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US5128262A Expired / Lapsed US ⏱️ 0.0 years remaining

Microbial decontamination of soils contaminated with hydrocarbons, in particular mineral oils by microbial oxidation

Assignee: Wintershall AG
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Filing: 1988-09-30
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Granted: 1992-07-07
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Expires: 2008-09-30
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Abstract

Abstract The microbial decontamination of soils contaminated with hydrocarbons, in particular with mineral oils, by microbial oxidation is improved by a process in which in addition to supplying the oxygen necessary for degradation, by aeration, soluble nutrients, water and soluble or dispersed biosurfactants as such or mixed with chemical surfactants are metered into the contaminated soils directly or into the removed contaminated soil layers, in one or more batches at time intervals, in an amount such that the formation of toxic intermediates which slow down or block microbial degradation in prevented, the accessibility of mineral oils and their products for the microorganisms is simultaneously increased and, as a result, accelerated, virtually complete mineralization by respiration to CO 2 and H 2 O is effected.

Inventors

  • 👤 Walter Lindoerfer
  • 👤 Kai-Udo Sewe
  • 👤 Axel Oberbremer
  • 👤 Reinhard Mueller-Hurtig
  • 👤 Fritz Wagner

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 06:17
CPC Classifications
C; C09; C09K; C09K3/00; C09K3/32; B; B09; B09C; B09C1/00; B09C1/10

Claims Analysis

Total Claims: 19
Claim 1
Independent Claim 49 words
In a process for the decontamination of soils contaminated with hydrocarbon which process consists essentially of aerating the soil with oxygen necessary for degradation of the hydrocarbon, adding water and surfactants, whereby the hydrocarbon is converted to carbon dioxide and water, the improvement wherein the surfactant comprises a biosurfactant.
Claim 2
Dependent Claim 49 words
In a process for the decontamination of soils contaminated with hydrocarbon which process consists essentially of aerating the soil with oxygen necessary for degradation of the hydrocarbon, adding water and surfactants, whereby the hydrocarbon is converted to carbon dioxide and water, the improvement wherein the surfactant comprises a biosurfactant.
Claim 3
Dependent Claim 31 words
The process of claim 1 wherein the surfactant comprises a mixture of (a) a biosurfactant and (b) a synthetically produced chemical surfactant in a weight ratio of from 0.1:1 to 1:1.
Claim 4
Dependent Claim 28 words
The process of claim 1 wherein the biosurfactant comprises a hydrophilic moiety containing at least one saccharide and a hydrophobic moiety containing at least one functionalized fatty acid.
Claim 5
Dependent Claim 25 words
The process of claim 3 wherein the biosurfactant is a member selected from the group consisting of trehalose dicorynomycolate, trehalose lipid triesters, and rhamnose lipids.
Claim 6
Dependent Claim 169 words
The process of claim 1, wherein the biosurfactant is (a) at least one glycolipid having the structural formula: ##STR9## wherein, in formulae I and II, the glycosidic bond 1,1; 1,2; 1,3; 1,4; 1,6 in the anomeric forms α,α; a,β; β, β and the groups R 1 to R 3 in the positions 1, 2, 3 and 4 are in the cis or trans configuration, and R 1 to R 3 are each hydroxyl, alkoxy, alkylcarbonyloxy, alkylcarboxamido or amino and R 4 is hydroxymethylene, aminomethylene, alkoxymethylene, alkylcarboxamido-N-methylene, carboxyl, carboxamido, alkoxycarbonyl or N-alkylcarboxamido, and in R 1 to R 4 the alkyl groups are the same or different and contain 8 to 60 carbon atoms or (b) a trehalose lipid tetraester of the formula ##STR10## where R 1 is ##STR11## or --OC(CH 2 ) y COOH and R 2 is ##STR12## CH 3 , where x is from 4 to 22, y is from 1 to 4 and z is from 4 to 22, and R 3 is H or alkyl.
Claim 7
Dependent Claim 73 words
The process of claim 1, wherein the biosurfactant is selected from the group consisting of (a) an anionic rhamnose lipid, 2-O-α-L-rhamnopyranosyl-α-L-rhamnopyranosyl-β-hydroxydecanoyl-β-hydroxydecanoic acid of the structural formula: ##STR13## (b) an α-L-rhamnopyranosyl-β-hydroxydecanoyl-β-hydroxydecanoic acid of the structural formula: ##STR14## (c) a rhamnolipid having a β-hydroxydecanoyl radical in the molecule (with a molecular weight of 334 or 480) of the structural formula: ##STR15## and (d) an β-L-rhamnopyranosyl-β-hydroxydecanoic acid (rhamnolipid or 2-O-α-L-rhamnopyranosyl-β-L-rhamnopyranosyl-β-hydroxydecanoic acid) of the structural formula: ##STR16##
Claim 8
Dependent Claim 38 words
The process of claim 1 wherein the contaminated soil is additionally treated with at least one bacterial nutrient which is a water-soluble salt of a compound selected from the group consisting of Na, K, Ca, Mg and Fe.
Claim 9
Dependent Claim 37 words
The process of claim 7 wherein the salt is (NH 4 ) SO 4 , MgSO 4 .7H 2 O, KCl, CaCl 2 .2H 2 O, CaCl 2 .6H 2 O or FeCl 3 .6H 2 O.
Claim 10
Dependent Claim 130 words
The process of claim 1 wherein contaminated soil layers are removed, introduced into at least one reactor and fluidized therein with water, with the addition of nutrients, at a constant temperature in the range from 10° to 40° C. and at pH of from 4 to 8 and with the addition of a surfactant which comprises an anionic or nonionic biosurfactant, with aeration of the contaminated soil layers with the natural microorganism population present therein, for rapid microbial oxidation of the hydrocarbons with formation of CO 2 and an aqueous solution to form a mixture of a solid phase and a liquid phase which contains hydrocarbon-free solid and a biomass, separating the mixture containing the solid phase and the liquid phase from the aqueous solution and removing the aqueous solution.
Claim 11
Dependent Claim 23 words
The process of claim 9 wherein the surfactant comprises a mixture of a nonionic or anionic biosurfactant and a synthetically produced chemical surfactant.
Claim 12
Dependent Claim 25 words
The process of claim 9, wherein the aeration rate is from 0.05 to 1.0 liters (S.T.P.) of air per liter of reactor volume per minute.
Claim 13
Dependent Claim 15 words
The process of claim 9 wherein the conversion is carried out in a continuous procedure.
Claim 14
Dependent Claim 31 words
The process of claim 9 wherein a plurality of reactors is used and at least one reactor is a mechanically stirred reactor and at least one reactor is a hydrodynamic reactor.
Claim 15
Dependent Claim 11 words
The process of claim 1, wherein comminuted bark is additionally added.
Claim 16
Dependent Claim 11 words
The process of claim 14 wherein the bark is pine bark.
Claim 17
Dependent Claim 19 words
The process of claim 1 wherein from 0.5 to 20 g of biosurfactant is added per kg of hydrocarbon.
Claim 18
Dependent Claim 83 words
The process of claim 1, wherein the decontamination of the soil is carried out in situ by a procedure in which compressed air in combination with surfactant composition containing at least one of a nonionic biosurfactant is sprayed as a dispersion into the contamination soil through a flexible pipeline system, which pipeline has orifices arranged at intervals, whereby the natural microorganism population present in the soil is enhanced and microbial oxidation of the hydrocarbon to CO 2 and H 2 O is accelerated.
Claim 19
Dependent Claim 16 words
The process of claim 17 wherein the surfactant composition further contains a synthetically produced chemical surfactant.

References Cited (Backward Citations)

US4146470A Cited
US4349633A Cited
US4401569A Cited
US4522261A Cited
US4814272A Cited
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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) 1995-07-07 1996-01-06 1996-07-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1999-07-07 2000-01-06 2000-07-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2003-07-07 2004-01-06 2004-07-07 $7700.00 Window Closed / Lapsed

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