Patent Grant
7500996
The present invention relates to an additive, to its use as a cold flow improver for vegetable or animal fuel oils and to correspondingly additized fuel oils.
In view of decreasing world crude oil reserves and the discussion about the environmentally damaging consequences of the use of fossil and mineral fuels, there is increasing interest in alternative energy sources based on renewable raw materials. These include in particular natural oils and fats of vegetable or animal origin. These are generally triglycerides of fatty acids having from 10 to 24 carbon atoms and a calorific value comparable to conventional fuels, but are at the same time regarded as being less harmful to the environment. Biofuels, i.e. fuels derived from animal or vegetable material, are obtained from renewable sources and, when they are combusted, generate only as much CO2 as had previously been converted to biomass. It has been reported that less carbon dioxide is formed in the course of combustion than by the equivalent amount of crude oil distillate fuel, for example diesel fuel, and that very little sulfur dioxide is formed. In addition, they are biodegradable.
Oils obtained from animal or vegetable material are mainly metabolism products which include triglycerides of monocarboxylic acids, for example acids having from 10 to 25 carbon atoms, and corresponding to the formula
where R is an aliphatic radical which has from 10 to 25 carbon atoms and may be saturated or unsaturated.
In general, such oils contain glycerides from a series of acids whose number and type vary with the source of the oil, and they may additionally contain phosphoglycerides. Such oils can be obtained by processes known from the prior art.
As a consequence of the sometimes unsatisfactory physical properties of the triglycerides, the industry has applied itself to converting the naturally occurring triglycerides to fatty acid esters of low alcohols such as methanol or ethanol.
A hindrance to the use of triglycerides and also of fatty acid esters of lower monohydric alcohols as a replacement for diesel fuel alone or in a mixture with diesel fuel has proven to be the flow behavior at low temperatures. The cause of this is the high uniformity of these oils in comparison to mineral oil middle distillates. For example, the rapeseed oil methyl ester (RME) has a Cold Filter Plugging Point (CFPP) of −14° C. It has hitherto been impossible using the prior art additives to reliably obtain a CFPP value of −20° C. required for use as a winter diesel in Central Europe, or of −22° C. or lower for special applications. This problem is increased when oils are used which comprise relatively large amounts of the likewise readily available oils of sunflowers and soya.
EP-B-0 665 873 discloses a fuel oil composition which comprises a biofuel, a fuel oil based on crude oil and an additive which comprises (a) an oil-soluble ethylene copolymer or (b) a comb polymer or (c) a polar nitrogen compound or (d) a compound in which at least one substantially linear alkyl group having from 10 to 30 carbon atoms is bonded to a nonpolymeric organic radical, in order to provide at least one linear chain of atoms which includes the carbon atoms of the alkyl groups and one or more nonterminal oxygen atoms, or (e) one or more of the components (a), (b), (c) and (d).
EP-B-0 629 231 discloses a composition which comprises a relatively large proportion of oil which consists substantially of alkyl esters of fatty acids which are derived from vegetable or animal oils or both, mixed with a small proportion of mineral oil cold flow improvers which comprises one or more of the following:
EP-B-0 543 356 discloses a process for preparing compositions having improved low temperature behavior for use as fuels or lubricants, starting from the esters of naturally occurring long-chain fatty acids with monohydric C1-C6-alcohols (FAE), which comprises
DE-A-40 40 317 discloses mixtures of fatty acid lower alkyl esters having improved cold stability comprising
EP-B-0 153 176 discloses the use of polymers based on unsaturated dialkyl C4-C8-dicarboxylates having an average alkyl chain length of from 12 to 14 as cold flow improvers for certain crude oil distillate fuel oils. Mentioned as suitable comonomers are unsaturated esters, in particular vinyl acetate, but also α-olefins.
EP-B-0 153 177 discloses an additive concentrate which comprises a combination of
WO 95/22300 (=EP 0 746 598) discloses comb polymers in which the alkyl radicals have an average of less than 12 carbon atoms. These additives are especially suitable for oils having cloud points of less than −10° C., although the oils may also be native hydrocarbon oils (page 21, line 16 ff.). However, native oils have cloud points of about −2° C. upward.
It has hitherto often been impossible using the existing additives to reliably adjust fatty acid esters to a CFPP value of −20° C. required for use as a winter diesel in Central Europe or of −22° C. and lower for special applications. An additional problem with the existing additives is the lacking cold temperature change stability of the additized oils, i.e. the CFPP value of the oils attained rises gradually when the oil is stored for a prolonged period at changing temperatures in the region of the cloud point or below.
It is therefore an object of the invention to provide additives for improving the cold flow behavior of fatty acid esters which are derived, for example, from rapeseed oil, sunflower oil and/or soya oil and attain CFPP values of −20° C. and below which remain constant even when the oil is stored for a prolonged period in the region of its cloud point or below.
It has now been found that, surprisingly, an additive comprising ethylene copolymers and comb polymers is an excellent flow improver for such fatty acid esters.
The invention therefore provides an additive comprising
of the molar averages of the carbon chain length distributions in the alkyl radicals of monomer 1 on the one hand and the alkyl radicals of the amide and/or imide groups of monomer 2 on the other hand is from 23 to 27, where
The invention further provides a fuel oil composition comprising a fuel oil of animal or vegetable origin and the above-defined additive.
The invention further provides the use of the above-defined additive for improving the cold flow properties or fuel oils of animal or vegetable origin.
The invention further provides a process for improving the cold flow properties of fuel oils of animal or vegetable origin by adding the above-defined additive to fuel oils of animal or vegetable origin.
In a preferred embodiment of the invention, Q has values of from 24 to 26.
Here, side chain length of olefins refers to the alkyl radical branching from the polymer backbone, i.e. the chain length of the monomeric olefin minus the two olefinically bonded carbon atoms. In the case of olefins having nonterminal double bonds, for example olefins having vinylidene moiety, it is correspondingly the total chain length of the olefin minus the double bond merging into the polymer backbone that has to be taken into account.
Useful ethylene copolymers A) are those which contain from 8 to 21 mol % of one or more vinyl and/or (meth)acrylic ester and from 79 to 92 mol % of ethylene. Particular preference is given to ethylene copolymers having from 10 to 18 mol % and especially from 12 to 16 mol %, of at least one vinyl ester. Suitable vinyl esters are derived from fatty acids having linear or branched alkyl groups having from 1 to 18 carbon atoms and preferably from 1 to 12 carbon atoms. Examples include vinyl acetate, vinyl propionate, vinyl butyrate, vinyl hexanoate, vinyl heptanoate, vinyl octanoate, vinyl laurate and vinyl stearate, and also esters of vinyl alcohol based on branched fatty acids, such as vinyl isobutyrate, vinyl pivalate, vinyl 2-ethylhexanoate, vinyl isononanoate, vinyl neononanoate, vinyl neodecanoate and vinyl neoundecanoate. Particular preference is given to vinyl acetate. Likewise suitable as comonomers are esters of acrylic and methacrylic acids having from 1 to 20 carbon atoms in the alkyl radical, such as methyl (meth)acrylate, ethyl (meth)acrylate, propyl (meth)acrylate, n- and isobutyl (meth)acrylate, and hexyl, octyl, 2-ethylhexyl, decyl, dodecyl, tetradecyl, hexadecyl and octadecyl (meth)acrylate, and also mixtures of two, three, four or else more of these comonomers.
Apart from ethylene, particularly preferred terpolymers of vinyl 2-ethylhexanoate, of vinyl neononanoate or of vinyl neodecanoate contain preferably from 3.5 to 20 mol %, in particular from 8 to 15 mol %, of vinyl acetate, and from 0.1 to 12 mol %, in particular from 0.2 to 5 mol %, of the particular long-chain vinyl ester, the total comonomer content being between 8 and 21 mol %, preferably between 12 and 18 mol %. In addition to ethylene and from 8 to 18 mol % of vinyl esters, further preferred copolymers additionally contain from 0.5 to 10 mol % of olefins such as propene, butene, isobutylene, hexene, 4-methylpentene, octene, diisobutylene and/or norbornene.
The copolymers A preferably have molecular weights which correspond to melt viscosities at 140° C. of from 20 to 10 000 mPas, in particular from 30 to 5000 mPas, and especially from 50 to 1000 mPas. The degrees of branching determined by means of 1H NMR spectroscopy are preferably between 1 and 9 CH3/100 CH2 groups, in particular between 2 and 6 CH3/100 CH2 groups, for example from 2.5 to 5 CH3/100 CH2 groups, which do not stem from the comonomers.
The copolymers (A) can be prepared by the customary copolymerization processes, for example suspension polymerization, solution polymerization, gas phase polymerization or high pressure bulk polymerization. Preference is given to carrying out the high pressure bulk polymerization at pressures of from 50 to 400 MPa, preferably from 100 to 300 MPa, and temperatures from 100 to 300° C., preferably from 150 to 220° C. In a particularly preferred preparation variant, the polymerization is effected in a multizone reactor in which the temperature difference between the peroxide feeds along the tubular reactor is kept very low, i.e. <50° C., preferably <30° C., in particular <15° C. The temperature maxima in the individual reaction zones preferably differ by less than 30° C., more preferably by less than 20° C. and especially by less than 10° C.
The reaction of the monomers is initiated by radical-forming initiators (radical chain initiators). This substance class includes, for example, oxygen, hydroperoxides, peroxides and azo compounds, such as cumene hydroperoxide, t-butyl hydroperoxide, dilauroyl peroxide, dibenzoyl peroxide, bis(2-ethylhexyl) peroxydicarbonate, t-butyl perpivalate, t-butyl permaleate, t-butyl perbenzoate, dicumyl peroxide, t-butyl cumyl peroxide, di(t-butyl) peroxide, 2,2′-azobis(2-methylpropanonitrile), 2,2′-azobis(2-methylbutyronitrile). The initiators are used individually or as a mixture of two or more substances in amounts of from 0.01 to 20% by weight, preferably from 0.05 to 10% by weight, based on the monomer mixture.
The high pressure bulk polymerization is carried out in known high pressure reactors, for example autoclaves or tubular reactors, batchwise or continuously, and tubular reactors have proven particularly useful. Solvents such as aliphatic and/or aromatic hydrocarbons or hydrocarbon mixtures, benzene or toluene may be present in the reaction mixture. Preference is given to the substantially solvent-free procedure. In a preferred embodiment of the polymerization, the mixture of the monomers, the initiator and, if used, the moderator, are fed to a tubular reactor via the reactor entrance and also via one or more side branches. Preferred moderators are, for example, hydrogen, saturated and unsaturated hydrocarbons, for example propane or propene, aldehydes, for example propionaldehyde, n-butyraldehyde or isobutyraldehyde, ketones, for example acetone, methyl ethyl ketone, methyl isobutyl ketone, cyclohexanone, and alcohols, for example butanol. The comonomers and also the moderators may be metered into the reactor either together with ethylene or else separately via sidestreams. The monomer streams may have different compositions (EP-A-0 271 738 and EP-A-0 922 716).
Examples of suitable co- or terpolymers include:
Preference is given to using mixtures of the same or different ethylene copolymers. The polymers on which the mixtures are based more preferably differ in at least one characteristic. For example, they may contain different comonomers, different comonomer contents, molecular weights and/or degrees of branching. The mixing ratio of the different ethylene copolymers is preferably between 20:1 and 1:20, preferably from 10:1 to 1:10, in particular from 5:1 to 1:5.
The copolymers B are preferably derived from ethylenically unsaturated dicarboxylic acids and their derivatives such as esters and anhydrides. Preference is given to maleic acid, fumaric acid, itaconic acid and the esters thereof with lower alcohols having from 1 to 6 carbon atoms and also anhydrides thereof, for example maleic anhydride. Particularly suitable comonomers are monoolefins having from 10 to 20, in particular having from 12 to 18, carbon atoms. These are preferably linear and the double bond is preferably terminal as, for example, in dodecene, tridecene, tetradecene, pentadecene, hexadecene, heptadecene and octadecene. The ratio of dicarboxylic acid or dicarboxylic acid derivative to olefin or olefins in the polymer is preferably in the range from 1:1.5 to 1.5:1, and it is especially equimolar.
Also present in copolymer B may be minor amounts of up to 20 mol %, preferably <10 mol %, especially <5 mol %, of further comonomers which are copolymerizable with ethylenically unsaturated dicarboxylic acids and the olefins specified, for example relatively short- and relatively long-chain olefins, allyl polyglycol ethers, C1-C30-alkyl (meth)acrylates, vinylaromatics or C1-C20-alkyl vinyl ethers. Poly(isobutylene) having a molecular weight up to 5000 g/mol are likewise used in minor amounts, and preference is given to highly reactive variants having a high proportion of terminal vinylidene groups. These further comonomers are not taken into account in the calculation of the factor Q determining the effectiveness.
Alkyl polyglycol ethers correspond to the general formula
where
The copolymers B) according to the invention are preferably prepared at temperatures between 50 and 220° C., in particular from 100 to 190° C., especially from 130 to 170° C. The preferred preparative process is the solvent-free bulk polymerization, although it is also possible to carry out the polymerization in the presence of aprotic solvents such as benzene, toluene, xylene or of relatively high-boiling aromatic, aliphatic or isoaliphatic solvents or solvent mixtures, such as kerosene or Solvent Naphtha. Particular preference is given to the polymerization in aliphatic or isoaliphatic solvents having little moderating influence. The proportion of solvent in the polymerization mixture is generally between 10 and 90% by weight, preferably between 35 and 60% by weight. In the case of the solution polymerization, the reaction temperature can be set in a particularly simple manner via the boiling point of the solvent or by working under reduced or elevated pressure.
The average molecular mass of the inventive copolymers B is generally between 1200 and 200 000 g/mol, in particular between 2000 and 100 000 g/mol, measured by means of gel permeation chromatography (GPC) against polystyrene standards in THF. Inventive copolymers B have to be oil-soluble in the dosages relevant to the practice, i.e. they have to dissolve without residue at 50° C. in the oil to be additized.
The reaction of the monomers is initiated by radical-forming initiators (radical chain initiators). This substance class includes, for example, oxygen, hydroperoxides and peroxides such as cumene hydroperoxide, t-butyl hydroperoxide, dilauroyl peroxide, dibenzoyl peroxide, bis(2-ethylhexyl) peroxydicarbonate, t-butyl perpivalate, t-butyl permaleate, t-butyl perbenzoate, dicumyl peroxide, t-butyl cumyl peroxide, di(t-butyl) peroxide, and azo compounds such as 2,2′-azobis(2-methylpropanonitrile) or 2,2′-azobis(2-methylbutyronitrile). The initiators are used individually or as a mixture of two or more substances in amounts of from 0.01 to 20% by weight, preferably from 0.05 to 10% by weight, based on the monomer mixture.
The copolymers can be prepared either by reaction of maleic acid, fumaric acid and/or itaconic acid or the derivatives thereof with the appropriate amine and subsequent copolymerization or by copolymerization of olefin or olefins with at least one unsaturated dicarboxylic acid or a derivative thereof, for example itaconic anhydride and/or maleic anhydride, and subsequent reaction with amines. Preference is given to carrying out a copolymerization with anhydrides and converting the resultant copolymer after the preparation to an amide and/or an imide.
In both cases, the reaction with amines is effected, for example, by reacting with from 0.8 to 2.5 mol of amine per mole of anhydride, preferably with from 1.0 to 2.0 mol of amine per mole of anhydride, at from 50 to 300° C. When approx. 1 mol of amine is used per mole of anhydride, monoamides which additionally bear one carboxyl group per amide group are formed preferentially at reaction temperatures of from approx. 50 to 100° C. At higher reaction temperatures of from approx. 100 to 250° C., amides are formed preferentially from primary amines with elimination of water. When relatively large amounts of amine are used, preferably 2 mol of amine per mole of anhydride, amide ammonium salts are formed at from approx. 50 to 200° C. and diamides are formed at higher temperatures of, for example, 100-300° C., preferably 120-250° C. The water of reaction can be distilled off by means of an inert gas stream or removed by means of azeotropic distillation in the presence of an organic solvent. For this purpose, preference is given to using 20-80% by weight, in particular 30-70% by weight, especially 35-55% by weight, of at least one organic solvent. Useful monoamides are copolymers (50% dilution in solvent) having acid numbers of 30-70 mg of KOH/g, preferably 40-60 mg of KOH/g. Corresponding copolymers having acid numbers of less than 40 mg of KOH/g, especially less than 30 mg of KOH/g, are considered as diamides or imides. Particular preference is given to monoamides and imides.
Suitable amines are primary and secondary amines having one or two C8-C16-alkyl radicals. They may bear one, two or three amino groups which are bonded via alkylene radicals having two or three carbon atoms. Preference is given to monoamines. In particular, they bear linear alkyl radicals, but they may also contain minor amounts, for example up to 30% by weight, preferably up to 20% by weight and especially up to 10% by weight of (1- or 2-)branched amines. Either shorter- or longer-chain amines may be used, but their proportion is preferably below 20 mol % and especially below 10 mol %, for example between 1 and 5 mol %, based on the total amount of amines used.
Particularly preferred primary amines are octylamine, 2-ethylhexylamine, decylamine, undecylamine, dodecylamine, n-tridecylamine, isotridecylamine, tetradecylamine, pentadecylamine, hexadecylamine and mixtures thereof.
Preferred secondary amines are dioctylamine, dinonylamine, didecylamine, didodecylamine, ditetradecylamine, dihexadecylamine, and also amines having different alkyl chain lengths, for example N-octyl-N-decylamine, N-decyl-N-dodecylamine, N-decyl-N-tetradecylamine, N-decyl-N-hexadecylamine, N-dodecyl-N-tetradecylamine, N-dodecyl-N-hexadecylamine, N-tetradecyl-N-hexadecylamine. Also suitable in accordance with the invention are secondary amines which, in addition to a C8-C16-alkyl radical, bear shorter side chains having from 1 to 5 carbon atoms, for example methyl or ethyl groups. In the case of secondary amines, it is the average of the alkyl chain lengths of from C8 to C16 that is taken into account as the alkyl chain length n for the calculation of the Q factor. Neither shorter nor longer alkyl radicals, where present, are taken into account in the calculation, since they do not contribute to the effectiveness of the additives.
Particularly preferred copolymers B are monoamides and imides of primary monoamines.
The use of mixtures of different olefins in the polymerization and mixtures of different amines in the amidation or imidation allows the effectiveness to be further adapted to specific fatty acid ester compositions.
In a preferred embodiment, the additives, in addition to constituents A and B, may also comprise polymers and copolymers based on C10-C24-alkyl acrylates or methacrylates (constituent C). These poly(alkyl acrylates) and methacrylates have molecular weights of from 800 to 1 000 000 g/mol and are preferably derived from caprylic alcohol, caproic alcohol, undecyl alcohol, lauryl alcohol, myristyl alcohol, cetyl alcohol, palmitoleyl alcohol, stearyl alcohol or mixtures thereof, for example coconut alcohol, palm alcohol, tallow fatty alcohol or behenyl alcohol.
In a preferred embodiment, mixtures of the copolymers B according to the invention are used, with the proviso that the mean of the Q values of the mixing components in turn assumes values of from 23 to 27 and preferably values from 24 to 26.
The mixing ratio of the additives A and B according to the invention is (in parts by weight) from 20:1 to 1:20, preferably from 10:1 to 1:10, in particular from 5:1 to 1:2. The proportion of component C in the formulations of A, B and C may be up to 40% by weight; it is preferably less than 20% by weight, in particular between 1 and 10% by weight.
The additives according to the invention are added to oils in amounts of from 0.001 to 5% by weight, preferably from 0.005 to 1% by weight and especially from 0.01 to 0.5% by weight. They may be used as such or else dissolved or dispersed in solvents, for example aliphatic and/or aromatic hydrocarbons or hydrocarbon mixtures, for example toluene, xylene, ethylbenzene, decane, pentadecane, petroleum fractions, kerosene, naphtha, diesel, heating oil, isoparaffins or commercial solvent mixtures such as Solvent Naphtha, ®Shellsol AB, ®Solvesso 150, ®Solvesso 200, ®Exxsol, ®Isopar and ®Shellsol D types. They are preferably dissolved in fuel oil of animal or vegetable origin based on fatty acid alkyl esters. The additives according to the invention preferably comprise 1-80%, especially 10-70%, in particular 25-60%, of solvent.
In a preferred embodiment, the fuel oil, which is frequently also referred to as biodiesel or biofuel, is a fatty acid alkyl ester made from fatty acids having from 12 to 24 carbon atoms and alcohols having from 1 to 4 carbon atoms. Typically, a relatively large portion of the fatty acids contains one, two or three double bonds.
Examples of oils which are derived from animal or vegetable material and in which the additive according to the invention can be used are rapeseed oil, coriander oil, soya oil, cottonseed oil, sunflower oil, castor oil, olive oil, peanut oil, maize oil, almond oil, palmseed oil, coconut oil, mustardseed oil, bovine tallow, bone oil, fish oils and used cooking oils. Further examples include oils which are derived from wheat, jute, sesame, shea tree nut, arachis oil and linseed oil. The fatty acid alkyl esters also referred to as biodiesel can be derived from these oils by processes known from the prior art. Rapeseed oil, which is a mixture of fatty acids partially esterified with glycerol, is preferred, since it is obtainable in large amounts and is obtainable in a simple manner by extractive pressing of rapeseeds. In addition, preference is given to the likewise widely available oils of sunflowers and soya, and also to their mixtures with rapeseed oil.
Particularly suitable biofuels are low alkyl esters of fatty acids. These include, for example, commercially available mixtures of the ethyl, propyl, butyl and in particular methyl esters of fatty acids having from 14 to 22 carbon atoms, for example of lauric acid, myristic acid, palmitic acid, palmitolic acid, stearic acid, oleic acid, elaidic acid, petroselic acid, ricinolic acid, elaeostearic acid, linolic acid, linolenic acid, eicosanoic acid, gadoleic acid, docosanoic acid or erucic acid, each of which preferably has an iodine number of from 50 to 150, in particular from 90 to 125. Mixtures having particularly advantageous properties are those which comprise mainly, i.e. comprise at least 50% by weight, methyl esters of fatty acids having from 16 to 22 carbon atoms, and 1, 2 or 3 double bonds. The preferred lower alkyl esters of fatty acids are the methyl esters of oleic acid, linoleic acid, linolenic acid and erucic acid.
Commercial mixtures of the type mentioned are obtained, for example, by hydrolyzing and esterifying or by transesterifying animal and vegetable fats and oils with lower aliphatic alcohols. Equally suitable as starting materials are used cooking oils. To prepare lower alkyl esters of fatty acids, it is advantageous to start from fats and oils having a high iodine number, for example sunflower oil, rapeseed oil, coriander oil, castor oil, soya oil, cottonseed oil, peanut oil or bovine tallow. Preference is given to lower alkyl esters of fatty acids based on a novel type of rapeseed oil, more than 80% by weight of whose fatty acid component is derived from unsaturated fatty acids having 18 carbon atoms.
A biofuel is therefore an oil which is obtained from vegetable or animal material or both or a derivative thereof which can be used as a fuel and in particular as a diesel or heating oil. Although many of the above oils can be used as biofuels, preference is given to vegetable oil derivatives, and particularly preferred biofuels are alkyl ester derivatives of rapeseed oil, cottonseed oil, soya oil, sunflower oil, olive oil or palm oil, and very particular preference is given to rapeseed oil methyl ester, sunflower oil methyl ester and soya oil methyl ester. Particularly preferred biofuels or components in the biofuel are additionally also used fatty acid esters, for example used fatty acid methyl esters.
The additive can be introduced into the oil to be additized in accordance with prior art processes. When more than one additive component or coadditive component is to be used, such components can be introduced into the oil together or separately in any desired combination.
The additives according to the invention allow the CFPP value of biodiesel to be adjusted to values of below −20° C. and sometimes to values of below −25° C., as required for provision on the market for use in winter in particular. Equally, the pour point of biodiesel is reduced by the addition of the inventive additives. The inventive additives are particularly advantageous in problematic oils which contain a high proportion of esters of saturated fatty acids of more than 4%, in particular of more than 5% and especially having from 7 to 25%, for example having from 8 to 20%, as present, for example, in oils from sunflowers and soya. Such oils are characterized by cloud points of above −5° C. and especially of above −3° C. It is thus also possible using the inventive additives to adjust mixtures of rapeseed oil methyl ester and sunflower and/or soya oil fatty acid methyl ester to CFPP values of −20° C. and below. In addition, the oils additized in this way have a good cold temperature change stability, i.e. the CFPP value remains constant even on storage under winter conditions.
To prepare additive packages for specific solutions to problems, the additives according to the invention can also be used together with one or more oil-soluble coadditives which alone improve the cold flow properties of crude oils, lubricant oils or fuel oils. Examples of such coadditives are polar compounds which effect paraffin dispersion (paraffin dispersants) and also oil-soluble amphiphiles with the proviso that they differ from the comb polymers B.
The additives according to the invention can be used in a mixture with paraffin dispersants. Paraffin dispersants reduce the size of the paraffin crystals and have the effect that the paraffin particles do not separate but remain dispersed colloidally with a distinctly reduced tendency to sedimentation. Useful paraffin dispersants have proven to be both low molecular weight and polymeric oil-soluble compounds having ionic or polar groups, for example amine salts and/or amides. Particularly preferred paraffin dispersants comprise reaction products of secondary fatty amines having from 20 to 44 carbon atoms, in particular dicocoamine, ditallow fat amine, distearylamine and dibehenylamine with carboxylic acids and derivatives thereof. Paraffin dispersants which are obtained by reacting aliphatic or aromatic amines, preferably long-chain aliphatic amines, with aliphatic or aromatic mono-, di-, tri- or tetracarboxylic acids or their anhydrides (cf. U.S. Pat. No. 4,211,534) have proven particularly useful. Equally suitable as paraffin dispersants are amides and ammonium salts of aminoalkylene polycarboxylic acids such as nitrilotriacetic acid or ethylenediaminetetraacetic acid with secondary amines (cf. EP 0 398 101). Other paraffin dispersants are copolymers of maleic anhydride and α,β-unsaturated compounds which may optionally be reacted with primary monoalkylamines and/or aliphatic alcohols
(cf. EP 0 154 177) and the reaction products of alkenyl-spiro-bislactones with amines (cf. EP 0 413 279 B1) and, according to EP 0 606 055 A2, reaction products of terpolymers based on α,β-unsaturated dicarboxylic anhydrides, α,β-unsaturated compounds and polyoxyalkylene ethers of lower unsaturated alcohols.
The mixing ratio (in parts by weight) of the additives according to the invention with paraffin dispersants is from 1:10 to 20:1, preferably from 1:1 bis 10:1.
The additives can be used alone or else together with other additives, for example with other pour point depressants or dewaxing assistants, with antioxidants, cetane number improvers, dehazers, demulsifiers, detergents, dispersants, defoamers, dyes, corrosion inhibitors, conductivity improvers, sludge inhibitors, odorants and/or additives for reducing the cloud point.
Characterization of the Test Oils:
The CFPP value is determined to EN 116 and the cloud point is determined to ISO 3015.
The following additives were used:
The ethylene copolymers used are commercial products having the characteristics specified in Table 2. The products were used as 65% or 50% (A3) dilutions in kerosene.
Maleic anhydride (MA) is polymerized with α-olefins in a relatively high-boiling aromatic hydrocarbon mixture at 160° C. in the presence of a mixture of equal parts of tert-butyl peroxybenzoate and tert-butyl peroxy-2-ethylhexanoate as a radical chain initiator. Table 3 lists by way of example, various copolymers and the molar proportions of the monomers used to prepare them, and also chain length (R) and molar amount (based on MA) of the amine used for derivatization and the factor Q calculated therefrom. Unless stated otherwise, the amines used are monoalkylamines.
The reactions with amines are effective in the presence of Solvent Naphtha (50% by weight) at from 50 to 100° C. to give the monoamide or to give the amide ammonium salt, and at from 160 to 200° C. with azeotropic separation of water of reaction to give the imide or diamide. The degree of amidation is inversely proportional to the acid number.
The poly(alkyl (meth)acrylates) used were the compounds listed in the table as 50% dilutions in relatively high-boiling solvent. The K values were determined according to Ubbelohde at 25° C. in 5% toluenic solution.
Effectiveness of the Terpolymers
The CFPP value (to EN 116, in ° C.) of different biofuels according to the above table was determined after the addition of 1200 ppm, 1500 ppm and also 2000 ppm, of additive mixture. Percentages relate to parts by weight in the particular mixtures. The results reported in Tables 5 to 7 show that comb polymers having the factor Q according to the invention achieve excellent CFPP reductions even at low dosages and offer additional potential at higher dosages.
Cold temperature change stability of fatty acid methyl esters
To determine the cold temperature change stability of an oil, the CFPP
DIN EN 116 before and after a standardized cold temperature change treatment are compared.
500 ml of biodiesel (test oil E1) are treated with the appropriate cold temperature additive, introduced into a measuring cylinder and stored in a programmable cold chamber for a week. Within this time, a program is run through which repeatedly cools to −13° C. and then heats back to 3° C. 6 of these cycles are run through in succession (Table 8).
Subsequently, the additized oil sample is heated to room temperature without agitation. A sample of 50 ml is taken for CFPP measurements from each of the upper, middle and lower sections of the measuring cylinder.
A deviation between the mean values of the CFPP values after storage and the CFPP value before storage and also between the individual phases of less than 3 K shows a good cold temperature change stability.
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|---|---|---|---|
| 103 49 851 | Oct 2003 | DE | national |
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