A METHOD FOR THE DESTRUCTION OF HALOGEN-CONTAINING SUBSTANCES

Abstract: A method for the destruction of a halogen-containing substance (7), such as halocarbons or a chlorenated organic substances, by conversion of the substance. The method is characterized mainly by reacting the halogen-containing substance (7) with molten iron so as to form an iron salt or iron salts, by introducing the substance into an iron bath together with oxygen gas (5) and/or oxygen-containing material (3), wherein the iron salt or salts is/are caused to leave the bath (2) in a dust and gas flow (10).

Description: A Method for the Destruction of HalcαenH-onteinirto: Substances The present invention relates to a method for the destruction of halogen-conta uig, envirαπmental harmful substances,such as a haloge carbon substance or dhlorenated organic substances, by converting said substances to substances that are not considered to be environ¬ mentally harmful. The occurrence of substances of the aforedescribed kind are today considered to constitute a serious problem to the environment and there is a great need for methods which will enable such substances to be destroyed. Examples of substances for which the method is intended are halocarbons in the form of CFC and halon and dhlore¬ nated organic substances in the form of KB. These substances are exemplified more in detail later on. The method is also intended for the destruction of mixtures of halogen-containing, environmentally harmful substances of the type in question, wherein the method is intended for the destruction, for instance, of one or more types of halon and/or one or more types of CPC and/or one or more PCB-containi substances. The Swedish Patent Specification Nos. 7706876-5, 8103201-3, 8301159-3 and 8503571-5 teach processes for converting carbon to carbon gas, converting iron ore to crude iron or combinations thereof, these processes being characterized by introducing appropriate reactants into a bath of molten iron and causing the reactants to react at a tøπperature of 1400-1500°C, at which the .reaction rate is high and conversion takes place quickly and with a high degree of conversion. The present invention is based on the understanding of the reaction conditions which exist, for instance, in the process described in Swedish Patent Specification No. 8301159-3, i.e. the reaction between organic material, such as coal (carbon) , peat, etc. delivered to the process and an oxidizing substance, such as oxygen gas, iron ore, etc., wherein the iron bath functions, among other things, as a heat transfer medium, solvent and oxide builder. Thus, according to the present invention, the iron bath is used to transfer heat, to dissolve a given part of the material introduced thereto, and to form salts, wherein a primary object of the invention is to destruct organic, environmentally harmful substances which are .mtroduced into the iron bath to this end. The inventive method enables environmentally harmful material to be destructed highly effectively and at relatively low costs, the resul¬ tant end products being unharmful to the environment and capable of being handled in a ∞πventiαnal manner. The invention thus relates to a method for the destruction of a halogen-cxartaining substance, such as a halocarbon substance or a άhlαrenated organic substance, by ∞πverting the substance to an environmentally harmless state. The method is particularly characterized by causing the halogen- containing substance to react with molten iron and to form an iron salt or iron salts, by i_nt_roducing said substance into the bath together with oxygen gas and/or an αxygen-contaiiήng material, and by causing the iron salt/salts to leave the bath in the form of a dust and gas flow. The invention will now be described in more detail with reference to an exemplifying embodiment thereof and with reference to the accom¬ panying drawing, the single Figure of which illustrates schematically apparatus for ca_rrying out the inventive method. The system of apparatus illustrated in the drawing includes a reactor vessel 1, an iron bath 2, an outlet aperture 3, and injection nozzles 4. In the illustrated case, the nozzles 4 are mounted in the bottom of the reactor vessel 1 and function to inject oxygen gas 5 or the like, additional fuel 6, such as coal 6, and a halogen-contaiiύng substance αr substances 7 into the molten bath. The reference numeral 8 identifies reaction zones which extend up through the bath, while the reference numeral 9 identifies liquid slag on the surface of the bath. In the illustrated case, the oxygen gas 5 forms an oxidant for oxidi¬ zing of the carbon contained in the substance or substances to be destroyed. Naturally, the oxidant may consist of same other oxygen- ∞ntaiiiing material, such as iron ore, or combinatiσns of oxygen gas and some other oxygen-containing material. It is often preferred to introduce oxygen gas and/or oxygen- ontaining material into the bath in substantially stoichicroetric quantities in relation to the total amount of carbon introduced to the bath, this carbon being in the form of the carbon contained by the substance or substances delivered to the bath. In certain applications, it is also possible to introduce hydrogen- containing material into the bath, such as certain kinds of carbon powder, hydrogen gas, water, etc. , with the intention of forming hydrogen coπpounds, primarily acids. Supplementary fuel 6 is supplied when there is a need for addi¬ tional energy. The fuel 6 may consist of for instance coal in powder form and/or hydrocarbons, such as propane. The halogens in the halogen-containing substance, the "environmentally harmful" substance, react with iron in the iron bath to form iron halides, which can be dumped or converted to acids with, for instance, water in a later process stage and the acids handled in a conventional manner. Halogens in this state are no longer considered to be harmful to the environment. Halocarbons often include chlorine (Cl) , fluorine (F) or bromine (Br) in addition to carbon (C) . The course taken by the reaction in the conversion of halocarbons can be described schematically with the general reaction (1) Fe(l) + CXyCl/g) + 0.50 2 (g) * = FeXy(s/l) + 00(g) (1) where (s) , (1) , (g) signify solid, liquid and gas phases respec¬ tively and CXy is a halocarbon. Examples of such are presented in Table 1. The course taken by the reactions with same of these ccπcpounds is given by the reactions (2) and (3) . Table 1. Examples of halocarbons. Compound Chemical Formula CPC 11 CCI3F CPC 12 CC1 2 F 2 CPC 113 CC1 2 F - CC1F 2 CFC 114 CC1F 2 - CC1F 2 CFC 115 CC1F 2 - CF 3 HCPC 22 CHC1F 2 Halon 1202 CBr 2 F 2 Halon 1211 CBrClF 2 Halon 1301 CBrF 3 Halon 2402 C r 2 F 4 6 CX.I3F + 11 Fe + 0 2 = 6 CO + 9 FeCl 2 + 2 FeF^ (2) 2 CBrF3 + 3 Fe + 0 2 = 2 CO + FeBr 2 + 2 FeF 3 (3) CO-, + C = 2 CO (4) Iron salts and gas are formed when the halocarbons come into contact with an iron bath which is heated to a τ__πperature of 1500°C. The salts farmed are primarily FeCl 2 , FeBr 2 and FeF 3 . The iron salts leave the iron bath 2 in a flow 10 of dust and gas. During one process stage in which the reaction products leave the iron bath and are cooled and separated, the products transform from a condensed state to a solid, particulate state. The state of the compounds at different tøiperature are set forth in Table 2 below. Table 2. The melting points of some iron salts. Iron Salt Melting Point FeBr 2 691°C FeF 3 >1827°C FeF 2 1100°C FeCl 2 677°C (Fe 1536°C) The formation of iron salts has been confirmed by experiments carried out in an iron bath in which halon 1301 was injected into the bath. The bromine and fluorine salts left the bath and were separated in dust form. Same of the ∞mpσunds to be destructed failed to generate sufficient heat for the method to be autogeneσus. Because the reaction (4) is displaced pronouncedly to the right under the conditions prevailing in the iron bath, it is not possible to obtain all energy to be delivered to the iron bath in order to compensate for endothermic reactions, enthalpy in waste gas and reaction losses, by oxidation of the carbon, C, present to carbon monoxide, CO. The process can be compensated for energy-demanding reactions in a number of ways. One method is to combust the carbon monoxide above the bath surface with oxygen gas or some other oxidant and thereby generate sufficient heat in the reactor, this heat thus cooperating to cover the amount of destruction energy required. In this case, oxygen gas and/or an oxygen-cont_a_i_ning material is delivered to the dust and gas flow 10. Another method is to gasify an appropriate fuel in the process, for instance powdered carbon, such as to supply energy. Same types of coal pcwder will, at the same time, release hydrogen gas which reacts with the halogens to form HBr, HCl and HF. More generally, the hydroge halides can be farmed by introducing hydrogen gas and/or hydrogen- containing material to the iron bath and/or to said dust and gas flow. The illustrated system of apparatus includes a first gas conduit 11 through which the flew of dust and gas passes from the reactor 1 to a first wet so called scrubber 12, in which the gas/dust suspension is cooled and the dust extracted, and a second gas conduit 13 through which the dust and gas flow passes from the first scrubber 12 to a second wet scrubber 14, in which the suspension is cooled and dust extracted therefrom. Liquid, primarily water, draining from the first scrubber 12 is collected in a separator 15, such as a lamellar separator 15, where particles are extracted from the liquid, and a settling device 16, such as a settling tank positioned downstream of the separator. Liquid which drains from the second scrubber 14 is conducted to a c_crιditiαning apparatus 17 which includes a tank in which the pH of the liquid is adjusted, in the illustrated case with sodium hydroxide, NaOH, before passing the liquid to the settling tank 16, to which calcium hydroxide Ca(0H) 2 may also be supplied. Calcium halides and clean water can be removed from the tank 16. Clean gas is removed from the second wet scrubber 14 and, in accordance with the illustrated example, passes to a droplet separator 18 and a measuring station 19. The destruction of a halogen-containing organic material is described belcw by way of example. One tonne of halogen-contaiiing material, halon 1301, was injected each hour into a 10-tonne iron bath contained in a reactor vessel, together with 75 m 3 n oxygen. In order to prevent the accumulation of carbon in the iron bath, oxygen gas was introduced in stoichiαmetric quantities tjrrcugh nozzles mounted in the reactor wall. Gasification of the carbon in the iron bath takes place through partial combustion of the carbon added, therewith forming carbon monoxide. The material -urtroduced had a short residence time in the bath (<ls) , but was efffectively degraded due to the extremely good heat transf r achieved and due to the high average bath temperature, 1500°C (local temperature 2000-2300°C) . 726 kg FeBr 2 , 759 kg FeF 3 and 150 m 3 n CO were formed. After leaving the iron bath, the dust and gas passed through a gas conduit prior to cooling and dust-extraction in a wet scrubber. The teiφerature of the gas entering the gas scrubber was about 1200°C and the total residence time of the gas and dust in the system upstream of the scrubber was from 2-5 seconds, depending on gas flow and pressure. This process thus provides very good conditions for degrading or breaking-dcwn organic material effectively and hcmogenαusly. The iiTventive method will be understood essentially from the afore¬ going. Thus, the halogen-containing, environmentally harmful material concerned is converted to iron salt or iron salts in a high-temperatur iron bath having good heat transfer properties, whereafter the iron salt or salts leaving the bath are treated conventionally and released to atmosphere, recovered or dumped, said salt or salts being harmless to the environment. As will be understood from the aforegoing, halogen-contairύng, en¬ vironmentally harmful waste can be handled very effectively and relatively simply by means of the inventive method. Although the invention has been described in the aforegoing with reference to an exeπplifying embodiment thereof, it will be understood that other embodiments and minor changes are conceivable, without departing from the concept of the invention. It will also be understood from the aforegoing that the flow of dust and gas can be subsequently treated in a manner different to that illustrated in Figure 1. The halogen-containing substance can be introduced into the iron bath by injecting the substance beneath the surface of the bath and/or by injecting the substance from above down onto the bath surface. According to one embodiment, environmentally harmful substances present in the gas and dust flow are oxidized by delivering oxygen gas and/or oxygen-ccntaining material to said flow. According to another embodiment, the dust and gas flew is heated in an afterburner zone so as to ensure that no environmentally harmful substances remain after destruction. The dust and gas flow is prefer¬ ably heated by means of an oxygen-gas/gasol, plasma or the like. Destruction can take place at atmosjiieric pressure or at a pressure above atmospheric. According to one embodiment sometimes preferred, the dust and gas flew is passed through a dry or a wet/dry gas cleaning process, where calcium compounds are used to absorb hydrogen halides. The invention is thus not restricted to the aforedescribed embodi¬ ments, since modifications are possible within the scope of the following Claims.

Claims: Claims 1. A method for the destruction of a halogen-containing substance, such as a halocarbon substance or a chlorenated organic substance, by conversion of said substance, c h a r a c t er i z e d by reacting the halogen-cxmtaining substance (7) with molten iron to form iron salt or salts by introducing said substance to a molten iron bath together with oxygen gas (5) and/or αxygen-contc ning material (3) , said iron salt or salts leaving the bath (2) in a dust and gas flow (10) . 2. A method acxording to Claim 1, c h a r a c t e r i z ed by -introducing oxygen gas and/or oxygen-containing material in substan¬ tially stoiehicmetric quantities. 3. A method aα_x3_cding to Claim l αr 2, ch a r a c ¬ t e r i z e d bry injecting the halogen-containing substance (7) into the bath (2) beneath the top surface thereof and/or from above onto the top surface of said bath. 4. A method acxx_arding to Claim 1, 2 or 3, c h a r a c ¬ t e r i z e d by -introducing oxygen gas and/or oxygen-conteining material into said gas and dust flew with the intention of genera¬ ting heat to assist in covering the amount of energy required for the destruction process. 5. A method according to Claim 1, 2, 3 αr 4, ch a r a c ¬ t e r i z e d bry introducing hydrogen gas and/or hydrogen- c_oπt_aining material to the iron bath and/αr to said dust and gas flow for the purpose of fanning hydrogen halides. 6. A method according to Claim 1, 2, 3, 4 or 5, char a c ¬ t er i z e d by supplying and combusting carton or carbαnacecus material, such as hydrocarbons, such as to supply heat to the iron bath. 7. A method according to Claim 1, 2, 3, 4, 5 or 6, char¬ acter i z ed by gasifying fuel, such as powdered coal, in the iron bath in order to supply energy thereto. 8. A method acxording to Claim 1, 2, 3, 4, 5, 6 or 7, character i z ed by oxidizing env_i_ronmentally harmful substances in the dust and gas flow by supplying oxygen gas and/or oxygen-containing material. 9. A method acxording to Claim 1, 2, 3, 4, 5, 6, 7 or 8, character i zed by heating the dust and gas flow in an afterburner zone, thereby ensuring that no environmentally harmful substances remain after the destruction process. 10. A method according to Claim 1, 2, 3, 4, 5, 6, 7, 8 or 9, characteri z ed by carrying out the process of destruction at a pressure above atmosf-eric pressure. 11. A method according to any one of the preceding Claims, character i z ed in that the halogen-containing substance is one or more types of halon and/or one or more types of CFC and/or one or more PCB-cαntaining substances. 12. A method according to any one of the preceding Claims, character i z ed by passing the dust and gas flow exiting from the bath through at least one so-called wet scrubber in which cooling and dust extraction take place. 13. A method according to airy one of the preceding Claims, character i z ed by passing the dust and gas flow leaving the bath through a dry or wet/dry gas cleaning stage, in which calcium cαttpσunds are added with the intention of absorbing hydrogen halides.

Inventors: AXELSSON CARL-LENNART, TOERNEMAN BJOERN, TORSELL KRISTER, AXELSSON, CARL-LENNART, TOERNEMAN, BJOERN, TORSELL, KRISTER
Applicants: IPS INTERPROJECT SERVICE AB
Application year: 1990
Main classification: B09B3
IPC codes: A62D3, A62D101, B01D53