|Número de publicación||US3378418 A|
|Tipo de publicación||Concesión|
|Fecha de publicación||16 Abr 1968|
|Fecha de presentación||11 Abr 1966|
|Fecha de prioridad||11 Abr 1966|
|Número de publicación||US 3378418 A, US 3378418A, US-A-3378418, US3378418 A, US3378418A|
|Inventores||Lissant Kenneth J|
|Cesionario original||Petrolite Corp|
|Exportar cita||BiBTeX, EndNote, RefMan|
|Citas de patentes (6), Citada por (8), Clasificaciones (12)|
|Enlaces externos: USPTO, Cesión de USPTO, Espacenet|
April 16, 1963 K. J. LISSANT 3,378,418
METHOD OF RESOLVING THIXOTROPIC JET AND ROCKET FUEL EMULSIONS Filed April 11, 1966 FLOWMETER p DEMULSIFIER- ABSORBER SUP|PLY 6 EMULSIFIED nursn FUEL SUPPLY METERING PUMP P p 1 P $4 THROTTLING METERING VALVE VALVE PUMP CLEAN FUEL STORAGE INVENTOR. KENNETH J. LISSANT United States Patent T 3,378,418 METHOD OF RESOLVING THKXOTRUPHI JET AND ROCKET FUEL EMULSIONS Kenneth J. Lissant, St. Louis, Mo., assignor to Petrolite Corporation, Wilmington, DeL, a corporation of Delaware Filed Apr. 11, 1966, Ser. No. 541,738 8 Claims. (Cl. 149-109) ABSTRACT OF THE DISCLOSURE A process of resolving jet and rocket thixotropic hydrocarbon-in-water emulsions comprising Water, an emulsifiable hydrocarbon and an emulsifying agent, said hydrocarbon being present in said emulsion fuel in an amount of at least 80% hydrocarbon by volume of the emulsion, which process is characterized by contacting said emulsion with a substantially insoluble breaker-absorber such as argillacious earth or clayey materials, thereby breaking the emulsion and also removing the Water-ty e external phase.
This invention in general relates to certain thixotropic emulsions.
In the following copending patent applications: S.N. 286,877 filed May 20, 1963 (relating to certain unique thixotropie emulsions), now abandoned; S.N. 302,001, filed Aug. 14, 1963 (relating in general to certain unique thixotropic hydrazine emulsions); S.N. 302,177, filed Aug. 14, 1963, (relating to certain unique thixotropic jet and rocket fuel emulsions), now abandoned; and SN. 411,103, filed Nov. 13, 1964, (relating to process of continually preparing these unique emulsions); there are disclosed certain thixotropic emulsions and systems relating thereto. These patent applications are, by reference, incorporated into the present application as if part hereof.
The advantages of the emulsified fuels described in the above patent applications have been demonstrated. Among other things, it has been found that when liquid fuels are subjected to crashes or military action and exposed to firearms or other means of ignition under fire power, serious fires and explosions often result. However, when emulsified fuels are subjected to crashes or to firearms or other fire power, the danger from serious fires and explo- 45 sions is substantially reduced or eliminated.
In using fuels in conventional systems such as jet engines which have not been adopted to employ emulsified fuels, it is necessary to revert the emulsified fuel to the liquid fuel itself. When reversion is effected, the external phase becomes suspended in the fuel. This requires lengthy and difficult separations before a fuel will meet original specification so it can be employed as a fuel in conventional engines, such as in jet engines.
Although emulsions of these types can be resolved by subjecting them to shear and/0r demulsifiers, the emulsions often invert under such treatment thus resulting in a dispersion of the original minor external phase in the major internal phase. This poses certain problems. For example, when the thixotropic emulsified fuel is inverted, it is necessary to remove the original external phase before it can be used in certain fuel systems because demulsificatio-n often produces a course dispersion of water in the fuelthus making it unacceptable for military applications.
In certain instances, separation of these particles can 3,378,418 Patented Apr. 16, 1968 be effected by allowing the dispersion to stand undisturbed for a sufficient length of time so that the suspended Water particles can settle out. However, as a practical matter,
the time required for settling and the size of the equipment 5 required to achieve this is too impractical for military field use.
I have now discovered that emulsified fuels can be facilely resolved to yield a satisfactory fuel by contacting the emulsion with a material capable of breaking the emulsion, which material is also immiscible in either phase. For example, the emulsion can be broken and the external phase removed by employing a solid breakerabsorber capable of both breaking the emulsion and absorbing the external phase so that the internal phase is recovered without contamination. Thus, when a hydrophilic insoluble solid such as clay is contacted with the emulsion, the emulsion is not only broken but the external phase is absorbed on the clay which is removed by any suitable means such as settling, centrifugation, filtration, electrostatic precipitation and the like. For ease of operation a small filtration unit is preferred.
In summary, the breaker-absorber not only breaks the emulsion but also removes the water-type external phase.
The unique thixotropic emulsions described herein have been amply described in the above patent applications. It should be noted that these emulsions can be prepared by any suitable emulsifying agent. Although oxyalkylates are preferred, other types of suitable emulsifiers can be employed.
By using the means of selecting suitable emulsifiers described in the above applications, one can select and em ploy emulsifiers, for example, of the following types:
I. Anionic (A) Carboxylic acids:
(1) Carboxyl joined directly to the hydrophobic group (subclassification on basis of the hydrophobic group), e.g. fatty acids, soaps, rosin soaps, etc.
(2) Carboxyl joined through an intermediate linkage.
(a) Amide group as intermediate link.
(b) Ester group as intermediate link.
(c) Sulfoamide group as intermediate link.
(d) Miscellaneous intermediate links, ether,
SO -S-, etc.
(B) Sulfuric esters (sulfates):
( 1) Sulfate joined directly to hydrophobic group.
(a) Hydrophobic group contains no other polar structures (sulfated alcohol and sulfated olefin type).
(b) Sulfuric esters with hydrophobic groups con- .taining other polar structures (sulfated oil type).
(2) Sulfate group joined through intermediate linkage.
(a) Ester linkage (Artie Syntex M. type).
(b) Amide linkage (Xynornine type).
(c) Ether linkage (Triton 770 type).
(d) Miscellaneous linkages (e.g., oxyalkylimidazole sulfates).
(C) Alkane sulfonic acids:
(1) Sulfonic group directly linked (a) Hydrophobic group bears other polar substituents (highly sulfated oil type). Chloro, hydroxy, acetoxy, and olefin sulfonic acids (Nytron type).
(b) Unsubstituted alkane sulfonic acids (MP 189 type; also cetane sulfo acid type).
(c) Miscellaneous sulfonic acids of uncertain structure, e.g., oxidation product-s of sulfurized olefins, sulfonated rosin, etc.
(2) Sulfonic groups joined through intermediate linkage.
(a) Ester linkage.
(l) RCOOXSO H (Igepon AP type). (2) ROOCX-SO H (Aerosol and sulfoacetate type).
(b) Amide link-age.
(1) RCONHXSO H (Igepon T type). (2) RNHOC-X-SO H (sulfosuccinamide type).
(c) Ether linkage (Triton 720 type).
(d) Miscellaneous linkages and two or more linkages.
(D) Alkyl aromatic sulfonic acids:
(1) Hydrophobic group joined directly to sulfonated aromatic nucleus (subclasses on basis of nature of hydrophobic group. Alkyl phenols, terpene, and rosin-aromatic condensates, alkyl aromatic ketones, etc.).
(2) Hydrophobic group joined to sulfonated aromatic nucleus through as intermediate linkage.
(a) Ester linkage (sulfophthalates, sulfobenzoates).
(b) Amide and imide linkages.
(1) RCONH-ArSO H type. (2) Sulfobenzamide type.
(c) Ether linkage (alkyl phenyl ether type).
(d) Heterocyclic linkage (Ultravon type, etc.).
(e) Miscellaneous and two or more links.
(E) Miscellaneous anionic hydrophillic groups:
(1) Phosphages and phosphonic acids.
(2) Persulfa-tes, thiosulfates, etc.
(4) Sulfamic acids, etc.
II. Cationic (A) Amine salts (primary, secondary, and tertiary amines): (1) Amino group joined directly to hydrophobic group.
(a) Aliphatic and aromatic amino groups. (b) Amino group is part of a heterocycle (alkaterge type). (2) Amino group joined through an intermediate link.
(a) Ester link. (b) Amide link. Ether link.
(d) Miscellaneous links. (B) Quaternary ammonium compounds:
(1) Nitrogen joined directly to hydrophilic group. (2) Nitrogen joined through an intermediate link.
(a) Ester link. (b) Amide link. (c) Ether link. (d) Miscellaneous links. (C) Other nitrogenous bases:
(1) Non-quaternary bases (classified as guanidine,
thiuronium salts, etc.). (2) Quaternary bases. (D) Non-nitrogenous bases:
(1) Phosphonium compounds. (2) Sulfonium compounds, etc.
Ill. Non-ionic (A) Ether linkage to solubilizing groups. (B) Ester linkage. (C) Amide linkage. (D) Miscellaneous linkages. (E) Multiple linkages.
l IV. Ampholytic (A) Amino and carboxy:
(1) Non-quaternary. (2) Quaternary. (B) Amino and sulfuric ester: (1) Non-quaternary. (2) Quaternary. (C) Amine and alkane sulfonic acid. (D) Amine and aromatic sulfonic acid. (E) Miscellaneous combinations of basic and acidic groups.
The breaker-absorber employed herein can be any solid material which will maintain its solid form during treatment and is capable of breaking the emulsion and absorbing the outer water-type phase.
In general, these materials are water-absorbing or hydrophilic solids insoluble in either phase.
Non-limiting examples include argillacious earth or clayey materials, for example, montmorillonite, bentonite, silica, calicum sulfate, aluminum silicate, etc. In addition, water absorbant high surface fibers such as cellulose, asbestos, rockwool, etc. can be employed. Other insoluble hydrate-forming salts can be employed. Any suitable method of treating can be emp1oyedfor example, a slurry, a fixed bed, combinations thereof, etc.
The amount of breaker-absorber employed will vary depending on many factors, for example, on particle size, hydrophilic properties, the amount of water in the emulsion, contact time, rate of stirring, etc. With an emulsion containing about 10% or less water preferably having about 5% or less water and employing a clay, such as montmorillonite clay, I employ, for example, at least about 0.25 g./l00 ml. of emulsion, for example about 0.3 to 3.0 g., such as about 0.25 to 1.5 g., but preferably about .5 to 1.0 g.
The particle size of the hydrophilic material, for example montmorillonite clay can also vary widely, for example, one having a particle size of about l,u. to 10,000 or greater, such as 1 to lOOQu, but preferably Sp. to 500 In order to make the breaker-absorber more effective, it is preferable to employ as little water as possible consistent with producing a satisfactory emulsion, for example less than about 10% water, such as less than about 8% water, for example less than about 5%, but preferably less than about 5% water, such as 52% water. In certain instances, Where it is desirable, higher ratios of water may be employed such as 20% or more of water.
In general, demulsification is effected by intimately mixing the solid breaker-absorber with the emulsified fuel and then separating the solid breaker-absorber from the fuel. Fast high shear mixing also assists in breaking the emulsion. The product is a clean fuel which meets military specifications.
Examples The following examples .are presented for purpose of illustration and not of limitation. The system employed is presented in the flow sheet in the drawing where P in the drawing represents pressure.
The smooth, white, highly thixotropic O/W emulsion prepared as in Example 1 of SN. 411,103 from about 96-97% kerosene and about 34% water, by volume, employing n-decanol+PrO(l.96)+Et0(2.6l) as an emulsifier, indicates weights of oxides based on weight of n-decanol, was fed to the demulsification system at the rate of about 1800 ml./minute. A kerosene slurry of montmorillonite-type clay (particle size 50 was employed 1.5 g. of clay/100 ml. of kerosene) and added at a rate so that 1 g. of clay treated 100 ml. of fuel emulsion. The clay filtered easily so as to yield a clear fuel which meets military specification.
To save repetitive details the treatment of other emulsified fuels, similarly demulsified is presented in the following table.
TABLE I Ratio (g.) Emulsion Prepared Demulsifier-Dehydraof Active Ex. According to S.N. tor, 1. g/100 ml. Solids Comment Kerosene to ml.
Emulsion 1 Ex. 77 of 286,877 l Fullers Earth 50;/. 1/100 Breaks and filters clean. Meets military specifications. 2 do 1 Synthetic Calcium 1/100 Do.
Silicate 1p. 3-.- do I Bentonite 200 4 1/100 Do. 4 .410 l Anhydrous C3304 1/100 Do. 100011..
of oxide per part of ioots. This application is now abandoned.
The above examples are illustrative of .this invention. Other thioxotropic emulsions described in the above application are also broken in a similar manner to yield fuels which meet military specifications. For example, the emulsions prepared in Table I of SN. 411,103 are similarly broken.
As is quite evident, other breaker-absorbers besides those specifically mentioned herein can be employed in my invention. It is, therefore, not only impossible to attempt a comprehensive catalogue of such compositions, but to attempt to describe the invention in its broader aspects in terms of specific chemical names would be too voluminous and unnecessary since one skilled in the art could by following the description of the invention herein select a useful breaker-absorber. This invention lies in the use of suitable breaker-absorbers and their individual compositions are important only in the sense that their properties can affect this function. To precisely define each specific useful breaker-absorber in light of the present disclosure would merely call for chemical knowledge within the skill of the art in .a manner analogous to a mechanical engineer who prescribes in the construction of a machine the proper materials and the proper dimensions thereof. From the description in this specification and with the knowledge of a chemist, one will know or deduce with confidence the applicability of specific breaker-absorbers suitable for this invention by applying them in the process set forth herein. In analogy to the case of a machine, wherein the use of certain materials of construction or dimensions of parts would lead to no practical useful result, various materials will be rejected as inapplicable where others would be operative. One can obviously assume that no one will wish to use a useless breaker-absorber, nor will be misled because it is possible to misapply the teachings of the present disclosure to do so. Thus any breaker absorber that can perform the function stated herein can be employed.
The thixotropic emulsions of this invention described in the above applications are particularly useful in commercial and military operations. For example, when placed in fuel receptacles such as storage tanks, portable fuel receptacles, aircraft, rocket or jet fuel tanks, etc., they are less susceptible to fire or explosion on crashes, under firepower or other igniting conditions, thus resulting in a great saving of life and property.
Thus, any of the unique thixotropic emulsions prepared herein, for example, those in Example 1 of S.N. 4 11, 103, Example 77 of SN. 286,877, now abandoned, and others described in the applications incorporated by reference into this application, when contained in such receptacles on the ground or in the air are useful in preventing fire and explosions.
Having thus described my invention what I claim as new and desire to obtain by Letters Patent is:
1. A process of resolving a jet and rocket thixotropic hydrocarbon-inwater emulsion fuel comprising (1) water, ('2) an emulsifiable hydrocarbon, and (3) an emulsifying agent, said hydrocarbon being present in said emulsion fuel in an amount of at least hydrocarbon by volume of the emulsion, said emulsion having the characteristics of a solid fuel when at rest and the characteristics of a liquid fuel when a force is exerted on it, said emulsion tending to be nonadhes-ive, said emulsion having a critical shear point sufiicient to permit pumping at high rates, and said emulsion having an apparent rest viscosity greater than about 1000 cps., which is characterized by contacting said emulsion with a substantially insoluble breaker-absorber which is capable of interacting with the water phase so as to break the emulsion.
2. The process of claim 1 wherein said hydrocarbon is present in said emulsion in an amount of .at least by volume of said emulsion.
3. The process of claim 1 where the breaker-absorber is a clayey material.
4. The process of claim 3 where the breaker-absorber is a montmor-illonitetype clay.
5. The process of claim 1 where the breaker-absorber is a hydrate-forming material.
6. The process of claim 3 wherein said hydrocarbon is present in said emulsion in an amount of at least 90% by volume of said emulsion.
7. The process of claim 4 wherein said hydrocarbon is present in said emulsion in an amount of at least 90% by volume of said emulsion.
8. The process of claim 5 wherein said hydrocarbon is present in said emulsion in an amount of at least 90% by volume of said emulsion.
References Cited UNITED STATES PATENTS OARL D. QUARFORTH, Primary Examiner. BENJAMIN R. PADGETT, Examiner. S. J. LEOHERT, JR., Assistant Examiner.
|Patente citada||Fecha de presentación||Fecha de publicación||Solicitante||Título|
|US1911797 *||18 May 1927||30 May 1933||Blake Smith L||Method of breaking emulsions|
|US1911839 *||30 Jul 1930||30 May 1933||Blakesmith L||Continuous method of breaking emulsions|
|US1974692 *||21 May 1932||25 Sep 1934||Blake Smith L||Process for resolving emulsions|
|US2522378 *||22 May 1946||12 Sep 1950||Owens Corning Fiberglass Corp||Resolving water and oil emulsions|
|US3085068 *||22 Ene 1958||9 Abr 1963||Ralph W Hippen||Method of resolving emulsions|
|US3242097 *||27 Abr 1961||22 Mar 1966||Phillips Petroleum Co||Separation of liquid phases|
|Patente citante||Fecha de presentación||Fecha de publicación||Solicitante||Título|
|US3974116 *||20 Mar 1974||10 Ago 1976||Petrolite Corporation||Emulsion suspensions and process for adding same to system|
|US4029596 *||23 Dic 1974||14 Jun 1977||Th. Goldschmidt Ag||De-emulsifier for breaking petroleum emulsions|
|US5276247 *||21 Sep 1992||4 Ene 1994||Cassella Aktiengesellschaft||Process for obtaining the hydrocarbon from a hydrocarbon-rich gel|
|US5276248 *||2 Sep 1992||4 Ene 1994||Cassella Aktiengesellschaft||Process for the storage and transportation of liquid hydrocarbons|
|US5977194 *||15 Nov 1995||2 Nov 1999||The Dow Chemical Company||High internal phase emusions and porous materials prepared therefrom|
|US6147131 *||18 Nov 1998||14 Nov 2000||The Dow Chemical Company||High internal phase emulsions (HIPEs) and foams made therefrom|
|US6303834||25 Ago 2000||16 Oct 2001||The Dow Chemical Company||High internal phase emulsions (HIPEs) and foams made therefrom|
|US6391928 *||12 May 2000||21 May 2002||Indian Institute Of Science||Process for preparing a novel synergistic solid/semi-solid organic composition|
|Clasificación de EE.UU.||516/138, 149/109.6|
|Clasificación internacional||C06B21/00, C10L7/02, C10L1/32, C10L7/00|
|Clasificación cooperativa||C10L1/328, C10L7/02, C06B21/0091|
|Clasificación europea||C06B21/00F, C10L1/32D, C10L7/02|