CN101875839B - Multifunctional preparation for controlling biological corrosion and blockage of oil field production system - Google Patents

Multifunctional preparation for controlling biological corrosion and blockage of oil field production system Download PDF

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CN101875839B
CN101875839B CN 200910083124 CN200910083124A CN101875839B CN 101875839 B CN101875839 B CN 101875839B CN 200910083124 CN200910083124 CN 200910083124 CN 200910083124 A CN200910083124 A CN 200910083124A CN 101875839 B CN101875839 B CN 101875839B
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20ppm
sodium
oil field
inhibitor
corrosion
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CN101875839A (en
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关密生
朱志宏
向廷生
韩红雁
杜文军
冯业庆
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Petrochina Co Ltd
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Petrochina Co Ltd
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Abstract

The invention relates to a multifunctional preparation for controlling biological corrosion and blockage of an oil field production system, which comprises the following components in percentage by weight in treated water: and (3) bactericide: glutaraldehyde, acrolein, dodecyl dimethyl benzyl amine chloride or dodecyl dimethyl benzyl amine bromide 20-200 ppm; inhibitor (B): sodium nitrate or sodium nitrite: 10-100 ppm; and/or 10-20ppm of sodium molybdate, sodium tungstate or lithium molybdate; corrosion inhibitor: imidazoline quaternary ammonium salt 10-20 ppm; or/and a sulfur removal agent: 20-50ppm of trihydroxymethyl nitromethane; and/or penetrant: 10-20ppm of alkylphenol polyoxyethylene ether; the components generate synergistic action, so that the concentration of a single component is obviously reduced by 25-90%, and the SRB killing efficiency is over 90%.

Description

The multifunctional preparation of control oil field development system biological corrosion and obstruction
Technical field
The present invention relates to a kind of multifunctional preparation of controlling oil field development system biological corrosion and obstruction.
Background technology
Microorganism generally is divided into anaerobion and aerobic microbiological in the oil-field flooding, and anaerobion mainly is sulphate reducing bacteria, anaerobically fermenting bacterium, methanogen and denitrifying bacteria, and aerobic microbiological mainly is hydrocarbon oxidation bacterium, iron bacteria and saprophytic microorganism.To oil field flood pattern and the generation microbiological corrosion obstruction of water filling stratum mainly is sulphate reducing bacteria, iron bacteria and saprophytic microorganism.As long as there is the oxygen saprophytic microorganism of trace just can breed, just there is where bacterial slime to exist saprophytic microorganism, the crude oil in this mucus and the mud, corrosion product, dirt stick together and form the bacterium foundry loam, are attached on pipeline and the equipment.Easily form anaerobic environment under the foundry loam, SRB begins breeding, produces the hydrogen sulfide corrosion metal, and forms Fe with the iron reaction 2S 3, stop up duct and down-hole facility.
The method of at present oil field solution sulfate reducing bacteria corrosion mainly is to adopt chemical means directly to kill SRB.But because the sterilant that adopts is difficult to penetrate microbial film and dirt, can only kill the free SRB in the water, so low and oil field equipment is still corroded to the kill efficiency of SRB.Large for the chemical agent toxicity of directly killing SRB at present, life-time service is contaminate environment not only, also easily produces resistance, the sterilant kind that only continues to increase dosage and more renew.Present technological method is not in time removed the hydrogen sulfide and the Iron sulfuret that form, still can produce Corrosion blockage to stratum and underground equipment.
Summary of the invention
The purpose of this invention is to provide a kind of multifunctional preparation of controlling sulfate reducing bacteria corrosion and obstruction.According to the physical condition of field produces, relate to sterilant, sulfur elimination, permeate agent, inhibiter and metabolic poison and acting synergistically, thereby effectively the hydrogen sulfide that produced by sulphate reducing bacteria of control is to corrosion and the fouling of oil field development system facility.The method is applicable to hydrocarbon-bearing pool reservoir, producing well and water injection well, oil field gathering and transportation pipe network and Produced Liquid ground processing facility.
The present invention controls corrosion and stops up multifunctional preparation and mainly is comprised of sterilant and metabolic poison, is aided with simultaneously permeate agent, sulfur elimination and inhibiter, thereby reaches 25-90% so that these components generation synergies obviously reduce single concentration of component.
The present invention adopts non oxidizing bactericide.Suitable non oxidizing bactericide comprises, for example aldehydes (such as formaldehyde, glutaraldehyde or propenal), amine (such as dodecyl dimethyl benzyl amine bromide, poly-nitrogen heterocyclic quaternary amine, poly-quaternary ammonium salt, diquaternary amine salt or dodecyl dimethyl benzyl ammonia chloride), halogenated compound (such as bronopol and DBNPA), sulfide (such as isothiazolinone and metronidazole).
The metabolic poison that the present invention is suitable for comprises such as nitrate (such as SODIUMNITRATE, Jing Ti/Bao Pian COBALT NITRATE CRYSTALS/FLAKES, nickelous nitrate, cupric nitrate, nitrocalcite etc.), nitrite, molybdate (such as Sodium orthomolybdate and lithium molybdate), tungstate, selenate or anthraquinone.
The sulfur elimination that the present invention is suitable for comprises the metallic compound (such as copper carbonate, zinc subcarbonate, ferric oxide) that mainly contains copper, zinc and iron.
The applicable inhibiter of the present invention has lipid acid amine salt, amine, acid amides, quaternary amine, tetrahydroglyoxaline, pyridine, polymeric amide.
The applicable permeate agent of the present invention mainly is comprised of nonionogenic tenside, can comprise the mixture of fatty alcohol-polyoxyethylene ether, alkylphenol polyoxyethylene or multiple nonionogenic tenside.The weight content of each functional preparation in processing water is as follows:
Sterilant: glutaraldehyde, propenal, dodecyl dimethyl benzyl ammonia chloride or dodecyl dimethyl benzyl amine bromide 20-200ppm;
Inhibitor: SODIUMNITRATE or Sodium Nitrite: 10-100ppm; And/or Sodium orthomolybdate, sodium wolframate or lithium molybdate 10-20ppm;
Inhibiter: tetrahydroglyoxaline quaternary amine 10-20ppm;
Or/and sulfur elimination: trishydroxymethylnitromethane 20-50ppm;
Or/and permeate agent: alkylphenol polyoxyethylene 10-20ppm.
Sterilant of the present invention and the inhibitor working concentration in oil field flood pattern will depend on water quality and the adding mode thereof of oilfield injection water.Generally can adopt and add continuously or batch process.From economic point of view, adopt intermittent type to process to be preferably method.The employed sterilant of the method and inhibitor concentration should remain on 50-100ppm, and medicament is minimum in system will to continue 4-8 hour.In reality was implemented, the batch process cycle was 1 time or two all 1 time weekly, and its efficient of killing SRB reaches more than 90%.Usually continuously process that add total cost than regularly high, generally by every day the 10-30ppm chemical feeding quantity process continuously.
The effect of invention.
(1) eliminated biogenetic H 2S pollutes, thereby has reduced widely H 2S corrodes production system, and the iron sulphide of having eliminated reservoir and equipment stops up.Reduce Infrastructure and the anticorrosion expense of production unit.The preparation of various functions plays synergy, kills more thorough for the sulphate reducing bacteria of absorption.
(2) carry out tertiary oil recovery with possible minimum overseas crude oil cost.Treatment formulations and reservoir salt compatible.Processing will not damage reservoir or production system.
(3) for the production of hydrocarbons environment, can reduce transportation and use has the sterilization chemical agent.
(4) operation on the oil field, the practical and easy operation of method.
(5) kept the value of sweet oil gas.
Embodiment
Embodiment 1
At the test initial stage, the weight content of each functional preparation in processing water is as follows:
1) sterilant: glutaraldehyde or dodecyl dimethyl benzyl ammonia chloride 20-200ppm;
2) inhibitor: SODIUMNITRATE: 10-100ppm; With Sodium orthomolybdate or sodium wolframate 10-20ppm;
3) inhibiter: tetrahydroglyoxaline quaternary amine 10-20ppm
4) sulfur elimination: trishydroxymethylnitromethane 20-50ppm
5) permeate agent: alkylphenol polyoxyethylene 10-20ppm
Be combined in by above-mentioned preparation with various functions and concur when the oil field is brought into use, can
Improve sterilant and inhibitor and kill the effect of SRB, and eliminate existing sulfide and stop up.
Embodiment 2
Different from example 1, propenal has the function of sterilization and sulphide removal, so multifunctional preparation also can adopt following composition.
The weight content of each functional preparation in processing water is as follows:
(1) sterilant: propenal or dodecyl dimethyl benzyl amine bromide 20-200ppm;
(2) inhibitor: Sodium Nitrite: 10-100ppm; With Sodium orthomolybdate or lithium molybdate 10-20ppm;
(3) inhibiter: tetrahydroglyoxaline quaternary amine 10-20ppm
(4) permeate agent: alkylphenol polyoxyethylene 10-20ppm
Embodiment 3
(such as 3 months) after for some time are carried out in test, adjust the content of each functional preparation in good time, can reach production requirement, save cost.The concentration of sterilant can reduce by 50%, and inhibitor is cheap, and its concentration then can double.Density of corrosion inhibitor can reduce 50%.
The weight content of each functional preparation in processing water is as follows:
(1) sterilant: glutaraldehyde or dodecyl dimethyl benzyl ammonia chloride 20-100ppm;
(2) inhibitor: Sodium Nitrite: 50-100ppm; With Sodium orthomolybdate or lithium molybdate 10-20ppm;
(3) inhibiter: tetrahydroglyoxaline quaternary amine 10ppm
Embodiment 4
After half a year is carried out in test, can further reduce the consumption of each functional preparation.
The weight content of each functional preparation in processing water is as follows:
(1) sterilant: glutaraldehyde or dodecyl dimethyl benzyl ammonia chloride 20-50ppm;
(2) inhibitor: SODIUMNITRATE: 10-50ppm; Sodium Nitrite: 50-100ppm; With Sodium orthomolybdate or lithium molybdate 10-20ppm;
(3) inhibiter: tetrahydroglyoxaline quaternary amine 10ppm
The dosing method continous way of above-mentioned example or intermittent type add in re-injection water system or wellhead of water injection well, and add-on is determined according to injection allocation amount or the production fluid amount of on-the-spot re-injection water.
Also can in the annular space of recovery well, add the equipment corrosion in the production control well.The dosing cycle is 7-14 days.Chemical feeding quantity is calculated according to individual well production fluid every day amount.Be 100m such as individual well production fluid amount 3, require that effective concentration is 50ppm in the production fluid, then need sterilant 5kg; SODIUMNITRATE 5kg; Sodium Nitrite 5kg; Keep inhibiter 10ppm concentration, then need the 1kg medicament.Above-mentioned medicament all calculates by 100% effective concentration
Embodiment 5
Add from recovery well, pharmaceutical quantities can suitably strengthen.It is composed as follows:
1) sterilant: glutaraldehyde or dodecyl dimethyl benzyl ammonia chloride 20-200ppm;
2) inhibitor: Sodium Nitrite: 10-100ppm; With Sodium orthomolybdate or sodium wolframate 10-20ppm;
3) inhibiter: tetrahydroglyoxaline quaternary amine 10-20ppm
4) sulfur elimination: trishydroxymethylnitromethane 20-50ppm
5) permeate agent: alkylphenol polyoxyethylene 10-20ppm
Embodiment 6
Inject 3 composition and the consumptions that can suitably adjust medicament after taking turns by embodiment 5.It is composed as follows:
1) sterilant: propenal or dodecyl dimethyl benzyl ammonia chloride 20-200ppm;
2) inhibitor: Sodium Nitrite: 10-100ppm;
3) inhibiter: polymeric amide 10-20ppm

Claims (1)

1. multifunctional preparation of controlling oil field development system biological corrosion and obstruction is characterized in that: the weight content of each functional preparation in processing water is as follows
Sterilant: glutaraldehyde, propenal, dodecyl benzyl dimethyl ammonium chloride or dodecyl dimethyl benzyl ammonium bromide 20-200ppm;
Inhibitor: SODIUMNITRATE or Sodium Nitrite: 10-100ppm; With Sodium orthomolybdate, sodium wolframate or lithium molybdate 10-20ppm;
Inhibiter: tetrahydroglyoxaline quaternary amine 10-20ppm;
Sulfur elimination: trishydroxymethylnitromethane 20-50ppm;
Permeate agent: alkylphenol polyoxyethylene 10-20ppm.
CN 200910083124 2009-04-30 2009-04-30 Multifunctional preparation for controlling biological corrosion and blockage of oil field production system Active CN101875839B (en)

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