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CN118420136A - Preparation method of compound phosphorus-free environment-friendly scale inhibitor - Google Patents

Preparation method of compound phosphorus-free environment-friendly scale inhibitor Download PDF

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Publication number
CN118420136A
CN118420136A CN202410882144.8A CN202410882144A CN118420136A CN 118420136 A CN118420136 A CN 118420136A CN 202410882144 A CN202410882144 A CN 202410882144A CN 118420136 A CN118420136 A CN 118420136A
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scale inhibitor
preparation
polycarboxylic
stirring
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CN118420136B (en
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洒盼盼
马信
赵文彬
王文雅
胡蕾
张兰云
雷明凯
邵强
陈杰
王超
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Shandong Shangyuan Environmental Protection Technology Co ltd
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F251/00Macromolecular compounds obtained by polymerising monomers on to polysaccharides or derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F5/00Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
    • C02F5/08Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
    • C02F5/10Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/52Amides or imides
    • C08F220/54Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide
    • C08F220/58Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide containing oxygen in addition to the carbonamido oxygen, e.g. N-methylolacrylamide, N-(meth)acryloylmorpholine
    • C08F220/585Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide containing oxygen in addition to the carbonamido oxygen, e.g. N-methylolacrylamide, N-(meth)acryloylmorpholine and containing other heteroatoms, e.g. 2-acrylamido-2-methylpropane sulfonic acid [AMPS]

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Polymers & Plastics (AREA)
  • Medicinal Chemistry (AREA)
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  • Life Sciences & Earth Sciences (AREA)
  • Water Supply & Treatment (AREA)
  • Environmental & Geological Engineering (AREA)
  • Engineering & Computer Science (AREA)
  • Hydrology & Water Resources (AREA)
  • General Chemical & Material Sciences (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)

Abstract

The invention belongs to the field of environmental protection water treatment, and relates to a preparation method of a compound phosphorus-free environment-friendly scale inhibitor, in particular to a preparation method of a modified starch polymer and a polycarboxylic sulfonic acid copolymer, wherein the finally obtained scale inhibitor comprises a hydroxyethyl starch and polycarboxylic sulfonic acid copolymer, and the existence of sulfonic groups in the copolymer can ensure that the scale inhibitor has better water solubility and prevent gelation of the scale inhibitor. The finally obtained compound phosphorus-free environment-friendly scale inhibitor can obviously play the synergistic effect of two polymers, improve the efficiency of the scale inhibitor, reduce the use amount of the scale inhibitor and reduce the scale inhibition cost of enterprises.

Description

Preparation method of compound phosphorus-free environment-friendly scale inhibitor
Technical Field
The invention belongs to the field of environmental protection water treatment, and relates to a preparation method of a compound phosphorus-free environment-friendly scale inhibitor containing hydroxyethyl starch and a polycarboxylic sulfonic acid copolymer, wherein the scale inhibitor is a phosphorus-free high polymer copolymer and belongs to the environment-friendly scale inhibitor.
Background
With the rapid development of the industry in China, the use amount of industrial cooling water is greatly increased. The biggest problem faced in the use of cooling water is scale deposition. Along with the continuous flow of water in the cooling circulation system, calcium, magnesium and iron plasma in the water gradually deposit on the inner wall of the cooling circulation system equipment, so that scale is formed, the cooling efficiency is reduced, the equipment is corroded, and the consumption of the cooling water is greatly increased. Therefore, the scale inhibitor is added into the circulating water system, so that ion deposition can be effectively prevented, and equipment corrosion and cooling efficiency reduction are avoided.
Conventional scale inhibitors generally contain a large amount of phosphate, and although the scale inhibitor has very high scale inhibition efficiency, the large amount of phosphate ions can cause eutrophication of water, so that algae microorganisms in water are excessively propagated, and ecological balance is seriously damaged. In order to solve the above problems, the art has also developed organic polyacrylic acid and polymaleic acid scale inhibitors, which do not contain nitrogen and phosphorus elements, do not cause eutrophication of water, and a large amount of carboxyl groups can be chelated with metal ions such as calcium, magnesium, iron and the like to damage the lattice structure of the surface of the scale, so that the scale on the inner wall of a pipeline can be removed. However, the scale inhibition efficiency is limited due to the single function of the carboxylic acid group, and a large amount of carboxylic acid groups are easy to form gel with metal ions, so that the scale inhibition effect is reduced. In addition, compared with inorganic phosphate scale inhibitors, the organic scale inhibitors have lower efficiency and high production cost, and bring great economic burden to enterprises.
Therefore, aiming at the problems faced by the existing polyacrylic acid and polymaleic acid scale inhibitors, the development of a novel high-molecular polymer scale inhibitor is urgently needed, the efficiency of the scale inhibitor is improved, the use amount of the scale inhibitor is reduced, and the scale inhibition cost of enterprises is reduced.
Disclosure of Invention
In order to solve the problems, the invention provides a preparation method of a compound phosphorus-free environment-friendly scale inhibitor, which is characterized in that a modified starch polymer and a polycarboxylic sulfonic acid copolymer are compounded, and the finally obtained scale inhibitor comprises a copolymer of hydroxyethyl starch and polycarboxylic sulfonic acid, wherein the existence of sulfonic groups in the copolymer can ensure that the scale inhibitor has better water solubility and prevent gelation of the scale inhibitor. The finally obtained compound phosphorus-free environment-friendly scale inhibitor can obviously play the synergistic effect of two polymers, improve the efficiency of the scale inhibitor, reduce the use amount of the scale inhibitor and reduce the scale inhibition cost of enterprises.
The invention aims to achieve the aim, and the aim is achieved by the following technical scheme:
the preparation method of the compound phosphorus-free environment-friendly scale inhibitor comprises the following specific preparation steps of hydroxyethyl starch and a polycarboxylic sulfonic acid copolymer: wherein the weight parts of the components are as follows,
(1) Preparation of hydroxyethyl starch derivatives containing propenyl groups:
Adding 10-20 parts of hydroxyethyl starch into 50-200 parts of solvent, stirring for 10-30 minutes at 10-40 ℃, then adding 4-7 parts of acrylic acid and 11-19 parts of condensing agent, maintaining the temperature of the mixed solution at 10-40 ℃, adding 0.1-0.5 part of 4-dimethylaminopyridine, and continuously stirring for 4-10 hours; then the reaction solution is poured into 500-2000 parts of methanol, stirred for 20-40 minutes, filtered, and the solid is respectively washed three times by 50-80 parts of methanol, and dried to obtain the hydroxyethyl starch derivative containing propenyl.
(2) Preparation of modified starch polymer:
Adding the hydroxyethyl starch derivative containing the propenyl, 18-26 parts of acrylic acid and 5-8 parts of maleic anhydride prepared in the step (1) into 100-150 parts of deionized water, introducing argon for 10-30 minutes under the stirring condition, then adding 0.3-0.7 part of potassium peroxodisulfate, heating to 70-90 ℃, and stirring for 2-4 hours; cooling to 10-30 ℃, pouring the reaction liquid into 800-2000 parts of methanol, filtering, washing the solid with 100-150 parts of methanol for three times respectively, and drying to obtain a modified starch polymer;
In the step, the structure of hydroxyethyl starch is modified by acrylic acid, and the obtained acrylic acid modified starch is copolymerized with acrylic acid and maleic anhydride to obtain a modified starch polymer, wherein the polymer contains a large number of hydroxyethyl glucose structural units and a large number of oxygen atoms and can coordinate with a plurality of metal ions to form chelate, so that various metal ions can be effectively removed. The polymer is a hyperbranched polymer, can form a hyperbranched network structure, has a more stable structure after metal ions are chelated with the polymer, and can remarkably improve the efficiency and the capability of removing the metal ions of the scale inhibitor.
(3) Preparation of a polycarboxylic sulfonic acid copolymer:
Adding 16-19 parts of 2-acrylamide-2-methylpropanesulfonic acid, 10-14 parts of acrylic acid and 12-16 parts of maleic anhydride into 130-180 parts of deionized water, introducing argon for 10-30 minutes under the stirring condition, adding 0.5-0.9 part of potassium persulfate, heating to 70-90 ℃, and stirring for 2-4 hours; cooling to 10-30 ℃, pouring the reaction solution into 1200-2200 parts of methanol, filtering, washing the solid with 150-200 parts of methanol for three times respectively, and drying to obtain the polycarboxylic sulfonic acid copolymer;
The polycarboxylic sulfonic acid copolymer of the 2-acrylamide-2-methylpropanesulfonic acid obtained in the step has a large amount of sulfonic acid groups, and the solubility of the sulfonic acid groups after being combined with metal ions is good; after being compounded with other components, the anti-scaling agent can improve the solubility of the anti-scaling agent, and meanwhile, the acrylic acid and the starch compounds can be prevented from being chelated with metal ions to form gel.
(4) Preparation of a compound environment-friendly phosphorus-free scale inhibitor containing hydroxyethyl starch and a polycarboxylic sulfonic acid copolymer:
And (3) directly blending the modified starch polymer prepared in the step (2) and the polycarboxylic acid copolymer prepared in the step (3) to obtain the compound phosphorus-free scale inhibitor containing hydroxyethyl starch and the polycarboxylic acid copolymer.
The modified starch polymer and the polycarboxylic sulfonic acid copolymer are blended, so that the production cost is low, the synergistic effect of the modified starch polymer and the polycarboxylic sulfonic acid copolymer can be remarkably exerted, the efficiency of the scale inhibitor is improved, the use amount of the scale inhibitor is reduced, and the scale inhibition cost of enterprises is reduced.
Preferably, in the preparation method, the following steps are adopted:
in the step (1), the solvent is dimethyl sulfoxide or N, N-dimethylformamide.
In the step (1), the condensing agent is 1- (3-dimethylaminopropyl) -3-ethylcarbodiimide hydrochloride or dicyclohexylcarbodiimide.
In the step (2), potassium persulfate is added in two batches, wherein 0.1-0.4 part of potassium persulfate is added in the first batch and 0.2-0.3 part of potassium persulfate is added in the second batch. The two batches are separated by at least 30 minutes, which prevents the presence of unreacted monomers in the system, resulting in an insufficient final degree of polymerization.
For the same reason, in the step (3), potassium persulfate is added in three batches, wherein the first batch is added with 0.2-0.3 part, the second batch is added with 0.2-0.3 part, and the third batch is added with 0.1-0.3 part. The batch interval is also 30 minutes or more.
Compared with the prior art, the invention has the following beneficial effects:
The modified starch polymer is prepared by modifying the structure of hydroxyethyl starch by acrylic acid, preparing hydroxyethyl starch derivative containing propenyl, and further copolymerizing acrylic acid and maleic anhydride, and contains a large number of hydroxyethyl glucose structural units and a large number of oxygen atoms, and has good chelation effect on a large number of metal ions. And after the acrylic acid reacts with the hydroxyethyl starch, the acrylic acid and the maleic anhydride are further copolymerized to generate a hyperbranched structure, and a large amount of metal ions can be filled in the hyperbranched network structure, so that the efficiency and the capability of removing the metal ions of the scale inhibitor can be obviously improved.
The invention also prepares the polycarboxylic sulfonic acid copolymer containing 2-acrylamide-2-methylpropanesulfonic acid, and the existence of sulfonic acid groups can ensure that the scale inhibitor has better water solubility and prevent the scale inhibitor from gelation. According to the invention, the modified starch polymer and the polycarboxylic sulfonic acid copolymer are compounded, so that the synergistic effect of the two polymers can be remarkably exerted, the efficiency of the scale inhibitor is improved, the use amount of the scale inhibitor is reduced, and the scale inhibition cost of enterprises is reduced.
Detailed Description
The invention will be further explained below with reference to specific embodiments, which are only suitable for a further, completely clear explanation of the invention, the described embodiments being only some, but not all, of the embodiments of the invention. All other embodiments created based on this invention are within the scope of this invention. The following examples and experimental examples are all conventional techniques using instruments, reagents, etc.
Example 1: the preparation method of the compound phosphorus-free environment-friendly scale inhibitor comprises the following specific preparation steps: wherein the weight parts of the components are as follows,
(1) Preparation of hydroxyethyl starch derivatives containing propenyl groups:
Adding 10 parts of hydroxyethyl starch into 50 parts of dimethyl sulfoxide, stirring for 10 minutes, adding 4 parts of acrylic acid and 11 parts of 1- (3-dimethylaminopropyl) -3-ethylcarbodiimide hydrochloride, maintaining the temperature of the mixed solution at 10 ℃, adding 0.1 part of 4-dimethylaminopyridine, continuously stirring for 4 hours, pouring the reaction solution into 500 parts of methanol, stirring for 20 minutes, filtering, washing the solid with 50 parts of methanol for three times, and drying to obtain the hydroxyethyl starch derivative containing propenyl;
(2) Preparation of modified starch polymer:
Adding the hydroxyethyl starch derivative containing the propenyl, 18 parts of acrylic acid and 5 parts of maleic anhydride prepared in the step (1) into 100 parts of deionized water, introducing argon for 10 minutes under the stirring condition, adding potassium peroxodisulfate in two batches, adding 0.1 part in the first batch and 0.2 part in the second batch, heating to 70 ℃ at intervals of 30 minutes, stirring for 2 hours, cooling to 10 ℃, pouring the reaction solution into 800 parts of methanol, filtering, washing the solid with 100 parts of methanol for three times, and drying to obtain a modified starch polymer;
(3) Preparation of a polycarboxylic sulfonic acid copolymer:
adding 16 parts of 2-acrylamide-2-methylpropanesulfonic acid, 10 parts of acrylic acid and 12 parts of maleic anhydride into 130 parts of deionized water, introducing argon for 10 minutes under the stirring condition, adding potassium peroxodisulfate in three batches, adding 0.2 part in the first batch, 0.2 part in the second batch, 0.1 part in the third batch, heating to 70 ℃ at intervals of 30 minutes, stirring for 2 hours, cooling to 10 ℃, pouring the reaction solution into 1200 parts of methanol, filtering, washing the solid with 150 parts of methanol for three times, and drying to obtain a polycarboxylic sulfonic acid copolymer;
(4) Preparation of a compound phosphorus-free scale inhibitor containing hydroxyethyl starch and a polycarboxylic sulfonic acid copolymer:
and (3) blending the modified starch polymer prepared in the step (2) and the polycarboxylic acid copolymer prepared in the step (3) to obtain the compound phosphorus-free scale inhibitor containing hydroxyethyl starch and the polycarboxylic acid copolymer.
Example 2: the preparation method of the compound phosphorus-free environment-friendly scale inhibitor comprises the following specific preparation steps: wherein the weight parts of the components are as follows,
(1) Preparation of hydroxyethyl starch derivatives containing propenyl groups:
Adding 20 parts of hydroxyethyl starch into 200 parts of N, N-dimethylformamide, stirring for 30 minutes, adding 7 parts of acrylic acid and 19 parts of dicyclohexylcarbodiimide, maintaining the temperature of the mixed solution at 40 ℃, adding 0.5 part of 4-dimethylaminopyridine, continuously stirring for 10 hours, pouring the reaction solution into 2000 parts of methanol, stirring for 40 minutes, filtering, washing the solid with 80 parts of methanol for three times, and drying to obtain a hydroxyethyl starch derivative containing propenyl;
(2) Preparation of modified starch polymer:
Adding the hydroxyethyl starch derivative containing the propenyl, 26 parts of acrylic acid and 8 parts of maleic anhydride prepared in the step (1) into 150 parts of deionized water, introducing argon for 30 minutes under the stirring condition, adding potassium peroxodisulfate in two batches, adding 0.4 part of potassium peroxodisulfate in the first batch, adding 0.3 part of potassium peroxodisulfate in the second batch, heating to 90 ℃ at intervals of 35 minutes, stirring for 4 hours, cooling to 30 ℃, pouring the reaction liquid into 2000 parts of methanol, filtering, washing the solid with 150 parts of methanol for three times, and drying to obtain a modified starch polymer;
(3) Preparation of a polycarboxylic sulfonic acid copolymer:
Adding 19 parts of 2-acrylamide-2-methylpropanesulfonic acid, 14 parts of acrylic acid and 16 parts of maleic anhydride into 180 parts of deionized water, introducing argon for 30 minutes under the stirring condition, adding potassium peroxodisulfate in three batches, adding 0.3 part in the first batch, adding 0.3 part in the second batch, adding 0.3 part in the third batch, heating to 90 ℃ at intervals of 35 minutes, stirring for 4 hours, cooling to 30 ℃, pouring the reaction solution into 2200 parts of methanol, filtering, washing the solid with 200 parts of methanol for three times, and drying to obtain a polycarboxylic sulfonic acid copolymer;
(4) Preparation of a compound phosphorus-free scale inhibitor containing hydroxyethyl starch and a polycarboxylic sulfonic acid copolymer:
and (3) blending the modified starch polymer prepared in the step (2) and the polycarboxylic acid copolymer prepared in the step (3) to obtain the compound phosphorus-free scale inhibitor containing hydroxyethyl starch and the polycarboxylic acid copolymer.
Example 3: the preparation method of the compound phosphorus-free environment-friendly scale inhibitor comprises the following specific preparation steps: wherein the weight parts of the components are as follows,
(1) Preparation of hydroxyethyl starch derivatives containing propenyl groups:
adding 16 parts of hydroxyethyl starch into 110 parts of dimethyl sulfoxide, stirring for 20 minutes, adding 5.4 parts of acrylic acid and 15 parts of dicyclohexylcarbodiimide, maintaining the temperature of the mixed solution at 25 ℃, adding 0.31 part of 4-dimethylaminopyridine, continuously stirring for 6 hours, pouring the reaction solution into 1200 parts of methanol, stirring for 30 minutes, filtering, washing the solid with 65 parts of methanol for three times, and drying to obtain the hydroxyethyl starch derivative containing propenyl;
(2) Preparation of modified starch polymer:
Adding the hydroxyethyl starch derivative containing the propenyl, 22 parts of acrylic acid and 6.4 parts of maleic anhydride prepared in the step (1) into 122 parts of deionized water, introducing argon for 20 minutes under the stirring condition, adding potassium persulfate in two batches, adding 0.25 part in the first batch and 0.25 part in the second batch, heating to 80 ℃ at intervals of 30 minutes, stirring for 3 hours, cooling to 20 ℃, pouring the reaction solution into 1200 parts of methanol, filtering, washing the solid with 130 parts of methanol for three times, and drying to obtain a modified starch polymer;
(3) Preparation of a polycarboxylic sulfonic acid copolymer:
Adding 17 parts of 2-acrylamide-2-methylpropanesulfonic acid, 12 parts of acrylic acid and 14 parts of maleic anhydride into 160 parts of deionized water, introducing argon for 20 minutes under the stirring condition, adding potassium peroxodisulfate in three batches, adding 0.25 part in the first batch, 0.25 part in the second batch, adding 0.15 part in the third batch, heating to 80 ℃ at intervals of 30 minutes, stirring for 3 hours, cooling to 20 ℃, pouring the reaction solution into 1700 parts of methanol, filtering, washing the solid with 170 parts of methanol for three times, and drying to obtain a polycarboxylic sulfonic acid copolymer;
(4) Preparation of a compound phosphorus-free scale inhibitor containing hydroxyethyl starch and a polycarboxylic sulfonic acid copolymer:
and (3) blending the modified starch polymer prepared in the step (2) and the polycarboxylic acid copolymer prepared in the step (3) to obtain the compound phosphorus-free scale inhibitor containing hydroxyethyl starch and the polycarboxylic acid copolymer.
Comparative example: the composite scale inhibitor was prepared according to the method described in example 2 in the method for producing the composite scale inhibitor of polyaspartic acid and polyacrylic acid under the patent name of application number CN 201410672769.8:
Adding 30 parts of maleic anhydride and 52 parts of ammonia water into a reaction kettle, starting stirring, adding 2 parts of a mixture of ferric oxide and nickel oxide when the temperature is raised to 55 ℃, stopping stirring uniformly, standing at a constant temperature for 1.1 hours, starting stirring, adding 6 parts of deionized water, stopping heating, reducing the reaction temperature to 25 ℃ under the stirring condition, adjusting the pH value of the reaction solution to 9-10 by using a 1M sodium hydroxide aqueous solution, adding 10 parts of polyacrylic acid, and stirring for 30 min to obtain the carboxylic acid scale inhibitor.
Experimental example 1: and (3) testing the scale inhibition performance of the calcium carbonate:
Preparing a sodium bicarbonate standard solution with the concentration of bicarbonate ions of 18.3 mg/mL, a calcium chloride standard solution with the concentration of calcium ions of 6.0 mg/mL, an EDTA standard solution with the concentration of 0.01 mol/L, a potassium hydroxide solution with the mass fraction of 200 g/L and a calcium-carboxylic acid indicator.
250ML of water was added to a 500 mL volumetric flask, a volume of calcium chloride standard solution was added with a burette, a quantity of the sample solutions of examples 1-3 and comparative example was added with a pipette, and shaking was performed. Then adding 20mL borax buffer solution, and shaking uniformly. Slowly adding a certain volume of sodium bicarbonate standard solution into a burette, shaking uniformly, dripping, diluting to scale with water, and shaking uniformly. And simultaneously, a blank experiment without adding a scale inhibitor is carried out.
The conical flask containing the blank and reagent solution was immersed in a constant temperature water bath at 80 c, the reagent solution level was not higher than the water bath level, the solution was placed at constant temperature for 10h, and the solution was filtered while hot with medium speed quantitative filter paper, after the filtrate was cooled, 25.0 filtrate mL was removed, placed in a 250mL conical flask, water was added to 80 mL, and 5mL potassium hydroxide solution and about 0.1g of calcium-carboxylic acid indicator were added. And titrating the solution from purple to bright blue by using an ethylenediamine tetraacetic acid disodium standard solution to obtain the final point. The mass concentration of the calcium ions in the test solution and the blank test solution are calculated according to the following formula.
The concentration of calcium ions in the aqueous solution, ρ, is expressed in mg/mL:
ρ=V1CM/V
Wherein:
the mass concentration of rho-calcium ions is mg/mL;
V 1 -the value of the volume of the disodium ethylenediamine tetraacetate standard solution consumed in titration is in mL;
accurate value of actual concentration of disodium C-ethylenediamine tetraacetate in mol/L, (c=0.01)
The molar mass of M-calcium ions is given in g/mol (M=40.08)
V-the value of the volume of the standard solution of calcium chloride taken, in mL, (V=25)
Scale inhibition performance of the water treatment agent is calculated by eta, and the numerical value is expressed as percent:
η=(ρ32)/(ρ12 )×100
Wherein:
ρ 3 -the numerical value of the mass concentration of calcium ions after the test of adding the water treatment agent into the test solution is mg/mL;
ρ 2 -the numerical value of the mass concentration of calcium ions after the blank test solution without the water treatment agent is tested, and the unit is mg/mL;
ρ 1 -the value of the mass concentration of calcium ions in water under actual working conditions or in formulated water, the unit is mg/mL.
TABLE 1 calculation results of scale inhibition ratio for calcium carbonate
As shown in the results of Table 1, the scale inhibitor of the invention in example 2 shows a good scale inhibition efficiency for calcium carbonate, the scale inhibition efficiency can reach 89.96% when the concentration of the scale inhibitor is 15 mg/mL, the scale inhibition efficiency can reach 94.85% when the concentration of the scale inhibitor is 20 mg/mL, the concentration of the scale inhibitor is continuously increased, the scale inhibition efficiency tends to be stable, and the use amount of the scale inhibitor can not be increased any more for controlling the cost. And the scale inhibition rate of the examples is obviously better than that of the comparative examples, and has very remarkable progress.
Experimental example 2: calcium sulfate scale inhibition performance test:
Preparing a sodium sulfate standard solution with sulfate ion concentration of 18.3 mg/mL, a calcium chloride standard solution with calcium ion concentration of 6.0 mg/mL, an EDTA standard solution with concentration of 0.01mol/L, a potassium hydroxide solution with mass fraction of 200 g/L and a calcium-carboxylic acid indicator.
250 ML of water was added to a 500 mL volumetric flask, a volume of a standard solution of calcium chloride was added with a burette, a quantity of the sample solutions of examples 1-3 and comparative example was added with a pipette, and shaking was performed. Slowly adding a certain volume of sodium sulfate standard solution by using a burette, shaking uniformly, dripping, diluting to a scale by using water, and shaking uniformly. And simultaneously, a blank experiment without adding a scale inhibitor is carried out.
Immersing the conical flask containing the blank and the reagent solution in a constant temperature water bath at 60 ℃, keeping the liquid level of the reagent solution not higher than the liquid level of the water bath, standing at a constant temperature for 6h, filtering with medium-speed quantitative filter paper while the reagent solution is hot, taking 25.0 of mL of the filtrate after the filtrate is cooled, placing the filtrate in a conical flask at 250 mL, adding water to 80mL, adding 5mL of potassium hydroxide solution and about 0.1 g of calcium-carboxylic acid indicator. And titrating the solution from purple to bright blue by using an ethylenediamine tetraacetic acid disodium standard solution to obtain the final point. The mass concentrations of the calcium ions in the test solution and the blank test solution were calculated respectively according to the formula in experimental example 1.
TABLE 2 calculation of the scale inhibition ratio of calcium sulfate
As shown in Table 2, the scale inhibitor of example 2 of the present invention also shows excellent scale inhibition efficiency for calcium sulfate, the scale inhibition efficiency can reach 98.89% when the concentration of the scale inhibitor is 5 mg/mL, and the scale inhibition efficiency reaches 100% when the concentration of the scale inhibitor is more than 10 mg/mL. And the scale inhibition rate of the examples is obviously better than that of the comparative examples, and has very remarkable progress.
Experimental example 3: static scale inhibition experiment and rotary hanging piece corrosion inhibition experiment for circulating water
Simulated circulating water was formulated to test the scale and corrosion inhibition rates of examples 1,2, 3 and comparative examples. Wherein, the pH of the solution=8.0, the total hardness is 500.0 mg/L, the alkalinity is 300.0 mg/L and the Cl - 1348.82 mg/L,SO4 2- 1143.2 mg/L.
Static scale inhibition was performed according to the scale inhibition test method for calcium carbonate in the above-described test example 1.
Corrosion inhibition experiment of water treatment agent: firstly, wiping 20# carbon steel with rust-proof grease by using filter paper, then wiping the carbon steel with absorbent cotton in absolute ethyl alcohol, after wiping the carbon steel clean, sucking the carbon steel dry by using the filter paper, placing the carbon steel in a dryer for 4h, weighing (accurate to 0.2 mg), and storing the carbon steel in the dryer for standby.
Preparing water: the calcium chloride dihydrate of 7.35 g, the magnesium sulfate heptahydrate of 4.93 g and the sodium chloride of 6.58 g are weighed and dissolved in the water of about 7L, and after complete dissolution, the mixture is uniformly mixed, and the sodium bicarbonate of 1.68 g is weighed and dissolved in the water of about 1L, and after complete dissolution, the mixture is uniformly mixed. Mixing the two solutions, diluting with water to 10L, and mixing. The standard prepared water has a calcium ion concentration of 200.4 mg/L, a magnesium ion concentration of 48.62 mg/L, a chloride ion concentration of 399.1 mg/L and a bicarbonate ion concentration of 122.0 mg/L.
Finally, 2000 mL beakers are taken, 2000 mL of the preparation water is added, a certain amount of sample solutions of examples 1-3 and comparative examples are added by a pipette, the dosing concentration is 20mg/L, a certain amount of sodium bicarbonate is added, the pH is adjusted to 8.3, the solution is placed in a 45 ℃ water bath for stabilizing 2h, a weighed carbon steel hanging piece is added, a test piece is taken out after 72 h, firstly, the hanging piece is washed by tap water, secondly, about 30s is washed in an acid washing solution (10% hydrochloric acid and 0.5% hexamethylenetetramine), and the test piece is taken out. The water was quickly rinsed with tap water. Immediately immersed in sodium hydroxide solution for about 30s, taken out, rinsed with pure water, wiped with filter paper and blotted dry. Soaking in absolute ethanol for about 3 min, placing on clean filter paper, drying with filter paper, placing in a dryer for more than 4h, and weighing.
The hanger erosion rate is calculated as v in mm/a, as follows:
v=8760×(m-m0)×10/spt
Wherein:
the m-hanging piece mass loss value is expressed as g;
m 0 -the value of the mass loss average value of the hanging piece pickling blank test, wherein the unit is g;
The surface area value of the s-hanging piece is cm 2;
The density value of the p-hanging piece is expressed in g/cm 3
T-time value of experiment, the unit is h;
8760-hours corresponding to one year in h/a;
10-a number of millimeters equivalent to 1 cm in mm/cm.
The inhibition rate of the hanging piece is calculated by eta, the numerical value is expressed as percent, and the hanging piece is calculated according to the following formula:
η=(v0-v1)/v0 ×100
Wherein:
v 0 -the number of corrosion rates in mm/a for the hanging blank test;
v 1 -the value of the corrosion rate of the coupon in mm/a.
TABLE 3 calcium carbonate scale inhibition and 20# carbon steel corrosion inhibition for examples 1, 2,3 and comparative example versus circulating water
As shown by the results in Table 3, under the condition that the dosing concentration is 20 mg/L in the examples 1,2, 3 and comparative example, the scale inhibitor of the application in the example 2 has the scale inhibition efficiency of 98.32% on circulating water and the corrosion inhibition rate of 97.95% on carbon steel, and the scale inhibition rate of the examples is obviously better than that of the comparative example, so that the application prospect of the technical scheme of the application is very wide.
Circulating water actual condition water experiment case 1: some coking group circulating water example
The scale inhibitor prepared in experimental examples 1,2 and 3 and comparative example is tested by taking circulating water of a certain coking group in actual operation, and the dosing concentration is 20 mg/L, and the scale inhibition rate and corrosion inhibition rate of the scale inhibitor are tested. Wherein, the pH=8.46, turbidity 33.77 NTU, total hardness 483.94 mg/L, alkalinity 277.00 mg/L, calcium hardness 300.24 mg/L, cl - 1348.82 mg/L,Fe2+ 0.95 mg/L, total phosphorus 32.73 mg/L, COD 138.16 mg/L and ammonia nitrogen 1.07 mg/L of the circulating water.
Static scale inhibition was performed according to the scale inhibition test method for calcium carbonate in the above-described test example 1.
Corrosion inhibition experiments of the water treatment agent were carried out according to the hanging piece corrosion inhibition experiment method in the experiment example 3.
TABLE 4 Scale inhibition and corrosion inhibition of examples 1, 2, 3 and comparative examples on certain coking group circulating waters
As shown in the results of Table 4, the scale inhibitor of the invention of example 2 has a scale inhibition efficiency of 96.57% for circulating water in actual operation of a coking group, a corrosion inhibition rate of 97.39% for carbon steel, and the scale inhibition efficiency and corrosion inhibition efficiency of the examples are significantly better than those of the comparative examples.
Circulating water actual condition water experiment case 2: some group circulating water example
The scale inhibitor prepared in experimental examples 1,2 and 3 and comparative example is tested by taking circulating water of a certain group for actual operation, and the dosing concentration is 20 mg/L, and the scale inhibition rate and corrosion inhibition rate of the scale inhibitor are tested. Wherein, the pH=8.15, turbidity 5.23 NTU, total hardness 231.18 mg/L, alkalinity 99.08 mg/L, calcium hardness 185.15 mg/L, cl - 96.42 mg/L,Fe2+ 0.08.08 mg/L, total phosphorus 5.93 mg/L, COD 48.81 mg/L and ammonia nitrogen 34.34 mg/L of the circulating water.
Static scale inhibition was performed according to the scale inhibition test method for calcium carbonate in the above-described test example 1.
Corrosion inhibition experiments of the water treatment agent were carried out according to the hanging piece corrosion inhibition experiment method in the experiment example 3.
TABLE 5 Scale inhibition and corrosion inhibition for circulating water of chemical groups of examples 1, 2, 3 and comparative examples
As shown in the results of Table 5, the scale inhibitor of the invention of the example 2 has a scale inhibition efficiency of 99.65% for circulating water in actual operation of a chemical group, a corrosion inhibition rate of 96.91% for carbon steel, and the scale inhibition efficiency and corrosion inhibition efficiency of the example are significantly better than those of the comparative example.
Finally, it is pointed out that the above examples show and describe the basic principle of the invention, the characteristics of the product and the advantages of the method according to the invention. The present invention is not limited to the above embodiments, and various changes and modifications can be made without departing from the scope of the invention, and the invention is intended to be included in the scope of protection.

Claims (5)

1. The preparation method of the compound phosphorus-free environment-friendly scale inhibitor is characterized by comprising the following specific preparation steps: wherein the weight parts of the components are as follows,
(1) Preparation of hydroxyethyl starch derivatives containing propenyl groups:
Adding 10-20 parts of hydroxyethyl starch into 50-200 parts of solvent, stirring for 10-30 minutes at 10-40 ℃, then adding 4-7 parts of acrylic acid and 11-19 parts of condensing agent, maintaining the temperature of the mixed solution at 10-40 ℃, adding 0.1-0.5 part of 4-dimethylaminopyridine, and continuously stirring for 4-10 hours; pouring the reaction solution into 500-2000 parts of methanol, stirring for 20-40 minutes, filtering, washing the solid with 50-80 parts of methanol for three times respectively, and drying to obtain hydroxyethyl starch derivative containing propenyl;
(2) Preparation of modified starch polymer:
Adding the hydroxyethyl starch derivative containing the propenyl, 18-26 parts of acrylic acid and 5-8 parts of maleic anhydride prepared in the step (1) into 100-150 parts of deionized water, introducing argon for 10-30 minutes under the stirring condition, then adding 0.3-0.7 part of potassium peroxodisulfate, heating to 70-90 ℃, and stirring for 2-4 hours; cooling to 10-30 ℃, pouring the reaction liquid into 800-2000 parts of methanol, filtering, washing the solid with 100-150 parts of methanol for three times respectively, and drying to obtain a modified starch polymer;
(3) Preparation of a polycarboxylic sulfonic acid copolymer:
Adding 16-19 parts of 2-acrylamide-2-methylpropanesulfonic acid, 10-14 parts of acrylic acid and 12-16 parts of maleic anhydride into 130-180 parts of deionized water, introducing argon for 10-30 minutes under the stirring condition, adding 0.5-0.9 part of potassium persulfate, heating to 70-90 ℃, and stirring for 2-4 hours; cooling to 10-30 ℃, pouring the reaction solution into 1200-2200 parts of methanol, filtering, washing the solid with 150-200 parts of methanol for three times respectively, and drying to obtain the polycarboxylic sulfonic acid copolymer;
(4) Preparation of a compound environment-friendly phosphorus-free scale inhibitor containing hydroxyethyl starch and a polycarboxylic sulfonic acid copolymer:
And (3) directly blending the modified starch polymer prepared in the step (2) and the polycarboxylic acid copolymer prepared in the step (3) to obtain the compound phosphorus-free scale inhibitor containing hydroxyethyl starch and the polycarboxylic acid copolymer.
2. The method for preparing the compound phosphorus-free environment-friendly scale inhibitor, which is characterized by comprising the following steps: in the step (1), the solvent is dimethyl sulfoxide or N, N-dimethylformamide.
3. The method for preparing the compound phosphorus-free environment-friendly scale inhibitor, which is characterized by comprising the following steps: in the step (1), the condensing agent is 1- (3-dimethylaminopropyl) -3-ethylcarbodiimide hydrochloride or dicyclohexylcarbodiimide.
4. The method for preparing the compound phosphorus-free environment-friendly scale inhibitor, which is characterized by comprising the following steps: in the step (2), the potassium persulfate is added in two batches, wherein the first batch is added with 0.1-0.4 part, and the second batch is added with 0.2-0.3 part, and the intervals between the batches are at least 30 minutes.
5. The method for preparing the compound phosphorus-free environment-friendly scale inhibitor, which is characterized by comprising the following steps: in the step (3), the potassium persulfate is added in three batches, wherein the first batch is added with 0.2-0.3 part, the second batch is added with 0.2-0.3 part, and the third batch is added with 0.1-0.3 part, and the intervals between the batches are at least 30 minutes.
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
LU62292A1 (en) * 1970-09-28 1971-05-18
US5087376A (en) * 1990-10-15 1992-02-11 Calgon Corporation Multifunctional scale inhibitors
JP2004293028A (en) * 2003-03-13 2004-10-21 Hakuto Co Ltd Scale inhibitor and scale inhibitory method for barium sulfate in water system
CN107902770A (en) * 2017-10-24 2018-04-13 陈木玲 A kind of non-phosphorus scale and corrosion inhibitor and its preparation process
US20230322977A1 (en) * 2022-04-11 2023-10-12 Independence Oilfield Chemicals Llc Aqueous formulations

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
LU62292A1 (en) * 1970-09-28 1971-05-18
US5087376A (en) * 1990-10-15 1992-02-11 Calgon Corporation Multifunctional scale inhibitors
JP2004293028A (en) * 2003-03-13 2004-10-21 Hakuto Co Ltd Scale inhibitor and scale inhibitory method for barium sulfate in water system
CN107902770A (en) * 2017-10-24 2018-04-13 陈木玲 A kind of non-phosphorus scale and corrosion inhibitor and its preparation process
US20230322977A1 (en) * 2022-04-11 2023-10-12 Independence Oilfield Chemicals Llc Aqueous formulations

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
WOO, BH ET AL.: "Preparation and characterization of a composite PLGA and poly(acryloyl hydroxyethyl starch) microsphere system for protein delivery", 《PHARMACEUTICAL RESEARCH》, vol. 16, no. 11, 31 December 2001 (2001-12-31), pages 1600 - 1606 *
李宇请: "聚羧酸型阻垢分散剂的研制", 《江苏化工》, no. 4, 31 December 1990 (1990-12-31), pages 14 - 16 *
王超等: "酰胺类无磷缓蚀阻垢剂对稀有鮈鲫的急性毒性研究", 《广东化工》, vol. 42, no. 12, 30 June 2015 (2015-06-30), pages 49 - 50 *

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