CN103318996B - A kind of method sea water desaltination water is applied in recirculating cooling water system - Google Patents
A kind of method sea water desaltination water is applied in recirculating cooling water system Download PDFInfo
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Abstract
The invention discloses a kind of method be applied to by sea water desaltination water in recirculating cooling water system, the method comprises and is applied in recirculating cooling water system using sea water desaltination water as moisturizing, add inhibiter and pH adjusting agent, the pH value of recirculated cooling water is made to be 9-12, wherein, described inhibiter contains the first inhibiter and the second inhibiter, described first inhibiter be selected from vanadate, tungstate and molybdate one or more, described second inhibiter be selected from gluconate, borate, silicate, sulfonated lignin and tannin one or more.Little and the environmental protection of the corrosion of present method to circulating cooling wetting system.
Description
Technical field
The present invention relates to a kind of method be applied to by sea water desaltination water in recirculating cooling water system.
Background technology
Along with the development of world economy, Freshwater resources day is aobvious deficient, and the utilization of sea water desaltination water is more and more subject to the most attention of maritime nation.According to international desalination association statistics, within nearly 5 years, sea water desaltination contract capacity is more than 2 × 10
7m
3/ d, close to the summation of Past 30 Years, estimates that coming 10 years also will double on this basis.Need in the industrial production to use water in a large number at present, wherein recirculated cooling water accounts for significant proportion, as petroleum chemical enterprise's recirculated cooling water water accounts for more than 80% of water of productive use.Sea water desaltination Water circulation will be reduced the consumption of fresh water as recirculated cooling water greatly in industrial circulating cooling water, thus solve the problem of fresh water undersupply.
At present, sea water desaltination mainly takes the method for reverse osmosis method to obtain.Seawater is after reverse-osmosis treated, and its desalination water has that content of mineral substances is few, the feature of slant acidity (pH value is 6.5 ~ 7.5).In addition, containing more chlorion in sea water desaltination water, have slight erosion, sea water desaltination water, in the process being used as industrial circulating cooling water, easily causes pipeline and equipment corrosion, therefore, needs to process accordingly sea water desaltination water.The method of the process sea water desaltination water of present stage mainly adds containing the mineral such as calcium, magnesium material in sea water desaltination water, protects water system to avoid being corroded with stabilizing water quality.But the fouling of equipment can be caused again after adding calcium, magnesium material, therefore need to add Scale inhibitors in sea water desaltination water.The consumption adding the unnecessary material of initiation and the energy of Scale inhibitors.The breeding of the corrosion and microorganism that directly utilize water treatment agent to carry out operating device can reduce the cost that sea water desaltination water is used as recirculated water, and simplification of flowsheet, makes sea water desaltination water have better development prospect in application aspect.
At present, the domestic formula being used as the sea water desaltination water treatment of industrial circulating cooling water mostly is organic phospho acid formula, sterilant many employings Babysafe, strong chlorine oil, quaternary ammonium salt etc.Organic phospho acid have good chemical stability, not facile hydrolysis, can higher temperature resistant, inhibition and scale inhibition function can be had concurrently in the treating processes of recirculated cooling water, although the working concentration of organic phospho acid in recirculated cooling water is only 4-10mg/L, the phosphorus content now in organic phospho acid still can pollute environment.After the sterilant such as strong chlorine oil, Babysafe uses, tricarbimide residual in water can cause Organic substance in water to increase, and this type organic is comparatively difficult to degraded at occurring in nature, then also can cause environmental issue.
CN1636891A discloses the treatment process using a kind of seawater as recirculated cooling water, the method by adding inhibiter in the seawater, Scale inhibitors, oxidizing biocides, non-oxidative bactericide process and desalinize seawater.Containing organophosphorus medicament in Scale inhibitors in the method, unfavorable to environmental protection.
CN101962234A discloses a kind of for the Scale inhibitors in circularly-cooling sea water system, and its composition is polyacrylic acid (PAA), acrylic acid esters co-polymer, hydrolytic polymaleic anhydride, poly aspartic acid and tensio-active agent.This invention solves the concentrated rear fouling distinct issues of seawater, but sea water desaltination water is not resolved to the problem of equipment corrosion when being used as recirculated cooling water.
CN1338435A discloses a kind of method of cycle for the treatment of water coolant, and the method is included in recirculated cooling water and adds alkaline matter its pH value is controlled at 9.5-14.But there is dissolved oxygen in recirculated cooling water, depending merely on adjust ph can not control corrosion rate effectively.This invention is not resolved to the problem of equipment corrosion when being used as recirculated cooling water to sea water desaltination water.
Summary of the invention
The object of the invention is to overcome the shortcoming easily circulating water equipment being caused to corrosion when current sea water desaltination water is used as recirculated cooling water, provide a kind of sea water desaltination water little to the corrosion of circulating water equipment to be applied to method in recirculating cooling water system.
The invention provides a kind of method be applied to by sea water desaltination water in recirculating cooling water system, the method comprises when being applied in recirculating cooling water system as recirculated cooling water by sea water desaltination water, add inhibiter and pH adjusting agent, the pH value of recirculated cooling water is made to be 9-12, wherein, described inhibiter contains the first inhibiter and the second inhibiter, described first inhibiter is selected from water miscible vanadate, one or more in tungstate and molybdate, described second inhibiter is selected from water miscible gluconate, borate, silicate, one or more in sulfonated lignin and tannin.
Compared with the existing method be applied to by sea water desaltination water in recirculating cooling water system, method sea water desaltination water being applied to recirculated cooling water provided by the invention, can control the corrosion of sea water desaltination water to circulating cooling wetting system effectively.Such as, corrosion coupon in embodiment 1 is 45 DEG C in temperature, rotating speed is that to record erosion rate after running 72h under 75r/min condition be 0.051mm/a, and the concentration of sodium wolframate in comparative example 2 when being 40mg/L corrosion coupon be 45 DEG C in temperature, rotating speed is that to record erosion rate after running 72h under 75r/min condition be 0.505mm/a, and present method significantly reduces the corrosion of sea water desaltination water to circulating cooling wetting system.
Embodiment
According to method sea water desaltination water is applied in circulating water system of the present invention, the method comprises and is applied in recirculating cooling water system using sea water desaltination water as recirculated cooling water, and add inhibiter and pH adjusting agent, the pH value of recirculated cooling water is made to be 9-12, wherein, described inhibiter contains the first inhibiter and the second inhibiter, described first inhibiter is selected from water-soluble vanadate salt, one or more in tungstate and molybdate, described second inhibiter is selected from Water-Soluble Glucose hydrochlorate, borate, silicate, one or more in sulfonated lignin and tannin.
In the present invention, being applied in recirculating cooling water system as recirculated cooling water by sea water desaltination water can be that recirculating cooling water system uses sea water desaltination water as recirculated cooling water completely, also sea water desaltination water can be used as moisturizing, and namely component loops water coolant is above-mentioned sea water desaltination water.
First inhibiter and the second inhibiter can successively add, and also can add simultaneously.Add fashionable simultaneously, can add separately, also can add as a mixture.
According to method of the present invention, although the weight ratio of various the first described inhibiter and the second inhibiter all can realize object of the present invention, preferably, the weight ratio of described first inhibiter and the second inhibiter is 1: 0.5-5, is preferably 1: 1-3.Adopt the first inhibiter of above-mentioned weight ratio and the second inhibiter can reduce the recirculated cooling water of gained of the present invention better to the corrosion of circulating cooling wetting system.
According to method of the present invention, although the first inhibiter of various type of service all can realize object of the present invention, the type of service of the first inhibiter can be powder type, also can be solution form.No matter the type of service of the first inhibiter is powder type is also solution form, preferably, described first inhibiter uses in the form of a solution.Preferably, the concentration of described first inhibiter in recirculated cooling water is 20-100mg/L, is preferably 40-80mg/L further.When described first inhibiter is selected from one or more in vanadate, tungstate and molybdate, the concentration of vanadate is with VO
4 3-meter, tungstate are with WO
4 2-the concentration of meter, molybdate is with MoO
4 2-meter.
According to method of the present invention, although the second inhibiter of various type of service all can realize object of the present invention, the type of service of the second inhibiter can be powder type, also can be solution form.No matter the type of service of the second inhibiter is powder type is also solution form, preferably, the concentration of described second inhibiter in recirculated cooling water is 50-150mg/L, more preferably 60-120mg/L.When described second inhibiter is selected from one or more in gluconate, borate, silicate, sulfonated lignin and tannin, boratory concentration is with B
4o
7 2-meter, gluconate concentration in the concentration of Sunmorl N 60S, silicate with SiO
2the concentration of meter, sulfonated lignin is in sulfomethylated lignin acid group.
According to method of the present invention, the kind of the present invention to described pH adjusting agent does not have particular requirement, and various pH adjusting agent of the prior art all can realize goal of the invention.Preferably, described pH adjusting agent is inorganic alkaline compound.The present invention does not have particular requirement to described inorganic alkaline compound, preferably, described inorganic alkaline compound be selected from sodium hydroxide, potassium hydroxide, sodium carbonate, salt of wormwood one or more.
According to method of the present invention, the present invention does not have particular requirement to described vanadate, preferably, described vanadate be selected from 12 water sodium orthovanadates, two water sodium metavanadates, anhydrous sodium metavanadate and potassium metavanadate one or more, more preferably from 12 water sodium orthovanadates.
According to method of the present invention, the kind of the present invention to described tungstate does not have particular requirement, preferably, described tungstate be selected from anhydrous wolframic acid sodium, tungstate dihydrate acid sodium and anhydrous wolframic acid potassium one or more, be more preferably tungstate dihydrate acid sodium and/or anhydrous wolframic acid sodium.
According to method of the present invention, the kind of the present invention to described molybdate does not have particular requirement, and preferably, described molybdate is selected from anhydrous molybdic acid sodium, Sodium Molybdate Dihydrate and five water potassium molybdates; Be more preferably Sodium Molybdate Dihydrate.
According to method of the present invention, the kind of the present invention to described gluconate does not have particular requirement, preferably, described gluconate be selected from Sunmorl N 60S, Potassium Gluconate and Zinc Gluconate one or more, be more preferably Sunmorl N 60S.
According to method of the present invention, the present invention does not have particular requirement to described boratory kind, and preferably, described borate is selected from Sodium Tetraborate and/or potassium borate.Further under preferable case, described Sodium Tetraborate be selected from sodium borate decahydrate, five hydration sodium tetraborates and four hydration eight Sodium Tetraboratees one or more.
According to method of the present invention, the kind of the present invention to described silicate does not have particular requirement, preferably, described silicate be selected from sodium metasilicate, Starso, positive potassium silicate and potassium metasilicate one or more, more preferably Starso.When silicate is Starso, described Starso be preferably in metasilicate pentahydrate sodium, non-hydrate sodium metasilicate and anhydrous sodium metasilicate one or more.
According to method of the present invention, the kind of the present invention to described sulfonated lignin does not have particular requirement, and preferably, described sulfonated lignin are preferably sodium lignosulfonate and/or calcium lignin sulphonate, is further preferably sodium lignosulfonate.
According to method of the present invention, preferably, described first inhibiter is 12 water sodium orthovanadates and anhydrous molybdic acid sodium, described second inhibiter is five hydrated sodium borates and metasilicate pentahydrate sodium, wherein, the weight ratio of 12 water sodium orthovanadates and anhydrous molybdic acid sodium is the weight ratio of 1: 1-1.2, five hydrated sodium borates and metasilicate pentahydrate sodium is 1: 2-2.2.When inhibiter is the combination of 12 water sodium orthovanadates, anhydrous molybdic acid sodium, five hydrated sodium borates and metasilicate pentahydrate sodium, minimum to the corrosion of circulating cooling wetting system.
According to method of the present invention, preferably, in recirculated cooling water, chlorine ion concentration is 150-750mg/L.When the chlorine ion concentration of recirculated cooling water is 150-750mg/L, the corrosion to circulating cooling wetting system can be reduced further.
According to method of the present invention, the method can also comprise carries out sterilization by recirculating cooling water system.Wherein, the method for described sterilization is selected from one or more in ultraviolet-sterilization, ozone sterilization and hydrogen peroxide sterilization.
In the present invention, described ultraviolet-sterilization can carry out with reference to the method for the ultraviolet-sterilization of routine of the prior art, such as, can adopt UV-device irradiation cycle water coolant.Ultraviolet device can be produced disclosed in prior art and all can be used for the present invention, the uviolizing recirculated cooling water that the present invention preferably adopts ultraviolet device to produce; Described ultraviolet device is preferably low-pressure high-strength ultraviolet lamp; The power of described ultraviolet lamp is preferably 100-300W.When adopting ultraviolet-sterilization, preferably, the recirculated cooling water through ultraviolet-sterilization accounts for global cycle amount 20-60 volume %.
Described ozone sterilization can carry out with reference to the method for ozone sterilization conventional in prior art, and such as, described ozone is produced by ozonizer.When adopting ozone sterilization, the ozone amount in sea water desaltination water or recirculated cooling water controls at 0.05-0.20mg/L.
Described hydrogen peroxide sterilization can be carried out with reference to the method for hydrogen peroxide sterilization conventional in prior art, does not repeat them here.Under preferable case, it is add 1-3 time that hydrogen peroxide adds frequency every day, and the effective concentration added is 2-15mg/L.
Describe the present invention in detail below in conjunction with embodiment, but be not used for limiting the present invention.
In following examples, test water is the recirculated cooling water of preparation, and carbon steel test piece is 20# steel.Table 1 is depicted as the water quality of the test 1# recirculated cooling water prepared according to the water quality of recirculated cooling water during circulating water equipment initial launch; After circulating water equipment steady running, the water quality of the recirculated cooling water after evaporation concentration and the water quality of formulated test 2# recirculated cooling water.The test 2# recirculated cooling water after the steady running of simulation loop wetting system is adopted to do rotary hanging plate experiment.
The water quality of table 1 test water
| The kind of recirculated cooling water and numbering | PH value | Cl -/(mg/L) | Specific conductivity (μ s/cm) |
| When circulating water equipment is initial (1#) | 6.5 | 200 | 200 |
| After circulating water equipment is stable (2#) | - | 700 | 700 |
In following examples, the testing method related to is as follows:
1, pH value: GB/T6920-1986 " the mensuration glass electrode method of water pH value "
2, specific conductivity: GB/T6908-2008 " mensuration of boiler feed water and water coolant analytical procedure specific conductivity "
3, erosion rate: the test piece of 20# qualitative carbon steel is fixed on lacing film instrument, put into the 2# test water being added with the drug concentration added by embodiment, steady temperature 45 ± 1 DEG C, keep rotating speed 75rpm to rotate 72h, the weight of test piece before and after record test, calculates average corrosion rate.Corrosion speed quality adopts the regulation of " the small-sized experimental analogic method of testing laboratory " in " water coolant analysis and the test method " of standard GB/T 50050-2007 " Code for design of industrial recirculating cooling water treatment " and production department of China PetroChemical Corporation and development division establishment to evaluate.
Average corrosion rate calculation formula is:
C: computational constant, during with mm/a (millimeter/year) for unit, C=8.76 × 10
7
Δ 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)
4, the mensuration of heterotrophic bacterium: get test water sample, adopts former water 10 times of dilution technologies in sterilisable chamber, test water sample is diluted to suitable multiple, and is inoculated in culture dish by the water sample of corresponding extension rate.Then aseptic culture medium being poured in culture dish, mix with water sample, cultivating 72 ± 4h etc. being inverted after culture medium solidifying to be placed in the incubator of 29 ± 1 DEG C.After cultivation, take out culture dish, select those culture dish with 30-300 bacterium colony to count, colony number is multiplied by the heterotrophic bacterium number that corresponding dilution training number is this water sample.The evaluation of heterotrophic bacterium number adopts the regulation of " the small-sized experimental analogic method of testing laboratory " in " water coolant analysis and the test method " of standard GB/T 50050-2007 " Code for design of industrial recirculating cooling water treatment " and production department of China PetroChemical Corporation and development division establishment.
5, adhere to the mensuration of speed: be arranged on by test tube in the bypass of interchanger, take out test tube after off-test, after cleaning test tube outer wall, constant temperature drying, takes the heavy (W of band bur test tube
1).Then inboard wall of test tube bur is cleaned, dry, take the heavy (W of test tube
2), calculate and adhere to speed F '.
A: the area (cm of test specimen
2); T: corrosion test time (h).
In following examples 1-15, comparative example 1-9, the recirculated cooling water of the determination test of erosion rate is the 2# recirculated cooling water shown in table 1, the cumulative volume of recirculated cooling water of test is 2L, and in recirculated cooling water, the pH value of the kind of the concentration of inhibiter, the pH adjusting agent of test and recirculated cooling water, the erosion rate that records are respectively as shown in table 2 and table 3.
Table 2
Table 3
Embodiment 16
In order to simulated field, carry out dynamic analog test.Dynamic analog test method is undertaken by People's Republic of China (PRC) chemical industry standard HG/T2160-2008, and controling parameters is as follows.
The water quality of test initial sum make up water: 1# recirculated cooling water as shown in table 1
Flow velocity: 1.0m/s
Temperature in: 32 ± 1 DEG C of temperature difference: 10 DEG C
Days running: 20 days
System internal recycle water cumulative volume: 180L
Cycles of concentration: utilize specific conductivity to control
A tower: by the composite corrosion inhibitor composition in embodiment 4 and concentration, is first added in the 1# recirculated cooling water as table 1 by inhibiter, be 11.7 ± 0.1 by sodium hydroxide adjust ph simultaneously.The water outlet of drawing 55L/h enters bypass (namely by the water of recirculated cooling water internal circulating load 55 volume % through ultraviolet-sterilization), after the low-pressure high-strength ultra violet lamp that power is 150W, return water tank again.Reach after 700 μ s/cm until specific conductivity, the specific conductivity controlling its circulating water system maintains 700 μ s/cm.Analog result is in table 4, table 5.
B tower: by the composite corrosion inhibitor composition in embodiment 7 and concentration, is first added to inhibiter in the 1# recirculated cooling water as table 1.Opened by ozonizer, make the concentration of ozone in recirculating cooling water system reach 0.20mg/L, be 10.5 ± 0.1 by salt of wormwood adjust ph, reach after 700 μ s/cm until specific conductivity, the specific conductivity controlling its circulating water system maintains 700 μ s/cm simultaneously.Analog result is in table 4, table 5.
C tower: by the composite corrosion inhibitor composition in embodiment 9 and concentration, first inhibiter is added in the 1# recirculated cooling water as table 1, is 11.6 ± 0.1 by sodium hydroxide adjust ph, adds hydrogen peroxide simultaneously, add 2 every day, the effective concentration adding hydrogen peroxide is 14mg/L.Reach after 700 μ s/cm until specific conductivity, the specific conductivity controlling its circulating water system maintains 700 μ s/cm.Analog result is in table 4, table 5.
D tower: by the composite corrosion inhibitor composition in embodiment 12 and concentration, is first added to inhibiter in the 1# recirculated cooling water as table 1.Ozonizer is opened, makes the concentration of ozone in recirculating cooling water system reach 0.05mg/L, be 9.4 ± 0.1 by sodium carbonate adjust ph simultaneously, control density of corrosion inhibitor in real time afterwards.Run the 5th day to rise, the water outlet of drawing 28L/h enters bypass (namely by the water of recirculated cooling water internal circulating load 28 volume % through ultraviolet-sterilization), after the low-pressure high-strength ultra violet lamp that power is 120W, return water tank again.Reach after 700 μ s/cm until specific conductivity, the specific conductivity controlling its circulating water system maintains 700 μ s/cm.Analog result is in table 4, table 5.
E tower: by the composite corrosion inhibitor composition in embodiment 15 and concentration, first inhibiter is added in the 1# recirculated cooling water as table 1, be 11.2 ± 0.1 by sodium hydroxide adjust ph, add hydrogen peroxide simultaneously, add 1 every day, the effective concentration adding hydrogen peroxide is 6mg/L, runs and rises for the tenth day, the water outlet of drawing 32L/h enters bypass (namely by the water of recirculated cooling water internal circulating load 32 volume % through ultraviolet-sterilization), after the low-pressure high-strength ultra violet lamp that power is 200W, return water tank again.Reach after 700 μ s/cm until specific conductivity, the specific conductivity controlling its circulating water system maintains 700 μ s/cm.Analog result is in table 4, table 5.
Table 4 dynamic analog test test tube result
Table 5 heterotrophic bacterium monitoring result (heterotrophic bacterium number unit: individual/mL)
| Sample time | 1st day | 5th day | 10th day | 15th day | 20th day |
| A tower | 4.6×10 3 | 7.5×10 3 | 6.5×10 3 | 8.1×10 3 | 9.6×10 3 |
| B tower | 6.7×10 3 | 6.0×10 3 | 9.1×10 3 | 1.2×10 4 | 1.8×10 4 |
| C tower | 5.2×10 3 | 1.0×10 4 | 1.7×10 4 | 2.3×10 4 | 3.8×10 4 |
| D tower | 6.2×10 3 | 6.0×10 3 | 7.7×10 3 | 6.3×10 3 | 6.8×10 3 |
| E tower | 7.0×10 3 | 7.9×10 3 | 1.3×10 4 | 6.9×10 3 | 9.3×10 3 |
As can be seen here, adopt method of the present invention, the erosion rate of each tower test tube of A, B, C, D, E, all lower than 0.036mm/a, reaches " the small-sized experimental analogic method of testing laboratory " " good level " standard in " water coolant analysis and the test method " of production department of China PetroChemical Corporation and development division establishment; Adhere to speed all lower than 7mcm, reach " good level " standard in " the small-sized experimental analogic method of testing laboratory " in " water coolant analysis and the test method " of production department of China PetroChemical Corporation and development division establishment; Heterotrophic bacterium is all being less than 1.0 × 10
5in span of control, meet the criterion of acceptability in " the small-sized experimental analogic method of testing laboratory " in " water coolant analysis and the test method " of production department of China PetroChemical Corporation and development division establishment.
Claims (9)
1. sea water desaltination water to be applied to the method in recirculating cooling water system by one kind, the method comprises and is applied in recirculating cooling water system using sea water desaltination water as recirculated cooling water, and add inhibiter and pH adjusting agent, the pH value of recirculated cooling water is made to be 9-12, wherein, described inhibiter is made up of the first inhibiter and the second inhibiter, the weight ratio of described first inhibiter and the second inhibiter is 1:1-5, described first inhibiter is water miscible vanadate, described second inhibiter is selected from water miscible borate, silicate, one or more in sulfonated lignin and tannin, the concentration of described first inhibiter in recirculated cooling water is 20-100mg/L, the concentration of described second inhibiter in recirculated cooling water is 50-150mg/L.
2. method according to claim 1, wherein, the weight ratio of described first inhibiter and the second inhibiter is 1:1-3.
3. method according to claim 1, wherein, the concentration of described first inhibiter in recirculated cooling water is 40-80mg/L.
4. method according to claim 1, wherein, the concentration of described second inhibiter in recirculated cooling water is 60-120mg/L.
5. method according to claim 1 and 2, wherein, described pH adjusting agent is inorganic alkaline compound.
6. method according to claim 5, wherein, described pH adjusting agent is one or more in sodium hydroxide, potassium hydroxide, sodium carbonate and salt of wormwood.
7. method according to claim 1, wherein, described vanadate be selected from 12 water sodium orthovanadates, two water sodium metavanadates, anhydrous sodium metavanadate and potassium metavanadate one or more; Described borate is selected from Sodium Tetraborate and/or potassium borate; Described silicate be selected from sodium metasilicate, Starso, positive potassium silicate and potassium metasilicate one or more; Described sulfonated lignin are sodium lignosulfonate and/or calcium lignin sulphonate.
8. method according to claim 1 and 2, wherein, the chlorine ion concentration of described recirculated cooling water is 150-750mg/L.
9. method according to claim 1 and 2, wherein, the method also comprises carries out sterilization to recirculating cooling water system, the method for described sterilization be selected from ultraviolet-sterilization, ozone sterilization and hydrogen peroxide sterilization one or more.
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| CN106435596A (en) * | 2016-10-09 | 2017-02-22 | 广西大学 | Corrosion inhibitor |
| CN112645479B (en) * | 2019-10-10 | 2022-12-13 | 中国石油化工股份有限公司 | Scaling retarding method for coal gasification black ash water system |
| CN111995037A (en) * | 2020-07-15 | 2020-11-27 | 华电电力科学研究院有限公司 | Circulating water carbon steel corrosion inhibitor collaborative dosing system of thermal power plant |
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