FR2927983A1 - Treating filth or waste, comprises subjecting filth or waste to compression to separate into a putrescible fraction and a dry fraction, and subjecting the putrescible fraction to an anaerobic digestion to produce biogas - Google Patents

Abstract

The filth or waste (13) treating process comprises subjecting filth or waste to compression to separate (14) into a putrescible fraction in the form of pulp (15) having relative humidity of greater than 50% and into a dry fraction having relative humidity of less than 20%, and subjecting the putrescible fraction to an anaerobic digestion to produce biogas. A part of the dry fraction is converted by an endothermic gasification treatment to produce synthesis gas. The synthesis gas comprises a fuel gas able to be burned by exothermic oxidation. The filth or waste (13) treating process comprises subjecting filth or waste to compression to separate (14) into a putrescible fraction in the form of pulp (15) having relative humidity of greater than 50% and into a dry fraction having relative humidity of less than 20%, and subjecting the putrescible fraction to an anaerobic digestion to produce biogas. A part of the dry fraction is converted by an endothermic gasification treatment to produce synthesis gas. The synthesis gas comprises a fuel gas able to be burned by exothermic oxidation. The endothermic gasification treatment is carried out in a gasification reactor at 700-900[deg] C using many reagents comprising a part of dry fraction (10%) and water vapor. The heat energy for the endothermic gasification treatment is provided outside the reactor by a combustion of biogas and the dry fraction with a quantity of oxidizing comburant gas (6000 m 3>per tonne) in the gasification reactor. The comburant gas is heated by heat exchange between a portion of synthesis gas produced by the endothermic gasification treatment and the comburant gas. The separation into the putrescible fraction and the dry fraction is carried out at a pressure of 720-750 bars in a compression chamber having extrusion orifices through which the putrescible fraction flows. A gas composition including recycling gas is prepared and stored in the reactor. The gas includes a quantity of synthesis gas and a quantity of biogas and natural gas.

Description

PROCESS FOR TOTAL GASIFICATION OF GARBAGE OR WASTE

The invention relates to a method of treating garbage or waste for their optimal recovery.

Garbage or waste, such as household waste, agricultural waste (manure, plants), food, represent an important source of energy that it is desirable to be able to exploit optimally. Until now, garbage or waste has essentially raised the problem of their elimination or inerting. Part of the energy contained in the garbage or waste is eventually recovered during these operations. Nevertheless, the treatments applied until now on this garbage or waste have not really been optimized for the recovery of the energy they contain. Direct incineration of raw waste produces complex and harmful fumes, requiring treatment of fumes, and residues of purification of these fumes. The strong presence of moisture in garbage or waste significantly affects its performance, and the proportion of ash produced is large, typically 30 to 32%. This previously widespread solution requires heavy equipment, is expensive and does not allow optimal energy recovery of waste.

To overcome these drawbacks, it is now preferred to previously separate the materials capable of undergoing anaerobic fermentation and thereby produce, by methanization, biogas. These materials include on the one hand putrescible materials of animal or vegetable origin, and, on the other hand, cellulosic materials (paper, cardboard, ...). However, the separation steps of these materials are complex and expensive, and, moreover, that the internal energy of other materials from garbage or raw waste, for example non-recyclable polymeric synthetic materials, is not valued. EP 0563173 describes a waste or waste treatment process in which, after extraction of the inert materials (materials neither fuels nor putrescible, such as glasses, metals ...), it compresses the garbage or non-inert waste until at a final pressure higher than 800 bar (800 105Pa), which makes it possible to separate a wet fraction and a combustible fraction. The wet fraction essentially made up of biomass can be treated by known methods, for example by appropriate biological seeding, in order to produce either composts by aerobic fermentation or gases by anaerobic fermentation (biogas anaerobic digestion) susceptible to provide heat energy, the anaerobic digestate of fermentation being itself compostable. The solid fuel fraction of low relative humidity (less than 20%) can either be directly and immediately incinerated in a furnace, or stored outside, then be reclaimed and incinerated during periods to meet a delayed energy demand. Nevertheless, this combustible fraction which is still considered as a waste remains subject to waste treatment regulations. In particular, its incineration involves the use of a regulatory furnace, a flue gas treatment device, and a solution for inerting the purification residues of these fumes. As a result, it involves very expensive investments. Furthermore, devices and methods for gasifying solid wastes have recently been proposed. WO 2007/037768 describes a particularly complex process that is supposed to be able to produce combustible gases from various wastes. One of the steps of the process consists of gasification of non-inert solid waste previously dried, crushed and packed into granules. This method is not usable in the case of waste containing a significant proportion of biomass, and in any case is extremely complex and non-competitive, the cost of treatment being greater than the gains that can be obtained by the valuation. Also, US 2007/0181047 discloses a solid waste treatment method of drying the waste and then gasifying it to produce a combustible gas. However, again, the process is not applicable to waste containing a high proportion of biomass and is in any case uncompetitive taking into account the steps of drying, grinding and filtering to be performed before the gasification. In this context, the invention aims to provide a method of treating garbage or waste which, on the one hand, applies to all kinds of garbage and waste, including high biomass content, and, d On the other hand, it is possible to produce, under economically competitive conditions on an industrial scale, materials which are no longer waste and a minimum quantity of inert final residues. More particularly, the invention aims to provide such a method that allows to significantly increase the amount of energy that can be recovered per unit mass of garbage or waste. In the rest of the text, the units of gaseous volume (m) are the normalized units, that is to say representing the volume occupied by a gas or gas mixture at a temperature of 0 ° C. and under a pressure of 1 bar ( 105Pa). In the rest of the text, the term "endothermic gasification" denotes a chemical reaction, of which at least one of the products is a gas and whose overall energy balance shows an absorption of energy, this energy being in particular provided in the form of heat. Exothermic combustion or oxidation means a chemical reaction whose energy balance is positive, the energy produced being dissipated in the form of a heat emission.

To this end, the invention relates to a waste or waste treatment method in which: at least one compression step is subjected to waste or waste under conditions suitable for separating them into a fraction, called a putrescible fraction, under a pulp of relative humidity greater than 50%, and in a fraction, referred to as the dry fraction, of relative humidity of less than 20%, and then the putrescible fraction is subjected to an anaerobic fermentation treatment producing a biogas, characterized in that at least a portion of said dry fraction is converted by an endothermic gasification treatment.

The inventor has indeed noted with surprise on the one hand that the wet fraction extracted by compression of garbage or waste (after possible extraction of inert materials), as described for example by EP 0563173, is made of putrescible materials, original fast-fermenting animal or plant and, on the other hand, that the dry fraction, which is formed of cellulose-based materials (paper, cardboard, ...) and polymeric synthetic materials (possibly including composite materials) , can be subjected to a simple endothermic gasification treatment, of good yield and producing a synthetic gas (essentially a mixture of carbon monoxide, hydrogen, nitrogen and carbon dioxide) which can then be directly valorized by combustion, possibly mixed with natural gas and / or with the biogas resulting from the methanisation of the putrescible fraction. In addition, the inventor has found that the dry fraction, as produced at the outlet of the press in the form of blocks of compact sheets has a density substantially of the order of 0.85 and is nonflammable compact mass. However, the inventor has also observed that said dry fraction is easily breakable, after simple disintegration, dry matter having a pulverulent character, therefore very reactive to combustion and gasification. The endothermic gasification of such a pulverulent dry matter avoids the occurrence of preferential passages for the gases in the dry matter and allows a homogeneous treatment of all of said dry matter. Moreover, the inventor has found that the dry fraction obtained after preliminary sorting followed by compression typically comprises substantially 93% endothermic pyrolysis gasifiable material, 3% of inert material neither combustible nor gasifiable nor fermentable and only 4% of putrescible organic matter. In particular, the inventor has found that the simple endothermic gasification treatment of a quantity of dry fraction, obtained by compression of garbage or waste (after possible extraction of inert materials). formed of cellulose-based materials and polymeric synthetic materials produces a small amount of ultimate residues that remain waste. The mass proportion of ultimate residues obtained after endothermic gasification of a quantity of dry fraction is less than 20% of the mass of the starting dry fraction, in particular less than 10%, especially substantially close to 5%. Consequently, the process according to the invention makes it possible to transform garbage or waste entirely into gas (which is not waste), compost, and inert material (glasses, metals and other recyclables, final waste in small quantities). In a process according to the invention, the non-inert materials are converted into gas, in particular fuel gas, of high energy value with excellent production efficiency and low cost, which makes it possible to achieve an overall recovery rate of the waste. greater than 90%. In addition, it should be noted that the cost of producing an endothermic gasification and synthesis gas combustion installation obtained is much lower than that of a combustion and flue gas treatment plant. In addition, in a process according to the invention, all putrescible materials are transformed into energy-efficient biogas and compost with an organic matter content of greater than 30%, said compost being adapted to serve as a fertilizer in agriculture.

Advantageously and according to the invention, the endothermic gasification treatment is carried out so as to produce a gaseous composition, called synthetic gas, comprising at least one combustible gas, capable of being burned by exothermic oxidation. In particular, the endothermic gasification process according to the invention allows the production of a quantity of synthesis gas of which at least a proportion is oxidizable and which is capable of supplying energy during their subsequent oxidative combustion. The endothermic gasification process of the dry fraction according to the invention is thus different from combustion incineration processes which produce fully oxidized gases, and which are not energetically recoverable. Advantageously and according to the invention, the endothermic gasification treatment is carried out in a reactor, called a gasification reactor, so as to produce a synthesis gas comprising at least one fuel gas chosen from the group consisting of dihydrogen (H2) and monoxide. of carbon (CO). The endothermic gasification of said dry fraction is carried out and a synthesis gas composed essentially of dihydrogen (H2) and carbon monoxide (CO), which are oxidizable and recoverable combustible gases and to a lesser extent nitrogen, is produced. (N2) and carbon dioxide (CO2). It is possible that an endothermic gasification treatment produces nitrogen (N2) and carbon dioxide (CO2) but the total proportion of these two gases in the synthesis gas mixture will not exceed a molar proportion of 15. %, typically of the order of 10%. It is also possible that an endothermic gasification treatment according to the invention, for example in a reducing medium, produces a quantity of synthesis gas containing methane (CH4), which is a gas of particular interest because of its number of oxidation (-4) weak. Advantageously and according to the invention, a quantity of energy for the endothermic gasification treatment is provided in the form of heat energy. The inventor has observed that the increase in the temperature of the dry fraction composed of cellulose-based materials and synthetic materials allows the production of synthesis gas, said synthesis gas being devoid of toxic agents contained in the waste or garbage . Advantageously and according to the invention, the endothermic gasification treatment is carried out from a plurality of reagents comprising at least said portion of dry fraction and water vapor. In particular, the dry fraction obtained by compression has a relative humidity of less than 20%. release of the press. When storing the dry fraction for a delayed endothermic gasification treatment, the relative humidity of the dry fraction can: increase and stabilize, for example, to a value between 26% and 28%. According to a particular variant of a process according to the invention, the endothermic gasification treatment is carried out without adding additional water. However, in another variant, the amount of water necessary for the optimal completion of the endothermic gasification is adapted by adding an additional quantity of water if necessary according to the particular chemical composition of the dry fraction. In a particular embodiment of a process according to the invention, the quantity of water required for carrying out the endothermic gasification is provided in the form of water vapor, by adding this water vapor in the endothermic gasification reactor during endothermic gasification.

Furthermore, the endothermic gasification treatment can be carried out in any case known per se. For example, the endothermic gasification treatment is carried out at atmospheric pressure by disposing, in a shaft furnace, also called a gasifier, a layer of dry fraction derived from waste through which an oxidizing gas is blown in the presence of a amount of water vapor.

It is also possible to use a reactor, called fixed bed, co-current or counter-current, pressurized or not, or other. Advantageously and according to the invention, the endothermic gasification treatment is carried out at a temperature of between 700 ° C. and 900 ° C. Preferably, the endothermic gasification treatment is carried out at a temperature of between 800 ° C. and 850 ° C. In particular, this endothermic gasification temperature is sufficient to effect the endothermic gasification of at least a portion of the dry fraction of relative humidity of less than 20%. Advantageously and according to the invention, at least a portion of the amount of heat energy for the endothermic gasification treatment is provided by a combustion of at least a portion, said part to be burned, of the dry fraction with a quantity of gas oxidizing oxidant, said combustion being carried out in the gasification reactor. Oxidative combustion of a portion of the dry fraction is carried out with an amount of oxidizing oxidant gas to produce the energy necessary to increase and maintain the temperature for the endothermic gasification reaction to occur. In a first possible embodiment according to the invention, the endothermic gasification treatment and the combustion of said part to be burned are carried out simultaneously in a single gasification reactor.

Thus the energy produced by combustion of said portion to be burned allows the rise of the temperature of the dry fraction which decomposes, in the presence of water vapor, into synthesis gas. The inventor has found that the combustion of said part to be burned leads to the production of non-combustible gases, in particular carbon dioxide, but also advantageously makes it possible to reach the endothermic gasification temperature which produces valuable combustible gases. The oxidizing gas is a gaseous composition comprising molecular oxygen. The oxidizing gas is in particular chosen from the group consisting of atmospheric air and pure molecular oxygen. The oxidizing gas is brought into contact with said part to be burned by means of devices known per se, making it possible to introduce an oxidizing gas composition into a combustion chamber, and also to control the quantity and the rate of delivery of the quantity of oxidizing gas. in contact with said part to be burned in order to maintain the optimal temperature of endothermic gasification and to optimize the production of synthetic gas that can be recovered and is liable to be burned by exothermic oxidation. Advantageously, in the first variant according to the invention, the endothermic gasification treatment is carried out with a mass proportion of said part to be burned between 5% and 25%, in particular of the order of 10%, of the dry fraction. The inventor has observed that the combustion in air of a small part, in particular a mass proportion of the order of 10%, of the dry fraction advantageously makes it possible to gasify the complementary fraction of 90% of said dry fraction, producing a quantity of synthetic gases that can be recovered and liable to be burned by exothermic oxidation, as well as a small quantity of ash and inert residues.

Advantageously, in the first variant according to the invention, the endothermic gasification treatment is carried out with a quantity of oxidizing oxidizing gas of the order of 6000 m3 per ton of said part to be burned. The inventor has also determined that the amount of oxidizing oxidizing gas necessary for the oxidative combustion of one ton of dry fraction resulting from the compression of refuse or waste according to the invention is 6000 m3, this volume of oxidizing gas thus allowing to gasify about 9 tonnes of dry fraction resulting from the compression of garbage or waste. Advantageously, in the first variant according to the invention, the endothermic gasification treatment is carried out from a quantity of oxidant gas previously heated and then introduced into the gasification reactor by increasing the production efficiency of synthesis gas. Advantageously and according to the invention, said amount of oxidizing gas is heated by heat exchange between at least a portion of the synthesis gas produced by the endothermic gasification treatment and said amount of oxidizing gas. In particular, advantageously and according to the invention, a heat exchange is carried out between a quantity of a hot synthesis gas produced by the endothermic gasification treatment and said amount of oxidizing gas prior to its introduction into the gasification reactor. This results in a heating of the amount of oxidant gas but also, advantageously, a cooling of the synthesis gas produced. In a second embodiment according to the invention, which can be combined with the first variant mentioned above, at least a portion of the amount of heat energy required for the endothermic gasification treatment is produced outside the gasification reactor, said gasification reactor then being able to be hermetically closed, especially with respect to atmospheric gases. According to an embodiment of this second variant, the endothermic gasification treatment is carried out in a closed gasification reactor whose endothermic gasification furnace is heated to a temperature of between 700 ° C. and 900 ° C. with heating means. outside the gasification reactor. External reactor heating means known per se are used, making it possible to avoid producing, in the furnace of the endothermic gasification reactor, a quantity of non-combustible gas, in particular a molar proportion of non-combustible gas greater than 10%. . Advantageously, in the second variant of the invention, the endothermic gasification treatment is carried out in a gas-tight endothermic gasification plant, maintained under a pressure greater than atmospheric pressure, or on the contrary in an installation maintained under a vacuum of such In this way, endothermic gasification gas does not escape from the gasification plant and atmospheric gases do not enter the gasification plant. The endothermic gasification treatment can also advantageously be carried out in so-called rotating grid installations, in which the ashes and inert gasification residues are evacuated automatically. According to another embodiment of implementation of the second variant of the invention, the endothermic gasification treatment is carried out in a closed gasification reactor whose endothermic gasification furnace is heated to a temperature of between 1200.degree. 1300 ° C with heating means external to the gasification reactor to produce biofuels. Advantageously, in the second variant of the invention, at least a part of the amount of heat energy for the endothermic gasification treatment is produced by a combustion, outside the gasification reactor, of at least a part, said portion to be burned, of the dry fraction with a quantity of oxidizing oxidizing gas. In particular, the quantity of heat required for the endothermic gasification treatment is produced by means of the combustion of a portion of the dry fraction, with a relative humidity of less than 20%, which is consequently combustible, outside the reactor of gasification, and said amount of heat is transmitted to said endothermic gasification reactor. Thus the gasification reactor 2927983 is separated from the home in which the combustion of said portion to be burned, and can not contain non-combustible gas from the combustion of said portion to burn the combustible dry fraction. Thus, in order to effect the gasification of a major part of the dry fraction, the gasification reactor 5 is heated by separate combustion of a small portion of the dry fraction. Advantageously, in either of the two above-mentioned variants of the invention, at least a portion of the amount of heat energy for the endothermic gasification treatment is produced by combustion of a portion of the syngas produced by endothermic gasification. Thus, a quantity of synthesis gas produced by an endothermic gasification treatment is advantageously used as a fuel, possibly after storage, as a heat energy source for a subsequent endothermic gasification treatment. Furthermore, advantageously and according to the invention, at least a portion of the amount of heat energy required for the endothermic gasification treatment is produced by combustion, inside and / or outside the endothermic gasification reactor. part of the biogas produced by anaerobic fermentation of the putrescible fraction. In particular, at least a portion of the amount of thermal energy required for the endothermic gasification treatment is produced by a combustion of a gaseous composition comprising an amount of biogas produced by anaerobic fermentation of the putrescible fraction and a quantity of gaseous gas. synthesis produced by endothermic gasification of a portion of dry fraction. The different variants mentioned above for producing the endothermic gasification energy can be combined. The endothermic gasification reactor is, furthermore, adapted to allow the collection of the synthesis gases produced during the endothermic gasification treatment of the dry fraction resulting from the compression separation. In addition, the endothermic gasification reactor is equipped with devices known per se and for introducing the dry fraction into the endothermic gasification reactor, and known devices for extracting ashes and inert gasification residues. The daily endothermic gasification capacity of the hearth of an endothermic gasification reactor may vary according to the amounts of dry fraction to be gasified, with a capacity typically comprised between one hundred kilograms and ten hundred kilograms of dry fraction for applications in the field. scale, with a capacity of several hundred tonnes of dry fraction for industrial applications. Advantageously and according to the invention, prior to the separation by compression of the putrescible fraction and the dry fraction, a step is taken to extract inert materials neither putrescible nor combustible, so that the garbage or waste resulting from this separation are essentially formed of non-inert materials. In particular, the putrescible fraction subjected to methanation and the dry fraction subjected to endothermic gasification are substantially free of inert materials neither putrescible nor gasifiable.

Advantageously and according to the invention, for separating the putrescible fraction and the dry fraction, said garbage or waste is compressed to a pressure greater than 700 bar (700 105 Pa), in particular between 720 bar (720 105 Pa) and 750 bar (750 bar). 105Pa), in at least one compression chamber provided with extrusion orifices through which the putrescible fraction flows.

The inventor has also observed an acceleration of the anaerobic fermentation rate, leading to a considerable reduction in the time required for this fermentation, because of the penetration of the agents of the fermentation, facilitated by the destructuring of the animal and / or plant tissues. under the combined effect of high pressure applied to garbage or waste during compression and pressure variation during extrusion. Advantageously and according to the invention, the separation treatment is carried out at a site, called a separation site, distinct from a site, called a gasification site, on which the endothermic gasification treatment is carried out. In particular, a site for separation of waste by compression is chosen so as to minimize the distance separating it from the areas of production of household waste. Thus, it reduces the transport of fresh garbage freshly collected, avoiding nuisance likely to be generated by the transport of said garbage or raw waste to the site of separation of garbage or waste. In addition, an endothermic gasification site of the dry fraction is chosen so as to minimize the distance between the gas production sites (by endothermic gasification) and the energy conversion site of the gas produced by endothermic gasification. In particular, an anaerobic fermentation site of the putrescible fraction which is close to the site of separation of the waste by compression is chosen so as to reduce the time between the steps of production and controlled methanization of the putrescible fraction and avoiding the production of uncontrolled gas, outside a biogas enclosure. In addition, the bringing together of the production sites of the putrescible fraction and methanization of said putrescible fraction makes it possible in particular to avoid the transport, particularly by road, of this putrescible fraction, with rapid fermentation, and liable to generate nuisances for the environment during transport. Advantageously and according to the invention, the treatment is carried out by endothermic gasification of the dry fraction after a storage time. The dry fraction having a low content of putrescible material and a relative humidity of less than 20%, is particularly suitable for being transported and stored without nuisance. The stability of said dry fraction thus makes it possible to delay the production of gas over time. The postponement of the endothermic gasification treatment by means of the temporary storage of the dry fraction makes it possible to adapt the production of synthesis gas in order to meet energy needs, and in particular for synthesis gas. Advantageously and according to the invention, there is prepared a gas composition, called recycling gas, comprising a quantity of synthesis gas and an amount of at least one gas selected from the group consisting of said biogas and natural gas. The inventor has further observed that the gases constituting the synthesis gas produced by endothermic gasification of the dry fraction as well as the biogas produced by anaerobic fermentation of the putrescible fraction, obtained according to the invention from the waste or garbage, are not more legally considered as waste and can be used as a combustible raw material for the production of energy. Advantageously and according to the invention, the recycle gas is stored prior to combustion. The storage of the recycling gas obtained by a process according to the invention, said recycling gas being composed for part of biogas obtained by anaerobic fermentation (delayed or instantaneous) of the putrescible fraction resulting from the compression of the waste or garbage and for a other part of synthesis gas obtained by endothermic gasification treatment (delayed or instantaneous) of the dry fraction resulting from the compression of the waste or garbage, allows the use, itself instantaneous or deferred, of the recycling gas for energy needs in industrial sectors, in communities, for the production of electricity. Thus, prior to its combustion, the recycling gas is stored and if necessary, it is transported in containers or through a network of pipes. In a particular embodiment of the invention, the biogas and the synthesis gas are separately stored. In addition, at least one step of purification of biogas and synthesis gas is carried out.

Advantageously, at least 90%, typically 93% to 95%, of the waste or waste is converted into at least one fraction of combustible gas that can be burned by exothermic oxidation, into a residual compost of anaerobic digestion comprising from 40% to 50% organic matter, and in at least a fraction of inert materials neither putrescible nor combustible, but mostly recyclable (glasses, metals, etc ....). The invention also relates to a process characterized in combination by all or some of the characteristics mentioned above or below. Other objects, features and advantages of the invention will appear on reading the following description of its implementation examples given in a non-limiting manner, and which refers to the single appended figure which is a general schematic flowchart of a process according to the invention. The treatment method according to the invention is applied to a starting composition 10 which consists of household waste or waste. The starting composition 10 can be formed of any composition of raw waste containing both putrescible materials (biomass) and non-putrescible materials (including cellulose-based materials: paper, cardboard, ... and polymeric synthetic materials : thermoplastics, thermosets, resins, textiles ...).

In the case of household waste, the average composition resulting from an urban collection is typically the following (by weight): putrescible materials (biomass of animal or vegetable origin): 32%, combustible materials: 45%, namely: essentially cellulosic materials: 34% polymeric synthetic materials or composites: 11%, inert materials: 23%. In a first step 11, the inert materials are extracted (that is to say the materials neither putrescible nor combustible nor gasifiable such as metals, glasses ...). This extraction is carried out conventionally by mechanical sorting, automatic or manual and / or by magnetic sorting. This extraction step 11 produces on the one hand inert materials 12, and a composition 13 of garbage or waste resulting from this extraction, formed almost entirely of degradable (non-inert) materials, that is to say scalable. Typically, in a composition of household waste, the inert materials 12 extracted by mechanical and / or magnetic sorting represent of the order of 20% to 25% of the starting composition 10. The composition 13 of garbage or waste obtained after extraction of the inert materials is subjected to a high pressure compression separation treatment 14 in a press, until it undergoes a final pressure greater than 700 bar (700 × 105 Pa), typically of the order of 720 bar (720 × 10 5 Pa) at 750 bar (750 105Pa), which has the effect of separating: a pulp with a relative humidity of greater than 50% composed of putrescible biomass, expelled under the effect of the high pressure through extrusion orifices of at least one compression chamber of the press, a dry residue 16, with a relative humidity of less than 20%, very fragmented, composed of shreds of combustible dry matter, initially compact, but which separates, when manipulated, into pieces. very weak cohesion. This separation step 14 can be performed in a manner well known per se, for example as described by EP 0563173, or EP 1173325, or FR 2577167, or the like. The wet pulp 15 is the fraction of the composition 13 of garbage or waste that can flow through the extrusion orifices under the effect of the pressure applied to this composition 13. The moist pulp 15 of uniform brown color is in a more or less pasty state has in any case a high relative humidity, typically between 50% and 60%, and is a putrescible fraction that can be immediately shipped for a future treatment delocalized or treated on the spot in time required to take advantage of its relatively pure biomass quality; it is subjected to a biological anaerobic fermentation treatment 17 producing a biogas 18 comprising methane (typically of the order of 60%), carbon dioxide, carbon monoxide and various other gases in lesser amounts. The wet pulp 15 generated at the end of the separation step 14 has a very fast fermentation capacity due to the burst, subsequent to the extrusion, of the cells constituting the putrescible organic matter (of animal origin or vegetable). It also has a water retention capacity of the order of 2.5 times its mass of dry matter. As a result, the wet pulp 15 does not leak liquid. The biological anaerobic fermentation treatment 17 of the wet pulp 15 further generates a residual methanization compost, comprising from 40% to 50% organic material, substantially free of inert or plastic undesirable, particularly suitable for use as agricultural fertilizer. In particular, the agricultural fertilizer complies with the French NF U44-051 standard, fixing at 30% the minimum proportion of organic matter used in composts. The residual compost of anaerobic digestion is further enriched in mineral fertilizing materials which are not modified during the methanisation. For example, the putrescible fraction is subjected, immediately after the compression separation treatment, to an anaerobic fermentation treatment in a bioreactor as marketed by the company LINDE (Switzerland). In a period of 3 weeks, the anaerobic fermentation treatment of the putrescible fraction resulted in the average production of 149 m3 of biogas per ton of treated wet pulp. The gas produced by the anaerobic fermentation treatment of the putrescible fraction is predominantly (60%) methane. The dry fraction 16 is subjected to an endothermic gasification treatment 19 at a temperature between 700 ° C. and 900 ° C. to produce a synthetic gas comprising carbon monoxide (typically of the order of 45%), The calorific value of the synthetic gas thus produced is between 12500 kJ / m 3 and 19 000 kJ / m 3 (typically of the order of 50%) and in lower proportions of the nitrogen gas (N 2) and carbon dioxide. The dry fraction 16 contains at the same time mainly cellulosic materials (paper, cardboard, sanitary textiles, etc.) and polymeric synthetic materials (in this including composite materials) .This dry fraction can be subject to a endothermic gasification treatment, with good yields and good conditions, especially in view of its low humidity, the absence of biomass and its loose particulate form, at the end of this gasification treatment. In addition to synthesis gas 20, a small proportion of inert ash is recovered. The biogas 18 can be burned 21 and the synthetic gas can be burned 22, these combustions can be carried out in appropriate facilities to use these gases 18, 20 as fuels for example in boilers for heating or hot water production, steam or electricity production or other. As shown schematically in the figure, the biogas 18 and the synthetic gas 20 can be mixed in whole or in part with each other (mixing step 23) and / or with natural gas (mixing step 24) before being used as fuels in a combustion step 21 and / or 22. EXAMPLE 750 tons (750 105 Pa) of 8.5 tonnes of waste are treated per hour in a chamber pierced with multiple orifices, household waste (not not collected separately) collected in the region of Alès (France), after removal of inert materials, including glasses, metals and minerals. It can be seen that the waste thus treated separates into an extruded fraction, flowing through the die of the press, in the form of a putrescible organic pulp containing a mass proportion of 96 to 97% of putrescible material and a non-extruded fraction. , called dry fraction, retained inside the enclosure of the press and containing proportions by mass of 93% of pyrogasifiable materials (of which 68% of cellulosic materials, in particular papers, cardboard, sanitary textiles, and 25% of plastics ), 3% incombustible inert substances (glasses, metals, miscellaneous minerals and others that escaped initial sorting) and 4% putrescible organic matter.

The dry fraction is in the form of blocks of compact sheets, easily manipulated, and whose density is substantially close to 0.85 at the press outlet. It is observed that these blocks constituting the dry fraction, stored in the open air, are only superficially penetrated by rainwater and that these blocks of dry fraction emit, consequently, no water of percolation. It is further observed that these blocks constituting the dry fraction have, despite the presence of a reduced proportion of putrescible material (3%), no significant sign of fermentation. These blocks of combustible material are inert and present no risk of autoignition. They do not give off any odor.

In addition it has been observed that these blocks of dry matter are, in the form of compact masses, completely non-flammable and are therefore perfectly suitable for secure storage. However, they are easily breakable, by manipulation or by mislaying, to generate a dry fraction having a powdery character, in the form of plots of paper, cardboard, plastics. The relative humidity of the dry fraction varies from 20% at the immediate exit of the press and stabilizes at a value of between 26 and 28% after storage, by natural re-humidification by the humidity of the air. The elemental composition of the dry gasifiable fraction is as follows, as a percentage by mass of dry matter: carbon 53.5%, dihydrogen 7.7%, sulfur 0.5%, dioxygen 37.0%, dinitrogen 0.7% and chlorine 0.6%. A pilot endothermic gasification experiment is carried out on these dry materials resulting from the compression of household waste freed from inert materials. About 150 to 200 kg of dry matter obtained by compression separation are placed in a closed gasification reactor. The endothermic gasification temperature is maintained at between 800 ° C and 850 ° C. The relative share of the reactor load devoted to creating the conditions of the endothermic gasification is of the order of 10% of the dry matter to be treated. The air consumption is of the order of 0.6 m3 per kilogram of dry matter. The air used for the combustion of a portion of the dry fraction is heated prior to its introduction into the reactor by recovering the heat released by the gas produced by gasification. A quantity of gas of 0.83 kg is obtained from 1 kg of dry fraction, composed of gaseous dihydrogen (H2, 50%), carbon monoxide (45%), and to a lesser extent, nitrous oxide N2 and carbon dioxide. carbon dioxide. The product gas has a heating value substantially close to 15,000 kJ / m3. The invention can be the subject of numerous alternative embodiments, in particular as regards the processes and installations used to carry out the separation processes by compression 14, anaerobic fermentation 17, or endothermic gasification 19. These treatments are well known in themselves and can be chosen and optimized according to the compositions to be treated.

Claims (2)

1 / - Method of treatment of garbage or waste in which: one submits garbage or waste to at least one step (14) compression under conditions to separate them into a fraction, said putrescible fraction (15), in form of pulp of relative humidity greater than 50%, and in a fraction, referred to as the dry fraction (16), of relative humidity of less than 20%, and then the putrescible fraction (15) is subjected to a fermentation treatment (17). anaerobically producing a biogas (18), characterized in that at least a portion of said dry fraction (16) is converted by an endothermic gasification treatment (19). 2 / -Procédé according to claim 1, characterized in that the endothermic gasification treatment (19) is carried out so as to produce a gaseous composition, called synthesis gas, comprising at least one combustible gas capable of being burned by oxidation exothermic. 3 / -Procédé according to claim 2, characterized in that the endothermic gasification treatment (19) is carried out in a reactor, said gasification reactor, so as to produce a synthesis gas comprising at least one fuel gas selected in the group consisting of dihydrogen (H2) and carbon monoxide (CO). 4 / - Method according to one of claims 1 to 3, characterized in that a quantity of energy for the endothermic gasification treatment (19) is provided in the form of heat energy. 5 / - Method according to one of claims 1 to 4, characterized in that the endothermic gasification treatment (19) is made from a plurality of reagents comprising at least said portion of dry fraction (16) and of water vapor. 6 / - Method according to one of claims 1 to 5, characterized in that the endothermic gasification treatment (19) is carried out at a temperature between 700 ° C and 900 ° C.7 / - Method according to one of Claims 1 to 6, characterized in that at least a part of the amount of heat energy for the endothermic gasification treatment (19) is provided by a combustion of at least a part, so-called part to be burned, of the fraction dryer (16) with a quantity of oxidizing oxidant gas, said combustion being carried out in the gasification reactor. 8 / - Method according to claim 7, characterized in that the endothermic gasification treatment (19) is carried out with a mass proportion of said part to be burned between 5% and 25%, in particular substantially close to 10%, of the fraction dry (16). 9 / -Procédé according to one of claims 7 or 8, characterized in that the endothermic gasification treatment (19) is carried out with a quantity of oxidizing oxidizing gas of the order of 6000 m3 per ton of said part to be burned. 10 / - Method according to one of claims 7 to 9, characterized in that the endothermic gasification treatment (19) is made from the amount of oxidizing gas previously heated and then introduced into the gasification reactor. 11 / - A method according to claim 10, characterized in that the amount of oxidizing gas is heated by heat exchange between at least a portion of the synthesis gas produced by the endothermic gasification treatment (19) and said amount of oxidant gas. 12 / - Method according to one of claims 1 to 11. characterized in that at least a portion of the amount of heat energy required for the endothermic gasification treatment (19) is produced outside the gasification reactor. 13 / - The method of claim 12, characterized in that at least a portion of the amount of heat energy for the endothermic gasification treatment (19) is produced by a combustion, outside the gasification reactor, d at least a portion, said part to be burned, of the dry fraction (16) with a quantity of oxidizing oxidizing gas. 14 / - Method according to one of claims 1 to 13, characterized in that at least a portion of the amount of thermal energy for the endothermic gasification treatment (19) is produced by a combustion of a portion of the gas synthesis product. 15 / -Procédé according to one of claims 1 to 14, characterized in that at least a portion of the amount of heat energy required for the endothermic gasification treatment (19) is produced by a combustion of at least a portion biogas (18). 16 / - Method according to one of claims 1 to 15, characterized in that prior to the separation (14) by compression of the putrescible fraction (15) and the dry fraction (16), a step is carried out (11) extraction of inert materials neither putrescible nor combustible, so that garbage or waste (13) resulting from this separation (14) are essentially formed of non-inert materials. 17 / - Method according to one of claims 1 to 16, characterized in that for separating the putrescible fraction (15) and the dry fraction (16), said garbage or waste is compressed to a pressure greater than 700 bar ( 700 105Pa), in particular between 720 bars (720 105Pa) and 750 bars (750 105Pa), in at least one compression chamber provided with extrusion orifices through which the putrescible fraction (15) flows. 18 / - Method according to one of claims 1 to 17, characterized in that carries out the separation treatment (14) on a site, said separation site, distinct from a site, said gasification site, on which the endothermic gasification treatment (19) is carried out. 19 / - Method according to one of claims 1 to 18, characterized in that carries out the treatment by endothermic gasification (19) of the dry fraction (16) after a storage time. 20 / - Method according to one of claims 1 to 19, characterized in that prepares and stores a gas composition, said recycle gas, comprising a quantity of synthesis gas and a quantity of at least one gas selected from the group consisting of said biogas (18) and natural gas. 21 / - Method according to one of claims 1 to 20, characterized in that stores the recycle gas prior to combustion.