrolysis of crystalline cellulose is rendered difficult because its ordered structure impedes the approach of enzymes or other reagents to the glycosidic links in the cellulose chains thereby making it difficult for these reagents to break down the glycosidic links, In recent years a considerable amount of research has been carried out to find satisfactory processes for the solubilisation and hydrolysis of glycosidically linked carbohydrates such as cellulose or starch to produce simpler materials including higher sacchorides, tri-, di- saccharides and particularly monosaccharides such as glucose. In our co-pending UX Patent Application No. 8210005 and our published European Patent Application No. 44622 we propose processes for treating glycosidically linked carbohydrates with mixtures comprising inorganic acids and various metal halides including calcium chloride. Additionally UsP 4018620 discloses a process for hydrolysing cellulose to monosaccharides in high yields by reflexing a slightly acid mixture of the cellulose and calcium chloride. At first sight the use of calcium chloride as the metal halide in such a process offers a number of advantages including for example low materials cost and ease of recovery. However use of calcium chloride in processes such as those mentioned above also presents a disadvantage in that solubilisation and hydrolysis can be incomplete. For example, when a solution containing a saturation concentration of calcium chloride and less than 3-446 hydrogen chloride by weight is used, incomplete solubilisation and hydrolysis occurs and dehydration of glucose is rapid especially at temperatures above 90 C. We have now found that the relative amounts of the various components included in the reaction mixture for the solubilisation and hydrolysis of cellulose using calcium chloride and hydrochloric acid can have a significant effect upon the course of the reaction. In particular the water content of the reaction mixture is important. According to the present invention we provide a process for the solubilisation and/or hydrolysis of a cellulose-containing material in which the material is contacted with hydrogen chloride, water and calcium chloride to form a reaction mixture comprising 30 to 60 water, 18 to 45% hydrogen chloride, 3 to 35% calcium chloride and 1 to 30% cellulose-containing material (all percentages being by weight based upon the total weight of the reaction mixture), the reaction mixture is maintained in a closed system under a pressure in the range 3 to 50 atmospheres absolute for a period of tine in the range 2 minutes to 12 hours, a suiar-contain- ing product is removed from the closed system and from this product hydrogen chloride and calcium containing materials are separated and recovered. The process of the invention is suitable for the solubilisation and/or hydrolysis of any cellulose-containing material in any form. Thus the process can be applied to cellulose alone or, more usually, to cellulose admixed with other constituents either in natural products or manufactured articles. Examples of cellulose-containing materials to which the process may be applied include wood, straw, mechanical pulp, chemical pulp, newspaper, cardboard, bagasse, brewer's grain, corn stover, cotton, waste paper from paper manufacturers, other naturally occurring sources, agricultural products, waste products, by-products and manufactured products. The process is applicable to crystalline cellulose and to cellulose occurring with lignin without prior delignification. Some forms of cellulose-containing materials may require a prior treatment before being supplied to the process of the invention. A prehydrolysis of the lignocellulosic material can be used to separate and recover the hemicellulosic or pectinaceous sugars. These include xylose, glucose, arabinose and mannose amongst others. It also has the effect of removing highly proteinaceous material from some of the lignocellulosic substrate, for example brewing grain waste and bagasse or sugar beet pulp which can be easily recovered and used as a component of the diet in anaal feed. It also has the added facility of opening up the cellulosic structure for the later main hydrolysis. The prehydrolysis that has been used in this process is dilute acid, preferably HC1, at concentrations of not greater than 2% W/w. The concentration of the lignocellulosic substrate is between 5-324 W/w. The mixture generated is heated between 1000C - 1800C for 10-60 minutes dependent on the type of lignocellulosic material used. At higher temperatures unwanted byproducts may accumulate and it is therefore essential to optimise the conditions of the prehydrolysis to suit the choice of substrate. Using this technique the vast majority of the hemicellulosic component of the substrate is hydrolysed to the resulting monosaccharides without directly affecting the cellulosic and lignin components which remain as suspended matter. The resulting solution is separated from the undissolved solids by filtration, at lower substrate concentrations or by compressing the solids to exclude the liquid. The solids are then subjected to full hydrolysis as described below. The solution can be neutralised by addition of alkali. It has been found that between pH 2.0 - 4.5 proteins precipitate out of solution and can be collected and recovered by simple filtration or centrifugation. These can be used as components in animal feed. The rFn=irring solution can be recycled with or without addition of acid to pretreat further quantities of lignocellulosic material. The solution from these pretreatments can then be used for fermentation, or by purification, for chemical manufacture for example, the hydrogenation of the purified xylose component to xylitol. The sugar-containing product produced by the process may contain higher saccbarides, tri-, di- saccharides and monosaccharides. More specifically the product may contain cellodextrins, cellotriose, cellobiose and particularly glucose. The composition of the product depends upon the reaction conditions employed. Preferably the process is operated to produce a syrup containing a high proportion of glucose. Products include as would be expected, some degradation products produced by acid catalysis of glucose to hydroxymethyl furfural and other degradation products. However using the process of the invention the amounts of these degradation products are minimal except at temperatures above 120 C. In operating the process of the invention to produce glucose it is theoretically possible to achieve 110 conversion, i.e. 1 tonne of cellulose converts to 1.1 tonnes of glucose, the added mass being due to addition of water. Suitably the process is operated to achieve conversions of at least 60% and preferably 80 to a higher level between 100% and the theoretical maxim. Preferably the proportions in which the various components of the reaction mixture are present in that mixture as initially formed are as follows: (a) water 35% to 528; (b) hydrogen chloride 20% to 35%, especially 23% to 30K; (c) calcium chloride 5% to 25%, especially 10% to 25%; and (d) cellulose containing material 5% to 20%. All percentages are by weight based upon the total weight of the reaction mixture when it is first formed. The suitable form of calcium chloride in a given situation depends upon the form in which the hydrogen chloride is added and upon the amount of water in the cellulose-containing material. Thus if concentrated aqueous hydrogen chloride is used or if the cellulose-containing material is one containing a large proportion of water, e.g. brewers grain, anhydrous calcium chloride is preferred. Alternatively if anhydrous hydrogen chloride is used CaC12.6 0 is preferred. In some circumstances it may be useful to add hydrogen chloride both as concentrated aqueous and as anhydrous hydrogen chloride. Anhydrous calcium chloride and anhydrous hydrogen chloride can be added together if the cellulose-containing material is one having a large water content After formation of the reaction mixture it is retained in the closed system for a period of time in the range 2 minutes to 12 hours which is the duration of the treatment of the cellulosecontaining material with the hydrogen chloride/water/calcium chloride reagent mixture. During treatment the cellulose first solubilises and then hydrolyses. The duratian of the treatment depends upon the temperature and upon the concentration of the cellulose-containing material in the reaction mixture. For instance the lower the concentration of the cellulose-containing material in the reaction mixture the shorter the treatment time which is required. The treatment can be carried out in one or two stages. However when very short treatment times are used, i.e. 2 to 20 minutes, it is preferred to have only one treatment stage. The treatment, solubilisation and hydrolysis, takes place in a closed system in which an internally generated pressure is produced by calcium chloride absorbing water. hydrogen chloride comes out of solution in the reaction mixture. The pressure on the reaction mixture depends upon the temperature and upon the free space in the system above the reaction mixture. For solubilisation the pressure is preferably in the range 3 to 10 atmospheres absolute and for hydrolysis the pressure is preferably in the range 5 to 10 atmospheres. Suitable temperatures for the process of the invention are in the range 200 to 1200C. Solubilisation can take place at lower temperatures than those required for hydrolysis. Consequently when the treatment of cellulose-containing material with the reagent mixture is begun at a temperature towards the lower end of the suitable range, i.e. 200 to 500C, it will be advisable to raise the temperature after a while to assist hydro lysis to occur. Using temperatures in the range 500 to 1200, preferably 800 to 1000, solubilisation and hydrolysis can be achieved using the same temperature. At higher temperatures, i.e. above 1200C, solubilisatibn and hydrolysis can still be achieved but at such temperatures glucose which is produced is increasingly dehydrated to produce unwanted by-products, particularly furan derivatives. Consequently use of temperatures in excess of 120 C is not preferred. The process can be performed in two stages with further water being added to the reaction mixture after solubilisation of the cellulose-containing material has occurred. This variation of the process can produce an increase of 10 to 20% in the conversion of cellulose to glucose. The additional water is introduced into the system after an appropriate time has elapsed for solubilisation to have taken place. Generally the addition may be made after from 5 to 60 minutes from the beginning of the treatment depending upon the temperature. The amount of water added to the system in such an addition is suitably in the range 5 to 25g by weight based upon the total weight of the reaction mixture when the addition is made. It should be noted that the percentages quoted hereinbefore for the components present in the reaction mixture are for the reaction mixture when it is formed initially and do not take into account any later addition of water after solubilisation. After solubilisation and hydrolysis of the cellulosecontaining material the sugar-containing product is removed from the closed system and treated to separate hydrogen chloride and calcium containing materials - mainly calcium chloride - from it so that these can be re-used. The product can be passed into a large vessel thereby releasing the pressure upon it and causing hydrogen chloride to 'flash' off. The hydrogen chloride thus released can be condensed and collected. Preferably the product is passed into a large vessel which is under vacuum to facilitate release of hydrogen chloride. Any hydrogen chloride rAmPining in solution after this treatment can be neutralised preferably with calcium hydroxide. This will produce more calcium chloride in the solution which can be separated together with that already present therein. Any suitable method may be used for recovering calcium chloride from the Sugar-contsining product. A solvent extraction process may be used. When the process of the invention is used to produce a glucose-containing syrup this separation and extraction treatment will produce a glucose-containing syrup having some residual calcium chloride in it. This syrup may be subjected to further treatment if such further treatment is considered desirable. This will depend upon the quality of the extraction already performed and upon the quality of syrup which is required which will depend upon the end use of the syrup. Father treatments can be by ion exchange, dialysis, salting out or other conventional techniques. The treatment may be a combination of any of these techniques. A recovery method which is particularly advantageous with low concentrations of calcium chloride is electrodialysis. This method relies on the ionic nature of calcium chloride and upon the non-ionic nature of glucose. Essentially when electrodialysis is used a mixture of calcium chloride and glucose in aqueous solution enters an electrodialytic cell and is subjected to an electrical current at right angles to the direction of flow. Calcium chloride ionises in the presence of this current and both the calcium ions and the chloride ions migrate across charged membranes in the cell towards the electrodes. A stream contain ing glucose, which is not affected by electrical charges, flows straight through the cell. The diverted streams containing calcium and chloride ions are combined together and calcium chloride is thus separated from glucose. Hydrogen chloride and calcium chloride thus separated from the product can be re-used. The process of the invention may be performed as a batch or as a continuous process. In the case of a continuous process separated hydrogen chloride and calcium chloride may be re-cycled continuously to the reaction mixture. Mgnin and any unreacted cellulose containing material may be removed from the product at or after the stage at which hydrogen chloride is recovered. The cellulose-containing material may be subjected to a prior treatment before solubilisation and hydrolysis by the process of the invention in order to separate hemicellulose. This prior treatment may be with weak acid. Alternatively the hemicellulose component can be solubilised and hydrolysed by the process of the invention in which case the product will con tain an increased amount of sugars other than glucose. Whether or not a prior treatment is used depends upon the use intended for the product. The accompanying drawing is a schematic diagram of a plant for carrying out the process of the invention. In this an aqueous cellulose-containing substrate, containing e.g. brewers grain or waste paper pulp, passes from a supply vessel 1 to cellulosic feed preparation tank 2 in which it is mixed with hydrogen chloride, calcium chloride and water. Further water, hydrogen chloride and chloride from the recycle is added at point 3 to mixed feed flowing from preparation task 2 along pipe 4 to form a reaction mixture containin the various components in the correct proportions for the process. Prom point 3 the reaction mixture passes further along pipe 4 to pressurised hydrolysis vessel 5 where it is maintained at a pressure in the range 3 to 50 atmospheres absolute for a period of time within the range 2 minutes to 12 hours during which period solubilisation and hydrolysis occurs. A sugar-containing product is removed from pressurised hydrolysis vessel 5 along pipe 6 and hydrogen chloride separated from this product is passed along pipe 7 into recycled reagents preparation vessel 8. After separation of hydrogen chloride, the remainder of the sugar-containing product continues further along pipe 7 until it enters lignin and solids removal vessel 9. Waste lignin with a potential calorific value is separated from the product in vessel 9 and passes along pipe 10. The remainder of the product passes along pipe 11 to separator 12 from which calcium chloride is separated from the product to pass along pipe 13 into reagents preparation vessel 8. From separator 12 the product passes along pipe 14, through evaporator 15 and syrup purification stage 16, to enter storage vessel 17 as a purified glucose syrup, In recycled reagents preparation vessel 8, used hydrogen chloride and calcium chloride are mixed with water in appropriate proportions and the resulting mixture is fed into the mixed feed flowing along pipe 4 at point 3 to form the reaction mixture. Any material contained in the cellulose-containing substrate which is not to be allowed to pass via pipe 4 into the process is removed from cellulosic feed preparation tank 2 along waste pipe 18. The invention is illustrated by the following Examples :- XAMP 1 Three mixtures were made up. In each case anhydrous CaC12 (10 g) was dissolved in 30 mls (35.4 g) concentrated EC1 (35.38 g HCl/g H20). From the resulting solutions 10 g were taken and added to 1.25 g of Whatman filter paper NoO 1 in closed vessels. The mixtures contained: Cellulose 1.1875 g 10.56% W/w CaC12 2.2026 g 19.58% W/w HC1 2.7587 g 24.524/0 W/w Water 5.1012 g 45.34% W/w The mixtures were heated in the closed vessels at 700C for 7.5 minutes. At this stage 0.81 g R20 was added to one closed vessel, 1.92 g R20 to another and no water addition to the third. Further heating at 90 C for 4 minutes then followed. The closed vessels were cooled and their contents analysed for glucose using the automated Beckman Glucose analyser 2. The glucose analyses were as follows: 1. No water addition : 0.8194 g glucose. 2. 0.81 g R20 addition : 0.8907 g glucose. 3. 1.92 g H2O addition : 0.999 g glucose. EXAMPLE 2 Anhydrous CaC12 (30 g) was dissolved in 90 mls (106.2 g) concentrated HCl (35.38 g HCl/g H2O) at room temperature. From the resulting solution 10 g were taken and added to 1.25 g newsprint and 2.5 g newsprint in separate experiments. The newsprint contained 42% W/w cellulose. The compositions of the mixtures were as follows:- (i) 1.25 g newsprint newsprint 1.25 g 11.11% W/w CaCl2 2.203 g 19.58% W/w HCl 2.7590 g 24.52% W/w Water 5.038 g 44.78% W/w (ii) 2.5 g newsprint newsprint 2.5 g 20.0% W/w CaC12 2.203 g 17.62% W/w HCl 2.7590 g 22.07% w/w Water 5.038 g 40.3% W/w The mixtures were then heated in closed vessels for 8 minutes at 70 C and then cooled. Implicates of each reaction were run. After cooling water (2 g) was added to one of each of the duplicates, the vessels were heated again at 90 C for a further 4 minutes, cooled and analysed for glucose as described in the previous example:- (i) 1.25 g newsprint (a) no water addition : 0.4514 g glucose (b) 2 g water addition : 0.4919 g glucose (ii) 2.5 g newsprint (a) no water addition : 0.7245 g glucose (b) 2 g water addition : 0.8358 g glucose EXAMPLE 3 3 Three weak acid solutions were made up by putting 2.5 ml, 5 ml, 10 ml aliquots of concentrated hydrochloric acid into 100 ml volumetric flasks and making up to volume 100 ml with deionised water. Prom each of these solutions 10 g was taken and added to 1.25 g dried brewing grain waste. Two samples were done at each acid concentration. The mixtures produced contained respectively: (1) Brewing grain waste 1.25 g 11.1% w/w concentrated RCl (35.0% HCl W/w) 0.25 g 2.2% W/w Water 9.75 g 86.7% w/w (2) Brewing grain waste 1.25 g 11.1% W/w concentrated HC1 (35*0N HCl W/w) 0.5 g 4.4% w/w Water 9.5 g 84.4% W/w Brewing grain waste 1.25 g 11.1% w/w concentrated HCl (350% 1 W/w) 1. g 8.9% W/w Water 9. g 80. % W/w DB. In the above mixtures the W/w percentages quoted for HC1 are percentages of the 35.0% acid. One mixture of each acid concentration was heated at 1100 and 1500C respectively for 30 minutes then analysed for xylose, glucose and arabinose by HPLC. The mixtures at each acid concentration were heated at 1100 and 1500C respectively for 30 minutes and then analysed for xylose, glucose and arabinose by high pressure liquid chromatography. The analysis results for these sugars were as follows: At 1100C ffi xylose % glucose % arabinose 2.2% Conc. HC1 10.4 1.6 9.6 4.4% Conc. HC1 14.4 4.0 8.8 8.9% Conc. HC1 17.6 5.6 9.6 At 1500C % xylose % glucose % arabinose 2.2% Conc. HC1 17.6 6.4 9.6 4.4% Conic. HC1 15.2 7.2 8.8 8.9% Conc. HC1 12.8 7.2 8.0 The results are expressed as the percentage conversions to sugars of the total weight of solids treated. EXAMPLE 4 Hemicellulose hydrolysis - Brewing grain waste. A weak acid solution was made by putting 2.5 mls concentrated hydrochloric acid into a 100 ml volumetric flask and making up to volume with deionised water. From this solution 10 g was taken and added to 1.25 g of brewing grain waste (dried). The resulting mixture contained: Brewing grain waste 1.25 g 11.1% w/w Conc. HO1 0.25 g 2.2% W/w R20 9.75 g 86.7% W/w 0 This mixture was heated at 140 C for 30 minutes and the surplus liquor was then decanted off. (1X) When 10 mls of this liquor had been collected it was used to hydrolyse a fresh batch of brewing grain waste under the same conditions as before, surplus liquor again being decanted off (2X). The surplus liquor which was decanted off on each occasion, i.e. (1X) and (2X), was analysed for glucose, xylose and arabinose by high pressure liquid chromatography. The analysis results were as follows: % xylose % glucose % arabinose 1X 2 0.7 1.1 2x 3.8 1.3 2.3 The above figures are the total percentage of each sugar in the decanted solution. EXAMPLE 5 The method described in Example 2 was repeated using brewing grain containing 14% cellulose by weight, as determined by analysis, in place of newsprint. The results obtained were as follows: (i) 1.25 g brewing grain (a) no water addition : 0.156 g glucose (b) 2 g water addition : 0.185 g glucose (ii) 2.5 g brewing grain (a) no water addition : 0.29 g glucose (b) 2 g water addition : 0.35 g glucose EXAMPLE 6 Two mixtures were made up. In each case 10 g CaC12 was dissolved in 30 mls (3504 g) concentrated HC1 (35.38 g HCl/g H2O). From the resulting solutions 10 g was taken and added to 0.6 g. Whatman No. 1 filter paper in closed vessels. The resulting mixtures contained: Cellulose 0.57 g 5.1% W/w CaC12 2.2026 g 20.8 W/w HCl 2.7587 g 26.054 w/w H20 5.0712 g 47.8% w/w The Whatman filter paper used contained 5% W/w moisture. The mixtures were heated in closed vessels at 70 C for 7.5 minutes. At this stage 1.92 g R20 was added to one closed vessel, no water being added-to the other. Further heating at 900C for 4 minutes then followed. The closed vessels were cooled and their contents were analysed for glucose using a Beckmxn Glucose Analyser 2. The glucose analyses were as follows: g glucose (i) No water addition : 0.47 (ii) 1.92 g water addition : 0.56 EXAMPLE 7 Hydrolysis of straw Two mixtures were made up. In each case 10 g anhydrous CaC12 was dissolved in 30 ml (35.4 g) concentrated HC1. (35.38 g RCl/g H2O). Prom the resulting solutions 5 g aliquots were taken and were added to 0.63 g straw in closed vessels. The straw contained 32% cellulose. The resulting mixtures contained: Straw 0.63 g 11.11% W/w CaC12 1.1015 g 19.58% W/w HCl 1.3795 g 24.52% W/w R20 2.519 g 44.8% w/w The mixtures were heated for 7.5 minutes at 700C and were then cooled. After cooling, water (2 g) was added to one of the mixtures and both mixtures were heated again at 900C for 4 minutes. The closed vessels containing the mixtures were cooled and their contents were analysed for glucose. Analysis results were as follows: (1) No water addition : 0.15 g glucose (2) 2 g water addition : 0.17 g glucose EXXMPLE 8 150 g concentrated hydrochloric acid was cooled to -10 C in a sealed container. To this was added 50 g anhydrous calcium chloride and the container was again sealed. The contents of the sealed container were mixed for 1 hour after which they were stored at -100C overnight. The resulting clear solution (A) was used to effect solubilisation/hydrolysis in the following experiments:- (i) 4 g of Whatman Filter Paper No. 1 were placed in a tube to which was added 36 g of solution (A) and the tube was sealed containing the mixture having the following composition: Cellulose 4 g 9.5% W/w CaC12 1.83 g 4.69/0 w/w HC1 13.69 g 34.2% W/w Water 20.48 g 51.71% W/w The tube was heated at 600C for 15 minutes until its contents were solubilised. It was then heated at 90 C for a further 3 minutes to complete the reaction giving a 75% conversion of cellulose to glucose. (ii) Experiment (i) was repeated with a reduced cellulose concentration, the total weight being maintained at 40 g. The mixture had the following composition: Cellulose 3.0 g 7.13% W/w CaC12 3- 9 g 7.67% W/w HCl2 13.51 g 33.78% W/w Water 20.4 g 51.0% w/w The tube was heated at 600C for 15 minutes with mixing, until its contents were solubilised. It was then heated at 900C for a further 3 minutes to complete the reaction giving a conversion of cellulose to glucose of 82.5%. EXEMPLE 9 Comparative Example Cellulose hydrolysis using hiVh CaC12 and low 1101 concentrations A cellulose-containing reaction mixture was made up having the following composition: Cellulose : 12.2% W/w CaC12 : 43.9% W/w 1101 8.8% W/w Water : 35.1% W/w The CaC12 was added as a mixture of CaC12 . 6 0 and anhydrous CaC12 but the percentage quoted above is for anhydrous CaC12. Using the conditions of Examples 1 and 2 the reaction was carried out for 2 hours at 60 0C. After this time the product mixture was evaluated and found to have the following composition: % W/w of total Product component product composition glucose 60.6 disaccharides 15.5 triaccharides & higher oligomers 2.55 other saccharides (unidentified) 4.3 hydroxymethylfurfural 0.55 % W/w of total Product component product composition humans, as block residue 14.6 ether soluble products 1.9 Thus using these conditions (high CaC12 and low HCl concentrations) a relatively large concentration of by-products is produced. For instance humins and hydroxymethylfurfural together total 15.15% W/w of the product0

Claims: 1. A process for the solubilisation and/or hydrolysis of a cellulose-containing material in which the material is contacted with hydrogen chloride, water and calcium chloride to form a reaction mixture comprising 30 to 60%o water, 18 to 45% hydrogen chloride, 3 to 35% calcium chloride and 1 to 30% cellulose-containing material (all percentages being by weight based upon the total weight of the reaction mixture), the reaction mixture is maintained in a closed system under a pree- sure in the range 3 to 50 atmospheres absolute for a period of time in the range 2 minutes to 12 hours, a sugar-conta7nnng product is removed from the closed system and from this product hydrogen chloride and calcium containing materials are separated and recovered. 2. A process according to claim 1 wherein the sugarcontaining product comprises glucose. 3. A process according to claim 1 or claim 2 wherein the reaction mixture comprises 35% to 55% water. 4. A process according to any one of the preceding claims wherein the reaction mixture comprises 20% to 35% of hydrogen chloride. 5. A process according to any one of the preceding claims wherein the reaction mixture comprises 5% to 25% calcium chloride. 6. A process according to any one of the preceding claims wherein the reaction mixture comprises 5% to 2046 cellulose-con tanning material. 7. A process according to any one of the preceding claims wherein before the formation of the reaction mixture the cellulosecontaining material is treated with an acid at a concentration not greater than 2% W/w for a period within the range 10 to 60 minutes and at a temperature within the range 200 to 1200C. 8. A process according to any one of the preceding claims wherein an additional amount of water within the range 5% to 25% by weight based upon the total weight of the reaction mixture when the addition is made is added to the reaction mixture after solubilisation of the cellulose-containing material has occurred. 9. A process according to any one of the preceding claims wherein the reaction mixture is maintained in the closed system at a temperature within the range 200 to 1200C. 10. A process according to any one of the preceding claims wherein hydrogen chloride and calcium containing materials are separated from the sugar-containing product by electrodialysis.

Inventors: BARKER, SIDNEY ALAN, BEARDSMORE, ANDREW JOHN, RODGERS, BRIAN LEWIS FREDERICK, SOMERS, PETER JOHN
Applicants: IMPERIAL CHEMICAL INDUSTRIES PLC
Application year: 1983
Main classification: C13K1
IPC codes: C13K1