Carbon black composition and polymer compositions comprising the same
Abstract
The invention relates to a carbon black composition and to polymeric compositions comprising the same, used as semiconductive compositions or masterbatch compositions. According to the invention, the carbon black composition comprises carbon black and 0.1...50% by weight of at least one binder containing polyhydric alcohol. The claimed polymer composition comprises a polymeric component, carbon black and at least one binder. The carbon black composition comprises ethoxylated esters, polyethers, ethoxylated alcohols or non-ethoxylated esters to be embedded into the fluffy carbon black composition in a pelletizing process to obtain free flowing, low dust, attrition resistant carbon black pellets which impart the polymer systems enhanced mechanical and rheological properties.
Term
Term ended
Expired 11 January 2016, 10.7 years ago.
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29 claims: 5 independent, 24 dependent
- 1Revendicări 1. Compoziție de negru de fum, caracterizată prin aceea că conține negru de fum și 0,1...50 % în greutate din cel puțin un liant ales din cel puțin una din următoarele grupe:i) un alcool polihidroxilic etoxilat având cel puțin 3 grupe hidroxil per moleculă înainte de etoxilare, în care numărul total de molecule de etilenoxid per alcool polihidroxilic este de cel puțin 3;ii) un ester al unui acid alchil carboxilic cu un alcool polihidroxilic etoxilat având cel puțin 3 grupe hidroxil per moleculă înainte de etoxilare, în care acidul alchil carboxilic are 8...30 atomi de carbon și poate fi saturat sau nesaturat și în care funcționalitatea monoester este de cel puțin 80 % restul fiind o funcționalitate diester și în care numărul de molecule de etilenoxid per ester al alcoolului polihidroxilic este de cel puțin 3;iii) un ester al unui acid alchil carboxilic cu un alcool polihidroxilic având cel puțin 3 grupe hidroxil per moleculă înainte de esterificare, în care acidul alchil carboxilic are 8...30 atomi de carbon, și poate fi saturat sau nesaturat și în care funcționalitatea monoester este de cel puțin 80 %, restul fiind funcționalitate diester;iv) un ester al unui acid alchil carboxilic etoxilat cu un alcool polihidroxilic având cel puțin 3 grupe hidroxil per moleculă înainte de esterificare, în care acidul alchil carboxilic are 8...30 atomi de carbon, și poate fi saturat sau nesaturat și în care funcționalitatea monoester este de cel puțin 80 %, restul fiind o funcționalitate diester, iar numărul de molecule de etilenoxid per ester al alcoolului polihidroxilic este de cel puțin 3 și v) un bloc copolimer polietilenoxid-polipropilenoxid.
- 2Compoziție conform revendicării 1, caracterizată prin aceea că alcoolul polihidroxilic este, de preferință, ales din grupa formată din trietanolamină, glicerină, pentaeritritol, sorbitol, sorbitan, sucroză și o poligliceridă. RO 121129 Β1
- 3Compoziție conform revendicării 1, caracterizat prin aceea că liantul are o valoare 1 HLB de 8...30.
- 4Compoziție conform revendicării 1, caracterizată prin aceea că liantul este ales 3 din grupa i).
- 5Compoziție conform revendicării 1, caracterizată prin aceea că liantul este ales 5 din grupa ii).
- 6Compoziție conform revendicării 1, caracterizată prin aceea că liantul este ales 7 din grupa iii).
- 7Compoziție conform revendicării 1, caracterizată prin aceea că liantul este ales 9 din grupa iv).
- 8Compoziție conform revendicării 1, caracterizată prin aceea că liantul este ales 11 din grupa v).
- 9Compoziție conform revendicării 1, caracterizată prin aceea că liantul este pre- 13 zent într-o cantitate de 1,0...20 % în greutate.
- 10Compoziție conform revendicării 1, caracterizată prin aceea că numărul total de 15 molecule de oxid de etilenă per alcool polihidroxilic din liant variază de la 3 la 500.
- 11Compoziție conform revendicării 1, caracterizată prin aceea că numărul total de 17 molecule de oxid de etilenă per alcool polihidroxilic din liant variază de la 5 la 100.
- 12Compoziție conform revendicării 1, caracterizată prin aceea că, negru de fum 19 este tratat cu liant.
- 13Compoziție de polimer, caracterizată prin aceea că conține un component poli- 21 meric, 0,1...65 % în greutate dintr-o compoziție de negru de fum definită în revendicarea 1 și 0,1 ...50 % în greutate din cel puțin un liant ales din cel puțin una din următoarele grupe:23 i) un alcool polihidroxilic etoxilat având cel puțin 3 grupe hidroxil per moleculă înainte de etoxilare, în care numărul total de molecule de etilenoxid per alcool polihidroxilic este de 25 cel puțin 3;ii) un ester al unui acid alchil carboxilic cu un alcool polihidroxilic etoxilat având cel 27 puțin 3 grupe hidroxil per moleculă înainte de etoxilare, în care acidul alchil carboxilic are 8...30 atomi de carbon, și poate fi saturat sau nesaturat, și în care funcționalitatea monoester 29 este de cel puțin 80 %, restul fiind o funcționalitate diester și în care numărul de molecule de etilenoxid per ester al alcoolului polihidroxilic este de cel puțin 3;31 iii) un ester al unui acid alchil carboxilic cu un alcool polihidroxilic având cel puțin 3 grupe hidroxil per moleculă înainte de esterificare, în care acidul alchil carboxilic are 8...30 33 atomi de carbon, și poate fi saturat sau nesaturat, iar funcționalitatea monoester este de cel puțin 80 %, restul fiind o funcționalitate diester;35 iv) un ester al unui acid alchil carboxilic etoxilat cu un alcool polihidroxilic având cel puțin 3 grupe hidroxil per moleculă înainte de esterificare, în care acidul alchil carboxilic are 37 8...30 atomi de carbon, și poate fi saturat sau nesaturat, iar funcționalitatea monoester este de cel puțin 80 %, restul fiind o funcționalitate diester, și în care numărul de molecule de eti- 39 lenoxid per ester al alcoolului polihidroxilic este de cel puțin 3 și v) un bloccopolimer polietilen oxid-polipropilen oxid-polietilen oxid. 41
- 14Compoziție conform revendicării 13, caracterizată prin aceea că alcoolul polihidroxilic este, de preferință, ales din grupa formată din trietanolamină, glicerina, 43 pentaeritritol, sorbitol, sorbitan, sucroză și o poligliceridă.
- 15Compoziție conform revendicării 13, caracterizată prin aceea că liantul are o 45 valoare HLB de 8,0...30. RO 121129 Β1
- 16Compoziție conform revendicării 13, caracterizată prin aceea că liantul este ales din grupa i).
- 17Compoziție conform revendicării 13, caracterizată prin aceea că liantul este ales din grupa ii).
- 18Compoziție conform revendicării 13, caracterizată prin aceea că liantul este ales din grupa iii).
- 19Compoziție conform revendicării 13, caracterizată prin aceea că liantul este ales din grupa iv).
- 20Compoziție conform revendicării 13, caracterizată prin aceea că liantul este ales din grupa v).
- 21Compoziție conform revendicării 13, caracterizată prin aceea că, compoziția de negru de fum și liant este prezentă într-o cantitate de 1,0...20 % în greutate.
- 22Compoziție conform revendicării 13, caracterizată prin aceea că numărul total de molecule de oxid de etilenă per alcool polihidroxilic al liantului variază de la 3 la 500.
- 23Compoziție conform revendicării 13, caracterizată prin aceea că numărul total de molecule de oxid de etilenă per alcool polihidroxilic al liantului variază de la 5 la 100.
- 24Compoziție conform revendicării 13, caracterizată prin aceea că negru de fum se tratează cu liant.
- 25Compoziție semiconductoare, caracterizată prin aceea că, conține 25...55 % în greutate o compoziție care conține negru de fum și 0,5...10 părți per 100 părți negru de fum din cel puțin un liant ales din cel puțin una din următoarele grupe:i) un alcool polihidroxilic etoxilat având cel puțin 3 grupe hidroxil per moleculă înainte de etoxilare, în care numărul total de molecule de etilenoxid per alcool polihidroxilic este de cel puțin 3;ii) un ester al unui acid alchil carboxilic cu un alcool polihidroxilic etoxilat având cel puțin 3 grupe hidroxil per moleculă înainte de etoxilare, în care acidul alchil carboxilic are 8...30 atomi de carbon, și poate fi saturat sau nesaturat și în care funcționalitatea monoester este de cel puțin 80 %, restul fiind o funcționalitate diester, în care numărul de molecule de etilenoxid per ester al alcoolului polihidroxilic este de cel puțin 3;iii) un ester al unui acid alchil carboxilic cu un alcool polihidroxilic având cel puțin 3 grupe hidroxil per moleculă înainte de esterificare, în care acidul alchil carboxilic are 8...30 atomi de carbon, și poate fi saturat sau nesaturat, și în care funcționalitatea monoester este de cel puțin 80 %, restul fiind o funcționalitate diester;iv) un ester al unui acid alchil carboxilic etoxilat cu un alcool polihidroxilic având cel puțin 3 grupe hidroxil per moleculă înainte de esterificare, în care acidul alchil carboxilic are 8...30 atomi de carbon, și poate fi saturat sau nesaturat, și în care funcționalitatea monoester este de cel puțin 80 %, restul fiind o funcționaliate diester, și în care numărul de molecule de etilenoxid per ester al alcoolului polihidroxilic este de cel puțin 3 și v) un bloccopolimerpolietilenoxid-polipropilen oxid-polietilenoxid, până la 2 % în greutate stabilizator sau antioxidant, până la 5 % în greutate peroxid organic, de preferință peroxid de dicumil, până la 10 % în greutate vinii silan, restul fiind un polimer sau un amestec de polimeri aleși dintre homopolimer al etilenei, etilenă copolimerizată cu una sau mai multe alfa olefine, cum ar fi propilena, butena sau hexena, etilenă copolimerizată cu propilenă și un monomer dienic, de preferință norbornenă, un copolimer al etilenei cu unul sau mai mulți monomeri aleși dintre acetat de vinii, acid acrilic, acid metacrilic, esteri ai acidului acrilic sau metacrilic conținând 1 ...8 atomi de carbon, anhidridă maleică sau monoester derivat de la acidul fumărie sau maleic, clorură de vinii sau clorură de viniliden. RO 121129 Β1
- 26Compoziție conform revendicării 25, caracterizată prin aceea că negru de fum 1 este tratat cu liant.
- 27Compoziție de preamestec, caracterizată prin aceea că, conține 70...40 % în 3 greutate homopolimer sau copolimer al etilenei în care comonomerul este ales dintre hexenă, propenă, butenă, octenă sau acetat de vinii și 30...60 % în greutate dintr-o compo- 5 ziție care conține negru de fum și 0,1...50 % în greutate din cel puțin un liant ales din cel puțin una din următoarele grupe:7 i) un alcool polihidroxilic etoxilat având cel puțin 3 grupe hidroxil per moleculă înainte de etoxilare, în care numărul total de molecule de etilenoxid per alcool polihidroxilic este de 9 cel puțin 3;ii) un ester al unui acid alchil carboxilic cu un alcool polihidroxilic etoxilat având cel 11 puțin 3 grupe hidroxil per moleculă înainte de etoxilare, în care acidul alchil carboxilic are 8...30 atomi de carbon, și poate fi saturatsau nesaturat, și în care funcționalitatea monoester13 este de cel puțin 80 %, restul fiind o funcționalitate diester, și în care numărul de molecule de etilenoxid per ester al alcoolului polihidroxilic este de cel puțin 3;15 iii) un ester al unui acid alchil carboxilic cu un alcool polihidroxilic având cel puțin 3 grupe hidroxil per moleculă înainte de esterificare, în care acidul alchil carboxilic are 8...3017 atomi de carbon, și poate fi saturat sau nesaturat, și în care funcționalitatea monoester este de cel puțin 80 %, restul fiind o funcționalitate diester;19 iv) un ester al unui acid alchil carboxilic etoxilat cu un alcool polihidroxilic având cel puțin 3 grupe hidroxil per moleculă înainte de esterificare, în care acidul alchil carboxilic are 21 8...30 atomi de carbon, și poate fi saturatsau nesaturat, și în care funcționalitatea monoester este de cel puțin 80 %, restul fiind o funcționalitate diester, și în care numărul de molecule 23 de etilenoxid per ester al alcoolului polihidroxilic este de cel puțin 3 și v) un bloccopolimer polietilenoxid-polipropilenoxid-polietilenoxid.25
- 28Compoziție conform revendicării 27, caracterizată prin aceea că negru de fum este tratat cu liant.27
- 29Compoziție pe bază de negru de fum, caracterizată prin aceea că conține negru de fum și 0,1 ...50 % în greutate distearat de sucroză.29
Independent claims29
385 paragraphs, as filed
The invention relates to a composition of carbon black and to polymer compositions containing it, the composition of carbon black being used to obtain smash-resistant, fluid and low dust smokeless black pellets, which are light dispersible in most polymer systems which gives them improved mechanical and rheological properties, necessary for making cables, semiconductor wires or other similar products.
There are several known processes for producing black smoke.
Thus, black of smoke obtained by the furnace process generally has bulk densities ranging from 0.02 to 0.1 g / cm<sup>3</sup> and it is generally known as fluffy black. Black fluffy smoke disperses easily into liquids and certain polymer systems. However, fluffy black is generally adherent and, for this reason, is difficult to handle in transport and dosing operations.
The fluffy black is agglomerated by different types of mechanical processes, either in the dry state or with the aid of a liquid to obtain pellets with improved handling characteristics. Liquid pelletizing agents are usually oil and water. The process of agglomerating fluffy carbon black to obtain carbon black pellets is known as pelletizing.
Unfortunately, the usual densification or agglomeration processes, known as pelletization, have harmful effects on the dispersion characteristics of the black carbon.
Therefore, it is known in the art that in the pelletization of carbon black there is a sensible balance between acceptable handling characteristics and ease of dispersion.
US 2065371 discloses a process for pelletizing the carbon black through a typical wet pelletizing process, in which the fluffy carbon black is combined with a liquid, preferably water, and stirred until spherical beads are formed. These balls are then dried to reduce the water content, preferably below 1% to form black carbon pellets.
The state-of-the-art patents also show the use of binders in the wet pelletizing process to improve the handling characteristics.
US 2850403 discloses the use of carbohydrates, for example sugar, molasses, soluble starches, sugars and lignin derivatives as pellet binders, in the range of 0.1% to 0.4%, by weight, as compared to carbon black. dry. The preferred drying temperature of wet pellets is 150 to 425 ° C, which, during the standstill, is sufficient to produce carbonization of the binder.
US Patent No. 2908586 discloses the use of a rosin emulsion as a binder for pellets as an alternative to carbohydrates. The preferred level of rosin binder is in the range of 0.5% to 1.0%, by weight, relative to dry black smoke.
US Patent 2639225 discloses the use of sulfonated anionic surfactants and sulfates as pellet binders at levels of 0.1% to 0.5% by weight, based on dry black smoke.
US 35565658 discloses the use of a nonionic ethoxylated fatty amine surface agent in the range of 2 to 50 moles ethylene oxide per fatty amine group. The preferred level of surface agent in the pelletizing water is in the range from 0.05% to 5%, by weight, relative to the black of dry smoke.
Similarly, U.S. Patent 36,45765 discloses the use of an ethoxylated resinic acid or nonionic surfactant, wherein the level of ethoxylation is 5 to 15 moles ethylene per acid group. The preferred level of addition to the carbon black is in the range of 0.1% to 10% by weight relative to the dry carbon black.
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USSR Patent 937492 claims the use of 0.1% ... 5%, by weight, based on 1 black of dry smoke, an aqueous solution of the reaction product between urea and an ethoxylated alkyloylamide. The preferred ethoxylation level is 1-7 moles of ethylene oxide per molecule of 3 alkylolamide.
US Patent No. 3844809 discloses the reduction of the dust level of the pellets by incorporating 5 of 0.4% ... 2.5% by weight, relative to the dry black carbon, from an aqueous solution containing 0.001% ... 0.1% by weight non-ionic surface agent with poly (ethylene oxide) and poly (di-7-methyl silicone) groups, which are repeated randomly. It is also included molasses, at a high concentration, up to 2% by weight, as co-binding and nitric acid, up to 15%, by weight, as 9 source of oxidation.
The use of carbohydrates, rosin or surface active agents, presented in the aforementioned patents, is directed towards improving the handling properties of the pellets. The mentioned patents do not show that the pelletizing treatments affect the performance of the black carbon in the final applications, which are generally in the rubber industry. 15
JP 1201369 discloses the use of a carboxylic acid alkyl amphoteric surface agent in a concentration range of 0.001% ... 0.1% by weight, in water of 17 pellets, to obtain carbon black pellets with low adhesion and excellent dispersibility. 19
U.S. Patent No. 30,14810 discloses the advantages of wet pelletizing a series of pigments, including carbon black, with a mixture of quaternary ammonium compound and ob / s (-2-hydroxy-21 ethyl) alkyl amine. Improvements in dispersion speed, viscosity stability and antistatic properties for mixtures of surface active agents are presented. 2. 3
The oil pelletization, in the presence and absence of water, is presented in US Pat. Nos. 2635057, 3011902 and 4102967 as beneficial for improving the handling properties of 25 black smoke pellets.
Several patents, including US Patents 25,111,140, 24,57962, 44,40807, 45,69834, 27
5168012 and JP 77130481 present polymers in emulsion, solutions in organic solvents and melts as a means of modifying the properties of black carbon pellets. 29
US patent 4277288 presents a fluidized granulation process for obtaining, in the absence of water, pigment granules without dust and free flowing. The organic component 31 required to obtain dust-free granules is composed of two components, 5 ... 20% non-aqueous granulation auxiliary and a nonionic surfactant, for example ethoxylated sorbitan oleate 33, as the second component. The description shows the obtaining of free-flowing organic and inorganic pigments, which contain carbon black. 35
US Patent 4397652 discloses a process for obtaining preparations of organic dyes and optical bleaches with a low dust content. The process involves dry mixing, at temperatures between 30 and 80 ° C, of the dye or optical bleach with 2 ... 10%, by weight, of an adhesive chosen from the group consisting of polyhydroxyl alcohol, such as sorbitol, mannitol , 39 mannitose, lactose, hydrated dextrose, neopentyl glycol and polyethylene glycol with a molar mass greater than 3,000. Included in the composition is 1 ... 10% powder aid selected from the group 41 consisting of ethanolamide of a fatty acid, amide of a fatty acid, alkyl alcohol, substituted phenol and polyethylene glycol with a molar mass between 200 and 1000. 43
US Patent No. 4,303,501 discloses a plastic dispersible pigment concentrate, which is prepared by combining 51 ... 85% by weight pigment and 14 ... 49% by weight waxy corn. The waxy component is presented as a natural, petroleum or synthetic wax that blends with either polyethylene glycol or a hydrocarbon resin to reduce melt viscosity and allow for better pigment incorporation.
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Polyethylene glycol is known as an additive for direct compounding in thermoplastic compositions.
US Patent 40,13622 discloses the incorporation of 100 ... 600 ppm polyethylene glycol with molecular masses of 600 ... 20,000, preferably 1300 ... 75000 to reduce polyethylene breakage during the film forming operation, which is evidenced by formation of ice.
U.S. Patent No. 48,125,544,4440,671 and 4305849 disclose the use of polyethylene glycols with molar masses of 1,000 ... 20,000 as beneficial for reducing thermal characteristics and water wetting in polyolefin compositions used for electrical insulation. Similarly, US patent 4612139 extends this concept of reducing wetting to include polyethylene glycol in semiconductor polyolefin compositions containing carbon black.
Similar compositions are claimed in DE 2723488, wherein polyethylene glycol and other mobile additives are shown to be beneficial for reducing interlaminar adhesion between the insulator layer and the outer conductive layer in an electrical cable construction. Polyethylene glycol and branched ethoxylated molecules are presented as plasticizers for ethylene-acrylic acid copolymers in US Pat. No. 3361702.
GB 975847 discloses the use of polyethylene glycol or an aliphatic derivative in an aqueous solution as a means of obtaining agglomerates of organic rubber chemicals. In the middle, a paste is formed which turns into pellets and dries at a low temperature.
The invention relates to a composition of carbon black, containing carbon black and 0.1 ... 50% by weight of at least one binder chosen from at least one of the following groups consisting of:
i) an ethoxylated polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to ethoxylation, wherein the total number of ethylene oxide molecules per polyhydroxyl alcohol is at least 3;
ii) an ester of a carboxylic alkyl acid with an ethoxylated polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule before ethoxylation, wherein the carboxylic alkyl acid has
8 ... 30 carbon atoms and can be saturated or unsaturated and in which the monoester functionality is at least 80% the rest being diester functionality, and in which the number of ethylene oxide molecules per ester of the polyhydroxyl alcohol is at least 3;
iii) an ester of a carboxylic alkyl acid with a polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to esterification, wherein the carboxylic alkyl acid has 8 ... 30 carbon atoms, may be saturated or unsaturated, and in which functionality monoester is at least 80%, the rest being diester functionality;
iv) an ester of an ethoxylated carboxylic alkyl acid with a polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to esterification, wherein the alkyl carboxylic acid has
8 ... 30 carbon atoms, can be saturated or unsaturated and in which the monoester functionality is at least 80%, the rest being diester functionality, and the number of ethylene oxide molecules per ester of the polyhydroxyl alcohol is at least 3 and
v) a polyethylene oxide-polypropylene oxide copolymer block.
Polyhydroxyl alcohol is preferably selected from the group consisting of triethanolamine, glycerine, pentaerythritol, sorbitol, sorbitan, sucrose and a polyglyceride.
The binder has an HLB value of 8 ... 30 and is selected from group i), group ii), group iii), group iv) or group v) and is present in an amount of 1.0. ..20% by weight.
The total number of ethylene oxide molecules per polyhydroxyl alcohol in the binder ranges from 3 to 500 or 5 to 100. Black smoke is treated with binder.
The invention further deals with a polymer composition, comprising a polymeric component, 0.1-65% by weight of a carbon black composition as defined in claim 1 and 0.1 ... 50% by weight of at least one binder. chosen from one of the following groups:
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i) an ethoxylated polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule before ethoxylation, wherein the total number of ethylene oxide molecules per polyhydroxyl alcohol is at least 3; 3 ii) a carboxylic acid ester with an ethoxyl polyhydric alcohol having at least hydroxyl groups per molecule prior to ethoxylation, wherein the carboxylic alkyl acid has 8 ... 305 carbon atoms, may be saturated or unsaturated, and wherein the monoester functionality is at least 80%, the remainder being diester functionality in which the number of 7 ethylene oxide molecules per ester of the polyhydroxyl alcohol is at least 3;
iii) an ester of a carboxylic alkyl acid with a polyhydroxyl alcohol having at least 39 hydroxyl groups per molecule prior to esterification, wherein the carboxylic alkyl acid has 8 ... 30 carbon atoms, may be saturated or unsaturated, and the monoester functionality is of at least 80%, the rest being diester functionality;
iv) an ester of an ethoxylated carboxylic alkyl acid with a polyhydroxyl alcohol having at least 13 hydroxyl groups per molecule prior to esterification, wherein the carboxylic alkyl acid has
8 ... 30 carbon atoms, it can be saturated or unsaturated, and the monoester functionality is at least 15% 80, the rest being a diester functionality in which the number of ethylene oxide molecules per ester of the polyhydroxyl alcohol is at least 3 and 17
v) a polyethylene oxide-polypropylene oxide-polyethylene oxide block copolymer.
In the invention there is also treated a semiconductor composition, which contains 25 ... 55% by 19 weight, a composition containing black smoke and 0.5 ... 10% by weight black smoke with at least one binder chosen from at least one of the following groups: 21
i) an ethoxylated polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule before ethoxylation, wherein the total number of ethylene oxide molecules per polyhydroxyl alcohol is at least 23;
ii) an ester of a carboxylic alkyl acid with an ethoxylated polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to ethoxylation, wherein the carboxylic alkyl acid has
8 ... 30 saturated or unsaturated carbon atoms, and in which the monoester functionality is at least 27%, the remainder being diester functionality, wherein the number of ethylene oxide molecules per ester of the polyhydroxyl alcohol is at least 3; 29 iii) an ester of a carboxylic alkyl acid with a polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to esterification, wherein the carboxylic alkyl acid has 8 ... 3031 carbon atoms, may be saturated or unsaturated, and wherein the monoester functionality is at least 80%, the remainder being diester functionality; 33 iv) an ester of an ethoxylated carboxylic alkyl acid with a polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to esterification, wherein the carboxylic alkyl acid has 35
8 ... 30 carbon atoms, saturated or unsaturated, and in which the monoester functionality is at least 80%, the rest being a functional diester in which the number of ethylene oxide molecules 37 per polyhydroxyl alcohol ester is at least 3 and
v) a polyethylene oxide-polypropylene oxide-polyethylene oxide blocker, up to 2% by weight of stabilizer or antioxidant, up to 5% by weight of organic peroxide, preferably dicumyl peroxide, up to 10% by weight of vinyl silane, the rest being a polymer or a mixture 41 of polymers selected from ethylene homopolymers, ethylene copolymerized with one or more alpha-olefins, such as propylene, butene or hexene, a ethylene copolymerized with propylene 43 and a diene monomer, preferably norbornene, a copolymer of ethylene with one or more monomers selected from vinyl acetate, acrylic acid, methacrylic acid, acrylic 45 or methacrylic acid esters containing 1 ... 8 carbon atoms, maleic anhydride or monoester derived from fumaric or maleic acid, vinyl chloride or vinylidene chloride. 47
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The invention also relates to a premixture composition, containing 70 ... 40% by weight homopolymer or copolymer of ethylene in which the monomer is selected from hexene, propene, butene, octene or vinyl acetate and 30 ... 60% in weight of a composition containing carbon black and 0.1 ... 50% by weight of at least one binder component selected from one of the following groups:
i) an ethoxylated polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to ethoxylation, wherein the total number of ethylene oxide molecules per polyhydroxyl alcohol is at least 3;
ii) an ester of a carboxylic alkyl acid with an ethoxylated polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule before ethoxylation, wherein the carboxylic alkyl acid has
8 ... 30 saturated or unsaturated carbon atoms, and wherein the monoester functionality is at least 80%, the rest being diester functionality where the number of ethylene oxide molecules per ester of the polyhydroxyl alcohol is at least 3;
iii) an ester of a carboxylic alkyl acid with a polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to esterification, wherein the carboxylic alkyl acid has 8 ... 30 carbon atoms, saturated or unsaturated, wherein the monoester functionality is at least 80%, the rest being diester functionality;
iv) an ester of an ethoxylated carboxylic alkyl acid with a polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to esterification, wherein the alkyl carboxylic acid has
8 .. .30 saturated or unsaturated carbon atoms, wherein the monoester functionality is at least 80%, the remainder being a diester functionality where the number of ethylene oxide molecules per ester of the polyhydroxyl alcohol is at least 3 and
v) a polyethylene oxide-polypropylene oxide-polyethylene oxide block copolymer.
The invention also relates to a composition based on carbon black, which contains carbon black and 0.1 ... 50% by weight of sucrose distearate.
It is preferred that the binders in groups i, ii, iii, iv and v have an HLB value of between 8.0 and 30. The HLB value refers to the value of the hydrophilic-lipophilic balance that can be determined by the method described in Non-lonic Surfactants vol. 23, edited by Martin Schick (Marcel Dekker lnc. (New York) 1987JSBN 0-8247-7530-9), pg.440. Non-lonic Surfactants Vol 23 presents equations that correlate the structure of the surface agent molecule with the HLB value. The HLB value is also discussed in the article: Griffin WC, J.Soc.Cosmetic Chemist, vol.l, pg.311 et seq. (1949) and you 5, pg.249 (1954). From the data regarding the percentage of ethylene oxide in the molecule, the saponification number of the ester link and the acid value of the fatty acid, one can directly calculate the HLB value with one of the following equations:
- for polyhydroxyl esters of fatty acid
HLB = 20 (1-S / A) wherein S = saponification number of ester and A- acid index of acid and
- for ethoxylated polyhydroxyl alcohols:
HLB = (E + P) / 5, wherein E = weight of ethylene oxide percentage = weight of polyhydric alcohol pigment.
Although any smoke black may be used in the compositions according to the present invention, preferably smoke black from the smoke black composition has a specific nitrogen area (N2SA) from 15 to 1800 m<sup>2</sup>/ g, a value of the absorption of dibutyl phthalate (DBP) by
50 .. .350 cm<sup>3</sup>/ 100g and an absorption value of trimethylammonium bromide (CTAB) of
15 .. .1500 m<sup>2</sup>/ G.
The compositions according to the invention can be obtained by any method known in the art such as physical mixing of the components, mixing the melt of the components or combining the components during the pelletization of the carbon black. Preferably, the carbon black compositions are obtained by pretreating the carbon black with binder.
RO 121129 Β1
Smoke black compositions can be obtained by a pelletizing process by: 1
-contacting a black of fluffy smoke in a pelletizer with an aqueous solution containing a binder selected from the mentioned group of compounds, in which the preferred level of binder in water 3 of pelletizing is 0.5% ... 5O%, preferably 20 to 40% by weight and
-heating of wet pellets under conditions of temperature and controlled duration so that the water 5 is removed from the pellets, but the binder does not undergo substantial decomposition, and the final level of binder in black of smoke is 0.1% ... 5O% . 7
The invention also relates to novel polymer compositions comprising:
- a polymeric component and 0.1 ... 65%, preferably 0.1 ... 20%, by weight, of a 9 composition of carbon black containing 0.1 ... 50%, preferably 1 ... 20%, of at least one binder chosen from one of the groups i, ii, iii, iv or v mentioned above. Preferably, 11 smoke black is pretreated with the binder, smoke black and the preferred binder in the smoke black compositions according to the invention have been presented previously. Polymer compositions may also include other conventional additives such as pigments, reinforcing agents and so on.
Although in the polymer compositions according to the invention, any polymer can be used, preferred polymers to be used include, but are not limited to:
a) homo or ethylene graft copolymers and polymers wherein the comonomers are selected from 17 of butene, hexene, propene, octene, vinyl acetate, acrylic acid, methacrylic acid, acrylic acid esters, methacrylic acid esters, maleic anhydride, semi- maleic anhydride esters 19 and carbon monoxide;
b) elastomers selected from natural rubber, polybutadiene, polyisoprene, statistical butadiene-styrene rubber (SBR), polychloroprene, acrylonitrile-butadiene, ethylene-propylene co- and terpolymers; 23
c) homo and styrene copolymers, including linear polymer and styrene-butadiene-styrene as radial terpolymer, acrylonitrile-butadiene-styrene (ABS) and styrene-acrylonitrile (SAN);
d) polyester or linear or branched polyester-polyols;
e) crystalline and amorphous polyesters and polyamides; 27
f) alkyd resins, resin acids or resin esters, hydrocarbon resins obtained by thermal polymerization or Friedel Crafts of cyclic dienes such as dicyclopentadiene, indene, 29 cumene and
g) hydrocarbon oils such as paraffinic oil, naphthenic oil and hydrogenated naphthenic oil 31.
The polymer compositions according to the invention can be obtained by any method known in the art 33 for combining polymers with dry or aqueous components.
The invention also relates to articles obtained from the polymer composition according to the invention. For use in applications in cables and semiconductor wires, a typical formulation according to the invention comprises: 37
- 25 ... 55% by weight of a composition containing smoke black and 0.5 ... 10 parts per 100 parts black of smoke of at least one binder component selected from one of groups i, ii, iii, 39 iv or v, mentioned above;
- up to 2% by weight of stabilizer or antioxidant 41
- up to 5% by weight of organic peroxide, preferably dicumyl peroxide;
- up to 10% by weight of silane vinegar; 43 the remainder being a polymer or a mixture of polymers selected from the following groups: ethylene homopolymer, ethylene copolymerized with one or more alpha olefins, such as propylene, 45 butene or hexene, ethylene copolymerized with propylene and a dienene monomer, preferably norborn. and a copolymer of ethylene with one or more monomers selected from 47 vinyl acetate, acrylic acid, methacrylic acid, acrylic or methacrylic acid esters containing 1 ... 8 atoms.
EN 121129 Β1 carbon, maleic anhydride or monoester derived from fumaric or maleic acid, vinyl chloride or vinylidene chloride.
The semiconductor composition of the invention may further include a polymeric additive such as an acrylonitrile-butadiene elastomer containing 25-55% by weight acrylonitrile.
For use, as a premix composition, a typical formulation according to the invention is that which comprises:
- 30 ... 60% by weight of a composition containing carbon black and 0.1 ... 50%, preferably 1 ... 20% of at least one binder component selected from one of the groups i, ii , iii, iv or v, mentioned above, and
- 70 ... 40% by weight of a homopolymer or copolymer of ethylene, wherein the comonomer is preferably selected from hexene, propene, butene, octene or vinyl acetate. Preferably, the polymer is polyethylene, low density polyethylene, low density linear polyethylene, high density polyethylene or a polyethylene wax. The premix composition may further comprise antioxidants, peroxide decomposers, sterically prevented amine light stabilizers, substituted benzophenone UV absorbers or processing aids.
An advantage of the carbon black compositions according to the invention is that all the dry carbon black compositions according to the invention have improved handling properties compared to the fluffy or conventional pelletized black.
Another advantage of the polymer compositions according to the invention is that they exhibit improved rheological or mechanical properties.
Other advantages of carbon black compositions and polymer compositions according to the invention are evident from the detailed presentation of the invention.
The invention relates to carbon black compositions which, in dry form, have improved handling characteristics and which give superior performance to polymer compositions.
Smoke black compositions include: smoke black and 0.1% to 5%, preferably
1 ... 20% by weight of at least one binder chosen from one of the following groups:
i) an ethoxylated polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to ethoxylation, wherein the total number of ethylene oxide molecules per polyhydroxyl alcohol is at least 3; preferably, the polyhydroxyl alcohol is selected from the group consisting of triethanolamine, glycerine, pentaerythritol, sorbitol, sorbitan, sucrose or a polyglyceride and / or the total number of ethylene oxide molecules per polyhydroxyl alcohol varies from 3 to 500 and more preferably varies from 5 to 5 the 100;
ii) an ethoxylated alkyl carboxylic acid and polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to ethoxylation, wherein the carboxylic alkyl acid has 8 ... 30 carbon atoms and can be saturated or unsaturated, and in which the monoester functionality is at least 80%, the remainder being diester functionality and wherein the number of ethylene oxide molecules per polyhydroxyl alcohol ester is at least 3; the polyhydroxyl alcohol is selected from the group consisting of triethanolamine, glycerine, pentaerythritol, sorbitol, sorbitan, sucrose or a polyglyceride and / or the total number of ethylene oxide molecules per polyhydroxyl alcohol ester varies from 3 to 500 and more preferably varies from 5 to 100;
iii) an alkyl carboxylic acid ester with a polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to esterification, wherein the carboxylic alkyl acid has 8 ... 30 carbon atoms, and may be saturated or unsaturated, and in which functionality mono-ester is at least 80% the rest being d / '- ester functionality; preferably, the polyhydroxyl alcohol is selected from the group consisting of: triethanolamine, glycerin, pentaerythritol, sorbitol, sorbitan, sorbitol and a polyglyceride;
Iv) an ethoxylated alkyl carboxylic acid ester with a polyhydroxyl alcohol having at least 1 hydroxyl group per molecule prior to esterification, wherein the carboxylic acid has 8 ... 30 carbon atoms, and may be saturated or unsaturated, and wherein the monoester functionality is at least 80% the remainder being a diester functionality, and wherein the number of ethylene oxide molecules per polyhydric alcohol ester is at least 3; preferably the polyhydroxyl alcohol is 5 selected from the group consisting of: triethanolamine, glycerine, pentaerythritol, sorbitol, sorbitan and a polyglyceride and / or the total number of ethylene oxide molecules per polyhydroxyl alcohol ester 7 varies from 3 to 500 and more preferably varies. from 5 to 100;
v) a polyethylene oxide-polypropylene oxide-polyethylene oxide copolymer block. 9
It is preferred that the binders in groups i, ii, iii, iv and v have an HLB value of between 8.0 and 30. The HLB value can be determined as described above. 11
Although any type of smoke black may be used in the compositions according to the invention, preferably the black of smoke must have a specific nitrogen surface (N<sub>2</sub>SA) between 15 and 13 1800 m<sup>2</sup>/ g, an absorption value of dibutyl phthalate (DBP) of 50 ... 350 cm<sup>3</sup>/ 100g and an absorption value of trimethylammonium bromide (CTAB) of 15 ... 1500 m<sup>2</sup>/ G. 15
Smoke black compositions can be obtained by any conventional technique of combining smoke black with dry or aqueous components. Preferably, the 17 carbon black compositions are obtained by pretreating the carbon black with the binder. Smoke black compositions can be obtained, in dry form, through a conventional pelletizing process. For example 19, the carbon black compositions according to the invention can be obtained by contacting the fluffy carbon black in a needle pelletizer with an aqueous solution containing a binder chosen 21 from the above mentioned group of compounds and wherein the binder level in the water is pelletizing is 0.5% ... 5O% and heating the wet pellets under controlled temperature and time conditions, 23 so that the water is removed from the pellets, but the binder does not undergo substantial decomposition, and the final level of binder on carbon black is 0.1% ... 4O%. The preparation of 25 aqueous solutions containing the binder compositions used in the present invention is within the scope of those skilled in the art. 27
Needle pelletizers that can be used to obtain compositions according to the invention are known in the art and include the pelletizers described in US Pat. No. 3528785, 29 which is: incorporated by reference in the present specification. US Patent 3528785 also discloses a conventional pelletizing process, which can be used to obtain compositions according to the invention.
The present invention also includes novel polymer compositions containing: 33
- a polymeric component and 0.1 ... 65%, preferably 0.1 ... 20%, by weight, composition containing carbon black and 0.1 ... 50%, preferably 1 ... 20 %, of at least one binder chosen 35 from one of the following groups:
i) an ethoxylated polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to ethoxylation 37, wherein the total number of ethylene oxide molecules per polyhydroxyl alcohol is at least 3; preferably, the polyhydric alcohol is selected from the group consisting of triethanolamine, 39 glycerin, pentaerythritol, sorbitol, sorbitan, sucrose or a polyglyceride and / or the total number of ethylene oxide molecules per polyhydroxyl alcohol varies from 3 to 500 and more preferably, varies 41 from 5 to 100;
ii) an ethoxylated alkyl carboxylic acid and polyhydroxyl alcohol having at least 3 43 hydroxyl groups per molecule prior to ethoxylation, wherein the carboxylic alkyl acid has 8 ... 30 carbon atoms and may be saturated or unsaturated, and in which functionality monoester is 45 at least 80% the rest being diester functionality, and in which the number of ethylene oxide molecules per polyhydroxyl alcohol ester is at least 3; preferably the polyhydroxyl alcohol 47 is selected from the group consisting of triethanolamine, glycerine, pentaerythritol, sorbitol, sorbitan,
EN 121129 Β1 sucrose or a polyglyceride and / or the total number of ethylene oxide molecules per polyhydric alcohol ester ranges from 3 to 500 and more preferably ranges from 5 to 100;
iii) an alkyl carboxylic acid ester with a polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to esterification, wherein the carboxylic alkyl acid has 8 ... 30 carbon atoms, and may be saturated or unsaturated, and in which functionality monoester is at least 80%, the rest being diester functionality; preferably, the polyhydroxyl alcohol is selected from the group consisting of: triethanolamine, glycerine, pentaerythritol, sorbitol, sorbitan, sorbitol and a polyglyceride;
iv) an ethoxylated alkyl carboxylic acid ester with a polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to esterification, wherein the carboxylic acid has 8 ... 30 carbon atoms, and may be saturated or unsaturated, and in which functionality monoester is at least 80% the rest being a diester functionality, and in which the number of ethylene oxide molecules per polyhydroxyl alcohol ester is at least 3; preferably, the polyhydroxyl alcohol is selected from the group consisting of trtriethanolamine, glycerine, pentaerythritol, sorbitol, sorbitan and a polyglyceride and / or the total number of ethylene oxide molecules per polyhydroxyl alcohol ester varies from 3 to 500 and more preferably varies from 5 the 100;
v) a polyethylene oxide-polypropylene oxide-polyethylene oxide copolymer block.
Preferably, the carbon black is pretreated with a binder component, the carbon black and the preferred binder for the carbon black compositions according to the invention are mentioned above. For example, it is preferred that the binder has an HLB value of 8.0 ... 30. Polymer compositions may also include other conventional additives such as pigments, reinforcing agents and so on.
Although any polymer may be used in the polymer compositions according to the invention, preferred polymers to be used include, but are not limited to:
a) homo or ethylene graft copolymers and polymers in which the comonomers are selected from butene, hexene, propene, octane, vinyl acetate, acrylic acid, methacrylic acid, acrylic acid esters, methacrylic acid esters, maleic anhydride, anhydride semi-esters maleic and carbon monoxide;
b) elastomers selected from natural rubber, polybutadiene, polyisoprene, statistical styrene-butadiene rubber (SBR), polychloroprene, acrylonitrile-butadiene, co- and ethylene-propylene terpolymers;
c) styrene homo and copolymers, including linear and radial styrene-butadiene-styrene, acrylonitrile-butadiene-styrene (ABS) and styrene-acrylonitrile (SAN) polymers;
d) linear and branched polyester or polyester;
e) crystalline and amorphous polyesters and polyamides;
f) alkyd resins, resin acids or resin esters, hydrocarbon resins obtained by thermal polymerization or Friedel Crafts of cyclic diene monomers such as dicyclopentadiene, indene, cumene and
g) hydrocarbon oils such as paraffinic oil, naphthenic oil and hydrogenated naphthenic oil.
The polymer compositions according to the invention can be obtained in the art known for combining polymers with dry or aqueous components.
From the polymer compositions according to the invention, technical articles with various uses can be obtained.
For use with semiconductor wires and cables, a typical formulation comprises:
- 25 ... 55% by weight a composition containing carbon black and 0,5 ... 10 parts per 100 parts black of smoke, of at least one binder chosen from at least one of the following groups:
i) an ethoxylated polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule before ethoxylation, wherein the total number of ethylene oxide molecules per polyhydroxyl alcohol is
At least 3, preferably polyhydroxyl alcohol is selected from the group consisting of triethanolamine, 1 glycerol, pentaerythritol, sorbitol, sorbitan, sucrose or a polyglyceride and / or the total number of ethylene oxide molecules per polyhydroxyl alcohol at 3 500 and more preferably vary 3 from 5 to 100;
ii) an ethoxylated alkyl carboxylic acid ester and polyhydroxyl alcohol having at least 3 5 hydroxyl groups per molecule before ethoxylation, wherein the carboxylic alkyl acid has 8 ... 30 carbon atoms and may be saturated or unsaturated, and in which functionality monoester is 7 at least 80% the rest being diester functionality and wherein the number of ethylene oxide molecules per polyhydroxyl alcohol ester is at least 3, preferably, the polyhydroxyl alcohol 9 is selected from the group consisting of triethanolamine, glycerine, pentaerythritol, sorbitol, sorbitan, sucrose or a polyglyceride and / or the total number of ethylene oxide molecules per ester of 11 polyhydroxyl alcohol varies from 3 to 500 and more preferably varies from 5 to 100;
iii) an alkyl carboxylic acid ester with a polyhydroxyl alcohol having at least 3 hydroxyl groups 13 per molecule prior to esterification, wherein the carboxylic alkyl acid has 8 ...... 30 carbon atoms, and may be saturated or unsaturated, and where the monoester functionality is at least 80%, the rest being diester functionality; preferably, the polyhydroxyl alcohol is selected from the group consisting of: triethanolamine, glycerin, pentaerythritol, sorbitol, sorbitan, sorbitol and a polyglyceride;
iv) an ethoxylated alkyl carboxylic acid ester with a polyhydroxyl alcohol having at least 19 3 hydroxyl groups per molecule prior to esterification, wherein the carboxylic acid has 8 ... 30 carbon atoms and may be saturated or unsaturated and wherein the monoester functionality is at least 80%, the rest being a diester functionality and in which the number of ethylene oxide molecules per polyhydroxyl alcohol ester is at least 3, preferably the polyhydroxyl alcohol is 23 selected from the group consisting of: triethanolamine, glycerine, pentaerythritol, sorbitol, sorbitan and a polyglyceride and / or the total number of ethylene oxide molecules per polyhydroxyl alcohol ester 25 varies from 3 to 500 and more preferably varies 5 to 100;
v) a polyethylene oxide-polypropylene oxide-polyethylene oxide copolymer block; 27
- up to 2% by weight of a stabilizer or antioxidant;
- up to 5% by weight of organic peroxide, preferably dicumyl peroxide; 29
- up to 10% by weight of silane vinegar;
the remainder being a polymer or a mixture of polymers selected from the following group: homopolymer 31 of ethylene; ethylene copolymerized with one or more alpha olefins, such as propylene, butene or hexene; ethylene copolymerized with propylene and a dienic monomer, preferably 33 norbornene and ethylene copolymer with one or more monomers selected from vinyl acetate, methacrylic acid, acrylic acid, acrylic or methacrylic acid esters containing 1 ... 8 carbon atoms , maleic anhydride or monoester derived from fumaric or maleic acid, vinyl chloride or vinylidene chloride. 37
The vulcanizable semiconductor compositions according to the invention may further contain an additive polymer such as acrylonitrile-butadiene elastomer containing 25-55% by weight 39 acrylonitrile.
For use as a premix composition, a typical formulation according to the invention 41 may comprise:
- 70 ... 40% by weight of homopolymer or copolymer of ethylene, wherein comonomer 43 is selected from hexene, propene, butene, octene or vinyl acetate, and
- 30 ... 60% by weight of composition containing carbon black and 0.1 ... 50% by weight, 45 of at least one binder component selected from one of the following groups:
i) an ethoxylated polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule before ethoxylation 47, wherein the total number of ethylene oxide molecules per polyhydroxyl alcohol is
At least 3, preferably polyhydroxyl alcohol is selected from the group consisting of triethanolamine, glycerine, pentaerythritol, sorbitol, sorbitan, sucrose or a polyglyceride and / or the total number of ethylene oxide molecules per polyhydroxyl alcohol at 500 and varies from 3 to 500. , more preferably, ranges from 5 to 100;
ii) an ethoxylated alkyl carboxylic acid and polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule before ethoxylation, wherein the carboxylic alkyl acid has 8 ... 30 carbon atoms and may be saturated or unsaturated, wherein the monoester functionality is of at least 80%, the rest being diester functionality, and in which the number of ethylene oxide molecules per polyhydroxyl alcohol ester is at least 3; preferably ranges from 3 to 500, more preferably ranges from 5 to 100, and wherein the polyhydroxyl alcohol is selected from the group consisting of triethanolamine, glycerin, pentaerythritol, sorbitol, sorbitan, sucrose or a polyglyceride;
iii) an alkyl carboxylic acid ester with a polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to esterification, wherein the carboxylic alkyl acid has 8 ... 30 carbon atoms and may be saturated or unsaturated, and wherein the mono functionality -ester is at least 80%, the rest being d / -ester functionality; preferably the polyhydroxyl alcohol is selected from the group consisting of: triethanolamine, glycerine, pentaerythritol, sorbitol, sorbitan, sorbitol and a polyglyceride;
iv) an ethoxylated alkyl carboxylic acid ester with polyhydroxyl alcohol having at least 3 hydroxyl groups per molecule prior to esterification, wherein the carboxylic acid has 8 ... 30 carbon atoms, and may be saturated or unsaturated, and wherein the monoester functionality is at least 80%, the remainder being a diester functionality, and wherein the number of ethylene oxide molecules per polyhydric alcohol ester is at least 3, preferably ranging from 3 to 500, more preferably it ranges from 5 to 100, and wherein the polyhydroxyl alcohol is selected from the group consisting of: triethanolamine, glycerin, pentaerythritol, sorbitol, sorbitan and a polyglyceride;
v) a polyethylene oxide-polypropylene oxide-polyethylene oxide copolymer block; preferably, the polymer composition is polyethylene, low density polyethylene, low density linear polyethylene, high density polyethylene or a polyethylene wax. The premix composition may further include antioxidants, peroxide decomposers, sterically hindered amine light stabilizers, substituted UV benzophenone adsorbents, or processing aids.
The efficacy and advantages of the various aspects and embodiments of the present invention are further illustrated by 52 non-limiting embodiments, in which the test procedures described below are used.
The following tests are used to evaluate the analytical properties of carbon black. The value of DBP (the value of the adsorption of dibutyl phthalate) of the carbon black used, expressed as cubic centimeters of DBP per 100 g of black carbon (cm<sup>3</sup>/ 100g), is determined according to the procedure of ASTM D2414. The specific nitrogen surface area (N2SA) of the carbon black used in the examples, expressed as square meters per gram (m)<sup>2</sup> / g), is determined according to ASTM D3 037 Method A.
Smoke black pellets described in the following examples are evaluated by the following tests. Pellet resistance is determined according to ASTM D1937. The pellet crushing is evaluated using a modified version of ASTM D4324, in which the test procedure is modified to generate the dust level after stirring the samples for 5 minutes.
The moisture content of the pellets is determined by drying the samples at constant weight in an air circulation oven at 150'C and calculating the percentage of moisture by comparing the weight before drying with the weight after drying.
The polymer compositions, including the premix compositions, described in the examples are tested by the tests presented below.
RO 121129 Β1
The melt index is determined according to ASTM D1238. 1
The pressure increase of the premix compositions determines by introducing a 325 mesh site (hole size47) behind the plate of the extruder breaker a single 3 screw of 0.025 m (l / inch) provided with a pressure transducer to measure the pressure variation in the site region . 5
The viscosity of the polymer compositions is measured using a Carri-Med CS viscometer, manufactured and marketed by TA Instruments in Wilmington, Delaware, at temperature and 7 at a shear rate specified in the examples.
Passages through the three-roller roller are evaluated by passing the polymer compositions 9 through a three-roller roller and recording the number of passes required to generate zero cracks on the Hegman apparatus and also the residual sand value 11 is recorded.
The dispersion of the diluted samples is determined by diluting the premix compositions 13 to a 2% by weight, carbon black EVA resin in a Brabender mixer operating at 85 ° C and 50 rpm. The mixing time is 15 2 minutes. The samples are then pressed between the microscope slides and the dispersion determined at a magnification of 100X by the Cabot Corporation evaluation method in which the numbers (1 - 6) refer to the size of the dispersed particles, 1 being for the small and 6 for the large; and the letters (AE) refer to the number of particles in the visual field, A being 1 -2 particles and E being for 19 more than 50 particles. Small numbers and first letters indicate better dispersion, so AI indicates good dispersion, and 6E indicates poor dispersion. 21 in Examples 18-26, the dispersion of the black smoke pellets was determined by measuring the number and size of the tape imperfections formed by a compound that has 23 pellets incorporated, using a 100X optical microscope and a reflected light source.
The polymer compositions were evaluated from the point of view of the exfoliation using the following technique. Compositions containing 40% carbon black in ethylene-vinyl acetate resin were compounded in a Brabender mixer with 1% dicumyl peroxide, maintaining the temperature 27 below 150 ° C. The material was transferred to a heated hydraulic press (temperature 130 ° C) and a 1.2 mm plate was obtained. Similarly, a plate with a content of 1% dicum- 29 thousand peroxide was obtained. The two plates were laminated together at a pressure of 7,030 kg / cm<sup>2</sup> (100 psi) and were cured at 180 ° C for 15 min. The laminate was allowed to cool to 31 cup at room temperature under pressure. The delamination force was recorded at an exfoliation angle of 180 ° and a separation speed of 0.10 m / min (3.94 inches / min); results 33 represent the average of 28 exfoliation tests.
The modulus, strength and elongation of the polymer compositions are measured by procedure 35 according to ASTM D 412.
Shore A hardness of rubber compounds is determined according to ASTM 37 D-2240-86.
The maximum torque is determined from the motor load curve as a function of time, 39 in a Brabender mixer.
The unloading torque (Nm) is determined from the value of the final torsion at the end of the 41 mixing cycle.
The total energy (Nm) is determined by calculating the area under the complete curve of 43 mixing.
MDR @ 170 ° C T50 (mm) and T90 (mm) are determined according to the procedure of ASTM 45 2084.
Mooney viscosity (ML (1 +4) @ 100 ° C is determined according to the procedure in ASTM 47
1646.
RO 121129 Β1
IRHD hardness is determined according to ASTM D1415.
The efficiency and advantages of the present invention will be illustrated by the following examples.
Examples 1 4. Examples 1 - 4 illustrate the use and benefits of carbon black compositions according to the invention, compared to conventional carbon black pellets, in polypropylene fiber coatings.
Four compositions of black carbon pellets A, B, C and D were obtained by introducing 400 g of fluffy black, identified as CB-1, with a DBP value of 60 cm.<sup>3</sup>/ 100 g and a specific nitrogen nitrogen content of 112 m<sup>2</sup>/ g, in a pelletizer together with a solution containing 20 g of binder and 300 g of water. The binder used for each pellet composition is presented in the table below.
<td>Pellet composition</td><td>Binder</td>
<td>A</td><td>The water</td>
<td>B</td><td>5% ethoxylated sorbitan monostearate with 20 moles (group iv)</td>
<td>C</td><td>5% ethoxylated 5 mole sorbitan monooleate (group iv)</td>
<td>D</td><td>5% ethoxylated sorbitan monooleate with 20 moles (group iv)</td>
Composition A of carbon black pellets was for comparison, compositions of carbon black pellets B, C and D were according to the invention.
The black smoke / binder mixture was stirred for 5 minutes at a rotation of 800 rpm. The resulting pellets were dried at 120 ° C until the moisture content of the pellets was below 0.51. Pellet resistance for each composition was assessed qualitatively. The results are presented in table 1.
Smoke black pellets were combined with polypropylene homopolymer with a melt index of 35 in a double screw extruder to obtain a premix containing 35% by weight of black smoke, the rest being polypropylene and binder.
The polypropylene composition was introduced in a single-screw extruder until the equilibrium pressure conditions. The premix was introduced and the pressure variation was recorded according to the procedure described above. The results are presented in table 1.
Table 1
<td>Composition of black smoke pellets</td><td>Pellet resistance</td><td>Increased pressure (kg / cm<sup>2</sup>) / G</td>
<td>A</td><td>small</td><td>0.342 (4.86 psi / g)</td>
<td>B</td><td>big</td><td>0.305 (4.34 psi / g)</td>
<td>C</td><td>big</td><td>0.299 (4.25 psi / g)</td>
<td>D</td><td>big</td><td>0.209 (2.97 psi / g)</td>
These results indicate that the carbon black compositions B, C and D, according to the invention, have an improved pellet strength compared to the composition A obtained only with water. In addition, reducing the pressure rise in the premix compositions containing carbon black B, C and D, according to the invention, as compared to the premix composition containing the composition of carbon black, has the effect of reducing the frequency of variation of the die in a line.
EN 121129 Β1 of fiber production and therefore the operating capacity is improved, and the operating costs 1 are reduced.
Examples 5-10. Examples 5-10 illustrate the use and benefits of 3 carbon black compositions according to the invention, compared to conventional black carbon pellets, in applications to polypropylene fibers. 5
Two compositions of carbon black pellets, E and F, were obtained in a continuous process, by combining fluffy black, identified as CB-2, with a DBP value of 7 112 cm. <sup>3</sup>/ 100 g and a specific surface area of 60 m nitrogen<sup>2</sup>/ g, in a pelletizer with discontinuous needles, with a binder solution. The pellets were obtained in a pelletizer with continuous needles which operates at a rotation of 800 rpm, obtaining wet pellets with an average water content of 50%. The wet pellets were dried in a heated rotary drum, obtaining dry pellets, with a moisture content below 0,6%.
The binder used in each pelletizing composition is presented in the table below. 13
<td>Pellets composition</td><td>Binder</td>
<td>E</td><td>The water</td>
<td>F</td><td>2% ethoxylated sorbitan monooleate with 20 moles (group iv)</td>
There were 4 experiments with composition E and two with composition F. Composition E of the carbon black pellet was a control composition and composition F was a carbon black composition according to the invention.
The pellets were evaluated in terms of the strength of the pellet and the wear using the procedures described above. In addition, the pellets were used to obtain a premix, as in Examples 1 -4, and the increase in pressure was determined as described above. The results are presented in table 2.
Table 2
<td>Composition of black smoke pellets</td><td></td><td>Pellet resistance (kilograms)</td><td>Dust (%) 5 min.</td><td>Increased pressure (kg / cm<sup>2</sup>) / G</td>
<td>E</td><td>Exp.1</td><td>6.80 (15 Ibs.)</td><td> 1,2</td><td>0.773 (11.0 psi / g)</td>
<td>E</td><td>Exp.2</td><td>6.35 (14 Ibs.)</td><td> 1,2</td><td>0.801 (11.4 psi / g)</td>
<td>E</td><td>Exp.3</td><td>7.26 (16 Ibs.)</td><td> 2,8</td><td>0.907 (12.9 psi / g)</td>
<td>E</td><td>Exp.4</td><td>8.16 (18 Ibs.)</td><td> 1,6</td><td>0.640 (9.1 psi / g)</td>
<td>F</td><td>Exp.1</td><td>19.95 (44 Ibs.)</td><td> 0.4</td><td>0.513 (7.3 psi / g)</td>
<td>F</td><td>Exp.2</td><td>26.30 (58 1 bs)</td><td> 0,2</td><td>0.372 (5.3 psi / g)</td>
RO 121129 Β1
These results illustrate the significant improvement of the strength of the pellets and the wear resistance by incorporating a binder of the type used in the present invention during the pelletizing process in the preparation of composition F according to the invention. The F composition of the black carbon pellet according to the invention has an improved dispersion compared to the composition E of the black carbon pellet conventionally pelleted with water, as can be seen from reducing the pressure increase when extruded by a die. , which results in improved productivity at reduced operating cost.
Examples 11-14. Examples 11-14 illustrate the advantages of black carbon pellet compositions according to the invention for uses in the field of polyurethanes.
Two types of fluffy carbon black, identified as CB-3 and CB-4, are pelletized to obtain compositions of carbon black pellets. CB-3 and CB-4 smoke black have the analytical properties presented below:
<td>Fluffy black smoke</td><td>DBP</td><td>N2 SA</td>
<td>CB-3</td><td>112cm<sup>3</sup>/ 100g</td><td>58 m<sup>2</sup>/ g</td>
<td>CB-4</td><td>140 cm<sup>3</sup>/ 100g</td><td>68 m<sup>2</sup>/ g</td>
Four compositions of smoke black pellets, G, Η, I and J were obtained in a continuous process by combining the smoke black in a pelletizer with needles together with a binder solution.
The pellets were obtained in a continuous needle pelletizer at a rotor speed of 1000 rpm and dried in a rotary drum to obtain pellets with a moisture content below 0.3%. The binder and smoke black used in each composition are shown in the table below.
<td>Pellet composition</td><td>Carbon black</td><td>Binder</td>
<td>G</td><td>CB-3</td><td>the water</td>
<td>H</td><td>CB-3</td><td>2% sorbitan monooleate with 20 moles ethylene oxide (group iv)</td>
<td>I</td><td>CB-4 water</td><td>the water</td>
<td>J</td><td>CB-4</td><td>2% sorbitan monooleate with 20 moles ethylene oxide (group iv)</td>
Pellets of carbon black, G and I were control compositions, and compositions H and J were compositions according to the invention.
The pellets were evaluated from the point of view of the resistance of the pellets in the way presented above. The results were as follows:
<td>Pellet composition</td><td>Pellet strength - kg</td>
<td>G</td><td>6.35 - 7.26 (14-16 pounds)</td>
<td>H</td><td>23.13 (51 pounds)</td>
<td>I</td><td>4.53 (10 pounds)</td>
<td>J</td><td>11.79 (26 pounds)</td>
RO 121129 Β1
The compositions of black smoke pellets G, Η, I and J were compounded in a polyol 1 polyol with a viscosity of 150 mPa.s at 25'C and a hydroxyl content of 3.5% to obtain a smoke black paste 30%. In addition, the polyether polyol composition was obtained by rubbing the CB-4 smoke black with the CB-4 smoke black with a polyol and adding a 2% sorbitan monooleate binder with 20 moles of ethylene oxide directly into the polyol. Each 5-compounding operation involved pre-dispersion at a high shear rate, in a Dispermat mixer, for 5 minutes at a speed of 2 000 rpm. 7
The paste was then transformed into a roller with three rollers for the final reduction of the size. The number of roller crossings required to generate zero exfoliation on a Hegman device9 was recorded along with the residual "sand" value.
The paste was then diluted and the viscosity was measured on a Carri-Med CS viscometer at a shear rate of 300 s-1. The results are presented in table 3.
Table 313
<td>Composition of black smoke pellets</td><td>Number of triple roller passes</td><td>"Sand" (microns)</td><td>Viscosity shear stress (dyne / cm<sup>z</sup>)</td>
<td>G</td><td> 5</td><td> 37</td><td> 2800</td>
<td>H</td><td> 5</td><td> 19</td><td> 1900</td>
<td>I</td><td> 6</td><td> 17</td><td> 1860</td>
<td>J</td><td> 5</td><td> 17</td><td> 1400</td>
<td>CB-4, Binder added to polyol</td><td> 7</td><td> 26</td><td> 1790</td>
The above experiments illustrate the improved strength and dispersion of the pellets, 23 and a reduced viscosity of the compound of the H and J smoke black pellet compositions according to the invention, compared with the use of the P and G black H pellets only 25 with water. . The data also demonstrate the advantages of incorporating a binder directly onto the carbon black (by pretreating the carbon black with a binder), as compared to adding the binder 27 to the polymeric system.
This example is representative of polyurethane foam and sealants and 29 demonstrates the improvements achieved in the dispersion and rheology of polymer compositions containing carbon black compositions according to the invention. The reduction of viscosity allows the use of 31 low pressures when applying polyurethane seals, either directly to the windows, or to the units of double or triple windows. 33
Examples 15-17. These examples illustrate the advantages of using carbon black compositions according to the invention in ink formulations. 35
The smoke black compositions G and H of Examples 11-14 were evaluated in a typical oil-based glossy ink using the same procedure as that of Examples 11-14. 37 in this case the basic system was an oil (McGee 47) and a thermosetting resin (Lawter Vehicle 3477) in a gravimetric ratio of 1: 9. A third ink formulation was obtained by adding 20 mol of sorbitan monooleate with 20 moles of ethylene oxide to a composition of carbon black G and oil used in the compounding process. 41
The compounding operation involves pre-dispersing, at high shear rate, in a Dispermat mixer, for 5 minutes at a speed of 2000 rpm. The paste was then transferred 43 on a three-roller roller for final size reduction. The number of passes through the three-roller roller required to produce zero exfoliation on a Hegman 45 device together with the residual sand value was determined. The paste was diluted with polyol to obtain one
RO 121129 Β1 load of 12% black smoke and viscosity was measured on a Carri-Med CS viscometer at a shear rate of 300 s'<sup>1</sup>. The results are presented in table 4.
Table 4
<td>Composition of black smoke pellets</td><td>Number of triple roller passes</td><td>"Sand" (microns)</td><td>Viscosity shear stress (dyne / cm<sup>2</sup>)</td>
<td>G</td><td> 5</td><td> 18</td><td> 330</td>
<td>H</td><td> 4</td><td> 15</td><td> 165</td>
<td>G, with binder added to the oil</td><td> 4</td><td> 17</td><td> 240</td>
These results demonstrate the improved dispersion and the reduced viscosity obtained when the binder composition used in the carbon black compositions according to the invention is incorporated either into the carbon black or added directly to the ink carrier. the incorporation of the binder on the black of smoke presents the best improvement. The binder helps reduce the mixing time for ink, and reduced viscosity and improved dispersion reduce wear in applications.
Examples 18-26. Examples 18-26 illustrate the use of carbon black compositions according to the invention in semiconductor compounds.
Three compositions of smoke black pellets K, L and M were obtained by combining fluffy black smoke, denoted by CB-5, having a DBP value of 140 cm.<sup>3</sup>/ 100 g and a specific surface area of 70 m nitrogen<sup>2</sup>/ g, in a needle pelletizer, together with a binder solution. Smoke black has been combined with different binder solutions in a needle pelletizer operating at 1050 rpm to obtain wet pellets with a content of sorbitan monooleat with 20 moles of ethylene oxide up to 4. The pellets have dried. in a rotary drum to obtain dry pellets with a moisture content below 0.6%. The binder used in each pelletizing composition is presented in the table below.
<td>Pellet composition</td><td>Binder</td>
<td>K</td><td>the water</td>
<td>IT</td><td>2% sorbitan monooleate with 20 moles ethylene oxide (group iv)</td>
<td>M</td><td>4% sorbitan monooleate with 20 moles ethylene oxide (group iv)</td>
Smoke black was compounded into an ethylene-vinyl acetate resin (vinyl acetate content 40%, melt index 3), using a double-screw extruder, to obtain a compound with 40% black smoke content . The compound was then extruded to obtain a band and the dispersion level of the black smoke was evaluated by measuring the number and size of the surface imperfections using an optical microscope (100x) with reflected light source, by the described procedure.
RO 121129 Β1
The results are as follows:
<td>EVA composition - smoke black</td><td>The surface of the black of the smoke not dispersed</td>
<td>K</td><td> 0,0470 %</td>
<td>IT</td><td> 0,0056 %</td>
<td>M</td><td> 0,0067 %</td>
The reduction of the black of non-dispersed smoke is reflected in the final extruded cable, whose surface is smoother. Reducing the imperfections of the surface of the semiconductor insulation layer reduces the frequency of electrical interruptions.
EVA compositions containing K and L smoke black compositions, as previously presented, were evaluated in terms of desisolation on a polyethylene substrate using the following technique: the 40% carbon black compound in ethylene-vinyl acetate resin was compounded in a Brabendercu 1% dicumyl peroxide mixer, keeping the mixing temperature below 150 ° C. The material was transferred to a heated hydraulic press at 130'C and a plate with a thickness of 1.2 mm was formed. A 2 mm polyethylene plate containing 1% dicumyl peroxide was similarly formed. The two plates were laminated together at a pressure of 7,030 kg / cm<sup>2</sup> (100 psi) and were exposed to a vulcanization cycle at 180 ° C for 15 min. The laminate was allowed to cool to ambient temperature under pressure. The delamination force was recorded at an exfoliation angle of 180 'and a separation speed of 0.10 m / min (3.94 inches / min); the results represent the average of 28 exfoliation tests:
<td>EVA-black composition of smoke</td><td>kg / cm</td><td>(lb / 0.5 inch)</td>
<td>K</td><td> 2,33 +/-0,16</td><td> (6,55+/-0,46)</td>
<td>IT</td><td> 1,83 +/-0,16</td><td> (5,12+/-0,44)</td>
The data indicate a reduction in the force required to remove the semiconductor protective compound from the insulating start. This is important in cable connection operations or terminal connections. A smaller force results in faster operation and minimizes the gaps / imperfections of the systems that require a high de-isolation force and, consequently, reduce the potential interruptions of the electric current.
Examples 27 - 37. Examples 27 - 37 illustrate the use of carbon black compositions in polyolefin premix compositions.
Four types of smoke black have been used to obtain smoke black compositions according to the invention and control smoke black compositions. The smoke black used was noted with CB-6, CB-7, CB-8 and CB-9 and has the properties presented below:
<td>Carbon black</td><td>DBP cm<sup>3</sup>/ 100 g</td><td>N<sup>2</sup>TO m<sup>2</sup>/ g</td>
<td>CB-6</td><td> 140</td><td> 68</td>
<td>CB-7</td><td> 135</td><td> 180</td>
<td>CB-8</td><td> 136</td><td> 120</td>
<td>CB-9</td><td> 168</td><td> 53</td>
RO 121129 Β1
Smoke black has been combined with either water or a solution of sorbitan monooleate with 20 moles of ethylene oxide in a continuous pelletizer operating at a rotor speed of 1000 rpm to obtain wet pellets. The pellets were dried in an air circulation oven at 120 ° C, obtaining pellets with a moisture content below 0.4%. The 11 different compositions were obtained as below:
<td>Composition</td><td>Carbon black</td><td>Binder</td>
<td>N</td><td>CB-6</td><td>the water</td>
<td>A</td><td>CB-6</td><td>0.5% sorbitan monooleate with 20 moles ethylene oxide (group iv according to the invention)</td>
<td>P</td><td>CB-6</td><td>1.0% sorbitan monooleate with 20 moles ethylene oxide (group iv according to the invention)</td>
<td>Q</td><td>CB-6</td><td>2.0% sorbitan monooleate with 20 moles ethylene oxide (group iv according to the invention)</td>
<td>R</td><td>CB-6</td><td>4.0% sorbitan monooleate with 20 moles ethylene oxide (group iv according to the invention)</td>
<td>S</td><td>CB-7</td><td>the water</td>
<td>T</td><td>CB-7</td><td>2.0% sorbitan monooleate with 20 moles ethylene oxide (group iv according to the invention)</td>
<td>u</td><td>CB-8</td><td>the water</td>
<td>V</td><td>CB-8</td><td>2.0% sorbitan monooleate with 20 moles ethylene oxide (group iv according to the invention))</td>
<td>w</td><td>CB-9</td><td>the water</td>
<td>X</td><td>CB-9</td><td>2.0% sorbitan monooleate with 20 moles ethylene oxide (group iv according to the invention)</td>
Smoke black compositions were evaluated in terms of pellet resistance and wear resistance using the procedures described. The results are presented in table 5.
Table 5
<td>Composition</td><td>Pellet resistance kilograms</td><td colspan="2">Dust (%)</td>
<td></td><td></td><td> 5'</td><td> 10'</td>
<td>N</td><td>11.34 (25 Ibs.)</td><td> 4.4</td><td> 5.0</td>
<td> 0</td><td>27.66 (61 Ibs.)</td><td> 0.5</td><td> 1.1</td>
<td>P</td><td>22.22 (49 Ibs.)</td><td> 0.6</td><td> 1.5</td>
<td>Q</td><td>24.94 (55 Ibs.)</td><td> 0.2</td><td> 0.4</td>
<td>R</td><td>22.67 (50 Ibs.)</td><td> 0.8</td><td> 0.6</td>
<td>S</td><td>19.95 (44 Ibs)</td><td> 3.6</td><td> 15.0</td>
<td>T</td><td>37.64 (83 Ibs.)</td><td> 0,3</td><td> 1,5</td>
<td>u</td><td>28.11 (62 Ibs.)</td><td> 0,8</td><td> 5,2</td>
<td>V</td><td>53.97 (119 Ibs.)</td><td> 0,2</td><td> 0,4</td>
<td>w</td><td>7.71 (17 Ibs.)</td><td> 2,5</td><td> 4,8</td>
<td>X</td><td>9.52 (21 Ibs.)</td><td> 1.2</td><td> 2.4</td>
RO 121129 Β1
Each of the carbon black compositions were identically compounded in low density polyethylene having a melt index of 26 using a Brabender mixer to obtain a premix with a carbon black content of 40%.
The viscosity of the premix was measured at 130 ° C and at a shear rate of 50 s'<sup>1</sup>. The results are presented in table 6.
Table 6
<td>Composition</td><td>Viscosity (Pa.s)</td>
<td>N</td><td> 5116</td>
<td>A</td><td> 4045</td>
<td>P</td><td> 3389</td>
<td>Q</td><td> 2873</td>
<td>R</td><td> 2536</td>
<td>S</td><td> 4329</td>
<td>T</td><td> 3695</td>
<td>u</td><td> 4591</td>
<td>V</td><td> 3804</td>
<td>w</td><td> 5487</td>
<td>X</td><td> 4373</td>
The data in Table 6 illustrate the reduction of viscosity obtained by using a carbon black treated with a binder composition according to the invention. This reduction in viscosity facilitates the dispersion of the polyethylene premix in a film obtained by blow extrusion or extruded profile and also improves the yield. It is expected that the improvement of the dispersion of the carbon black will also produce an improvement in the efficiency of pigmentation, UV protection and mechanical performance (eg tensile or impact resistance).
Examples 38-49. These examples illustrate the use of different binder compositions to obtain carbon black compositions according to the invention, and the advantages of using carbon black compositions in ethylene vinyl acetate (EVA) applications.
11 compositions of HH, II, JJ, KK, LL, MM, NN, 00, PP, QQ and RR black smoke compositions were obtained by combining 400 g of fluffy black with a DBP value of 128 cm.<sup>3</sup>/ 100 g and a specific nitrogen area of 68 m<sup>2</sup>/ g, called CB-12, together with 8 g of binder dissolved in 500 g of water, in a needle pelletizer. The binder compositions used were the following:
<td>Composition</td><td>Binder</td>
<td>HH</td><td>the water</td>
<td>II</td><td>sucrose monoester of fatty acid from fat (group iii)</td>
<td>JJ</td><td>sucrose monostearate (group iii)</td>
<td>KK</td><td>sucrose distearate</td>
<td>LL</td><td>ethoxylated glyceride (group i)</td>
<td>MM</td><td>ethoxylated triglyceride (group i)</td>
<td>NN</td><td>SYNPERONIC PE / L61 surface agent (group v)</td>
RO 121129 Β1
Table (continued)
<td>Composition</td><td>Binder</td>
<td>OO</td><td>SYNPERONIC PE / 85 surface agent (group v)</td>
<td>PP</td><td>SYNPERONIC PE / F127E surface agent (group v)</td>
<td>QQ</td><td>SYNPERONIC PE / 38E surface agent (group v)</td>
<td>RR</td><td>SYNPERONIC PE / 108E surface agent (group v)</td>
'Synperonic is a commercial name for surface agents produced and marketed by ICI Chemicals & Polymers and comprises ethylene oxide-propylene oxide copolymers. Synperonic PE surface agents are described in Surfactants Europe, ED.2 (GLHollis publisher and published by Tergo Data, Darlington.UK, ISBN 0 95505473 IX) as polyethylene oxide-polypropylene oxide-polyethylene oxide copolymers.
The mixture was stirred at 800 rpm for 2 min to obtain black pelletized smoke. Black smoke pellets were dried at 125 ° C to a moisture content below 1%.
The resistance of the pellets in the composition of black smoke was determined according to the described procedure. The results are presented in table 7.
Each smoke black composition was combined with an ethylene-vinyl acetate copolymer containing 40% vinyl acetate and a melt index 3, in a Brabender mixer at 65 ° C. The compound was stirred for 6 min at 50 rpm to obtain a fully dispersed compound containing 40% carbon black. These compounds were evaluated in terms of melt index (Ml) at 190 ° C using a load of 21.6 kg, according to the described procedure. The results are presented in Table 9, which also indicates the HLB for each binder.
Table 7
<td>Comp.</td><td>Binder</td><td>HLB</td><td>MPS (kg)</td><td>ml (G / 10m)</td><td>Avail. Diluted samples</td>
<td>HH</td><td>The water</td><td></td><td>0.72 (1.6 1b)</td><td> 6,58</td><td>2C</td>
<td>II</td><td>Animal fatty acid sucrose monoester</td><td> 14,5</td><td>6.89 (15.2 1b)</td><td> 9,86</td><td>1C</td>
<td>JJ</td><td>Sucrose monoester</td><td> 15,0</td><td>7.16 (15.81b)</td><td> 6,88</td><td>1B</td>
<td>KK</td><td>Sucrose distearate</td><td> 12,0</td><td>10.34 (22.81b)</td><td> 9,18</td><td>1B</td>
<td>LL</td><td>Ethoxylated glyceride</td><td> 15,7</td><td>2.22 (4.9 1b)</td><td> 8,84</td><td>1C</td>
RO 121129 Β1
Table 7 (continued) 1
<td>Comp.</td><td>Binder</td><td>HLB</td><td>MPS (kg)</td><td>Ml (G / 10m)</td><td>Avail. Diluted samples</td>
<td>MM</td><td>Ethoxylated triglyceride</td><td> 14,4</td><td>3.04 (6.7 1b)</td><td> 14,00</td><td>1D</td>
<td>NN</td><td>Synperonic PE / L61 surface agent</td><td> 16,0</td><td>4.26 (9.4 1b)</td><td> 10,34</td><td>1B</td>
<td>OO</td><td>Surface agent Synperonic PE / 85</td><td> 16,0</td><td>1.31 (2.9 1b)</td><td> 10,55</td><td>1C</td>
<td>PP</td><td>Synperonic PE / F127E Surface Agent</td><td> 22,0</td><td>1.18 (2.61b)</td><td> 6,70</td><td>1E</td>
<td>QQ</td><td>Surface agent Synperonic PE / 38E</td><td> 30,5</td><td>1.40 (3.1 1b)</td><td> 7,90</td><td>1B</td>
<td>RR</td><td>Surface agent Synperonic PE / 108E</td><td> 27,0</td><td>1.59 (3.5 1b)</td><td> 7,97</td><td>1E</td>
Comp. = Composition; Avail. diluted samples = dispersion of diluted samples.
Comp. = Composition; Avail. diluted samples = dispersion of diluted samples.
These examples illustrate improving the dispersion quality and reducing the viscosity with improving the handling properties of the pellets in commercial systems. These 21 results refer to shorter mixing cycles and improved extrusion characteristics. 2. 3
Examples 50 - 52. These examples illustrate obtaining the carbon black compositions according to the invention and the advantages of using the carbon black compositions according to the invention 25 in ethylene vinyl acetate (EVA) applications.
Three compositions of smoke black, SS, TT and UU were obtained by combining fluffy black 27 with a specific surface area of 70 m nitrogen.<sup>2</sup>/ g and a DBP value of 140 cm <sup>3</sup>/ 100 g black smoke, called CB-13, with a binder solution containing sorbitan monooleate in a 29 pelletizer with continuous needles operating at 1050 rpm for wet pellets. The resulting pellets containing either 0%, 2% or 4% binder were dried in a heated rotary drum 31 to obtain dry pellets with a moisture content below 0.6%. The percentage of binder used in each composition was as follows: 33
<td>Composition</td><td>Binder (% by weight)</td>
<td>SS</td><td>0.0% sorbitan monooleate (water)</td>
<td>TT</td><td>2% sorbitan monooleate (group i according to the invention)</td>
<td>UU</td><td>2% sorbitan monooleate (group i according to the invention)</td>
The treated carbon black was compounded into different polymers using a Brabender mixer at 50 rpm and with an initial room temperature of 85 ° C. The composites were evaluated from the point of view of the melt viscosity at 130'C and at a shear rate of 50 s'.<sup>1</sup>. 43
RO 121129 Β1
<td>Polymeric</td><td colspan="3">Viscosity (Pa.s) Percentage of binder</td>
<td></td><td> 0</td><td> 2</td><td> 4</td>
<td>ethylene-vinyl acetate (40% vinyl acetate, Ml 3.0)</td><td> 8155</td><td> 3210</td><td> 3080</td>
<td>ethylene-vinyl acetate (18% vinyl acetate, 2.5 ml)</td><td> 7368</td><td> 3564</td><td> 3498</td>
<td>ethylene ethyl acrylate (18% ethyl acrylate, Ml 6.0)</td><td> 7018</td><td> 3170</td><td> 2558</td>
The data indicate a significant reduction of the viscosity of the melt using said binder, which is reflected in a reduction of the pressure at the head of the die in the cable manufacturing process. Visually this fact is observed in improving the quality of the extrudate and in increasing the productivity.
The polymers used are classic types of polymers used in formulations in the field of conductive and semiconductor materials. Polymers with either 18% vinyl acetate or ethyl acrylate content are typically used for applications to bonded conductors or semiconductors, while polymer with 40% vinyl acetate content is more suitable for a semiconductor product. which can be disassociated.
It is obvious that the examples presented are intended only to illustrate the present invention and not to limit it.
52 members in 28 offices
Priority claims8
| Document | Office | Kind | Date |
|---|---|---|---|
| 37070995 | United States of America | A | |
| 37070995 | United States of America | A | |
| 9600088 | United States of America | W | |
| 9600088 | United States of America | W | |
| 0837070995 | – | – | – |
| 199600088 | – | – | – |
| US19950370709 | – | – | – |
| WO1996US00088 | – | – | – |
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| FI972921A7 | Finland | A7 | |
| FI972921L | Finland | L | |
| CO4520146A1 | Colombia | A1 | |
| EP0802950A1 | European Patent Office (EPO) | A1 | |
| MX9705155A | Mexico | A | |
| PL321291A1 | Poland | A1 | |
| CO4560368A1 | Colombia | A1 | |
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| TW473522B | Taiwan Province of China | B | |
| EP0802950B1 | European Patent Office (EPO) | B1 | |
| AT224931T | Austria | T | |
| ATE224931T1 | Austria | T1 | |
| DE69623927D1 | Germany | D1 | |
| DE69623927T2 | Germany | T2 | |
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| CN1121459C | China | C | |
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Numbers
- Publication, DOCDB
- 121129
- Publication, EPODOC
- RO121129
- Application
- 9701285
- Application, DOCDB
- 9701285
- Application, EPODOC
- RO19970001285
Titles2
- English
- CARBON BLACK COMPOSITION AND POLYMER COMPOSITIONS COMPRISING THE SAME
- Romanian
- COMPOZIŢIE DE NEGRU DE FUM ŞI COMPOZIŢII DE POLIMER CARE O CONŢIN
Classification
- CPC, 9
- H01B1/24
- C09C1/48
- C08K3/04
- C08K5/103
- C09C1/56
- C09C1/58
- C01P2006/12
- C01P2006/22
- Y10T428/30
- IPC, 13
- C08J3 22
- C09C1 58
- C08K3 04
- C08K5 103
- C08K9 08
- C08K13 02
- C08L23 00
- C08L71 00
- C08L87 00
- C09C1 48
- C09C1 56
- C09D11 00
- H01B1 24