# Patent

## Title
Chemical vessel environmental chamber

## Abstract

Method to convert refuse derived fuel (RDF) into a combustible gas, whereby the refuse derived fuel is gasified and the derived gas undergoes a process of catalytic cracking in which at least one alkaline additive or an equivalent product is used, the gas being passed through a cyclone separator to collect the particulate solids and thereafter undergoing a cooling process with recovery of hot air before being passed through sleeve filters, the ashes of the gasification and the particulate solids being sent to a dump for ashes, the ashes of gasification being riddled beforehand to gather the fines, which are mixed with fines coming from the sleeve filters and are employed as further catalysts in the catalytic cracking process.

## Background
1. Field of the Invention

This invention concerns a method to convert refuse derived fuel, whether of an urban or industrial origin, into a combustible gas, as set forth in the main claim.

The method of the invention is applied adantageously, but not only, to the processes of gasification and/or pyrolysis of conventional solid fuels or fuels derived from the screening of solid urban refuse or from the processing of biomasses.

2. Discussion of the Prior Art

The gasification technology which has been developed for some time now for the production of gas from coal or wood has been used recently with more difficult fuels, such as the residues of the processing of biomasses, solid urban refuse, and solid industrial refuse or the combustible fraction derived therefrom and conventionally called refuse derived fuel.

This technology is worthwhile since it enables the ashes to be separated from the gaseous products, which have a smaller volume than the products resulting from simple incineration, and therefore makes possible a reduction of the volumes of the equipment required to treat the gaseous products and a more efficient technique for the combustion.

Moreover, the various available technologies give birth to a gaseous mixture consisting essentially of light gases such as CH.sub.4, CO, H.sub.2, H.sub.2 O, N.sub.2 and CO.sub.2, but also of a moderate quantity of vapours of high-boiling hydrocarbons (tars) and of ashes containing volatile metals.

The energy content of the tars amounts to about 20% of the calorific power of the gas produced and is therefore an important fraction for the yield of heat of the process.

The chemical-physical properties of these products make problematical the employment of the gas produced in traditional usage equipment such as boilers or gas-powered engines since the gas produces harmful emissions and also deposits along the pipes and in the equipment.

It is therefore worthwhile to recover and convert these products into a usable form.

One of the most promising ways has been found to be catalytic cracking.

In the state of the art the gasification process and the successive treatment to scrub the gas thus produced comprise according to the state of the art the following steps: controlled quantity of oxidizing gas; residual content of unburnt carbon, mainly in the fine fraction (fine bottom ashes). The coarse fraction (coarse bottom ash) consists mainly of sintered material, carbon free, in a glassy form suitable to undergo the leaching test limits for sanitary dumps; furnace, the gas consisting mainly of CH.sub.4, CO, H.sub.2, H.sub.2 O, N.sub.2, CO.sub.2 and of hydrocarbons with a wide boiling-point spectrum (tars); quantity of a high-temperature oxidising gas (air, for instance) and of a catalytic support (dolomite, for instance); hydrogen sulphide, contained in the gas by means of adsorption on beds of dolomite; step, in a cyclone chamber or another suitable separator; or by atomised water; process air to be used for the gasification and catalytic cracking; CH.sub.4, CO, H.sub.2, H.sub.2 O, N.sub.2 and CO.sub.2, and therefore suitable for subsequent employment in technical usage apparatus devoid of final treatment of fumes, such as endothermic engines, boilers, heating furnaces, etc.; wastes due to a high content of heavy volatile metals and toxic organic compounds (e.g. PAH=polyaromatic hydrocarbons, dioxines); systems to filter the gas thus produced are sent to appropriate controlled dumps.

The combustion of the gas obtained by this treament produces flu gases with a reduced corrosive action and a lower content of harmful products such as dioxin, NO.sub.2 and acid products derived from the combustion of hydrogen-halogen products present in the refuse derived fuel.

The present applicant has studied, tested and brought about this invention so as to obviate the shortcomings of the state of the art and to achieve further advantages.

The invention is set forth and characterized in the main claim, while the dependent claims describe variants of the idea of the main solution.

The attached FIGURE shows as an example a block diagram of the cyle according to the invention.

In the process of gasification of the refuse derived fuel according to the invention the fine fraction of the ashes gathered from the bottom of the gasification furnace and the ashes separated by the bag filter installed on the line of the gas downstream of the heat exchangers are recycled and not sent directly to the disposal dump.

The ashes from the bottom of the gasification furnace are rich in residual alkalinity and, according to the invention, are sieved and divided into a fine fraction (smaller than 2-3 mm.) and a coarse sintered fraction suitable for dumping.

The fine fraction of the ashes from the bottom of the gasification furnace and the ashes collected by the bag filter system are mixed with a suitable alkaline additive, or an equivalent product such as lime or ash, so as to generate the catalyst mixture to be sent to the cracking step.

This mixture, which acts as a catalyst for the reaction that take place during catalytic cracking, can be sent to the cracking reactor, for instance by a pneumatic conveyor.

In this way the quantity of catalyst to be fed to the cracking reactor is reduced considerably, with a resulting economical advantage for the process of treatment of the gas itself.

According to the invention a suitable quantity of lime or of an equivalent alkaline product to abate the chlorine content is introduced into the cycle together with the ashes.

According to the invention the ashes and the lime are introduced into the cycle in the gas line upstream of the catalytic cracking reactor so as to accomplish a reduction of unburnt material and a partial recovery of energy.

In this way, besides the economical advantage of a greater yield of the gasification process, there is also an environmental advantage resulting from the reduction inertization of the solid effluent to be sent for dumping.

Moreover, during the gasification process according to the invention the gas leaving the catalytic cracking reactor undergoes a step of separation, by means of a cyclone separator for instance, before being cooled.

The particulate solid thus separated undergoes a postcombustion treatment with preheated air at a high temperature.

The heat generated by this postcombustion is used directly to complete the catalytic cracking reactions.

The mass of recirculated ashes consists, for the most part, of solid carbon coke, which in the established cracking conditions is converted efficiently, by means of reaction with the water vapour present, into oxides of carbon and hydrogen, thus increasing the yield of combustible gases.

Moreover, in the method according to the invention the recirculated ashes contribute towards keeping the cracking conditions stable and and improving the heat recovery during the subsequent treatment steps.

The quantity of recirculated ashes can be regulated suitably, and also automatically, so as to keep the operational cracking conditions stable and thus to lessen the problems due to fluctuations, even sudden fluctuations, in the characteristics of the gas produced in the previous gasification step.

The operational conditions of the postcombustion enable residual ashes to be obtained with a minimum content of unburnt material and with an efficient thermal destruction of harmful organic carbonous products.

This postcombustion of unburnt ashes takes place advantageously, but not necessarily, in an appropriate chamber located below the discharge of the cyclone separator.

In this way the residual solids of the postcombustion step consist of inert materials and represent the only solid effluent of the treatment cycle together with the coarse ashes from the bottom of the gasification furnace.

The quantity of this solid effluent of the cycle amounts to about 8% to 10% by weight of the burnt refuse derived fuel.

In this way, besides the reduction of the unburnt material, there is also a partial recovery of energy, which increases the yield of the gasification process and makes the process still more worthwhile financially.

## Claims

1. Method to convert refuse derived fuel (RDF) into a combustible gas, comprising the following steps: gas and ashes of gasification; additive is used; separator to collect particulate solids; particulate solids to a dump for ashes; bag filters and adding said mixture to said derived gas as catalysts in the catalytically cracking step.

2. Method as claimed in claim 1, in which the alkaline additive is added during the step of mixing the fines.

3. Method as claimed in claim 1, in which lime product is added during the step of mixing the fines.

4. Method as claimed in claim 1, in which the particulate solids leaving the cyclone separator undergo a postcombustion step.

5. Method as claimed in claim 1, wherein hot air recovered by said cooling step is employed in a further step of postcombustion of the particulate solids leaving the cyclone separator.

6. Method as claimed in claim 5, in which said postcombustion step produces heat used directly to complete the catalytic cracking reactions.

7. Method as claimed in claim 1, in which said recirculated fines consists of activated carbon, and said cracking step includes converting said carbon, by reaction with water vapour, into oxides of carbon and hydrogen, thereby increasing the yield of the combustible gases.

8. Method as claimed in claim 1, wherein said fines added to said derived gas comprise a step of keeping the cracking conditions stable and homogeneous and increasing heat exchange of subsequent treatment steps.

9. Method as claimed in claim 1, wherein there is further included the step of automatically regulating the fines added to said derived gas.

10. Method as claimed in claim 5, wherein said postcombustion step includes the step of reducing content of unburnt material and thermal destruction of harmful organic carbonous products.