A METHOD OF PREPARING A PUZZOLANIC MATERIAL FORM PAPER RESIDUE AND A METHOD FOR THE MANUFACTURE OF CEMENT FROM SAID MATERIAL

Abstract: The invention relates to a method for the incineration under precisely defined conditions, of kaolin-containing material such as waste paper and other residues stemming from recycling of waste paper for reuse in the paper industry, yielding a material of puzzolanic properties. To this end the incineration takes place in a fludized bed at a temperature of preferably 780 DEG C wherein the same or a lower temperature prevails in the freeboard. Due to its hydraulic properties the puzzolanic material is suitable for the manufacture of concrete of a high compression strength. The invention also relates to a cement containing the puzzolanic material manufactured by the method of the invention.

Description: A method of preparing a puzzolanic material from paper residue and a method for the manufacture of cement from said material The present invention relates to a method for the thermal conversion of kaolin-containing material to a material of puzzolanic properties, wherein the kaolin-containing material is thermally treated in a fluidized bed installation having a freeboard in the presence of oxygenous gas. Such a method is known from DE OS 38 38 379. Paper residue is incinerated in a fluidized bed at a temperature above 400°C, preferably at 800-1000°C. The resulting sludge paper ash is used in the manufacture of sandlime brick. The sludge paper ash obtained at 800-1000°C is added in an amount of 0.5-2% to mortar of lime and sand. Sandlime brick manufac¬ tured with such mortar no longer expands or shrinks under the influence of moisture. It is the object of the present invention to improve the method according to the preamble and in particular to pro¬ vide a method for the thermal conversion of kaolin-containing material to a material of improved puzzolanic and hydraulic properties. To this end the method according to the invention is characterized in that the fluidized bed is operated at a tem¬ perature between 720 and 850°C and the temperature of the freeboard is 850°C or below, and that the fluidized bed is provided with means to promote heat transfer. By accurately controlling the temperature in the fluidized bed and the freeboard a puzzolanic material is obtained containing metakaolinite and calcium oxide converted into calcium hydroxide. Careful control of the process condi¬ tions avoids that the produced metakaolinite is converted into a material of poorer puzzolanic properties. Further, the puzzolanic material obtained only contains a limited amount of calcium oxide, which oxide - in contrast with the hydroxide - has adverse effects on the strength of the concrete and hardened cement manufactured with puzzolanic material. Due to the presence of water that is released during incineration, that is present in the starting material and that optionally is added, it is possible to obtain in one single plant - the fluidized bed installation - a puzzolanic material which is suitable as cement or one of its components. In this way the method according to the invention saves on a further instal¬ lation for the conversion of calcium oxide into calcium hydro- xide, which, from an economic point of view, is favourable. The kaolin-containing material used is preferably waste paper or residues that stem from recycling of waste paper for reuse in the paper industry. Said residues, which may serve as starting material in the method according to the invention, may be inferior paper residue, that is to say paper residue having on average too short a fibre length or sludge from waste water purifica¬ tion plants of the paper industry using waste paper as basic material. In this way a residue is utilized for the manufac- ture of a high-grade puzzolanic material. According to a preferred embodiment the method according to the invention is characterized in that the temperature of the fluidized bed is 780°C. Concrete manufactured with puzzolanic material anu- factured at this temperature is shown to possess the greatest compression strength. The present invention also relates to a method for the manufacture of cement, characterized in that puzzolanic material manufactured according to the invention is added to the usual starting material, or part of the usual starting materials for cement is replaced by the puzzolanic material. Because of the good hydraulic properties of the puzzolanic material manufactured by the method according to the invention, this cement may be used for the manufacture of concrete having at least an equivalent compression strength. The term "cement" as used in the present invention should be interpreted in the broadest sense and comprises dry and wet cement products which may or may not contain gravel, etc. The invention will now be further elucidated by means of the following embodiment example, wherein reference is made to Figures la, b and c representing graphs of the temperature profile in a fluidized bed installation. Paper residue derived from the preparation of start- ing material based on waste paper from the paper industry is, according to the invention, incinerated in a fluidized bed installation at a temperature of preferably 750 to 800°C and in particular 780°C, wherein the temperature in the freeboard is lower than or the same as that in the fluidized bed, yield- ing a puzzolanic material. The puzzolanic material of the pre¬ sent invention is understood to be a material possessing hydraulic and/or the hydraulic properties of other material strengthening properties. The incorporated paper residue has a water content of 25 to 75% by weight in relation to the total. All the kaolin is converted to metakaolin. Table A illustrates the compression strength of concrete manufactured with puzzo¬ lanic material prepared at different temperatures. This shows that an optimal puzzolanic material is obtained at a tempera¬ ture of 780°C. Table A Fluidized bed temperature Compression strength °C MPa 720 3.66 ± 0.15 760 3.84 ± 0.09 780 4.24 ± 0.17 800 4.23 ± 0.09 850 2.81 ± 0.09 Preparation: Mix 1 part puzzolanic material, 1 part calcium hydroxide, 5.4 parts standard sand and 2 parts water according to EN 196. Mixing time 3 min. Mixtures densified according to EN 196. Compression strength measured after hardening for 28 days. The compression strengths at 780 and 800°C are com¬ parable. As at 780°C the compression strength's sensitivity to change in temperature decreases, preference goes to 780°C. In addition, the products manufactured using puzzolanic material according to the invention show good green strength. An agent promoting heat transfer, such as sand, is introduced into the fluidized bed. It happens quite often that in fluidized bed installations the heat transfer agent is blown out, ending up in the product. With the above-mentioned temperature there is, surprisingly, an increase in the heat transfer promoting agent stemming from material derived from the kaolin-containing material which, with respect to its com- position, shows resemblance to the puzzolanic material accord- ing to the invention. This makes it possible to operate the fluidized bed with the aid of own-production heat transfer promoting agent. This not only takes away the necessity to purchase heat transfer promoting agent to replenish agent that was discharged and mixed with the product, but the product remains free from pollution by a different heat transfer pro¬ moting agent. With a view to utilization in cement and/or concrete compositions a fine and restricted grain-size distribution of the product is desirable. The grains resulting from the method according to the invention have a diameter smaller than 250 μm, wherein 90% is smaller than 64 μm. This material is carried along with the waste gasses and is, according to an advantageous embodiment, separated into a coarse and a fine fraction. The coarse fraction is, mixed into the paper resi¬ due, fed back into the fluidized bed installation where it is reduced in size. The heat distribution in the fluidized bed installa¬ tion can be further improved by using a compaction feeder, such as a screw conveyor with a constricted opening discharg¬ ing into the fluidized bed installation, so that the paper residue disintegrates less easily and there is less spark for¬ mation. This improves combustion performance and consequently the homogeneity of the heat distribution. Fig. la shows the temperature distribution in a fluidized bed installation during the thermal processing of paper residue. One can see that with the applied degree of cooling of the freeboard the temperature there rises to 900°C, resulting in a material possessing less satisfactory puzzolanic properties (Table B) . In Fig. lb the insulation sheath around the freeboard has been removed and the tempera¬ ture in the freeboard is maintained at below the fluidized bed temperature of 780°C. Table B shows that this results on the one hand in a puzzolanic material with which a product of good compression strength can be manufactured, but on the other hand that the consequential CO and C V H, emission is relatively high and the energy losses are economically rather unfavour¬ able. In Fig. lc the same fluidized bed installation is used as in Fig. la, i.e. with insulation of the freeboard, in com- bination with a compaction screw for the conveyance of the paper residue. Because of the improved combustion performance a homogenous temperature distribution can be achieved which, as can be seen in Table B, is coupled with very low emission values. Table B Emission Compression (mg/N ' at 11% 0 > in waste gas) strength MPa CO CH, non-compacted feed; NA NA 3.27±0.05 insulation non-compacted feed; 238 100 4.31±0.04 no insulation compacted feed; 190 <10 4.24±0.17 insulation Screw used: extrusion screw having a diameter at the end facing the fluidized bed installation 50% of the diameter of the end facing away from the fluidized bed installation. Preparation as in Table A. NA = not available. Calcium oxide has adverse effects on the compression strength of concrete containing it. This is because in the course of time calcium oxide takes up carbon dioxide, forming calcium carbonate. This results in an increase in volume which weakens the concrete. The conversion of calcium oxide into calcium hydroxide as well as mixing calcium hydroxide with metakaolinite is known in the manufacture of cement. In the method according to the invention the freeboard of the fluidized bed is used for the conversion of calcium oxide into calcium hydroxide. Because only a short time is passed in the fluidized bed and in the freeboard - in the order of seconds to several minutes - the undesirable reaction of metakaolinite with calcium hydroxide and water is limited. The calcium oxide content in the product can also be reduced by suppressing the conversion of calcium carbonate. In this case a product of mainly puzzolanic properties is obtained. Suppression of cal¬ cium carbonate conversion can be achieved by applying methods which influence the chemical balance between calcium carbonate and calcium oxide plus carbon dioxide. An example of this method is raising the carbon dioxide concentration, for instance by choosing the right fuel (e.g. during the combus¬ tion of coal more carbon dioxide per energy unit is produced than during the combustion of natural gas) . The freeboard of the fluidized bed is maintained at a temperature below 850°C, preferably below 800°C. This prevents the metakaolinite formed during incineration from being con¬ verted into a product of poorer puzzolanic properties, as illustrated in Fig. la, b and Table B. In order to allow the calcium oxide which is formed during combustion, to bind water to form calcium hydroxide, the freeboard - or alternatively a successive calcium oxide conversion chamber - is maintained at a temperature of 500°C or lower, in particular at 150-350°C. The temperature is achieved by cooling the freeboard respectively the calcium oxide conversion chamber, whereby the absorbed heat can be used for drying kaolin-containing material that is to be inci¬ nerated. This can be achieved by introducing water into said spaces. To obtain a good conversion, wherein undesirable reac¬ tions resulting in products of poorer puzzolanic properties are limited, the water vapour concentration in the freeboard respectively the alternative calcium oxide conversion chamber is maintained preferably at 30-50% by volume. In this manner, in a simple fluidized bed installation, a material is formed of good puzzolanic and hydraulic properties. Concrete manufactured from Portland cement, to which the puzzolanic material produced by using the method according to the invention was added, is stronger than without this addition (Table C) . Table C Portland cement puzzolanic material Compression strength % % (MPa) 100 0 39 ± 0.5 90 10 44.7 ± 1.6 Method of preparation: Mix 1 part Portland cement + puzzolanic material with 3 parts standard sand and 0.5 parts water (according to EN 196) . Compression strength measured after hardening for 14 days. The water required for the conversion of calcium oxide stems from the incineration of the starting material, and may include fuels used for additional heating of the fluidized bed, or from water present in the starting material and, if necessary, from water added to the fluidized bed or preferably the freeboard. The water fed to the freeboard of alternatively to the successive calcium oxide conversion cham¬ ber is preferably abstracted from the residues to be inciner¬ ated. The composition of the puzzolanic material manufac¬ tured by the method according to the invention comprises 40% metakaolinite, 50% calcium hydroxide, calcium carbonate and calcium oxide, whereby the calcium oxide is present in such small amounts that it has a negligible effect on the compres- sion strength of concrete containing it, and furthermore metals, chlorides and sulphates in concentrations which have no adverse effect on the strength and applicability of the products manufactured by using the puzzolanic material. It goes without saying that the exact composition also depends on the starting material used. It is known that the temperature in the freeboard favourably affects the limitation of dioxin emissions. How¬ ever, it is surprising to find that the combination of, on the one hand an incineration temperature between 750 and 800°C and in particular 780°C and the consequential through put and on the other hand the lowered temperature of the freeboard to below the fluidized bed temperature, should result in dioxin emissions of a degree that even without any further equipment for the removal of dioxins, the strict Dutch environmental standards are met (Table D) . This aspect also contributes to the economy of the method according to the invention. Table D | ι ..h., ι ul units of dioxin °C °C ngT l /m' 850 850 0.35 780 770-780 0.034 (Dutch standard: 0.1 ng T^/m t ) By using the method according to the invention resi¬ dues, which otherwise would have to be disposed of at high costs, can be utilized in the manufacture of a high-grade material of puzzolanic properties.

Claims: CLAIMS 1. A method for the thermal conversion of kaolin-con- taining material to a material of puzzolanic properties, wherein the kaolin-containing material is thermally treated in a fluidized bed installation having a freeboard in the pres¬ ence of oxygenous gas, characterized in that the fluidized bed is operated at a temperature between 720 and 850°C and the temperature of the freeboard is 850°C or lower, and that the fluidized bed is provided with means for promoting heat transfer. 2. A method according to claim 1, characterized in that the kaolin-containing material used is waste paper or residues that stem from recycling waste paper for reuse in the paper industry. 3. A method according to claim 1 or 2 , characterized in that the temperature in the fluidized bed is 750-800°C. 4. A method according to claim 3, characterized in that the temperature in the fluidized bed is 780°C. 5. A method according to one of the preceding claims, characterized in that the temperature in the freeboard is maintained at the same level as or lower than the temperature in the fluidized bed. 6. A method according to claim 5, characterized in that the temperature in the freeboard or successive calcium oxide conversion chamber is maintained at 500°C or lower. 7. A method according to claim 6, characterized in that the temperature in the freeboard or the successive cal- cium oxide conversion chamber is maintained at 150-350°C. 8. A method according to one of the preceding claims, characterized in that the freeboard or the successive calcium oxide conversion chamber is cooled and the absorbed heat is utilized for drying kaolin-containing material that is to be thermally treated. 9. A method according to one of the preceding claims, characterized in that the water vapour concentration in the freeboard or the successive calcium oxide conversion chamber is maintained at 30-50% by volume. 10. A method according to one of the preceding claims, characterized in that water is fed to the freeboard or a successive calcium oxide conversion chamber. 11. A method according to claim 10, characterized in that the water fed to the freeboard is abstracted from kaolin- containing material that is to be incinerated. 12. A method according to one of the preceding claims, characterized in that incineration takes place in the presence of material formed from kaolin-containing material, as means to promote the heat transmission. 13. A method for the manufacture of cement, charac¬ terized in that puzzolanic material manufactured according to any one of the claims 1 to 12 is added to the usual starting materials for cement, or that part of the usual starting materials for cement is replaced by the puzzolanic material. 14. A method according to one of the preceding claims, characterized in that the kaolin-containing material is fed to the fluidized bed installation in compacted form. 15. A method according to one of the preceding claims, characterized in that the puzzolanic material is sep¬ arated into a coarse and a fine fraction and that the coarse fraction mixed with the kaolin-containing material is fed back into the fluidized bed installation.

Inventors: BIERMANN JOSEPH JAN PETER, BLEIJERVELD ROBERT, HULSCHER HENDRIK JACOBUS, VOOGT NICOLAAS, BIERMANN, JOSEPH, JAN, PETER, BLEIJERVELD, ROBERT, HULSCHER, HENDRIK, JACOBUS, VOOGT, NICOLAAS
Applicants: BIERMANN JOSEPH JAN PETER, BLEIJERVELD ROBERT, BRP DE BILT BV, CDEM HOLLAND BV, HULSCHER HENDRIK JACOBUS, VOOGT NICOLAAS, BIERMANN, JOSEPH, JAN, PETER, BLEIJERVELD, ROBERT, BRP DE BILT B.V., CDEM HOLLAND B.V., HULSCHER, HENDRIK, JACOBUS, VOOGT, NICOLAAS
Application year: 1995
Main classification: C04B18
IPC codes: B01J6, B01J8, C04B2, C04B7, C04B14, C04B18, C04B28