JP5872204B2 - How to remove scale - Google Patents
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- JP5872204B2 JP5872204B2 JP2011178141A JP2011178141A JP5872204B2 JP 5872204 B2 JP5872204 B2 JP 5872204B2 JP 2011178141 A JP2011178141 A JP 2011178141A JP 2011178141 A JP2011178141 A JP 2011178141A JP 5872204 B2 JP5872204 B2 JP 5872204B2
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- 238000000034 method Methods 0.000 claims description 56
- 238000004140 cleaning Methods 0.000 claims description 55
- 230000002378 acidificating effect Effects 0.000 claims description 47
- 239000012459 cleaning agent Substances 0.000 claims description 37
- 238000001035 drying Methods 0.000 claims description 29
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 claims description 24
- 239000000463 material Substances 0.000 claims description 20
- 229940098779 methanesulfonic acid Drugs 0.000 claims description 12
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims description 8
- 238000002156 mixing Methods 0.000 claims description 5
- 239000003599 detergent Substances 0.000 description 38
- 239000000243 solution Substances 0.000 description 30
- 239000007788 liquid Substances 0.000 description 21
- 238000005406 washing Methods 0.000 description 19
- 238000012360 testing method Methods 0.000 description 18
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 14
- 238000012545 processing Methods 0.000 description 14
- 230000000694 effects Effects 0.000 description 13
- 239000000203 mixture Substances 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 238000011156 evaluation Methods 0.000 description 8
- 239000008399 tap water Substances 0.000 description 8
- 235000020679 tap water Nutrition 0.000 description 8
- AEMRFAOFKBGASW-UHFFFAOYSA-N Glycolic acid Chemical compound OCC(O)=O AEMRFAOFKBGASW-UHFFFAOYSA-N 0.000 description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 6
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 6
- 238000007654 immersion Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 235000015165 citric acid Nutrition 0.000 description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- RGHNJXZEOKUKBD-SQOUGZDYSA-N D-gluconic acid Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C(O)=O RGHNJXZEOKUKBD-SQOUGZDYSA-N 0.000 description 4
- FEWJPZIEWOKRBE-JCYAYHJZSA-N Dextrotartaric acid Chemical compound OC(=O)[C@H](O)[C@@H](O)C(O)=O FEWJPZIEWOKRBE-JCYAYHJZSA-N 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric acid Natural products [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 4
- 238000005260 corrosion Methods 0.000 description 4
- 230000006866 deterioration Effects 0.000 description 4
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 4
- LNOPIUAQISRISI-UHFFFAOYSA-N n'-hydroxy-2-propan-2-ylsulfonylethanimidamide Chemical compound CC(C)S(=O)(=O)CC(N)=NO LNOPIUAQISRISI-UHFFFAOYSA-N 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
- 239000010935 stainless steel Substances 0.000 description 4
- 239000011975 tartaric acid Substances 0.000 description 4
- 235000002906 tartaric acid Nutrition 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 3
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 238000010790 dilution Methods 0.000 description 3
- 239000012895 dilution Substances 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 229940079593 drug Drugs 0.000 description 3
- 229910017604 nitric acid Inorganic materials 0.000 description 3
- -1 silicate compound Chemical class 0.000 description 3
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 3
- RGHNJXZEOKUKBD-UHFFFAOYSA-N D-gluconic acid Natural products OCC(O)C(O)C(O)C(O)C(O)=O RGHNJXZEOKUKBD-UHFFFAOYSA-N 0.000 description 2
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 2
- 229910019142 PO4 Inorganic materials 0.000 description 2
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- 238000007605 air drying Methods 0.000 description 2
- BJEPYKJPYRNKOW-UHFFFAOYSA-N alpha-hydroxysuccinic acid Natural products OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 description 2
- KDYFGRWQOYBRFD-NUQCWPJISA-N butanedioic acid Chemical compound O[14C](=O)CC[14C](O)=O KDYFGRWQOYBRFD-NUQCWPJISA-N 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 239000002738 chelating agent Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000174 gluconic acid Substances 0.000 description 2
- 235000012208 gluconic acid Nutrition 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000004310 lactic acid Substances 0.000 description 2
- 235000014655 lactic acid Nutrition 0.000 description 2
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 2
- 239000011976 maleic acid Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000010452 phosphate Substances 0.000 description 2
- 238000005554 pickling Methods 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 2
- 235000017557 sodium bicarbonate Nutrition 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- BJEPYKJPYRNKOW-REOHCLBHSA-N (S)-malic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O BJEPYKJPYRNKOW-REOHCLBHSA-N 0.000 description 1
- SZHQPBJEOCHCKM-UHFFFAOYSA-N 2-phosphonobutane-1,2,4-tricarboxylic acid Chemical compound OC(=O)CCC(P(O)(O)=O)(C(O)=O)CC(O)=O SZHQPBJEOCHCKM-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- 229910000906 Bronze Inorganic materials 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 229910001854 alkali hydroxide Inorganic materials 0.000 description 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 1
- 239000002280 amphoteric surfactant Substances 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000000861 blow drying Methods 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000010974 bronze Substances 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- KUNSUQLRTQLHQQ-UHFFFAOYSA-N copper tin Chemical compound [Cu].[Sn] KUNSUQLRTQLHQQ-UHFFFAOYSA-N 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000001530 fumaric acid Substances 0.000 description 1
- 235000011087 fumaric acid Nutrition 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- 239000001630 malic acid Substances 0.000 description 1
- 235000011090 malic acid Nutrition 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 239000002736 nonionic surfactant Substances 0.000 description 1
- 235000012149 noodles Nutrition 0.000 description 1
- 235000019645 odor Nutrition 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
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Description
本発明は、硬質材料表面のスケールの除去方法に関する。 The present invention relates to a method for removing scale on a surface of a hard material.
従来から水道水を使用した装置内部の硬質材料表面には、水道水の硬度成分に由来する炭酸カルシウム等のスケール(石灰スケール)が析出し、蒸気発生のための装置熱伝達性の低下、あるいは水または蒸気配管系詰まり発生原因となることより、それを除去するために定期的に酸性洗浄剤による除去処理が実施されている。また、水道水以外(例えば純水や地下水、海水、アルコール)を使用する場合であっても、添加物や溶質に由来する汚れ、カルシウム等を含むスケールが付着することがある。 Conventionally, scales (lime scale) such as calcium carbonate derived from hardness components of tap water are deposited on the hard material surface inside the device using tap water, and the heat transfer of the device is reduced due to steam generation, or Since it causes clogging of the water or steam piping system, removal treatment with an acidic cleaning agent is periodically performed to remove it. Moreover, even when using water other than tap water (for example, pure water, groundwater, seawater, alcohol), a scale containing dirt, calcium, and the like derived from additives and solutes may adhere.
これらのスケールは、塩酸、硫酸、硝酸、リン酸等の無機酸、あるいはクエン酸、リンゴ酸、酢酸、スルファミン酸、グルコン酸、グリコール酸、酒石酸、乳酸、アジピン酸、コハク酸、蓚酸、フマル酸の有機酸を主成分とする酸性洗浄剤による洗浄処理にて除去出来ることは、従来から公知である。 These scales include inorganic acids such as hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, or citric acid, malic acid, acetic acid, sulfamic acid, gluconic acid, glycolic acid, tartaric acid, lactic acid, adipic acid, succinic acid, succinic acid, fumaric acid It is conventionally known that it can be removed by a cleaning treatment with an acidic cleaning agent containing as a main component an organic acid.
また、特許文献1(特表平9−508930)には、その改良された酸性洗浄剤として、マレイン酸に非イオン性、陰イオン性、陽イオン性、両性等の界面活性剤を混合した組成物が有効であるとの知見も公示されており、酸成分としてマレイン酸にスルファミン酸、メタンスルホン酸、クエン酸、リン酸、塩酸またはそれらの混合物を含む組成物も使用可能であることも言及されている。 Patent Document 1 (Japanese Patent Publication No. 9-508930) discloses a composition in which a maleic acid is mixed with a nonionic, anionic, cationic, amphoteric surfactant as an improved acidic detergent. It is also publicly known that the product is effective, and it is also possible to use a composition containing sulfamic acid, methanesulfonic acid, citric acid, phosphoric acid, hydrochloric acid or a mixture thereof as maleic acid as the acid component. Has been.
また、特許文献2(特開2011−32396)には、ステンレス製茹で麺装置に付着したでんぷん、小麦粉たんぱく質やカルシウム等を含むスケール汚れ、あるいはリン酸塩を含む特別なスケール汚れ除去剤として、メタンスルホン酸と硝酸とリン酸を含み、硝酸含有割合が1〜20重量%である酸性洗浄剤が有効であるとの開示がなされている。また本公開特許において、当該付着スケールを効率的に除去するには、当該スケール付着面を上記酸性洗浄剤を用いて洗浄した後に、アルカリ性洗浄剤にて洗浄する手法が好ましいとの言及もなされている。 Further, Patent Document 2 (Japanese Patent Application Laid-Open No. 2011-32396) discloses methane as a special scale soil removing agent containing starch, wheat flour protein, calcium, etc., which is attached to a noodle device using a stainless steel koji or phosphate. It is disclosed that an acidic detergent containing sulfonic acid, nitric acid and phosphoric acid and having a nitric acid content of 1 to 20% by weight is effective. Further, in this published patent, in order to efficiently remove the adhesion scale, it is also mentioned that a method of washing the scale adhesion surface with the above-mentioned acidic detergent and then washing with an alkaline detergent is preferable. Yes.
さらに、特許文献3(特開2008−266562)には、飲料水配管中の固形沈積物(鉄閉塞)を除去する目的に1〜14重量%のスルファミン酸、5〜10重量%のメタンスルホン酸、0.075〜0.15重量%のホスホノブタン−トリカルボン酸、0.3重量%の2−プロパノールと100重量%とするに必要な軟水を含む洗浄剤が有効であると公示されている。 Furthermore, Patent Document 3 (Japanese Patent Application Laid-Open No. 2008-266562) describes 1 to 14% by weight of sulfamic acid and 5 to 10% by weight of methanesulfonic acid for the purpose of removing solid deposits (iron clogging) in drinking water piping. , 0.075-0.15 wt.% Phosphonobutane-tricarboxylic acid, 0.3 wt.% 2-propanol and a softener necessary to make 100 wt.
本発明は、硬質材料表面に付着するスケールの効率的除去方法に関するものである。
水道水を装置に使用した場合、水道水に含まれる硬度成分が炭酸カルシウムあるいは炭酸マグネシウムを主体とした炭酸塩系スケールとして装置の硬質材料(一般的には、ステンレス板材、クロムメッキ青銅製ヒーター管)に沈着することは、よく散見される現象である。The present invention relates to a method for efficiently removing scale adhered to a hard material surface.
When tap water is used in the device, the hardness component contained in the tap water is a hard material of the device as a carbonate scale mainly composed of calcium carbonate or magnesium carbonate (generally, stainless steel plate, chrome-plated bronze heater tube) ) Is a common phenomenon.
これらの炭酸塩系の無機スケールは、一般的に公知の酸性洗浄剤による洗浄処理によって容易に除去されるものの、実際の使用態様では、使用水特性、加熱条件、使用配管種類の影響、使用過程における添加薬剤条件の影響によって、形成されるスケールは、炭酸塩に加えて水不溶性のケイ酸塩化合物(以下、シリカという)、鉄錆、リン酸塩化合物が混在したものとなる場合も多く、これらの混合無機スケールは、従来から公知の酸性洗浄剤による洗浄処理では容易に除去され難い、いわゆる、難除去性無機スケール化したものの多い状況である。 Although these carbonate-based inorganic scales are easily removed by a cleaning treatment with a generally known acidic cleaning agent, in actual usage, the characteristics of water used, the heating conditions, the influence of the type of piping used, the process of use In many cases, the scale formed due to the influence of the additive agent conditions in the mixture is a mixture of carbonate, water-insoluble silicate compound (hereinafter referred to as silica), iron rust, phosphate compound, These mixed inorganic scales are in a state where there are many so-called hard-to-removable inorganic scales that are not easily removed by a cleaning treatment with a conventionally known acidic detergent.
また、水道水以外の液体を装置に使用する場合であっても、その溶質、例えばデンプンやタンパク質、金属イオン、カルシウム等によってスケールが付着することがある。 Further, even when a liquid other than tap water is used in the apparatus, the scale may adhere due to its solute, such as starch, protein, metal ions, calcium, and the like.
本発明は、処理装置の再使用に不都合な硬質材料表面の部材劣化を生起させず、上記のように難除去性である無機スケールであっても高レベルかつ迅速に除去し得る合理的な除去する方法を提案するものである。 The present invention does not cause deterioration of the hard material surface, which is inconvenient for reuse of processing equipment, and can be removed at a high level and quickly even with inorganic scales that are difficult to remove as described above. The method to do is proposed.
本願発明は、以下に示す三つの処理ステップをもって課題が達成される。
第1ステップ:スケールが付着している硬質材料表面に対する酸性洗浄剤による洗浄処理の実施。なお、酸性洗浄剤としてメタンスルホン酸とヒドロキシカルボン酸との混合液の使用が特に好ましい。
第2ステップ:第1ステップ処理面に対する乾燥処理の実施。
第3ステップ:第2ステップ処理面に対するアルカリ性洗浄剤による洗浄処理の実施。The subject of the present invention is achieved by the following three processing steps.
1st step: Execution of the cleaning process by the acidic cleaning agent with respect to the hard material surface to which the scale adheres. It is particularly preferable to use a mixed liquid of methanesulfonic acid and hydroxycarboxylic acid as the acidic cleaning agent.
Second step: The drying process is performed on the first step processing surface.
3rd step: Implementation of a cleaning process with an alkaline cleaning agent on the 2nd step processing surface.
本願発明者は、第1ステップとしての酸性洗浄剤による洗浄処理と第3ステップとしてのアルカリ性洗浄剤による洗浄処理の中間に、第2ステップとして当該処理面に対する乾燥処理を加える手法が、効率的課題解決手段として極めて有用であることを見出し、本願発明を完成するに至った。 The inventor of the present application has an efficient problem of adding a drying process to the processing surface as the second step between the cleaning process using the acidic cleaning agent as the first step and the cleaning process using the alkaline cleaning agent as the third step. The present invention has been found to be extremely useful as a solution, and the present invention has been completed.
第1ステップで使用される酸性洗浄剤は、一般的に公知の酸性洗浄剤も使用可能であるが、塩酸、硫酸、スルファミン酸等の強酸は、優れたスケール除去効果を発揮する半面、材料腐食を生起させる可能性が大きいことより汎用性に欠ける洗浄剤群であり、その使用は制限される一方、クエン酸有機酸を主体として洗浄剤群は、材料への腐食等の影響が少ないことより、汎用性に優れている。 As the acidic detergent used in the first step, generally known acidic detergents can be used. However, strong acids such as hydrochloric acid, sulfuric acid, and sulfamic acid exhibit excellent descaling effect, but material corrosion. It is a group of detergents that lack general versatility due to its high possibility of causing odors, and its use is limited, but the group of detergents mainly composed of citric acid organic acid is less affected by corrosion, etc. Excellent in versatility.
特に本発明の目的に対し優れた特性を発揮する洗浄剤としては、メタンスルホン酸と、グリコール酸、酒石酸、乳酸、クエン酸、DL−リンゴ酸、グルコン酸等から選ばれた1種または2種以上のヒドロキシカルボン酸とを含む酸性洗浄剤であり、これらヒドロキシカルボン酸の中では、グリコール酸、酒石酸、クエン酸が、目的効果発現に関する速効性、部材劣化影響が少ないことより特に好適に使用出来る。 In particular, as a detergent exhibiting excellent characteristics for the purpose of the present invention, one or two selected from methanesulfonic acid, glycolic acid, tartaric acid, lactic acid, citric acid, DL-malic acid, gluconic acid and the like It is an acidic detergent containing the above hydroxycarboxylic acid, and among these hydroxycarboxylic acids, glycolic acid, tartaric acid, and citric acid can be particularly preferably used because they have a quick effect on the manifestation of the intended effect and less influence on member deterioration. .
また、上記混合系酸性洗浄剤は、必要に応じて一般的に使用される金属腐食防止剤、洗浄力を補強する為の界面活性剤、キレート剤を混合したものであってもよい。 The mixed acidic cleaning agent may be a mixture of a generally used metal corrosion inhibitor, a surfactant for reinforcing cleaning power, and a chelating agent.
ヒドロキシカルボン酸とメタンスルホン酸との混合物の酸性洗浄剤としての使用は、除去すべきスケールに対する相乗的に高いレベルの除去効果が発揮されること、最終的にはその除去効果レベルの高さと被処理材料の腐食・劣化影響の最少化を両立することが可能となる。 The use of a mixture of hydroxy carboxylic acid and methane sulfonic acid as an acidic detergent provides a synergistically high level of removal effect on the scale to be removed, and ultimately the high removal effect level and coverage. It is possible to simultaneously minimize the effects of corrosion and deterioration of the processing material.
ヒドロキシカルボン酸とメタンスルホン酸との混合比率については、重量比で99:1〜1:99の範囲であり、特に70:30〜30:70の範囲が好ましい。
また、上記混合系酸性洗浄剤の発揮特性を最良化するための別の因子は、洗浄液pHを最適化することであり、実処理液の最適なpH範囲は0.3〜2.5、好ましくは0.8〜2.0の範囲である。0.3以下では部材劣化への影響が大きくなること、2.5以上においてはスケール除去効果が低下する傾向があり、好ましくない。About the mixing ratio of hydroxycarboxylic acid and methanesulfonic acid, it is the range of 99: 1 to 1:99 by weight ratio, and the range of 70:30 to 30:70 is especially preferable.
In addition, another factor for optimizing the performance of the mixed acidic detergent is to optimize the pH of the cleaning solution, and the optimum pH range of the actual processing solution is preferably 0.3 to 2.5, preferably Is in the range of 0.8 to 2.0. If it is 0.3 or less, the influence on the member deterioration becomes large, and if it is 2.5 or more, the scale removal effect tends to decrease.
上記実処理液のpHは、使用直前に水酸化ナトリウム、水酸化カリウム等の水酸化アルカリ剤等を使用して調整する方法も可能であるが、実処理液に稀釈する前の配合原液調製段階で前もってpHを調製しておく方法が、洗浄作業時の煩雑性を回避できることより好ましい。
上記混合系酸性洗浄剤の一般的適用方法は、原液を濃厚な溶液で調製し、実際の使用に際しては目的性能が適切に発揮される最適な濃度に水稀釈して供される場合が多い。The pH of the actual processing solution can be adjusted by using an alkali hydroxide such as sodium hydroxide or potassium hydroxide immediately before use. The method of adjusting the pH in advance is more preferable because the complexity during the cleaning operation can be avoided.
In general, the mixed acidic detergent is generally prepared by preparing a concentrated solution as a concentrated solution and diluting with water to an optimum concentration at which the target performance is appropriately exhibited in actual use.
第2ステップで実施する乾燥処理は、酸性洗浄剤による洗浄処理後の処理面にスケールが付着・残存している場合に実施する処理であり、付着スケールは、乾燥処理によって次の第3ステップのアルカリ性洗浄剤による洗浄時において容易に剥離し易くするために実施する重要な工程である。
この乾燥処理は、自然乾燥であってもよいし、送風乾燥(室温〜300℃)、加熱乾燥のいずれでもよい。The drying process performed in the second step is a process that is performed when the scale adheres and remains on the treated surface after the cleaning process using the acidic detergent. This is an important process to be carried out in order to facilitate easy peeling at the time of washing with an alkaline detergent.
This drying treatment may be natural drying, blow drying (room temperature to 300 ° C.), or heat drying.
この乾燥処理によって、付着スケールが剥離し易くなる効果とは、酸性洗浄剤による洗浄処理によってスケール内部に空隙部が発生し、スケール自体が乾燥によって収縮し、その収縮力がスケールの材料界面付着点に対するズレ力として作用する、即ち、スケールの材料界面に対する付着力の低下(浮きの発生)を狙って実施するものである。 The effect that the drying scale easily peels off due to this drying treatment is that voids are generated inside the scale due to the washing treatment with the acidic detergent, the scale itself shrinks due to drying, and the shrinkage force is the adhesion point of the scale material interface. This is performed with the aim of reducing the adhesion force (occurrence of floating) to the material interface of the scale.
第3ステップで使用するアルカリ性洗浄剤は、アルカリ性を示す洗浄剤であれば使用することができ、特にその組成は限定されるものではない。
洗浄剤の例としては、炭酸水素ナトリウム(重曹)、炭酸ソーダをベースとしたもの、水酸化ナトリウム及び/又は水酸化カリウムを含み、更にケイ酸塩、非イオン界面活性剤、キレート剤を含むアルカリ性洗浄剤が好適に使用できる。The alkaline detergent used in the third step can be used as long as it is an alkaline detergent, and its composition is not particularly limited.
Examples of cleaning agents include sodium hydrogen carbonate (sodium bicarbonate), sodium carbonate based, sodium hydroxide and / or potassium hydroxide, and alkaline, including silicates, nonionic surfactants, chelating agents A cleaning agent can be preferably used.
本願発明を構成するもう一つ主眼点は、第1ステップとしての酸性洗浄剤による洗浄処理、第2ステップとしての乾燥処理、第3ステップとしてのアルカリ性洗浄剤による洗浄処理をこの順序にて組合せて適用することにあり、適用順序を違えると目的効果の発揮は不十分なものとなる。この適用順序が有効である理由は、現時点では必ずしも明確ではないが、酸性洗浄剤処理によるスケール構造のルーズ化、乾燥処理によるスケール構造の収縮、収縮力により付着スケールの材料界面に対する付着力の低減、その低減がアルカリ性洗浄剤処理による付着スケールの材料界面からの剥離効果の有効性を高めるといった付着異物除去に関する好ましい循環系が形成される為ではないかと推察される。 Another main point constituting the present invention is to combine the cleaning process with the acidic detergent as the first step, the drying process as the second step, and the cleaning process with the alkaline detergent as the third step in this order. If the order of application is different, the purpose and effect will be insufficient. The reason why this application order is effective is not necessarily clear at present, but the scale structure is loosened by the acidic cleaning agent treatment, the scale structure is shrunk by the drying treatment, and the adhesion force to the material interface of the adhesion scale is reduced by the shrinkage force. It can be inferred that this reduction is due to the formation of a favorable circulation system for removing adhered foreign substances such as increasing the effectiveness of the peeling effect from the material interface of the adhesion scale by the alkaline cleaning agent treatment.
本発明のスケールの除去方法は、硬質材料表面に付着したスケールを高レベルかつ迅速に除去することができ、使用水特性や添加物、使用状況の影響によって難除去性となったスケールであっても同様に高レベルかつ迅速に除去することが可能となる。 The scale removal method of the present invention is a scale that can remove scales adhering to the surface of a hard material at a high level and quickly, and has become difficult to remove due to the influence of water characteristics, additives, and usage conditions. Similarly, it can be removed at a high level and quickly.
以下、本発明の除去方法について、各ステップごとに説明する。
第1ステップにて実施する酸性洗浄剤による洗浄処理は、スケールが付着している硬質材料表面に対し最適濃度の酸性洗浄剤を最適条件にて接液することで実施される。接液とは、硬質材料表面に対し洗浄剤液を接触した状態で保持することを言い、具体的方法としては、洗浄剤液中に被処理面を有する硬質材料を浸漬する方法、硬質材料表面を有する容器内に洗浄剤液を充填・保持する方法、あるいは硬質材料表面に洗浄剤を吹き付ける、あるいは塗布する等の手法によって実施される。一般的に好ましく実施される手法は、硬質材料表面を有する容器内に洗浄剤液を充填・保持する方法である。洗浄剤の最適濃度は、スケール付着量、接液する条件によって変動するが、一般的適用条件としては、薬剤濃度は有効成分として0.1〜10wt%、好ましくは0.5〜2wt%範囲、液温は10〜100℃、処理時間:10分〜24時間で適用される。また、迅速にスケール除去を達成するには、適用薬剤濃度を高めに設定し、高液温条件にて適用する方法が進められる。Hereinafter, the removal method of the present invention will be described for each step.
The cleaning treatment with the acidic cleaning agent performed in the first step is performed by contacting the surface of the hard material on which the scale is adhered with the optimal concentration of the acidic cleaning agent under the optimal conditions. Liquid contact means holding the cleaning liquid in contact with the surface of the hard material. Specific methods include a method of immersing a hard material having a surface to be treated in the cleaning liquid, a surface of the hard material. It is carried out by a method of filling and holding a cleaning agent solution in a container having the above, or a method of spraying or applying a cleaning agent on the surface of a hard material. A generally preferred method is a method of filling and holding a cleaning liquid in a container having a hard material surface. The optimum concentration of the cleaning agent varies depending on the amount of scale adhesion and the conditions in contact with the liquid, but as a general application condition, the concentration of the drug is 0.1 to 10 wt% as an active ingredient, preferably in the range of 0.5 to 2 wt%. The liquid temperature is 10 to 100 ° C., and the treatment time is 10 minutes to 24 hours. Moreover, in order to achieve descaling quickly, a method of applying a high liquid temperature condition by setting the applied drug concentration high is advanced.
実質的な薬剤処理は、装置に対する供給液を薬剤液に置き換え、通常運転処理を実施し、処理終了後は薬剤液を排出し、すすぎ水を注入し、短時間の運転処理を行うことを数回繰り返すことによって、洗浄処理面に洗浄剤が残らないようすすぎ洗いを施すことによって実施される。 Substantial drug processing involves replacing the liquid supplied to the device with chemical liquid, performing normal operation processing, discharging the chemical liquid after the end of processing, injecting rinse water, and performing short-time operation processing. By repeating the process once, rinsing is performed so that no cleaning agent remains on the cleaning surface.
また、別処理法としては、保温機能を有する薬液タンクを用意し、その中で調製した処理液を循環ポンプにて被処理面(槽内)と薬液タンク間で規定時間循環させる(薬液循環法)方法で処理することができる。 As another treatment method, a chemical solution tank having a heat retaining function is prepared, and the treatment solution prepared therein is circulated for a specified time between the surface to be treated (in the tank) and the chemical solution tank by a circulation pump (chemical solution circulation method). ) Can be processed by the method.
第2ステップにて実施する乾燥処理は、自然乾燥あるいは送風による強制乾燥、加熱による強制乾燥のいずれの手法でも実施できる。ここで、本発明にいう乾燥とは、少なくとも被洗浄部を手で触っても液体が手に転移しない程度に液体を減少させることをいう。 The drying process performed in the second step can be performed by any method of natural drying, forced drying by blowing air, or forced drying by heating. Here, the term “drying” as used in the present invention means that the liquid is reduced to such an extent that the liquid does not transfer to the hand even if at least the portion to be cleaned is touched by hand.
第3ステップにて実施するアルカリ性洗浄剤による洗浄処理は、基本的には酸性洗浄剤による処理法に準じた手法で適用される。 The cleaning treatment with the alkaline cleaning agent performed in the third step is basically applied by a method according to the processing method with the acidic cleaning agent.
以下に本発明をより具体的に説明するため実施例を示すが、本発明はこれらの実施例に限定されるものではない。 Examples are shown below to describe the present invention more specifically, but the present invention is not limited to these Examples.
(実施例1〜7及び比較例1〜14)
供試洗浄剤は酸性洗浄剤として、表1に示した配合組成物(A−1〜7)を使用した。(Examples 1-7 and Comparative Examples 1-14)
The compound detergent (A-1-7) shown in Table 1 was used as a test cleaning agent as an acidic cleaning agent.
アルカリ性洗浄剤としては、表2に示した配合組成物B−1を使用した。 As an alkaline cleaner, the blend composition B-1 shown in Table 2 was used.
被洗浄物としては、水道水の長期使用によって下表3に示した構成元素比率のスケール付着が認められたタオルスチーマー(日板工業社製電気式タオル蒸し器)のステンレススチール製缶体内壁(被洗浄物1)より3cm×3cm片を多数切り出し、その中より近似のスケール付着量片を選定し、洗浄試験に供した。 As the objects to be cleaned, the inner wall of the stainless steel can of the towel steamer (Electric towel steamer manufactured by Niita Kogyo Co., Ltd.) that has been confirmed to adhere to the scales of constituent elements shown in Table 3 below after long-term use of tap water. A large number of 3 cm × 3 cm pieces were cut out from the washed product 1), and an approximate scale adhering amount piece was selected from them, and subjected to a washing test.
被洗浄物片(以下、試験片という)に対する洗浄処理は、規定洗浄液中に試験片を1時間静置浸漬処理する方法にて実施し、同一試験片に対し、酸性洗浄液あるいはアルカリ性洗浄液による一次洗浄処理を実施し、次いで乾燥処理、次いで酸性洗浄液あるいはアルカリ性洗浄液による二次洗浄処理を実施する方法を基本とした。
試験片数は、各洗浄処理毎に三個とし、洗浄液量は200ml、洗浄液温は60℃±1℃となるよう洗浄液容器を恒温槽内に保管した。
洗浄処理後の試験片は、200mlの新しい清水(水道水)中2分間の浸漬処理を3回繰り返すすすぎ処理を実施し、付着洗浄液を洗い流した。The cleaning of the object piece to be cleaned (hereinafter referred to as “test piece”) is performed by a method in which the test piece is allowed to stand for 1 hour in a specified cleaning solution, and the same test piece is subjected to primary cleaning with an acidic cleaning solution or an alkaline cleaning solution. Based on the method of carrying out the treatment, followed by the drying treatment and then the secondary washing treatment with the acidic washing solution or the alkaline washing solution.
The number of test pieces was three for each cleaning treatment, the amount of the cleaning solution was 200 ml, and the cleaning solution container was stored in a thermostat so that the temperature of the cleaning solution was 60 ° C. ± 1 ° C.
The test piece after the cleaning treatment was rinsed by repeating the immersion treatment for 2 minutes in 200 ml of fresh water (tap water) three times, and the attached cleaning solution was washed away.
試験片乾燥処理は、D−1あるいはD−2のいずれかの方法にて実施した。D−1として気温約25℃、相対湿度約65%の室内空間中に10時間の自然放置する方法(風乾処理)。D−2として80℃熱風中に30分間放置する方法(強制乾燥処理)である。 The test piece drying process was implemented by the method of either D-1 or D-2. D-1 is a method of leaving it naturally in an indoor space having an air temperature of about 25 ° C. and a relative humidity of about 65% (air drying treatment). D-2 is a method of standing in hot air at 80 ° C. for 30 minutes (forced drying treatment).
試験片上付着スケールの除去状態は、下記の手法にて評価した。
各洗浄処理後の試験片上スケール付着状態を肉眼にて観察し、その状態を1(付着スケール除去無し状態(洗浄前状態))〜5(付着スケール完全除去状態)間の数値割付を実施し、三試験片評価値の平均値をもってその洗浄処理条件でのスケール除去度とした。The removal state of the adhesion scale on the test piece was evaluated by the following method.
The state of scale adhesion on the test piece after each cleaning treatment is observed with the naked eye, and the state is assigned a numerical value between 1 (state without attached scale removal (state before cleaning)) to 5 (state completely removed with attached scale), The average value of the three test piece evaluation values was taken as the degree of scale removal under the cleaning treatment conditions.
各種処理条件を組合せて実施した洗浄処理試験結果を表4に示した。
表4試験結果表から、実施例1〜7の手法(酸性洗浄剤による一次洗浄処理、次いで乾燥処理、次いでアルカリ性洗浄剤による二次洗浄処理の実施)は、比較例1〜7の手法(アルカリ性洗浄剤による一次洗浄処理、次いで乾燥処理、次いで酸性洗浄剤による二次洗浄処理の実施)および比較例8〜13の手法(酸性洗浄剤による一次洗浄処理、次いで乾燥処理無し、次いでアルカリ性洗浄剤による二次洗浄処理の実施)より優れた付着異物除去効果を発揮することが確認された。
また、メタンスルホン酸とヒドロキシカルボン酸を配合した酸性洗浄剤を使用した実施例2〜5は、メタンスルホン酸単独(実施例1)、あるいはヒドロキシカルボン酸単独配合系酸性洗浄剤(実施例6〜7)より高い付着異物除去効果を発揮することが確認された。Table 4 shows the results of the cleaning treatment test carried out by combining various treatment conditions.
From the Table 4 test result table, the methods of Examples 1 to 7 (primary cleaning treatment with an acidic detergent, then drying treatment, and then secondary washing treatment with an alkaline detergent) are the same as the methods of Comparative Examples 1 to 7 (alkaline Primary cleaning treatment with a cleaning agent, followed by drying treatment, then secondary cleaning treatment with an acidic cleaning agent) and the methods of Comparative Examples 8 to 13 (primary cleaning treatment with an acidic cleaning agent, then no drying treatment, then with an alkaline cleaning agent) (Execution of secondary cleaning process) It was confirmed that the adhered foreign matter removal effect was more excellent.
Moreover, Examples 2-5 using the acidic cleaning agent which mix | blended methanesulfonic acid and hydroxycarboxylic acid are methanesulfonic acid independent (Example 1), or hydroxycarboxylic acid independent mixing type acidic cleaning agent (Example 6- 7) It was confirmed that a higher adhering foreign matter removing effect was exhibited.
(実施例8〜9及び比較例15〜18 )
被洗浄物2として、表5に示した構成元素組成のスケールが付着したステンレススチール製連続レトルト滅菌装置内容器運搬容器(キャリア)部材より5cm×5cmサイズ片を多数切り出しし、その中より近似のスケール付着量片を選定し、洗浄試験に供した。(Examples 8-9 and Comparative Examples 15-18)
As the
供試洗浄剤としては、酸性洗浄剤として表6に示した配合組成物のA−8、A−9を使用し、アルカリ性洗浄剤として表2に示した配合組成物B−2を使用した。 As the test detergent, A-8 and A-9 of the blending composition shown in Table 6 were used as the acidic detergent, and the blending composition B-2 shown in Table 2 was used as the alkaline detergent.
洗浄処理としては、酸性洗浄剤処理として処理液温50±1℃、浸漬時間3時間にて実施し、アルカリ性洗浄剤処理として処理液温50±1℃、処理時間3時間にて実施し、乾燥処理として先に示したD−1(風乾処理)にて実施した。
特性評価方法としては、実施例1〜7、比較例1〜14にて適用した手法にて実施した。The cleaning treatment is performed as an acidic cleaning agent treatment at a treatment liquid temperature of 50 ± 1 ° C. and an immersion time of 3 hours, and as an alkaline cleaning agent treatment is carried out at a treatment liquid temperature of 50 ± 1 ° C. and a treatment time of 3 hours, followed by drying The treatment was carried out by D-1 (air drying treatment) described above.
As a characteristic evaluation method, it implemented by the method applied in Examples 1-7 and Comparative Examples 1-14.
特性評価結果としては、表7のような結果となった。 The result of characteristic evaluation was as shown in Table 7.
表7試験結果表から、実施例8および9の手法(酸性洗浄剤による一次洗浄処理、次いで乾燥処理、次いでアルカリ性洗浄剤による二次洗浄処理の実施)による最終的被洗浄物上のスケール除去度は、対応する比較例15〜16および17〜18の手法(アルカリ性洗浄剤による一次洗浄処理、次いで乾燥処理、次いで酸性洗浄剤による二次洗浄処理。あるいは酸性洗浄剤による一次洗浄処理、次いで乾燥処理無し、次いでアルカリ性洗浄剤による二次洗浄処理する手法)の場合より、明らかに高いレベルとなることが確認された。
また、メタンスルホン酸と酒石酸を配合した酸性洗浄剤を使用した場合のスケール除去度は、メタンスルホン酸単独を酸性洗浄剤として使用する場合より全般的に高いレベルとなることが確認された。Table 7 From the test result table, the degree of descaling on the final object to be cleaned by the methods of Examples 8 and 9 (primary washing treatment with acidic detergent, then drying treatment, and then secondary washing treatment with alkaline detergent). Corresponding to the methods of Comparative Examples 15 to 16 and 17 to 18 (primary washing treatment with an alkaline detergent, then drying treatment, then secondary washing treatment with an acidic detergent, or primary washing treatment with an acidic detergent, then drying treatment) It was confirmed that the level was clearly higher than that in the case of none and then a secondary cleaning treatment with an alkaline detergent.
It was also confirmed that the degree of scale removal when using an acidic detergent containing methanesulfonic acid and tartaric acid was generally higher than when methanesulfonic acid alone was used as the acidic detergent.
メタンスルホン酸配合酸性洗浄液pHのスケール除去性に及ぼす影響を下記の手法にて評価した。
供試洗浄液として15倍水稀釈液pHが0.62、0.95、1.22、1.41、1.72、1.99、2.30となるように配合NaOH量を変化させたA−9の15倍水稀釈液を用いた。被洗浄物としては、被洗浄物1の3cm×3cm切り出し片を用いた。洗浄試験方法及び特性評価方法としては、洗浄液浸漬処理は処理液温50℃、浸漬時間1時間とし、その他実施法・条件は、実施例1〜7にて実施した手法に準拠した。
評価結果として洗浄液pHとスケール除去度の関係を図1に示した。図1より明らかなように、洗浄液pHが2を超えるとスケール除去度は明らかに低下することが確認された。The effect of methanesulfonic acid-containing acidic cleaning solution pH on scale removal was evaluated by the following method.
As the test washing solution, the amount of blended NaOH was changed so that the pH of the diluted solution of 15 times water was 0.62, 0.95, 1.22, 1.41, 1.72, 1.99, 2.30 A -9 15-fold water dilution was used. As an object to be cleaned, a 3 cm × 3 cm cut piece of the object to be cleaned 1 was used. As a cleaning test method and a property evaluation method, the cleaning solution immersion treatment was performed at a treatment solution temperature of 50 ° C. and an immersion time of 1 hour, and the other implementation methods and conditions were in accordance with the methods implemented in Examples 1 to 7.
As a result of the evaluation, the relationship between the cleaning solution pH and the degree of scale removal is shown in FIG. As is clear from FIG. 1, it was confirmed that when the cleaning solution pH exceeds 2, the degree of scale removal clearly decreases.
本願発明の手法と酸性洗浄剤長時間浸漬処理時のスケール除去特性の評価を下記のように実施した。
供試洗浄液及び乾燥処理の条件としては、酸性洗浄剤処理としてA−3、6倍水稀釈液を用い、アルカリ性洗浄剤処理としてB−1、6倍水稀釈液を用い、乾燥処理として80℃熱風乾燥機中30分間を行った。被洗浄物としては、スケール付着量が14.3g/m2である被洗浄物2を用いた。実施洗浄手法としては、酸洗単独法として液温50℃にて浸漬3時間、12時間、24時間の各連続処理を行った。そして本願方法として液温50℃にて浸漬3時間の酸性洗浄剤による洗浄、次いで乾燥処理、次いで液温50℃にて浸漬1時間のアルカリ性洗浄剤による洗浄処理を行った。そして従来法として、液温50℃にて3時間の酸性洗浄剤による洗浄、次いで液温50℃にて浸漬1.5時間および3時間のアルカリ性洗浄剤による洗浄処理を行った。
特性評価法としては、実施例8にて実施した手法に準拠した。評価結果として合計処理時間に対するスケール除去度の関係を図2に示した。図2より明らかなように、本願手法は、酸洗単独法および従来法より短時間の処理にてスケールを完全除去できることが確認された。The method of the present invention and the evaluation of the scale removal characteristics during the long-time immersion treatment of the acidic cleaning agent were carried out as follows.
The conditions of the test cleaning solution and the drying treatment were as follows: A-3, 6-fold water dilution solution was used as the acidic cleaning treatment; B-1, 6-fold water dilution solution was used as the alkaline cleaning treatment; 30 minutes in a hot air dryer. The article to be cleaned, the scale deposition amount was used the
As a characteristic evaluation method, the method performed in Example 8 was used. FIG. 2 shows the relationship between the scale removal degree and the total processing time as an evaluation result. As is clear from FIG. 2, it was confirmed that the method of the present application can completely remove the scale in a shorter time than the pickling method and the conventional method.
Claims (1)
A method of sequentially performing a cleaning process with an acidic cleaning agent, then a drying process, and then a cleaning process with an alkaline cleaning agent in this order on the surface of the hard material to which the scale is attached, and the methanesulfonic acid is used as the acidic cleaning agent. And a hydroxycarboxylic acid mixed in a mixing ratio of 30:70 to 70:30, and having a pH in the range of 0.8 to 2.0. .
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