WO1995010484A1 - Process for decreasing chlorine content in chlorinated hydrocarbons - Google Patents
Process for decreasing chlorine content in chlorinated hydrocarbons Download PDFInfo
- Publication number
- WO1995010484A1 WO1995010484A1 PCT/US1994/011697 US9411697W WO9510484A1 WO 1995010484 A1 WO1995010484 A1 WO 1995010484A1 US 9411697 W US9411697 W US 9411697W WO 9510484 A1 WO9510484 A1 WO 9510484A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- mmol
- process according
- hours
- bis
- ether
- Prior art date
Links
Classifications
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D3/00—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances
- A62D3/30—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances by reacting with chemical agents
- A62D3/37—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances by reacting with chemical agents by reduction, e.g. hydrogenation
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D2101/00—Harmful chemical substances made harmless, or less harmful, by effecting chemical change
- A62D2101/20—Organic substances
- A62D2101/22—Organic substances containing halogen
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D2203/00—Aspects of processes for making harmful chemical substances harmless, or less harmful, by effecting chemical change in the substances
- A62D2203/04—Combined processes involving two or more non-distinct steps covered by groups A62D3/10 - A62D3/40
Definitions
- This invention pertains to a process for decreasing the content of chlorine in chlorinated hydrocarbons, and for reducing aromatic halide content in haiogenated aromatic hydrocarbons.
- chlorinated hydrocarbons such as polychlorinated biphenyls, tetrachloroethylene, trichloroethylene, 1,2,3-trichloropropane, polychlorinated naphthalene, chlorine containing fluorocarbons ("Freons"), polychlorinated cyclodienes such as aldrin and dieldrin, polychlorinated bicycloalkanes such as mirex etc., are recognized environmental contaminants. Numerous chemical, physical, and microbiological methods for eliminating these presently are under investigation.
- Bosin et al . Tetrahedron Letters , 4699-4650 (1973) report on the reduction of aryl halides with a sodium borohydride-palladium system.
- the present invention involves a method for chemically reducing the overall chlorine or halide content in compounds, generally but not necessarily chlorinated hydrocarbons or haiogenated aromatic hydrocarbons.
- the process is characterized by the ability to operate economically in a mixed ambient environment, notably in the presence of water and oxygen found in air.
- it has particular value as a pretreatment to microbiological degradation of chlorinated hydrocarbons in that highly chlorinated compounds which are resistant to bioremediation can be converted to compounds having a lower content of chlorine, thereby being more susceptible to microbiological degradation.
- the process involves bringing the chlorinated hydrocarbon into contact with a dechlorination reagent of the type described herein. Heat can be applied to accelerate the reaction.
- the dechlorination reagent contains two principal components.
- the first component of the dechlorination reagent is a metal complex having at least two oxidation states.
- the complex In a first, lower oxidation state, the complex is operable to transfer an electron to the chlorinated hydrocarbon and thereby reductively eliminate a chlorine atom from the chlorinated hydrocarbon.
- the complex In transferring the electron, the complex assumes its second, higher oxidation state; i.e., it is oxidized.
- the second component of the reagent is a reducing agent operable to reductively return the complex from its second oxidation step to its first oxidation stage; i . e. , to reduce the complex back to its original oxidation state.
- the net result of these two reactions is the consumption of the second component and the regeneration of the first component. Consequently the first component effectively acts as a catalyst in the sense that while it participates in the reduction of chlorinated hydrocarbon, it is returned to its original oxidation state in which it can enter into a further reaction. Consequently the amount of the first component which must be introduced into the environment is relatively small.
- these two components are referred to herein as a reagent or system in that they co-act, in use they can be introduced either in pre-formed combination or separately. It is critical to the process, however, that both components operate under the ambient conditions of the environment and do so without causing further contamination.
- complexes containing nickel may be technically effective as the first component in reducing chlorinated hydrocarbon but are unsuitable because the nickel of the complex thus introduced into the environment itself is toxic.
- sodium hydride and lithium aluminum hydride in theory are effective as the second component but both react with water and thus are unsuitable, being unstable in a mixed environment.
- the first component will contain a substantially nontoxic transition metal of Group 4 or 5 (IVa or Va) and will form a complex with multidentate and unidentate organic and inorganic ligands.
- a substantially nontoxic transition metal of Group 4 or 5 IVa or Va
- titanium and zirconium compounds including benzoates, chlorides, salen complexes, prophyrins, tris(pyrazoyl) borates, poly (alkylamino) complexes, poly (alkylamino) chelates, poly(thioalkyl) complexes, poly (thioalkyl) chelates, and mixtures thereof.
- organometallic complexes of titanium and zirconium such asbis-( ⁇ 5 -cyclopentadienyl)titanium dichloride, bis-( ⁇ -cyclopentadienyl)zirconium dichloride, ⁇ 5 -cyclopentadienylzirconium trichloride, and ⁇ 5 -cyclopentadienyltitanium trichloride.
- organometallic complexes of titanium and zirconium such asbis-( ⁇ 5 -cyclopentadienyl)titanium dichloride, bis-( ⁇ -cyclopentadienyl)zirconium dichloride, ⁇ 5 -cyclopentadienylzirconium trichloride, and ⁇ 5 -cyclopentadienyltitanium trichloride.
- Particularly useful in view of its currently relatively low cost and performance is bis-( ⁇ 5 -cyclopentadienyl)
- the second component will be a hydridoborate, typically a polyhydridoborate, such as an alkali metal or ammonium salt of a tetrahydridoborate, thiocyanatotrihydridoborate, cyanotrihydridoborate, acyloxytridridoborate, octahydridotrihydridoborate, trialkylhydridoborate, acetanilidotrihydridoborate, trialkoxyhydridoborate, and metal chelates thereof.
- a hydridoborate typically a polyhydridoborate, such as an alkali metal or ammonium salt of a tetrahydridoborate, thiocyanatotrihydridoborate, cyanotrihydridoborate, acyloxytridridoborate, octahydridotrihydridoborate, trialkylhydrido
- the hydridoborate may show some dechlorination properties but the rate is far slower and the range of chlorinated compounds in which such dechlorination is seen is far more limited than when the metal complex is present.
- the amine which is added can be any aliphatic amine such as trimethylamine, triethylamine, dimethylethylamine, etc. , an aromatic amine such as N,N-dimethylaniline, N,N-dimethylnaphthylamine, etc. , or an aromatic or nonaromatic heterocyclic amine such as pyridine, 1-methylimidazole, quinoline, piperidine, etc.
- primary and secondary amines can be employed, preferably the amine is a tertiary amine. Generally a molar excess of the amine is employed. While other non-amine bases such as sodium methoxide appear to have a slight effect in accelerating the underlying reaction, this is by no means as dramatic as that observed upon addition of an amine.
- the target polychlorinated hydrocarbons particularly polychlorinated aromatic compounds, often present a complex mixture of cogeners.
- the cogeners present can number in the hundreds. It thus is convenient to study the use of the present reagent with substantially pure chlorinated compounds. As shown below, the usefulness of the reagent in reducing the chlorine content of pure compounds also is seen in mixtures of chlorinated compounds.
- the haiogenated hydrocarbons on which the process is operable include haiogenated aromatic, aliphatic, and olefinic compounds such as polychlorinated biphenyls (PCB's), tetrachloroethylene, trichloroethylene, 1,2,3-trichloropropane, and the like.
- PCB's polychlorinated biphenyls
- Other functional groups such as oxo groups (ketones, carboxylic acids and esters), amino groups (including secondary and tertiary amino groups), nitro groups and the like also can be present in the compound or compounds being treated. Such if such a groups, if susceptible to reduction, may be reduced in the course of the process.
- Such products generally are equally or more amenable to bioremediation.
- the reactive intermediate generated from the chlorinated hydrocarbon can react with other organic materials present in the rection area.
- the products can include not only 1,2,4-trichlorobenzene but also N,N-dimethyl-2,4,5-trichloroaniline.
- 1,3,5-trichlorobenzene both N,N-dimethyl-3,5-dichloroaniline and 1,3-dichlorobenzene will be produced.
- the reaction to which an amine is added can be conducted in a variety of inert organic solvents such as diglyme, triglyme, bis-(2-ethoxyethyl) ether, tetrahydrofuran, dimethylsulfoxide, dimethylformamide, ethylene glycol dimethyl ether and the like.
- inert organic solvents such as diglyme, triglyme, bis-(2-ethoxyethyl) ether, tetrahydrofuran, dimethylsulfoxide, dimethylformamide, ethylene glycol dimethyl ether and the like.
- ethers such as diglyme.
- the designations used herein for the metal complexes used are as follows:
- 1,2,4,5-tetrachlorobenzene (starting compound) . . . . .0.12 trichlorobenzene . . . . . . . . . . . . . . . . . . . . . . . . . . 0.45
- 1,2,3-Trichloropropane was treated with sodium tetrahydridoborate and metal complex E at 100°C for 1 hour in substantially the fashion described above. Gas chromatography/mass spectrography indicated no 1,2,3-trichloropropane remained in the reaction mixture.
- a commercial mixture of polychlorinated biphenyls (Aroclor 1248, 3.3 parts by weight) was extracted with ether and the ether then evaporated in vacua . To the residue were added 21 parts by weight of bis-( ⁇ 5 -cyclopentadienyl)-titanium tetrahydridoborate and 1 part by volume of dimeth- ylformamide. The mixture was heated at 100°C. After a total of 18 hours, the reaction products were extracted with ether and passed through a short column of silica gel to remove the residual metal complex. Upon analysis, the reaction product contained about 40% (1.31 parts by weight) of polychlorinated biphenyls, indicating a 60% dechlorination.
- a mixture of 0.3 mmol of metal complex E and 30.0 mmol of sodium tetrahydridoborate in 30 mL of dimethylformamide was heated with stirring for 1 hour at 92°C in an air atmosphere in a reaction vessel equipped with a condenser.
- the reaction product was filtered through a Celite plug and a fine glass frit to produce the dehalogenation reagent as a dark brown solution.
- 1,2,4,5-tetrachlorobenzene is added to this solution and the mixture then heating at 92°C, it is reduced to a level below 10% in about 60-65 minutes with the formation of 1, 2 , 4-trichlorobenzene and N,N-dimethyl-2,4,5-trichloroaniline (as determined by gas chromatography/mass spectrography).
- EXAMPLE 13 A reaction vessel equipped with a condenser is charged with approximately 5 g of soil contaminated with polychlorinated biphenyls. A portion of sodium tetrahydridoborate, and 150 mg of metal complex E in dimethylformamide are added and the mixture is heated with stirring at 100°C in an air atmosphere in a reaction vessel. After 30 minutes, additional sodium tetrahydridoborate and metal complex E are added. (Any material on the walls of the vessel can be washed off with dimethylformamide.) After another 20 minutes, additional sodium tetrahydridoborate is added and the reaction mixture is stirred for 18 hours. The reaction can be quenched with water and the reaction mixture exhaustively extracted with ether (to insure partition of all chlorinated biphenyls). Analysis of the ethereal extracts is performed by gas chromatograph and compared against the untreated contaminated soils.
- the soil sample Approximately 2 to 5 g of the soil sample are placed into a 20 mL serum vial, the sample is amended with an equal volume mL/g of distilled water and to this mixture are added 10 mL of diethyl ether. The vial is sealed and shaken on a rotary shaker for 24 hours. The ether phase then is transferred to a 1.5 mL serum vial for analysis. (If needed, the original ether extract can be either concentrated or diluted to ensure accurate sample analysis.)
- Samples containing interfering substances are cleaned using appropriate methods.
- Non-PCB oils hydroaulic fluids, mineral oil, etc.
- the retained PCBs are eluted from the matrix with hexane and the wash is either diluted or concentrated for GC analysis.
- Samples which are found to contain elemental sulfur are cleaned by combining 2 mL of the sample extract with 1 mL of reagent containing 3.39 g of tetrabutylammonium hydrogen sulfate and 25 g sodium sulfite in 100 mL of water and 1 mL of 2-propanol. After mixing for five minutes, an additional 3 mL of water are added to remove the alcohol and reagent.
- the column is temperature programmed from 160°C to 200°C at 2°C/min/no hold time to 240°C at 8°C/min and held for 10 minutes.
- the gas flow rates are set as follows: carrier gas (helium) at 23 cm/sec (067 mL/min); make-up gas (nitrogen) at 33 mL/min; and a split ratio of 16.
- Chromatograms of the samples are integrated on a peak-by-peak basis and the area of each peak is normalized with respect to standard mixtures of known PCB composition.
- Figure 1 is a gas chromatrogram of soil before treatment from which Samples I and II were taken.
- the plotting attenuation is 40.
- the retention time is a function of the degree of chlorination.
- Figures 1A and 1B are gas chromatograms of Samples I and II, respectively, after dechlorination as described above.
- the plotting attenuation for Figure 1A is 21; that for Figure 1B is 31.
- Figure 2 is a gas chromatogram of Sample III before treatment. The plotting attenuation is 56.
- Figure 2A is the chromatrogram (plotting attenuation of 11) after dechlorination as described above. Again a shift in population from highly chlorinated compounds (retention time above about 30 minutes) to more lightly chlorinated compounds accompanies a reduction in overall chlorine content.
- a flask equipped with a magnetic stir bar and a water cooled condenser with an oil bubbler was charged with sodium tetrahydridoborate (568 mg, 15.0 mmol), bis-( ⁇ 5 -cyclopentadienyl) titanium dichloride (374 mg, 1.5 mmol), Aroclor ® 1248 (1095 mg, 3.75 mmol based on an average molecular formula: C 12 H 6 Cl 4 ), and N,N-dimethylacetamide (DMA; 15.0 mL).
- the flask was heated at 75°C for 10 hours and at 105°C for 4.25 hours.
- the reaction mixture was quenched with water (30 mL) and extracted with ethyl acetate (50 mL).
- 1,2,4,5-tetrachlorobenzene (648 mg, 3.0 mmol), sodium tetrahydridoborate (1135 mg, 30.0 mmol), bis-( ⁇ 5 -cyclopentadienyl) titanium dichloride (75 mg, 0.3 mmol), and 1-methyl- 2-pyrrolidine (NMP; 30.0 mL).
- the reaction mixture was heated at 96°C in an oil bath. After 4.25 hours, lithium chloride (1.09 g, 30.0 mmol) was added. Aliquots were withdrawn by syringe, quenched with water, and extracted with diethyl ether. The ether layer was analyzed with the results shown in the following table. Only trichlorobenzene was produced.
- gas mostly trimethylamine
- a sequential addition procedure can be used to maintain relatively low concentrations of sodium tetrahydridoborate in the system.
- a reaction vessel was charged with chlorinated hydrocarbons (Aroclor ® 1248), a magnetic stir bar, sodium tetrahydridoborate (0.5 g), bis-( ⁇ 5 -cyclopentadienyl)titanium dichloride (80 mg), and N,N-dimethylformamide (30.0 mL).
- the bottle was isolated by an oil bubbler and was heated to 95°C. After 1.5 hours, additional sodium tetrahydridoborate (0.5 g) was added. Gas evolution was observed immediately. After an additional two hours, 0.5 g of sodium tetrahydridoborate was added. Two more additions of sodium tetrahydridoborate (0.5 g) were conducted within 1.5 hours, and the reaction mixture was further heated for 20 minutes. The total amount of sodium tetrahydridoborate added to the reaction mixture was 2.5 g, and the reaction was heated at 95°C for 5 hours and 20 minutes. The reaction mixture was quenched with 25 mL of water and extracted with ethyl acetate (25 mL).
- the ethyl acetate layer was collected, dried over sodium carbonate, filtered through a short column of silica gel and washed with ethyl acetate. GC analysis was conducted and the efficiency of dechlorination was higher than in the case of one-time addition of sodium tetrahydridoborate.
- 1,2,4,5-tetrachlorobenzene (0.449 g, 2.1 mmol), dimethylformamide (20.0 mL) and water (0.1 mL, corresponding to 1% water in the reaction mixture).
- the reaction was heated at 85oC with the rate of reduction being shown in the following table.
- Titanocene dichloride (171 mg, 0.69 mmol), sodium tetrahydridoborate (622 mg, 16.4 mmol) and octachlorodibenzo-p-dioxin (195 mg, 0.39 mmol, 3.14 mmol C-Cl) were combined under a nitrogen atmosphere.
- bis-(2-Methoxyethyl) ether (20 ml) and pyridine (1.35 ml, 16.7 mmol) were injected under a nitrogen atmosphere.
- the reaction mixture then was heated at 125°C under a nitrogen atmosphere.
- the reaction was stopped after 3.5 hours by addition of water and the reaction mixture extracted by toluene.
- the toluene layer was purified by a short column of silica gel and analyzed by gas chromotography (GC). Octachlorodibenzo-p-dioxin was completely converted to dibenzo-p-dioxin, the only product detected by GC.
- GC gas chromotography
- Titanocene dichloride 125 mg, 0.5 mmol
- sodium tetrahydridoborate (454 mg, 12.0 mmol)
- 4-bromobiphenyl (2.33 g, 10.0 mmol) were combined in a reaction vessel under a nitrogen atmosphere.
- bis-(2-Methoxyethyl) ether (20 ml)
- pyridine 1.0 ml, 12.4 mmol
- the reaction mixture was heated at 125oC under a nitrogen atmosphere.
- An aliguot (about 1.0 1) was withdrawn by a syringe and quenched with water, and then the reaction mixture was ex..acted by diethyl ether.
- Titanocene dichloride 125 mg, 0.50 mmol
- sodium tetrahydridoborate 180 mg, 4.76 mmol
- decabromobiphenyl 300 mg, 0.318 mmol, 3.18 mmol C-Br
- bis-(2-Methoxyethyl) ether (10.0 ml)
- pyridine 0.385 ml, 4.76 mmol
- the reaction was stopped after 24 hours by addition of water, and the reaction mixture extracted by toluene.
- the toluene layer was purified on a short column of silica gel and analyzed by GC/MS. Quantitative analysis (by addition of tridecane as an internal standard) indicated biphenyl was the major reaction product.
- Titanocene dichloride 75 mg, 0.30 mmol
- sodium tetrahydridoborate 80 mg, 2.11 mmol
- 2,4,6-trichloro-p-terphenyl 15 mg, 0.045 mmol, 0.135 mmol C-Cl
- bis- (2-Methoxyethyl) ether 5.0 ml
- pyridine 0.17 ml, 2.10 mmol
- the reaction mixture was heated at 125°C under a nitrogen atmosphere and the reaction then stopped after 16 hours by addition of water.
- the reaction mixture was extracted by toluene and the toluene layer purified on a short column of silica gel.
- the starting material, 2,4,6-trichloro-p-terphenyl was found to be completely converted to p-terphenyl, the only product detected by GC/MS.
- Titanocene dichloride 75 mg, 0.30 mmol
- sodium tetrahydridoborate 80 mg, 2.11 mmol
- 1,2,3,4,-tetrachloronaphthalene 50 mg, 0.19 mmol, 0.75 mmol C-Cl
- bis-(2-Methoxyethyl) ether 5.0 ml
- pyridine 0.17 ml, 2.10 mmol
- a reaction vessel was charged with titanocene dichloride (75 mg, 0.30 mmol), sodium tetrahydridoborate (80 mg, 2.11 mmol) and octachlorodibenzofuran (30 mg, 0.068 mmol, 0.54 mmol C-Cl) under a nitrogen atmosphere.
- bis-(2-Methoxyethyl) ether (5.0 ml) and pyridine (0.17 ml, 2.10 mmol) were injected under a nitrogen atmosphere.
- the reaction mixture was heated at 125°C under a nitrogen atmosphere.
- the reaction was stopped after 16 hours by addition of water and then the reaction mixture extracted by toluene.
- the toluene layer was purified by a short column of silica gel and analyzed by GC/MS, which demonstrated that octachlorodibenzofuran was completely reduced to dibenzofuran.
- Titanocene dichloride (175 mg, 0.70 mmol), sodium tetrahydridoborate (533 mg, 14.0 mmol) and 1,1,1-trichloro-2,2-bis-(4-chlorophenyl) ethane (500 mg, 1.41 mmol, 7.05 mmol C-Cl) were mixed under a nitrogen atmosphere and bis-(2-methoxyethyl) ether (10 ml), pyridine (0.57 ml, 7.05 mmol) and N,N-dimethyloctylamine (1.44 ml, 7.00 mmol) were injected under a nitrogen atmosphere. The reaction mixture was heated at 125oC.
- Titanocene dichloride 125 mg, 0.50 mmol
- sodium tetrahydridoborate 378 mg, 10.0 mmol
- bis-(2-methoxyethyl) ether 8.0 ml
- pyridine 0.8 ml, 10.0 mmol
- tetrachloroethylene 0.2 ml, 8.00 mmol C-Cl
- Aroclor ® 1248 (1.05 gm, 14.8 mmol C-Cl, 9.3% PCB by weight).
- the soil sample was suspended in 20 ml of bis- (2- methoxyethyl) ether and heated at 125°C with titanocene dichloride (171 mg, 0.687 mmol, 0.05 equiv. per Cl), sodium tetrahydridoborate (822 mg, 21.7 mmol, 1.47 equiv. per Cl), pyridine (0.68 ml, 8.4 mmol, 0.57 equiv. per Cl) and N,N-dimethyloctylamine (1.73 ml, 8.4 mmol, 0.57 equiv. per Cl).
- a mixture containing about 50% biphenyl and about 50% 3-chlorobiphenyl was obtained after 24 hours of treatment.
- a freshly dried and spiked soil sample (10.2 gm soil, 1.02 gm Aroclor ® 1248, 14.4 mmol C-Cl, 9.1% PCB by weight) was heated at 125°C in 20 ml of bis-(2-methoxyethyl) ether in the presence of titanocene dichloride (366 mg, 1.47 mmol, 0.10 equiv. per Cl), sodium tetrahydridoborate (1.335 g, 35.28 mmol, 2.4 equiv. per Cl), pyridine (1.43 ml, 17.7 mmol, 1.2 equiv.
- a reaction vessel is charged with 171 mg (0.687 mmol) of titanocene dichloride and 622 mg (16.4 mmol) of sodium tetrahydridoborate under a nitrogen atmosphere.
- a solution of 1000 mg of Aroclor 1248, a polychlorinated biphenyl (3.43 mmol, based on an average MW 292, assuming 13.7 mmol of C-Cl functional groups), and 1.35 ml of pyridine (16.7 mmol) in 20 mL of bis-(2-methoxyethyl) ether is added.
- the reaction mixture is heated at 125°C.
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7512086A JPH09503789A (en) | 1993-10-14 | 1994-10-14 | Method for reducing chlorine content in chlorinated hydrocarbons |
BR9407819A BR9407819A (en) | 1993-10-14 | 1994-10-14 | Process for reducing the halide content of halogenated aromatic hydrocarbons by reducing the presence of a reagent |
AU79799/94A AU7979994A (en) | 1993-10-14 | 1994-10-14 | Process for decreasing chlorine content in chlorinated hydrocarbons |
EP94930779A EP0723525A4 (en) | 1993-10-14 | 1994-10-14 | Process for decreasing chlorine content in chlorinated hydrocarbons |
KR1019960701918A KR960704807A (en) | 1993-10-14 | 1994-10-14 | How to reduce the chlorine content of chlorinated hydrocarbons |
NO961482A NO961482L (en) | 1993-10-14 | 1996-04-12 | Process for reducing the chlorine content of chlorinated hydrocarbons |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/136,660 US5345031A (en) | 1992-04-16 | 1993-10-14 | Reduction of aromatic halide content |
US08/136,660 | 1993-10-15 | ||
US29005894A | 1994-08-15 | 1994-08-15 | |
US08/290,058 | 1994-08-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1995010484A1 true WO1995010484A1 (en) | 1995-04-20 |
Family
ID=26834513
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1994/011697 WO1995010484A1 (en) | 1993-10-14 | 1994-10-14 | Process for decreasing chlorine content in chlorinated hydrocarbons |
Country Status (11)
Country | Link |
---|---|
EP (1) | EP0723525A4 (en) |
JP (1) | JPH09503789A (en) |
KR (1) | KR960704807A (en) |
AU (1) | AU7979994A (en) |
BR (1) | BR9407819A (en) |
CA (1) | CA2173970A1 (en) |
CZ (1) | CZ108296A3 (en) |
IL (1) | IL111277A0 (en) |
NO (1) | NO961482L (en) |
SG (1) | SG49250A1 (en) |
WO (1) | WO1995010484A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10130108A1 (en) * | 2001-06-21 | 2003-02-27 | Birgit Kraft | Purifying water contaminated with halogenated organic compounds comprises catalytically dehalogenating the contaminants in solvent |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7754641B2 (en) * | 2008-02-14 | 2010-07-13 | General Electric Company | Hydrogen storage material and related processes |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4188346A (en) * | 1978-05-18 | 1980-02-12 | The Dow Chemical Company | Dehydrohalogenation of (polyhaloalkyl)benzenes |
US4468297A (en) * | 1983-02-25 | 1984-08-28 | Regents Of The University Of California | Degradation and detoxification of halogenated olefinic hydrocarbons |
US5004551A (en) * | 1990-06-22 | 1991-04-02 | Abb Environmental Services Inc. | Catalytic oxidation of hazardous wastes |
US5345032A (en) * | 1988-05-09 | 1994-09-06 | The Public Health Laboratory Service Board | Use of metal chelate complexes in dehalogenation |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3876711A (en) * | 1973-03-29 | 1975-04-08 | Du Pont | Selective reduction of chlorofluorobenzenes |
EP0636110A4 (en) * | 1992-04-16 | 1995-03-15 | Univ Princeton | Process for decreasing chlorine content of chlorinated hydrocarbons. |
DE59305733D1 (en) * | 1992-11-18 | 1997-04-17 | Hoechst Ag | Process for the preparation of 1,3-difluorobenzene |
-
1994
- 1994-10-13 IL IL11127794A patent/IL111277A0/en unknown
- 1994-10-14 AU AU79799/94A patent/AU7979994A/en not_active Abandoned
- 1994-10-14 JP JP7512086A patent/JPH09503789A/en active Pending
- 1994-10-14 EP EP94930779A patent/EP0723525A4/en not_active Withdrawn
- 1994-10-14 WO PCT/US1994/011697 patent/WO1995010484A1/en not_active Application Discontinuation
- 1994-10-14 CA CA002173970A patent/CA2173970A1/en not_active Abandoned
- 1994-10-14 KR KR1019960701918A patent/KR960704807A/en not_active Application Discontinuation
- 1994-10-14 SG SG1996008355A patent/SG49250A1/en unknown
- 1994-10-14 BR BR9407819A patent/BR9407819A/en not_active Application Discontinuation
- 1994-10-14 CZ CZ961082A patent/CZ108296A3/en unknown
-
1996
- 1996-04-12 NO NO961482A patent/NO961482L/en unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4188346A (en) * | 1978-05-18 | 1980-02-12 | The Dow Chemical Company | Dehydrohalogenation of (polyhaloalkyl)benzenes |
US4468297A (en) * | 1983-02-25 | 1984-08-28 | Regents Of The University Of California | Degradation and detoxification of halogenated olefinic hydrocarbons |
US5345032A (en) * | 1988-05-09 | 1994-09-06 | The Public Health Laboratory Service Board | Use of metal chelate complexes in dehalogenation |
US5004551A (en) * | 1990-06-22 | 1991-04-02 | Abb Environmental Services Inc. | Catalytic oxidation of hazardous wastes |
Non-Patent Citations (4)
Title |
---|
BULLETIN OF ENVIRONMENTAL CONTAMINATION AND TOXICOLOGY, Volume 22, No. 6, August 1979, DENNIS JR. et al., "Catalytic Dechlorination of Organochlorine Compounds V. Polychlorinated Biphenyls-Arochlor 1254", pp. 750-754. * |
J. ORG. CHEM., Volume 54, No. 21, 1989, BERGBREITER et al., "Soluble Polyethylene and Polystyrene-Bound Tin Halides as Catalysts for Reductions of Alkyl and Aryl Bromides and Lodides by Sodium Borohydride", pp. 5138-5141. * |
JOURNAL OF ORGANOMETALLIC CHEMISTRY, Volume 204, 1981, MEUNIER, "Reduction of Aromatic Halides with Sodium Borohydride Catalysed by Titanium Complexes, Unexpected Role of Air", pages 345-346. * |
See also references of EP0723525A4 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10130108A1 (en) * | 2001-06-21 | 2003-02-27 | Birgit Kraft | Purifying water contaminated with halogenated organic compounds comprises catalytically dehalogenating the contaminants in solvent |
DE10130108B4 (en) * | 2001-06-21 | 2007-11-29 | Birgit Kraft | Process and reactor for the catalytic degradation of halogenated organic pollutants |
Also Published As
Publication number | Publication date |
---|---|
BR9407819A (en) | 1997-05-06 |
NO961482L (en) | 1996-06-12 |
AU7979994A (en) | 1995-05-04 |
EP0723525A4 (en) | 1996-09-25 |
EP0723525A1 (en) | 1996-07-31 |
CA2173970A1 (en) | 1995-04-20 |
KR960704807A (en) | 1996-10-09 |
NO961482D0 (en) | 1996-04-12 |
JPH09503789A (en) | 1997-04-15 |
CZ108296A3 (en) | 1996-10-16 |
SG49250A1 (en) | 1998-05-18 |
IL111277A0 (en) | 1994-12-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Albrecht et al. | Production and dechlorination of 2, 3, 7, 8-tetrachlorodibenzo-p-dioxin in historically-contaminated estuarine sediments | |
US5994604A (en) | Method and apparatus for low temperature destruction of halogenated hydrocarbons | |
Ukisu et al. | Dechlorination of dioxins with supported palladium catalysts in 2-propanol solution | |
Mitoma et al. | Approach to highly efficient dechlorination of PCDDs, PCDFs, and coplanar PCBs using metallic calcium in ethanol under atmospheric pressure at room temperature | |
Ryu et al. | CuCl2-catalyzed PCDD/F formation and congener patterns from phenols | |
US5345031A (en) | Reduction of aromatic halide content | |
Ukisu et al. | Dechlorination of polychlorinated dibenzo-p-dioxins catalyzed by noble metal catalysts under mild conditions | |
US5608135A (en) | Process for decreasing chlorine content of chlorinated hydrocarbons | |
Brunelle et al. | Reaction removal of polychlorinated biphenyls from transformer oil: treatment of contaminated oil with poly (ethylene glycol)/potassium hydroxide | |
US5093011A (en) | Process for dehalogenation of contaminated waste materials | |
KR20090017677A (en) | Dehalogenation of aromatic halides | |
Tabaei et al. | Dehalogenation of organic compounds. 3. Dechlorination of polychlorinated biphenyls (PCBs), 4-chlorobiphenyl, and chloro-p-xylene with alkoxyborohydrides | |
Yang et al. | Catalytic detoxification of polychlorinated dibenzo-p-dioxins and polychlorinated dibenzofurans in fly ash | |
Ryu et al. | Metal-mediated chlorinated dibenzo-p-dioxin (CDD) and dibenzofuran (CDF) formation from phenols | |
WO1995010484A1 (en) | Process for decreasing chlorine content in chlorinated hydrocarbons | |
Wang et al. | Rapid transformation of 1, 2, 3, 4-TCDD by Pd/Fe catalysts | |
Kornel et al. | PCB destruction: a novel dehalogenation reagent | |
Mitoma et al. | Highly effective degradation of polychlorinated biphenyls in soil mediated by a Ca/Rh bicatalytic system | |
Múčka et al. | Radiolytic dechlorination of PCBs in presence of active carbon, solid oxides, bentonite and zeolite | |
Mackenzie et al. | Reductive destruction of halogenated hydrocarbons in liquids and solids with solvated electrons | |
Liu et al. | Thermal desorption of PCBs from contaminated soil with copper dichloride | |
Ghaffar et al. | Enhanced dechlorination of chlorobenzene compounds on fly ash: Effects of metals, solvents, and temperature | |
Zhang et al. | Dechlorination of dioxins with Pd/C in ethanol–water solution under mild conditions | |
Hinton et al. | Effect of zinc, copper, and sodium on formation of polychlorinated dioxins on MSW incinerator fly ash | |
Lee et al. | Effects of a sodium hydroxide addition on the decomposition of 2-chlorophenol in supercritical water |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AU BR CA CN CZ HU JP KR NO NZ PL RO RU UA US US VN |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FR GB GR IE IT LU MC NL PT SE |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2173970 Country of ref document: CA |
|
WWE | Wipo information: entry into national phase |
Ref document number: 275719 Country of ref document: NZ |
|
WWE | Wipo information: entry into national phase |
Ref document number: PV1996-1082 Country of ref document: CZ |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1994930779 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: 1994930779 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: PV1996-1082 Country of ref document: CZ |
|
WWW | Wipo information: withdrawn in national office |
Ref document number: 1994930779 Country of ref document: EP |
|
WWR | Wipo information: refused in national office |
Ref document number: PV1996-1082 Country of ref document: CZ |