SU1090264A3 - Emulsifier for preparing microemulsions - Google Patents
Emulsifier for preparing microemulsions Download PDFInfo
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- SU1090264A3 SU1090264A3 SU782640396A SU2640396A SU1090264A3 SU 1090264 A3 SU1090264 A3 SU 1090264A3 SU 782640396 A SU782640396 A SU 782640396A SU 2640396 A SU2640396 A SU 2640396A SU 1090264 A3 SU1090264 A3 SU 1090264A3
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- SU
- USSR - Soviet Union
- Prior art keywords
- surfactant
- emulsifier
- microemulsions
- water
- microemulsion
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- 239000004530 micro-emulsion Substances 0.000 title claims abstract description 20
- 239000003995 emulsifying agent Substances 0.000 title claims description 10
- 239000004094 surface-active agent Substances 0.000 claims abstract description 25
- 239000000203 mixture Substances 0.000 claims abstract description 10
- 150000003839 salts Chemical class 0.000 claims abstract description 6
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 12
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 5
- 229930195729 fatty acid Natural products 0.000 claims description 5
- 239000000194 fatty acid Substances 0.000 claims description 5
- 150000004665 fatty acids Chemical class 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 235000013162 Cocos nucifera Nutrition 0.000 claims description 4
- 244000060011 Cocos nucifera Species 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims description 3
- 150000007513 acids Chemical class 0.000 claims description 3
- 125000000217 alkyl group Chemical group 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 150000001875 compounds Chemical class 0.000 claims description 2
- 239000008398 formation water Substances 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 13
- 229930195733 hydrocarbon Natural products 0.000 abstract description 6
- 150000002430 hydrocarbons Chemical class 0.000 abstract description 6
- 239000004215 Carbon black (E152) Substances 0.000 abstract description 5
- 239000002280 amphoteric surfactant Substances 0.000 abstract description 3
- 239000003208 petroleum Substances 0.000 abstract description 2
- 125000004432 carbon atom Chemical group C* 0.000 abstract 1
- MWKFXSUHUHTGQN-UHFFFAOYSA-N decan-1-ol Chemical compound CCCCCCCCCCO MWKFXSUHUHTGQN-UHFFFAOYSA-N 0.000 abstract 1
- 125000000816 ethylene group Chemical group [H]C([H])([*:1])C([H])([H])[*:2] 0.000 abstract 1
- SNRUBQQJIBEYMU-UHFFFAOYSA-N Dodecane Natural products CCCCCCCCCCCC SNRUBQQJIBEYMU-UHFFFAOYSA-N 0.000 description 9
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N hexan-1-ol Chemical compound CCCCCCO ZSIAUFGUXNUGDI-UHFFFAOYSA-N 0.000 description 6
- 150000001298 alcohols Chemical class 0.000 description 5
- 239000003921 oil Substances 0.000 description 5
- KBPLFHHGFOOTCA-UHFFFAOYSA-N caprylic alcohol Natural products CCCCCCCCO KBPLFHHGFOOTCA-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000005755 formation reaction Methods 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N n-Octanol Natural products CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000003643 water by type Substances 0.000 description 2
- 241000761389 Copa Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 241000283903 Ovis aries Species 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 239000003945 anionic surfactant Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 125000005586 carbonic acid group Chemical group 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/58—Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
- C09K8/584—Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids characterised by the use of specific surfactants
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Cosmetics (AREA)
- Detergent Compositions (AREA)
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
- Extraction Or Liquid Replacement (AREA)
- Liquid Carbonaceous Fuels (AREA)
- Colloid Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Description
Изобретение относитс к разработке нефт ных месторождений с применением микроэмульсий дл пластов с высокой минерализацией пластовых вод. Известно получение микрозмульсий дистиллированной водой и углеводорода , содержащих поверхностно-актив ное вещество и соповерхностно-актив ные вещества р . Известен эмульгатор дл приготов лени микроэмульсий, используемых дл извлечени нефти на основе ПАВ котензида (соповерхностно-активног вещества) Г2. Недостатком известных микроэмуль вл етс то, что оба эти типа поверхностно-активных ионитов реагируют в среде высококонцентрированно соли с риском выпасть в осадок, сил но адсорбиру сь на минеральных частицах . Цель изобретени - повьшение ста бильности микроэмульсии при повышен ном содержании солей в пластовых во дах. Поставленна цель достигаетс те что эмульгатор дл приготовлени микроэмульсий, используемых дл извлечени нефти на основе ПАВ и котензида, в качестве ПАВ он содерж соединение общей формулы СНг-СООКа где R - алкильна цепочка с распределением углеродов, соответ ствующим жирным кислотам ко ра, кислотам с углеродными цепочками от С;, до С , а объемное соотношение ПАВ к котензиду составл ет 1:(О,5-4,5). В качестве котензида используют смесь И-гексанола, н -октанола и изопропанола. Амфотерное ПАВ, принадлежащее к группе алкилбетаинов, -амфозоль может быть представлено следующей общей формулой R-N-CHj-COgNa СНт 41 где R - ёлкильный остаток жирной кислоты копра. Жирные кислоты копра представл ют собой смесь кислот с разной длиной цепи от С до С вес.%: Cj7,8-9,5 ,5-9,7 44-51 13-18,5 ,5-10,5 (насьпценна ) 1-3 (ненасыщенна ) 6-10,8 Соповерхностно-активные вещества выбирают из группы спиртов с в зависимости от их коэффициента распределени между водой и углеводородной составл ющей микроэмульсии. Дл исследовани стабильности микроэмульсий готов т смеси, включающие амфотерное поверхностно-активное вещество; соповерхностно-активные вещества, имеющие строение спиртов; углеводород: сыра нефть петролейна фракци - газойль - кеосин или очищенна фракци сырой нефти или ,сжиженный газ; воду, соержащую одно- или двухвалентные ионы с концентрацией, превосход щей 60 г/л. Дп сравнени образовани микромульсий в соленой среде берут эмульгатор с классическим анионным ПАВ. Эмульгатор (1), содержащий ПАВ Нз B-N-CH2-C02lfaCl, де R -Су((} (жирные кислоты копа ) , котензид,%: Изопропанол72 н-Гексанол14 н-Октанол14 Эмульгатор (2), содержащий ПАВ аурилсульфонат натри , котензида,%: Изопропанол 72 Н-Гексанол 14 Н-Октанол14 асло-додекан. В табл.1 представлены результаты табильности микроэмульсии с маслом сильно соленой среде, особенно в рисутствии двухвалентных ионов даже ри высокой температуре. На фиг. 1-4 представлены двойные иаграммы: де С - поверхностно-активное вещество и .соповерхностно-активное вещество; Е - вода из месторождени ; Р - углеводород. Кажда построенна раздел к ца крива показьтает, что выше нее рас положена область гомогенных растворов или микроэмульсий, а под ней область многофазного состава. Пр и м е р 1. Вода из месторож дени , содержаща 200 г/л NaCfc; мас ло - додекан и ПАВ со строением алкилбетаина , где R - радикал копра в водном растворе, содержащем 25% активного вещества и 18% изопропанола; соповерхностно-активные вещес ва представлены н -гексанолом и Н-октанолом, смешанные в объемном соотношении 50-50. Объемное отношение ПАВ к котензиду варьируетс от 0,1 до 1,5, предпочтительно в интервале 0,5-1,0 Микроэмульсию готов т как просту смесь из воды месторождени , додека на как углеводорода, смеси ПАВ и котензида. Крива на диаграмме (фиг.1) показьюает , что можно получить обширную гамму микроэмульсий из воды из месторождений с 200 г NaC на литр додекана, устойчивых во времени и при 80 С. Пример 2. Тройна диаграмм ( фиг.2) определ ет область существо вани микроэмульсий, образованных и воды с 100 г/л СаСС додекана И теми же системами ПАВ и спиртов, ко торые описаны в примере 1. Пример 3. Диаграмма (фиг.З) определ ет область существовани микроэмульсий, образованных из воды со средним содержанием солей 60 г/л NaCt и 15 г/л CaCl, додекана и смеси амфозоли в водном 35%-ном растворе с изопропанолом и гексанолом , смешанными в объемных соотношени х 1/3 - 2/3. Соотношение ПАВ/спирты варьируют от 0,25 до 4,5. Устойчивость микроэмульсий так же хороша, как ив предыцупщх случа х. Пример 4. Диаграмма (фиг.4) определ ет область существовани устойчивых микроэмульсий и устойчивость к нагреву, получение которых возможно из воды из месторождени с высоким содержанием солей 100 г/л NaCt и 20 г/л CaCl,додекана и системы ПАВ - спирты, указанные в примере 3. Объемное соотношение ПАВ/спиртов составл ет 0,30-4,50. Ниже привод тс составы микроэмульсий соответственно примерам 1-4. В табл.2 привод т весовые проценты точек, расположенных на кривой расслоени раствора дл соответствующих максимальных ионных сил. Таким образом, 0lкpoэмyльcии, приготовленные с применением указанного эмульгатора, вл ютс устойчивыми при сильно минерализованной воде и повышенной пластовой температуре . Таблица 1The invention relates to the development of oil fields using microemulsions for formations with high salinity of formation waters. It is known to obtain micro-emulsions with distilled water and hydrocarbons containing surfactant and co-surfactants p. A known emulsifier for the preparation of microemulsions used to extract oil based on coenzide surfactant (co-surfactant) is G2. A disadvantage of the known microemul is that both of these types of surface-active ion exchangers react in a highly concentrated salt medium with the risk of precipitating, but are adsorbed on the mineral particles. The purpose of the invention is to increase the stability of a microemulsion with an elevated salt content in reservoir waters. This goal is achieved by the fact that the emulsifier for the preparation of microemulsions used to extract oil on the basis of surfactant and codenside, as a surfactant, it contains a compound of the general formula CHg-COOKa where R is an alkyl chain with carbon distribution corresponding to fatty acids of carbon, acids with carbonic acids chains from C ;, to C, and the volume ratio of surfactant to codenside is 1: (O, 5-4.5). A mixture of i-hexanol, n-octanol and isopropanol is used as a coenzide. An amphoteric surfactant belonging to the group of alkyl betaines, α-amphosol can be represented by the following general formula R-N-CHj-COgNa CHt 41 where R is the residual residue of copra fatty acid. Copra fatty acids are a mixture of acids with different chain lengths from C to C wt.%: Cj7.8-9.5, 5-9.7 44-51 13-18.5, 5-10.5 (exemplary) 1-3 (unsaturated) 6-10.8 The surfactants are selected from the group of alcohols with, depending on their distribution coefficient between the water and the hydrocarbon component of the microemulsion. To study the stability of microemulsions, mixtures are prepared that include an amphoteric surfactant; co-surfactants having the structure of alcohols; hydrocarbon: crude oil, petroleum fraction - gas oil - keosin, or refined crude oil fraction, or liquefied gas; water containing mono- or divalent ions with a concentration greater than 60 g / l. For comparison of the formation of micromulsions in saline media, take an emulsifier with a classical anionic surfactant. Emulsifier (1) containing surfactant Hz BN-CH2-C02lfaCl, de R-Su ((} (copa fatty acids), codenzide,%: Isopropanol 72 n-Hexanol 14 n-Octanol 14 Emulsifier (2) containing surfactant sodium auryl sulfonate, codenzide, %: Isopropanol 72 N-Hexanol 14 H-Octanol14 Aslo-dodecane Table 1 shows the results of microamulsion stability with oil in a highly salty medium, especially in the presence of divalent ions even at high temperatures. C is a surfactant and a surfactant; E is water from a deposit; P - hydrocarbon. Each built-up section to the curve shows that the area of homogeneous solutions or microemulsions is located above it, and the area of multiphase composition below it. Ex. 1. Water from the field site containing 200 g / l of NaCfc; - dodecane and surfactants with the alkylbetaine structure, where R is the copra radical in an aqueous solution containing 25% of the active substance and 18% isopropanol; the co-surfactant substances are n-hexanol and H-octanol mixed in a 50-50 volume ratio. The volume ratio of surfactant to codenzide varies from 0.1 to 1.5, preferably in the range of 0.5-1.0. The microemulsion is prepared as a simple mixture of field water, a dodec as a hydrocarbon, a mixture of surfactant and codenside. The curve in the diagram (figure 1) shows that it is possible to obtain an extensive range of microemulsions from water from fields with 200 g of NaC per liter of dodecane that are stable in time and at 80 C. Example 2. The triple diagram (figure 2) defines the region of existence microemulsions formed and water with 100 g / l of SASS dodecane AND the same systems of surfactants and alcohols described in example 1. Example 3. The diagram (Fig. 3) defines the region of existence of microemulsions formed from water with an average salt content 60 g / l NaCt and 15 g / l CaCl, dodecane and mixtures of amphosol in an aqueous 35% plant thief with isopropanol and hexanol mixed in 1/3 - 2/3 volume ratios. The ratio of surfactant / alcohols vary from 0.25 to 4.5. The stability of microemulsions is as good as in previous cases. Example 4. The diagram (figure 4) defines the region of existence of stable microemulsions and resistance to heat, which can be obtained from water from a deposit with a high salt content of 100 g / l NaCt and 20 g / l CaCl, dodecane and surfactant system - alcohols, as indicated in Example 3. The surfactant / alcohols volume ratio is 0.30-4.50. The following are the compositions of microemulsions according to examples 1-4. Table 2 lists the weight percentages of points located on the solution splitting curve for the corresponding maximum ionic forces. Thus, lambs prepared using this emulsifier are resistant to highly saline water and elevated reservoir temperature. Table 1
58,958.9
0.50.5
1one
33
4.54.5
60,860,8
0,50.5
1one
33
4,54.5
8080
200200
f + + ff + + f
ff
100100
Таблица 2table 2
8,658,932,58,658,932,5
22.238,639,222.238,639.2
31.323,345,431,323,345,4
49.415,934,749,415,934,7
57.54,837,757.54,837,7
9,160,830,19,160,830,1
21,537,640,921,537,640,9
32.824,642,6 45,314,640,132,824,642,6 45,314,640,1
54.94,640,554.94,640,5
Продолжение табл. 1Continued table. one
ЭмульгаторEmulsifier
Продолжение табл. 2Continued table. 2
10,067,422,610,067,422,6
27.747,225,1 37,027,036,027.747,225.1 37.027.036.0
49.615,734,7 59,34,835,949,615,734,7 59,34,835,9
10,768,520,810,768,520,8
28.846,924,328.846,924.3
39.7.27,632,7 51,515,533,0 60,34,735,039.7.27,632.7 51,515,533.0 60.34,735.0
Claims (2)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR7721093A FR2396866B1 (en) | 1977-07-08 | 1977-07-08 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU1090264A3 true SU1090264A3 (en) | 1984-04-30 |
Family
ID=9193155
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU782640396A SU1090264A3 (en) | 1977-07-08 | 1978-07-07 | Emulsifier for preparing microemulsions |
Country Status (14)
| Country | Link |
|---|---|
| JP (1) | JPS5437002A (en) |
| BE (1) | BE868821A (en) |
| BR (1) | BR7804406A (en) |
| CA (1) | CA1106587A (en) |
| DE (1) | DE2829617C2 (en) |
| DK (1) | DK306478A (en) |
| FR (1) | FR2396866B1 (en) |
| GB (1) | GB2001377B (en) |
| IT (1) | IT1096925B (en) |
| NL (1) | NL7807384A (en) |
| NO (1) | NO149859C (en) |
| OA (1) | OA06005A (en) |
| RO (1) | RO83822B (en) |
| SU (1) | SU1090264A3 (en) |
Families Citing this family (22)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3025383C2 (en) * | 1980-07-04 | 1982-05-13 | Th. Goldschmidt Ag, 4300 Essen | Use of mixtures of betaines or amine oxides and polyoxyethylene esters of naphthenic acids in oil production |
| US4479894A (en) * | 1981-02-09 | 1984-10-30 | Mobil Oil Corporation | Oil recovery by surfactant-alcohol waterflooding |
| US4370243A (en) * | 1981-02-09 | 1983-01-25 | Mobil Oil Corporation | Oil recovery by surfactant-alcohol waterflooding |
| US4502540A (en) * | 1981-06-01 | 1985-03-05 | Mobil Oil Corporation | Tertiary oil recovery |
| EP0077947B1 (en) * | 1981-10-22 | 1985-08-07 | Harry Dr. Distler | Application of amine-sulphur-dioxide adducts and sulfitobetaines as bactericides against sulfate reducing bacteria |
| DE3143362A1 (en) * | 1981-11-02 | 1983-05-11 | Basf Ag, 6700 Ludwigshafen | Use of sulphitobetaines as bactericides against sulphate-reducing bacteria |
| DE3431414A1 (en) * | 1984-08-27 | 1986-02-27 | Hoechst Ag, 6230 Frankfurt | MOBILITY CONTROL OF GAP, SLOT OR PORE FLOWS |
| US4976315A (en) * | 1989-11-06 | 1990-12-11 | Texaco Inc. | Use of taurine additives in enhanced oil recovery with anionic surfactants |
| US5376397A (en) * | 1993-05-06 | 1994-12-27 | Kraft General Foods, Inc. | Microemulsions of oil and water |
| US7220709B1 (en) | 1999-08-26 | 2007-05-22 | Bj Services Company | Process of diverting stimulation fluids |
| US6432885B1 (en) * | 1999-08-26 | 2002-08-13 | Osca, Inc. | Well treatment fluids and methods for the use thereof |
| US6509301B1 (en) | 1999-08-26 | 2003-01-21 | Daniel Patrick Vollmer | Well treatment fluids and methods for the use thereof |
| US6608005B2 (en) * | 2000-04-07 | 2003-08-19 | Schlumberger Technology Corporation | Wellbore fluids and their application |
| AU2001256023A1 (en) * | 2000-05-03 | 2001-11-12 | Trican Well Service Ltd. | Fracturing fluid |
| US7943554B2 (en) | 2006-06-26 | 2011-05-17 | Bp Exploration Operating Company Limited | Wellbore fluid comprising at least one polymer containing pendant alkyl groups |
| MX346963B (en) | 2012-09-21 | 2017-03-07 | Inst Mexicano Del Petróleo | Process for preparing a micro emulsion for improving the flow of heavy hydrocarbons. |
| CN110382661A (en) * | 2017-03-09 | 2019-10-25 | 沙特阿拉伯石油公司 | Nanometer surfactant for improving and intensified oil reduction is applied |
| US11084972B2 (en) | 2017-03-09 | 2021-08-10 | Saudi Arabian Oil Company | Surface charge modified nanosurfactants for reduced retention by reservoir rock |
| US11066594B2 (en) | 2017-03-09 | 2021-07-20 | Saudi Arabian Oil Company | Fluoropolymers to reduce retention of nanosurfactants to carbonate reservoir rock for applications in oil fields |
| US11066914B2 (en) | 2017-03-09 | 2021-07-20 | Saudi Arabian Oil Company | Foam from low cost petroleum sulfonate surfactants for fracturing along with wettability alteration |
| US11078405B2 (en) | 2017-03-09 | 2021-08-03 | Saudi Arabian Oil Company | 3 in 1 foam formulation for enhanced oil recovery including conformance control, ultra-low interfacial tension, and wettability alteration |
| CN113717008B (en) * | 2021-08-13 | 2022-10-14 | 四川鸿康科技股份有限公司 | Monoammonium phosphate anti-caking agent and application thereof |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3275552A (en) * | 1963-04-23 | 1966-09-27 | Milchem Inc | Well treating composition and method |
| US3939911A (en) * | 1975-03-14 | 1976-02-24 | Texaco Inc. | Surfactant oil recovery process usable in high temperature formations containing water having high concentrations of polyvalent ions |
| US4008165A (en) * | 1975-03-14 | 1977-02-15 | Texaco Inc. | Surfactant oil recovery process usable in high temperature formations having high concentrations of polyvalent ions |
| DE2532469C3 (en) * | 1975-07-19 | 1978-10-12 | Institut Fuer Erdoelforschung, 3000 Hannover | Use of betaines in oil production |
| DE2600779C2 (en) * | 1976-01-10 | 1986-08-28 | Degussa Ag, 6000 Frankfurt | Use of betaines |
| DE2600778C2 (en) * | 1976-01-10 | 1985-01-03 | Henkel KGaA, 4000 Düsseldorf | Use of betaines in oil production |
-
1977
- 1977-07-08 FR FR7721093A patent/FR2396866B1/fr not_active Expired
-
1978
- 1978-07-05 DE DE2829617A patent/DE2829617C2/en not_active Expired
- 1978-07-05 GB GB787828866A patent/GB2001377B/en not_active Expired
- 1978-07-06 OA OA56555A patent/OA06005A/en unknown
- 1978-07-06 RO RO94583A patent/RO83822B/en unknown
- 1978-07-06 JP JP8249078A patent/JPS5437002A/en active Pending
- 1978-07-07 NL NL7807384A patent/NL7807384A/en unknown
- 1978-07-07 CA CA307,003A patent/CA1106587A/en not_active Expired
- 1978-07-07 BE BE189137A patent/BE868821A/en not_active IP Right Cessation
- 1978-07-07 DK DK783064A patent/DK306478A/en unknown
- 1978-07-07 NO NO782390A patent/NO149859C/en unknown
- 1978-07-07 SU SU782640396A patent/SU1090264A3/en active
- 1978-07-07 BR BR7804406A patent/BR7804406A/en unknown
- 1978-07-10 IT IT25480/78A patent/IT1096925B/en active
Non-Patent Citations (1)
| Title |
|---|
| 1. Патент US № 4192755, кл. Е 21 В 43/22, опублик. 1980. 2. Патент US № 3644499, кл. С 07 С 143/02, опублик. 1972. * |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5437002A (en) | 1979-03-19 |
| NL7807384A (en) | 1979-01-10 |
| CA1106587A (en) | 1981-08-11 |
| RO83822A (en) | 1984-04-02 |
| OA06005A (en) | 1981-06-30 |
| DK306478A (en) | 1979-01-09 |
| GB2001377B (en) | 1982-01-20 |
| NO782390L (en) | 1979-01-09 |
| GB2001377A (en) | 1979-01-31 |
| NO149859B (en) | 1984-03-26 |
| IT1096925B (en) | 1985-08-26 |
| BE868821A (en) | 1978-11-03 |
| DE2829617A1 (en) | 1979-01-18 |
| DE2829617C2 (en) | 1982-02-11 |
| BR7804406A (en) | 1979-03-13 |
| NO149859C (en) | 1984-07-04 |
| RO83822B (en) | 1984-04-30 |
| FR2396866A1 (en) | 1979-02-02 |
| IT7825480A0 (en) | 1978-07-10 |
| FR2396866B1 (en) | 1982-10-08 |
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