US4416767A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method and apparatus for the removal of excess sodium reagent and byproducts of reaction produced during the destruction and removal of polychlorinated biphenyls from oil
Assignee: SUNOHIO Inc
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Filing: 1981-11-16
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Granted: 1983-11-22
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Expires: 2001-11-16
Abstract
Abstract A method for removing the excess sodium and byproducts of reaction which occur during the destruction of PCBs from oil. A predetermined quantity of water is mixed with the decontaminated oil and the byproducts, which include sodium chloride and polyphenyl polymer, to form sodium chloride and sodium hydroxide. Centrifuging removes most of the oil from the remaining aqueous mixture which then is agitated and treated with carbon dioxide gas to form less hazardous sodium carbonate and sodium bicarbonate. Any excess carbon dioxide gas is vented to the atmosphere and the sodium carbonate and sodium bicarbonate is collected into containers for disposal. Small amounts of oil remaining in the aqueous waste mixture that is discharged from the centrifuge is decanted from the remaining material in a waste separator due to its lighter specific gravity. A pump intermittently injects waste from the waste separator into a converter where it reacts with the carbon dioxide gas. A corresponding amount of the treated waste is ejected from the converter and collected in waste containers. A releif valve on the discharge end of the converter is adjusted to a valve lower than a check valve in the carbon dioxide gas incoming line to ensure a sufficient supply of gas in the converter. A pump continuously agitates and recirculates the waste material in the converter to ensure a thorough mixing and reaction with the carbon dioxide gas.
Inventors
- 👤 Otis D. Jordan
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 07:39
CPC Classifications
C; C10; C10G; C10G29/00; C10G29/04; B; B01; B01D; B01D17/00; B01D17/02; C02; C02F; C02F1/00; C02F1/66; C02F2101/00; C02F2101/30; C02F2101/36; C02F2101/363; Y; Y10; Y10S; Y10S210/00; Y10S210/902; Y10S210/908; Y10S210/909
Claims Analysis
Total Claims: 21
Claim 1
Independent Claim
170 words
A method for the continuous removal of an excess sodium reagent and byproducts of reaction produced during the destruction and separation of polychlorinated biphenyl from a contaminated transformer oil in which said byproducts include sodium chloride and polyphenyl polymer, said method including the steps of: (a) providing a continuous flow of the decontaminated oil containing the excess sodium reagent and byproducts of reaction produced during the destruction of the polychlorinated biphenyl in the contaminated transformer oil; (b) continuously mixing a predetermined quantity of water with the oil, sodium reagent and byproducts to form an aqueous mixture containing oil, sodium hydroxide and sodium chloride, said quantity of water being continuously sufficient to convert all of the excess sodium to sodium hydroxide and to dissolve and hold in solution said sodium hydroxide; (c) continuously supplying said aqueous mixture to a centrifuge; (d) continuously removing the separated oil from the centrifuge; and (e) removing the waste aqueous mixture remaining in the centrifuge after removal of the oil from the centrifuge for subsequent disposal.
Claim 2
Independent Claim
170 words
A method for the continuous removal of an excess sodium reagent and byproducts of reaction produced during the destruction and separation of polychlorinated biphenyl from a contaminated transformer oil in which said byproducts include sodium chloride and polyphenyl polymer, said method including the steps of: (a) providing a continuous flow of the decontaminated oil containing the excess sodium reagent and byproducts of reaction produced during the destruction of the polychlorinated biphenyl in the contaminated transformer oil; (b) continuously mixing a predetermined quantity of water with the oil, sodium reagent and byproducts to form an aqueous mixture containing oil, sodium hydroxide and sodium chloride, said quantity of water being continuously sufficient to convert all of the excess sodium to sodium hydroxide and to dissolve and hold in solution said sodium hydroxide; (c) continuously supplying said aqueous mixture to a centrifuge; (d) continuously removing the separated oil from the centrifuge; and (e) removing the waste aqueous mixture remaining in the centrifuge after removal of the oil from the centrifuge for subsequent disposal.
Claim 3
Dependent Claim
55 words
The method defined in claim 1 including the steps of injecting the waste aqueous mixture from the centrifuge into a converter chamber; agitating the removed waste mixture in the converter chamber; and injecting carbon dioxide gas into the agitated waste mixture converting most of the sodium hydroxide contained therein into sodium carbonate and sodium bicarbonate.
Claim 4
Dependent Claim
41 words
The method defined in claim 2 including the step of removing the sodium carbonate, sodium bicarbonate, sodium hydroxide and sodium chloride contained in the aqueous waste mixture from the converter chamber and storing the same in a container for subsequent disposal.
Claim 5
Dependent Claim
45 words
The method defined in claim 3 including the step of maintaining the pressure of the carbon dioxide gas being injected into the agitated waste mixture at a higher pressure than the pressure at which the waste mixture is removed from the converter chamber for storage.
Claim 6
Dependent Claim
49 words
The method defined in claim 2 including the step of separating and removing any traces of oil from the waste aqueous mixture after its removal from the centrifuge in a waste separator prior to agitating the waste mixture and mixing it with carbon dioxide gas in the converter chamber.
Claim 7
Dependent Claim
32 words
The method defined in claim 5 including the step of injecting the removed traces of oil from the waste aqueous mixture back into an incoming supply of oil and byproducts before centrifuging.
Claim 8
Dependent Claim
20 words
The method defined in claim 5 in which the traces of oil are removed from the waste separator by decanting.
Claim 9
Dependent Claim
31 words
The method defined in claim 2 including the step of venting to the atmosphere any carbon dioxide gas which does not mix with the waste aqueous mixture in the converter chamber.
Claim 10
Dependent Claim
22 words
The method defined in claim 2 in which approximately 99% of the waste products are separated from the oil in the centrifuge.
Claim 11
Dependent Claim
150 words
Apparatus for the continuous removal of excess sodium reagent and the byproducts of reaction from decontaminated oil produced during the continuous destruction and removal of polychlorinated biphenyl from contaminated oil, including: (a) means for continuously mixing a predetermined quantity of water with the decontaminated oil, excess sodium reagent and byproducts to form an aqueous mixture containing oil, sodium hydroxide and sodium chloride; (b) centrifuging means for continuously separating the oil from the aqueous mixture and returning it for reuse, and for periodically discharging the remaining waste materials; (c) a supply of carbon dioxide gas; (d) means for mixing the carbon dioxide gas from the supply of said gas with the periodically discharged waste materials which remain after the oil has been removed therefrom to form less harmful byproducts; and (e) means for collecting and storing the less harmful byproducts produced from mixing the waste materials with the carbon dioxide gas.
Claim 12
Dependent Claim
150 words
Apparatus for the continuous removal of excess sodium reagent and the byproducts of reaction from decontaminated oil produced during the continuous destruction and removal of polychlorinated biphenyl from contaminated oil, including: (a) means for continuously mixing a predetermined quantity of water with the decontaminated oil, excess sodium reagent and byproducts to form an aqueous mixture containing oil, sodium hydroxide and sodium chloride; (b) centrifuging means for continuously separating the oil from the aqueous mixture and returning it for reuse, and for periodically discharging the remaining waste materials; (c) a supply of carbon dioxide gas; (d) means for mixing the carbon dioxide gas from the supply of said gas with the periodically discharged waste materials which remain after the oil has been removed therefrom to form less harmful byproducts; and (e) means for collecting and storing the less harmful byproducts produced from mixing the waste materials with the carbon dioxide gas.
Claim 13
Dependent Claim
27 words
The apparatus defined in claim 10 in which separator means receives the waste materials from the centrifuging means for removing any oil remaining in said waste materials.
Claim 14
Dependent Claim
63 words
The apparatus defined in claim 11 in which the separator means is a vessel having a hollow interior; in which an inlet opening is formed in an upper portion of the vessel and an outlet opening is formed in a lower portion of the vessel; and in which an oil discharge opening is formed in said vessel intermediate the inlet and outlet openings.
Claim 15
Dependent Claim
29 words
The apparatus defined in claim 12 in which baffle means is mounted within the hollow interior of the vessel beneath the inlet opening for diffusing the incoming waste materials.
Claim 16
Dependent Claim
37 words
The apparatus defined in claim 12 in which pump means operatively communicates with the oil discharge opening of the separator means for removing the oil from said separator means and injecting it back into the centrifuging means.
Claim 17
Dependent Claim
35 words
The apparatus defined in claim 12 in which pump means operatively communicates with the outlet opening of the separator means for transferring the remaining waste materials from the separator means to the gas mixing means.
Claim 18
Dependent Claim
37 words
The apparatus defined in claim 11 in which the gas mixing means includes a hollow container for receiving the remaining waste materials from the centrifuge means and pump means for agitating the waste materials with the gas.
Claim 19
Dependent Claim
83 words
The apparatus defined in claim 16 in which pressure-regulating check valve means is mounted between the gas mixing means and the supply of gas for regulating the pressure of the incoming gas; in which relief valve means is mounted between the gas mixing means and the byproduct collecting and storing means for regulating the pressure at which the byproducts leave the gas mixing means; and in which the pressure-regulating check valve means is set to a higher pressure than the relief valve means.
Claim 20
Dependent Claim
44 words
The apparatus defined in claim 16 in which the gas mixing means is formed of stainless steel and has a baffle mounted in an upper portion thereof to provide opening means to affect the flow of the agitated aqueous mixture from said mixing means.
Claim 21
Dependent Claim
36 words
The apparatus defined in claim 10 including a pump and a supply of water; and in which the pump injects the predetermined quantity of water from said water supply into the oil and byproducts of reaction.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1986-11-21 | 1987-05-23 | 1987-11-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-11-21 | 1991-05-23 | 1991-11-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-11-21 | 1995-05-23 | 1995-11-22 | $7700.00 | Window Closed / Lapsed |