CN1272255C - Method for treating reciculated cooling water containing out oil product - Google Patents

Method for treating reciculated cooling water containing out oil product Download PDF

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Publication number
CN1272255C
CN1272255C CN 200310117372 CN200310117372A CN1272255C CN 1272255 C CN1272255 C CN 1272255C CN 200310117372 CN200310117372 CN 200310117372 CN 200310117372 A CN200310117372 A CN 200310117372A CN 1272255 C CN1272255 C CN 1272255C
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acid
cooling water
recirculated cooling
multipolymer
oil product
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CN1626450A (en
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闫岩
郦和生
任志峰
李春丽
郭红卫
张春原
王亭
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INST OF BEIJING YANSHAN BRANCH CHINA PETROCHEMICAL CORP
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INST OF BEIJING YANSHAN BRANCH CHINA PETROCHEMICAL CORP
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Abstract

The present invention relates to a method for treating reciculated cooling water containing a leaked oil product, which comprises the steps: an oil product is stripped from a dispersing agent, a scale inhibitor is slowly corroded, nutrient substance for the growth of microorganism is simultaneously added in a recirculated cooling water system or is added in the recirculated cooling water system step by step, wherein the nutrient substance for the growth of microorganism contains a carbon source and a nitrogen source, the effective concentration of the carbon source in recirculated cooling water is from 1 to 3 mg/L, and the effective concentration of the nitrogen source in the recirculated cooling water is from 0.2 to 1.0 mg/L. The present invention adopts a dispersion and degradation technology so that a system can stably operate by low dirt discharge and high concentration multiple under the background of leakage. Meanwhile, the system has the advantages of stabilization, little drug consumption, guarantee of a water treatment effect, obvious water saving and discharge reduction and extension of the service life of equipment.

Description

A kind of treatment process that contains the recirculated cooling water that leaks oil product
Technical field
The present invention relates to a kind of treatment process of recirculated cooling water, relate in particular to a kind of treatment process that contains the recirculated cooling water that leaks oil product.
Background technology
Usually during the circulating water system generation oil leak of large chemical complex, take the method for large excretion and large complement, promptly add adhesive mud remover earlier, after peeling off, a large amount of drainings add corrosion inhibiting and descaling agent again, but this method are difficult to remove the greasy dirt that adheres to cooling system.
Chinese patent application CN1193609A discloses the cleaning prefilming agent that is used for dirts such as cleaning system microorganism dirt in a kind of circulating water system, clean prefilming agent and constitute by biological enzyme scavenging agent, biostats, inorganic salt complex agent with by the conventional water quality stabilizer that inhibiter and dispersion agent are formed, wherein inorganic salt complex agent is made up of silicate, manganate, carbonate, orthophosphoric acid salt.Purging method is under the normal operating condition of circulating water regiment commander thermal load, biological enzyme scavenging agent, biostats, inorganic salt complex agent and conventional water quality stabilizer are joined in the recirculated water by the specific concentrations of always possessing the water yield respectively, and kept this concentration 15-60 days.Chinese patent application CN1125697A discloses the using method of a kind of biological cleanser in circulating water system, and biological enzyme scavenging agent is added in the circulating water system, and biological enzyme scavenging agent is a fat hydrolase.Can add conventional water quality stabilizer in the circulating water system.Adopt this method the greasy dirt in the recirculated water can be removed, make the leaked substance degraded.Its shortcoming is has used expensive biological enzyme scavenging agent.
Summary of the invention
The object of the present invention is to provide a kind of treatment process that contains the recirculated cooling water that leaks oil product.Use method of the present invention can carry out oil removing to the equipment of circulating water system, peel off microorganism viscosity mud, can once finish, need not a large amount of blowdowns.
To achieve the above object of the invention, the invention provides a kind of treatment process that contains the recirculated cooling water that leaks oil product, comprise that oil product is peeled off dispersion agent, corrosion inhibiting and descaling agent, microorganism growth nutritive substance while or substep to add in the recirculating cooling water system, wherein said microorganism growth nutritive substance contains carbon source, nitrogenous source and water, and the effective concentration of described carbon source in recirculated cooling water is that 1-3mg/L, the nitrogenous source effective concentration in recirculated cooling water is 0.2-1.0mg/L.
The present invention can peel off above-mentioned oil product dispersion agent, corrosion inhibiting and descaling agent, microorganism growth nutritive substance and join in the recirculated cooling water simultaneously after composite, join simultaneously in the recirculated cooling water after also can preparing respectively, also can prepare the back respectively and successively join in the recirculated cooling water.Preferably oil product is peeled off dispersion agent, corrosion inhibiting and descaling agent and added earlier in the recirculated cooling water, again the microorganism growth nutritive substance is added in the recirculated cooling water.The equipment of oil product from cooling system is peeled off and prevented equipment scaling and corrosion when being scattered in the water, and the microbial nutrition material that adds subsequently can impel microbial growth, quickens being scattered in the degraded of the oil product in the water.Quaternary ammonium salt in the dispersion agent has dual function: the one, keep the effect of the sterilant of low dosage, and with the quantity of controlling microbial, in water, set up a good eubiosis, the 2nd, help controlling the generation of foundry loam.
Carbon source of the present invention is at least a material that is selected from lactic acid, glucose.
Nitrogenous source of the present invention is at least a material that is selected from urea, saltpetre, peptone, extractum carnis, SODIUMNITRATE.
Prior art is disclosed to be made oil product peel off and be scattered in single oil product the water from the equipment of cooling system to peel off dispersion agent or compound oil product and peel off dispersion agent and all can be used for the present invention.Oil product of the present invention is peeled off dispersion agent preferably by C 12-C 16Alkyl quaternary ammonium salts, C 10-C 16Alkyl tertiary amine, C 10-C 16The alkanol fatty amide is formed.The effective concentration of described quaternary ammonium salt in recirculated cooling water is that 5-20mg/L, the tertiary amine effective concentration in recirculated cooling water is that 5-20mg/L, the effective concentration of alkanol fatty amide in recirculated cooling water are 20-80mg/L.Described quaternary ammonium salt is C 12-C 16Alkyl two C 1-C 4Alkyl benzyl halogenation ammonium is preferably dodecyl benzyl dimethyl ammonium chloride and tetradecyl dimethyl benzyl ammonium chloride, cetalkonium chloride; Described tertiary amine is C 10-C 16Alkyl two C 1-C 4Alkylamine is preferably N, N-dimethyl amino dodecane, N, N-dimethyl tetradecy lamine, N, N-dimethyl cetylamine; Described alkanol fatty amide is that alkanolamine is (as thanomin, diethanolamine, Propanolamine etc.) with lipid acid (as cocinic acid, laurostearic acid, TETRADECONIC ACID, stearic acid and oleic acid etc.) condensation product, particularly, the alkanol fatty amide can be the ethanol fatty amide, the di-alcohol fatty amide, propyl alcohol fatty amide, more preferably ethanol Oleum Cocois acid amides, the ethanol lauramide, the ethanol myristamide, the ethanol stearylamide, the ethanol oleylamide, di-alcohol Oleum Cocois acid amides, the di-alcohol lauramide, the di-alcohol myristamide, the di-alcohol stearylamide, the di-alcohol oleylamide, propyl alcohol Oleum Cocois acid amides, the propyl alcohol lauramide, the propyl alcohol myristamide, the propyl alcohol stearylamide, the propyl alcohol oleylamide.Adopt above-mentioned oil product to peel off dispersion agent oil product is effectively separated with the equipment of cooling system, and stable dispersion can prevent that oil product from adhering on the equipment once more in recirculated water.In addition, above-mentioned oil product is peeled off dispersion agent and is also had certain corrosion inhibition, is applied in the recirculated cooling water with conventional corrosion inhibiting and descaling agent, and anticorrosion-antiscaling effect is all fine.In addition, because oil product is peeled off quaternary ammonium salt in the dispersion agent and also had that certain foundry loam is peeled off, dispersion and germicidal action, can keep the balance of microorganism.
The conventional water quality stabilizer that corrosion inhibiting and descaling agent of the present invention is made up of dirt dispersion agent and inhibiter.The disclosed conventional water quality stabilizer of prior art all can be used for the present invention, preferably contains molybdate, organic phospho acid, contains the corrosion inhibiting and descaling agent that carboxylic acid-based copolymer and zinc salt constitute.Its effective concentration in recirculated cooling water is: 1-4mg/L zinc salt (by the cubage of zinc), 1-15mg/L molybdate, 1-15mg/L organic phospho acid, 8-20mg/L contain the carboxylic acid-based copolymer.
Molybdate of the present invention is Sodium orthomolybdate or potassium molybdate; Described organic phospho acid is at least a 1-Hydroxy Ethylidene-1,1-Diphosphonic Acid (HEDP), Amino Trimethylene Phosphonic Acid (ATMP), the 2-phosphonate group-1 of being selected from, 2,4-butane tricarboxylate (PBTCA), hydroxyethylidene diphosphonic acid guanidine-acetic acid (HPAA), ethylene diamine tetra methylene phosphonic acid (EDTMP), diethylene triamine pentamethylene phosphonic, to the compound of two phosphono and sulfonics, glycine two methene phosphonic acids, L-glutamic acid two methene phosphonic acids, thionamic acid two methene phosphonic acids, taurine two methene phosphonic acids, PAPE; The described carboxylic acid-based copolymer of containing is selected from toxilic acid (acid anhydride)/styrene sulfonic acid multipolymer, vinylformic acid (AA)/styrene sulfonic acid multipolymer, acrylate/styrene sulfonic acid multipolymer, toxilic acid (acid anhydride)/allyl sulphonic acid multipolymer, vinylformic acid/allyl sulphonic acid multipolymer, vinylformic acid/vinyl sulfonic acid multipolymer, vinylformic acid/2-methyl-2 '-acrylamido propane sulfonic acid (AMPS) multipolymer, acrylic acid/2-methyl-2 '-acrylamido propane sulfonic acid multipolymer, acrylic acid/esters/2-methyl-2 '-acrylamido propane sulfonic acid multipolymer, vinylformic acid/toxilic acid/2-methyl-2 '-acrylamido propane sulfonic acid multipolymer, vinylformic acid/2-acrylamido-2-methylpropanephosphonic acid/2-methyl-2 '-acrylamido propane sulfonic acid multipolymer, the acrylic acid/esters multipolymer, wherein said acrylate is preferably from methyl acrylate, ethyl propenoate, Propylene glycol monoacrylate (HPA); Described zinc salt is zinc sulfate, zinc chloride and zinc carbonate.
Method of the present invention can comprise also that according to a conventional method impact adds conventional oxidative bactericide in recirculated cooling water, with the microorganism in the Control Circulation cooling water system.Conventional oxidative bactericide and oil product of the present invention are peeled off dispersion agent and are acted synergistically together, and effectively the microorganism of Control Circulation cooling water system prevents a large amount of generations of microorganism excess growth and foundry loam.Conventional oxidative bactericide can be chlorine, clorox, Surchlor GR 60 (abbreviation Puritabs, trichloroisocyanuric acid (abbreviation strong chlorine oil), active bromine etc.
Oil product of the present invention is peeled off the form that dispersion agent, corrosion inhibiting and descaling agent, microorganism growth nutritive substance generally are mixed with the aqueous solution, available ordinary method preparation, and the reinforced order of each component is unimportant, can prepare respectively, also can be together composite.
Method of the present invention is peeled off dispersion agent, corrosion inhibiting and descaling agent, microorganism growth nutritive substance by adding oil product, can be when guaranteeing anticorrosion-antiscaling effect, the oil product of circulating water system is disperseed, adopt the microorganism growth nutritive substance again, the microbial growth that exists in the promotion recirculated water, thereby make microbiological degradation go out extracellular enzyme-cellulase, amylase, proteolytic enzyme,, reach leaking the biological degradation of oil product by enzyme and action of microorganisms.Its advantage is in natural operational conditions or transfers under the pH operation, need not the large excretion and large complement of water, can realize cleaning online restoration methods after the oil removing with the present invention, and the oil product degradable has been saved expense, has simplified operation.
Adopt dispersion, degraded, sterilization technology, system can leak under the background with low blowdown flow rate, than the high concentration multiple smooth running.At this moment, system stability, medicine consumption is little, can guarantee the water treatment effect, and water-saving and emission-reducing is more remarkable, also can prolong the work-ing life of equipment.
Recirculated cooling water of the present invention is from surface water or underground water, and its calcium ion concn is that 80-900mg/L (in lime carbonate), basicity are 80-500mg/L.When the temperature of recirculated cooling water is a room temperature to 50 ℃.
Embodiment
The following examples will help to illustrate the present invention, but not limit to its scope.
" rotary hanging plate weight-loss method " in " water coolant analysis and the test method " that the following examples are all write according to production department of China PetroChemical Corporation and development division (1993, general petrochemical works, Anqing information center publishes) is rotated coupon corrosion test.Test temperature is 30-50 ℃ in " rotary hanging plate weight-loss method ", and the test piece rotating speed is 75 rev/mins (rpm), and the lacing film material is a carbon steel.The former water of the test of following embodiment is the on-the-spot recirculated water of refinery.The test raw water quality is: Ca 2+(with CaCO 3Meter, down together) 400-800mg/L, total alkalinity is (with CaCO 3Meter, down together) all with CaCO 3Meter, 80-180mg/L, Cl -73.5-242.3mg/L, SO 4 2-146-339mg/L, pH7.4-9.4, specific conductivity 1200-3950 μ s/cm, iron ion 0.3-0.9mg/L.
Embodiment 1
Oil product is peeled off the preparation of dispersion agent: with 10g dodecyl benzyl dimethyl ammonium chloride and 10g tetradecyl dimethyl benzyl ammonium chloride, 15g N, N-dimethyl amino dodecane and 5g N, N-dimethyl tetradecy lamine, 35g cocinic acid diethanolamine condenses (di-alcohol Oleum Cocois acid amides), 25g water adds in the container, shakes up.
The preparation of corrosion inhibiting and descaling agent: the Zinc Sulphate Heptahydrate of 6.5g is dissolved in the 33.5 gram water, dissolving evenly, add the 5g Sodium orthomolybdate, fully dissolving, add 10g concentration and be 50% HEDP and 10g concentration and be 50% PBTCA, shake up, (weight ratio is AA/HPA=70/30 to add the 35g solid content and be 30% AA/HPA copolymer, limit viscosity number in the time of 30 ℃ is 0.060-0.095dl/g), shake up.
The preparation of microorganism growth nutritive substance: SODIUMNITRATE 4 grams are dissolved in the 66 gram water, and dissolving evenly adds lactic acid 30 grams, and fully dissolving shakes up.
To test and simultaneously smear the uniform sweat oil of last layer with lacing film (is high oil-containing soft wax, mixture for liquid wax oil, lubricating oil and small molecules alkane, fusing point is less than 55 ℃), form an oil lamella, place the former water of test, adding pyrolysis gasoline 100mg/L, oil product are peeled off dispersion agent 90mg/L and water-soluble Sodium orthomolybdate 5mg/L, after 4 hours, add microorganism growth nutritive substance 7mg/L.
In the rotary hanging plate instrument, test temperature is 30 ℃, and the test piece rotating speed is 75 rev/mins (rpm), and test period is 10 days, at duration of test, keeps that corrosion inhibiting and descaling agent, oil product are peeled off dispersion agent, the effective concentration of each component of nutritive substance in recirculated water is constant.Add Babysafe 80mg/L the last day.Test-results sees Table 1.
Embodiment 2
Oil product is peeled off the preparation of dispersion agent: 20g tetradecyl dimethyl benzyl ammonium chloride, 15g N, N-dimethyl tetradecy lamine, 35g cocinic acid diethanolamine condenses and 30g water are added in the container, shake up.
The preparation of corrosion inhibiting and descaling agent: the zinc chloride of 6g is dissolved in the 36 gram water, dissolving evenly, fully dissolving, add the 8g Sodium orthomolybdate, fully dissolving adds 10g concentration and is 40% HPAA and 10g concentration and be 50% PBTCA, shake up, adding 30g solid content is 30% AA/HPA copolymer (weight ratio is AA/HPA=80/20, and the limit viscosity number in the time of 30 ℃ is 0.060-0.095dl/g), shakes up.
The preparation of microorganism growth nutritive substance: saltpetre 3 grams, peptone 2 grams are dissolved in the 60 gram water, and dissolving evenly adds glucose 35 grams, and fully dissolving shakes up.
To test with lacing film and simultaneously smear the uniform sweat oil of last layer, form an oil lamella, place the former water of test, adding pyrolysis gasoline 100mg/L, oil product are peeled off dispersion agent 90mg/L and water-soluble Sodium orthomolybdate 8mg/L, after 4 hours, add microorganism growth nutritive substance 6mg/L.
Test temperature is 35 ℃ in the rotary hanging plate instrument, and the test piece rotating speed is 75 rev/mins (rpm), and test period is 12 days.At duration of test, keep that corrosion inhibiting and descaling agent, oil product are peeled off dispersion agent, the effective concentration of each component of nutritive substance in recirculated water is constant, adds Babysafe 80mg/L the last day.Test-results sees Table 1.
Embodiment 3
Oil product is peeled off the preparation of dispersion agent: 15g dodecyl benzyl dimethyl ammonium chloride, 10g N, N-dimethyl amino dodecane, 45g di-alcohol palmitamide and 30g water are added in the container, shake up.
The preparation of corrosion inhibiting and descaling agent: the zinc chloride of 5g is dissolved in the 34 gram water, dissolving evenly, add the 5g Sodium orthomolybdate, fully dissolving, add 8g concentration and be 40% HPAA, 8g concentration and be 55% Amino Trimethylene Phosphonic Acid (ATMP) and 10g concentration and be 50% PBTCA, shake up, adding 30g solid content is that 30% AA/AMPS contains the sulfonic group copolymer (weight ratio is AA/AMPS=70/30, limit viscosity number in the time of 30 ℃ is 3 0.060-0.095dl/g), shake up.
The preparation of microbial enzyme nutritive substance: urea 2 grams, extractum carnis 3 grams are dissolved in the 60 gram water, and dissolving evenly adds glucose 20g, lactic acid 15g, and fully dissolving shakes up.
To test with lacing film and simultaneously smear the uniform sweat oil of last layer, form an oil lamella, place the former water of test, adding pyrolysis gasoline 100mg/L, oil product are peeled off dispersion agent 100mg/L and the water-soluble ammonium molybdate inhibiter of 5mg/L, after 8 hours, add microbial enzyme nutritive substance 5mg/L.
Test temperature is 40 ℃ in the rotary hanging plate instrument, and the test piece rotating speed is 75 rev/mins (rpm), and test period is 12 days.At duration of test, keep that corrosion inhibiting and descaling agent, oil product are peeled off dispersion agent, the effective concentration of each component of nutritive substance in recirculated water is constant.Add clorox 200mg/L (effective chlorine density 12%) before the off-test.Test-results sees Table 1.
Embodiment 4
Oil product is peeled off the preparation of dispersion agent: 20g dodecyl benzyl dimethyl ammonium chloride and 20g water are mixed, add 20g N, N-dimethyl amino dodecane, and 40g ethanol myristamide shakes up.
The preparation of corrosion inhibiting and descaling agent: the zinc chloride of 6.5g is dissolved in the 26.5g water, dissolves evenly, add the 10g Sodium orthomolybdate, fully dissolving, adding 15g concentration is 40% HPAA, 10g concentration is 50% PBTCA, shakes up.Add the 32g solid content and be 30% AA/AMPS/HPA and contain sulfonic group copolymer (weight ratio is AA/AMPS/HPA=60/20/20, and the limit viscosity number in the time of 30 ℃ is 0.060-0.095dl/g), shake up.
The preparation of microorganism growth nutritive substance: peptone 2 grams are dissolved in the 60 gram water, and dissolving evenly adds urea 6 grams, lactic acid 30 grams, and fully dissolving shakes up.
To test with lacing film and simultaneously smear the uniform sweat oil of last layer, form an oil lamella, place the former water of test, add pyrolysis gasoline 100mg/L simultaneously, oil product is peeled off dispersion agent 60mg/L, water-soluble Sodium orthomolybdate 10mg/L and microorganism growth nutritive substance 4mg/L.
Test temperature is 40 ℃ in the rotary hanging plate instrument, and the test piece rotating speed is 75 rev/mins (rpm), and test period is 6 days.At duration of test, keep that corrosion inhibiting and descaling agent, oil product are peeled off dispersion agent, the effective concentration of each component of nutritive substance in recirculated water is constant.Test-results sees Table 1.
Comparative Examples 1
Test is not except that adding the microorganism growth nutritive substance, and test conditions and testing sequence are with embodiment 2.Test-results sees Table 1.
Comparative Examples 2
Test is peeled off the dispersion agent except that the non-refuelling product, and test conditions and testing sequence are with embodiment 3.Test-results sees Table 1.
Comparative Examples 3
Test is except that the non-refuelling product are peeled off dispersion agent and microorganism growth nutritive substance, and test conditions and testing sequence are with embodiment 4.Test-results sees Table 1.
Table 1
Oil film Corrosion of carbon steel speed (mm/a) Chemical oxygen demand cod (mg/L) Heterotrophic bacterium several 1 *(individual/mL) Heterotrophic bacterium several 2 *(individual/mL)
Embodiment 1 Do not have 0.0312 36 3.7×10 5 7.3×10 2
Embodiment 2 Do not have 0.0470 35 5.0×10 5 8.6×10 2
Embodiment 3 Do not have 0.0350 30 4.4×10 5 7.9×10 2
Embodiment 4 Do not have 0.0227 37 8.9×10 4 -
Comparative Examples 1 Do not have 0.0553 122 2.5×10 4 2.3×10 2
Comparative Examples 2 Have 0.0412 38 3.2×10 6 3.5×10 2
Comparative Examples 3 Have 0.0361 105 1.1×10 6 -
* heterotrophic bacterium several 1 is for adding the heterotrophic bacterium data before the sterilant the last day; Heterotrophic bacterium adds behind the sterilant 4 hours heterotrophic bacterium data several 2 the last daies.
By the data of the foregoing description and Comparative Examples as can be seen: adopt method of the present invention to handle when containing the recirculated cooling water that leaks oil product, deoiling effect reaches the effect that oil is degraded, and (COD is low more, degradation effect to oil is good more) all fine, and can effectively control the microorganism that contains in the recirculated cooling water that leaks oil product.

Claims (12)

1 one kinds of treatment processs that contain the recirculated cooling water that leaks oil product, comprise that oil product is peeled off dispersion agent, corrosion inhibiting and descaling agent, microorganism growth nutritive substance while or substep to add in the recirculating cooling water system, wherein said microorganism growth nutritive substance contains carbon source, nitrogenous source, and the effective concentration of described carbon source in recirculated cooling water is that 1-3mg/L, the nitrogenous source effective concentration in recirculated cooling water is 0.2-1mg/L.
2. the treatment process of recirculated cooling water according to claim 1 is characterized in that described carbon source is at least a material that is selected from lactic acid, glucose.
3. the treatment process of recirculated cooling water according to claim 1 and 2 is characterized in that described nitrogenous source is at least a material that is selected from urea, saltpetre, extractum carnis, peptone, SODIUMNITRATE.
4. the treatment process of recirculated cooling water according to claim 1 and 2 is characterized in that oil product is peeled off dispersion agent, corrosion inhibiting and descaling agent to add earlier in the recirculated cooling water, adds the microorganism growth nutritive substance in the recirculated cooling water again.
5. the treatment process of recirculated cooling water according to claim 1 and 2 is characterized in that described oil product peels off dispersion agent by C 12-C 16Alkyl quaternary ammonium salts, C 10-C 16Alkyl tertiary amine, C 10-C 16The alkanol fatty amide is formed.
6. the treatment process of recirculated cooling water according to claim 5 is characterized in that described quaternary ammonium salt is C 12-C 16Alkyl two C 1-C 4Alkyl benzyl halogenation ammonium, described tertiary amine are C 10-C 16Alkyl two C 1-C 4Alkylamine, described alkanol fatty amide are ethanol fatty amide, di-alcohol fatty amide, propyl alcohol fatty amide.
7. the treatment process of recirculated cooling water according to claim 6 is characterized in that described quaternary ammonium salt is dodecyl benzyl dimethyl ammonium chloride, tetradecyl dimethyl benzyl ammonium chloride, cetalkonium chloride; Described tertiary amine is N, N-dimethyl amino dodecane, N, N-dimethyl tetradecy lamine, N, N-dimethyl cetylamine; Described alkanol fatty amide is ethanol Oleum Cocois acid amides, ethanol lauramide, ethanol myristamide, ethanol stearylamide, ethanol oleylamide, di-alcohol Oleum Cocois acid amides, di-alcohol lauramide, di-alcohol myristamide, di-alcohol stearylamide, di-alcohol oleylamide, propyl alcohol Oleum Cocois acid amides, propyl alcohol lauramide, propyl alcohol myristamide, propyl alcohol stearylamide, propyl alcohol oleylamide.
8. the treatment process of recirculated cooling water according to claim 5 is characterized in that the effective concentration of described quaternary ammonium salt in recirculated cooling water is that 5-20mg/L, the tertiary amine effective concentration in recirculated cooling water is that 5-20mg/L, the effective concentration of alkanol fatty amide in recirculated cooling water are 20-80mg/L.
9. the treatment process of recirculated cooling water according to claim 1 and 2 is characterized in that the conventional water quality stabilizer that described corrosion inhibiting and descaling agent is made up of dirt dispersion agent and inhibiter.
10. the treatment process of recirculated cooling water according to claim 9, it is characterized in that described corrosion inhibiting and descaling agent contains molybdate, organic phospho acid, contains carboxylic acid-based copolymer and zinc salt, its effective concentration in recirculated cooling water is: press the cubage of zinc, 1-4mg/L zinc salt, 1-15mg/L molybdate, 1-15mg/L organic phospho acid, 8-20mg/L contain the carboxylic acid-based copolymer.
11. the treatment process of the described recirculated cooling water of claim 10 is characterized in that described molybdate is Sodium orthomolybdate or potassium molybdate; Described organic phospho acid is at least a 1-Hydroxy Ethylidene-1,1-Diphosphonic Acid (HEDP), Amino Trimethylene Phosphonic Acid (ATMP), the 2-phosphonate group-1 of being selected from, 2,4-butane tricarboxylate (PBTCA), hydroxyethylidene diphosphonic acid guanidine-acetic acid (HPAA), ethylene diamine tetra methylene phosphonic acid (EDTMP), diethylene triamine pentamethylene phosphonic, to the compound of two phosphono and sulfonics, glycine two methene phosphonic acids, L-glutamic acid two methene phosphonic acids, thionamic acid two methene phosphonic acids, taurine two methene phosphonic acids, PAPE; The described carboxylic acid-based copolymer of containing is selected from toxilic acid or maleic anhydride/styrene sulfonic acid multipolymer, vinylformic acid (AA)/styrene sulfonic acid multipolymer, acrylate/styrene sulfonic acid multipolymer, toxilic acid or maleic anhydride/allyl sulphonic acid multipolymer, vinylformic acid/allyl sulphonic acid multipolymer, vinylformic acid/vinyl sulfonic acid multipolymer, vinylformic acid/2-methyl-2 '-acrylamido propane sulfonic acid (AMPS) multipolymer, acrylic acid/2-methyl-2 '-acrylamido propane sulfonic acid multipolymer, acrylic acid/esters/2-methyl-2 '-acrylamido propane sulfonic acid multipolymer, vinylformic acid/toxilic acid/2-methyl-2 '-acrylamido propane sulfonic acid multipolymer, vinylformic acid/2-acrylamido-2-methylpropanephosphonic acid/2-methyl-2 '-acrylamido propane sulfonic acid multipolymer, the acrylic acid/esters multipolymer, wherein said acrylate is selected from methyl acrylate, ethyl propenoate, Propylene glycol monoacrylate (HPA); Described zinc salt is zinc sulfate, zinc chloride and zinc carbonate.
12. the treatment process of claim 1 or 2 described recirculated cooling waters is characterized in that impact adds conventional oxidative bactericide in recirculated cooling water.
CN 200310117372 2003-12-12 2003-12-12 Method for treating reciculated cooling water containing out oil product Expired - Lifetime CN1272255C (en)

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CN102578088A (en) * 2012-01-04 2012-07-18 中国石油大学(华东) Compound agent with effects of sterilization, corrosion inhibition and scale inhibition
CN103420493B (en) * 2012-05-16 2015-04-15 中国石油化工股份有限公司 Processing method of circulation cooling water comprising sulfur ions
CN102911651A (en) * 2012-11-09 2013-02-06 天津亿利科能源科技发展股份有限公司 Oil field compound type anti-scale corrosion inhibitor and preparation method thereof
CN106315873A (en) * 2016-08-29 2017-01-11 山东胜伟园林科技有限公司 Fluorescently-labeled scale inhibitor and preparation method thereof
CN107777790B (en) * 2016-08-29 2021-06-08 中国石油化工股份有限公司 High-calcium high-salt sewage denitrification carbon source
CN109399796A (en) * 2017-08-15 2019-03-01 中国石油化工股份有限公司 Circulating water cooling treatment system and its method with circulating water cooling treatment
CN109399804A (en) * 2017-08-15 2019-03-01 中国石油化工股份有限公司 Circulating water cooling treatment composition and its method of application and circulating water cooling treatment
CN109399797A (en) * 2017-08-15 2019-03-01 中国石油化工股份有限公司 Circulating water cooling treatment system and its method of application and circulating water cooling treatment
CN110872152B (en) * 2019-11-29 2022-04-29 武汉钢铁有限公司 Composite scale inhibitor for blast furnace gas washing water and preparation and use methods thereof

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