CN103771599B - The treatment process of non-Phosphorus composite anti incrustation eorrosion snhibiter and application and recirculated water - Google Patents
The treatment process of non-Phosphorus composite anti incrustation eorrosion snhibiter and application and recirculated water Download PDFInfo
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- CN103771599B CN103771599B CN201210411697.2A CN201210411697A CN103771599B CN 103771599 B CN103771599 B CN 103771599B CN 201210411697 A CN201210411697 A CN 201210411697A CN 103771599 B CN103771599 B CN 103771599B
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/08—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
- C23F11/10—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
- C23F11/173—Macromolecular compounds
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/08—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
- C23F11/10—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F14/00—Inhibiting incrustation in apparatus for heating liquids for physical or chemical purposes
- C23F14/02—Inhibiting incrustation in apparatus for heating liquids for physical or chemical purposes by chemical means
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Abstract
The invention discloses the treatment process of a kind of non-Phosphorus composite anti incrustation eorrosion snhibiter and application and recirculated water.This non-Phosphorus composite anti incrustation eorrosion snhibiter contains Scale inhibitors, dispersion agent, organic non-phosphate inhibitor and manganese salt, described Scale inhibitors is poly aspartic acid and/or poly-epoxy succinic acid, the weight ratio of described Scale inhibitors, dispersion agent, organic non-phosphate inhibitor and manganese salt is 1:0.2-10:0.5-100:0.025-1, and wherein the weight of manganese salt is by mn ion.Non-Phosphorus composite anti incrustation eorrosion snhibiter of the present invention and non-oxidative bactericide particularly isothiazolinone have good synergistic effect, can significantly improve the sterilization effect of non-oxidative bactericide, show as that sterilization is fast and effective drug duration is long.Non-Phosphorus composite anti incrustation eorrosion snhibiter of the present invention is environmentally friendly in addition, have without phosphorus, without the characteristic of nitrogen, meet the requirement of environmental protection, alleviate environmental pressure; And the subject range of non-Phosphorus composite anti incrustation eorrosion snhibiter of the present invention to water quality is wide, be easy to apply.
Description
Technical field
The present invention relates to the treatment process of a kind of non-Phosphorus composite anti incrustation eorrosion snhibiter and application and recirculated water, particularly, relate to a kind of non-Phosphorus composite anti incrustation eorrosion snhibiter and the application in circulating water treatment thereof and utilize the circulating water treatment method of this non-Phosphorus composite anti incrustation eorrosion snhibiter.
Background technology
Water is the primary condition that the mankind depend on for existence, but water resources is limited in the world.The water yield per capita of China be only the world per capita the water yield 1/4th, water resources is more poor.Along with the high speed development of industry, the eubiosis of water is subject to havoc.For solving water resources crisis, adapt to Sustainable development, must rationally water saving.Cooling water amount in process water accounts for the 60-80 % by weight of total water consumption, and therefore, the major objective of saving process water recycles water coolant, improves repeating utilization factor as much as possible, reduce blowdown simultaneously.But in water coolant use procedure, along with constantly circulating and concentrating, the content of water mineral also can constantly increase, and exacerbates pipeline and equipment corrosion and scale problems, so water conditioner must be added to improve the quality of water coolant in water coolant, thus ensure equipment safety operation.
At present, to anti-incrustation corrosion inhibitor research in water conditioner the most active be organic phosphoric acid anti-incrustation corrosion inhibitor and copolymer anti-scale disperser.Organic phosphoric acid compound particularly organic multicomponent phosphoric acid and salt thereof has stable chemical performance, higher temperature resistant and higher pH and the obvious feature such as " threshold effect " and " synergistic effect ", therefore its appearance water technology is striden forward major step, a now widely used class water conditioner, as ATMP, HEDP, PBTCA etc.But organic phosphoric acid compound effectively can not suppress calcium phosphate scale, zinc dirt and solve the problems such as iron oxide precipitation, and itself easily forms organic phosphoric acid dirt.In addition, because phosphorous water conditioner degraded discharges inorganic phosphorus, make phosphorous in recirculated water draining and cause environmental pollution, and along with the reinforcement of people's environmental consciousness and the increasingly strict of respective environment regulation, environmental administration starts to limit the use to phosphorus, such as Germany requires that the discharge of phosphorus is less than or equal to 1mg/L, so the application of organic phosphoric acid compound is restricted.Therefore the important topic that low-phosphorous or without phosphorus novel green anti-incrustation corrosion inhibitor has become domestic and international water conditioner aspect research is developed.
Common non-phosphorus scale and corrosion inhibitor formula mainly comprises poly-epoxy succinic acid or poly aspartic acid, without phosphorus containing carboxylic acid group polymer, non-phosphate inhibitor and zinc salt.Zinc salt more than in formula can form zinc hydroxide precipitation in metallic surface and cover cathode surface, thus forms cathodic corrosion inhibitor film and reduce corrosion of metal.
In the treatment process of recirculated water, also need while adding anti-incrustation corrosion inhibitor to add sterilant to suppress microbial growth in recirculated water, but when using the above-mentioned anti-incrustation corrosion inhibitor containing zinc salt, anti-incrustation corrosion inhibitor and sterilant are without remarkable synergistic effect, when particularly using isothiazolinone as sterilant, sterilant takes effect slow and effective drug duration is short.
Summary of the invention
The object of the invention is to overcome the deficiencies in the prior art, providing a kind of has the non-Phosphorus composite anti incrustation eorrosion snhibiter of better synergistic effect and the treatment process of application and recirculated water thereof with sterilant.
To achieve these goals, on the one hand, the invention provides a kind of non-Phosphorus composite anti incrustation eorrosion snhibiter, it is characterized in that, this non-Phosphorus composite anti incrustation eorrosion snhibiter contains Scale inhibitors, dispersion agent, organic non-phosphate inhibitor and manganese salt, described Scale inhibitors is poly aspartic acid and/or poly-epoxy succinic acid, and the weight ratio of described Scale inhibitors, dispersion agent, organic non-phosphate inhibitor and manganese salt is 1:0.2-10:0.5-100:0.025-1, and wherein the weight of manganese salt is by mn ion.
On the other hand, the invention provides the application of above-mentioned non-Phosphorus composite anti incrustation eorrosion snhibiter in circulating water treatment.
Again on the one hand, the invention provides a kind for the treatment of process of recirculated water, it is characterized in that, the method comprises and add above-mentioned non-Phosphorus composite anti incrustation eorrosion snhibiter and sterilant in recirculated water.
The present inventor finds, non-Phosphorus composite anti incrustation eorrosion snhibiter of the present invention and non-oxidative bactericide particularly isothiazolinone have good synergistic effect, can significantly improve the sterilization effect of isothiazolinone, show as sterilization soon and effective drug duration long.Non-Phosphorus composite anti incrustation eorrosion snhibiter of the present invention is environmentally friendly in addition, avoids using P contained compound, have without phosphorus, without the characteristic of nitrogen, meet the requirement of environmental protection, alleviate environmental pressure; Non-Phosphorus composite anti incrustation eorrosion snhibiter of the present invention to calcium and alkali tolerance high, wide to the subject range of water quality, to total hardness and total alkalinity sum at 300mgL
-1above water quality and total hardness and total alkalinity sum are at 100mgL
-1following water quality all has excellent anticorrosion-antiscaling property, is easy to apply.
Other features and advantages of the present invention are described in detail in embodiment part subsequently.
Embodiment
Below the specific embodiment of the present invention is described in detail.Should be understood that, embodiment described herein, only for instruction and explanation of the present invention, is not limited to the present invention.
Non-Phosphorus composite anti incrustation eorrosion snhibiter of the present invention contains Scale inhibitors, dispersion agent, organic non-phosphate inhibitor and manganese salt, described Scale inhibitors is poly aspartic acid and/or poly-epoxy succinic acid, the weight ratio of described Scale inhibitors, dispersion agent, organic non-phosphate inhibitor and manganese salt is 1:0.2-10:0.5-100:0.025-1, be preferably 1:1-2.5:2.5-30:0.125-0.5, wherein the weight of manganese salt is by mn ion.
According to the present invention, described manganese salt can be the manganese salt of any solubility, as long as can produce Mn after being added in recirculated water
2+, under preferable case, described manganese salt is one or more in Manganous chloride tetrahydrate, manganous sulfate and manganous nitrate.
According to the present invention, described dispersion agent can be the polymkeric substance containing carboxylic acid group polymer and/or acid anhydrides that the main various this areas routine playing dissemination uses, such as, can be the multipolymer of carboxylic acid or its acid anhydrides and/or the multipolymer of carboxylic acid or its acid anhydrides and sulfonate.Under preferable case, described dispersion agent is polyacrylic acid, polymaleic acid, polymaleic anhydride, the multipolymer of vinylformic acid and acrylate, toxilic acid and acrylic acid multipolymer, maleic anhydride and acrylic acid multipolymer, the multipolymer of toxilic acid and styrene sulfonic acid, the multipolymer of maleic anhydride and styrene sulfonic acid, the multipolymer of vinylformic acid and styrene sulfonic acid, the multipolymer of acrylate and styrene sulfonic acid, the multipolymer of toxilic acid and allyl sulphonic acid, the multipolymer of maleic anhydride and allyl sulphonic acid, the multipolymer of vinylformic acid and allyl sulphonic acid, the multipolymer of vinylformic acid and vinyl sulfonic acid, the multipolymer of vinylformic acid and 2-acrylamide-2-methylpro panesulfonic acid, the multipolymer of vinylformic acid and acrylamide and 2-acrylamide-2-methylpro panesulfonic acid, the multipolymer of vinylformic acid and acrylate and 2-acrylamide-2-methylpro panesulfonic acid, the multipolymer of vinylformic acid and toxilic acid and 2-acrylamide-2-methylpro panesulfonic acid, one or more in the multipolymer of vinylformic acid and Propylene glycol monoacrylate and 2-acrylamide-2-methylpro panesulfonic acid.
Wherein, described acrylate can be vinylformic acid C
1-8ester, such as vinylformic acid C
1-8alkyl ester and/or vinylformic acid C
1-8hydroxy alkyl ester, be preferably in methyl acrylate, ethyl propenoate and Propylene glycol monoacrylate one or more.It should be noted that: initiator system during above-mentioned Macroscopic single crystal has two, one is phosphorous inferior sodium phosphate and ammonium persulphate initiator system; Another is without phosphorus Sodium Pyrosulfite and ammonium persulphate initiator system, consider the pollution of phosphorus to environment, the initiator system during Macroscopic single crystal that the present invention uses is preferably Sodium Pyrosulfite and ammonium persulphate initiator system, the concrete synthesis step of above-mentioned polymkeric substance is well known to those skilled in the art, does not repeat them here.
According to the present invention, described organic non-phosphate inhibitor can be the various inhibiter that this area routine uses, and is preferably one or more in organic Amine Cation Type inhibiter, Thiourea Type inhibiter, tartrate salt form inhibiter and gluconic acid salt form inhibiter.
Preferably, described organic Amine Cation Type inhibiter is one or more in urotropine, tetrahydroglyoxaline, glyoxal ethyline quinoline, morpholine, piperazine, 2-methylpiperazine and Isosorbide-5-Nitrae-lupetazin.
Preferably, described Thiourea Type inhibiter is one or more in thiocarbamide, methylthiourea, ethyl thiourea, diphenyl thiourea, thiosinamine and tolylthiourea.
Preferably, described tartrate salt form inhibiter and gluconic acid salt form inhibiter are the organic acid salt of solubility.As described in tartrate salt form inhibiter be more preferably sodium tartrate.As described in gluconic acid salt form inhibiter be more preferably Sunmorl N 60S.
According to the present invention, described anti-incrustation corrosion inhibitor can also contain copper material corrosion inhibitor, to strengthen the function that non-Phosphorus composite anti incrustation eorrosion snhibiter of the present invention suppresses copper corrosion further.The weight ratio of described copper material corrosion inhibitor and described Scale inhibitors can be 0.025-0.75:1.The nitrogen azole material that described copper material corrosion inhibitor can be commonly used for this area, is preferably mercaptobenzothiazole and/or benzotriazole.
The present invention also provides the application of above-mentioned non-Phosphorus composite anti incrustation eorrosion snhibiter in circulating water treatment.Wherein, the consumption of described non-Phosphorus composite anti incrustation eorrosion snhibiter is preferably 16.5-243.5mg/L recirculated water, is more preferably 33-61mg/L recirculated water.
The treatment process of recirculated water provided by the invention, is characterized in that, the method comprises and add above-mentioned non-Phosphorus composite anti incrustation eorrosion snhibiter and sterilant in recirculated water.
According to the present invention, described sterilant preferably includes oxidative bactericide and non-oxidative bactericide.Non-Phosphorus composite anti incrustation eorrosion snhibiter and sterilant can add in recirculated water simultaneously, also can add respectively.Wherein sterilant can microorganism effectively in controlled circulation water and in the treating processes of recirculated water, the method that usual employing oxidative bactericide and non-oxidative bactericide are used alternatingly, the principle be used alternatingly and method are well known to those skilled in the art, and therefore repeat no more.
Wherein, described oxidative bactericide can be selected from one or more in liquid chlorine, clorox, dioxide peroxide, trichloroisocyanuric acid, DICHLOROISOCYANURIC ACID, bromochlorodimethyl hydanton and dibromo dimethyl hydantoin.The consumption of described oxidative bactericide can be 0.5-30mg/L recirculated water usually.
Described non-oxidative bactericide can be selected from CMIT, MIT, glutaraldehyde, dodecyl benzyl dimethyl ammonium chloride, dodecyl dimethyl benzyl ammonium bromide, myristyl benzyl dimethyl ammonium chloride, tetradecyl tributyl phosphorus chloride, 2, one or more in 2-bis-bromo-3-nitrilo propionic acid amide and 2-bromo-2-nitro-1,3-propylene glycol.The consumption of described non-oxidative bactericide can be 5-100mg/L recirculated water usually.
In circulating water treatment method of the present invention, described non-Phosphorus composite anti incrustation eorrosion snhibiter and the sterilizing rate that isothiazolinone is composite when using are improved, and its reason may be the Mn in described non-Phosphorus composite anti incrustation eorrosion snhibiter
2+have good synergistic effect with described isothiazolinone, therefore preferred described non-oxidative bactericide is isothiazolinone.Described isothiazolinone is the commercial sterilization mould inhibitor of a class broad-spectrum high efficacy, can by commercially available, the effective constituent of described isothiazolinone is CMIT and MIT, and the weight ratio of the two can be 2-5:1 usually, be preferably 3:1, but be not limited thereto.When using non-Phosphorus composite anti incrustation eorrosion snhibiter of the present invention and isothiazolinone disinfecting agent cycle for the treatment of water, the bactericidal property of isothiazolinone can be improved.
According to the present invention, the consumption of described non-Phosphorus composite anti incrustation eorrosion snhibiter can be 16.5-243.5mg/L recirculated water.
According to the present invention, as long as prepare described non-Phosphorus composite anti incrustation eorrosion snhibiter according to aforementioned base materials formula can realize object of the present invention, described non-Phosphorus composite anti incrustation eorrosion snhibiter can be prepared before use, as added after each raw material mixing again in recirculated water according to aforementioned formula; Also each raw material directly can be added in recirculated water without mixing step according to aforementioned formula.
According to the present invention, process total hardness and total alkalinity sum at 300mgL
-1during above water quality, generally adopt sour adjust pH technique, namely first add non-Phosphorus composite anti incrustation eorrosion snhibiter of the present invention, adding sour control ph is again 6.5-8.5, be preferably 7.8-8.3, the various acid that described acid can be commonly used for this area, such as sulfuric acid and/or nitric acid.
Below will be described the present invention by embodiment.
In following examples, the water quality testing former water is as shown in table 1, will test former water 1 and 2 respectively and concentrate 5 times as test water 1 and 2, will test former water 3 and concentrate 3 times as test water 3, wherein Ca
2+, total alkalinity and total hardness be all with CaCO
3meter, Ca
2+represent calcium hardness, the measuring method of each parameter is as follows:
Ca
2+: reference standard GB/T6910-2006;
Total alkalinity: reference standard GB/T15451-2006;
Total hardness: reference standard GB/T6909-2008;
Cl
-: reference standard GB/T15453-2008;
SO
4 2-: reference standard GB/T14642-2009;
PH value: reference standard GB/T6920-1986;
Specific conductivity: reference standard GB/T6908-2008;
Total molten solid: reference standard GB/T14415-2007;
Table 1
In following examples, " blank sample " represents and does not add any medicament (anti-incrustation corrosion inhibitor and/or sterilant) but other treatment steps test water sample identical with test (or test) step.
Sterilizing rate has reacted the sterilization effect of non-Phosphorus composite anti incrustation eorrosion snhibiter and bactericide compounded use described in specified time, and the calculation formula of sterilizing rate is:
The bacteria containing amount of sterilizing rate=(bacteria containing amount of bacteria containing amount-certain time sample of blank sample) × 100%/blank sample;
Scale inhibition performance is defined as the scale inhibition efficiency of corrosion inhibiting and descaling agent, and the calculation formula of scale inhibition performance is:
Scale inhibition performance=(C-C
0)/(nC
1-C
0) × 100%, wherein,
C: remain Ca in water after cooling
2+concentration (mg/L)
C
0: the Ca of blank sample
2+concentration (mg/L)
C
1: the Ca in former water
2+concentration (mg/L)
N: cycles of concentration
Average corrosion rate is defined as the inhibition efficiency of corrosion inhibiting and descaling agent, and the calculation formula of average corrosion rate (F) is: F=(C × △ W)/(A × T × ρ), wherein,
C: computational constant, with mm/a(millimeter/year) for unit time, C=8.76 × 10
7
△ W: the corrosion weight loss (g) of test specimen
A: the area (cm of test specimen
2)
T: corrosion test time (h)
ρ: the density (kg/m of material for test
3)
The polymkeric substance used in embodiment is as follows:
Poly aspartic acid (PASP,
active quantities is 40%), the multipolymer of T225(vinylformic acid and 2-acrylamide-2-methylpro panesulfonic acid, AA/HPA, the weight ratio of each structural unit is 4/1, active quantities is 30%, when 30 DEG C, Limiting Viscosity is 0.072dl/g), vinylformic acid and 2-acrylamide-2-methylpro panesulfonic acid and Propylene glycol monoacrylate multipolymer (AA/AMPS/HPA, the weight ratio of each structural unit is 14/3/3, and active quantities is 30%, when 30 DEG C, Limiting Viscosity is 0.081dl/g), poly-epoxy succinic acid (PESA
active quantities is 40%), vinylformic acid and Propylene glycol monoacrylate and maleic acid (AA/HPA/MA, the weight ratio of each structural unit is 14/3/3, active quantities is 30%, when 30 DEG C, Limiting Viscosity is 0.073dl/g), vinylformic acid and 2-acrylamide-2-methylpro panesulfonic acid multipolymer (AA/AMPS, the weight ratio of each structural unit is 7/3, active quantities is 30%, when 30 DEG C, Limiting Viscosity is 0.075dl/g), toxilic acid and Styrene Sulfonic Acid Copolymer (MA/SS, the weight ratio of each structural unit is 7/3, active quantities is 30%, when 30 DEG C, Limiting Viscosity is 0.072dl/g), polyacrylic acid (PAA,
active quantities is 50%, when 30 DEG C, Limiting Viscosity is 0.073dl/g), vinylformic acid and acrylamide and 2-acrylamide-2-methylpro panesulfonic acid multipolymer (AA/AM/AMPS, active quantities is 30%, the weight ratio of each structural unit is 14/3/3, when 30 DEG C, Limiting Viscosity is 0.073dl/g), polymaleic anhydride (PMAH
active quantities is 50%), vinylformic acid and allyl sulphonic acid multipolymer (AA/AS, active quantities is 30%, the weight ratio of each structural unit is 7/3, when 30 DEG C, Limiting Viscosity is 0.073dl/g), vinylformic acid and Styrene Sulfonic Acid Copolymer (AA/SS, active quantities is 30%, the weight ratio of each structural unit is 7/3, when 30 DEG C, Limiting Viscosity is 0.072dl/g), vinylformic acid and toxilic acid and 2-acrylamide-2-methylpro panesulfonic acid multipolymer (AA/MA/AMPS, active quantities is 30%, the weight ratio of each structural unit is 14/3/3, when 30 DEG C, Limiting Viscosity is 0.072dl/g), toxilic acid and acrylic copolymer (MA/AA, active quantities is 30%, the weight ratio of each structural unit is 7/3, when 30 DEG C, Limiting Viscosity is 0.072dl/g), (active quantities is 30% for methyl acrylate and Styrene Sulfonic Acid Copolymer, the weight ratio of each structural unit is 7/3, when 30 DEG C, Limiting Viscosity is 0.072dl/g), isothiazolinone (both CMIT and MIT mixture, the two weight ratio is 3:1, effective content is 1.6%, Beijing Tianqing Chemical Co., Ltd.), (effective content is 45% to dodecyl benzyl dimethyl ammonium chloride, the calm and peaceful water treatment company limited in Shandong).
Embodiment 1
Respectively to test water 1,2,3(sulfuric acid regulates the pH value of test water within the scope of 7.8-8.3) in add poly aspartic acid, thiocarbamide, T225, Manganous sulfate monohydrate and isothiazolinone, make poly aspartic acid in water, thiocarbamide, T225, Mn
2+4mg/L, 100mg/L, 8mg/L, 1mg/L and 50mg/L is respectively with the concentration of isothiazolinone.
Embodiment 2
Respectively to test water 1,2,3(sulfuric acid regulates the pH value of test water within the scope of 7.8-8.3) in add poly-epoxy succinic acid, methylthiourea, AA/HPA/MA, Manganous chloride tetrahydrate and isothiazolinone, make poly-epoxy succinic acid in water, methylthiourea, AA/HPA/MA, Mn
2+6mg/L, 110mg/L, 9mg/L, 1.5mg/L and 80mg/L is respectively with the concentration of isothiazolinone.
Embodiment 3
Respectively to test water 1,2,3(sulfuric acid regulates the pH value of test water within the scope of 7.8-8.3) in add poly aspartic acid, urotropine (Jinan Da Rui Chemical Co., Ltd.), AA/AMPS/HPA, Manganous sulfate monohydrate and isothiazolinone, make poly aspartic acid in water, urotropine, AA/AMPS/HPA, Mn
2+8mg/L, 120mg/L, 10mg/L, 2mg/L and 100mg/L is respectively with the concentration of isothiazolinone.
Embodiment 4
In test water 1,2,3, each material is added according to the mode of embodiment 3, unlike, isothiazolinone is replaced by dodecyl benzyl dimethyl ammonium chloride.
Comparative example 1
In test water 1,2,3, each material is added according to the mode of embodiment 3, unlike, Manganous sulfate monohydrate is replaced by Zinc vitriol.
Comparative example 2
Respectively to test water 1,2,3(sulfuric acid regulates the pH value of test water within the scope of 7.8-8.3) in add isothiazolinone, make the concentration of isothiazolinone in water be 100mg/L.
Comparative example 3
Respectively to test water 1,2,3(sulfuric acid regulates the pH value of test water within the scope of 7.8-8.3) in add dodecyl benzyl dimethyl ammonium chloride, make the concentration of dodecyl benzyl dimethyl ammonium chloride in water be 100mg/L.
Embodiment 5
Respectively to test water 1,2,3(sulfuric acid regulates the pH value of test water within the scope of 7.8-8.3) in add poly-epoxy succinic acid, Sunmorl N 60S, MA/SS, polyacrylic acid, Manganous sulfate monohydrate and isothiazolinone, make poly-epoxy succinic acid in water, Sunmorl N 60S, MA/SS, polyacrylic acid, Mn
2+9mg/L, 25mg/L, 5mg/L, 5mg/L, 1.25mg/L and 80mg/L is respectively with the concentration of isothiazolinone.
Embodiment 6
Respectively to test water 1,2,3(sulfuric acid regulates the pH value of test water within the scope of 7.8-8.3) in add poly-epoxy succinic acid, poly aspartic acid, sodium tartrate, AA/HPA/MA, Manganous sulfate monohydrate and isothiazolinone, make poly-epoxy succinic acid in water, poly aspartic acid, sodium tartrate, AA/HPA/MA, Mn
2+4mg/L, 4mg/L, 40mg/L, 8mg/L, 1.5mg/L and 80mg/L is respectively with the concentration of isothiazolinone.
Embodiment 7
Respectively to test water 1,2,3(sulfuric acid regulates the pH value of test water within the scope of 7.8-8.3) in add poly-epoxy succinic acid, poly aspartic acid, 2-methylpiperazine (Heze San Heyuan Chemical Co., Ltd.), AA/AM/AMPS, polymaleic anhydride and Manganous sulfate monohydrate, make poly-epoxy succinic acid in water, poly aspartic acid, 2-methylpiperazine, AA/AM/AMPS, polymaleic anhydride and Mn
2+concentration be respectively 2mg/L, 2mg/L, 80mg/L, 4mg/L, 4mg/L and 0.5mg/L.
Embodiment 8
Respectively to test water 1,2,3(sulfuric acid regulates the pH value of test water within the scope of 7.8-8.3) in add poly-epoxy succinic acid, poly aspartic acid, thiosinamine, AA/AS and Manganous sulfate monohydrate, make poly-epoxy succinic acid in water, poly aspartic acid, thiosinamine, AA/AS and Mn
2+concentration be respectively 8mg/L, 6mg/L, 150mg/L, 6mg/L and 2mg/L.
Embodiment 9
Respectively to test water 1,2,3(sulfuric acid regulates the pH value of test water within the scope of 7.8-8.3) in add poly-epoxy succinic acid, glyoxal ethyline quinoline (fine chemicals factory of Dandong City), diphenyl thiourea, AA/SS and Manganous sulfate monohydrate, make poly-epoxy succinic acid in water, glyoxal ethyline quinoline, diphenyl thiourea, AA/SS and Mn
2+concentration be respectively 2mg/L, 80mg/L, 80mg/L, 15mg/L and 2mg/L.
Embodiment 10
Respectively to test water 1,2,3(sulfuric acid regulates the pH value of test water within the scope of 7.8-8.3) in add poly-epoxy succinic acid, poly aspartic acid, 1,4-lupetazin (Guang Tuo Chemical Co., Ltd.), tolylthiourea, AA/MA/AMPS and Manganous sulfate monohydrate, make poly-epoxy succinic acid in water, poly aspartic acid, Isosorbide-5-Nitrae-lupetazin, tolylthiourea, AA/MA/AMPS and Mn
2+concentration be respectively 8mg/L, 8mg/L, 100mg/L, 80mg/L, 20mg/L and 2mg/L.
Embodiment 11
Respectively to test water 1,2,3(sulfuric acid regulates the pH value of test water within the scope of 7.8-8.3) in add poly aspartic acid, morpholine, Sunmorl N 60S, MA/AA, methyl acrylate and Styrene Sulfonic Acid Copolymer and Manganous sulfate monohydrate, make poly aspartic acid in water, morpholine, Sunmorl N 60S, MA/AA, methyl acrylate and Styrene Sulfonic Acid Copolymer and Mn
2+concentration be respectively 14mg/L, 200mg/L, 10mg/L, 5mg/L, 5mg/L and 2mg/L.
Comparative example 4
Respectively to test water 1,2,3(sulfuric acid regulates the pH value of test water within the scope of 7.8-8.3) in add the 2-phosphate-1 that active ingredient is 50%, 2,4-butane tricarboxylate (PBTCA) and hydroxy ethylene diphosphonic acid (HEDP), AA/AMPS and Zinc vitriol, make PBTCA, HEDP, AA/AMPS and Zn in water
2+concentration be respectively 8mg/L, 6mg/L, 9mg/L and 2mg/L.
The mensuration of sterilization effect
Measure the bacteria containing amount in the water of blank sample, embodiment 1-6 and comparative example 1-3 after 4h, 24h, 48h, 72h respectively and calculate sterilizing rate, measuring method is with reference to the regulation of " the static bactericidal assay of heterotrophic bacterium " in " water coolant analysis and the test method " of production department of China PetroChemical Corporation and development division establishment.Result is as shown in table 2, and the "/" in table 2 represents and calculates.
Table 2
In upper table, the results contrast of embodiment 1-3 and comparative example 1-2 can be found out, non-Phosphorus composite anti incrustation eorrosion snhibiter of the present invention and the composite use of isothiazolinone have synergistic effect, and the sterilizing rate recorded during 4h and 72h in embodiment 1-3 is apparently higher than the sterilizing rate recorded during 4h and 72h in comparative example 2, illustrate that circulating water treatment method of the present invention sterilization is fast and effective drug duration is long; Again the results contrast of embodiment 1-3 and embodiment 4 can be found out, although the sterilant quick result that embodiment 4 uses, but effective drug duration is short, sterilizing rate in each test water is recorded all below 14% when 24h, bacteria containing amount during 48h is higher than blank sample, just there is no obvious sterilization effect, and in embodiment 1-3 each time period all show higher sterilization effect; And embodiment 4 is substantially close with the result of comparative example 3, illustrate that non-Phosphorus composite anti incrustation eorrosion snhibiter of the present invention and the composite use of dodecyl benzyl dimethyl ammonium chloride do not have synergistic effect.
So, as can be seen from the data of table 2, the sterilization effect of non-Phosphorus composite anti incrustation eorrosion snhibiter of the present invention and the composite use of isothiazolinone is obviously better than the anti-incrustation corrosion inhibitor of filling a prescription containing zinc salt and the sterilization effect of the composite use of isothiazolinone and the sterilization effect of non-Phosphorus composite anti incrustation eorrosion snhibiter of the present invention and the composite use of other non-oxidative bactericides.
The evaluation of anticorrosion-antiscaling property
In 80 ± 1 DEG C of waters bath with thermostatic control, adopt volumetric flask method to leave standstill 10h the test water having added medicament in each embodiment and comparative example, remain Ca in sampling analysis water after cooling
2+concentration, make blank sample simultaneously, and calculate scale inhibition performance.
The test piece of 20# qualitative carbon steel is fixed on lacing film instrument, put into each embodiment and comparative example has added the test water of medicament, steady temperature is 40 ± 1 DEG C, keeps rotating speed to be that 75rpm rotates 72h, the weight of test piece before and after record test, calculates average corrosion rate (F).
Evaluation result is as shown in table 3:
Table 3
The data of table 3 show, the subject range of composite scale-inhibiting corrosion inhibitor of the present invention to water quality is wide, have excellent anticorrosion-antiscaling property.
Dynamic analog test
In order to simulated field, also carry out dynamic analog test.Dynamic analog test method is undertaken by People's Republic of China (PRC) chemical industry standard HG/T2160-91, and controling parameters is as follows:
Water quality: the former water 3 in table 1
Cycles of concentration: A tower 4.0 ± 0.2B tower 4.0 ± 0.2
PH:A tower controls 8.0 ± 0.2B tower and controls 8.0 ± 0.2
Flow velocity: 1.0m/s
Medicament: A tower: the compound of embodiment 3
B tower: the compound of comparative example 1
Temperature in: 32 ± 1 DEG C of temperature difference: 10 DEG C
Dynamic analog test test tube the results are shown in Table 4.
Table 4
Specify in standard GB/T 50050-95 " Code for design of industrial recirculating cooling water treatment " 3.1.6, the erosion rate of the carbon steel tube wall of open type system is less than or equal to 0.125mm/a; In " water coolant analysis and the test method " of production department of China PetroChemical Corporation and development division establishment, " the small-sized experimental analogic method of testing laboratory " specifies that the corrosion speed of carbon steel is " very well " level between 0-0.028mm/a, being " good " level between 0.028-0.056mm/a, is " can allow " level at 0.056-0.070mm/a; Adhesion speed is " very well " level at 0-6mcm, and being " good " level at 6-15mcm, is " can allow " level at 15-20mcm.
As can be seen here, apply non-Phosphorus composite anti incrustation eorrosion snhibiter of the present invention in hard, the high-alkali water quality of former water 3(height) cycles of concentration is when being 4, the erosion rate of test tube is 0.023mm/a, reaches China Petrochemical Industry's " very well " grade standard, adhesion speed is 5.2mcm, reaches " very well " grade standard.
More than describe the preferred embodiment of the present invention in detail; but the present invention is not limited to the detail in above-mentioned embodiment, within the scope of technical conceive of the present invention; can carry out multiple simple variant to technical scheme of the present invention, these simple variant all belong to protection scope of the present invention.
It should be noted that in addition, each concrete technical characteristic described in above-mentioned embodiment, in reconcilable situation, can be combined by any suitable mode, in order to avoid unnecessary repetition, the present invention illustrates no longer separately to various possible array mode.
In addition, also can carry out arbitrary combination between various different embodiment of the present invention, as long as it is without prejudice to thought of the present invention, it should be considered as content disclosed in this invention equally.
Claims (18)
1. a non-Phosphorus composite anti incrustation eorrosion snhibiter, it is characterized in that, this non-Phosphorus composite anti incrustation eorrosion snhibiter is made up of Scale inhibitors, dispersion agent, organic non-phosphate inhibitor and manganese salt, described Scale inhibitors is poly aspartic acid and/or poly-epoxy succinic acid, the weight ratio of described Scale inhibitors, dispersion agent, organic non-phosphate inhibitor and manganese salt is 1:0.2-10:0.5-100:0.025-1, and wherein the weight of manganese salt is by mn ion.
2. non-Phosphorus composite anti incrustation eorrosion snhibiter according to claim 1, wherein, the weight ratio of described Scale inhibitors, dispersion agent, organic non-phosphate inhibitor and manganese salt is 1:1-2.5:2.5-30:0.125-0.5.
3. non-Phosphorus composite anti incrustation eorrosion snhibiter according to claim 1 and 2, wherein, described manganese salt is one or more in Manganous chloride tetrahydrate, manganous sulfate and manganous nitrate.
4. non-Phosphorus composite anti incrustation eorrosion snhibiter according to claim 1 and 2, wherein, described dispersion agent is polyacrylic acid, polymaleic acid, polymaleic anhydride, the multipolymer of vinylformic acid and acrylate, toxilic acid and acrylic acid multipolymer, maleic anhydride and acrylic acid multipolymer, the multipolymer of toxilic acid and styrene sulfonic acid, the multipolymer of maleic anhydride and styrene sulfonic acid, the multipolymer of vinylformic acid and styrene sulfonic acid, the multipolymer of acrylate and styrene sulfonic acid, the multipolymer of toxilic acid and allyl sulphonic acid, the multipolymer of maleic anhydride and allyl sulphonic acid, the multipolymer of vinylformic acid and allyl sulphonic acid, the multipolymer of vinylformic acid and vinyl sulfonic acid, the multipolymer of vinylformic acid and 2-acrylamide-2-methylpro panesulfonic acid, the multipolymer of vinylformic acid and acrylamide and 2-acrylamide-2-methylpro panesulfonic acid, the multipolymer of vinylformic acid and acrylate and 2-acrylamide-2-methylpro panesulfonic acid, the multipolymer of vinylformic acid and toxilic acid and 2-acrylamide-2-methylpro panesulfonic acid, one or more in the multipolymer of vinylformic acid and Propylene glycol monoacrylate and 2-acrylamide-2-methylpro panesulfonic acid.
5. non-Phosphorus composite anti incrustation eorrosion snhibiter according to claim 4, wherein, described acrylate is one or more in methyl acrylate, ethyl propenoate and Propylene glycol monoacrylate.
6. non-Phosphorus composite anti incrustation eorrosion snhibiter according to claim 1 and 2, wherein, described organic non-phosphate inhibitor is one or more in organic Amine Cation Type inhibiter, Thiourea Type inhibiter, tartrate salt form inhibiter and gluconic acid salt form inhibiter.
7. non-Phosphorus composite anti incrustation eorrosion snhibiter according to claim 6, wherein, described organic Amine Cation Type inhibiter is one or more in urotropine, tetrahydroglyoxaline, glyoxal ethyline quinoline, morpholine, piperazine, 2-methylpiperazine and Isosorbide-5-Nitrae-lupetazin; Described Thiourea Type inhibiter is one or more in thiocarbamide, methylthiourea, ethyl thiourea, diphenyl thiourea, thiosinamine and tolylthiourea.
8. a non-Phosphorus composite anti incrustation eorrosion snhibiter, it is characterized in that, this non-Phosphorus composite anti incrustation eorrosion snhibiter is by Scale inhibitors, dispersion agent, organic non-phosphate inhibitor, manganese salt and copper material corrosion inhibitor composition, described Scale inhibitors is poly aspartic acid and/or poly-epoxy succinic acid, described copper material corrosion inhibitor is mercaptobenzothiazole and/or benzotriazole, described Scale inhibitors, dispersion agent, the weight ratio of organic non-phosphate inhibitor and manganese salt is 1:0.2-10:0.5-100:0.025-1, wherein the weight of manganese salt is by mn ion, the weight ratio of described copper material corrosion inhibitor and described Scale inhibitors is 0.025-0.75:1.
9. non-Phosphorus composite anti incrustation eorrosion snhibiter according to claim 8, wherein, the weight ratio of described Scale inhibitors, dispersion agent, organic non-phosphate inhibitor and manganese salt is 1:1-2.5:2.5-30:0.125-0.5.
10. non-Phosphorus composite anti incrustation eorrosion snhibiter according to claim 8 or claim 9, wherein, described manganese salt is one or more in Manganous chloride tetrahydrate, manganous sulfate and manganous nitrate.
11. non-Phosphorus composite anti incrustation eorrosion snhibiters according to claim 8 or claim 9, wherein, described dispersion agent is polyacrylic acid, polymaleic acid, polymaleic anhydride, the multipolymer of vinylformic acid and acrylate, toxilic acid and acrylic acid multipolymer, maleic anhydride and acrylic acid multipolymer, the multipolymer of toxilic acid and styrene sulfonic acid, the multipolymer of maleic anhydride and styrene sulfonic acid, the multipolymer of vinylformic acid and styrene sulfonic acid, the multipolymer of acrylate and styrene sulfonic acid, the multipolymer of toxilic acid and allyl sulphonic acid, the multipolymer of maleic anhydride and allyl sulphonic acid, the multipolymer of vinylformic acid and allyl sulphonic acid, the multipolymer of vinylformic acid and vinyl sulfonic acid, the multipolymer of vinylformic acid and 2-acrylamide-2-methylpro panesulfonic acid, the multipolymer of vinylformic acid and acrylamide and 2-acrylamide-2-methylpro panesulfonic acid, the multipolymer of vinylformic acid and acrylate and 2-acrylamide-2-methylpro panesulfonic acid, the multipolymer of vinylformic acid and toxilic acid and 2-acrylamide-2-methylpro panesulfonic acid, one or more in the multipolymer of vinylformic acid and Propylene glycol monoacrylate and 2-acrylamide-2-methylpro panesulfonic acid.
12. non-Phosphorus composite anti incrustation eorrosion snhibiters according to claim 11, wherein, described acrylate is one or more in methyl acrylate, ethyl propenoate and Propylene glycol monoacrylate.
13. non-Phosphorus composite anti incrustation eorrosion snhibiters according to claim 8 or claim 9, wherein, described organic non-phosphate inhibitor is one or more in organic Amine Cation Type inhibiter, Thiourea Type inhibiter, tartrate salt form inhibiter and gluconic acid salt form inhibiter.
14. non-Phosphorus composite anti incrustation eorrosion snhibiters according to claim 13, wherein, described organic Amine Cation Type inhibiter is one or more in urotropine, tetrahydroglyoxaline, glyoxal ethyline quinoline, morpholine, piperazine, 2-methylpiperazine and Isosorbide-5-Nitrae-lupetazin; Described Thiourea Type inhibiter is one or more in thiocarbamide, methylthiourea, ethyl thiourea, diphenyl thiourea, thiosinamine and tolylthiourea.
The application of non-Phosphorus composite anti incrustation eorrosion snhibiter in 15. claim 1-14 described in any one in circulating water treatment.
16. application according to claim 15, wherein, the consumption of described non-Phosphorus composite anti incrustation eorrosion snhibiter is 16.5-243.5mg/L recirculated water.
The treatment process of 17. 1 kinds of recirculated waters, is characterized in that, the method comprises in recirculated water, to add non-Phosphorus composite anti incrustation eorrosion snhibiter in claim 1-14 described in any one and sterilant.
18. methods according to claim 17, wherein, described sterilant comprises oxidative bactericide and non-oxidative bactericide, and described non-oxidative bactericide is isothiazolinone.
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| CN108017165A (en) * | 2016-10-31 | 2018-05-11 | 中国石油化工股份有限公司 | Non-Phosphorus composite anti incrustation eorrosion snhibiter and its application and the processing method of recirculated cooling water |
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| CN114427095B (en) * | 2020-09-25 | 2024-06-04 | 中国石油化工股份有限公司 | Zinc-containing composition and application thereof |
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| CN112811614A (en) * | 2020-12-03 | 2021-05-18 | 嘉兴沃特泰科环保科技股份有限公司 | Circulating water phosphorus-free scale inhibitor and preparation method thereof |
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