2-SUBSTITUTED SUCCINATE ESTERS

Abstract: This invention relates to a process for producing 2-substituted succinate esters of formula (I) by reacting (a) a dicarboxylic compound with a first alcohol R'O[CHR''.CH2O]xH where x is 0 or an integer from 1-6 in the presence of a catalyst to form a hydrocarbyl ester or, when x = 1-6, a hydrocarbyloxy alkylene ester of maleic and/or fumaric acid and (b) the ester from step (a) with an alkaline earth metal alkoxide in the presence of a second alcohol R.OH to form the 2-substituted succinate ester of formula (I). The esters and paint formulations based thereon are also claimed.

Description: 2-SϋBSTITUTEP SUCCINATE ESTERS This invention relates to a process for producing 2-substituted succinate esters with low colour and use of said ether esters as diluents in paint and polymer formulations One of the processes used hitherto to produce 2-substituted succinate esters is the combined transesterification and Michael addition reaction of an alcohol or a monoether of a polyoxyal ylene glycol as described in GB-A-552715 in which ether esters of hydroxysuccinic acid and unsaturated alcohols are prepared by reacting in a single step under anhydrous conditions an alkyl ester of maleic acid with an unsaturated alcohol in the presence of a magnesium alkoxide catalyst. However, this method when repeated for instance with an octadienol/di methyl maleate system using magnesium methoxide as a catalyst gives products which have a deep red colour It may be possible to overcome this colour problem in the products described in this prior art by distillation However, such a method is unlikely to be practicable with the synthesis of esters contemplated in the present invention since they are all meant to have relatively low volatility and hence are not amenable to purification by distillation. It has now been found that 2-substituted succinate esters, some of which are novel, can be produced in commercially viable yields and purity by using a two- stage process Accordingly, the present invention relates to a process for producing 2- substituted succinate esters of the formula (I) said process comprising reacting a. a dicarboxylic compound selected from the group consisting of maleic acid, maleic anhydride, fumaric acid and the dialkyl ester of maleic or fumaric acid with an alcohol R'0[CHR" CT^O^H where x is 0 or an integer from I -6 in the presence of a catalyst to form a hydrocarbyl ester or, when x = 1-6, a hydrocarbyloxy alkylene ester of aleic and/or fumaric acid and the ester from step (a) with an alkaline earth metal alkoxide in the presence of a further amount of the alcohol to form the 2-substituted succinate ester of formula (I) in which R' is an u satui ated hydi ocarbyl oi allyhcallty unsaturated hydrocarbyloxy alkylene gi oup having at least carbon atoms, R" is H or an alkyl oi an alkylene group having 1 to 2 carbon atoms and, each of a and Λ is same oi diffei ent and has a value of 0 or is an integer from 1 -6 By the expression "alkylene" as used herein and thi oughout the specification is meant a divalent hydi ocarbyl group such as eg a -CH 2 -(CHR") / - CH 2 -gιoup wherein / = 0 oi an integer and R" has the same notation as above R' is denved fi om the l eactant alcohol R'0[CHR" CH 2 O] A H where x is 0 oi an integei from 1 -6 which is used lot making the succinate ester and can be an allylic hydiocaibyl or an allylic hydi ocarbyloxy alkylene group Thus, the reactant alcohol is an allylic alcohol and includes inter alia 2-ethyl-hex-2-en- l -ol, 2-octen- l -ol, l -octen-3-ol, 2,7-octadienol, 2-ethyl allyl alcohol, hept-3-en-2-ol, 4-methyl pent-3-en-2-ol, 4-t-butoxy but-2-en- l -ol (also called l ,4-but-2-ene diol mono- tertiary butyl ethei ), 4-n-butoxy but-2-en- l -ol (also called l ,4-but-2-ene diol mono-n-butyl ethei ); cinnamyl alcohol, and isophorol The l eactant alcohol, R'0[CHR" CH 2 0] v H where x is 0 or an integer from 1 -6, can be pi epared in sevei al ways known to those skilled in the art For instance, this reactant alcohol, eg an allylic alcohol, can be produced by the l eduction of the corresponding α,β-unsaturated aldehyde eg by hydrogenation, which will generate a mixtui e of the allylic alcohol and its saturated analogue Some other allylic alcohols may be produced from conjugated dienes via the well known addition reactions Fui thei moi e, othei allylic alcohols may be produced by initially foi ming an unsatui ated estei ti m an olefin and a carboxy c acid followed by hydrolysis of the ester to a mixture of isomeric allylic alcohols. This latter reaction may, like some of the other reactions mentioned above, result in a mixture of products which includes inter alia the desired allylic alcohol, isomers thereof and saturated analogues thereof The mixtures of allylic alcohol with the saturated analogue thereof and/or the isomers thereof can be then used as such, or, after further purification to isolate the desired allylic alcohol, to prepare the esters represented by formula (I) above. Where the reactant alcohol is itself an allylic unsaturated hydroxy ether, ie x = 1 -6, this may be derived by alkoxylation of an alcohol, eg allylic ether alcohol, suitably in the presence of a catalyst to form the hydroxy ether. Where a catalyst is used it should be such that it does not cause rearrangement of the allylic function and hence, amphoteric, basic or acidic catalysts may be used. The catalyst can be heterogeneous or homogeneous The alkoxylation step is suitably carried out in the presence of a base catalyst. Examples of base catalysts that may be used include alkali metal hydroxides such as sodium or potassium hydroxide and other metal salts such as potassium acetate. The alkoxylation reaction to form the hydroxy ether of the allylic alcohol can be carried out using one or more of the epoxides which include inter alia ethylene oxide, propylene oxide, butene oxide and butadiene mono-oxide. The amount of epoxide used for this step would depend upon the number of alkoxy groups desired in the hydroxy ethe The amount of epoxide used is suitably in the range from 0. 1 to 20 moles, preferably from I to moles based on the allylic alcohol reactant. The alkoxylation reaction is suitably carried out at a temperature in the range from 50 to 180°C, preferably from 60 to 140°C. The reaction pressure for this step is suitably autogenous but is preferably from 100 to 700 KPa. The hydroxy ether formed in this step is suitably separated from the reaction mixture by neutralisation using eg magnesium silicate, then filtered to remove the neutralising agent and the salt of neutralisation so formed to leave behind filtrate comprising the desired hydroxy ether. The hydroxy ether so produced can be used either as such without purification, or, optionally, after purification (eg by distillation) for the esterification stage. Thus, the 2-succinate esters of formula (I) are prepared by reacting in the first stage (a) the reactant alcohol with maleic acid or anhydride and/or fumaric acid or esters thereof in the presence of a catalyst The catalyst used in this step can be zinc acetate, dibutyl tin oxide, stannous oxalate, para-toluene sulphonic acid oi phosphoric acid This reaction is suitably carried out at a temperature below 150°C, preferably from 100-130°C The completion of the reaction is ascertained by GC analysis using a CP-SIL5 50 m capillary column and a flame ionisation detectoi Upon completion of the reaction, the unreacted materials are stripped out by steam stripping oi by azeoti opic distillation eg using an azeotroping agent such as eg cyclohexane The catalyst may then be neutralised or removed as appropriate, the solids filtered and the ester in the filtrate recovered The ester product from this step (a) is then further reacted in a step (b) with a further amount of the leactant alcohol in the piesence of an alkaline earth metal alkoxide catalyst The function of this step (b) is to enhance the amount of the desired 2-succmate estei in the pioduct fio step (a) at the expense of the maleates and fumaiates in said pi duct The alkaline earth metal alkoxide may be dei ive from the second leactant alcohol or from another alcohol The alkaline earth metal alkoxide is piefei ably magnesium alkoxide The amount of alkaline earth metal alkoxide used must be sufficient to compensate for loss of catalyst due to its l eaction with any l esidual acids oi watei present in the products from stage (a) of the leaction or the leactant alcohol The reaction with the alkaline earth metal alkoxide is suitably earned out at a tempeiatui e below 120°C, suitably in the l ange from 40 to 80°C and step (b) is suitably earned out at atmospheric, subatmospheπc oi supeiatmospheiic piessuies T he piessures used are preferably in the l ange fiom atmosphei ic to 50 Kpa, mote piefeiably fiom atmospheric to 5 KPa This division of the reaction into two stages allows the use of relatively mildei conditions than has hitherto been possible and as a consequence affords an impi oved pioduct which is less coloured The estei s foi med by this piocess may be a mixtuie of the desired esters of formula (1) and the corresponding unsatuiated analogues comprising the maleic acid oi fumaπc acid estei s Thus, foi example, leaction of 2-ethyl hexenol with maleic acid oi anhydiide followed by l eaction of the product with magnesium alkoxide of 2-ethylhexenol as catalyst would give use to a pioduct which primarily compπses 2-(2-ethyl hexenoxy)-dι[2-(2-ethyl hexenyl)j succinate Similarly, when octadienoxy ethanol is leaded with maleic acid oi anhydride, followed by the l eaction of this product with the magnesium alkoxide of octadienoxy ethanol as catalyst the l esultant pi duct compi ises dι-f(2-octadιenoxy) ethyl]-2-[(2- octadienoxy) ethoxy] succinate Both of these are novel esters not reported hitherto Similarly, when 2,7-octadienol is reacted with dimethyl maleate, followed by reaction of the resultant product with further aliquots of the reactant alcohol in the presence of magnesium alkoxide catalyst, the product obtained is 2- octadienoxy di-octadienyl succinate A feat i e of the two-stage process of the present invention is that it uses relatively milder conditions than a conventional Michael addition reaction For instance, no l eflux conditions need be used during this step Furthermore, the present pi cess enables the proportion of the 2-substituted succinate ester in the reaction pi oduct to be enhanced considerably without leading to undesirable polymei formation or increasing the colouration of the ester product Moreover, the pi esent process gives better yields of the desired 2-substιtuted succinate ester due to the mildei conditions employed The estei of the present invention have low volatility and relatively low viscosity suitably below 1 00 mPa s, thereby rendering them a suitable solvent component foi cui able paint and varnish formulations These ether esters are especially suitable as the so called "reactive dilutents" foi paint formulations and m particulai those containing alkyd iesins Reactive diluents ai e usually compounds oi mixtui es of compounds of i elatively low viscosity, a relatively high boiling point (oi low satui ated vapoui pi essure) which act as solvents during the formulation and processing of the coating An advantage of reactive diluents is that such diluents can copolymei ise with components of the alkyd resin Hence reactive diluents may be used to l eplace part oi all of the ti aditional solvents normally used in such foi mulations thei eby l educing losses of the solvent to atmosphere on drying of the coating Use of l eactive diluents comprising esters of polyhydnc alcohols which have been partially etheπfied with allyl alcohol are described in EP- A-0 253 474 Alkyd tesins ai e well known components of decorative paints (see, for example, "The T echnology of Paints, Varnishes and Lacquers" by C R Maι tens(Fd ), published by Robert Krieger Publishing ( 1 74) and can be prepared fi om polybasic acids oi anhydndes, polyhydnc alcohols and fatty acids or oils US-A-3 8 19 720 descnbes methods of preparing such alkyd formulations Alkyd coating compositions usually contain large amounts of solvents (eg mineral spirits and ai omatic hydi ocai bons) The compositions of the pi esent invention ai e highly suitable for use as reactive diluents The relative ratios of reactive diluent to the alkyd resin in a formulation can be derived from the ranges quoted in published EP-A-0 305 006 In an example in which the ieactive diluent replaces all of the traditional solvent, the ratio of reactive diluent to alkyd resin is suitably in the range from 1 -50 99-50 parts by weight, eg 5-50 95-50, preferably from 5-25 95-75 and more preferably from 5- 15 95-85 parts by weight On the othei hand, where used in a conventional paint foimulation, such a diluent can replace all or part of a traditional solvent such as white spirit 1 he foimulations may contain further components such as catalyst, dnei , antiskmning agent, pigments, pigment stabilisers, rheology controllers (e g for sag conti ol), UV and oxidation stabilisers, flow additives, microgels (e g to enhance hardness) and other additives The formulations may also need to include watei scavengei such as t alkyl orthoformates, molecular sieves oi zeolites whei e the i eactive diluent used is susceptible to hydrolysis such as eg some of the ethei estei de vatives Furthermor e, where such water scavengers ai e used it may be necessai y to use them in combination with compatible pigment stabilizei s Whei e a dnei (siccative) is used this may further conti ibute towai ds the solvent content of the formulation For formulations compnsing an oxidatively curing alkyd resin and a siccative/dnei such as cobalt complexes, impurities which can have a co-ordination affinity for the siccative dnei such as cobalt complexes can affect adversely the drying speed and stability of the paint Examples of such impurities include maleic acid and tnethyl amine In pat ticulai , it has been found desn able to minimise the acidity of the estei mixtui e used as i eactive diluent in such formulations to a value of 7000 ppm, pi efeiably 3000 pp moi e pi efei ably ^ 1000 ppm w/w of KOH It has also been found that when a mixtuie of esters, le the succinates, fumai tes and maleates, is used as a i eactive diluent in such formulations compnsing an oxidatively cunng alkyd l esins, the pi opeities/performance of the diluent can be vaned by changing the l elative pioportions of the three esters present in such a diluent Foi example, mixtures with a lelatively lower amount of maleates exhibit bettei hai dness and drying pi perties compared with those having relatively highei amounts of such maleates Moi eover it has also been observed that foi mulations compnsing these estei s display a decreased tendency towards wi inkling This i e dei s them pai ticulai ly suitable when using formulations comprising high solid systems/one-coat paints have to be applied to generate a gieatei thickness of the i elevant coating without impai ng the ability of such thicker layers to harden thiough For some uses it is preferable that the free alcohol content of the diluent is minimised in order to facilitate drying of the formulation A feature of the present invention is that ether esters of formula (I) when used as reactive diluents in paint oi coating formulations, especially those compnsing alkyd resins, enhance the performance of these formulations In particulai , whei e a mixture of products comprising ether esters of the present invention derived by reacting an allylic alcohol or a hydroxy ether thereof with maleic acid/anhydride 01 fuma c acid is used as reactive diluent, they enhance their pei formance when compai ed with that of the unsaturated esters when used alone A furthei aspect of the present invention is that such esters when used in a relatively pui e state do not cause any haze in the formulation Where there is likely to be a nsk of such haze toi mation, eg due to the presence of impurities such as eg l esins oi poiymei s formed din ing the synthesis of the esters used or during storage of such foi mulations, it is beneficial to use inhibitors such as eg butylated hydroxy- toluene (2,6-butoxy-4-methyl phenol) oi 2,4 b-tei /-butyl phenol Such inhibitors not only have the advantage of pi eventing haze formation but also render the foi mulations safei to handle by inhibition of othei unwanted reactions in the formulation such as eg pei oxidation Uses of the molecules of this invention include the partial or total l eplacement of ti aditional hydi ocai bon-based solvents in solvent-borne alkyd paints used foi pnmei , undei coat and topcoat decoi ative applications as well as in lndustnal applications such as alkyd pnmei s and UV-cure The molecules of this invention are also suitable for use as co-monomers, f i example in vinyl acetate-based poiymei s used in emulsion paints In this case, the molecules of this invention impart a temporary plasticisation to the paint film, befoi e aii-cunng to a hai d finish They can, thei efoi e, facilitate the partial or total l eplacement of coalescent solvents In addition, the molecules could be used in watei -based paints based on aci ylic and alkyd l esms, in addition to, oi instead of, coalescent solvents The pi esent invention is fui thei lllusti ated with refeience to the following Examples EXAMPLE 1 : Genet al Method Reaction of * an allylic ethei -alcohol with a maleate The following appai atus was assembled A five-litre flanged flask with an insert pipe for a nitrogen sparge, a thermowell for thermocouple, and a Dean and Stark apparatus with double-walled condenser. The flask was heated with an electric heating mantle which was controlled with a eurotherm controller connected to the thermocouple. The nitrogen sparge pipe was inserted so that the nitrogen flow agitated the flask contents and provided mixing during the course of the reaction The nitrogen flow also served to entrain out the liberated methanol and force the reaction to completion. To the flask was added dimethyl maleate (914.3g), 2,7-octadienol (2375g) and stannous oxalate (3 1.2g). The mixture was sparged with nitrogen for 10 minutes to remove air and the nitrogen flow was then reduced to a level which ensured efficient mixing. The mixture was then heated in stages to 130°C ( e.g. 80°C for 1 minutes, then 100°C for 10 minutes and then 120°C for 10 minutes). The progress of the reaction was monitored by collection of the methanol collected in the Dean and Stark apparatus. In order to drive the reaction to completion the temperature was raised to I40°C after 7hrs at 130°C When 90% of the methanol had been collected, the reaction mixture was sampled hourly and analysed by GC. The reaction was adjudged complete when the level of the "half ester" (methyl octadienyl maleate/fumarate) fell to below 0.3% w/w and this took approximately 3 I hours. At this point the heating was switched off and the reaction mixture allowed to cool to room temperature The product from the reaction was then decanted from any solids in the reaction flask. This product was then charged to a heated decanter (40°C) with an equal volume of 5% w/w aqueous sodium hydroxide solution The mixture was stirred for 20 minutes and then allowed to separate and the lower aqueous phase decanted. This base wash was repeated and the remaining organic phase was washed with saturated brine until the aqueous phase reached a steady pH. The organic phase was then heated (100°C) under reduced pressure (<- 500 Pa (- 5 mBar)) on a rotatory evaporator to remove residual water and the majority of the excess octadienol. After cooling, the product was filtered and transferred to a 5-litre three-necked round-bottomed quickfit flask This flask was equipped with a still-head condenser and reciever flask (Perkin triangle), a thermocouple, a stream inlet pipe, and a eurotherm controlled heating mantle The apparatus was evacuated to 4000 Pa (40 mBar) and the product heated to I 20°C The supply of steam was then connected and the residual traces of octadienol were removed The purification was judged complete when the volume of the heads product aqueous phase to increased more than 5 times that of the organic phase. A ter cooling down the product was then treated with activated carbon ( l%w/w, 100°C 2Hrs, < 500 Pa (< 5 mBar)) on a rotatory evaporator. The cooled mixture was filtered through dried celite to obtain the final product which had the following analyses: OH number - 4 mg KOH/g (titration) total acid - 46 ppm KOH/g (titration) maleic acid / anhydride - I Oppm (HPLC) Fumaric acid - - l Oppm (HPLC) tin - l Oppm (atomic absorption) sodium - 20ppm ( atomic absorption, detection limit) chlorine - ' l Oppm (atomic absorption detection limit) GC "CPSil5" column - octadienyl methyl fϊimarate/maleate (0. 1 l % w/w) di-(2,7-octadienyl) maieate (73% w/w) - di-(2,7-octadienyl) fumarate (22% w/w) 2-(2,7-octadienoxy) di-(2,7-octadienyl) succinate (3% w/w) The GC assignment was supported by GC/MS and a H nmr and C nmr studies. The GC/MS used a VG Trio- 1000, operated according to the manufacturers instructions under the following conditions: GC column 25mx0.32mm DB5 (0.25 micron film) temperature programme 40°C (3 mins) @ l OC/min to 320 r> C( l ϋmins) injection I microlitre ( l % solution in acetone) on column 40°C ammonia chemical ionisation (Cl) scan range 50-800 scan rate l /s It was found that the deduction of molecular weights from the CI spectra is rather less straightforward than is usual account of (a) extensive rearrangements of fumarates in particular giving [M+3] and [M+20] ions in addition to the usual [PvH l J and [M+ l 8] ions and (b) extensive fragmentation exhibited by some species. As a result the GC peaks were assigned by interpretation. In addition to the assigned peaks an additional species was identified which was assigned to a lactone. These assignments were confirmed by H and ' C nmr. Table 1 gives tentative assignments of the observed C nmr peaks It should be noted that the two isomeric octadienols ( 2,7-octadienol and l,7-octadien-3-ol) though not separable by the GC method used can be identified by nmr and are recorded in the nmr assignment Table 1. The correspondence to the GC was confirmed again by integration of the nmr spectrum of several samples in which the composition varied The lactone found by GC/MS was also observed in the nmr and quantified at approximately 6 2% (tenative structure given in Table 1 ) TABLE 1 8 7 6 5 4 3 2 1 2,7-OctadienoI CH 2 =CH CH; CH; CH; CH=CH CH 2 OH Some of the assignments are tentative TABLE 1 (continued) 2-(2.7-octadienoxy) di-2.7-octadienyl succinate 8 7 6 5 4 3 2 1 9 10 1 1 12 Y <r T - 8' -> 1" 2" 3" 4" 6 5" 7" 8" Cl l;-CI I CH; CH 2 CH. CH=CH CH, 0 (0=)C CH 2 CH (C(=0) 0 CH. CH=CH CH 2 CH 2 CH 2 CH=CH 2 ) 0 CH 2 CH=CH CH 2 .CH 2 .CH 2 .CH---CH 2 NB Due to the loss of symmetry (cf maleate or fumarate) in the molecule, all the octadienyl/octadienoxy groups are magnetically ine uiva ent Lactones Species believed to be lactones have been identified in the octadienyl ester samples Whilst there appear to be two possible ro σ * > isomers of this lactone. the C NMR data fits the following structure CH 2 =CH CH 2 CH 2 CH=CH CH CH CH 2 C(=0) O CH 2 CH=CH.CH 2 CH 2 CH 2 CH=CH 2 8 7 6 5 4 3 2 1 1 10 9 1' The mixed ester product from step (a) comprising a relatively low amount of the 2-succinate ester is reacted in a step (b) with a second reactant alcohol in the presence of a magnesium alkoxide catalyst as follows: Step (b): AUyloxysiiccinate Enhancement - General method All apparatus used was dried ( 100°C oven) before use and the liquid reagents were be dried ( <0.05%w/w water - molecular sieves 3a). The total acid number (TAN) of the ester reagent was measured. To a conical flask was charged a pear shaped magnetic follower; The mixed ester product from step (a) - 546.6g 2,7-Octadienol - 14.82g magnesium ethoxide# - 4.858g # [assuming that I mole of acid is neutralised by I mole of magnesium ethoxide, l ppm KOH/g is - I x I 0 " '7 Mol Wt of KOH moles KOH/g I x l 0 ' " /56. l l moles KOH/g The molecular weight of magnesium ethoxide - 1 14.44 So TAN of I ppm KOH will require I 14.44 x 1 x I 0 "6 /56. 1 1/g If the sample weighs Y grams, if the sample TAN is Z pp /KOH then the amount of magnesium ethoxide required to neutralise the acid in the sample - I 14.44 x Y x Z x 1 x I 0 '( 756. 1 1 . To this amount must be added the amount of magnesium ethoxide needed to catalyse the reaction eg 0.35% w/w ] A nitrogen top cover was supplied to the flask and the mixture with magnetic stirring heated to 80°C. The reaction was monitored by GC and samples withdrawn at different degrees of conversion. The samples were purified by using the following procedure. An equal volume of saturated brine was added to the sample in the separating funnel and the mixture shaken for 5 minutes. The mixture separated into two phases, an upper organic phase and a lower aqueous phase The lower aqueous phase was decanted and the procedure repeated until the the aqueous layer pH decreased to l± 0.5 To the upper organic phase was added 1% w/w activated carbon and the mixture was heated to 100°C for l hr at 133.3 Pa ( l mmHg) on a rotatory evaporator The material was then allowed to cool to room temperature and filtered through a cake of dried celite filter. aid. It was found that it was possible to obtain conversions of the maleate starting material to the allyloxysuccinate in excess of 97% by this method. 2. Testing of reactive diluents in paint formulations: A good reactive diluent must meet a range of criteria including low odour and toxicity, low viscosity and the ability to "cut" the viscosity of the paint to facilitate application on the surface to be coated therewith. Furthermore, the diluent should not have a markedly adverse effect on the properties of the paint film such as drying speed, hardness, degree of wrinkling, durability and tendency to yellowing. The reactive diluents described above have therefore been tested in paint applications using both clear and pigmented paints. The diluents have been compared with paints formulated using white spirit, a conventional thinner. 2.1 Unpigmented "Clearcoat" Formulations: 2.1.1 Materials Used Unpigmented ("clearcoat") paint formulations were prepared using a high solids alkyd resin SETAL® EPL 9 1 / 1 / 14 (ex AKZO NOBEL, and described in "Polymers Paint and Colour Journal, 1 92, 182, pp. 372). In addition to the diluent, Siccatol® 938 drier (ex AKZO NOBEL) and methyl ethyl ketonc-oxime (hereafter "MEK-oxime") anti-skinning agent were used. Where used, the white spirit was Exxon type 100. The nominal proportions of the above materials in the paint formulations were FABLE 2 Note that, for white spirit formulations only, the proportions of drier and antiskinning agent were calculated on the basis of the resin only Thus, the concentration of these components in the paint was lower than for other diluents 2.1.2 Method of Preparation of Clearcoat Formulations: Alkyd resin and diluent (2-(2.7-octadienoxy)-di-2,7-octadienyl succinate) were mixed in glass jars for 2 hours (eg using a Luckham multi-mix roller bed) in the proportions required to achieve a viscosity (measured via the ICI cone and plate method using a viscometer supplied by Research Equipment (London) Limited) of 68 ± 3 Pa s (6.8 ± 0.3 poise). Typically, this resulted in a mixture which was ca. 85% w/w resin. If further additions of diluent or resin were required to adjust the viscosity to 68 ± 3 Pa s (6.8 ± 0 3 poise), a further hour of mixing was allowed. The required quantity of drier was added and, after mixing ( 1 hour), the required amount of anti- skinning agent was added. After final mixing for at least 30 minutes, the viscosity of the mixture was measured to ensure that the viscosity was between 61 and 69 Pa s (6. 1 and 6.9 poise). The mixture ("formulation") was then divided into two jars so as to leave ca 10- 15% v/v headspace of air in the sealed jars. One of the jars was stored at 23 °C in darkness for 7 days before paint applications tests were performed The second jar was stored ("aged") at 35°C in daylight for 14 days before applications tests were performed 3. Test Procedures used for Clearcoat Formulations: 3.1 Application of paint film: Thin films were applied to cleaned glass test plates using Sheen cube or draw-bar applicators with a nominal 75μm gap width 3.2 Viscosity measurements and results: The viscosity of each diluent was measured at 23 °C using a suspended level viscometer. Densities of the diluents were taken as an average of three readings made at 25°C using density bottles with a nominal 10 cm- 1 capacity, calibrated with wate TA BLE 3 : Viscosity of reactive diluents 3.3 Drying Performance: Drying performance was measured using films applied to 30 cm x 2.5 cm glass strips and BK drying recorders. The BK recorders were enclosed in a Fisons controlled temperature and humidity cabinet so that the drying experiment could be performed at 1 °C and at 70% relative humidity. Sample performance was assessed on the basis of the second stage xit ~ drying (dust drying time, T2). TABLE 4 The above process was repeated with the product from Example 1 using the enhancement method (b) which achieved an allyloxy succinate yield of 97%. The corresponding drying times were as follows: Fresh Aged 5 6 hours 4 hours

Claims: We Claim: 1 A process for producing 2- substituted succinate esters of the formula (I) said process comprising reacting a a dicarboxylic compound selected from the group consisting of maleic acid, maleic anhydride, fumaric acid and the dialkyl ester of maleic or fumaric acid with an alcohol R'0[CHR" CH 2 O] Λ H where x is 0 or an integer from 1 -6 in the presence of a catalyst to form a hydrocarbyl ester or, when = 1 - 6, a hydrocarbyloxy alkylene ester of maleic and/or fumaric acid and b the ester from step (a) with an alkaline earth metal alkoxide in the presence of a further amount of the alcohol to form the 2-substituted succinate ester of formula (1) in which R' = R and is an unsaturated hydrocarbyl or allylically unsaturated hydrocarbyloxy alkylene group having at least 5 carbon atoms, R" is H or an alkyl or an alkylene group having I to 2 carbon atoms as hereinbefore defined and, each of and b is same or different and has a value of 0 or is an integer from I -6 2 A process according to Claim I wherein R' is derived from the reactant alcohol R'O[CFFR" CH 2 O] x H where x is 0 or an integer from 1-6 which is used for making the succinate ester and can be an allylic hydrocarbyl or an allylic hydrocarbyloxy alkylene group 3 A process according to any one of the pieceding Claims wherein the leactant alcohol is an allylic alcohol and includes inlei alia 2-ethyl-hex-2-en-l-ol, 2-octen-l-ol, l-octen-3-ol, 2,7-octadienol, 2-ethyl allyl alcohol, hept-3-en-2-ol, 4- methyl pent-3-en-2-ol, 4-t-butoxy but-2-en-l-ol 4-n-butoxy but-2-en-l-ol; cinnamy] alcohol, and isophorol 4 A piocess according to any one of the pieceding Claims wherein the 2- succinate estei of formula (1) is piepaied by reacting in the first stage (a) the ieactaπt alcohol with maleic acid oi anhydiide and/or fumaric acid or esters thereof in the piesence of a catalyst 5 A piocess accoiding to ( lai 4 wheiem the catalyst used is selected from zinc acetate dibutyl tin oxide stannous oxalate paia-toluene sulphonic acid and phosphonc acid 6 A piocess accoiding to Claim 4 oi 5 wheiem leaction foi making succinate estei of foimuia (I) is earned out at a tempeiatuie below 120°C 7 A piocess accoiding to any one of the pieceding Claims wherein the ester pioduct fiom this step (a) is then fuithei leacted in a step (b) with a flirther amount of the leactant alcohol in the piesence oi an alkaline earth metal alkoxide catalyst at a tempei tuie below 120"C and at a piessuie in the iange from atmospheric to 50 Kpa to enhance the amount of the desned 2-suc ιnate estei in the pioduct fiom step (a) at the expense of the maleates and iumaiates in said product 8 A piocess accoiding to Claim 7 wheiem the alkaline earth metal alkoxide is magnesium alkoxide 9 A piocess accoiding to any one of the pieceding Claims wherein reaction of 2-ethyl hexenol with maleic acid oi anhydride followed by leaction of the pioduct with magnesium alkoxide oi 2-ethylhexenol as catalyst gives rise to a pioduct which piimaiily compiises 2-(2-ethyl hexenoxy) -dι[2-(2-ethyl hexenyl)] succinate 10 2-(2-ethyl hexenoxy) -dι[2-(2-ethyl hexenyl)] succinate l l A piocess accoiding to any one of the pieceding Claims 1-8 wherein leaction of octadienoxy ethanol with maleic acid oi anhydride followed by the icaction oi the pioduct with the magnesium alkoxide of octadienoxy ethanol as catalyst gives rise to a product comprising di-2-(octadienoxy) ethyl)-2-(2- octadienoxy) ethoxy) succinate 12 Di-[(2-octadienoxy) ethyl]-2-[(2-octadienoxy) ethoxy] succinate. 13 A paint or coating formulation based on alkyd resins and comprising ether esters of formula (I) as reactive diluents in paint or coating formulations. 14 A paint or coating formulation based on alkyd resins according to Claim 13 wherein said formulation also contains one or more of butylated hydroxy-toluene (2,6-butoxy-4-methyl phenol) and 2,4 6-/t * /7-butyl phenol to inhibit haze and/or peroxidation 15 Emulsion paints comprising vinyl acetate and a comonomer selected from one or more the ether esters prepared by a process according to any one of the preceding Claims 1 -9 and 1 1

Inventors: GRACEY BENJAMIN PATRICK, HALLETT CHRISTOPHER, GRACEY, BENJAMIN, PATRICK, HALLETT, CHRISTOPHER
Applicants: BP CHEM INT LTD, GRACEY BENJAMIN PATRICK, HALLETT CHRISTOPHER, BP CHEMICALS LIMITED, GRACEY, BENJAMIN, PATRICK, HALLETT, CHRISTOPHER
Application year: 1997
Main classification: C07C69
IPC codes: C07C67, C07C69, C08F22, C09D7, C09D131