JP3678740B1 - Method for dechlorination of PCB-containing high-concentration organic halogen compounds - Google Patents

Abstract

PROBLEM TO BE SOLVED: To dechlorinate polychlorinated biphenyl or a mixture of polychlorinated biphenyl and a halogenated aromatic compound, which is difficult to dechlorinate, by dechlorinating at a low temperature, and practically dechlorinating at a lower cost. To provide a method.
A reaction system comprising an organic halogen compound containing 50% by mass or more of polychlorinated biphenyl, an alcohol having a boiling point of 100 ° C. or less, and an alkali compound in the presence of a catalyst such as a carbon crystal compound or a metal-supported carbon compound. A method for dechlorination of an organic halogen compound by irradiating with microwaves,
(A) The alcohol ratio at the start of the reaction in the system (ratio of the number of moles of alcohol to the number of moles of organic halogen compound) is in the range of 5 to 1000, and
(B) The alkali ratio at the start of the reaction in the system (ratio of the number of moles of alkali compound to the number of moles of alcohol) is in the range of 0.005 to 0.1,
React at 10-80 ° C.
[Selection figure] None

Description

  The present invention provides a method for dechlorinating and detoxifying an organic halogen compound (hereinafter referred to as “polychlorinated biphenyls”) containing 50% by mass or more of polychlorinated biphenyl (hereinafter sometimes abbreviated as PCB). About.

  Among various halogenated organic compounds, PCB is extremely harmful to living organisms including the human body. Therefore, it was designated as a specific chemical substance in 1973, and its manufacture, import and use are prohibited. However, after that, tens of thousands of tons of PCBs are left untreated without determining an appropriate disposal method. PCB decomposes PCB safely technically because chlorinated dibenzo-p-dioxin (PCDD) and dibenzofuran (PCDF), which are highly toxic dioxins, are by-produced at high temperature (30 to 750 ° C) decomposition. This is difficult, and various safe and efficient decomposition methods for PCBs have been studied for many years.

  As a decomposition condition of PCB, implementation at high temperature and high pressure is generally known. However, implementation under such conditions requires a high-temperature and high-pressure container and further a corrosion-resistant container and requires a lot of energy. Met. Moreover, since it is a reaction at a high temperature, it is considered that there is a high possibility that a side reaction product is generated.

  Currently, assessment is necessary for the construction of PCB processing facilities, so PCBs can be rendered harmless at sites such as transformer storage without using special equipment, and PCBs can be safely processed in large quantities. It is desired to develop a method that can be decomposed at low cost.

  Therefore, a method of decomposing PCB by hydrogenation at normal pressure has been proposed as an improvement measure for high temperature and high pressure treatment. For example, Japanese Patent Application Laid-Open No. 2001-19646 (Patent Document 1) discloses that a mixed system containing activated carbon supporting platinum and an aromatic chlorine compound (parachlorophenol) is irradiated with microwaves while blowing hydrogen gas. A method for dechlorinating harmful organic chlorine compounds has been proposed. In this method, a reaction system containing a specific catalyst and parachlorophenol or mono-, di-, or tri-chlorobenzene is irradiated with microwaves in the presence of a reducing substance such as hydrogen or alcohol at a low temperature for a short time. It is said that aromatic chlorine compounds can be dechlorinated with

  However, in this method, it is necessary to supply hydrogen gas from the outside to the reaction system containing the aromatic chlorine compound, which is not preferable as a practical method. In addition, the target is about 50% aqueous solution of aromatic chlorine compounds, and it is not a technique for detoxifying higher concentrations. Moreover, it does not mention detoxification of polychlorinated biphenyl.

  Accordingly, the present inventors have disclosed polychlorinated biphenyls or polychlorinated biphenyl mixtures and hydrogen in Japanese Patent Application Laid-Open No. 2004-201701 and Japanese Patent Application Laid-Open No. 2004-201702 as techniques for detoxifying polychlorinated biphenyls using microwaves. A method for dechlorination of polychlorinated biphenyl was proposed in which a reaction system containing a donor is irradiated with microwaves in the presence of an alkali compound and a catalyst (see Patent Documents 2 and 3).

  These methods do not require a high-temperature and high-pressure vessel and are excellent in terms of cost because they can reduce the energy used for the reaction, and are excellent technologies that can decompose polychlorinated biphenyls in a short time. Due to the high temperature (about 160 ° C.), there was a problem in that by-product formation was a concern.

  On the other hand, in Japanese Patent Application Laid-Open No. 2004-34015 (Patent Document 4), a capacitor, a transformer, or the like containing PCB is put into a high-frequency induction heating furnace together with a heat generation promoting material such as an alkali compound, an aluminum piece, a carbon piece, etc. There has been proposed a method for detoxifying PCBs by blowing an inert gas into the heating furnace and heating to 1000 ° C. or higher in an oxygen-free atmosphere.

  This method is superior in that it eliminates the need for a detoxification process for containers and internal components that have been in contact with PCB insulating oil, since it does not require an extraction work process from the disassembly of the PCB-containing electrical equipment. The heating furnace is brought to a high temperature state of 1500 ° C., and aluminum or iron internal parts, which are containers for the condenser, are induction-heated and heated and melted in an instant. Therefore, it is difficult to say that the PCB can be easily detoxified at a site such as a transformer storage.

  Japanese Patent Application Laid-Open No. 2004-141815 (Patent Document 5) discloses a method in which an alkali metal dispersion, an organic halogen compound, and a hydrogen donor are dehalogenated in a microchannel (microchannel) of a reactor. Has been proposed. In this method, when PCB is dechlorinated with Na dispersion, Na particles and polymer products are present in the microchannel of the reactor, preventing the phenomenon of clogging the flow path, and no complicated temperature control is required. Therefore, it can be said that it is an excellent method in that it can be dehalogenated in an energy-saving and space-saving manner, and can also be processed at a transformer storage site.

However, since metal Na is used, it is necessary to be careful in handling, and there is a problem that a special reactor needs to be newly installed. In addition, although it is disclosed in the test examples that trichlorobenzene (TCB) can be dechlorinated to 0.05 ppm, there is no test example related to the hardly decomposable PCB.
JP 2001-19646 A (Claim 1, paragraph numbers 0008 to 0009, etc.) JP 2004-201701 (Claim 1, Example 1 of paragraph numbers 0041 to 0042, etc.) JP-A-2004-201702 (Claim 1, Example 1 of paragraph numbers 0046 to 0047, etc.) JP 2004-34015 A (Claim 1, paragraph numbers 0002, 0009, etc.) JP 2004-141815 A (Claim 1, test examples of paragraph numbers 0134 to 0136, etc.)

  The present invention has been made in view of the above-mentioned conventional problems. Polychlorinated biphenyls, which are difficult to dechlorinate, can be dechlorinated at low temperatures to make them harmless. It aims to provide a chlorination method.

  As a result of intensive studies to solve the above problems, the present inventors have selected an alcohol having a boiling point of 100 ° C. or lower as the hydrogen donor to be added to the reaction system, the ratio of the hydrogen donor to the polychlorinated biphenyls, and the hydrogen donation. The inventors have found that polychlorinated biphenyls can be dechlorinated at low temperatures by irradiating microwaves in the presence of a catalyst within a certain range of the ratio of the alkali compound to the body, and reached the present invention.

That is, the present invention is to fill at least one catalyst selected from the compounds obtained by supporting a metal on carbon crystal compound and a carrier in the column, polychlorinated biphenyls and an organic halogen compound containing more than 50 wt%, boiling point and 100 ° C. or less of alcohol, while the reaction solution containing the alkali compound is circulated in the column packed with the catalyst, a dechlorination method of an organic halogen compound for irradiating a microwave to the catalyst packed column,
(A) The alcohol ratio at the start of the reaction in the system (ratio of the number of moles of alcohol to the number of moles of organic halogen compound) is in the range of 5 to 1000, and
(B) The alkali ratio at the start of the reaction in the system (ratio of the number of moles of alkali compound to the number of moles of alcohol) is in the range of 0.005 to 0.1,
Provided is a method for dechlorination of an organic halogen compound, characterized by reacting at 10 to 80 ° C.

  In the method for dechlorinating an organic halogen compound of the present invention, the alcohol is preferably 2-propanol.

  In the method for dechlorinating an organic halogen compound of the present invention, the alkali compound is preferably NaOH or KOH.

  In the organic halogen compound dechlorination method of the present invention, the catalyst is preferably a palladium-supported carbon compound.

  In the organic halogen compound dechlorination method of the present invention, it is preferable to irradiate the solution in the apparatus filled with the catalyst with the microwave.

  The method of dechlorinating an organic halogen compound of the present invention is preferably applied to dechlorination of polychlorinated biphenyls extracted from a transformer.

  According to the present invention, a reaction system containing polychlorinated biphenyls and a specific amount of an alcohol having a boiling point of 100 ° C. or lower and an alkali compound is irradiated with microwaves and reacted at a low temperature, thereby requiring a high-temperature and high-pressure reaction vessel. Therefore, polychlorinated biphenyls can be dechlorinated at normal pressure without supplying hydrogen and heat from the outside. Moreover, since a high temperature / high pressure reaction is not performed, there are few side reaction products. In addition, PCBs can be easily detoxified at sites such as transformer stores. Therefore, since a large amount of PCB can be detoxified on a practical scale, its practical value is great.

  The polychlorinated biphenyls to be dechlorinated in the dechlorination method of the present invention are organic halogen compounds containing 50 mass% or more of polychlorinated biphenyls, specifically, polychlorinated biphenyls and polychlorinated biphenyls. And a mixture of halogenated aromatic compounds. The mixing ratio is not particularly limited, but in general, polychlorinated biphenyl / halogenated aromatic compound = 9/1 to 5/5 (mass ratio), and more preferably 7/3 to 6/4 (mass ratio). This is because when the ratio of the polychlorinated biphenyl / halogenated organic compound is less than 9/1, the viscosity of the oil becomes high, whereas when the ratio exceeds 5/5, the insulating performance decreases.

  The halogenated aromatic compound is not particularly limited as long as the aromatic compound is substituted with a halogen atom. Specific examples include trichlorobenzene (TCB), dichlorobenzene (DCB), and tetrachlorobenzene. In general, trichlorobenzene (TCB) is frequently used.

  As a mixture of commercially available polychlorinated biphenyl / halogenated aromatic compound, for example, KC-1000 (mixture of KC500 / TCB = 60/40 (mass ratio)), KC-1300 (KC) manufactured by Kaneka Chemical Co., Ltd. -300 + DCB + 4-chlorobenzene mixture).

  On the other hand, the polychlorinated biphenyl includes a compound in which a chlorine atom is substituted into a biphenyl compound, and the number of substituted chlorine atoms is 1 to 10. The average number of substituted chlorine atoms is generally 2-6. In this invention, at least 1 sort (s) selected from these polychlorinated biphenyls can be used, and each can be used individually or in combination of 2 or more types.

  In general, polychlorinated biphenyls do not exist as a single compound but exist as a mixture having different numbers of chlorine atoms and different substitution positions. Therefore, there are 209 isomers based on the combination of the number of chlorine atoms and the substitution position, and more than 100 isomers exist in the commercial product.

  For example, as a coplanar PCB, 3,4,4 ′, 5-tetrachlorobiphenyl, 3,3 ′, 4,4′-tetrachlorobiphenyl, 3,3 ′, 4,4 ′, 5-pentachlorobiphenyl, 3,3 ′, 4,4 ′, 5,5′-hexachlorobiphenyl, 2,3,3 ′, 4,4′-pentachlorobiphenyl, 2,3,4,4 ′, 5-pentachlorobiphenyl, 2 3 ′, 4,4 ′, 5-pentachlorobiphenyl, 2 ′, 3,4,4 ′, 5-pentachlorobiphenyl, 2,3,3 ′, 4,4 ′, 5-hexachlorobiphenyl, 2, 3,3 ′, 4,4 ′, 5′-hexachlorobiphenyl, 2,3 ′, 4,4 ′, 5,5′-hexachlorobiphenyl, 2,3,3 ′, 4,4 ′, 5,5 ′ -Heptachlorobiphenyl and the like

  PCBs are usually marketed as a mixture of PCBs alone, and these are used for capacitors and transformers. Specific examples include KC-200 (biphenyl dichloride), KC-300 (biphenyl trichloride), KC-400 (biphenyl tetrachloride), KC-500 (biphenyl pentachloride), KC of Kaneka Chemical Co., Ltd. -600 (biphenyl hexachloride) and Arrochlor 1254 (54% Chlorine) manufactured by Mitsubishi Monsite Corporation.

As an example, the distribution (mass%) of isomers of the commercial product KC-300 is shown below.
Monochrome biphenyl slightly dichlorobiphenyl 12.10%
Trichlorobiphenyl 54.98%
Tetrachlorobiphenyl 27.05%
Pentachlorobiphenyl 4.72%
Hexachlorobiphenyl 1.08%
Heptachlorobiphenyl slightly Octachlorobiphenyl 0
Nonachlorobiphenyl 0
Decachlorobiphenyl 0

  In the present invention, the polychlorinated biphenyls include various substances used when taking out the polychlorinated biphenyls from the apparatus (transformer, condenser, etc.) in which they are used, such as cleaning agents such as dodecane. It may be.

  In the present invention, examples of the alcohol having a boiling point of 100 ° C. or lower used as a hydrogen donor include methanol, ethanol, 1-propanol, 2-propanol, and t-butanol. The alcohols can be used alone or in any combination of two or more. These alcohol compounds are preferable because they are highly safe, can be obtained at low cost, can easily be controlled, and have high PCB decomposition efficiency. When a high-boiling point alcohol such as cyclohexanol (boiling point: 161 ° C.) is used as the hydrogen donor, the decomposition efficiency is high, but the possibility of generating a side reaction product is high, while the relatively low boiling point is high. By using this alcohol, the decomposition efficiency can be increased while maintaining the reaction temperature low. Here, the “hydrogen donor” means a compound capable of donating a hydrogen atom to a radical generated from polychlorinated biphenyls.

  Moreover, it is preferable from the viewpoint of suppressing the side reaction product that the alcohol has a boiling point higher than the reaction temperature described later.

  The alkali compound used in the present invention can be used without limitation as long as it can accelerate the dechlorination reaction of polychlorinated biphenyls, but from the viewpoint of increasing the dechlorination efficiency, NaOH, KOH, sodium alkoxide. , Potassium alkoxide, calcium hydroxide and the like are preferably used. Among these, NaOH or KOH is particularly preferable from the viewpoints of cost and handling properties. An alkali compound can be used individually or in combination of 2 or more types.

  The catalyst used in the present invention is at least one selected from a carbon crystal compound and a compound in which a metal is supported on a carrier, and can be used without limitation as long as it can accelerate the dechlorination reaction of polychlorinated biphenyls. The type is not particularly limited. An inorganic catalyst is preferable to an organic catalyst because it has a long catalyst life and is stable even in the presence of an alkali compound. The catalyst can be suitably used because it is considered to be highly safe in an alkaline atmosphere and exhibit high activity against microwaves, and a compound in which a metal is supported on a carrier is particularly preferable. Examples of the carrier include carbon such as activated carbon and graphite, metal oxides such as silica gel, alumina and zeolite, and composite metal oxides, and resins such as polyethylene. Among these carriers, dechlorination efficiency is included. A metal-supported carbon compound in which a metal is supported on a carbon support is preferable because it is high and has high safety in an alkaline atmosphere. A catalyst can be used individually or in combination of 2 or more types.

  Here, examples of the carbon crystal compound include graphite, carbon nanotubes (both including and not including metal), fullerene, and the like.

  Moreover, as said metal carrying | support carbon compound, if it is a carbon compound which carry | supported the metal, it can be used without a restriction | limiting, The metal carrying amount is 1-20 mass% with respect to the catalyst whole quantity, More preferably, it is 5-10. It is good that it is mass%. Examples of the supported metal include iron, silver, platinum, ruthenium, palladium, rhodium, and the like. From the viewpoint of increasing the dechlorination efficiency, palladium, ruthenium, and platinum are preferable, and palladium is more preferable. Specific examples of the metal-supported carbon compound include Pd / C (palladium-supported carbon compound), Ru / C (ruthenium-supported carbon compound), and Pt / C (platinum-supported carbon compound). The particle size of the metal-supported carbon compound is preferably 75 to 300 μm. When the particle size exceeds 300 μm, the reactivity is deteriorated, and when it is less than 75 μm, the handling property is deteriorated. More preferably, 125 to 250 μm is desirable.

In the dechlorination method of the present invention, the ratio of the alkali compound / alcohol / polychlorinated biphenyls at the start of the reaction in the system is 0.05 to 1/10 / 0.001-2 (molar ratio). There is a need. The molar ratio of the three components is more preferably 0.1 / 1/10 / 0.01-1. Accordingly, (a) the alcohol ratio at the start of the reaction in the system (ratio of the number of moles of alcohol to the number of moles of polychlorinated biphenyls) is in the range of 5 to 1000, and (b) at the start of the reaction in the system The alkali ratio (ratio of the number of moles of alkali compound to the number of moles of alcohol) needs to be in the range of 0.005 to 0.1. When the alcohol ratio is less than 5, the dechlorination reaction does not proceed. On the other hand, when the alcohol ratio exceeds 1000, the dechlorination reaction proceeds, but there is no practical meaning and the economy is inferior. On the other hand, when the alkali ratio is less than 0.005, the dechlorination reaction does not proceed. On the other hand, when the alkali ratio exceeds 0.1, stirring and mixing of the reaction system becomes difficult. More preferably, (a) the alcohol ratio at the start of the reaction in the system (ratio of the number of moles of alcohol to the number of moles of polychlorinated biphenyls) is in the range of 10 to 1000 , and (b) the start of reaction in the system It is desirable that the alkali ratio at that time (ratio of the number of moles of alkali compound to the number of moles of alcohol) is in the range of 0.01 to 0.1.

  The ratio (molar ratio) of alkali compound / polychlorinated biphenyls is preferably 1.0 or more from the viewpoint of improving the decomposition efficiency.

  The amount of the catalyst in the reaction system is preferably 0.005 to 0.2, more preferably 0.01 to 0.15, still more preferably 0.05 to 0 as a mass ratio to the total mass of the reaction solution. .1 should be good. When the amount of catalyst is too small, the amount of hydrogen generated is small, so that dechlorination does not proceed easily. On the other hand, when the amount of catalyst is too large, the economy is inferior. Furthermore, when a catalyst is added to the reaction system, stirring and mixing of the reaction system becomes difficult.

  The output, frequency, and irradiation method of the microwave used in the present invention are not particularly limited, and may be electrically controlled so that the reaction temperature can be maintained within a predetermined range. When the output is too low, the amount of hydrogen generation is reduced, and when the output is too high, the microwave utilization rate is deteriorated. Therefore, the electric control is performed in the range of 10 W to 20 kW, and more preferably in the range of 40 W to 5 kW. Is desirable.

  Further, the irradiation position of the microwave is not particularly limited as long as the catalyst in the reaction system is irradiated, but from the viewpoint of promoting the dechlorination by increasing the catalyst activity as much as possible, It is preferred to irradiate the solution.

  The microwave frequency is preferably 1 to 300 GHz. In the frequency range below 1 GHz or above 300 GHz, the catalyst and the hydrogen donor are not sufficiently heated. More preferably, a frequency of 1 to 5 GHz is desirable. Microwave irradiation may be either continuous irradiation or intermittent irradiation. The irradiation time and the irradiation stop time can be appropriately determined according to the type of polychlorinated biphenyls to be subjected to the reaction, alcohol, reaction catalyst, or the like.

  The reaction atmosphere is more preferably carried out in an inert gas because undesirable side reactions do not occur.

  The reaction temperature needs to be 10-80 ° C. When the reaction temperature is less than 10 ° C., the decomposition reaction becomes insufficient. On the other hand, when it exceeds 80 ° C., the dechlorination reaction proceeds sufficiently, but by-products are easily generated, and the economy is inferior. From the viewpoint of balancing the suppression of side reaction products and the PCB decomposition rate, the reaction is more preferably performed at 30 to 80 ° C. and at a temperature 10 ° C. or higher (preferably 20 ° C. or higher) lower than the boiling point of the alcohol. Good.

  The reaction time is not particularly limited, and may be performed until the dechlorination reaction sufficiently proceeds.

  According to the method for dechlorinating polychlorinated biphenyls of the present invention, the polychlorinated biphenyls themselves are decomposed and dechlorinated at a speed equal to or higher than that when hydrogen gas is blown into the reaction system from the outside. Although the mechanism is not clear, it is considered that the alkali metal radical provided from the alkali compound promotes the dechlorination reaction of the polychlorinated biphenyls, and the hydrogen radical from the hydrogen donor enters therein.

  In the present invention, when polychlorinated biphenyls such as transformers are dechlorinated, the required amount is extracted and transferred to a separately prepared reaction vessel, and a hydrogen donor and an alkali compound are added to dilute to a desired polychlorinated biphenyl concentration. Above, it is preferable to perform a decomposition treatment with a catalyst. After the decomposition treatment, the treated solution is stored in a treated solution tank prepared separately.

  EXAMPLES Next, although an Example demonstrates this invention concretely, this invention is not limited only to a following example.

(Example 1)
An experiment was conducted using a simple microwave reactor temperature control type ZMW-024 manufactured by Shikoku Keiki Kogyo Co., Ltd. Four of the five-necked flasks are used as a liquid phase supply port, return port, nitrogen introduction port, and sampling port to the column in the microwave reactor, and a Dimroth condenser is provided at the center port. The reaction product was taken out of the reaction system.

  KC-1000 (KC-500 / 6/4 (mass ratio) mixture of trichlorobenzene, manufactured by Kaneka Chemical Co., Ltd.) 1.5 ml, KOH flakes 2.45 g and Wako Pure Chemical Industries isopropyl alcohol (IPA) 150 ml was stirred with a 3000 rpm homomixer for 20 minutes to give a mixed solution and introduced into the above five-necked flask having an internal volume of 200 ml. After introducing these, after replacing the inside of the flask with nitrogen gas, the mixed solution in the flask was supplied to the column in the microwave reactor at 10 ml / min while stirring the inside of the flask with a magnetic stirrer. Was circulated. The column contains 12g of granular activated carbon (trade name: Diamond Hope 008) containing 5% palladium (Pd) (average particle size of about 1mm), and the frequency of the column surface is constant at 60 ° C. Irradiation was performed for 10 hours while electrically controlling a microwave of 2.45 GHz and an output of 40 to 60 W. Nitrogen gas was allowed to flow at 50 ml / min during the reaction.

(Example 2)
The PCB was decomposed by the same operation as in Example 1 except that the amount of KOH flake used was 2.94 g.

(Example 3)
PCB was decomposed in the same manner as in Example 1 except that 4.5 ml of KC-1000 and 8.82 g of KOH flakes were used and the reaction time was 13 hours.

(Example 4)
PCB was decomposed by the same operation as in Example 1 except that 1.5 ml of KC-400 (biphenyl tetrachloride, manufactured by Kaneka Chemical Co., Ltd.) was used instead of KC-1000 used in Example 1. .

(Comparative Example 1)
PCB was decomposed by the same operation as in Example 1 except that 7.5 ml of KC-1000, 14.7 g of KOH flakes were used, and the reaction time was 22 hours.

(Comparative Example 2)
The PCB was decomposed by the same operation as in Example 1 except that the amount of KOH flake used was 0.20 g.

(Evaluation methods)
The solution before and after the reaction was subjected to a gas chromatography mass spectrometer QP5050 (hereinafter referred to as “GC-MS”) manufactured by Shimadzu Corporation using DB1 (manufactured by J & W Scientific) as a capillary column. Dechlorination (PCB decomposition rate) was confirmed.

  Table 1 summarizes the experimental conditions and evaluation results of the examples and comparative examples. From the results in Table 1, it was confirmed that PCB decomposed 99% or more even at low temperatures according to the present invention.

Claims (6)

An organic halogen compound containing 50% by mass or more of polychlorinated biphenyl, an alcohol having a boiling point of 100 ° C. or less, a column packed with at least one catalyst selected from a carbon crystal compound and a compound having a metal supported on a carrier, , while circulating a reaction solution containing an alkaline compound to a column packed with the catalyst, a dechlorination method of an organic halogen compound for irradiating a microwave to the catalyst packed column,
(A) The alcohol ratio at the start of the reaction in the system (ratio of the number of moles of alcohol to the number of moles of organic halogen compound) is in the range of 5 to 1000, and
(B) The alkali ratio at the start of the reaction in the system (ratio of the number of moles of alkali compound to the number of moles of alcohol) is in the range of 0.005 to 0.1,
A method for dechlorination of an organic halogen compound, characterized by reacting at 10 to 80 ° C. The method for dechlorination of an organic halogen compound according to claim 1, wherein the alcohol is 2-propanol. The method for dechlorination of an organic halogen compound according to claim 1 or 2, wherein the alkali compound is NaOH or KOH. The method for dechlorination of an organic halogen compound according to any one of claims 1 to 3, wherein the catalyst is a palladium-supported carbon compound. Wherein an organic halogen compound is polychlorinated biphenyls in transformer, dechlorination of said polychlorinated biphenyls, which was withdrawn from the transformer, organohalogen compounds that dechlorination by the method according to any one of claims 1-4 Method. The organic halogen compound is a polychlorinated biphenyl in a transformer, and the polychlorinated biphenyl extracted from the transformer is dechlorinated by the method according to any one of claims 1 to 5. Method.