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Publication numberUS3254973 A
Publication typeGrant
Publication dateJun 7, 1966
Filing dateJul 31, 1962
Priority dateJul 31, 1962
Publication numberUS 3254973 A, US 3254973A, US-A-3254973, US3254973 A, US3254973A
InventorsGiammaria John J, Myron Becker
Original AssigneeSocony Mobil Oil Co Inc
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Gasolines and phosphorus-containing additives therefor
US 3254973 A
Abstract  available in
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Claims  available in
Description  (OCR text may contain errors)

United States Patent 3,254 973 GASOLINES AND PHOSiHORUS-CONTAINING ADDITIVES THEREFOR John J. Giammaria and Myron Becker, Woodbury, N.J.,

assignors to Socony Mobil Oil Company, Inc., a corporation of New York No Drawing. Filed July 31, 1962, Ser. No. 213,578 6 Claims. (Cl. 446) 'The present invention relates to novel lead-containing fuels for operation of internal combustion engines and to the operation of such engines with such fuels. More particularly, the present invention relates to novel leadcontaining fuels that reduce the abnormal combustion phenomena known as rumble and minimize preignition in operation of internal combustion engines.

As is well known to those skilled in the art, the compression ratio of internal combustion engines has been steadily increased. Such compression ratio increases have led to increased incidence of a combustion phenomenon known as rumble which is more prevalent in engines having compression ratios of at least 10:1 and higher. It is postulated that rumble is caused by abnormally high rates of pressure rise resulting from too rapid burning of the fuel-air mixture whereby vibrations are produced in overstressed engine parts causing a low frequency thudding noise that is associated with rumble.

As is also well known to those skilled in the art, the addition of lead anti-knock agents, such as tetraethyl lead and tetramethyl lead or mixtures thereof, to increase octane ratings is a well-established practice. It is also well known that the use of leaded gasolines have disadvantages, notably the occurrence of preignition. As the term implies, preignition is the ignition of the air-fuel mixture in the cylinder before the regular, timed spark ignition whereby the engine will behave as if the spark has been advanced beyond itsnormal timing. Such a phenomenon is, of course, a barrier to further increases in compression ratios. Thus, the problem of preignition has become more acute because of the trend to engines of increased compression ratio.

As is contemplated herein, preignition is caused by incandescent particles of combustion chamber deposits. Such deposits consist of a mixture of carbonaceous material and lead salts formed by decomposition of the lead anti-knock compounds. The lead salts resulting from the combustion of a leaded motor fuel are complex in nature. It is believed that they include lead chloride or bromide, lead oxide and lead sulfate, as well as mixed salts thereof formed through solid-solid reactions. These lead compounds have a catalytic effect upon the oxidation of the carbon in the combustion chamber deposits. The rapid oxidation of the carbon particles causes them to glow and to remain aglow for considerable periods of time after the combustion cycle. Accordingly, these glowing particles are present during the subsequent combustion cycle and cause preignition. Although pure carbon must be heated to about 1400 F. to make it glow, in the presence of lead salts the carbon glow is initiated as much as about 700 F. lower. Thus, it will be appreciated that obviating or minimizing the catalytic oxidation effect. of the lead salts will reduce preignition.

Certain phosphorus compounds are known to those skilled in the art to be effective types of compounds for rendering inert the stated catalytic effect of lead salts and, in general, it is known that a larger concentration of the phosphorus compounds is required in the fuel to minimize the rumble problem than is required to control the other forms of surface ignition. For example, in the use of a phosphorus compound such as tricresyl phosphate, 0.2 theory is normally required for the control of wild ping type of surface ignition whereas 0.4 to 1.0

theory is normally required to control rumble. In con nection with the proportional amount of phosphorus compound to the lead compound, as used herein, theory is the quantity of additive required to furnish 2 atoms of phosphorus for 3 atoms of lead in the fuel to form 3( 4)2- It has now been found that rumble and deposit-induced preignition of spark-ignition internal combustion engines can be materially reduced by addition of certain phosphorus-containing compounds and combinations thereof in leaded motor fuels and, more particularly, that, by use of the phosphorus-containing compounds embodied herein, a marked and unexpected increased activity on a phosphorus basis is obtained as compared to certain conventional phosphorus-containing additives for such purposes in leaded motor fuels.

The fuels contemplated herein are mixtures of hydrocarbons suitable for use in internal combustion engines of the spark ignition type, including motor gasolines and aviation gasolines. In general, motor gasolines have an initial boiling point as low as about F. and an end boiling point as high as about 440 F. and boil substantially continuously between the initial boiling point and the end boiling point. Aviation gasolines, on the other hand, are mixtures of hydrocarbons having an initial boiling point of about 80 F. and an end boiling point of about 340 F. and boiling substantially continuously between these points. Motor gasolines, at present, can, for example, contain up to about 4.0 ml. of tetraethyl lead per gallon whereas aviation gasolines can contain up to about 4.6 ml./ gallon of such a material. In general, the anti-knock compound is an organic lead compound as, for example, lead tetraalkyls, such as lead tetraethyl, lead tetramethyl, and mixtures thereof, and which gasolines are commonly referred to as leaded gasolines. Furthermore, it is common practice to add to the leaded gasoline a halohydrocarbon scavenger and, typical thereof are substances such as ethylene dichloride, ethylene dibromide, acetylene tetrabromide, and mixtures thereof. It is also common practice to use a combination of ethylene dichloride and ethylene dibromide in leaded motor gasolines whereas ethylene dibromide alone is used in leaded aviation gasolines. The amountsof scavenger utilized are calculated to avoid excessive wear and corrosion of the operating parts of the engine such as exhaust valves, and achieve effective scavenging of lead deposits. Thus, in the case of leaded motor gasolines, it has been the practiceto use one theory of ethylene dichloride and 0.5

theory of ethylene dibromide. On the other hand, it has been the practice to use one theory of ethylene dibromide in leaded aviation gasoline. As used herein, the term theory, as applied to the proportional amount of scavenger to lead, is intended to mean the amount of the scavenger required to convert all the lead present into a lead salt as, for example, into a lead salt such as lead chloride or bromide.

The phosphorus-containing compounds embodied for use in practice of this invention are high molecular weight phosphates having the structural formula:

wherein R is a divalent aliphatic hydrocarbon group, straight or branch chain, Ar is a member from the group consisting of aryl and substituted aryl in which the substituent is preferably an alkyl group or a halogen (e.g., chlorine), and R is the same or different members from 4 the group consisting of alkyl, aryl, alkaryl and halogensubstituted aryl. Preferably, in such high molecular I weight phosphates, R is a lower molecular weight aliphatic *fi fi hydrocarbon group containing, for example, from one to O CH: about 12 carbon atoms as in the fOllOWing illustrative 4,4"isopropylidene diphenol bis (dimethyl phosphate) groups; methylene, ethylidene, propylidene, and dode- I I cylidene, and still more preferably, divalent groups such Ha I as: (3H3 (3H1 orno P-o o-Q-o-moorn 1- a ll C'H, II

CH; CflHfi 4,4'-isopropylldene bis (2-t-buty1phenol) bis (dimethyl phosphate) Ar an aryl or alkaryl group such as may be derived CH; from phenol and substituted phenols as, for example, r P O I from cresol, xylenol, isopropyl phenol, t-butyl phenol, B a O P(OCBH") nonyl phenol, halogen-substituted phenols such as chloro- 0 CBIIIII phenols, polychlorophenols, etc.; and R is alkyl, aryl or 4,-l-(l-methylheptylldene) diphenol bis (di-octyl phosphate) alkaryl, and, illustratively, methyl, isopropyl, octyl, tolyl, xylyl, t-butyl phenyl, nonyl phenyl, etc. Preferably, R is 9 P an aromatic group as, generally, the presence of an aro- (CH)zP0CoP 0 matic hydrocarbon group in the R positions provides (3H3 g 1 compounds that are less antagonistic to the lead-containing ,Hdimtho he hi 710 y h 1 2 n th 1 1 H anti-detonant additives used in gasolines. As a very gg fit gig; 325, 5 y 19m) I CH pH, ocH; -r @r@ r o CH: 0

I 4,4-is0propylidene diphenol bis (methyl,' o-tolyl phosphate) specific embodiment, the present invention is carried out In reference to compounds of the foregoing formula with a compound of the following formula: wherein Ar and R are aryl or substituted-aryl groups,

CH3 CH3 1 II I ll 2 O CH: O

4,4"isopropylidene diphenol bis (dl-o-tolyl phosphate) Still other compounds embodied for use in practice of they may be synthesized by heating an appropriate phenothis invention are the following: lic compound with phosphorus oxychloride at, for exam- CH; OH;

I v (Jun 7 I Q Q 43 2 [I ll 2 O (13H: 0 I CH3 4,4-sec-butylidene dlphenol bis (di-o-tolyl phosphate) (EH3 r@r-@-r O lnHw 2 I C0 2 4,4-is0propylidene diphenol bis (di-p-nonylphenyl phosphate) CH3 CH3 CH3 CH3 l I I I 2 I II 2 O CHa O 4,4-isopropylidene bis (2-methy1pheno1) bis (di-o-tolyl phosphate) 0 Ha Cl C Ha 0 Ha I 2 H I ll 2 4,4-isopropylldene bis (2 chlorophenol) bis (di-o-tolyl phosphate) or c1 01 on: oi 01 01 i t t Q1 2 o 01 c1 CH3 01 or o 2 4,4"lsopropy1idene his (tetrachlorophenol) bis- (dt-o-chlorophenylphosphate) pic, 80 to 300 C. depending on the particular catalyst employed. For such a process, metal halides, as MgCl and AlCl are particularly suitable catalysts as they permit condensation times of 6-9 hours at 200 C. Evolu tion of hydrogen chloride generally starts at about 100 C. and is completed at about 225 C. when anhydrous MgCl is used as the catalyst. If desired, the reaction may be carried out in steps with isolation of the intermediates. Thus, and preferably using an excess of the phenolic reactant to drive the reaction to completion, the plural step process can be carried out as follows:

Purification, as desired, may include flash distillation of the crude reaction product mixture, washing with dilute caustic to neutralize any hydrogen chloride and extract partial esterification products or phenolic compounds, treatment with permanganate to improve color, and treatment with adsorbents and dehydration.

In reference to compounds of the foregoing formula wherein Ar is aryl or substituted aryl, and R is an aliphatic group, they may be synthesized by any of several methods, one of which is as follows and involves esterification of phosphorus oxychloride with an alcohol.

(1) o20 C. (ROMPCI 21101 2R'OH Pocn H amines or vacuum l0-30 C. 2(R'O)2IGC1+ NaOAr-R-ArONa The alkyl phosphoryl halide may be prepared by the addition of an alcohol to phosphorus oxychloride in approximately stoichiometric amounts at 020 C. with removal of the evolved hydrochloric acid by application of reduced pressures or by neutralization with amines such as pyridine, ammonia, etc. Purification may be achieved by Washing till neutral and fractional distillation. A second method of preparing the phosphoryl halide is by the addition of chlorine to a dialkyl hydrogen phosph-ite.

The alkyl phosphoryl halide may then be esterified with a phenolic compound by the Schotten-Baumann technique. The phosphoryl halide is added to a solution or suspension of the sodium arylate at 10-30 C. The ester product is separated and washed with dilute aqueous sodium hydroxide solution and water till neutral. Further purification, as desired, may be achieved by steaming to remove traces of alcohol, decolorization with permanganate solution and/ or adsorbents, filtration and dehydrat1on.

In a specific embodiment, the following procedure was used for preparation of 4,4'-isopropylidene d'iphenol bis (di-o-tolylphosphate (21) Preparation of di-o-tolyl phosphorochloridate. Phosphorus oxychloride (6 rn., 920 g.) plus anhydrous magnesium chloride (9 g.) were added to a liter flask equipped with a thermometer, a reflux condenser, a stirrer and an addition funnel. The reflux condenser was connected to two gas wash bottles in series containing known amounts of aqueous sodium hydroxide and phenolphthalein indicator (to measure the evolved hydrogen chloride). o-Cresol (12 rn., 1324 g., 98% pure) was added in portions to the fiask with stirring and heating. Three hundred grams ofthe o-cresol were added initially; the remainder during 255 minutes as the reaction mixture was heated to 110 C. (Hydrogen chloride began to evolve at about C.) Heating and stirring were continued for an additional two hours during which the temperature rose to 190 C. Nitrogen gas was passed through the reaction mixture during the last 55 minutes of this period to help expel the evolved HCl. A total of 12 moles of HCl were evolved during the reaction and were measured by absorption in the standardized aqueous sodium hydroxide solutions.

The reaction mixture was distilled under vacuum through a packed column.

Di-o-tolyl phosphorochloridate cuts distilling at 182- 187 C. at 5.0 to 5.5 mm. pressure were combined. Weight of this combined material was 824 g. Analyses of this product showed 12.1% C1 and 10.5% P; theoretical analyses of di-o-tolyl phosphorochloridate are 12.0% C1 and 10.4% P.

(b) Preparation of the 4,4'-is0pr0pylidene diphenol bis (di-o-tolylph osphate).-The di-o-tolyl phosphorochloridate (1 rn., 296.7 g.) and bis phenol A (4,4-isopropylidene diphenol) (0.5 rn., 114.1 g.) were placed in a fournecked flask equipped with a stirrer, thermometer, reflux condenser and a dropping funnel. Anhydrous magnesium chloride (0.5 .g.) was added to the mixture. All gases evolved from the reaction were passed through two wash towers containing measured amounts of aqueous sodium hydroxide solution and phenol-phthalein indicator. The mixture was heated with stirring from 25 to 215 C. during minutes and then maintained at 215 C. for 25 minutes. Nitrogen was passed through the mixture at 215 C. to help expel the evolved HCl. Evolution of HCl started at about 85 C. A total of about 0.9 m. of HCl was evolved.

Four hundred cc. of benzene was added to the reaction product. It was then washed with 50 cc. of 5% aqueous hydrochloric acid; 100 cc. of 5% aqueous sodium hydroxide; 50 cc. of 0.25% aq. HCl; and finally with water until neutral. Centrifuging or adding minor amounts of petroleum ether (less than 50 cc.) were used to break the emulsions which tended to form during the washings. The solvents were then stripped from the reaction product under vacuum until a pot temperature of 210 C. at a pressure of 19 mm. Hg was attained. Weight of product was 367 g.

To further purify this material, 355 g. of the above product was dissolved in 500 cc. benzene and passed through 500 g. of Alcoa activated alumina F-20 packed in a 25" x 1 /8" column. The benzene solvent was stripped from the eluate until a pot temperature of 205 C. at 10 mm. Hg was reached. The following analyses were obtained for the purified ester.

Found Theoretical Percent P 7 88 2 Percent C 6 9; Percent H 5.60 5.65 M01 Wt 765 cryoscopic 730 va Percent Cl .01 P i i f 0 the lead present in the gasoline formulation to form lead orthophosphate. Thus, 0.5 theory would indicate one half the amount of phosphorus-containing compound stoichiometrically required to react with all the lead present. Generally, in practice of this invention, the

amount of the phosphorus-containing compound will be between about 0.02 theory and about 2.0 theory, and preferably, between about 0.1 theory and about 0.5 theory.

In addition to additives such as lead anti-knock compounds and scavengers such as halohydrocarbons, and the phosphorus compounds embodied herein, the gasoline composition can contain other additives. Thus, for example, the gasolines can include dyes, carburetor de-icing agents such as isopropyl alcohol and lauryl mcrcaptoacetic acid, corrosion inhibitors such as polymerized fatty acids and salts of petroleum sulfonic acids, metal deactivators such as N,Ndisalicylidene-1,2-diaminopro-pane, anti-gum formation additives such as 2,6-ditertiarybutyl paracresol, etc.

The following examples are for the purpose of illustrating the preparation and the effectiveness, in the defined rumble and preignition tests, of the compositions of this invention. It is to be understood that this invention is not to be limited by the specific compositions of the examples or to the operations and manipulations involved. Other additives as described hereinbefore can be used as those skilled in the art will readily appreciate.

THE RUMBLE TEST The engine used for this test is a 1956 Buick V8 engine with a 322 cu. in. displacement. The piston crowns are modified to give a compression ratio of 11:1. Standard carburetion and ignition systems are employed. The engine is equipped with a conventional Dyn'aflow transmission connected to a TLC-74 D.C. dynamometer (200 H.P.). The dynamometer contains a flywheel which produces inertia characteristics like those imposed by the weight of a typical passenger car. In order to eliminate effects attributable to fluctuating conditions of intake air, it is supplied from an air conditioning system at constant temperature and humidity.

The engine is operated for 240 hours on an alternating operation schedule consisting of one hour at constant speed running at 1700 r.p.m. followed by onehour of cyclic operation between 500 and 1700 r.p.m. The engine operating conditions are set forth in Table I.

Rumble severity is determined every 24 hours during the test run by making 15 wide open throttle accelerations on isooctane +3 ml. TEL/ gal. Audible ratings of rumble severity are assigned to each acceleration from the following scale:

The average of the 15 ratings constitutes the daily rumble rate. An average of these daily rates (commencing with the 72 hour rating) is the over-all rumble rating, which is the reported value.

TABLE I Operating Conditions:

Test Duration-Approx. 240 hours Type of Operation-Alternating fixed and cyclic 8 PREIGNITION TEST This test is conducted with a La'beco 17.6 crankcase equipped with a single cylinder Olds modified conversion assembly which includes a 1953 Oldsmobile combustion chamber mounted on a wet sleeve cylinder. The engine, in good mechanical condition, is prepared for test with clean valves, combustion chamber, and new spark plug. Following an initial one-hour warm-up, the engine is run under preset cyclic conditions continuously for a total test time of hours. Performance of the test gasoline is judged by the rate of preignition counts per hour.

For the preignition test, the engine is considered ready for test if a minimum of 5.13 H.P. output (22 lbs-Toledo scale) can be obtained on clear isooctane at the following conditions:

MAP (manifold air pressure) Hg. abs. 30 Airzfuel ratio 13.0/1 Speed, r.p.m. 1400 Spark advance TDC Temperature, F.:

Jacket 212 Oil Air 100 Example 1 The fuel used for this example was a platinum reformate of the following properties and which contained an anti-oxidant (2,6-ditertiarybutyl paracresol), a metal deactivator (N,N-disalicylidene 1,2-diaminopropane) and a scavenger of ethylene dichloride and ethylene dibromide.

Gravity, API 42.4 RVP, lbs. 4.5 Distillation, F.:

Initial 92 End point 410 Mercaptan sulfur, ppm. 3.0 Lamp sulfur, wt. percent 0.0004 Aromatics, vol. percent 69.2 Olefin, vol. percent 0.7 Saturates, vol. percent 30.1 Research octane No. (3 ml. TEL/gal.) 105.8

RUMBLE ENGINE TEST RESULTS Run N0. Additive Rumble Rating 1 Base Fuel. None 8. 1 2 Base Fuel- 0.4 theory diphenyl tolyl phosphate... 6. 3 3 Base Fuel 0.4 theory 4.4-isopropy1idene diphcnol 1. 2 bis (dio'tolyl phosphate).

As is apparent from the foregoing, the base fuel was markedly suppressed against rumble by use of an addi- Type Fixed Cyclic Duration (hrs) l 1. Action Run-.. Deccl. Duration (secs) 16. Engine Speed (r.p.m.) 1,700-.- Dynamometer Speed (r.p m 1,640 To 400. BHP-Dynamometer 15.. Manifold vacuum (Hg). Jacket coolant temp., F 180 180. Inlet air:

Dry bulb, F 105. Wet bulb, F 69. Basic ignition timing. 5 BTC.

9 tive embodied for use herein (Run 3) as compared to the relatively small extent of suppression resulting from use of a conventional phosphorus-containing additive (Run 2) at the same 0.4 theory.

5 Example 2 Base gasoline composition same as in Example 1.

PREIGNITION ENGINE TESTS Preignition Run N o. Additive in Fuel 0,

counts/hour 1 Base Fuel None. i 83 2 Base Fuel 02 theory dipheuyl tolyl phosphate. 63 15 3 Base Fuel. 0.2 theory 4,4-isopropylidene diphenol 24 bis (di-o-tolyl phosphate).

As is apparent from the foregoing, use of the additive 20 embodied herein (Run 3) resulted in markedly improved performance in the preignition test as compared to the conventional additive (Run 2) at the same theory concentration.

Although the present invention has been described with preferred embodiments, it is to be understood that modifications and variations may be resorted to, without departing from the spirit and scope of this invention, as those skilled in the art will readily understand. Such variations and modifications are considered to be within 30 tetraethyl lead, per gallon of gasoline and between about 5 0.02 to about 2.0 theory of a phosphorus-containing compound of the following formula:

an aliphatic hydrocarbon group of one to twelve carbon atoms.

3. A composition, as defined in claim 2, wherein R is CH3 0 H3 4. A composition, as defined in claim 1, wherein R is alkyl-substituted aryl.

5. A composition, as defined in claim 1, wherein R is tolyl.

6. A composition, as defined in claim 1, wherein the phosphorus-containing compound is 4,4'-isopropylidene diphenol bis (di-o-tolylphosphate),

References Cited by the Examiner UNITED STATES PATENTS 2,520,090 8/1950 Barrett 260-461 2,643,265 6/1953 Toy 260461 2,885,430 5/1959 Scherer et a1 260-461 2,892,691 6/1959 Howell 44-69 3,038,791 6/1962 Orloif et a1. 44-69 DANIEL E. WYMAN, Primary Examiner.

ALPHONSO D. SULLIVAN, Examiner.

Y. M. HARRIS, Assistant Examiner.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2520090 *Dec 30, 1947Aug 22, 1950Monsanto ChemicalsPolyphosphates of divalent aryl hydrocarbons
US2643265 *Sep 15, 1950Jun 23, 1953Victor Chemical WorksBis (dialkyl phosphate) esters of alkylidene diphenols
US2885430 *Apr 2, 1957May 5, 1959Hoechst AgBis-(o:o-diethyl-dithiophosphoryl) 1:4-butylene-dimethyl ether
US2892691 *Apr 28, 1952Jun 30, 1959Exxon Research Engineering CoMotor fuels and motor fuel additives
US3038791 *Jul 16, 1959Jun 12, 1962Ethyl CorpPhenyl phosphate compositions
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3370345 *Jun 15, 1965Feb 27, 1968American Tech Mach CoBranch-pointing method and apparatus
US4134876 *Jan 12, 1977Jan 16, 1979Imperial Chemical Industries LimitedPhosphorus and linear polyester compositions and products containing them
US5420327 *Sep 10, 1993May 30, 1995Akzo Nobel N.V.Process for forming hydrocarbyl bisphosphate compound
US5457221 *Nov 15, 1993Oct 10, 1995Akzo Nobel N.V.Process for the manufacture of poly (hydrocarbylene aryl phosphate) compositions
US5679824 *Jul 24, 1996Oct 21, 1997Daihachi Chemical Industry Co., Ltd.Method of pulverizing aromatic phosphates
US5728859 *Oct 31, 1996Mar 17, 1998Akzo Nobel N.V.Process for making monohydroxy-terminated phosphate compositions
US5750756 *Jul 29, 1996May 12, 1998Akzo Nobel NvProcess for the formation of hydrocarbyl bis(hydrocarbyl phosphate)
US5756798 *Jun 13, 1997May 26, 1998Great Lakes Chemical CorporationProcess to prepare aryldiphosphoric esters
US5880308 *Dec 9, 1996Mar 9, 1999Daihachi Chemical Industry Co., Ltd.Process for preparing aromatic bisphosphates
US6136997 *Nov 1, 1994Oct 24, 2000Akzo Nobel NvProcess for the formation of hydrocarbyl BIS(hydrocarbyl phosphate)
US6319432Jun 11, 1999Nov 20, 2001Albemarle CorporationBisphenol-A bis(diphenyl phosphate)-based flame retardant
US6399685Dec 11, 2000Jun 4, 2002Albemarle CorporationPurification of arylene polyphosphate esters
EP0613902A1 *Feb 22, 1994Sep 7, 1994Akzo Nobel N.V.Process for the manufacture of poly(hydrocarbylene aryl phosphate)compositions
EP0789703A1 *Oct 20, 1995Aug 20, 1997Akzo Nobel N.V.Process for the formation of hydrocarbyl bis(hydrocarbyl phosphate)
EP0789703B1 *Oct 20, 1995Apr 23, 2003Akzo Nobel N.V.Process for the formation of hydrocarbyl bis(hydrocarbyl phosphate)
EP0918780A1 *Jun 13, 1997Jun 2, 1999Great Lakes Chemical CorporationProcess to prepare aryldiphosphoric esters
EP0918780A4 *Jun 13, 1997Jul 21, 1999Great Lakes Chemical CorpProcess to prepare aryldiphosphoric esters
WO1997047631A1 *Jun 13, 1997Dec 18, 1997Great Lakes Chemical CorporationProcess to prepare aryldiphosphoric esters
WO2002048158A1 *Nov 13, 2001Jun 20, 2002Albemarle CorporationPurification of arylene polyphosphate esters
Classifications
U.S. Classification44/382, 558/99, 987/228, 558/162
International ClassificationC07F9/00, C10L1/26, C10L1/30, C07F9/12, C10L1/14, C10L1/10
Cooperative ClassificationC10L1/306, C07F9/12, C10L1/2641, C10L1/14
European ClassificationC07F9/12, C10L1/14