CN105112037B - A kind of room temperature sulphur solvent and preparation method thereof - Google Patents

A kind of room temperature sulphur solvent and preparation method thereof Download PDF

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Publication number
CN105112037B
CN105112037B CN201510556480.4A CN201510556480A CN105112037B CN 105112037 B CN105112037 B CN 105112037B CN 201510556480 A CN201510556480 A CN 201510556480A CN 105112037 B CN105112037 B CN 105112037B
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sulphur
solvent
catalyst
room temperature
sulfur
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CN105112037A (en
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毛金成
杨小江
李勇明
赵金洲
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Southwest Petroleum University
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Southwest Petroleum University
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/52Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning
    • C09K8/528Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning inorganic depositions, e.g. sulfates or carbonates
    • C09K8/532Sulfur
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/54Compositions for in situ inhibition of corrosion in boreholes or wells
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17DPIPE-LINE SYSTEMS; PIPE-LINES
    • F17D1/00Pipe-line systems
    • F17D1/02Pipe-line systems for gases or vapours
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K2208/00Aspects relating to compositions of drilling or well treatment fluids
    • C09K2208/20Hydrogen sulfide elimination
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K2208/00Aspects relating to compositions of drilling or well treatment fluids
    • C09K2208/32Anticorrosion additives

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
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Abstract

The invention discloses efficient sulphur solvents of a kind of novel normal-temperature and preparation method thereof, belong to oil gas field chemical agent field, and the present invention is by with RNH2The primary amine class of structure is host agent, is configured according to a certain percentage with the co-catalyst with heterocyclic molecular structure with inorganic base catalyst, you can obtain the primary amine class sulphur solvent suitable for high sulfur Gas Fields.It is an advantage of the invention that the sulfur solubility of the sulphur solvent is high, solution rate is fast, ordorless, at low cost, non-corrosive and room temperature is easy to operate, molten more than the sulphur 0.8g of 1g solvents at normal temperatures, time is only 1.26min, hence it is evident that better than the molten sulphur effect of existing amine sulphur solvent.

Description

A kind of room temperature sulphur solvent and preparation method thereof
Technical field
The invention belongs to field of oilfield chemistry, and in particular to a kind of novel normal-temperature efficient sulphur solvent and preparation method thereof.
Background technology
The unconventional acid gas reservoir of a batch has now been found both at home and abroad, such gas reservoir in the process of development, can generate one kind Harmful substance is called elementary sulfur (i.e. S8).With the change of environmental condition, elementary sulfur will in the form of sulphur crystalline solid, from It condensation and is deposited in air-flow.Easily deposition causes sulphur to block to elementary sulfur in payzone, pit shaft and gathering system, especially causes The blocking of gas transmission line brings great harm to the exploitation of such gas reservoir, this problem in the exploitation of acid gas reservoir urgently It is to be solved.So it is to solve the problems, such as this fabulous selection to develop efficient sulphur solvent.
Since the eighties, the research to sulphur solvent has been begun to both at home and abroad, wherein external mainly with Canadian, the U.S. DMDS (dimethyl disulfide) sulfur solvent systems are representative, and early 20th century, domestic Li Li, Liu Jianyi et al. carries out the system Further research obtains the DMDS sulfur solvent systems of higher performance, but DMDS is expensive, high volatility, irritant Foul odour, strong toxicity.
CS without DMDS2(carbon disulfide) although molten sulphur effect is fine, its is toxic, burning point is low, explosive, seldom makes With although other amines, benzene series class and alcohols sulphur solvent also have certain molten sulphur ability, the sulfur solubility at 30 DEG C No more than 30%, and molten sulphur speed is slow, dosage is big, and relative cost is high.
Sulfur solubility of the best DMDS systems of generally acknowledged sulfur solubility at 25 DEG C is 173.6% at present, at 90 DEG C Sulfur solubility for 610.9%, but not only irritant stench, toxicity are big, stability is poor, and expensive, sexual valence by DMDS Than low.
2008, triethylene tetramine, ethanol amine, ethylene glycol were carried out 2 by Liu Jingcheng et al.:2:1 compounding, complex solvent have Higher sulfur solubility, sulphur solution rate is also very fast, but the system corrosivity is stronger.
Huang Xue pine et al. developed a kind of ordorless, small toxicity suitable for high sulfur Gas Fields in 2013, without strong thorn Swash the sulphur solvent of property smell, which is compounded by diethylenetriamine, DMF (dimethylformamide), although the system ratio Liu Jing into et al. exploitation triethylene tetramine system sulfur solubility and molten sulphur speed it is all high, but sulfur solubility only has 40.25% ~49.90%, sulfur solubility still cannot meet actual requirement, and triethylene tetramine and diethylenetriamine have very strong corruption Corrosion is serious to pipeline corrosion.
Invention content
The present invention in view of the above problems, develop new normal-temperature efficient, low-corrosiveness amine sulphur solvent and A kind of new and effective sulphur solvent and preparation method thereof is provided, this sulphur solvent is ordorless, at low cost, non-corrosive, sulfur solubility Height, solution rate is fast and room temperature is easy to operate.
The present invention adopts the following technical scheme that:
The present invention provides a kind of new and effective sulphur solvent, by the material composition of following mass parts:
50-80 parts of main solvent;
1-5 parts of catalyst;
1-5 parts of co-catalyst.
The main solvent for ethamine, n-propylamine, isopropylamine, n-butylamine, isobutyl amine, tert-butylamine, aniline, benzylamine, alpha-naphthylamine, The mixture of one or more of beta-naphthylamine.
The catalyst is the mixture of one or both of NaHS, potassium bisulfide.
The co-catalyst is mainly the mixture of one or more of pyridine, piperidines, pyrimidine, quinoline, isoquinolin, institute The big pi bond structure that stating co-catalyst has can interact with S8 rings, it is promoted to be dissolved by host agent.
The present invention also provides a kind of methods for preparing the sulphur solvent, include the following steps:
(1) a certain amount of main solvent is added in into reaction vessel in ventilation;
(2) catalyst (the 1.0% of main solvent quality) is added in, is stirred;
(3) co-catalyst (the 2.0% of main solvent quality) is added in, stirs to obtain normal-temperature efficient sulphur solvent.
Beneficial effects of the present invention:
(1) amine solvent used in the system is not only without corrosivity, also with certain antisepsis, and without evil It is smelly, at low cost, sulfur solubility is high, solution rate is fast;
(2) system is compounded by amine solvent and a kind of catalyst, a kind of co-catalyst, sulfur solubility considerably beyond The conventional sulphur solvent for being free of DMDS, under normal temperature condition, sulfur solubility can reach more than 80%, i.e. 1g solvents can dissolve 0.8g Above sulphur reaches 1.6 times or more of the sulphur solvent sulphur solvability without DMDS at present;
(3) the big pi bond structure that co-catalyst has can and S8Ring interacts, and makes the sulphur solution rate of the system significantly It improves, the sulphur solution rate of unit solvent can reach 0.78g/min, overcome conventional without DMDS sulphur solvent sulphur solution rates The shortcomings that slow.
Description of the drawings
The present invention will be further described in detail below with reference to the accompanying drawings and specific embodiments.
Fig. 1 is sulfur solubility in one~embodiment of the embodiment of the present invention five with catalyst variation diagram;
Fig. 2 is sulphur solution rate in one~embodiment of the embodiment of the present invention five with catalyst variation diagram;
Fig. 3 is sulfur solubility in six~embodiment of the embodiment of the present invention ten with co-catalyst variation diagram;
Fig. 4 is sulphur solution rate in six~embodiment of the embodiment of the present invention ten with co-catalyst variation diagram.
Specific embodiment
Below in conjunction with the attached drawing in the embodiment of the present invention, the technical solution in the embodiment of the present invention is carried out clear, complete Site preparation describes, it is clear that described embodiment is only part of the embodiment of the present invention, instead of all the embodiments.It is based on Embodiment in the present invention, those of ordinary skill in the art are obtained every other without creative efforts Embodiment shall fall within the protection scope of the present invention.
Embodiment one:
(25 DEG C or so) take 50 parts of main solvent agent to add in reaction vessel at room temperature, then add in 0 part of catalyst, stirring Uniformly, 0 part of co-catalyst is added, continues to stir evenly, is uniformly mixing to obtain sulphur solvent, sublimed sulfur is added in and carries out dissolving distillation Sulfur powder is tested, and records dissolution time, tests the molten sulphur speed of sulphur solvent, as a result such as attached drawing 1,2.
Experimental method and step:
Experiment carries out under atmospheric pressure, certain temperature, and sublimed sulfur (chemistry is pure) powder that quality is M0 is added to quality For in the sulphur solvent of M, the mixed liquor of sulphur and sulphur solvent is poured into equipped with matter after magnetic stirring apparatus rotating speed 250r/min, fully dissolving It measures and is filtered in the filter paper funnel for M1, and filter paper is rinsed with the tetrahydrofuran under relevant temperature, it then at low temperature will be on filter paper The liquid drying in face, until constant mass, is recorded as M2, and the molten sulphur time is recorded as T, and the sulphur of sulphur solvent is calculated using difference assay Solubility C=(M0-M1-M2)/M, sulphur solution rate is calculated using the method for average, by the sulfur capacity of unit interval unit mass solvent It demarcates, C=(M0-M1-M2)/M/T。
Embodiment two:
(25 DEG C or so) take 50 parts of main solvent agent to add in reaction vessel at room temperature, then add in 0.25 part of catalyst, It stirs evenly, adds 0 part of co-catalyst, continue to stir evenly, be uniformly mixing to obtain sulphur solvent, add in sublimed sulfur and dissolved Sublimed sulfur powder Experiment, and dissolution time is recorded, the molten sulphur speed of sulphur solvent is tested, as a result such as attached drawing 1,2.
Experimental method and step are identical with embodiment one.
Embodiment three:
(25 DEG C or so) take 50 parts of main solvent agent to add in reaction vessel at room temperature, then add in 0.5 part of catalyst, stir It mixes uniformly, adds 0 part of co-catalyst, continue to stir evenly, be uniformly mixing to obtain sulphur solvent, add in sublimed sulfur and carry out dissolving liter Magnificent sulfur powder experiment, and dissolution time is recorded, the molten sulphur speed of sulphur solvent is tested, as a result such as attached drawing 1,2.
Experimental method and step are identical with embodiment one.
Example IV;
(25 DEG C or so) take 50 parts of main solvent agent to add in reaction vessel at room temperature, then add in 1 part of catalyst, stirring Uniformly, 0 part of co-catalyst is added, continues to stir evenly, is uniformly mixing to obtain sulphur solvent, sublimed sulfur is added in and carries out dissolving distillation Sulfur powder is tested, and records dissolution time, tests the molten sulphur speed of sulphur solvent, as a result such as attached drawing 1,2.
Experimental method and step are identical with embodiment one.
Embodiment five:
(25 DEG C or so) take 50 parts of main solvent agent to add in reaction vessel at room temperature, then add in 2 parts of catalyst, stirring Uniformly, 0 part of co-catalyst is added, continues to stir evenly, is uniformly mixing to obtain sulphur solvent, sublimed sulfur is added in and carries out dissolving distillation Sulfur powder is tested, and records dissolution time, tests the molten sulphur speed of sulphur solvent, as a result such as attached drawing 1,2.
Experimental method and step are identical with embodiment one.
Embodiment six:
(25 DEG C or so) take 50 parts of main solvent agent to add in reaction vessel at room temperature, then add in 0.5 part of catalyst, stir It mixes uniformly, adds 0.125 part of co-catalyst, continue to stir evenly, be uniformly mixing to obtain sulphur solvent, it is molten to add in sublimed sulfur progress Sublimed sulfur powder Experiment is solved, and records dissolution time, tests the molten sulphur speed of sulphur solvent, as a result such as attached drawing 3,4.
Experimental method and step are identical with embodiment one.
Embodiment seven:
(25 DEG C or so) take 50 parts of main solvent agent to add in reaction vessel at room temperature, then add in 0.5 part of catalyst, stir It mixes uniformly, adds 0.25 part of co-catalyst, continue to stir evenly, be uniformly mixing to obtain sulphur solvent, it is molten to add in sublimed sulfur progress Sublimed sulfur powder Experiment is solved, and records dissolution time, tests the molten sulphur speed of sulphur solvent, as a result such as attached drawing 3,4.
Experimental method and step are identical with embodiment one.
Embodiment eight;
(25 DEG C or so) take 50 parts of main solvent agent to add in reaction vessel at room temperature, then add in 0.5 part of catalyst, stir It mixes uniformly, adds 0.5 part of co-catalyst, continue to stir evenly, be uniformly mixing to obtain sulphur solvent, add in sublimed sulfur and dissolved Sublimed sulfur powder Experiment, and dissolution time is recorded, the molten sulphur speed of sulphur solvent is tested, as a result such as attached drawing 3,4.
Experimental method and step are identical with embodiment one.
Embodiment nine:
(25 DEG C or so) take 50 parts of main solvent agent to add in reaction vessel at room temperature, then add in 0.5 part of catalyst, stir It mixes uniformly, adds 1 part of co-catalyst, continue to stir evenly, be uniformly mixing to obtain sulphur solvent, add in sublimed sulfur and carry out dissolving liter Magnificent sulfur powder experiment, and dissolution time is recorded, the molten sulphur speed of sulphur solvent is tested, as a result such as attached drawing 3,4.
Experimental method and step are identical with embodiment one.
Embodiment ten:
(25 DEG C or so) take 50 parts of main solvent agent to add in reaction vessel at room temperature, then add in 0.5 part of catalyst, stir It mixes uniformly, adds 2 parts of co-catalyst, continue to stir evenly, be uniformly mixing to obtain sulphur solvent, add in sublimed sulfur and carry out dissolving liter Magnificent sulfur powder experiment, and dissolution time is recorded, the molten sulphur speed of sulphur solvent is tested, as a result such as attached drawing 3,4.
Experimental method and step are identical with embodiment one.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all essences in the present invention With within principle, any modification, equivalent replacement, improvement and so on should all be included in the protection scope of the present invention god.

Claims (3)

1. a kind of room temperature sulphur solvent, it is characterised in that:By the material composition of following mass parts:
50-80 parts of main solvent;
1-5 parts of catalyst;
1-5 parts of co-catalyst;
The main solvent be primary amine solvent, including ethamine, n-propylamine, isopropylamine, n-butylamine, isobutyl amine, tert-butylamine, aniline, The mixture of one or more of benzylamine, alpha-naphthylamine, beta-naphthylamine;
The catalyst is the mixture of one or both of NaHS, potassium bisulfide;
The co-catalyst is mainly the mixture of one or more of pyridine, piperidines, pyrimidine, quinoline, isoquinolin.
2. a kind of room temperature sulphur solvent according to claim 1, it is characterised in that:The big pi bond knot that the co-catalyst has Structure can and S8Ring interacts, it is promoted to be dissolved by host agent.
A kind of 3. method for preparing any room temperature sulphur solvent in claim 1~2, it is characterised in that:Including following step Suddenly:
(1) main solvent is added in into reaction vessel in ventilation;
(2) catalyst is added in, is stirred;
(3) co-catalyst is added in, stirs to obtain room temperature sulphur solvent.
CN201510556480.4A 2015-09-02 2015-09-02 A kind of room temperature sulphur solvent and preparation method thereof Expired - Fee Related CN105112037B (en)

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Publication number Priority date Publication date Assignee Title
CN115505380B (en) * 2021-06-23 2024-02-20 中国石油化工股份有限公司 Composition with sulfur dissolving function without pungent odor, and preparation method and application thereof
CN115505379B (en) * 2021-06-23 2024-02-09 中国石油化工股份有限公司 Low-viscosity composition with sulfur dissolving function and preparation method and application thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN86101929A (en) * 1985-03-25 1986-09-24 埃尔夫·阿奎坦国营公司 Alkyl polysulfide is degraded to the method for the horizontal polysulfide of low-sulfur
US5180572A (en) * 1991-11-19 1993-01-19 Marathon Oil Company Conversion of hydrogen sulfide to sulfur and hydrogen
CN102408885A (en) * 2011-10-14 2012-04-11 西南石油大学 Efficient sulfur solving agent for sulfur deposits in sulfur-containing gas well

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN86101929A (en) * 1985-03-25 1986-09-24 埃尔夫·阿奎坦国营公司 Alkyl polysulfide is degraded to the method for the horizontal polysulfide of low-sulfur
US5180572A (en) * 1991-11-19 1993-01-19 Marathon Oil Company Conversion of hydrogen sulfide to sulfur and hydrogen
CN102408885A (en) * 2011-10-14 2012-04-11 西南石油大学 Efficient sulfur solving agent for sulfur deposits in sulfur-containing gas well

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
适用于高含硫气藏开采运输过程中沉积硫溶解的硫溶剂研究;王红娟;《中国优秀硕士学位论文全文数据库 工程科技I辑》;20130315;B019-183页 *

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