CN103395897A - Non-phosphorus environmentally-friendly water treatment agent and preparation method thereof - Google Patents

Non-phosphorus environmentally-friendly water treatment agent and preparation method thereof Download PDF

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Publication number
CN103395897A
CN103395897A CN2013103736690A CN201310373669A CN103395897A CN 103395897 A CN103395897 A CN 103395897A CN 2013103736690 A CN2013103736690 A CN 2013103736690A CN 201310373669 A CN201310373669 A CN 201310373669A CN 103395897 A CN103395897 A CN 103395897A
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maleic anhydride
natural high
high moleculer
moleculer eompound
water treatment
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CN103395897B (en
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李光海
吕萍
王宏义
刘康
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Hebei Jinhong Chemical Co., Ltd.
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TIANJIN KE WEI JIN HONG ENVIRONMENTAL TECHNOLOGY Co Ltd
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Abstract

The invention discloses a non-phosphorus environmentally-friendly water treatment agent and a preparation method thereof. The method comprises the following steps: performing grafting reaction on a natural high-molecular compound and maleic anhydride to obtain a maleic anhydride grafted natural high-molecular compound; performing copolymerization on the maleic anhydride grafted natural high-molecular compound and an acrylic acid monomer to obtain a copolymer; modifying the copolymer. The agent disclosed by the invention is green and pollution-free in synthetic process, and the product obtained is applied to a water treatment system and can be used as a corrosion and scale inhibitor to replace a conventional phosphorus containing agent. The agent disclosed by the invention is more excellent in performance and is suitable for large-scale industrial production.

Description

A kind of Phosphateless environmentally friendly water treatment agent and preparation method thereof
Technical field
The present invention relates to water treatment field, relate in particular to a kind of Phosphateless environmentally friendly water treatment agent and synthetic method thereof.
Background technology
At present, the processing of recirculated cooling water, mainly take chemical treatment as main, need to be added appropriate chemical treatment medicine and control the harm such as the corrosion and scaling of water coolant feedwater equipment and water-transmission line, bacterium algae, glutinous mud in recirculated cooling water.It is water treatment agent that the present recirculating cooling water system of China mainly adopts organophosphorus, they have excellent inhibition, scale-inhibiting properties, consumption is few, low price, but its a large amount of water quality nutrition accumulations that cause that use, impel the problem of the numerous life of a large amount of bacterium algae can not be ignored, so eco-friendly without phosphorus type water treatment agent becomes the focus of lot of domestic and foreign water treatment enterprise and research institution's research.
Without phosphorus water treatment corrosion inhibitors is the Focal point and difficult point of recirculated cooling water non-phosphorus scale and corrosion inhibitor formula.Generally speaking, the corrosion-mitigation scale-inhibition agent prescription is comprised of scale inhibition dispersed component and inhibition component two portions.Without phosphorus water treating corrosion and scale inhibitor of less types, and have the defect of self, its application be restricted, at present except the minority kinds such as molybdate, zinc salt, Sunmorl N 60S also with the composite use of phosphorus family corrosion inhibitor, basically being eliminated of other, the example of successful Application seldom.
" green scale corrosion inhibitor " of developing without phosphorus type must become the developing direction of industrial circulating cooling water treatment agent medicament.
Summary of the invention
Technical problem to be solved by this invention is, overcomes the deficiencies in the prior art, and water treatment agent and the novel preparation method thereof of a kind of excellent performance and Phosphateless environmentally friendly is provided.
Particular content of the present invention is: a kind of Phosphateless environmentally friendly water treatment agent is made by the preparation method who comprises following reactions steps: the copolyreaction that the graft reaction of natural high moleculer eompound and maleic anhydride obtains maleic anhydride graft natural high moleculer eompound, maleic anhydride graft natural high moleculer eompound and acrylic monomer obtains multipolymer.
Further, above-mentioned water treatment agent, also comprise in its preparation method the copolyreaction gained multipolymer of maleic anhydride graft natural high moleculer eompound and acrylic monomer is carried out the modification step, obtain water treatment agent.
The present invention also provides a kind of preparation method of novel non-phosphate environment-protective water treatment agent, the copolyreaction that the graft reaction that comprises natural high moleculer eompound and maleic anhydride obtains maleic anhydride graft natural high moleculer eompound process, maleic anhydride graft natural high moleculer eompound and acrylic monomer obtains the water treatment agent process, wherein
The graft reaction step of natural high moleculer eompound and maleic anhydride:
(1) take the soft water of counting by weight 400-600 part and join in stainless steel cauldron, stir; (2) will take the natural high moleculer eompound of counting by weight 100-300 part and join in aforesaid reaction vessel, and heat up and make its dissolving; (3) the powdery solid maleic anhydride that will count by weight 40-80 part at the uniform velocity joins in reactor; (4) add in the process of maleic anhydride powder, constantly drip the pH value in sodium hydroxide solution control reactor.(5) powder add complete after, be warming up to 10 ℃-80 ℃, continue reaction 1-4 hour, below the interior material pH value to 8 of sour conditioned reaction still, obtain product maleic anhydride graft natural high moleculer eompound;
Wherein also comprise in above-mentioned steps (3) and add the catalyst sulfuric acid titanium of counting by weight 2-6 part simultaneously in reactor; Wherein above-mentioned natural high moleculer eompound is a kind of in xylogen and modification derivant, Mierocrystalline cellulose and modification derivant thereof, starch and modification derivant thereof, and wherein the lignin modification derivative is selected from a kind of in sulfonated lignin, aminated lignin, alkylation xylogen, oxidative lignin; Cellulose modified derivative is selected from a kind of in etherified cellulose, esterified cellulose; The starch conversion derivative is selected from a kind of in modified starch, dextran.In above-mentioned natural high moleculer eompound and maleic anhydride graft reaction process, the pH value that drips in step (4) in sodium hydroxide solution control reactor is between 6-10.
The copolyreaction process of maleic anhydride graft natural high moleculer eompound and acrylic monomer comprises: the catalyzer that (1) will count 1-7 part by weight adds in the reactor of product maleic anhydride graft natural high moleculer eompound place, after intensification is dissolved catalyzer fully; (2) acrylic monomer of take initiator solution, counting by weight 60-100 part is added dropwise to reactor.(3) above-mentioned material dropping complete after, be warming up to 60 ℃-100 ℃, continue reaction 1-4 hour, obtain copolymer products, i.e. water treatment agent A; Step in wherein copolyreaction process (1) used catalyst is inorganic molysite, and wherein said inorganic molysite comprises a kind of in ferrous ammonium sulphate, ferrous sulfate, iron protochloride, iron(ic) chloride, ferric sulfate; Acrylic monomer in step (2) comprises one or more in vinylformic acid, methyl acrylate, ethyl propenoate, Propylene glycol monoacrylate, methacrylic acid, methyl methacrylate, β-dimethyl-aminoethylmethacrylate; Above-mentioned selected initiator solution is commercially available prod, can be selected from one or more in azo, peroxide, redox class initiator.
In addition, above-mentioned water treatment agent synthetic method, also comprise copolymer products---the modification step of water treatment agent A, wherein the modification step comprises: (1) obtains the copolyreaction gained copolymer products of maleic anhydride graft natural high moleculer eompound and acrylic monomer the thick product of brown after underpressure distillation; (2) control temperature 5-50 ℃, drip the vitriol oil in above-mentioned product, interval time the assaying reaction thing acid number, and calculate sulfonation degree,, when product reaches predetermined sulfonation degree, finish sulfonation reaction; (3) use again in sodium hydroxide solution and the excessive vitriol oil, obtain the water treatment agent B after modification; Wherein said predetermined sulfonation degree should be controlled in 20~50%.
The water treatment agent that obtains by the inventive method, can guarantee fully carrying out of each step reaction by accurate control synthesis condition, gained water treatment agent slowly-releasing scale-inhibiting properties is due to the ortho-water treatment agent of the existing method preparation in market at present, and whole building-up process green non-pollution, product is the non-phosphate environment-friendly type water treatment agent, can be used as inhibiter and be applied in water treatment system, excellent performance, be suitable for large-scale commercial production.
Embodiment
In order to make purpose of the present invention, technical scheme and advantage clearer, the present invention is further elaborated.
Embodiment 1
The graft reaction step of natural high moleculer eompound and maleic anhydride:
(1), to adding the soft water of 450g in churned mechanically 1L laboratory reaction still, stir (2) and add 150g, xylogen, rising temperature for dissolving under whipped state; (3) control temperature-stable at 30 ℃, add 4g titanium sulfate and powdery maleic anhydride 60g in reactor, drip simultaneously sodium hydroxide and control pH between 7-9; (4) after maleic anhydride adds, temperature is raised to 35 ℃, strengthens reaction 2 hours. below the material pH to 8 in hydrochloric acid conditioned reaction still, obtain product maleic anhydride graft natural high moleculer eompound.
The copolyreaction process of maleic anhydride graft natural high moleculer eompound and acrylic monomer:
(5) add the 1.1g ferrous sulfate to aforesaid reaction vessel, heat up it is dissolved fully, and drip 70g methyl acrylate and 80g initiator solution (i.e. 20% ammonium persulfate aqueous solution) uniformly in reactor, be controlled in 2 hours and all add.
(6) after material dropping finishes, temperature is controlled at 90 ℃ and continues reaction 2 hours, obtains copolymer products, i.e. water treatment agent A.
Be the modification step of water treatment agent A to copolymer products:
(7) the product underpressure distillation in step (6) is extremely steamed without moisture; (8) drip the vitriol oil in reactor, control temperature at 20 ℃, after 1.5 hours, vitriol oil add-on is 20g, and the product sulfonation degree reaches 30%, finishes sulfonation reaction; (9) to dripping in reactor in sodium hydroxide and the excessive vitriol oil, more than transferring PH to 2, discharging, obtain the water treatment agent B after modification.
Embodiment 2
The graft reaction step of natural high moleculer eompound and maleic anhydride:
(1), to adding the soft water of 500g in churned mechanically 1L laboratory reaction still, stir (2) and add 200g treated starch, rising temperature for dissolving under whipped state; (3) control temperature-stable at 30 ℃, add 4g titanium sulfate and powdery maleic anhydride 100g in reactor, drip simultaneously sodium hydroxide and control pH between 7-9; (4) after maleic anhydride adds, temperature is raised to 40 ℃, strengthens reaction 2 hours, below the material pH to 8 in sulfuric acid conditioned reaction still, obtains product maleic anhydride graft natural high moleculer eompound.
The copolyreaction process of maleic anhydride graft natural high moleculer eompound and acrylic monomer:
(5) add the 1.1g ferrous sulfate to aforesaid reaction vessel, heat up it is dissolved fully, and drip 80g vinylformic acid and 100g initiator solution (i.e. 10% the V-50 aqueous solution) uniformly in reactor, be controlled in 2 hours and all add.
(6) after material dropping finishes, temperature is controlled at 90 ℃ and continues reaction 2 hours, obtains copolymer products, i.e. water treatment agent A.
Be the modification step of water treatment agent A to copolymer products:
(7) the product underpressure distillation in step (6) is extremely steamed without moisture; (8) drip the vitriol oil in reactor, control temperature at 20 ℃, after 1.5 hours, vitriol oil add-on is 20g, and the product sulfonation degree reaches 25%, finishes sulfonation reaction; (9) to dripping in reactor in sodium hydroxide and the excessive vitriol oil, more than transferring PH to 2, discharging, obtain the water treatment agent B after modification.
Embodiment 3
The graft reaction step of natural high moleculer eompound and maleic anhydride:
(1), to adding the soft water of 450g in churned mechanically 1L four-hole boiling flask, stir (2) and add 180g oligose, rising temperature for dissolving under whipped state; (3) control temperature-stable at 30 ℃, add 4g titanium sulfate and powdery maleic anhydride 75g in reactor, drip simultaneously sodium hydroxide and control pH between 7-9; (4) after maleic anhydride adds, temperature is raised to 40 ℃, strengthens reaction 2 hours, below the material pH to 8 in hydrochloric acid conditioned reaction still, obtains product maleic anhydride graft natural high moleculer eompound.
The copolyreaction process of maleic anhydride graft natural high moleculer eompound and acrylic monomer:
(5) add the 1.1g ferrous sulfate to aforesaid reaction vessel, intensification is dissolved it fully, and drip 55g methacrylic acid, 20g methyl acrylate and 80g initiator solution (the 10% tertbutyl peroxide aqueous solution) uniformly in reactor, be controlled in 2 hours and all add.
(6) after material dropping finishes, temperature is controlled at 90 ℃ and continues reaction 2 hours, obtains copolymer products, i.e. water treatment agent A.
Be the modification step of water treatment agent A to copolymer products:
(7) the product underpressure distillation in step (6) is extremely steamed without moisture; (8) drip the vitriol oil in reactor, control temperature at 20 ℃, after 1.5 hours, vitriol oil add-on is 20g, and the product sulfonation degree reaches 45%, finishes sulfonation reaction; (9) to dripping in reactor in sodium hydroxide and the excessive vitriol oil, more than transferring PH to 2, discharging, obtain the water treatment agent B after modification.
The above is only the preferred embodiment of the present invention; should be pointed out that for those skilled in the art, under the premise without departing from the principles of the invention; can also make some improvements and modifications, these improvements and modifications also should be considered as protection scope of the present invention.
The product performance test
1. evaluation of antisludging performance--tosca method
In the present invention, the phosphate-free corrosion inhibition antisludging agent before and after processing through the 3rd step sulfonation modifying is done the static-state scale inhibition experiment, and to contrast commercially available traditional phosphorus be corrosion inhibiting and descaling agent and conventional phosphate-free corrosion inhibition antisludging agent (PESA, poly-epoxy succinic acid; PASP: poly aspartic acid), result following (experimental technique is with reference to GB/T16632-2008):
The CaCO of the different chemical feeding quantities of table 1 3The dirt scale inhibition performance
Figure BDA0000371453040000051
As can be seen from Table 1, the novel non-phosphate environment-protective water treatment agent of the present invention's preparation is better than commercially available traditional phosphorus aspect scale-inhibiting properties be corrosion inhibiting and descaling agent and conventional phosphate-free corrosion inhibition antisludging agent product, and through the scale-inhibiting properties of modification procedure after product, be significantly improved.
2. corrosion inhibition evaluation--rotary hanging plate etching test
Respectively take Songhua River System, ChangJiang River, Yellow River System, northwest quality of groundwater as foundation, having contrasted product of the present invention and commercially available traditional phosphorus is the corrosion inhibition of corrosion inhibiting and descaling agent and conventional phosphate-free corrosion inhibition antisludging agent product, test method is with reference to GB/T18175-2000,45 ℃ of experimental temperatures, experimental period 144 hours; Lacing film adopts A3 II shaped steel sheet, every group parallel two.
Table 2 inhibition experiment water quality:
Table 3 inhibition experimental result:
Figure BDA0000371453040000062
As can be seen from Table 3, the novel non-phosphate environment-protective water treatment agent of the present invention preparation is better than traditional phosphorous medicament and commercially available without phosphorus pharmaceutical products aspect corrosion inhibition, for the water quality in different basins, good corrosion mitigating effect is arranged.

Claims (10)

1. Phosphateless environmentally friendly water treatment agent, it is characterized in that being made by the preparation method who comprises following reactions steps: the copolyreaction that the graft reaction of natural high moleculer eompound and maleic anhydride obtains maleic anhydride graft natural high moleculer eompound, maleic anhydride graft natural high moleculer eompound and acrylic monomer obtains multipolymer.
2. water treatment agent as claimed in claim 1, is characterized in that in the preparation method also comprising the modification step to the gained multipolymer.
3. the preparation method of a Phosphateless environmentally friendly water treatment agent, it is characterized by to have adopted and comprise following synthetic reaction process: the copolyreaction that the graft reaction of natural high moleculer eompound and maleic anhydride obtains maleic anhydride graft natural high moleculer eompound, maleic anhydride graft natural high moleculer eompound and acrylic monomer obtains multipolymer, be water treatment agent A, wherein
Natural high moleculer eompound and maleic anhydride graft reaction process comprise: (1) takes the soft water of counting by weight 400-600 part and joins in stainless steel cauldron, stirs; (2) will take the natural high moleculer eompound of counting by weight 100-300 part and join in aforesaid reaction vessel, and heat up and make its dissolving; (3) the powdery solid maleic anhydride that will count by weight 40-80 part at the uniform velocity joins in reactor; (4) add in the process of maleic anhydride powder, constantly drip the pH value in sodium hydroxide solution control reactor; (5) powder add complete after, be warming up to 10 ℃-80 ℃, continue reaction 1-4 hour, below the interior material pH value to 8 of sour conditioned reaction still, obtain product maleic anhydride graft natural high moleculer eompound;
Wherein also comprise in above-mentioned steps (3) and add the catalyst sulfuric acid titanium of counting by weight 2-6 part simultaneously in reactor;
The copolyreaction process of maleic anhydride graft natural high moleculer eompound and acrylic monomer comprises: the catalyzer that (1) will count 1-7 part by weight adds in the reactor of product maleic anhydride graft natural high moleculer eompound place, heats up catalyzer is dissolved fully; (2) acrylic monomer of take initiator solution, counting by weight 60-100 part is added dropwise to reactor.(3) above-mentioned material dropping complete after, be warming up to 60 ℃-100 ℃, continue reaction 1-4 hour, obtain multipolymer, i.e. water treatment agent A.
4. synthetic method according to claim 3, it is characterized in that in described natural high moleculer eompound and maleic anhydride graft reaction process, described natural high moleculer eompound is a kind of in xylogen and modification derivant, Mierocrystalline cellulose and modification derivant thereof, starch and modification derivant thereof, and wherein the lignin modification derivative is selected from a kind of in sulfonated lignin, aminated lignin, alkylation xylogen, oxidative lignin; Cellulose modified derivative is selected from a kind of in etherified cellulose, esterified cellulose; The starch conversion derivative is selected from a kind of in modified starch, dextran.
5. synthetic method according to claim 3, is characterized in that wherein in natural high moleculer eompound and maleic anhydride graft reaction process, and dripping the pH value that sodium hydroxide solution controls in reactor in step (4) is between 6-10.
6. synthetic method according to claim 3, it is characterized in that in described maleic anhydride graft natural high moleculer eompound and acrylic monomer polymerization process, the acrylic monomer in step (2) comprises one or more in vinylformic acid, methyl acrylate, ethyl propenoate, Propylene glycol monoacrylate, methacrylic acid, methyl methacrylate, β-dimethyl-aminoethylmethacrylate.
7. synthetic method according to claim 3, it is characterized in that in described maleic anhydride graft natural high moleculer eompound and acrylic monomer polymerization process, the initiator solution described in step (2) is one or more in azo, peroxide, redox class initiator.
8. synthetic method according to claim 3, it is characterized in that in described maleic anhydride graft natural high moleculer eompound and acrylic monomer polymerization process, its step (1) used catalyst is inorganic molysite, and wherein said inorganic molysite comprises a kind of in ferrous ammonium sulphate, ferrous sulfate, iron protochloride, iron(ic) chloride, ferric sulfate.
9. as synthetic method as described in claim 3-8 any one, characterized by further comprising the modification step of water treatment agent, wherein the modification step comprises: (1) obtains the copolyreaction gained multipolymer of maleic anhydride graft natural high moleculer eompound and acrylic monomer the thick product of brown after underpressure distillation; (2) control temperature 5-50 ℃, drip the vitriol oil in above-mentioned product, interval time the assaying reaction thing acid number, and calculate sulfonation degree,, when product reaches predetermined sulfonation degree, finish sulfonation reaction; (3) use again in sodium hydroxide solution and the excessive vitriol oil, obtain the water treatment agent B after modification.
10. synthetic method according to claim 9, is characterized in that in described modification step, and the predetermined sulfonation degree of the described multipolymer of step (2) should be controlled in 20~50%.
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Cited By (10)

* Cited by examiner, † Cited by third party
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CN103964589A (en) * 2014-04-24 2014-08-06 宋晶冰 Preparation method for novel non-phosphorus corrosion inhibitor applied to circulating water system
CN106145396A (en) * 2016-08-09 2016-11-23 丁玉琴 A kind of preparation method of Phosphateless environmentally friendly dirt dispersion agent
CN107244752A (en) * 2017-06-09 2017-10-13 武汉理工大学 A kind of efficient and environment-friendly type anti-incrustation corrosion inhibitor and its preparation
CN107619117A (en) * 2016-07-13 2018-01-23 中国石油化工股份有限公司 Non-phosphate inhibitor and its preparation method and application and water treatment composition and its application
CN107720982A (en) * 2017-11-07 2018-02-23 安徽大学 A kind of without phosphorus water treatment agent and preparation method thereof
CN108439618A (en) * 2018-03-14 2018-08-24 兖矿水煤浆气化及煤化工国家工程研究中心有限公司 A kind of coal gasification buck scale preventative and preparation method thereof
CN110407331A (en) * 2019-06-12 2019-11-05 李辉 A kind of preparation method of green sustained release antisludging agent
CN111362429A (en) * 2020-02-28 2020-07-03 中国石油天然气股份有限公司 Non-phosphorus scale inhibitor and preparation method and application thereof
CN113415908A (en) * 2021-05-19 2021-09-21 河北津宏化工有限公司 Modified hydrolyzed polymaleic anhydride water treatment agent and preparation method thereof
CN117164128A (en) * 2023-11-03 2023-12-05 烟台康恩环保科技有限公司 Organic scale and corrosion inhibitor for high-dissolved-oxygen water quality and preparation method thereof

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CN103964589B (en) * 2014-04-24 2015-10-21 宋晶冰 A kind of non-phosphate inhibitor preparation method being applied to circulating water system
CN103964589A (en) * 2014-04-24 2014-08-06 宋晶冰 Preparation method for novel non-phosphorus corrosion inhibitor applied to circulating water system
CN107619117B (en) * 2016-07-13 2019-11-12 中国石油化工股份有限公司 Non-phosphate inhibitor and its preparation method and application and water treatment composition and its application
CN107619117A (en) * 2016-07-13 2018-01-23 中国石油化工股份有限公司 Non-phosphate inhibitor and its preparation method and application and water treatment composition and its application
CN106145396A (en) * 2016-08-09 2016-11-23 丁玉琴 A kind of preparation method of Phosphateless environmentally friendly dirt dispersion agent
CN107244752A (en) * 2017-06-09 2017-10-13 武汉理工大学 A kind of efficient and environment-friendly type anti-incrustation corrosion inhibitor and its preparation
CN107720982A (en) * 2017-11-07 2018-02-23 安徽大学 A kind of without phosphorus water treatment agent and preparation method thereof
CN108439618A (en) * 2018-03-14 2018-08-24 兖矿水煤浆气化及煤化工国家工程研究中心有限公司 A kind of coal gasification buck scale preventative and preparation method thereof
CN110407331A (en) * 2019-06-12 2019-11-05 李辉 A kind of preparation method of green sustained release antisludging agent
CN111362429A (en) * 2020-02-28 2020-07-03 中国石油天然气股份有限公司 Non-phosphorus scale inhibitor and preparation method and application thereof
CN111362429B (en) * 2020-02-28 2022-06-03 中国石油天然气股份有限公司 Non-phosphorus scale inhibitor and preparation method and application thereof
CN113415908A (en) * 2021-05-19 2021-09-21 河北津宏化工有限公司 Modified hydrolyzed polymaleic anhydride water treatment agent and preparation method thereof
CN113415908B (en) * 2021-05-19 2022-04-29 河北津宏化工有限公司 Modified hydrolyzed polymaleic anhydride water treatment agent and preparation method thereof
CN117164128A (en) * 2023-11-03 2023-12-05 烟台康恩环保科技有限公司 Organic scale and corrosion inhibitor for high-dissolved-oxygen water quality and preparation method thereof
CN117164128B (en) * 2023-11-03 2024-01-02 烟台康恩环保科技有限公司 Organic scale and corrosion inhibitor for high-dissolved-oxygen water quality and preparation method thereof

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