EP0324754A1

EP0324754A1 - Process for dehalogenation of hydrocarbons.

Info

Publication number: EP0324754A1
Application number: EP87906074A
Authority: EP
Inventors: Friedrich Bolsing
Original assignee: Individual
Current assignee: Individual
Priority date: 1986-09-24
Filing date: 1987-09-23
Publication date: 1989-07-26
Anticipated expiration: 2007-09-23
Also published as: JPH02500006A; US5108647A; WO1988002268A1; EP0324754B1; JPH0661373B2; DE3632363A1; DE3766500D1

Abstract

Pour déshalogéner des hydrocarbures, notamment des composés aromatiques polychlorés, que l'on peut trouver également dans des huiles, des crasses d'huile ou dans la vase ou la terre, on les disperse selon le procédé DCR, et on fait réagir le produit de réaction finement dispersé ainsi obtenu en présence d'un corps réactionnel nucléophile jusqu'à déshalogénation.To dehalogenate hydrocarbons, in particular polychlorinated aromatic compounds, which can also be found in oils, oil slags or in silt or earth, they are dispersed according to the DCR process, and the product of finely dispersed reaction thus obtained in the presence of a nucleophilic reactant until dehalogenation.

Description

Process for the dehalogenation of halogenated hydrocarbons

Description

Halogenated hydrocarbons can cause environmental problems. This applies in particular to compounds such as polychlorinated biphenyls, dibenzodioxins, dibenzofurans and other polycyclic aromatics. The compounds can be in substance, as an impurity in mineral oils, in substance or dissolved in mineral oil in the soil, e.g. B. in the form of seepage oils or, together with water, as seepage water from contaminated sites or as impurities in compact, in particular bituminous phases.

It is known that compounds of this type at high temperature, e.g. B. can burn without damage above 1200 ° C, provided that this temperature can be safely maintained over a longer distance in the combustion process. If this is not the case, if suitable starting materials are present, on the contrary, halogenated dioxins or dibenzofurans can be produced under the usual conditions of combustion, so that an additional pollution of the environment occurs.

It is also known that halogenated hydrocarbons can be dehalogenated with metals such as sodium and potassium. The reaction is carried out at elevated temperature, for example with molten sodium in the form of a suspension. ..

Halogenated hydrocarbons, which are present as contaminants in the soil, can be driven off in rotary kilns. The gas stream is then fed to a high-temperature combustion device or condensed. The halogenated hydrocarbons present in the condensed phase can then be subjected to a conventional dehalogenation reaction.

A number of dehalogenation reactions are described in the organic chemical literature. They all only work on the condition that they are purified substances. For example, pure halogenated hydrocarbons can be dehalogenated in a relatively simple manner by treating them with hypophosphorous acid in the presence of palladium catalysts. This method fails immediately if the smallest contaminants are present in the medium. It can therefore be seen that these processes cannot be used in the field of environmental protection because they are always mixtures with constituents which poison the required catalysts after a short time.

The methods mentioned have considerable disadvantages. If the dehalogenation consists in the fact that the halogenated hydrocarbon molecule is destroyed oxidatively overall, ie is destroyed by combustion, then unusually high temperatures are required. Processes of this type are therefore very expensive and there is a risk that, if the above-mentioned framework conditions are not met, highly toxic substances can be produced under these circumstances. In chemical methods outside of oxidative destruction, reactants are always required, possibly also catalysts that are based on heavily contaminated mixtures or on water-containing systems fail, such as the aforementioned dehalogenation using catalysts or using molten sodium metal or sodium alcoholates.

The object of the invention is therefore to provide a method which leads to a complete dehalogenation of halogenated hydrocarbons under relatively mild conditions and is also applicable to the highly contaminated, frequently water-containing problematic substances mentioned in practice mentioned at the outset in practice in an indefinable composition .

This object is achieved by chemically dispersing organic halogen compounds by themselves or as impurities in other materials and by allowing the finely dispersed reaction product to react until dehalogenation in the presence of a nucleophilic reaction partner.

It is known, in particular from numerous publications by the inventor, that substances and mixtures of substances can be dispersed chemically. Dispersion through chemical reactions (DCR for short) is a simple method for distributing liquid substances and solutions of solid or liquid substances in the course of the formation of large surfaces by chemical reaction and is the subject of German Patents 20 53 627, 23 28 777 , 23 28 778, 25 20 999, 25 33 789, 25 33 790, 25 33 791 and their foreign

Equivalents. Among the numerous chemical reactions that meet the condition for an increase in surface area in the sense described and which are therefore used for chemical distribution the reaction of calcium oxide with water to calcium hydroxide and the hydrolysis of aluminum alcoholates to aluminum hydroxide are particularly noteworthy. The compounds present in the resulting finely dispersed solid preparations have a particularly high chemical reactivity. One of the advantages of the chemical dispersing process is that one can co-disperse the reactants required to perform certain chemical reactions with the dispersed substances. In this way, both reactants are side by side in a highly reactive form.

For the dehalogenation of halogenated hydrocarbons, nucleophilic reaction partners are advantageously used. If calcium oxide is used as starting material (starting material) to carry out the dispersing reaction, a solid preparation with calcium hydroxide as carrier material is obtained. If the dispersing reactions are carried out with the introduction of halogenated hydrocarbons, the calcium hydroxide formed contains the halogen compound homogeneously. Halogen compounds and calcium hydroxide are therefore in a highly reactive form. Hydroxyl ions are nucleophilic reactants. When the solid preparation is heated in a closed system, the halogenated hydrocarbon is dehalogenated. With a residence time of around one hour, a reaction temperature of only about 500 ° C. is required for this. By co-dispersing nucleophilic reactants of higher reactivity, such as. B. alcoholates, the temperature decreases depending on the structure of the alcoholate to about 300 ° C. If potassium hydroxide is metered into the water which is required for the reaction of the calcium oxide to calcium hydroxide, the reaction temperature lowers to about 400 ° C. under otherwise identical conditions. In this context, the relationships known in chemistry between residence time, reaction temperature and nucleophilic reactivity and last but not least the solvent apply. By means of simple preliminary tests, the person skilled in the art is able to optimize the conditions for the halogenated hydrocarbon to be completely dehalogenated in combination with the cheapest starting material and a particularly effective nucleophilic reaction partner in such a way that the dehalogenation is as short as possible at the lowest possible temperature Time can be completed. It is therefore also quite possible for the finely dispersed reaction product to be allowed to react completely in the presence of the nucleophilic reaction partner at ambient temperature until dehalogenation.

Unless the nucleophilic reactant already arises from the educt of the dispersing chemical reaction, such as the. B. is the case with calcium or magnesium hydroxide, the nucleophilic reaction partner is added and expediently incorporated in the dispersion by chemical reaction. Particularly suitable nucleophilic reactants are, in addition to the alkali hydroxides and alcoholates already mentioned, alcohols or amines. If, in addition to KOH, alcohols are also present, e.g. B. diethylene glycol, alcohol ions are formed in equilibrium, which have a high nucleophilic reactivity. If heating is necessary for the dehalogenation of the halogenated hydrocarbons in the finely dispersed reaction product of the DCR process used in the presence of the nucleophilic reaction partner, this is expediently carried out in a closed reaction space in order to prevent the halogenated hydrocarbons from escaping before they are completely To prevent dehalogenation. In order to ensure a complete reaction of the possibly gaseous halogenated hydrocarbons with the solid reaction partners, it is advisable to keep the gas volume as small as possible so that the reaction space is filled as completely as possible by the finely dispersed reaction product and the nucleophilic reaction partners. However, the dehalogenation can also be carried out continuously in a fluidized bed or a fixed bed reactor, the hydrocarbons which are formed optionally being returned to the fluidized bed or the bed of the solids as long as they still contain halogenated components.

With the method according to the invention, highly toxic substances containing halogens can be dehalogenated and converted into substances with low risk potential in the simplest and most reliable manner, ie for example tetrachlorodibenzodioxin in dibenzodioxin, which, in contrast to the first compound, is not an ultra-poison at all, but one relatively harmless connection. However, in order to render the secondary products formed after dehalogenation harmless, the fully reacted product, ie the product after dehalogenation, which is still in powder form, can be subjected to normal combustion, ie one Incinerator that works at around 800 ° C. Since the secondary products always burn easily, the environmental hazard described above can no longer occur. For the purposes of the invention calcium oxide is in the form of commercially available quicklime, e.g. B. Weiß¬ fine lime, preferred, but also coarse grains are useful in many cases. The quicklime can contain up to 18% by weight magnesium oxide or other foreign components.

Halogenated pollutants can be "collected" in soils with the help of hydrophobized calcium oxide. This adsorption or pre-distribution can be improved by adding bituminous substances or mineral oils, which are preferably used in the form of waste materials.

In the following examples, all quantities are parts by weight.

Example 1:

14 parts of polychlorinated biphenyls (PCB) in the form of an industrially produced isomer mixture are stirred with 28 parts of CaO. By adding 10 parts of water, an exothermic dispersing chemical reaction produces a dry powdery preparation which is heated to 510 ° C. in a closed tube and held at this temperature for 30 minutes. 99.996% of the dehalogenation takes place under these conditions.

Example 2:

14 parts of a contaminated with 10,000 ppm PCB

Mineral oil with 28 parts CaO and 10 parts Water in which 1.4 parts of KOH were dissolved was dispersed chemically. After a dwell time of the reaction product of 30 minutes at 350 ° C, only 0.98 ppm PCB are detectable.

Example 3:

14 parts of a mineral oil contaminated with 10,000 ppm PCB are chemically dispersed with 28 parts CaO and 10 parts water, in which 1.4 parts KOH and 2 parts of a polyethylene glycol with an average molecular weight of 400 were dissolved. After a residence time of the reaction product of 30 minutes at 300 ° C, 1.4 ppm PCB are still detectable.

Example 4.

14.9 parts of a mineral oil-containing residue with 0.14 parts PCB and 0.9 parts tetrachloroethane from a storage tank are mixed with 28 parts CaO and 10 parts water, in which 1.4 parts KOH and 2 parts of a polyethylene glycol with a medium molecule Lar weight of 400 were dissolved, chemically dispersed. After a dwell time of 30 minutes at 350 ° C in the autoclave, no tetrachloroethane is detectable and PCB only 0.9 ppm.

Example 5;

14 parts of a waste material contaminated with 10,000 ppm of a 50% solution of PCB in trichlorobenzenes are chemically dispersed with 28 parts of CaO and 10 parts of water in which 1 part of NaOH was dissolved. After a residence time of 30 minutes at 350 ° C. in a fixed bed tractor, neither PCB nor trichlorobenzenes were detectable under otherwise identical analytical conditions. Example 6;

56 parts of a cohesive soil contaminated with 100,000 ppb of a mixture of chlorine-containing waste materials with more than 50% hexachlorobenzene from the production of crop protection agents were intimately mixed in a screw reactor with 50 parts of hydrophobic CaO in the presence of 18 parts of water. The organic impurities absorbed by the hydrophobic CaO in the mixing process can thus be chemically dispersed. With a residence time of the reaction mixture at 350 ° C of 30 minutes, 5.5 ppb halogenated hydrocarbons can still be detected.

If you add 1 part KOH to this approach, e.g. in the form of an aqueous solution, the degree of dehalogenation is increased to 99.9973% and only 1.1 ppb of halogenated hydrocarbons can be detected under otherwise identical analytical conditions.

Example 7;

56 parts of a sandy soil contaminated with 2,000,000 ppb of a mixture of chlorine-containing waste materials with more than 50% hexachlorobenzene in addition to pentachlorobenzene as well as tetra- and trichlorobenzenes, differently chlorinated naphthalene and small proportions of differently chlorinated dibenzodioxins from the production of crop protection products were intimately mixed in a screw reactor with 50 parts of hydrophobic CaO in the presence of 10 parts of a waste mineral oil. The one in the mixing process Organic impurities absorbed by the waste mineral oil can thus be chemically dispersed after the addition of 18 parts of water. The reaction mixture is kept at 350 ° C. for 30 minutes. Thereafter, 2.0 ppb of halogenated hydrocarbons can be detected.

An almost identical result is obtained if first waste mineral oils, bituminous waste materials, used bleaching earth loaded with low-volatile organic substances, or other substances which take the halogenated hydrocarbons in solution or, like the hydrophobic CaO, bind adsorptively and thus the nucleophile Make reaction partners optimally accessible, chemically dispersed and the hydrophobic reaction product of the dispersing chemical reaction subsequently mixed with the contaminated soil, sand or other contaminated substances and brought to the appropriate temperature for the appropriate time. Soil, sand, etc. must be almost dry.

In very general terms, the processes according to decontaminated soils and sands can be used as soil bodies, e.g. use as a paved surface, as they no longer release the remaining but contaminated traces of pollutants into the environment. This applies in particular if the floors are installed with compaction.

Claims

Patent claims

1. A process for the dehalogenation of halogenated hydrocarbons, characterized in that the halogenated hydrocarbons are dispersed chemically and the resulting, finely dispersed reaction product is allowed to react in the presence of a nucleophilic reaction partner until dehalogenation.

2. The method according to claim 1, characterized in that the finely dispersed reaction product is heated in the presence of a nucleophilic reaction partner to the temperature just required to end the reaction in the shortest possible time.

3. The method according to claim 1 or 2, characterized gekenn¬ characterized in that the heating is carried out in a closed reaction space.

4. The method according to any one of claims 1 to 3, characterized in that the reaction space is as completely as possible filled by the finely dispersed reaction product and the reactants.

5. The method according to any one of claims 1 to 4, da¬ characterized in that the dehalogenation is carried out dis¬ continuously in an autoclave.

6. The method according to any one of claims 1 to 4, da¬ characterized in that the dehalogenation is carried out continuously in a fixed bed reactor. - 12 - -

7. The method according to any one of claims 1 to 4, characterized in that the dehalogenation is carried out in a fluidized bed.

8. The method according to any one of claims 1 to 7, characterized in that the halogenated hydrocarbon is chemically dispersed in the presence of a nucleophilic reactant.

9. The method according to any one of claims 1 to 8, characterized in that the nucleophilic reaction partner is formed from the starting material of the dispersing chemical reaction.

- ¹ - ⁵ 10. The method according to any one of claims 1 to 9, da¬ characterized in that alkali metal hydroxides, alkali metal alcoholates, alcohols or amines are used as nucleophilic reaction partners.

11. The method according to any one of claims 1 to 10, characterized in that the dispersion by chemical reaction and the dehalogenation are carried out as a one-step process.

25 12. The method according to any one of claims 1 to 11, characterized in that polychlorinated aromatics, in particular chlorinated biphenyls and dioxins, are used as the halogenated hydrocarbons.

13. The method according to one of claims 1 to 12, characterized in that halogenated hydrocarbons are used which are present in oils, oil sludge, in the soil or in silt.