CN117566925A - Concentrated solution scale inhibitor - Google Patents

Concentrated solution scale inhibitor Download PDF

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CN117566925A
CN117566925A CN202311701450.9A CN202311701450A CN117566925A CN 117566925 A CN117566925 A CN 117566925A CN 202311701450 A CN202311701450 A CN 202311701450A CN 117566925 A CN117566925 A CN 117566925A
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scale inhibitor
acid
polyacrylic acid
carboxymethyl cellulose
corrosion
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CN117566925B (en
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杨述芳
庞宏磊
李恩红
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Beijing Polymer Technology Co ltd
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Beijing Polymer Technology Co ltd
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    • 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
    • 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
    • C02F5/12Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances containing nitrogen
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/08Corrosion inhibition

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

Abstract

The application relates to a concentrated solution scale inhibitor, which comprises the following components in percentage by weight: 40-50% of polyacrylic acid, 7-9% of carboxymethyl cellulose-polyacrylic acid grafted product, 7-9% of corrosion and scale inhibitor reinforcing agent, 3-5% of maleic acid-acrylic acid copolymer, 1-3% of dispersing auxiliary agent, 1-2% of acid regulator, 1-2% of bactericide, 0.5-1% of stabilizer and the balance of water; wherein the molecular weight of the polyacrylic acid is 500-5000; wherein the corrosion and scale inhibitor reinforcing agent comprises carboxymethyl starch-polyacrylamide grafted copolymer and sodium benzotriazole. The method can improve the corrosion and scale inhibition effect of the scale inhibitor while realizing the phosphorus-free scale inhibition water treatment.

Description

Concentrated solution scale inhibitor
Technical Field
The application relates to the field of water treatment scale inhibitors, in particular to a concentrated solution scale inhibitor.
Background
China is an industrial large country, and a large amount of water resources are consumed each year for industrial water. In industrial water use, in order to protect the environment and save the cost, a water circulation system is generally required to be arranged for recycling the industrial water. However, when industrial water is recycled in the system, the problems of scaling, corrosion and the like of pipelines and equipment are often accompanied, and the normal operation of the equipment is affected, so that certain economic loss and potential safety hazard are caused. In order to solve the problems of scaling and corrosion of water treatment equipment, corrosion and scale inhibitors are mainly used for treating water at present.
The corrosion and scale inhibitor commonly used in industry is mainly made of phosphorus, and the main varieties are as follows: polyphosphates, phosphoric acid vinegar, organic polyphosphonic acids, etc., but without dispersing. The polymer scale inhibition and dispersion agent is divided into natural and synthetic types, wherein the natural polymer scale inhibition and dispersion agent mainly comprises starch, tannin, lignin and the like, but is rarely used at present due to unstable products and high impurity content; the synthetic polymer scale inhibition and dispersion agent mainly comprises carboxylic acid, sulfonic acid and phosphorus, wherein the phosphorus-containing carboxylic acid polymer has good scale inhibition and dispersion performance, and the polymer has low phosphorus content, thereby being relatively beneficial to environmental protection.
However, at present, the annual phosphorus products used for producing corrosion and scale inhibitors are about 10 ten thousand tons, and the phosphorus-containing compounds are finally discharged as waste, so that serious pollution is caused to water environment, and therefore, aiming at the existing scale inhibitors, the development of novel corrosion and scale inhibitors with no phosphorus or lower phosphorus content and high efficiency is a direction of urgent development.
Disclosure of Invention
In order to achieve the effect of corrosion and scale inhibition of the scale inhibitor while achieving the phosphorus-free scale inhibition water treatment, the application provides a concentrated solution scale inhibitor.
The application provides a concentrated solution scale inhibitor which adopts the following technical scheme:
the concentrated solution scale inhibitor comprises the following components in parts by weight:
40-50% of polyacrylic acid, 7-9% of carboxymethyl cellulose-polyacrylic acid grafted product, 7-9% of corrosion and scale inhibitor reinforcing agent, 3-5% of maleic acid-acrylic acid copolymer, 1-3% of dispersing auxiliary agent, 1-2% of acid regulator, 1-2% of bactericide, 0.5-1% of stabilizer and the balance of water;
wherein the molecular weight of the polyacrylic acid is 500-5000;
wherein the corrosion and scale inhibitor reinforcing agent comprises carboxymethyl starch-polyacrylamide grafted copolymer and sodium benzotriazole.
By adopting the technical scheme, firstly, the polyacrylic acid contains a large amount of carboxyl functional groups, and the carboxyl functional groups can be combined with metal ions such as Ca which are easy to form scale in water 2+ 、Mg 2+ Bind to thereby hinder the binding of the scale forming anions (e.g. CO 3 2- ,SO 4 2- Etc.) to form scale forming particles to act as scale inhibitors; and the interaction force and cohesion between polymer molecules of polyacrylic acid with molecular weight of 500-5000The force is weaker than that of the polyacrylic acid with relatively high molecular weight, so that the polyacrylic acid can be better dissolved and dispersed in water, and the scale inhibition effect is further improved by more fully preventing scale formation particles from being contacted and aggregated with each other to form enlargement and deposition. The carboxymethyl cellulose also has a large number of carboxyl functional groups, more carboxyl functional groups can be introduced into the scale inhibitor through forming a carboxymethyl cellulose-polyacrylic acid grafted product, and the carboxymethyl cellulose-polyacrylic acid grafted product and polyacrylic acid cooperate to perform a structure with metal ions which are easy to form scale, so that the scale inhibition effect is further improved.
The maleic acid-acrylic acid copolymer also has the functions of corrosion inhibition and scale inhibition, has good high temperature resistance, and is compounded with polyacrylic acid and carboxymethyl cellulose-polyacrylic acid grafted products for use, so that the scale inhibitor has good scale inhibition effect in a higher-temperature water environment. The acidic regulator can regulate and neutralize the pH value of water to be treated, and other scale inhibition components can better inhibit scale of water with high alkalinity and high pH value.
The carboxymethyl starch-polyacrylamide graft copolymer and the benzotriazole sodium in the corrosion and scale inhibition reinforcing agent have film forming property, and a layer of film is formed on the surface of metal equipment, wherein the film formed on the surface of the equipment by the benzotriazole sodium can protect the surface of the metal and is not easy to corrode, so that the corrosion inhibition effect is achieved; meanwhile, because the carboxymethyl starch in the carboxymethyl starch-polyacrylamide graft copolymer also contains more carboxyl functional groups, after the carboxymethyl starch-polyacrylamide graft copolymer and the benzotriazole sodium form a film on the surface of the metal, the carboxymethyl starch-polyacrylamide graft copolymer can be combined with metal ions which are easy to form scale in water, and the formation of scale particles in a water area close to the metal of the equipment is further hindered, so that the scale inhibition effect is further improved.
All the components do not contain phosphorus, so that the formed scale inhibitor has more excellent corrosion and scale inhibition effects while being free of phosphorus.
Optionally, the preparation method of the carboxymethyl cellulose-polyacrylic acid grafted product comprises the following steps:
mixing hydroxypropyl methyl cellulose with alkaline solution with a certain concentration, adding isopropanol, heating in water bath and stirring for 1-2h, dropwise adding a certain amount of chloroacetic acid fully dissolved in the isopropanol into a reaction system, reacting for 2-4h, adjusting the pH of the product to be neutral, washing, filtering and drying to obtain carboxymethyl cellulose;
dissolving the obtained carboxymethyl cellulose in water, introducing inert gas, stirring for 1-2h in a water bath at 50-60 ℃, adding ammonium persulfate aqueous solution, dropwise adding acrylic acid solution according to a certain proportion after the mixed solution reacts for 15-18min, reacting for 2-3h, extracting and drying the reaction product, and crushing to obtain the carboxymethyl cellulose-polyacrylic acid grafted product.
By adopting the technical scheme, the hydroxypropyl methylcellulose is firstly heated in a water bath, so that the hydroxypropyl methylcellulose is fully swelled and alkalized, chloroacetic acid is used as a modifier to make the hydroxypropyl methylcellulose carry out carboxylation reaction to obtain carboxymethyl cellulose, and then the carboxymethyl cellulose and a certain proportion of acrylic acid are subjected to copolymerization grafting reaction to obtain a carboxymethyl cellulose-polyacrylic acid grafted product with a certain grafting rate.
Optionally, the molar ratio of the carboxymethyl cellulose to the acrylic acid is 1 (0.4-0.7).
By adopting the technical scheme, the grafting rate of the carboxymethyl cellulose-polyacrylic acid grafted product generated by copolymerization grafting of the carboxymethyl cellulose and the acrylic acid according to the molar ratio is 7.15-18.30 percent, and the film forming performance and the scale inhibition performance of the carboxymethyl cellulose-polyacrylic acid grafted product with the grafting rate are relatively better.
Optionally, the mass ratio of the carboxymethyl starch-polyacrylamide grafted copolymer and the sodium benzotriazole in the corrosion and scale inhibition reinforcing agent is 1: (0.7-0.9).
By adopting the technical scheme, the carboxymethyl starch-polyacrylamide grafted copolymer and the benzotriazole sodium are compounded according to the proportion range, so that the corrosion inhibition performance and the scale inhibition effect of the film formed by the carboxymethyl starch-polyacrylamide grafted copolymer and the benzotriazole sodium on the surface of metal equipment are relatively better.
Optionally, the dispersing auxiliary comprises the components with the mass ratio of 1: (0.4-0.6): (2.0-2.8): (2.5-3.5) isopropanolamine, sulfonic polycarboxylic acid, octylphenol polyoxyethylene ether and sodium alkyl sulfonate.
By adopting the technical scheme, the components have better dispersibility and lubricity, and the components are compounded according to the mass ratio, so that isopropanolamine, sulfonic polycarboxylic acid, octyl phenol polyoxyethylene ether and sodium alkyl sulfonate have synergistic effect, and scale forming particles can be better prevented from being contacted with each other and aggregated to form a scale, and the scale inhibition effect is further improved.
Optionally, the acidity regulator is selected from at least one of citric acid, potassium citrate, tartaric acid and fumaric acid.
Optionally, the bactericide is at least one selected from calcium hypochlorite, polyvinylpyrrolidone derivatives and polyurethane.
By adopting the technical scheme, the components can be used for efficiently killing bacteria, fungi and algae generated by depending on the fungi in water, so that the condition that the algae in the circulating water are bred to destroy a circulating water system is reduced.
Optionally, the stabilizer is at least one selected from sodium alginate, dibutyl tin dimaleate and dibutyl tin dilaurate.
By adopting the technical scheme, the components are synergistic, so that the scale inhibitor is reduced in the production and use processes, the possibility of denaturation of other components in the scale inhibitor due to the influence of temperature and pH is reduced, and the product stability of the scale inhibitor is improved.
In a second aspect, the preparation method of the concentrated solution scale inhibitor provided by the application adopts the following technical scheme:
the preparation method of the concentrated solution scale inhibitor comprises the following steps:
mixing and stirring polyacrylic acid, a carboxymethyl cellulose-polyacrylic acid grafted product, a maleic acid-acrylic acid copolymer, an acid regulator, a bactericide, a stabilizer and water, and stirring until the mixture is dissolved to obtain a first solution; and adding a corrosion and scale inhibitor and a dispersing aid into the first solution, and homogenizing to obtain the concentrated solution scale inhibitor.
By adopting the technical scheme, each component in the scale inhibitor can be more fully dissolved and dispersed, so that the product stability of the scale inhibitor is improved.
Optionally, the stirring speed of the mixing and stirring is 150-200r/min, and the stirring time is 3-6min; the homogenizing speed is 700-780r/min, and the homogenizing time is 20-30min.
In summary, the present application includes at least one of the following beneficial technical effects:
1. the carboxymethyl cellulose-polyacrylic acid grafted product and polyacrylic acid cooperate to more fully carry out structure with metal ions which are easy to form scale, and have excellent scale inhibition effect; the carboxymethyl starch-polyacrylamide grafted copolymer and the benzotriazole sodium in the corrosion and scale inhibition reinforcing agent can be adsorbed on the surface of metal equipment to form a layer of film, and the film formed on the surface of the equipment by the benzotriazole sodium can protect the surface of the metal and is not easy to corrode, so that a corrosion inhibition effect is achieved; meanwhile, the carboxymethyl starch-polyacrylamide grafted copolymer can be combined with metal ions which are easy to form scale in water, so that the formation of scale particles in water close to equipment metal is further hindered, and the scale inhibition effect is further improved;
2. the maleic acid-acrylic acid copolymer is compounded with polyacrylic acid and carboxymethyl cellulose-polyacrylic acid grafted products, so that the scale inhibitor has a good scale inhibition effect in a high-temperature water environment; the acidic regulator can regulate and neutralize the pH value of water to be treated, and other scale inhibition components can better inhibit the scale of water with high alkalinity and high pH value;
3. the grafting rate of the carboxymethyl cellulose-polyacrylic acid grafted product generated by the copolymerization grafting of the carboxymethyl cellulose and the acrylic acid according to the molar ratio is 7.15-18.30 percent, and the film forming property and the scale inhibition property of the carboxymethyl cellulose-polyacrylic acid grafted product with the grafting amount are relatively better.
Detailed Description
1. Examples
Example 1:
the concentrated solution scale inhibitor comprises the following components in parts by weight:
40% of polyacrylic acid, 7% of carboxymethyl cellulose-polyacrylic acid grafted product, 7% of corrosion and scale inhibitor reinforcing agent, 3% of maleic acid-acrylic acid copolymer, 1% of dispersing aid, 1% of acidity regulator, 1% of bactericide, 0.5% of stabilizer and the balance of water;
wherein the polyacrylic acid has a molecular weight of 500-5000, preferably a molecular weight of 1000-2000;
wherein the corrosion and scale inhibition reinforcing agent comprises carboxymethyl starch-polyacrylamide grafted copolymer and benzotriazole sodium in a mass ratio of 1:0.8;
wherein the dispersing auxiliary comprises the following components in percentage by mass: 0.5:2.4:3 isopropanolamine, sulfonic polycarboxylic acid, octyl phenol polyoxyethylene ether and sodium alkyl sulfonate;
wherein the bactericide is calcium hypochlorite, the acid regulator is potassium citrate, and the stabilizer is sodium alginate.
Preparing a carboxymethyl cellulose-polyacrylic acid grafted product:
mixing 20g of hydroxypropyl methylcellulose (purchased from Hebei purple gold chemical industry Co., ltd.) with 10mg/L NaOH aqueous solution, adding 150mL of isopropanol, heating in a water bath at 50 ℃, mechanically stirring for 2 hours, dropwise adding 10g of chloroacetic acid fully dissolved in the isopropanol into a reaction system, reacting for 4 hours, adding 2mol/L hydrochloric acid solution (mass fraction is 25%) to adjust the pH of the product to be neutral, washing and filtering with ethanol, and fully drying the obtained product in an oven for 48 hours to obtain carboxymethyl cellulose;
10g of the obtained carboxymethyl cellulose is dissolved in water, nitrogen is introduced, the mixture is stirred for 1h in a water bath at 60 ℃, then ammonium persulfate aqueous solution is added, after the mixed solution reacts for 15min, acrylic acid solution (2 mol/L) is continuously added dropwise according to a certain proportion in a nitrogen environment, and the reaction is carried out for 3h at 50 ℃. After the reaction is finished, settling the reaction product in ethanol, placing the reaction product in a vacuum oven at 50 ℃ for drying for 48 hours, taking out the reaction product after drying, and crushing the reaction product by a high-speed stirring crusher to obtain a carboxymethyl cellulose-polyacrylic acid grafted product after crushing;
wherein the molar ratio of the carboxymethyl cellulose to the acrylic acid is 1:0.5, and the amount of the substance added to the carboxymethyl cellulose is 0.038mol, so that the amount of the substance added to the acrylic acid is 0.019, namely 9.5ML of acrylic acid solution is added dropwise;
preparing carboxymethyl starch-polyacrylamide graft copolymer:
10g of water-soluble acrylamide (purchased from Shandong Hao forward chemical Co., ltd.) and 12g of carboxymethyl starch (purchased from Yingchu Jinyu chemical Co., ltd.) are added into 25g of water and alkyl glycoside emulsifier, 4g of sodium dodecyl benzene sulfonate is added, so that an emulsifying system is formed by acrylamide monomer and starch in a dispersion system, emulsion polymerization is carried out under the action of an initiator permanganate to form carboxymethyl starch-polyacrylamide graft copolymer, and the powdery carboxymethyl starch-polyacrylamide graft copolymer is obtained after azeotropic distillation and dehydration.
And (3) preparing concrete:
mixing and stirring 40g of polyacrylic acid, 7g of carboxymethyl cellulose-polyacrylic acid grafted product, 3g of maleic acid-acrylic acid copolymer, 1g of acid regulator, 1g of bactericide, 0.5g of stabilizer and 39.5g of water, wherein the stirring speed is 180r/min, the stirring time is 5min, and stirring until the mixture is dissolved to obtain a first solution; and adding 7g of corrosion and scale inhibitor and 1g of dispersing aid into the first solution, homogenizing at 740r/min for 26min to obtain the concentrated solution scale inhibitor.
Examples 2-3:
a concentrated scale inhibitor was different from example 1 in the following point as shown in Table 1.
Table 1:
example 4:
a concentrated scale inhibitor which is different from example 2 in that: in the process of preparing the carboxymethyl cellulose-polyacrylic acid grafted product, the molar ratio of the carboxymethyl cellulose to the acrylic acid is 1:0.4.
Example 5:
a concentrated scale inhibitor which is different from example 2 in that: in the process of preparing the carboxymethyl cellulose-polyacrylic acid grafted product, the molar ratio of the carboxymethyl cellulose to the acrylic acid is 1:0.7.
Example 6:
a concentrated scale inhibitor which is different from example 2 in that: polyacrylic acid with molecular weight of 500-1000 is selected.
Example 7:
a concentrated scale inhibitor which is different from example 2 in that: polyacrylic acid with molecular weight of 2000-5000 is selected.
Example 8:
a concentrated scale inhibitor which is different from example 2 in that: the mass ratio of the carboxymethyl starch-polyacrylamide grafted copolymer and the benzotriazole sodium in the corrosion and scale inhibitor reinforcing agent is 1:0.7.
Example 9:
a concentrated scale inhibitor which is different from example 2 in that: the mass ratio of the carboxymethyl starch-polyacrylamide grafted copolymer and the benzotriazole sodium in the corrosion and scale inhibitor reinforcing agent is 1:0.9.
Example 10:
a concentrated scale inhibitor which is different from example 2 in that: the mass ratio of isopropanolamine, sulfonic polycarboxylic acid, octyl phenol polyoxyethylene ether and sodium alkyl sulfonate in the dispersing auxiliary is 1:0.4:2.0:2.5.
example 11:
a concentrated scale inhibitor which is different from example 2 in that: the mass ratio of isopropanolamine, sulfonic polycarboxylic acid, octyl phenol polyoxyethylene ether and sodium alkyl sulfonate in the dispersing auxiliary is 1:0.6:2.8:3.5.
example 12:
a concentrated scale inhibitor which is different from example 2 in that: the acidity regulator is citric acid.
Example 13:
a concentrated scale inhibitor which is different from example 2 in that: the acidity regulator is tartaric acid.
Example 14:
a concentrated scale inhibitor which is different from example 2 in that: the stabilizer is dibutyl tin dimaleate.
Example 15:
a concentrated scale inhibitor which is different from example 2 in that: the stabilizer is dibutyl tin dilaurate.
2. Comparative example
Comparative example 1:
the difference from example 2 is that: the carboxymethyl cellulose-polyacrylic acid grafted product was equally replaced with polyacrylic acid.
Comparative example 2:
the difference from example 2 is that: the corrosion and scale inhibitor reinforcing agent is replaced by polyacrylic acid in an equivalent way.
Comparative example 3:
the difference from example 2 is that: the molar ratio of carboxymethyl cellulose to acrylic acid is 1:0.9.
Comparative example 4:
the difference from example 2 is that: the molar ratio of carboxymethyl cellulose to acrylic acid is 1:0.2.
Comparative example 5:
the difference from example 2 is that: the molecular weight of the polyacrylic acid was 7000.
Comparative example 6:
the difference from example 2 is that: the carboxymethyl starch-polyacrylamide grafted copolymer in the corrosion and scale inhibitor is replaced by sodium benzotriazole in an equivalent amount.
Comparative example 7:
the difference from example 2 is that: and the sodium benzotriazole in the corrosion and scale inhibition reinforcing agent is replaced by carboxymethyl starch-polyacrylamide grafted copolymer in an equivalent way.
Comparative example 8:
the difference from example 2 is that: the mass ratio of the carboxymethyl starch-polyacrylamide graft copolymer and the benzotriazole sodium in the corrosion and scale inhibition reinforcing agent is 1:0.5.
comparative example 9:
the difference from example 2 is that: the mass ratio of the carboxymethyl starch-polyacrylamide graft copolymer and the benzotriazole sodium in the corrosion and scale inhibition reinforcing agent is 1:1.1.
3. performance test
The scale inhibitor prepared in examples 1 to 15 and comparative examples 1 to 9 was diluted 11 times with water to obtain a reference liquid for the test; preparing a test solution containing a certain amount of calcium ions, adding the same dose of the reference solutions of examples 1-15 and comparative examples 1-9 into the test solution, setting a blank control group, and dripping bicarbonate solution into the test solutions of examples 1-15 and comparative examples 1-9 and the blank control group to continuously increase the supersaturation degree of calcium carbonate until calcium carbonate is formed.
1) And detecting the scale inhibition performance by a pH method:
the final point of precipitation of calcium carbonate was determined by the pH values of the test solutions of examples 1 to 15 and comparative examples 1 to 9 and the blank solutions, and the supersaturation degree value of calcium carbonate was calculated.
The test results are expressed as supersaturation degree S of calcium carbonate. The calculation formula is as follows:
wherein:
-the concentration of calcium ions, bicarbonate ions, carbonate ions, hydrogen ions in the pH before the decrease;
C 1 、C 2 -preparing reagent concentrations of CaCl2 and NaHCO3, C 1 =0.009mol/L,C 2 =0.30mol/L;
V 1 CaCl was added prior to the assay 2 V of (2) 1 =150mL
V 2 -NaHCO is added before the pH value decreases 3 Volume, mL of (2)
pHc-maximum pH in solution;
K 2 -secondary ionization equilibrium constant of carbonic acid, K at 25 DEG C 2 =10-10.33;
Ksp-solubility product constant of calcium carbonate, ksp=4.8X10-9 at 25 ℃;
evaluation principle: taking the supersaturation degree S of calcium carbonate as a judgment basis, the larger the S is, the better the scale inhibitor has the performance of inhibiting calcium carbonate scale.
2) And detecting the scale inhibition performance by a conductivity method:
the end point of precipitation of calcium carbonate was determined by measuring the conductivities of the test solutions of examples 1 to 15 and comparative examples 1 to 9 and the blank solutions, and the supersaturation degree value of calcium carbonate was calculated. The test results are expressed as supersaturation degree S of calcium carbonate.
The calculation formula is as follows:
wherein:
C 3 、C 4 -configured CaCl configuration 2 And NaCO 3 Concentration of reagent C 3 =0.003mol/L,C 4 =0.10mol/L;
V 3 CaCl was added prior to the assay 2 V of (2) 1 =100mL;
V 4 NaCO is added before the conductivity decreases 3 Is defined as volume in ml.
Evaluation principle: taking the supersaturation degree S of calcium carbonate as a judgment basis, the larger the S is, the better the scale inhibitor has the performance of inhibiting calcium carbonate scale.
The above test results are shown in table 2.
Table 2:
4. analysis and summary of results
As can be seen from a combination of examples 1 to 3 and Table 2, the contents of the respective components in examples 1 to 3 are different, and as can be seen from Table 2, the supersaturation degree by the pH method and the conductivity method in example 2 is higher than that in examples 1 and 3. And in combination with comparative examples 1-2, the carboxymethyl cellulose-polyacrylic acid grafted product in comparative example 1 was replaced with polyacrylic acid in equal amount, and the corrosion and scale inhibitor in comparative example 2 was replaced with polyacrylic acid in equal amount, as can be seen from Table 2, the supersaturation degree of comparative examples 1-2, as measured by the pH method and the conductivity method, was significantly lower than that of examples 1-3.
The scale inhibitor can be prepared by compounding the components such as polyacrylic acid, carboxymethyl cellulose-polyacrylic acid grafted product, corrosion and scale inhibitor reinforcing agent and the like, and can remarkably improve the scale inhibition performance of the scale inhibitor in the water treatment process; and the scale inhibitor has relatively better scale inhibition performance by proportioning according to the content of each component in the embodiment 2.
As can be seen from a combination of examples 2, examples 4 to 5 and Table 2, in the preparation of the carboxymethyl cellulose-polyacrylic acid graft product of examples 4 to 5, the molar ratio of carboxymethyl cellulose to acrylic acid was different from that of example 2, i.e., the grafting ratio of the produced carboxymethyl cellulose-polyacrylic acid graft product was different from that of example 2, and as can be seen from Table 2, the supersaturation degree of examples 4 to 5 as measured by the pH method and the conductivity method was significantly lower than that of example 2.
And in combination with comparative examples 3 to 4, the molar ratio of carboxymethyl cellulose and acrylic acid of comparative examples 3 to 4 was outside the range of the present application, and as can be seen from Table 2, the supersaturation degree of comparative examples 3 to 4, as measured by the pH method and the conductivity method, was significantly lower than that of examples 2 and examples 4 to 5.
From the above, in the process of preparing the carboxymethyl cellulose-polyacrylic acid grafted product, the molar ratio of the carboxymethyl cellulose to the acrylic acid is within the range of the application, so that the effect of improving the scale inhibition performance of the carboxymethyl cellulose-polyacrylic acid grafted product is better, and the molar ratio of the carboxymethyl cellulose to the acrylic acid is 1: at 0.5, the scale inhibition performance is improved relatively better.
As can be seen from a combination of examples 6 to 7 and Table 2, the molecular weights of the polyacrylic acids selected in examples 6 to 7 were different from those in example 2, and it can be seen from Table 2 that the supersaturation degree of examples 6 to 7 as measured by the pH method and the conductivity method was significantly lower than that of example 2. In addition, in combination with comparative example 5, the molecular weight of polyacrylic acid selected in comparative example 5 was outside the range of the present application, and as can be seen from Table 2, the supersaturation degree of comparative example 5 was significantly lower than that of examples 2 and examples 6 to 7 by the pH method and the conductivity method.
From the above, the polyacrylic acid with the molecular weight of 500-5000 can have remarkable improvement effect on the scale inhibition performance, and further, the polyacrylic acid with the molecular weight of 1000-2000 has relatively better improvement effect on the scale inhibition performance.
As can be seen from the combination of examples 8 to 9 and Table 2, the mass ratio of carboxymethyl starch-polyacrylamide graft copolymer and sodium benzotriazole in the corrosion and scale inhibitor in examples 8 to 9 was different from that in example 2, and it can be seen from Table 2 that the supersaturation degree of examples 8 to 9 was lower than that in example 2 by the pH method and the conductivity method.
And in combination with comparative examples 6 to 9, the equivalent substitution of carboxymethyl starch-polyacrylamide graft copolymer in the corrosion and scale inhibitor of comparative example 6 with sodium benzotriazole and the equivalent substitution of sodium benzotriazole in the corrosion and scale inhibitor of comparative example 7 with carboxymethyl starch-polyacrylamide graft copolymer, as can be seen from Table 2, the supersaturation degree of comparative examples 6 to 7, as measured by the pH method and the conductivity method, is significantly lower than that of examples 2 and examples 8 to 9; and the mass ratio of the carboxymethyl starch-polyacrylamide grafted copolymer and the sodium benzotriazole in the corrosion and scale inhibition reinforcing agents of the comparative examples 8-9 is outside the application range, and as can be seen from the table 2, the supersaturation degree of the comparative examples 8-9 measured by a pH method and a conductivity method is obviously lower than that of the examples 2 and 8-9.
From the above, the carboxymethyl starch-polyacrylamide graft copolymer and the sodium benzotriazole are prepared according to the mass ratio of 1: (0.7-0.9) can obviously improve the scale inhibition performance by compounding; and the mass ratio of the carboxymethyl starch-polyacrylamide grafted copolymer to the sodium benzotriazole is 1:0.8, so that the scale inhibition performance is improved relatively better.
As is clear from the combination of examples 10 to 11 and Table 2, the mass ratios of isopropanolamine, sulfonic polycarboxylic acid, octylphenol polyoxyethylene ether and sodium alkylsulfonate in the dispersion auxiliaries of examples 10 to 11 are different from those of example 2, and as is clear from Table 2, the supersaturation degree of examples 10 to 11 as measured by the pH method and the conductivity method is lower than that of example 2. From the above, the mass ratio of isopropanolamine, sulfonic polycarboxylic acid, octyl phenol polyoxyethylene ether and sodium alkyl sulfonate in the dispersion auxiliary agent is 1:0.5:2.4: and 3, the scale inhibition performance is improved relatively better.
The foregoing are all preferred embodiments of the present application, and are not intended to limit the scope of the present application in any way, therefore: all equivalent changes of products, methods and principles of this application are intended to be covered by the scope of this application.

Claims (10)

1. The concentrated solution scale inhibitor is characterized by comprising the following components in parts by weight:
40-50% of polyacrylic acid, 7-9% of carboxymethyl cellulose-polyacrylic acid grafted product, 7-9% of corrosion and scale inhibitor reinforcing agent, 3-5% of maleic acid-acrylic acid copolymer, 1-3% of dispersing auxiliary agent, 1-2% of acid regulator, 1-2% of bactericide, 0.5-1% of stabilizer and the balance of water;
wherein the molecular weight of the polyacrylic acid is 500-5000;
wherein the corrosion and scale inhibitor reinforcing agent comprises carboxymethyl starch-polyacrylamide grafted copolymer and sodium benzotriazole.
2. The concentrate scale inhibitor of claim 1, wherein the method of preparing the carboxymethyl cellulose-polyacrylic acid grafted product comprises the steps of:
mixing hydroxypropyl methyl cellulose with alkaline solution with a certain concentration, adding isopropanol, heating in water bath and stirring for 1-2h, dropwise adding a certain amount of chloroacetic acid fully dissolved in the isopropanol into a reaction system, reacting for 2-4h, adjusting the pH of the product to be neutral, washing, filtering and drying to obtain carboxymethyl cellulose;
dissolving the obtained carboxymethyl cellulose in water, introducing inert gas, stirring for 1-2h in a water bath at 50-60 ℃, adding ammonium persulfate aqueous solution, dropwise adding acrylic acid solution according to a certain proportion after the mixed solution reacts for 15-18min, reacting for 2-3h, extracting and drying the reaction product, and crushing to obtain the carboxymethyl cellulose-polyacrylic acid grafted product.
3. The concentrate scale inhibitor of claim 2, wherein: the molar ratio of the carboxymethyl cellulose to the acrylic acid is 1 (0.4-0.7).
4. The concentrate scale inhibitor of claim 1, wherein: the mass ratio of the carboxymethyl starch-polyacrylamide grafted copolymer to the sodium benzotriazole in the corrosion and scale inhibition reinforcing agent is 1: (0.7-0.9).
5. The concentrate scale inhibitor of claim 1, wherein: the dispersing auxiliary comprises the following components in percentage by mass: (0.4-0.6): (2.0-2.8): (2.5-3.5) isopropanolamine, sulfonic polycarboxylic acid, octylphenol polyoxyethylene ether and sodium alkyl sulfonate.
6. The concentrate scale inhibitor of claim 1, wherein: the acidity regulator is at least one selected from citric acid, potassium citrate, tartaric acid and fumaric acid.
7. The concentrate scale inhibitor of claim 1, wherein: the bactericide is at least one selected from calcium hypochlorite, polyvinylpyrrolidone derivatives and polyurethane.
8. The concentrate scale inhibitor of claim 1, wherein: the stabilizer is at least one selected from sodium alginate, dibutyl tin dimaleate and dibutyl tin dilaurate.
9. A process for preparing a concentrate scale inhibitor according to any one of claims 1 to 8, comprising the steps of:
mixing and stirring polyacrylic acid, a carboxymethyl cellulose-polyacrylic acid grafted product, a maleic acid-acrylic acid copolymer, an acid regulator, a bactericide, a stabilizer and water, and stirring until the mixture is dissolved to obtain a first solution; and adding a corrosion and scale inhibitor and a dispersing aid into the first solution, and homogenizing to obtain the concentrated solution scale inhibitor.
10. The method for preparing the concentrated scale inhibitor according to claim 9, wherein the method comprises the following steps: the stirring speed of the mixing and stirring is 150-200r/min, and the stirring time is 3-6min; the homogenizing speed is 700-780r/min, and the homogenizing time is 20-30min.
CN202311701450.9A 2023-12-12 Concentrated solution scale inhibitor Active CN117566925B (en)

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