Controlling the rheology of a metal ore residue
US-12122884-B2 · Oct 22, 2024 · US
US2016200879A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016200879-A1 |
| Application number | US-201514595634-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jan 13, 2015 |
| Priority date | Jan 13, 2015 |
| Publication date | Jul 14, 2016 |
| Grant date | — |
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A solvent-free emulsification process for making a latex where a high viscosity resin is prepared under pressure is described.
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1 . A process of solvent free emulsion comprising: a) heating at least one high viscosity resin to a temperature of about 90° C. or higher to form a heated resin in a reaction vessel comprising a mixing device; wherein the high viscosity resin comprises a resin having a melt viscosity of from about 10 to about 1,000,000 Pa*S at about 130° C.; b) combining the heated resin with a surfactant and a neutralization agent in the absence of an organic solvent to form a mixture in said reaction vessel; c) increasing pressure in said vessel to from about 10 to about 1000 kPa; d) adding water to said mixture to form an emulsion under agitation; and e) reducing pressure in said vessel to obtain a solvent-free emulsion comprising resin particles. 2 . The process of claim 1 , wherein the surfactant is present in an amount from about 1% to about 10% by weight of dry resin. 3 . The process of claim 1 , wherein the neutralization agent is present in an amount from about 1% to about 15% by weight of dry resin. 4 . The process of claim 1 , wherein amount of neutralization agent is adjusted based on acid value of the resin to obtain resin particles of a desired size. 5 . The process of claim 1 , wherein the resin particles comprises an average size of about 50 nm to about 900 nm. 6 . The process of claim 1 , wherein the high viscosity resin comprises a molecular weight of at least about 5,000. 7 . The process of claim 1 , wherein the high viscosity resin comprises a melt viscosity of from about 30 to about 500,000 Pa*S at about 130° C. 8 . The process according to claim 1 , wherein the neutralization agent comprises an inorganic basic agent or an organic basic agent. 9 . The process of claim 1 , wherein the neutralization agent comprises an organoamine, a monocyclic compound comprising at least one nitrogen atom, a polycyclic compound comprising at least one nitrogen atom or a secondary amine. 10 . The process of claim 1 , wherein the neutralization agent comprises ammonium hydroxide, potassium hydroxide, sodium hydroxide, sodium carbonate, sodium bicarbonate, lithium hydroxide, potassium carbonate or triethyl amine. 11 . The process of claim 1 , wherein said neutralization agent comprises an aziridine, an azetidine, a piperazine, a piperidine, a pyridine, a bipyridine, a terpyridine, a dihydropyridine, a morpholine, an N-alkylmorpholine, a 1,4-diazabicyclo[2.2.2]octane, a 1,8-diazabicycloundecane, a 1,8-diazabicycloundecene, a dimethylated pentylamine, a trimethylated pentylamine, a pyrrole, a pyrrolidine, a pyrrolidinone, an indole, an indoline, an indanone, a benzindazone, an imidazole, a benzimidazole, an imidazolone, an imidazoline, an oxazole, an isoxazole, an oxazoline, an oxadiazole, a thiadiazole, a carbazole, a quinoline, an isoquinoline, a naphthyridine, a triazine, a triazole, a tetrazole, a pyrazole, a pyrazoline or a combination thereof. 12 . The process of claim 1 , wherein the surfactant is selected from the group consisting of anionic surfactants, nonionic surfactants, cationic surfactants and combinations thereof. 13 . The process of claim 1 , wherein the high viscosity resin comprises a softening point of at least about 120° C. 14 . The process of claim 1 , wherein the high viscosity resin comprises a polyester resin. 15 . A process of solvent free emulsion comprising: a) heating at least one high viscosity polyester resin comprising a softening point of at least about 115° C. to a temperature of about 110° C. to about 120° C. to form a heated resin in a reaction vessel comprising a mixing device; wherein the high viscosity resin comprises a resin having a melt viscosity of from about 10 to about 1,000,000 Pa*S at about 130° C.; b) combining the heated resin with a surfactant and a neutralization agent in the absence of an organic solvent to form a mixture in said reaction vessel; c) increasing pressure in said vessel above 1 atmosphere; d) adding water to said mixture to form an emulsion; and e) reducing pressure in said vessel to obtain a solvent-free emulsion comprising resin particles. 16 . The process of claim 15 , wherein the neutralization agent is present in an amount from about 1% to about 15% by weight of dry resin. 17 . The process of claim 15 , wherein amount of neutralization agent is adjusted based on acid value of the resin to obtain resin particles of a desired size. 18 . The process of claim 15 , wherein the resin particles comprise an average size of about 50 nm to about 900 nm. 19 . The process of claim 15 , wherein the high viscosity resin comprises a molecular weight of at least about 5,000. 20 . The process of claim 12 , wherein the high viscosity resin comprises a melt viscosity of from about 30 to about 500,000 Pa*S at about 130° C.
Polyesters · CPC title
Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers · CPC title
from solid polymers · CPC title
whereby the components are brought together in a liquid dispersing medium · CPC title
from polymer solutions · CPC title
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