A kind of non-phosphorus copolymer antiscaling dispersant and preparation method thereof

A technology of scale inhibitor dispersant and copolymer, which is applied in the field of circulating cooling water treatment, can solve the problems of easy decomposition, increase the dosage of corrosion inhibitor and scale inhibitor, increase the cost of circulating water treatment, etc., and achieve high economic and social benefits , good scale inhibition and dispersion effect, simple preparation method

Active Publication Date: 2015-10-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] There are many patents on polycarboxylate scale inhibitors and dispersants at home and abroad, such as CN01123146 "low molecular weight (meth) acrylic acid (salt) polymer and its preparation method and use", CN94194415.8 "unsaturated carboxylic acid copolymer And its preparation method and application", etc., but with the continuous development of industrial circulating cooling water treatment process, the complexity and variability of the circulating water system are gradually deepening, and higher requirements are put forward for the adaptability of water treatment chemicals
In particular, the frequent occurrence of material leakage makes oily substances enter the circulating water. The COD, turbidity, oil content, suspended solids and other indicators of the circulating water are high. The commonly used corrosion and scale inhibitors are difficult to play a normal role and can only Increasing the amount of corrosion and scale inhibitors, or frequent sewage replacement, greatly increases the cost of circulating water treatment, and also increases the complexity of circulating water treatment
In addition, most of the scale inhibitors and dispersants that have been published and applied contain phosphorus. When these scale inhibitors and dispersants enter the circulating water system, they can provide rich nutrients for bacteria and algae in the water, are easily decomposed, and will increase the size of the circulating water system. The difficulty of sterilization and algae removal affects the stable operation of the circulating water system

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0054] Weigh 90g of acrylic acid, 11g of sodium metabisulfite, measure 110ml of isopropanol, stir to dissolve, add to a four-necked flask equipped with a stirrer, reflux condenser, constant pressure dropping funnel and thermometer; weigh 11g of ammonium persulfate , Dissolve in 40ml isopropanol, add to constant pressure funnel I; weigh 10g of oleic acid, dissolve in 50ml isopropanol, mix well, add to constant pressure funnel II; heat up, wait for the temperature to rise to 60 ℃, add persulfuric acid dropwise Ammonium solution and oleic acid solution; control the dripping for 2h; after the dripping is completed, heat up to the boiling point of isopropanol, polymerize at the boiling point of isopropanol for 3h; cool to get the product, the product's CaCO resistance 3 The fouling rate and iron stabilization rate are shown in Table 2.

Embodiment 2

[0056] Weigh 95g of acrylic acid, 11g of sodium metabisulfite, measure 110ml of isopropanol, stir to dissolve, add to a four-necked flask equipped with a stirrer, reflux condenser, constant pressure dropping funnel and thermometer; weigh 11g of ammonium persulfate , Dissolve in 40ml isopropanol, add to constant pressure funnel Ⅰ; weigh 5g of oleic acid, dissolve in 50ml isopropanol, mix well, add to constant pressure funnel Ⅱ; heat up, wait for the temperature to rise to 60 ℃, add persulfuric acid dropwise Ammonium solution and oleic acid solution; control the dripping for 2h; after the dripping is completed, heat up to the boiling point of isopropanol, polymerize at the boiling point of isopropanol for 3h; cool to get the product, the product's CaCO resistance 3 The fouling rate and iron stabilization rate are shown in Table 2.

Embodiment 3

[0058] Weigh 94g of maleic acid, 11g of sodium metabisulfite, measure 110ml of isopropanol, stir to dissolve, add to a four-necked flask equipped with a stirrer, reflux condenser, constant pressure dropping funnel and thermometer; weigh persulfuric acid Ammonium 11g, dissolved in 40ml isopropanol, added to constant pressure funnel I; weigh 6g of linoleic acid, dissolved in 50ml isopropanol, mix well, add to constant pressure funnel II; heat up, wait until the temperature rises to 60 ℃, drop Add ammonium persulfate solution and linoleic acid solution; control the dripping for 2h; after dripping, heat up to the boiling point of isopropanol, polymerize at the boiling point of isopropanol for 3h; cool to get the product, the product is CaCO resistant 3 The fouling rate and iron stabilization rate are shown in Table 2.

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Abstract

The invention relates to a non-phosphorus copolymer antiscale dispersant which is prepared by carrying out one-step polymerization on 5-15% of C16-C24 unsaturated fatty acid and 85-95% of C3-C8 unsaturated carboxylic acid in an organic solvent under the initiation action of inorganic peroxide. The invention also discloses a preparation method of the copolymer antiscale dispersant. The molecular structure of the copolymer antiscale dispersant contains carboxyl groups and long carbon chains; and thus, the copolymer antiscale dispersant has certain surface activity and stripping property on the premise of having favorable calcium carbonate scale inhibition property and dispersibility, and especially has better antiscale effect than common antiscale dispersants in a water body with higher oil content. The copolymer antiscale dispersant has the advantages of simple preparation method, low cost, low consumption and favorable antiscale and dispersion effects, is free of phosphorus, is green and environment-friendly, can be widely used in an industrial circulating cooling water system, and has higher economic benefit and social benefit.

Description

Technical field [0001] The invention relates to the field of circulating cooling water treatment, and more particularly to a phosphorus-free copolymer scale inhibitor and dispersant and a preparation method thereof. Background technique [0002] With the scale of industrial production and the rapid increase in population, water resources are severely scarce. The amount of circulating cooling water accounts for 60~70% of industrial water consumption, and reasonable saving of circulating cooling water is the most direct way to reduce industrial water consumption. The main method of saving circulating cooling water is to increase the circulating utilization rate of circulating cooling water, which not only increases the concentration ratio, but it will also cause serious corrosion and scaling problems to the circulating water system, which puts forward a higher level of water treatment technology. Claim. In order to ensure the normal operation of the circulating water system under...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F220/02C08F222/02C08F4/40C02F5/10
Inventor 郦和生王亭李长玥
Owner CHINA PETROLEUM & CHEM CORP
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