CHEMICAL SYNTHESIS OF HYBRID INORGANIC-ORGANIC NANOSTRUCTURED CORROSION INHIBITIVE PIGMENTS AND METHODS
20190300790 ยท 2019-10-03
Assignee
Inventors
Cpc classification
C09C3/10
CHEMISTRY; METALLURGY
C09C1/00
CHEMISTRY; METALLURGY
International classification
C09C1/00
CHEMISTRY; METALLURGY
C09C3/10
CHEMISTRY; METALLURGY
Abstract
A method for preparing a hybrid inorganic-organic nanostructured inhibitive pigment, includes premixing a first stock solution containing one or more cations and a second stock solution containing one or more oxoanions to form a premixture under pH control in the presence of polymers as surface modifiers. The premixture is then reacted to form a slurry. The slurry is then quenched to separate nanoparticles from the slurry, followed by surface functionalization in organic inhibitors.
Claims
1-14. (canceled)
15. A hybrid inorganic-organic nanostructured inhibitive pigment, comprising: two or more corrosion inhibitive species in an inorganic core, organic shell nanoparticle from a metal-ion-ligand/complex-polymer based precursor solution.
16. The hybrid inorganic-organic nanostructured inhibitive pigment as recited in claim 15, wherein the metal ions complexed with a chelating agent.
17. The hybrid inorganic-organic nanostructured inhibitive pigment as recited in claim 16, wherein the chelating agent include an organic amines.
18. The hybrid inorganic-organic nanostructured inhibitive pigment as recited in claim 17, wherein the organic amines include diethanolamine (DEA).
19. The hybrid inorganic-organic nanostructured inhibitive pigment as recited in claim 17, wherein the organic amines include triethanolanine (TEA).
20. The hybrid inorganic-organic nanostructured inhibitive pigment as recited in claim 15, wherein the chelating agent includes an organic acid.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0026] Various features will become apparent to those skilled in the art from the following detailed description of the disclosed non-limiting embodiment. The drawings that accompany the detailed description can be briefly described as follows:
[0027]
[0028]
DETAILED DESCRIPTION
[0029]
[0030] Initially, at least a first stock solution 20, such as, for example only, zinc (Zn.sup.2+) citric complex solution (1:1), cerium (Ce.sup.3+) EDTA complex solution (1:1), or praseodymium (P.sup.3+) tartaric complex solution (1:1) is premixed with a second stock solution 30, as an example, such as molybdate (MoO.sub.4.sup.2), phosphate (PO.sub.4.sup.3), silicate (SiO.sub.3.sup.), added with 1-2 w % polymers, such as polyacrylic acid (PAA) and Polyvinyl alcohol (PVA). The precursor solutions include the desired metal ions complexed with a chelating agent, and metal-oxide anions dispersed in polymer/surfactants (surface modifiers). The chelating agents include organic amines such as diethanolamine (DEA), and triethanolanine (TEA), as well as organic acids such as citric/oxalic/tartaric acid, etc. That is, two or more corrosion inhibitive species (i.e. Ce.sup.3+, Pr.sup.3+, Zn.sup.2+,VO.sub.3.sup., MoO.sub.4.sup.2, PO.sub.4.sup.3, SiO.sub.3.sup. and organic molecules, etc.) are incorporated in the form of the inorganic (core)-organic (shell) nanoparticles as inhibitive pigments, prepared from metal-ion-ligand/complex-polymer based precursor solutions.
[0031] The first stock solution 20 and the second stock solution 30 are, for example, communicated through respective high pressure pumps, 22, 32 to premix at a controlled pH 40. In this disclosed non-limiting embodiment, the flow rate is about 10-15 ml/min flow at 20 C. such that the pre-mixture is at 20 C., 25-50 MPa with the pH controlled to about 8-10 pH.
[0032] The premixed solution is then reacted in a heated and pressurized reactor 50. In this disclosed non-limiting embodiment, the premixed solution is heated and pressurized with distilled water 52 at about 300 C.-400 C., 25-50 MPa to generate a hydrothermal process at a supercritical condition. The distilled water 52 is communicated through a high pressure pump 60 which, in this disclosed non-limiting embodiment, is at about 300 C.-400 C. at a flow rate of about, 50-70 ml/min.
[0033] The reacted premixed solution produces a reaction product slurry 70 that is quenched and cooled by the distilled water 52. In this disclosed non-limiting embodiment, the distilled water is supplied at about 20 C., 25-50 MPa.
[0034] The nanoparticles are then separated by a membrane filter, washed with distilled water, then dispersed in organic inhibitors for surface functionalization to provide the hybrid inorganic-organic nanostructured inhibitive pigment 100 (
[0035] The chemical nature of the polymer/surfactant modified inorganic precursor core 108 with the organic porous polymer shell 110 (
[0036] Example organic inhibitor additives include, but are not limited to: 4,5-Diamino-2,6-dimercaptopyrimidine (C.sub.4H.sub.6N.sub.4S.sub.2); 4,5-Diaminopyrimidine (C.sub.4H.sub.6N.sub.4); Sodium diethyldithiocarbamate ((C.sub.2H.sub.5).sub.2NCSSNa); 2-Mercaptopyridine (CsHsNS); Thiophenol (C.sub.6H.sub.5SH); 4-mercaptobenzoate (C.sub.7H.sub.5O.sub.2S); 2-mercaptobenzoate (C.sub.7H.sub.5O.sub.2S); 6-Mercaptonicotinate (C.sub.6H.sub.5NO.sub.2S); 2-Mercaptonicotinate (C.sub.6H.sub.5NO.sub.2S); 2-mercaptosuccinate (C.sub.4H.sub.4O.sub.4S); mercaptoacetate (C.sub.2H.sub.3O.sub.2S); Sodium-mercaptopropionate (C.sub.3H.sub.5NaO.sub.2S).
[0037] Example polymers/surfactants include: acetylacetone polyacrylamide (PAM); phosphonate-polyethlene glycol (PEG); and polyacrylic acid (PAA), propylamine phosphonate-polyethlene glycol (PEG); sulfonated acylate copolymer; polyvinyl pyrrolidone (PVP); and hydroxypropylcellulose (HPC).
[0038] The hydrothermal process 10 provides one approach to synthesize a hybrid inorganic-organic nanostructured inhibitive pigments, having multiple corrosion protection modes for use as a chromate replacement. The nano-sized pigments reduce costs and improve coating performance as one challenge in applying nano-sized particles as pigments is the strong aggregation during their synthesis process commonly observed in nanoparticles that have been produced from the liquid phase. This agglomeration is, readily resolved by use of the disclosed in-situ surface modification technique during the pigment synthesis process.
[0039] Although particular step sequences are shown, described, and claimed, it should be understood that steps may be performed in any order, separated or combined unless otherwise indicated and will still benefit from the present disclosure.
[0040] The foregoing description is exemplary rather than defined by the limitations within. Various non-limiting embodiments are disclosed herein, however, one of ordinary skill in the art would recognize that various modifications and variations in light of the above teachings will fall within the scope of the appended claims. It is therefore to be understood that within the scope of the appended claims, the disclosure may be practiced other than as specifically described. For that reason the appended claims should be studied to determine true scope and content.