US3249535A - Method of retarding paraffin clogging in petroleum containers - Google Patents

Method of retarding paraffin clogging in petroleum containers Download PDF

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US3249535A
US3249535A US293245A US29324563A US3249535A US 3249535 A US3249535 A US 3249535A US 293245 A US293245 A US 293245A US 29324563 A US29324563 A US 29324563A US 3249535 A US3249535 A US 3249535A
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carbon atoms
petroleum
paraffin
retarding
oil
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US293245A
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Joseph W Keil
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Dow Silicones Corp
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Dow Corning Corp
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Priority to NL122510D priority Critical patent/NL122510C/xx
Application filed by Dow Corning Corp filed Critical Dow Corning Corp
Priority to US293245A priority patent/US3249535A/en
Priority to DK245464AA priority patent/DK107962C/en
Priority to ES300018A priority patent/ES300018A1/en
Priority to NL6405600A priority patent/NL6405600A/xx
Priority to CH701564A priority patent/CH457280A/en
Priority to FR976852A priority patent/FR1397716A/en
Priority to GB25518/64A priority patent/GB1004685A/en
Priority to DED44811A priority patent/DE1232897B/en
Priority to AT576864A priority patent/AT251157B/en
Priority to BE650206D priority patent/BE650206A/xx
Application granted granted Critical
Publication of US3249535A publication Critical patent/US3249535A/en
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    • 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
    • C09K8/52—Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning
    • C09K8/524—Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning organic depositions, e.g. paraffins or asphaltenes
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/04—Polysiloxanes
    • C08G77/22—Polysiloxanes containing silicon bound to organic groups containing atoms other than carbon, hydrogen and oxygen
    • C08G77/26—Polysiloxanes containing silicon bound to organic groups containing atoms other than carbon, hydrogen and oxygen nitrogen-containing groups
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/28—Organic compounds containing silicon
    • C10L1/285—Organic compounds containing silicon macromolecular compounds
    • E—FIXED CONSTRUCTIONS
    • E21—EARTH OR ROCK DRILLING; MINING
    • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B37/00—Methods or apparatus for cleaning boreholes or wells
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S507/00—Earth boring, well treating, and oil field chemistry
    • Y10S507/927—Well cleaning fluid
    • Y10S507/929—Cleaning organic contaminant
    • Y10S507/931—Organic contaminant is paraffinic

Definitions

  • This invention relates to a method of preventing or re tarding parafiin build up on the walls of petroleum conduits or containers, thereby reducing or preventing clogging.
  • the objective of applicants; invention is to prevent or retard the deposition of paraffin in petroleum conduits and containers.
  • This invention can be used to prevent deposition ⁇ on the walls of containers and conduits with other solutions, suspensions, dispersions and emulsions than crude oil.
  • This invention represents a substanital stride in the techniques of coping with paraflin in piping. It prevents parafiin deposition and saves "many man-hours of labor, when compared with the various paraflin-removal techniques. 1
  • plastic-coated pipe It is an advance over plastic-coated pipe in that it can be used in the well itself; it can be easily applied to, pipe that is already in place and operating; and it can be much cheaper.
  • Y is a molecule of a monovalent aliphatic carboxylic acid or cycloaliphatic carboxylic acid of from 1 to 10 carbon atoms, and a has a value from 0 to a value equal to the number of N atoms in 1) and from 99.75 to 90 mol percent, siloxane units of the formula 3 ASiO where A is a monovalent hydrocarbon radical with from 1 through 3 carbon atoms.
  • the term consisting essentially of means that the copolymer is substantially as described but it can contain small amounts of other siloxane units which do not materially affect the property of retarding paraffin deposition.
  • This copolymer can be made in the following Way:
  • Y need not be present (1.e., a may equal 0) in order for the copolymer to be useful 1n applicants invention, nor, if it is present, is it necessary for every amine group to have a Y added to it.
  • R can be any alkyl or alicyclic radical such as methyl, decyl, isobutyl, cyclohexyl, cyclopentyl, methylcyclohexyl, or octadecyl; or R can be any aminoalkyl radi etc.
  • the Y group can consist of any of the defined carboxylic acids such as formic acid, acetic acid, isobutyric
  • the material that is used by this invention is a silox'ane copolymer consisting essentially of from 0.25 to 10 mol percent, siloxane units of the formula Rf".
  • n is an integer of a value from 0 through 2
  • R is a hydrogen, alkyl, alicyclic, or aminoalkyl group
  • R is a divalent hydrocarbon that separates the N and the Si atoms by at least three carbon atoms
  • R" is a monovalent hydroacid, decanoic acid
  • cyclohexyl carboxylic acid 4-methylcyclohexylcarboxylic acid, acrylic acid, methacrylic acid, butynoic acid, vinylacetic acid, crotoni c acid, and CH CH(CH )-;COOH.
  • R has from 1 through 10 carbon atoms.
  • the R" group can be any of the defined radicals such as methyl, hexyl, isopropyl,
  • the A group can be methyl, ethyl, propyl, isopropyl, vinyl, allyl,
  • Example 1 A polymer was made by reacting 2.7 mol percent of H NCH CH NH(CH Si(OMe) with 97.3 mol percent dimethylsiloxane with OH endblocks and an average chain length of 29 siloxane units and a small excess of acetic acid in an isopropanol solvent. The product was a copolymer of 2.7 mol percent 4
  • Example 2 One-half gallon of the polymer described in Example 1 was added to a well by dump bailing at 2500 feet depth.
  • One-half gallon of a Humble Oil Company corrosion inhibitor, known as Corexit 801 was also added to the well.
  • Example 3 When copolymers of the following compositions are used to coat the inside of petroleum containers, or are added to the petroleum itself, effective retardation of the precipitation of paraffin on the container walls is noted:
  • n is an integer of a value from 0 through 2
  • A is a monovalent hydrocarbon radical with from 1 through 3 carbon atoms
  • R is selected from the group consisting of H, alkyl, alicyclic, and aminoalkyl radicals
  • R is a divalent hydrocarbon radical with at least 3 carbons atoms, the N atom and the Si being at least 3 carbon atoms apart
  • R is a monovalent hydrocarbon radical with from 1 through 6 carbon atoms
  • Y is selected from the group consisting of monocarboxylic aliphatic, and cycloaliphatic carboxylic acids of from 1 through 10 carbon atoms
  • a has a value from 0 to a value equal to the number of N atoms in (1); in amount suflicient to retard deposition of paraflin on the walls of a container through which the petroleum is passed.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Geology (AREA)
  • Mining & Mineral Resources (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Materials Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Fluid Mechanics (AREA)
  • General Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Silicon Polymers (AREA)
  • Paints Or Removers (AREA)
  • Lubricants (AREA)

Description

United States Patent Ofi 3,249,535 Patented May 3, 1966 ice Michigan No Drawing. Filed July 8, 1963, Ser. No. 293,245
9 Claims. (Cl. 2528.3)
This invention relates to a method of preventing or re tarding parafiin build up on the walls of petroleum conduits or containers, thereby reducing or preventing clogging.
The problem of parafiin clogging has plagued the oil industry for years. When oil is pumped to the surface it cools and the pressure on the oil is reduced due to gas release. Many crude oils have a high concentration of dissolved paraflins, and, upon cooling, and pressure reduction, these parafiins are likely to precipitate. The paraflin then collects'in a clogging mass on the walls inside the oil pipes or oil containers.
A good deal of work has been done in the field of pipe linings to retard parafiin clogging. Plastics, for eX- ample, are used to line crude oil transmission pipes after the oil has been brought to the surface, but this method cannot be used for oil Well pipe because of the abrasive action of sand and other particles that are brought up along with the crude oil. Also it is expensive.
Another technique used is to place immersion heaters into the' well shaft to heat the oil and redissolve the paraffin. j
Also, many oil wells are periodicallyclosed down and the paratfin is bored out. .This cleaning operation is a full-time profession for a number of people. Similarly, hot oil is sometimes recirculated into thewell shaft with the same end in mind. I
The objective of applicants; invention is to prevent or retard the deposition of paraffin in petroleum conduits and containers. This invention, however, can be used to prevent deposition {on the walls of containers and conduits with other solutions, suspensions, dispersions and emulsions than crude oil.
This is done by either coating the conduit or-container surface with the below-described copolymers, or by introducing small amounts of said material into the petroleum itself, either by placing it into the pipe or container along with the petroleum, or by continuously introducing it into a moving flow; of petroleum. The amount of copoly mer used is not critical so long as there is sufficient material to retard the deposition of parafiin. It has been found that this greatly inhibits the growth of parafiin deposits. i
,This invention represents a substanital stride in the techniques of coping with paraflin in piping. It prevents parafiin deposition and saves "many man-hours of labor, when compared with the various paraflin-removal techniques. 1
It is an advance over plastic-coated pipe in that it can be used in the well itself; it can be easily applied to, pipe that is already in place and operating; and it can be much cheaper.
carbon radical with from one through 6 carbon atoms, Y is a molecule of a monovalent aliphatic carboxylic acid or cycloaliphatic carboxylic acid of from 1 to 10 carbon atoms, and a has a value from 0 to a value equal to the number of N atoms in 1) and from 99.75 to 90 mol percent, siloxane units of the formula 3 ASiO where A is a monovalent hydrocarbon radical with from 1 through 3 carbon atoms.
The term consisting essentially of means that the copolymer is substantially as described but it can contain small amounts of other siloxane units which do not materially affect the property of retarding paraffin deposition.
This copolymer can be made in the following Way:
t f RNRSi(OMe) -n H0 (SIiO).n H- copolymeriY)... CHaOH where m is an integer and the other symbols retain their former identities. This reaction will proceed at room tem peature or upon warming the mixture.
It should be stressed that Y need not be present (1.e., a may equal 0) in order for the copolymer to be useful 1n applicants invention, nor, if it is present, is it necessary for every amine group to have a Y added to it.
The two R groups do not have to be identical. In this invention R can be any alkyl or alicyclic radical such as methyl, decyl, isobutyl, cyclohexyl, cyclopentyl, methylcyclohexyl, or octadecyl; or R can be any aminoalkyl radi etc.
The Y group can consist of any of the defined carboxylic acids such as formic acid, acetic acid, isobutyric The material that is used by this invention is a silox'ane copolymer consisting essentially of from 0.25 to 10 mol percent, siloxane units of the formula Rf". RzNRs i o (s-n) (Y): 1 2
where n is an integer of a value from 0 through 2, R is a hydrogen, alkyl, alicyclic, or aminoalkyl group; R is a divalent hydrocarbon that separates the N and the Si atoms by at least three carbon atoms, R" is a monovalent hydroacid, decanoic acid,
cyclohexyl carboxylic acid, 4-methylcyclohexylcarboxylic acid, acrylic acid, methacrylic acid, butynoic acid, vinylacetic acid, crotoni c acid, and CH CH(CH )-;COOH.
The R group can be any divalent hydrocarbon radical such as H5 C a 0 H2O H=C H- and -(0 H918- Preferably R has from 1 through 10 carbon atoms.
The R" group can be any of the defined radicals such as methyl, hexyl, isopropyl,
CHa=C-CH2CH cyclohexyl, phenyl, CH -CHCH=CH, etc.
The A group can be methyl, ethyl, propyl, isopropyl, vinyl, allyl,
C Hz=( J O H:
etc.
The following examples are illustrative only and should not be construed as limiting the invention which is properly set forth in the appended claims.
Example 1 A polymer was made by reacting 2.7 mol percent of H NCH CH NH(CH Si(OMe) with 97.3 mol percent dimethylsiloxane with OH endblocks and an average chain length of 29 siloxane units and a small excess of acetic acid in an isopropanol solvent. The product was a copolymer of 2.7 mol percent 4 Example 2 One-half gallon of the polymer described in Example 1 was added to a well by dump bailing at 2500 feet depth. One-half gallon of a Humble Oil Company corrosion inhibitor, known as Corexit 801 was also added to the well.
Six days later the well was reopened to cut the paraffin and none was found. This well was habitually cleaned of its. accumulated paraflin at weekly intervals.
The treatment of the well with silicon polymer and corrosion inhibitor was repeated, using the same quantities.
Seven days later the well was reopened, and still no paraffin was found.
There was no further treatment of the well.
Seven days thereafter the well was again reopened, and still no paraffin at all was found.
This well continued normal production throughout the duration of the experiment.
Example 3 When copolymers of the following compositions are used to coat the inside of petroleum containers, or are added to the petroleum itself, effective retardation of the precipitation of paraffin on the container walls is noted:
Mol percent Siloxane unit M01 percent Siloxanc unit 0.5 HzNCHzCHzCHzSiOa z 99.5..--
(oumsio 10.0 (CH )2NCHzCH2OHSiO 90.0 CH3siO CH: (CHM CH3 1.0 HzNCH2CH21 I(CH2)aSiO1 1 99.0 CHaClIzCHgS iO NHzCHzCHz CH; 19 \N s isio 98.1.. oupousio NH2CH2CH2/ a H+-0OC(OH2)1CH=CH;
OH; H CH3 0,1113 CH3 CH3 4.5 )HI ICH( ]H(CH2) SiO 95.s. ULI-Si0 n-r2 (32H. om
H H 8.1 HulroHzom)wI MCHmSiOa/Q 92.9 (oumsio H 3.5 l 1'SiO1 z 96.5 CH2=CHOH2slO s on,
H 0.7 C10H2 IiICH2OH=CH-SiO 93,3 (CllmSiO in -00c s H CHOH=G z M01 percent Siloxane unit M01 percent Siloxane unit CH; CH: 5.2 CH3N-Si0 OH; 94.8 Z-iO A HCH =CHz CH3 -0 0 O CH=CH2 H H 0.25- CHaIQCHrCHzILCHrCH=CHCHzSi0an 99.75 (CH3)2SiO -O OCCHCH2CH3 H CHaTHCHa 9.0 OHaI%I(OH);I |ICH|--Si0 91.0 (C s)zSiO 1 1 OOCH -OOCH CH3 and from 90 to 99.75 mol percent siloxane units of the formula ASlO where n is an integer of a value from 0 through 2, A is a monovalent hydrocarbon radical with from 1 through 3 carbon atoms, R is selected from the group consisting of H, alkyl, alicyclic, and aminoalkyl radicals, R is a divalent hydrocarbon radical with at least 3 carbon atoms, the N and the Si atoms being at least three carbon atoms apart, R" is a monovalent hydrocarbon radical with from 1 through 6 carbon atoms, Y is selected from the group consisting of monocarboxylic, aliphatic, and cycloaliphatic carboxylic acids of from 1 through 10 carbon atoms, and a has a value from 0 to a value equal to the number of nitrogen atoms in (l).
2. The method in accordance with claim 1 where A is CH3.
3. The method in accordance with claim 1 where (1) contains at least one Y group of from 1 to 3 carbon atoms inclusive.
4. The method in accordance with claim 1 where the copolymer used consists of 0.25 to 10 mol percent of groups, and 90 to 99.75 mol percent of C H; (ha) 611.
groups.
and from to 99.75 mol percent siloxane units of the formula AS iO where n is an integer of a value from 0 through 2, A is a monovalent hydrocarbon radical with from 1 through 3 carbon atoms, R is selected from the group consisting of H, alkyl, alicyclic, and aminoalkyl radicals, R is a divalent hydrocarbon radical with at least 3 carbons atoms, the N atom and the Si being at least 3 carbon atoms apart, R is a monovalent hydrocarbon radical with from 1 through 6 carbon atoms, Y is selected from the group consisting of monocarboxylic aliphatic, and cycloaliphatic carboxylic acids of from 1 through 10 carbon atoms, and a has a value from 0 to a value equal to the number of N atoms in (1); in amount suflicient to retard deposition of paraflin on the walls of a container through which the petroleum is passed.
6. The method in accordance with claim 5 where the siloxane copolymer is continuously added to the petroleum stream passing through the container.
7. The method in accordance with claim 5 where A iS CH3.
8. The method in accordance with claim 5 wherein (1) contains at least one Y group of from 1 to 3 carbon atoms inclusive.
9. The method in accordance with claim 5 where the copolymer used consists of 0.25 to 10 mol percent of groups, and 90 to 99.75 mol percent of groups.
References Cited by the Examiner UNITED STATES PATENTS 1,892,205 12/1932 De Groote et a1 252-83 2,762,823 9/ 1956 Speier 260-4482 3,085,908 4/1963 Morehouse et a1. 260-4482 3,170,865 2/1965 Allen et a1 252-83 FOREIGN PATENTS 659,810 3/1963 Canada.
JULIUS GREENWALD, Primary Examiner. H. B. GUYNN, Assistant Examiner.

Claims (1)

1. A METHOD COMPRISING RETARDING THE DEPOSITION OF PARAFFIN IN PETROLEUM CONTAINERS BY CONTACTING THE INSIDE OF THE CONTAINER WITH A SILOXANE COPOLYMER CONSISTING ESSENTIALLY OF 0.25 TO 10 MOLE PERCENT SILOZANE UNITS OF THE FORMULA
US293245A 1963-07-08 1963-07-08 Method of retarding paraffin clogging in petroleum containers Expired - Lifetime US3249535A (en)

Priority Applications (11)

Application Number Priority Date Filing Date Title
NL122510D NL122510C (en) 1963-07-08
US293245A US3249535A (en) 1963-07-08 1963-07-08 Method of retarding paraffin clogging in petroleum containers
DK245464AA DK107962C (en) 1963-07-08 1964-05-15 Method for preventing or delaying paraffin precipitation in mineral oil containers and pipelines.
ES300018A ES300018A1 (en) 1963-07-08 1964-05-19 A procedure to delay the deposition of paraffin in oil containers (Machine-translation by Google Translate, not legally binding)
NL6405600A NL6405600A (en) 1963-07-08 1964-05-20
CH701564A CH457280A (en) 1963-07-08 1964-05-29 Method to delay or prevent paraffin deposits
FR976852A FR1397716A (en) 1963-07-08 1964-06-03 Process for slowing down the deposition of paraffins in petroleum product reservoirs
GB25518/64A GB1004685A (en) 1963-07-08 1964-06-19 Improvements in or relating to retarding paraffin wax deposition in petroleum containers and conduits
DED44811A DE1232897B (en) 1963-07-08 1964-07-01 Use of copolymers based on organosiloxane to prevent paraffin deposits in pipelines or containers
AT576864A AT251157B (en) 1963-07-08 1964-07-06 Prevention of paraffin separation in pipes or containers
BE650206D BE650206A (en) 1963-07-08 1964-07-07

Applications Claiming Priority (1)

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US293245A US3249535A (en) 1963-07-08 1963-07-08 Method of retarding paraffin clogging in petroleum containers

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Country Status (10)

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US (1) US3249535A (en)
AT (1) AT251157B (en)
BE (1) BE650206A (en)
CH (1) CH457280A (en)
DE (1) DE1232897B (en)
DK (1) DK107962C (en)
ES (1) ES300018A1 (en)
FR (1) FR1397716A (en)
GB (1) GB1004685A (en)
NL (2) NL6405600A (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3395102A (en) * 1964-06-18 1968-07-30 Midland Silicones Ltd Process and antifoaming aqueous systems
US3416605A (en) * 1967-06-30 1968-12-17 Armour Ind Chem Co Paraffin deposition control
US3460216A (en) * 1965-10-22 1969-08-12 Dow Corning Aminoalkyl silicone glass lubricant
US3925582A (en) * 1971-05-10 1975-12-09 Texaco Inc Scale control
US4375420A (en) * 1982-02-22 1983-03-01 Olin Corporation Selected 4-hydroxyphenyl anilino alkoxysilanes and their use as antioxidants
US4818251A (en) * 1987-05-08 1989-04-04 Dow Corning Ltd. Removal of water haze from distillate fuel
US4854938A (en) * 1987-05-08 1989-08-08 Dow Corning, Ltd. Removal of water haze from distillate fuel
US5231207A (en) * 1991-10-15 1993-07-27 Shin-Etsu Chemical Co., Ltd. Organosilicon compound
US5374361A (en) * 1991-01-30 1994-12-20 Atlantic Richfield Company Well cleanout using caustic alkyl polyglycoside compositions
US5714524A (en) * 1994-04-13 1998-02-03 Three Bond Co., Ltd. Photocurable silicone composition
WO2016109218A1 (en) * 2014-12-30 2016-07-07 M-I L.L.C. Improving low temperature stability of fluid flow improvers

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2107725B (en) * 1981-10-03 1985-02-27 Dow Corning Siloxane quaternary ammonium salt preparation
US4507455A (en) * 1984-05-11 1985-03-26 Dow Corning Corporation Silicones bearing acylated diaminohydrocarbyl radicals and method therefor
CN116041706A (en) * 2022-12-30 2023-05-02 中国科学院广州能源研究所 A kind of microspherical hydrate inhibitor and its application

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1892205A (en) * 1926-02-23 1932-12-27 Tretolite Co Process for preventing accumulation of solid matter in oil wells, pipe lines and flow lines
US2762823A (en) * 1953-12-17 1956-09-11 Dow Corning Organosiloxane amines
CA659810A (en) * 1963-03-19 Pan American Petroleum Corporation Method for removing oil from wells
US3085908A (en) * 1959-05-26 1963-04-16 Union Carbide Corp Aminosilicon treated metals and methods of treatment and production
US3170865A (en) * 1961-07-17 1965-02-23 Dow Corning Method of retarding deposition of coke in petroleum furnaces

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1045091B (en) * 1955-02-14 1958-11-27 Dow Corning Process for the production of corrosion-resistant coatings, laminates, molded and cast bodies by hardening organopolysiloxane resins that do not have reactive groups on the silicon atom
GB886109A (en) * 1957-07-19 1962-01-03 Union Carbide Corp Aminosilicon treated metals and methods of treatment and production
US2873253A (en) * 1957-10-22 1959-02-10 Exxon Research Engineering Co Method of inhibiting the deposition of formally solid paraffins from a petroliferousfluid containing same
DE1252832B (en) * 1959-04-24 1967-10-26 Dow Corning A.G., Basel (Schweiz) Process for the production of anti-corrosive coatings on metal surfaces

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA659810A (en) * 1963-03-19 Pan American Petroleum Corporation Method for removing oil from wells
US1892205A (en) * 1926-02-23 1932-12-27 Tretolite Co Process for preventing accumulation of solid matter in oil wells, pipe lines and flow lines
US2762823A (en) * 1953-12-17 1956-09-11 Dow Corning Organosiloxane amines
US3085908A (en) * 1959-05-26 1963-04-16 Union Carbide Corp Aminosilicon treated metals and methods of treatment and production
US3170865A (en) * 1961-07-17 1965-02-23 Dow Corning Method of retarding deposition of coke in petroleum furnaces

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3395102A (en) * 1964-06-18 1968-07-30 Midland Silicones Ltd Process and antifoaming aqueous systems
US3460216A (en) * 1965-10-22 1969-08-12 Dow Corning Aminoalkyl silicone glass lubricant
US3416605A (en) * 1967-06-30 1968-12-17 Armour Ind Chem Co Paraffin deposition control
US3925582A (en) * 1971-05-10 1975-12-09 Texaco Inc Scale control
US4375420A (en) * 1982-02-22 1983-03-01 Olin Corporation Selected 4-hydroxyphenyl anilino alkoxysilanes and their use as antioxidants
US4818251A (en) * 1987-05-08 1989-04-04 Dow Corning Ltd. Removal of water haze from distillate fuel
US4854938A (en) * 1987-05-08 1989-08-08 Dow Corning, Ltd. Removal of water haze from distillate fuel
US5374361A (en) * 1991-01-30 1994-12-20 Atlantic Richfield Company Well cleanout using caustic alkyl polyglycoside compositions
US5231207A (en) * 1991-10-15 1993-07-27 Shin-Etsu Chemical Co., Ltd. Organosilicon compound
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DK107962C (en) 1967-07-24
AT251157B (en) 1966-12-27
NL122510C (en)
GB1004685A (en) 1965-09-15
DE1232897B (en) 1967-01-26
ES300018A1 (en) 1964-11-16
BE650206A (en) 1965-01-07
NL6405600A (en) 1965-01-11
FR1397716A (en) 1965-04-30
CH457280A (en) 1968-05-31

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