CA1161594A - Polyurethane binders - Google Patents

Abstract

ABSTRACT OF THE DISCLOSURE

The invention disclosed a polyurethane-based binder and a process for making same. The binder is useful in ?-castable solid propellants for rocket motors. The binder is formed by reacting a co-polyester with a diiso-cyanate.

Description

1 î ~159~L

This application is a division of applicant's co-pending Canadian application Serial No. 339,449, filed November 8, 19790 This invention relates to a new class of polyesters and to novel polyurethane-type elastomer binders useful in solid propellants, formed by reacting the novel polyesters with a diisocyanate.
Recently, a polyurethane-type elastomer binder has been developed for use in solid propellants. The binder is synthesized by reaction of a liquid polyester with a diisocyanate.
According to structure and molecular weight, the known polyesters presently employed are viscous liquids, solid resins or wax-like products.
Some of these known polyesters are hydroxy-termina~ed, having a molecular weight of about 2000, and are obtained through the polymerization of a mixture of ~-caprolactone and ~-methyl-~-caprolactone in the presence of ethylene glycol or oE glycerol. These polyesters have been used in the manufacture of polyurethane foam rubber.
Hydroxy-terminated polyesters are of specific interest in binders for solid propellants since they are compatible with cyclotetramethylene-tetranitramine (~X), nitrocellulose and nitro plasticizers commonly used in solid propellants. They also exhibit good hydrolytic stability, do not require anti-oxidants and give good adhesive properties to a solid loadO
Moreover, due to the polymerization method, these polyesters have very low acidity and a very low moisture content. These properties make it possible to obtain aluminized propellant compositions containing 80% solids, exhibiting a specific impulse of 272 seconds. However, these hydroxy-terminated poly-esters are generally solids melting at approximately 55-60C or liquids too viscous to accept solid loading of more than 8~/~o In an attempt to overcome these disadvantages, synthesis of copoly-mers of lactones e.g. ~-caprolactone with other monomers has been carried out, in an attempt to obtain hydroxy-terminated polyesters having lower viscosity at ambient temperature and a glass transition temperature lower than the homopolymer. It is believed that the use of a comonomer of a different structure to that of the ~-caprolactone, by introducing substitu--tion groups in the co-polymer, creates a certain amount of disorder in the polymeric chain and prevents solidification of the co-polyes-ter, most likely ~ , 1 - q~

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by lowering the Van der Waals force of the hydrogen bonds.
At present, this type of hydroxy-terminated polyester, specifically polylactone polyols, are used in the synthesis of polyurethane elastomers.
For example, the NIA ~ polyols PCP0240 and PCP0300 are used as diols and triols, respectively, in elastomeric binding agents for solid propellants.
However, PCP0240 has a wax-like consistency at ambient temperature, melts at temperature above 50C and has a viscosity of 0.65 N~s/m at 55 C.
PCP0300 is liquid at ambient temperature and has a viscosity of .
22.5 N.s/m2 at 20C. The high viscosity of these products does not allow for the mixing of aluminized propellant compositions which contain more than 80% solids. Moreover, the glass transition temperature (Tg) of polyurethane elastomers obtained from these products is approximately -70 C, i.e. lower than that of polyoxypropylene (-40 C) and almost as low as polybutadienes ( 78C) According to one aspect of the invention, novel Cr-caprolactone co-polyesters of structural formula I are contemplated, H(OR30OcR4co)X OCH2CH2O ~CO(CH2)5 ) y wherein R3 is the residual structure of a diol of structural formula II or a dehydrated derivative thereof HO-R-OH II

wherein R is an alkyl group containing 1 to 8 carbon atoms or an alkyl group containing 1 - 12 carbon atoms having a nitrogen atom in its backbone; wherein R4 is the residual structure of a diacid of structural formula III or a dehydrated derivative thereof

2~m III
wherein m is an integer from 1 to 36;
wherein x is an integer from about 1 to 10; and wherein y is an integer from about 1 to 10.
According to another aspect of the invention, a process for the preparation of co-polyester diols of structural formula I is also contemplated H(OR3OO~R4CO)x OCH2CH2O ~CO(CH2)5 ~ y t 3 6159~

which comprises (a) reacting ~-caprolactone or an C~-caprolactone polymer with the reaction product of (i) a diol of structural formula II or a dehydrated derivative thereof HO-R-OH II
wherein R is an alkyl group containing 1 to 8 carbon atoms or an alkyl group containing 1 - 12 carbon atoms having a nitrogen atom in its backbone; and`
(ii) a di-carboxylic acid of structural formula III or a dehydrated derivative thereof HOOC(C112)m COOH III
wherein m is an integer from 1 to 36; wherein R3 is the residual structure of a diol of structural formula II or a dehydrated derivative thereof, R4 is the residual structure of a diacid of structural formula III or a dehydrated derivative thereof and x and y are integers of about 1 - 10 and wherein (i) is an epoxide and (ii) is an anhydride, the reaction is effected in the presence of a primary diol as co-catalyst, or (b) reacting C-caprolactone with another lactone, in the presence of a primary diol as co-catalyst, wherein R3 and R4 are derived from the residual structure of said another lactone and x and y are integers of about 1 - 10.
The primary diol e.g. ethylene glycol, is not a true "catalyst"
since a reaction does occur between the diol and the monomer and is therefore referred to as a "co-catalyst".
According to yet another aspect of the invention, novel polyurethane binders useful in the production of solid propellants are contemplated, said binders being formed by reacting one of the aforementioned novel polyesters with a diisocynate e.g. isophorone diisocynate (IPDI).
According to yet another aspect of the invention solid propellants of high solids loading are contemplated comprising 12% w/w of a novel poly-urethane binder as mentioned above and 88% w/w solids including ammonium perchlorate and aluminum.
In the drawing which illustrates embodiments of the invention, Figure 1 is a graph illustrating the determination of molecular weight, by GPC, of various novel polyesters according to the invention, and ~ 1 ~1594 Figure 2 is a graph illustrating the viscosity at various tempera-tures of novel po]yesters according to the invention~
Figure 1 demonstrates the homogenity of the different compounds synthesized and enables determination of the molecular ueight by GPC of the different polyester diols. The abscissa is the time elapsed (count) to elude the molecule of a definite siæe, while the ordinate represents a measure of the absorbance of eludate by infra-red or with refractive index determinations.
The graphical results are shown in the tables under weight average (Mw) and number average (M ) molecular weights.

The viscosity of different synthetic polymers at several tempera-tures is shown in Figure 2 and was compared to either Niax Polyol PCP-0300 or Hydroxy terminated Polybutadiene R45-HT. The abcissa on the graph gives the temperature in Celsius (C) while the ordinate, the viscosity in Newton x second/meter square (N.s/m2) that i8 identical to Pascal x second (Pa.s) and ten times greater than poise.
The following examples further illustrate embodiments of the invention.
The use of N-methyl-diethanolamine or of polyesteramine (N-8) (formed from sebacic acid and N-methyl diethanolamine) as initiator of c~-caprolactone polymerization, has resulted in hydroxyl-terminated polyester-amines, that are solid at 50C.
EXAMPLE I
Preparation of copolyester diols from (N-8) polyesteramine diol and -capro-lactone.
A mixture of ~-caprolactone (20 moles) with l.0 mole of (N-8) polyesteramine diol (produced by the reac-tion of sebacic acid with (i) N-methyl-diethanolamine or with (ii) N-methyl-diethanolamine in the presence of a catalyst (lead-2-ethylhexanoate, or tetraoctyleneglycol titanate, 1%) is heated under a nitrogen a-tmosphere. Solid products at ambient temperature are obtained. The copolyester diols had a functionality varying from 1.6 to 1.8, a Tg of approximately - 70 and a viscosity of 2.3 N.s/m at 50 C (see table I).

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Preparation of a copolyester diol or triol from ~ dimer 1014 or Empo trimer 1040 and c-caprolactone The copolymerization of ~-caprolactone and a butylene oxide deriva-tive of Emery Empol dimer 1014 or Emery Empol trimer 1040 gives liquid copolyester diols or triols. Empol is a trademark for aliphatic dimer acids of 36 carbon atoms and trimer acids of 5~1 carbon atoms.

Diol Preparation:
10 moles of C~-caprolactone are made to react with one mole oE butyl-eneoxide derivative of Empol dimer acid 1014 (Emery Industries Inc.). The reaction is completed after 24 hours at 180C in nitrogen atmosphere, in the presence of 0.60% lead 2-ethylhexanoate as catalyst. The product obtained has an hydroxyl equivalent of 1018 and a average molecular weight (Mvpo) of 1950. It has a wax-like appearance at ambient temperature and a viscosity of 0.66 N.s/m at 50 C. The glass transition temperature (Tg) is -70 C.
Triol Preparation:
The butylene oxide derivative of the Empol trimer 1040 is substitu-ted for the derivative of Empol dimer 1014 in a mixture described in the preceding paragraph and a triol having an hydroxyl equivalent of 783 and a Mvpo of 2190 is obtained. The viscosity of this product at 20 C is 10.1 N.s/m2 and the Tg -68 C (See table II).
The butylene oxide derivative of the dimer or trimer acid may be represented as a long chain diol or a triol of general formula:
., . . . ~ .

(HO-CH-CH2-CO ~ R2-COO-CH2-CH - OH

where n = 1 for a diol and n = 2 for a triol and R2 = backbone of 36 carbon atoms of the dimer acid, from Emery Empol 1014 and R2 = backbone of 54 carbon atoms of the trimer acid, from Emery Empol 1040.

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Preparation of a copolyester diol from two lactones The copolymerization of two lactones of different structures was studied first. The copolyester synthesis from ~-caprolactone with ~-butyro-lactone (IOCH2CH2CH2CO) or ~-valerolactone (~-CH(CH3)CH2CH2 lO) in presence of a cationic catalyst, tetraoctyleneglycol titanate, and a co-catalyst, ethylene glycol, under a pressure of 0.7 MPa, indicates that a small proportion of these lactones is introduced in the copolymer. On the other hand, a lactone formed by a six-membered ring, e.g. ~-valerolactone, copolymerizes with the ~-caprolactone under the same conditions. This product is as crystalline as the caprolactone homopolymer and melts at a temperature of above 50C.

Preparation of copolyester diols from two lactones.
A monocyclic ether formed by a seven-membered ring, e.g.~-caprolac-tone, is copolymerized at 180C under a nitrogen atmosphere, in presence of 0.1V/o tetraoctyleneglycol titanate catalyst, with a six-membered ring lactone, a-valerolactone, and two pentagonal lactones respectively, ~-butyrolactone and ~-valerolactone.
While the ~-valerolactone easily copolymerizes with ~-caprolactone creating a solid product, the pentagonal lactones are difficult to polymerize alone, but in presence of the ~-caprolactone these two lactones are sufficiently integrated into the copolyester to lower the viscosity at 50C. (~ee Table III).

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-caprolactolle The react;on of a cyclic ether with a cyclic anhydride ~Eorms a po]y-ester. A new family of co-polyesters obtained from a mixture of ~-caprolac-tone, a cyclic ether and a cyc1ic anhydride in the presence of a co-catalyst such as ethylene glycol, and an initiator, such as tetraoctyleneglycol titanate, results in the co-polyester diol of the f~llowing probable structure, as for example the polycaprolactone-co-3-phenoxypropylene-1,2-cyclohexene dicarboxylate diol:

H (OCI-12CII-OOG Q CO)- OCH2CH~O- ~CO(CH2)5O ) yH

These copolyesters have a structure which tends to prevent crystalli~at;on and are liquid at ambient temperature. While ~ -caprolactone polymeri~es into a block and while its polymeri~ation rate is independent of the concentrat-ion of this monomer, the polymeri~ation rate of the second monomer is governed by the rate of condensation of the anhydride with the epoxide~

Preparation of a terpolyester diol from an anhydride, a cyclic ether and -caprolactone.
A mixture of an epoxide such as phenylglycidyl ether (PGE), 1,2-epoxy-cyclohexene (EC~) or allylglycidyl ether (AGE) (1.0 mole), a dicarboxylic acid anhydride such as cis-1,2-cyclohexanedicarboxylic anhydride ~CHDA), methylsuccinic anhydride (MSA), 3-methylglutaric anhydride (MCA), pyrotartaric anhydride (PTA), and phthalic anhydride (PA) (1.0 mole) and ~ -caprolactone (1.0 mole), is heated to 140-180 C in nitrogen atmosphere in the presence of a catalyst tetraoctylene glycol titanate (TOGT), tin dibutyldilaurate (DGSnDL) or lead 2-ethyl hexanoa-te (EHPb), 1.0% in weight of the monomers;

and oE a co-catalyst (ethylene glycol, 0.12 mole). The percentage of reactive anhydride is determined by calculating the acid number. An equimolecular mixture of epoxide and anhydride results in a co-polyester with carboxyl terminated groups, while an excess of epoxide results in a diol (See Table V).

_ 10 --The rate of reaction determined by the reduction of the acid mlmber is shown in Table VI. The rate of disappearance of ~ -caprolactone is measured by gas chromatographyO
The polymer obtained by the reaction of PGE, CHDA and ~- caprolac--tone, polycaprolactone-co-3-phenoxypropylene-1,2-cyclohexylene-dicarboxylate is a homogeneous product, while polymer obtained from AGE, MSA and ~ rcapr lactone, polycaprolactone-co-3-allyloxy-1,2-proplyene methylsuccinate is a mixture of two products.
The product obtained from ECH, MSA and ~-caprolactone i.e. poly-caprolactone-co-1,2-cyclohexylene methylsuccinate is also a homogeneous product and the molecular weights are calculated by GPC (See Table VII).

.
Preparation of a block co-po]yester diol, from a diacid, a diol, and a polymer of ~-caprolactone, namely, polycaprolactone (PCP.
A mixture of a diol (1,2-propanediol, 1.0 mole), a dicarboxylic acid (adipic, sebacic, 1.0 mole) and polycaprolactone (PCP 0530, 1.0 mole) is heated at 200-225 C under a nitrogen atmosphere in the presence of a catalyst (TOGT, lppm) until all the acid is completely eliminated. The residual monomers are evaporated by heating under reduced pressure~ The residual acid contents, hydroxyl group concentration, molecular weight are then determined by vapour phase osmometer and chromatography on a permeable gel as well as the viscosity. The results are shown in Table VIII.

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TABLE VI

Rate of reactlon of pol~ester diols Ratio in ether/anhydride/-caprolactone: 1,5/1,0/1,0 ___ _ Test No. Reagent Time3 Temp. Anhydride 36 PGE~Ms~cL/EHpb 7,2 1802l28l~96 14,4 8,2 18,0 6,4 21,6 2,2 25,2 1,2 32,L~ 0,2 37 PGE~hSA / CL/DBSnDL 271'26 180 73L2~99 32,l~ 18,9 34,2 15,7 L~ 3 2 ll8 8 64,8 5-~
76 4 21~8 .
38 PGE/i~A,/ CL/TOGT 271~26 180 256 62 32,4 7,5 34,2 5,5 43,2 1.3 57~,0 0,4 AGE/ M~S~/CL/TOGT O,9 140 9889 37 2,7 83 ~4 5,4 72,3 8,1 62,6 13,5 46,7 21,6 33,9 28,8 27,~
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~ 1 B1594 Preparation oE a sequenced co-polyester diol from a diacid, a diol and ~:caprolactone.
A mixture of a diol selected from 1,2-propanediol (PG), 1,3-butane-diol (13BD) and 3-methyl-1,5-pentanediol (3M15P) (1.1 mole), a dicarboxylic acid (adipic (AA) or sebacic (S~) 1.0 mole) and ~-caprolactone (1.0 mole) is heated to 200-250C in nitrogen atmosphere in presence of a catalyst (TOGT, boron trifluoride). Volatile products are evaporated through vacuum heating at 225C. The extent of the reaction is measured by the determination of the acid group and the quantity of non-polymerized ~-caprolactone. The hydroxyl concentration, the molecular mass are determined by a vapour phase osmometry and chromatography on a permeable gel, as well as the viscosity (see Table VIII).
Preparation of polyurethane binder from Empol co-polyester diol 1014BO/ ~-CL?
Em ol co- o]yester triol_1040BO/ ~-CL and a diisocyanate P . . _ _ We prepared elastomers from a mixture of Empo ~ co-polyester diol 1014BO/ ~-CL and Empol~ co-polyester triol 1040BO/ ~-CL. For comparison purposes, an elastomer was made from R45M (trade mark for a hydroxy-terminated polybutadiene sold by ~r~o Chemical Corp.). These products were transformed into elastomeric polyurethane by reaction with a diisocyanate. The mixtures were poured into teflo ~ moulds and placed into a 60C oven to constant shore A hardness. The mechanical properties of the binders (d , d , ~ , ~ , and E) were measured at ambient temperature (23C) using a Instron machine (Instron Canada Ltd., model TTC 1114) on rings manuEactured with a punch. These rings had an interior diameter of 3.17 cm. Samples are drawn at a speed of 0.212 cm/s. The effective gauge length of the test tube was 3.50 cm. Mechanical properties are shown in Table IX. The polyester elastomers have an energy comparable to polybutadienes. Exemplified diisocyanate are DDI diisocyanate, a trade mark for an intermediate made from a 36-carbon dimer aliphatic dibasic acid;

acid; isophorone diisocyanate (IPDI); and Isonate 901, a trade name for a polyfunctional isocyanate from Upjohn Polymer Chemicals of Kalamazoo, Michigan.

Il t~l594 In Figure l, the compounds analysed by GPC in curves 1 and 2 were obtained by the process reported in Example 6. It is also shown in Figure l that compounds 3 and 4 had much lower molecular weight ~higher GPC counts) than copolyester diols (curves 1 and 2). It is also shown that the copoly-ester diols (curves 1 and 2) are truly copolymer and not a mixture of polymer according to the form of the curves (only one peak). The curves of the additional compounds studied (Emery Empol dimer acid 1014, and hydroxyl terminated Empol 1014/BO) were given for comparison.

Preparation of polyurethane binders from a terpolymer diol, from polycaprolactone triol and from diisocyanate A mixture of terpolymer diol (AGE/PA/~CL) and of Niax Polyol triol PCP0300 is mixed with a diisocyanate according to the method described in the preceding paragraph. A mixture of Niax Polyol PCP0240 and PCP0300 was heated with the same isocyanate for comparison purposes. The elastomers obtained have properties similar to those from polybutadienes (Table IX).

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U~ O U~ ~o 1~ co ~ ~ ~o E-i Z ~ ~t ~ `;t ~ `;t ~0 CO ~1 ;1 1 1 6~594 Preparation of ~r_pellant from polyesters The propellant samples were prepared from ammonium perchlorate (mixture of 400, 200 and 17 /um, proportionately weighing 1.7, 2.7 and 1.0 respectively), of aluminum il-15 and of various ingreclients usecl in binders according to a conventional method. The various ingredients were mixed in a vertical-propeller mixer of 500 g (Atlantic Research Corp., Alexandria, (Virginia). To the mixture of polyester diol and plasticizer, we added the aluminu, the ammonium perchlorate and finally the diisocyanate (table IX) cluring a three-hour period, mixing constantly at a temperature of 60 C, in a vacuum. The load was poured into a Teflo ~ mould, which was then agitated in a vacuum, by a vibrator. It was heated at a constant temperature in an oven, until the hardness of the sample was constant. The propellant test-pieces were then tooled according to JANAF dimensions, and the mechanical properties in traction were determined following the usual method (3). JANAF
test-pieces, tooled from propellant blocks were used to determine the mechan-ical properties at 23 C and at -45 C. The mobile apron was moved at a speed of 0.0847 cm/s and at a deformation rate of 0.0123 s . The effective gauge length of the test-pieces was 8.43 cm. The maximum load and elongation obtained with the test-piece was determined from the tension-deformation curve which was used to calculate strain (a ) to maximal elongation (~'~ ). The initial modulus was calculated from the slope at the beginning of this same curve. Results of mechanical properties of the novel propellants are given in Table X.
Owing to their low viscosity and good compatibility with the plastici-zer isodecyl pelargonate, two copolyester binders, polycaprolac-tone-co-propy-lene sebacate and polycaprolactone-co-3-methyl pentamethylene sebacate (batch 69, 93, 102, 104 and 105, Table X) yielded propellants containing up to 88%/N
of solids. The mechanical properties of these propellants were superior to those obtained from polycaprolactone diols.

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The general s~ructural formula I was deducted from the apparent starting materials as set forth in the examples, giving alternate or block copolymers accordlng to the following Table XI.
TABLE XI

Epoxides or diols or lactones R3 1,2-epoxy cyclohexene (ECH) yield 1,2-cyclohexene 4-vinyl-1, 2-epoxy cyclohexene " 4-vinyl-1, 2-cyclohexene Allyl-glycidyl ether (AGE) " 3-propenyloxy-1, 2-propylene Phen'~l glycidyl ether (PGE) " 3-phenoxy-1, 2-propylene Polyesteramine diol " CH2-CH2-N(CH )CH CH
N-methyldiethanolamine " N-Methyldietheneamine '~-butyrolactone ~ 1, 3-propylene ~-valerolactone " 1, 3-butylene Propylene oxide " 1, 2-propylene Butylene oxide " 1, 2-butylene Propylene glycol " 1, 2-propylene 1,3-Butanediol " 1, 3-butylene 3-Methyl-1, 5-pentanediol " 3-methyl-1, 5-pentamethylene Niax polyol PCP 0530 " Polycaprolactone .. . . . . . _ _ Lactones, acids, anhydride R4 .. . ..
~-valerolactone yield tetramethylene ~-butyrolactone " 1, 3-propylene ~-valerolactone ~' 1, 3-butylene cis-1,3-cyclohexane dicarboxylic anhydride (CHDA) ~ 1, 2-cyclohexene Methyl succinic anhydride (MSA) " 1, 2-propylene Methyl succinic acid " 1, 2-propylene 3-methyl glutaric anhydride (MGA) or acid " 2-methyl-1,3-propylene Phthallic anhydride (PA) or acid " Phenylene Adipic acid (AA) tetramethylene Sebacic acid (SA) octamethylene (CH ) ~mpol 1014 C36 radical 2 8 . _ . _ . _ _ . . . _ _ . . _ From the gel permeation chromatography and nuclear magnetic resonance studies we can demonstrate the formation of only one copolyester of the written struc-ture. The "x" lmits were formed from a diol and a diacid (or the dehydrated derivatives) and the "y" units obtained from the ~-caprolactone monomer.

.. . . .. . .. . _ . ..

Claims

THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:

1 . A process for the preparation of a polyurethane binder, which comprises reacting a co-polyester diol of structural formula I
H(OR3OOCR4CO)x OCH2CH2O wherein R3 is the residual structure of a diol of structural formula II, HO-R-OH II
wherein R is an alkyl group containing 1 to 8 carbon atoms or an alkyl group containing 1 - 12 carbon atoms having a nitrogen group in its backbone; or a dehydrated derivative thereof, R4 is the residual structure of a diacid of structural formula III

HOOC(CH ) COOH III
2 m wherein m is an integer from 1 to 36; or a dehydrated derivative thereof, and x and y are integers of about 1 to 10, with a diisocyanate.

2 . A process according to claim 1, wherein the diisocyanate is selected from the group consisting of DDI diisocyanate, a trade mark for an intermediate made from a 36-carbon dimer aliphatic dibasic acid; isophorone diisocyanate (IPDI) and Isonate 901, a trade name for a polyfunctional isocyanate.

3 . A process according to claim 1, wherein the reaction product of .SIGMA.-caprolactone, sebacic acid and propylene glycol is reacted with Isonate 901, a polyfunctional isocyanate.

4 . A process according to claim 1, wherein the reaction product of .SIGMA.-caprolactone, sebacic acid and 1,3 butane diol is reacted with Isonate 901, a polyfunctional isocyanate.

5 . A process according to claim 1 , wherein the reaction product of .SIGMA.-caprolactone, cis-1,3-cyclohexane dicarboxylic anhydride and butylene oxide is reacted with Isonate 901, a polyfunctional isocyanate.

6 . A polyurethane binder for use in a solid propellant comprising the reaction product of a co-polyester diol of formula I as defined in claim 1 and a diisocyanate.

7 . A polyurethane binder according to claim 6, wherein the diisocyanate is selected from the group consisting of DDI diisocyanate, a trade mark for an intermediate made from a 36-carbon dimer aliphatic dibasic acid; isophorone diisocyanate (IPDI) and Isonate 901, a trade name for a polyfunctional iso-cyanate.

8 . A polyurethane binder according to claim 7, including a plasticizer.

9 . A polyurethane binder according to claim 8, wherein the plasticizer is isodecyl pelargonate.

10 . A co-polyester-urethane propellant comprising 70%/w of ammonium perchlorate, 18%/w of finely divided aluminum, and 12%/w of a binder as defined in claim 6 , 7 or 8.