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EP0103483A2 Expired / Lapsed EP ⏱️ 0.0 years remaining

A method of preparing modified heteropolysaccharides in buffered brine and their use for oil recovery

Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1983-09-13
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Granted: —
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Expires: 2003-09-13
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Abstract

Abstract A process for preparing modified aqueous saline heteropolysaccharide solutions containing at least 0.5 wt. % of inorganic salts wherein the solutions are stabilized against loss of pyruvate groups on heat treatment. The process comprises preparing an aqueous solution containing heteropolysaccharide and inorganic salts, adding a buffer to control pH between about 6.5 and 10.0, heating to a temperature of at least 100°C and maintaining the pH at from 6.0to 9.5 during heating, then removing cell debris. The buffered solutions do not suffer loss of pyruvate content while maintaining improved filterability and viscosity.

Inventors

  • 👤 George Michael Holzwarth

Bibliographic Details

Application Number —
Jurisdiction EP
Data Source google_patents
Last Synchronized 2026-11-09 01:38
CPC Classifications
C; C09; C09K; C09K8/00; C09K8/60; C09K8/84; C09K8/86; C09K8/88; C09K8/90; C09K8/905; C12; C12P; C12P19/00; C12P19/04; C12P19/06

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 342 words
A process for producing a heteropolysaccharide product stabilized against loss of pyruvate content, free of cell debris and having improved filterability which comprises : (a) preparing an aqueous solution which contains (i) from about 200 to about 30,000 parts per million by weight, of a heteropolysaccharide product produced by the bacterial fermentation of bacteria of the genus Xanthomonas, and (ii) at .least about 0.5 weight percent of at least one inorganic salt to obtain a saline heteropolysaccharide solution; (b) adding a buffer, said buffer being characterized by having a pH and a buffer capacity such that the saline heteropolysaccharide solution has an initial pH of about 6.5 to 10.0 and a pH of about 6.0 to 9.5 during heating; (c) heating said saline heteropolysaccharide solution to a temperature of at least about 100°C; . (d) maintaining said saline heteropolysaccharide solution at a temperature of at least about 100°Cj ( e ) maintaining said saline heteropolysaccharide at a pH of from about 6.0 to 9.5 during the heat treatment; and (f) removing or separating the proteinaceous materials and/or residual whole bacterial cells or other cell debris from the saline and heat-treated heteropolysaccharide product to thereby obtain a modified heteropolysaccharide capable of imparting a viscosity of at least 4.0 centipoises to an aqueous test solution containing 2 weight percent NaCl and 0.2 weight percent CaC1 2 when said modified heteropolysaccharide is added to said solution at a concentration of approximately 600 parts per million, by weight, as measured on a Brookfield viscosimeter with a UL adapter at 60 rpm at 25°C and said modified heteropolysaccharide is further capable of imparting a filterability such that more than 1000 ml of a different aqueous test solution containing 8.8 weight percent salt comprised of NaCl and CaCl 2 on a 10:1 weight ratio and approximately 600 parts per million concentration, by weight, of said modified heteropolysaccharide will pass without plugging through a Millipore filter having a diameter of 13 mm and a pore size of about 5 microns at a constant pressure drop of about 1.55 psig.
Claim 2
Dependent Claim 342 words
A process for producing a heteropolysaccharide product stabilized against loss of pyruvate content, free of cell debris and having improved filterability which comprises : (a) preparing an aqueous solution which contains (i) from about 200 to about 30,000 parts per million by weight, of a heteropolysaccharide product produced by the bacterial fermentation of bacteria of the genus Xanthomonas, and (ii) at .least about 0.5 weight percent of at least one inorganic salt to obtain a saline heteropolysaccharide solution; (b) adding a buffer, said buffer being characterized by having a pH and a buffer capacity such that the saline heteropolysaccharide solution has an initial pH of about 6.5 to 10.0 and a pH of about 6.0 to 9.5 during heating; (c) heating said saline heteropolysaccharide solution to a temperature of at least about 100°C; . (d) maintaining said saline heteropolysaccharide solution at a temperature of at least about 100°Cj ( e ) maintaining said saline heteropolysaccharide at a pH of from about 6.0 to 9.5 during the heat treatment; and (f) removing or separating the proteinaceous materials and/or residual whole bacterial cells or other cell debris from the saline and heat-treated heteropolysaccharide product to thereby obtain a modified heteropolysaccharide capable of imparting a viscosity of at least 4.0 centipoises to an aqueous test solution containing 2 weight percent NaCl and 0.2 weight percent CaC1 2 when said modified heteropolysaccharide is added to said solution at a concentration of approximately 600 parts per million, by weight, as measured on a Brookfield viscosimeter with a UL adapter at 60 rpm at 25°C and said modified heteropolysaccharide is further capable of imparting a filterability such that more than 1000 ml of a different aqueous test solution containing 8.8 weight percent salt comprised of NaCl and CaCl 2 on a 10:1 weight ratio and approximately 600 parts per million concentration, by weight, of said modified heteropolysaccharide will pass without plugging through a Millipore filter having a diameter of 13 mm and a pore size of about 5 microns at a constant pressure drop of about 1.55 psig.
Claim 3
Dependent Claim 21 words
A process according to .Claim 1 in which the heating in step (c) is in the range of 100 to 180°C.
Claim 4
Dependent Claim 33 words
A process according to either of claims 1 and 2 wherein the heating in step (d) is for a period of time sufficient to increase the injectivity and filterability charactersistics of the heteropolysaccharide.
Claim 5
Dependent Claim 29 words
A process according to any one of the preceding claims in which the heating in step (d) is maintained for a time period from about 30 to 300 minutes.
Claim 6
Dependent Claim 29 words
A process according to any one of the preceding claims in which the buffer is selected from sodium phosphate, potassium phosphate, imidazole, 2,4,6-trimethylpyridine, triethanolamine.Hcl, N-ethylmorpholine, sodium pyrophosphate and trii(hydroxymethyl)aminomethane.
Claim 7
Dependent Claim 24 words
A process according to any one of the preceding claims in which the inorganic salt is sodium chloride, calcium chloride or a mixture thereof.
Claim 8
Dependent Claim 23 words
A process according to any one of the preceding claims in which the inorganic salt concentration is from about 0.5 to 10 wt.X.
Claim 9
Dependent Claim 22 words
A process according to any one.of the preceding claims in which the pH is maintained in step (e) by adding additional buffer.
Claim 10
Dependent Claim 17 words
A process according to any one of the preceding claims in which the bacteria is Xanthomonas campestris.
Claim 11
Dependent Claim 64 words
The use of the product prepared by the process according to any one of the preceding claims for a crude oil recovery process, which process comprises injecting an aqueous solution of said product into a subterranean formation in an amount sufficient to provide mobility control to displace the oil from the formation, drive the displaced oil through the formation and recovering the displaced oil.

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