JPH11131381A - Corrosion inhibitor for digester and / or black liquor canister in kraft pulp manufacturing process and method of inhibiting corrosion - Google Patents
Corrosion inhibitor for digester and / or black liquor canister in kraft pulp manufacturing process and method of inhibiting corrosionInfo
- Publication number
- JPH11131381A JPH11131381A JP9300297A JP30029797A JPH11131381A JP H11131381 A JPH11131381 A JP H11131381A JP 9300297 A JP9300297 A JP 9300297A JP 30029797 A JP30029797 A JP 30029797A JP H11131381 A JPH11131381 A JP H11131381A
- Authority
- JP
- Japan
- Prior art keywords
- acid
- black liquor
- digester
- corrosion
- kraft pulp
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000005260 corrosion Methods 0.000 title claims abstract description 54
- 230000007797 corrosion Effects 0.000 title claims abstract description 54
- 239000003112 inhibitor Substances 0.000 title claims abstract description 24
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 22
- 239000002655 kraft paper Substances 0.000 title claims abstract description 18
- 230000002401 inhibitory effect Effects 0.000 title abstract description 11
- 239000000178 monomer Substances 0.000 claims abstract description 29
- 238000000034 method Methods 0.000 claims abstract description 16
- 150000003460 sulfonic acids Chemical class 0.000 claims abstract description 13
- 229910052783 alkali metal Inorganic materials 0.000 claims abstract description 11
- -1 alkali metal salts Chemical class 0.000 claims abstract description 10
- 150000003863 ammonium salts Chemical class 0.000 claims abstract description 10
- 229920001577 copolymer Polymers 0.000 claims abstract description 9
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims abstract description 7
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 claims abstract description 6
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims abstract description 5
- JAHNSTQSQJOJLO-UHFFFAOYSA-N 2-(3-fluorophenyl)-1h-imidazole Chemical compound FC1=CC=CC(C=2NC=CN=2)=C1 JAHNSTQSQJOJLO-UHFFFAOYSA-N 0.000 claims abstract description 5
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims abstract description 5
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 claims abstract description 5
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 claims abstract description 5
- 239000011976 maleic acid Substances 0.000 claims abstract description 5
- LVHBHZANLOWSRM-UHFFFAOYSA-N methylenebutanedioic acid Natural products OC(=O)CC(=C)C(O)=O LVHBHZANLOWSRM-UHFFFAOYSA-N 0.000 claims abstract description 5
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 claims abstract description 5
- 229920000536 2-Acrylamido-2-methylpropane sulfonic acid Polymers 0.000 claims abstract description 4
- XHZPRMZZQOIPDS-UHFFFAOYSA-N 2-Methyl-2-[(1-oxo-2-propenyl)amino]-1-propanesulfonic acid Chemical compound OS(=O)(=O)CC(C)(C)NC(=O)C=C XHZPRMZZQOIPDS-UHFFFAOYSA-N 0.000 claims abstract description 4
- OFNISBHGPNMTMS-UHFFFAOYSA-N 3-methylideneoxolane-2,5-dione Chemical compound C=C1CC(=O)OC1=O OFNISBHGPNMTMS-UHFFFAOYSA-N 0.000 claims abstract description 4
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 claims abstract description 4
- VSSGDAWBDKMCMI-UHFFFAOYSA-N 2-methyl-2-(2-methylprop-2-enoylamino)propane-1-sulfonic acid Chemical compound CC(=C)C(=O)NC(C)(C)CS(O)(=O)=O VSSGDAWBDKMCMI-UHFFFAOYSA-N 0.000 claims abstract description 3
- 239000012141 concentrate Substances 0.000 claims description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
- 230000000694 effects Effects 0.000 description 10
- 238000006116 polymerization reaction Methods 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 150000003839 salts Chemical class 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 description 4
- QUSNBJAOOMFDIB-UHFFFAOYSA-N Ethylamine Chemical compound CCN QUSNBJAOOMFDIB-UHFFFAOYSA-N 0.000 description 4
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 4
- BAVYZALUXZFZLV-UHFFFAOYSA-N Methylamine Chemical compound NC BAVYZALUXZFZLV-UHFFFAOYSA-N 0.000 description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 238000010411 cooking Methods 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 3
- 230000005764 inhibitory process Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000003505 polymerization initiator Substances 0.000 description 3
- 229910052979 sodium sulfide Inorganic materials 0.000 description 3
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- LCPVQAHEFVXVKT-UHFFFAOYSA-N 2-(2,4-difluorophenoxy)pyridin-3-amine Chemical compound NC1=CC=CN=C1OC1=CC=C(F)C=C1F LCPVQAHEFVXVKT-UHFFFAOYSA-N 0.000 description 2
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 229910000975 Carbon steel Inorganic materials 0.000 description 2
- 229910001209 Low-carbon steel Inorganic materials 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 150000008064 anhydrides Chemical class 0.000 description 2
- 239000010962 carbon steel Substances 0.000 description 2
- MAYPHUUCLRDEAZ-UHFFFAOYSA-N chlorine peroxide Chemical compound ClOOCl MAYPHUUCLRDEAZ-UHFFFAOYSA-N 0.000 description 2
- HPNMFZURTQLUMO-UHFFFAOYSA-N diethylamine Chemical compound CCNCC HPNMFZURTQLUMO-UHFFFAOYSA-N 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229920001778 nylon Polymers 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 150000002978 peroxides Chemical class 0.000 description 2
- 159000000001 potassium salts Chemical class 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- CHQMHPLRPQMAMX-UHFFFAOYSA-L sodium persulfate Substances [Na+].[Na+].[O-]S(=O)(=O)OOS([O-])(=O)=O CHQMHPLRPQMAMX-UHFFFAOYSA-L 0.000 description 2
- 159000000000 sodium salts Chemical class 0.000 description 2
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 239000012085 test solution Substances 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- YDIKCZBMBPOGFT-DIONPBRTSA-N (2s,3r,4s,5s,6r)-2-[5,7-dihydroxy-2-(4-hydroxy-3,5-dimethoxyphenyl)chromenylium-3-yl]oxy-6-(hydroxymethyl)oxane-3,4,5-triol;chloride Chemical compound [Cl-].COC1=C(O)C(OC)=CC(C=2C(=CC=3C(O)=CC(O)=CC=3[O+]=2)O[C@H]2[C@@H]([C@@H](O)[C@H](O)[C@@H](CO)O2)O)=C1 YDIKCZBMBPOGFT-DIONPBRTSA-N 0.000 description 1
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- DZSVIVLGBJKQAP-UHFFFAOYSA-N 1-(2-methyl-5-propan-2-ylcyclohex-2-en-1-yl)propan-1-one Chemical group CCC(=O)C1CC(C(C)C)CC=C1C DZSVIVLGBJKQAP-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 238000005227 gel permeation chromatography Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000004255 ion exchange chromatography Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 238000002161 passivation Methods 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 239000005077 polysulfide Substances 0.000 description 1
- 229920001021 polysulfide Polymers 0.000 description 1
- 150000008117 polysulfides Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical compound [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 description 1
- 235000019982 sodium hexametaphosphate Nutrition 0.000 description 1
- HYHCSLBZRBJJCH-UHFFFAOYSA-N sodium polysulfide Chemical compound [Na+].S HYHCSLBZRBJJCH-UHFFFAOYSA-N 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 235000010265 sodium sulphite Nutrition 0.000 description 1
- AKHNMLFCWUSKQB-UHFFFAOYSA-L sodium thiosulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=S AKHNMLFCWUSKQB-UHFFFAOYSA-L 0.000 description 1
- 235000019345 sodium thiosulphate Nutrition 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Paper (AREA)
Abstract
(57)【要約】
【課題】 クラフトパルプ製造工程における蒸解釜
及び黒液濃縮缶の腐食を抑制するのに有効な腐食抑制剤
及び、これを用いてなる腐食抑制方法を提供する。
【解決手段】 アクリル酸、メタクリル酸、マレイン
酸、無水マレイン酸、イタコン酸、無水イタコン酸およ
びこれらのアルカリ金属塩、アンモニウム塩から選ばれ
た1種以上の不飽和カルボン酸系単量体と、2−アクリ
ルアミド−2−メチルプロパンスルホン酸、2−メタク
リルアミド−2−メチルプロパンスルホン酸、およびこ
れらのアルカリ金属塩、アンモニウム塩から選ばれた1
種以上の不飽和スルホン酸系単量体を主要成分し、該不
飽和カルボン酸系単量体を70〜99モル%、該不飽和
スルホン酸系単量体を1〜30モル%より構成される水
溶性共重合体を含有することを特徴とするクラフトパル
プ製造工程における蒸解釜及び/あるいは黒液濃縮缶の
腐食抑制剤、及びこれを蒸解釜の循環白液及び/あるい
は黒液に対して1〜100ppmの範囲で添加する蒸解
釜及び/あるいは黒液濃縮缶の腐食抑制方法。PROBLEM TO BE SOLVED: To provide a corrosion inhibitor effective for suppressing corrosion of a digester and a black liquor concentrator in a kraft pulp manufacturing process, and a corrosion inhibitor method using the same. SOLUTION: One or more unsaturated carboxylic acid monomers selected from acrylic acid, methacrylic acid, maleic acid, maleic anhydride, itaconic acid, itaconic anhydride and alkali metal salts and ammonium salts thereof, 1 selected from 2-acrylamido-2-methylpropanesulfonic acid, 2-methacrylamido-2-methylpropanesulfonic acid, and alkali metal salts and ammonium salts thereof.
The unsaturated sulfonic acid-based monomer is composed of at least 70 to 99 mol% of the unsaturated sulfonic acid-based monomer and 1 to 30 mol% of the unsaturated sulfonic acid-based monomer. A corrosion inhibitor for a digester and / or a black liquor concentrator in a kraft pulp manufacturing process, characterized by containing a water-soluble copolymer, A method for inhibiting corrosion of a digester and / or a black liquor concentrator added in the range of 1 to 100 ppm.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、紙・パルプ工業の
クラフトパルプ製造工程の蒸解釜、及び/あるいは蒸解
廃液(以下「黒液」と称する)を濃縮する黒液濃縮缶の
腐食抑制剤及びこれらの腐食抑制方法に関するものであ
る。[0001] The present invention relates to a corrosion inhibitor for a black liquor concentrator for concentrating a digester and / or a cooking liquor (hereinafter referred to as "black liquor") in a kraft pulp manufacturing process of the paper and pulp industry. The present invention relates to these corrosion control methods.
【0002】[0002]
【従来の技術】クラフトパルプは、原料である木材チッ
プを、水酸化ナトリウムと硫化ナトリウムを主成分とす
る蒸解液中で高温高圧下、蒸煮することによって、木材
中に含まれるリグリンを溶出せしめパルプ化することに
よって製造される。蒸解液は白液を、場合によっては一
部黒液で希釈して使用され、蒸解温度は約170℃であ
る。白液の組成は、概略水酸化ナトリウム55〜100
g/L、硫化ナトリウム18〜45g/L、炭酸ナトリ
ウム10〜30g/L(いずれもNa2O換算)を含む水
溶液である。一方、蒸解後の廃液は黒液と呼ばれ、水酸
化ナトリウム、硫化ナトリウム、炭酸ナトリウム、多硫
化ナトリウム、硫酸ナトリウム、チオ硫酸ナトリウム、
亜硫酸ナトリウム、塩化ナトリウムなどの無機塩類を含
有し、黒液濃縮缶において、約120℃の温度で60〜
75%にまで濃縮した後、回収ボイラで焼却処理されて
いる。このように、蒸解釜や黒液濃縮缶は高温度で、か
つ塩類を多く含む水溶液に曝されており、その装置の材
料、特に炭素鋼を激しく腐食する原因となっている。2. Description of the Related Art Kraft pulp is made by boiling wood chips as a raw material in a cooking liquor containing sodium hydroxide and sodium sulfide at a high temperature and a high pressure to elute ligulin contained in the wood. It is manufactured by The cooking liquor is used by diluting white liquor, in some cases with black liquor, and has a cooking temperature of about 170 ° C. The composition of the white liquor is approximately sodium hydroxide 55 to 100.
g / L, 18 to 45 g / L of sodium sulfide, and 10 to 30 g / L of sodium carbonate (all in terms of Na 2 O). On the other hand, the waste liquid after digestion is called black liquor, and sodium hydroxide, sodium sulfide, sodium carbonate, sodium polysulfide, sodium sulfate, sodium thiosulfate,
It contains inorganic salts such as sodium sulfite and sodium chloride.
After being concentrated to 75%, it is incinerated in a recovery boiler. As described above, the digester and the black liquor concentrator are exposed to an aqueous solution containing a large amount of salts at a high temperature, and cause severe corrosion of the material of the apparatus, particularly carbon steel.
【0003】そこでこの腐食を抑制する手段として、ス
テンレスライニング、あるいはポリサルファイドの添加
による炭素鋼の不導態化などの方法が採られてきた。[0003] Therefore, as a means for suppressing this corrosion, a method such as stainless steel lining or passivation of carbon steel by adding polysulfide has been adopted.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、これま
での改良方法をもってしても蒸解釡や黒液濃縮缶の腐食
を満足に抑制するには至らず、より効果の高い腐食抑制
策が望まれている。本発明の目的は、かかる未解決の問
題を解決するためになされたもので、クラフトパルプ製
造工程の蒸解釡、黒液濃縮缶の腐食抑制剤、及びこれら
の腐食抑制方法を提供することにある。However, even with the above-mentioned improved method, the corrosion of the digester and the black liquor can has not been satisfactorily suppressed, and a more effective corrosion control measure is desired. I have. An object of the present invention is to solve such an unsolved problem, and it is an object of the present invention to provide a corrosion inhibitor for a digester kama, a black liquor concentrating can in a kraft pulp manufacturing process, and a method for inhibiting these corrosions. .
【0005】[0005]
【課題を解決する手段】本発明者は、クラフトパルプ製
造工程の蒸解釡及び黒液濃縮缶における腐食を抑制する
方法を確立することを意図し、蒸解釡及び黒液濃縮缶の
それぞれの運転条件下効果を示す腐食抑制剤及びそれを
用いてなる蒸解釡及び黒液濃縮缶の腐食抑制方法を鋭意
検討した結果、特定の不飽和カルボン酸系単量体と、特
定の不飽和スルホン酸系単量体を主要成分としてなる水
溶性共重合体が、高い腐食抑制効果を示すことを見いだ
し、本発明を完成するに至った。The inventor of the present invention intends to establish a method for suppressing corrosion in a digester kama and a black liquor can in a kraft pulp manufacturing process. As a result of intensive studies on a corrosion inhibitor exhibiting the following effects and a method for inhibiting the corrosion of digesters and black liquor cans using the same, it was found that a specific unsaturated carboxylic acid monomer and a specific unsaturated sulfonic acid monomer were used. The inventors have found that a water-soluble copolymer containing a monomer as a main component exhibits a high corrosion inhibiting effect, and have completed the present invention.
【0006】すなわち、本請求項1の発明は、アクリル
酸、メタクリル酸、マレイン酸、無水マレイン酸、イタ
コン酸、無水イタコン酸及びこれらのアルカリ金属塩、
アンモニウム塩から選ばれた1種以上の不飽和カルボン
酸系単量体と、2−アクリルアミド−2−メチルプロパ
ンスルホン酸、2−メタクリルアミド−2−メチルプロ
パンスルホン酸及びこれらのアルカリ金属塩、アンモニ
ウム塩から選ばれた1種以上の不飽和スルホン酸系単量
体を主要成分とし、不飽和スルホン酸系単量体が全単量
体の1〜30モル%であり、且つ、重量平均分子量が5
00〜20,000である水溶性共重合体を含有するこ
とを特徴とするクラフトパルプ製造工程における蒸解釜
及び/あるいは黒液濃縮缶の腐食抑制剤であり、 請求項
2の発明は、クラフトパルプ製造工程の蒸解釜白液に対
して、請求項1記載の腐食抑制剤を1〜100ppm添
加することを特徴とするクラフトパルプ製造工程におけ
る蒸解釜の腐食抑制方法であり、請求項3の発明は、ク
ラフトパルプ製造工程の黒液に対して、請求項1記載の
黒液濃縮缶の腐食抑制剤を1〜100ppm添加するこ
とを特徴とするクラフトパルプ製造工程における黒液濃
縮缶の腐食抑制方法である。That is, the present invention relates to acrylic acid, methacrylic acid, maleic acid, maleic anhydride, itaconic acid, itaconic anhydride and alkali metal salts thereof,
At least one unsaturated carboxylic acid monomer selected from ammonium salts, 2-acrylamido-2-methylpropanesulfonic acid, 2-methacrylamido-2-methylpropanesulfonic acid and alkali metal salts thereof, ammonium One or more unsaturated sulfonic acid-based monomers selected from salts as a main component, the unsaturated sulfonic acid-based monomer is 1 to 30 mol% of all monomers, and the weight average molecular weight is 5
A corrosion inhibitor for a digester and / or a black liquor concentrator in a kraft pulp manufacturing process, characterized in that the kraft pulp production process is characterized in that the kraft pulp is a corrosion inhibitor. A method for inhibiting corrosion of a digester in a kraft pulp production process, wherein 1 to 100 ppm of the corrosion inhibitor according to claim 1 is added to the digester white liquor in the production process. A method for inhibiting corrosion of a black liquor concentrate in a kraft pulp production process, which comprises adding 1 to 100 ppm of the corrosion inhibitor for a black liquor concentrate can according to claim 1 to black liquor in a kraft pulp production process. is there.
【0007】[0007]
【発明の実施の形態】以下、本発明について詳細に説明
する。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail.
【0008】本発明の水溶性共重合体は、不飽和カルボ
ン酸(その無水物を包含する)系単量体と不飽和スルホ
ン酸系単量体を主要成分として重合させることによって
得られる。不飽和カルボン酸系単量体は、アクリル酸、
メタクリル酸、マレイン酸、無水マレイン酸、イタコン
酸、無水イタコン酸およびこれらのアルカリ金属塩、ア
ンモニウム塩から選ばれた1種以上であり、アルカリ金
属塩の例としては、ナトリウム塩、カリウム塩があり、
アンモニウム塩としてはアンモニア、モノメチルアミ
ン、ジメチルアミン、モノエチルアミン、ジエチルアミ
ンなどのアミン類との塩がある。The water-soluble copolymer of the present invention can be obtained by polymerizing an unsaturated carboxylic acid (including its anhydride) monomer and an unsaturated sulfonic acid monomer as main components. Unsaturated carboxylic acid monomers include acrylic acid,
Methacrylic acid, maleic acid, maleic anhydride, itaconic acid, itaconic anhydride and at least one selected from alkali metal salts and ammonium salts thereof. Examples of the alkali metal salts include sodium salts and potassium salts. ,
Examples of the ammonium salt include salts with amines such as ammonia, monomethylamine, dimethylamine, monoethylamine, and diethylamine.
【0009】一方、不飽和スルホン酸系単量体は、2−
アクリルアミド−2−メチルプロパンスルホン酸、2−
メタクリルアミド−2−メチルプロパンスルホン酸、お
よびこれらのアルカリ金属塩、アンモニウム塩から選ば
れた1種以上であり、アルカリ金属塩の例としては、ナ
トリウム塩、カリウム塩があり、アンモニウム塩として
はアンモニア、モノメチルアミン、ジメチルアミン、モ
ノエチルアミン、ジエチルアミンなどの塩がある。On the other hand, the unsaturated sulfonic acid monomer is 2-
Acrylamide-2-methylpropanesulfonic acid, 2-
Methacrylamide-2-methylpropanesulfonic acid, and at least one selected from alkali metal salts and ammonium salts thereof. Examples of the alkali metal salts include sodium salts and potassium salts, and ammonium salts include ammonia. , Monomethylamine, dimethylamine, monoethylamine, diethylamine and the like.
【0010】本発明の水溶性共重合体において、不飽和
スルホン酸系単量体は全単量体の1〜30モル%3〜2
5モル%、さらに好ましくは、5〜20モル%である。
不飽和スルホン酸系単量体が全単量体の1〜30モル%
の外では、本発明の目的とする効果が十分発揮されず実
用的でない。[0010] In the water-soluble copolymer of the present invention, the unsaturated sulfonic acid-based monomer accounts for 1 to 30 mol% of the entire monomer.
It is 5 mol%, more preferably 5 to 20 mol%.
Unsaturated sulfonic acid monomer is 1 to 30 mol% of all monomers
In addition, the effects intended by the present invention are not sufficiently exhibited, and are not practical.
【0011】本発明の水溶性共重合体においては、また
本発明の目的とする効果が損なわれない範囲において他
の不飽和化合物を含むことを妨げるものではない。The water-soluble copolymer of the present invention does not prevent inclusion of other unsaturated compounds as long as the effects of the present invention are not impaired.
【0012】本発明の水溶性共重合体において、その重
量平均分子量は500〜20,000、好ましくは10
00〜15,000、さらに好ましくは2,000〜1
0,000である。重量平均分子量が500未満、ある
いは20,000より大きいものでは、腐食防止効果が
低下し、実用的でない。The water-soluble copolymer of the present invention has a weight average molecular weight of 500 to 20,000, preferably 10 to 20,000.
00 to 15,000, more preferably 2,000 to 1
It is 0000. If the weight-average molecular weight is less than 500 or greater than 20,000, the corrosion-preventing effect is reduced and is not practical.
【0013】これら構成成分や、組成比、分子量は本発
明者らの研究の結果、最適範囲として定めたものであ
り、この範囲の外でもそれなりの効果を有するものがあ
るが、経済的にみて効率が良いとはいえない。These constituents, composition ratios and molecular weights have been determined as optimal ranges as a result of the studies of the present inventors, and some of them have some effects outside this range, but from an economical point of view. It is not efficient.
【0014】本発明の重合体の製造方法は特に限定され
るものではないが、例えば、不飽和カルボン酸系単量体
と不飽和スルホン酸系単量体とを、遊離の状態、あるい
はアルカリ金属塩、あるいはアンモニウム塩として重合
反応に供することによって行われる。またマレイン酸、
イタコン酸はしれぞれ無水物として重合反応に供しても
よい。The method for producing the polymer of the present invention is not particularly limited. For example, an unsaturated carboxylic acid monomer and an unsaturated sulfonic acid monomer may be used in a free state or in an alkali metal. It is carried out by subjecting to a polymerization reaction as a salt or an ammonium salt. Maleic acid,
Itaconic acid may each be subjected to the polymerization reaction as an anhydride.
【0015】本発明の重合に用いられる重合開始剤は、
重合条件によっても変わるので本発明に制約を加えるも
のではないが、重合条件下で分解して遊離基を生成する
物質であればよく、例えば過硫酸ナトリウム、過酸化水
素、過酸化塩素、 ブチルヒドロパーオキサイド等の過酸
化物、アゾビスイソブチロニトリル等のアゾ化合物が挙
げられる。重合開始剤の使用量は、用いる重合開始剤の
種類、重合条件により異なるが、例えば過酸化水素では
不飽和単量体に対して0.5〜10モル%、好ましくは
1〜5モル%である。The polymerization initiator used in the polymerization of the present invention is:
Although it does not limit the present invention because it varies depending on the polymerization conditions, any substance capable of decomposing under the polymerization conditions to generate free radicals may be used, such as sodium persulfate, hydrogen peroxide, chlorine peroxide, and butylhydrogen. Examples include peroxides such as peroxides and azo compounds such as azobisisobutyronitrile. The amount of the polymerization initiator used depends on the type of polymerization initiator used and the polymerization conditions. For example, in the case of hydrogen peroxide, the amount is 0.5 to 10 mol%, preferably 1 to 5 mol%, based on the amount of the unsaturated monomer. is there.
【0016】重合に用いる溶媒としては水が好ましく用
いられるが、アルコール類、ジオキサン等の有機溶媒を
単独に、あるいは水−有機溶媒混合系にして用いること
もできる。As a solvent used in the polymerization, water is preferably used, but an organic solvent such as alcohols and dioxane can be used alone or in a water-organic solvent mixed system.
【0017】重合温度は、80〜110℃が好ましい。
80℃を下回る温度で重合させると、未反応の単量体が
多量に残ってしまうことになり好ましくないことがあ
る。The polymerization temperature is preferably from 80 to 110 ° C.
If the polymerization is carried out at a temperature lower than 80 ° C., a large amount of unreacted monomers may remain, which is not preferable.
【0018】本発明の腐食抑制剤の適用にあたってその
添加量は、蒸解釜の腐食抑制のためには白液に対して1
〜100ppm、好ましくは2〜80ppm、さらに好
ましくは5〜50ppmであり、黒液濃縮缶の腐食抑制
のためには黒液にに対して1〜100ppm、好ましく
は2〜80ppm、さらに好ましくは5〜50ppmで
ある。蒸解釜、黒液濃縮缶のいづれの場合も添加量が1
ppm未満では本発明の目的とする効果が充分でなく、
また100ppmを越えた添加では効果は充分に認めら
れるが、添加量に見合った効果の向上は認められず、経
済的見地から好ましくない。When the corrosion inhibitor of the present invention is applied, the amount of the additive added is 1 to white liquor for inhibiting corrosion of the digester.
From 100 ppm, preferably from 2 to 80 ppm, more preferably from 5 to 50 ppm, and more preferably from 1 to 100 ppm, preferably from 2 to 80 ppm, more preferably from 5 to 50 ppm, based on the black liquor for inhibiting corrosion of the black liquor concentration can. It is 50 ppm. Addition amount is 1 for both digesters and black liquor cans
If it is less than ppm, the effect intended by the present invention is not sufficient,
Addition of more than 100 ppm has a sufficient effect, but does not improve the effect in proportion to the amount added, which is not preferable from an economic viewpoint.
【0019】本発明の腐食抑制剤の蒸解釜または黒液濃
縮缶への添加方法は特に限定されるものではないが、蒸
解釜の腐食抑制のためには蒸解釜内であり、例えば循環
白液中に添加される。黒液濃縮缶の場合には、黒液濃縮
缶内に直接、あるいはパルプ蒸解釜から排出され黒液濃
縮缶に入るまでの液中に添加するのが操作上便利であ
る。本発明の腐食抑制剤は炭酸カルシウムを主体とした
スケール抑制にも効果があり、従ってパルプ蒸解釜の循
環白液中に加えると蒸解釜のスケール抑制とともに腐食
抑制も達せられ好都合なことがある。しかし蒸解釜循環
白液中に添加した腐食抑制剤はパルプに付着して製紙工
程に送られ、黒液濃縮缶に入る液中に残るの腐食抑制の
濃度は極めて低くなるので、黒液濃縮缶に直接、あるい
はパルプ蒸解釜から排出され黒液濃縮缶に入るまでの液
中に追加添加することが必要である。The method of adding the corrosion inhibitor of the present invention to a digester or a black liquor concentrator is not particularly limited. Is added during. In the case of a black liquor concentrating can, it is convenient in operation to add it directly into the black liquor concentrating can or into the liquid discharged from the pulp digester and entering the black liquor concentrating can. The corrosion inhibitor of the present invention is also effective in controlling the scale mainly composed of calcium carbonate. Therefore, when it is added to the circulating white liquor of the pulp digester, it can be advantageous that not only the scale of the digester but also the corrosion can be suppressed. However, the corrosion inhibitor added to the white liquor circulating in the digester adheres to the pulp and is sent to the papermaking process, and the concentration of the corrosion inhibitor remaining in the liquor entering the black liquor concentrator becomes extremely low. It needs to be added directly to the liquor or into the liquor from the pulp digester to the black liquor canister.
【0020】また、本発明の本来の目的が達成される限
り、他の任意の成分の添加剤を併用することに何ら制限
を加えるものではない。Further, as long as the original object of the present invention is achieved, there is no limitation on the use of additives of other optional components.
【0021】[0021]
【実施例】以下、実施例によって本発明を具体的に説明
するが、本発明はこれらの実施例に限定されるものでは
ない。EXAMPLES The present invention will be described below in detail with reference to examples, but the present invention is not limited to these examples.
【0022】[重合体の製造] 重合体−Gの製造:500mLの5つ口フラスコに無水
マレイン酸34.0g(0.35モル)及び水50gを加
え、これに50%水酸化ナトリウム水溶液を徐々に加え
て無水マレイン酸を溶解し、pHを6に調整した。フラ
スコ内を窒素ガス雰囲気とし、溶液を90℃に加温し、
撹拌しつつ、滴下ロートより過硫酸ナトリウム4.2g
を水50gで溶解した液、およびアクリル酸10.7g
(0.15モル)、2−アクリルアミド−2−メチルプロ
パンスルホン酸11.0g(0.053モル)を水50g
に溶解させた溶液をそれぞれゆっくり滴下した。滴下後
90℃にてさらに3時間撹拌を続け、水溶性共重合体水
溶液を得た。イオンクロマトグラフィーにより残存単量
体濃度を測定したところ、未反応の単量体は存在せず、
反応率は実質100%であることを確認した。ゲル浸透
クロマトグラフィー測定の結果、分子量は5,500で
あった。[Production of Polymer] Production of Polymer-G: To a 500 mL five-necked flask, 34.0 g (0.35 mol) of maleic anhydride and 50 g of water were added, and a 50% aqueous sodium hydroxide solution was added thereto. The maleic anhydride was dissolved slowly to adjust the pH to 6. The atmosphere in the flask was set to a nitrogen gas atmosphere, and the solution was heated to 90 ° C.
While stirring, 4.2 g of sodium persulfate from the dropping funnel
In 50 g of water and 10.7 g of acrylic acid
(0.15 mol), 11.0 g (0.053 mol) of 2-acrylamido-2-methylpropanesulfonic acid in 50 g of water
Were slowly added dropwise. After dropping, stirring was further continued at 90 ° C. for 3 hours to obtain a water-soluble copolymer aqueous solution. When the residual monomer concentration was measured by ion chromatography, there was no unreacted monomer,
It was confirmed that the reaction rate was substantially 100%. As a result of gel permeation chromatography measurement, the molecular weight was 5,500.
【0023】本発明の効果の評価には、得られた水溶性
共重合体水溶液そのままを用いて行った。The effect of the present invention was evaluated by using the obtained aqueous solution of the water-soluble copolymer as it was.
【0024】同様にして、各成分比を変えて各種重合体
を得た。実施例、比較例に用いた重合体の組成を表1に
示した。Similarly, various polymers were obtained by changing the ratio of each component. Table 1 shows the compositions of the polymers used in the examples and comparative examples.
【0025】また、比較として、冷却水系の腐食抑制剤
として知られている次の化合物を同様にして用いた。For comparison, the following compounds, which are known as corrosion inhibitors for cooling water systems, were similarly used.
【0026】化合物V:ヘキサメタリン酸ナトリウム
(米山化学工業製) 化合物W:1−ヒドロキシエチリデン−1−ジホスホン
酸(日本モンサント製、商品名:デイクエスト201
0)Compound V: sodium hexametaphosphate (manufactured by Yoneyama Chemical Industry) Compound W: 1-hydroxyethylidene-1-diphosphonic acid (manufactured by Nippon Monsanto, trade name: Dequest 201)
0)
【0027】[0027]
【表1】 [Table 1]
【0028】[腐食抑制効果の評価] A製紙工場連続蒸解釜の循環白液における腐食抑制
試験 循環白液を100Lづつガラスビーカーに取り、攪拌し
ながら、腐食抑制剤を所定量添加し均一に溶解させた。
この試験液をステンレス製オートクレーブに移し入れた
後、あらかじめ重量及び表面積を測定した軟鋼(JIS
G 3141SPCC−SB)テストピースを入れ、1
75℃のオイルバス中で24時間静置した。次いでオー
トクレーブを水道水に浸漬急冷した後、テストピースを
取り出し、表面の腐食生成物をナイロンたわしで除去し
た後、水洗、乾燥した。[Evaluation of Corrosion Inhibition Effect] A Corrosion Inhibition Test in Circulating White Liquor of Continuous Digester in Paper Mill A 100 L of the circulating white liquor was placed in a glass beaker, and a predetermined amount of a corrosion inhibitor was added while stirring to dissolve uniformly. I let it.
After transferring this test solution into a stainless steel autoclave, the weight and surface area of the mild steel (JIS) were measured in advance.
G 3141 SPCC-SB) Insert the test piece,
It was left still in an oil bath at 75 ° C. for 24 hours. Next, the autoclave was immersed in tap water and quenched, the test piece was taken out, and the corrosion products on the surface were removed with a nylon scrubber, followed by washing with water and drying.
【0029】試験前と試験後のテストピースの重量差を
測定し、腐食速度に換算した。結果を表2に示した。The weight difference between the test pieces before and after the test was measured and converted to the corrosion rate. The results are shown in Table 2.
【0030】[0030]
【表2】 [Table 2]
【0031】 B製紙工場多重効用黒液濃縮缶の濃黒
液における腐食抑制試験 濃縮された黒液を100mLづつガラスビーカーに取
り、攪拌しながら、腐食抑制剤を所定量添加し均一に溶
解させた。この試験液をステンレス製オートクレーブに
移し入れた後、あらかじめ重量及び表面積を測定した軟
鋼(JIS G 3141 SPCC−SB)テストピース
を入れ、120℃のオイルバス中で24時間静置した。
オートクレーブを水道水に浸漬急冷した後、テストピー
スを取り出し、腐食生成物をナイロンたわしで除去した
後、水洗いし乾燥した。試験前と試験後のテストピース
の重量差を測定し、腐食速度に換算して評価した。結果
を表3に示した。B Corrosion Inhibition Test of Multi-Effect Black Liquor Concentration Canister in Paper Mill at 100% of the concentrated black liquor was placed in a glass beaker, and a predetermined amount of a corrosion inhibitor was added and uniformly dissolved with stirring. . After the test solution was transferred to a stainless steel autoclave, a mild steel (JIS G 3141 SPCC-SB) test piece whose weight and surface area had been measured in advance was put therein, and allowed to stand in an oil bath at 120 ° C. for 24 hours.
After the autoclave was immersed in tap water and quenched, the test piece was taken out, the corrosion products were removed with a nylon scourer, then washed with water and dried. The difference in weight between the test pieces before and after the test was measured and converted into a corrosion rate for evaluation. The results are shown in Table 3.
【0032】[0032]
【表3】 [Table 3]
【0033】表2の結果から、本発明の腐食抑制剤は、
蒸解釜の循環白液によって起こる腐食に対し、また表3
の結果から黒液によって起こる腐食に対しそれぞれ極め
て高い抑制効果を有することがわかる。From the results shown in Table 2, the corrosion inhibitor of the present invention is:
Table 3 shows the corrosion caused by white liquor in the digester.
It can be seen from the results that each has an extremely high inhibitory effect on corrosion caused by black liquor.
【0034】[0034]
【発明の効果】本発明のクラフトパルプ製造工程蒸解釜
及び黒液濃縮缶における腐食抑制剤及び腐食抑制方法を
当該工程に適用すれば、連続的に腐食を抑制することが
でき、装置の寿命を大幅に延長でき、かつ安全に、安定
した操業を長期間にわたって行うことが可能となる。ま
た、本発明の腐食抑制剤は重金属、リンを含まないこと
から、周辺環境に公害上の問題を起こすこともなく、安
心して適用できる。According to the present invention, if the corrosion inhibitor and the method for inhibiting corrosion in the digester and the black liquor canister of the kraft pulp production process of the present invention are applied to the process, the corrosion can be continuously suppressed and the life of the apparatus can be extended. The operation can be greatly extended and stable operation can be performed safely for a long period of time. In addition, since the corrosion inhibitor of the present invention does not contain heavy metals and phosphorus, it can be applied without causing any pollution problem in the surrounding environment.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C08F 222/02 C08F 222/02 222/04 222/04 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI C08F 222/02 C08F 222/02 222/04 222/04
Claims (3)
酸、無水マレイン酸、イタコン酸、無水イタコン酸およ
びこれらのアルカリ金属塩、アンモニウム塩から選ばれ
た1種以上の不飽和カルボン酸系単量体と、2−アクリ
ルアミド−2−メチルプロパンスルホン酸、2−メタク
リルアミド−2−メチルプロパンスルホン酸、およびこ
れらのアルカリ金属塩、アンモニウム塩から選ばれた1
種以上の不飽和スルホン酸系単量体を主要成分とし、不
飽和スルホン酸系単量体が全単量体の1〜30モル%で
あり、且つ、重量平均分子量が500〜20,000で
ある水溶性共重合体を含有することを特徴とするクラフ
トパルプ製造工程における蒸解釜及び/あるいは黒液濃
縮缶の腐食抑制剤。1. An unsaturated carboxylic acid monomer selected from acrylic acid, methacrylic acid, maleic acid, maleic anhydride, itaconic acid, itaconic anhydride and alkali metal salts and ammonium salts thereof. , 2-acrylamido-2-methylpropanesulfonic acid, 2-methacrylamido-2-methylpropanesulfonic acid, and alkali metal salts and ammonium salts thereof.
At least one kind of unsaturated sulfonic acid-based monomer as a main component, the unsaturated sulfonic acid-based monomer is 1 to 30 mol% of all monomers, and has a weight average molecular weight of 500 to 20,000. A corrosion inhibitor for a digester and / or a black liquor concentrator in a kraft pulp manufacturing process, characterized by containing a certain water-soluble copolymer.
対して、請求項1記載の腐食抑制剤を1〜100ppm
添加することを特徴とするクラフトパルプ製造工程にお
ける蒸解釜の腐食抑制方法。2. The corrosion inhibitor according to claim 1, which is present in an amount of 1 to 100 ppm based on the digester white liquor in the kraft pulp production process.
A method for suppressing corrosion of a digester in a kraft pulp manufacturing process, characterized by adding.
て、請求項1記載の黒液濃縮缶の腐食抑制剤を1〜10
0ppm添加することを特徴とするクラフトパルプ製造
工程における黒液濃縮缶の腐食抑制方法。3. The black liquor concentrating can of claim 1 is added to the black liquor in the kraft pulp production process in an amount of 1 to 10%.
A method for suppressing corrosion of a black liquor concentrate in a kraft pulp manufacturing process, characterized by adding 0 ppm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9300297A JPH11131381A (en) | 1997-10-31 | 1997-10-31 | Corrosion inhibitor for digester and / or black liquor canister in kraft pulp manufacturing process and method of inhibiting corrosion |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9300297A JPH11131381A (en) | 1997-10-31 | 1997-10-31 | Corrosion inhibitor for digester and / or black liquor canister in kraft pulp manufacturing process and method of inhibiting corrosion |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11131381A true JPH11131381A (en) | 1999-05-18 |
Family
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Application Number | Title | Priority Date | Filing Date |
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JP9300297A Pending JPH11131381A (en) | 1997-10-31 | 1997-10-31 | Corrosion inhibitor for digester and / or black liquor canister in kraft pulp manufacturing process and method of inhibiting corrosion |
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JP (1) | JPH11131381A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007177154A (en) * | 2005-12-28 | 2007-07-12 | Toagosei Co Ltd | Acrylic acid copolymer, its production method, and its use |
CN100439267C (en) * | 2007-10-29 | 2008-12-03 | 山东泉林纸业有限责任公司 | Alkali digester and sulammonium process mixed straw pulping black liquor, alkali digester and sulammonium process mixed compression straw pulping black liquor, and preparation method thereof |
JP2016211087A (en) * | 2015-04-30 | 2016-12-15 | ナルコジャパン合同会社 | Cleaning method for deposits generated in dissolving pulp manufacturing process |
CN107032509A (en) * | 2017-03-14 | 2017-08-11 | 成都云图控股股份有限公司 | A kind of terpolymer concentration slow-release scale inhibitor and preparation method thereof |
-
1997
- 1997-10-31 JP JP9300297A patent/JPH11131381A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007177154A (en) * | 2005-12-28 | 2007-07-12 | Toagosei Co Ltd | Acrylic acid copolymer, its production method, and its use |
JP4534981B2 (en) * | 2005-12-28 | 2010-09-01 | 東亞合成株式会社 | Acrylic acid copolymer, process for producing the same and use thereof |
CN100439267C (en) * | 2007-10-29 | 2008-12-03 | 山东泉林纸业有限责任公司 | Alkali digester and sulammonium process mixed straw pulping black liquor, alkali digester and sulammonium process mixed compression straw pulping black liquor, and preparation method thereof |
JP2016211087A (en) * | 2015-04-30 | 2016-12-15 | ナルコジャパン合同会社 | Cleaning method for deposits generated in dissolving pulp manufacturing process |
CN107032509A (en) * | 2017-03-14 | 2017-08-11 | 成都云图控股股份有限公司 | A kind of terpolymer concentration slow-release scale inhibitor and preparation method thereof |
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