JPH0445554B2 - - Google Patents
Info
- Publication number
- JPH0445554B2 JPH0445554B2 JP60015469A JP1546985A JPH0445554B2 JP H0445554 B2 JPH0445554 B2 JP H0445554B2 JP 60015469 A JP60015469 A JP 60015469A JP 1546985 A JP1546985 A JP 1546985A JP H0445554 B2 JPH0445554 B2 JP H0445554B2
- Authority
- JP
- Japan
- Prior art keywords
- polymer
- monomers
- sulfonic acid
- group
- polymerizable
- 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.)
- Expired
Links
- 229920000642 polymer Polymers 0.000 claims description 41
- 239000000178 monomer Substances 0.000 claims description 38
- 239000002002 slurry Substances 0.000 claims description 26
- 239000000843 powder Substances 0.000 claims description 17
- 239000002270 dispersing agent Substances 0.000 claims description 16
- 125000003118 aryl group Chemical group 0.000 claims description 13
- 125000000542 sulfonic acid group Chemical group 0.000 claims description 9
- -1 aliphatic unsaturated sulfonic acid Chemical class 0.000 claims description 7
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 claims description 6
- 239000004215 Carbon black (E152) Substances 0.000 claims description 6
- 150000004945 aromatic hydrocarbons Chemical class 0.000 claims description 6
- 229930195733 hydrocarbon Natural products 0.000 claims description 6
- 150000002430 hydrocarbons Chemical class 0.000 claims description 6
- 230000000379 polymerizing effect Effects 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 20
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 11
- 229920001577 copolymer Polymers 0.000 description 10
- 150000003839 salts Chemical class 0.000 description 9
- 238000010298 pulverizing process Methods 0.000 description 6
- AGBXYHCHUYARJY-UHFFFAOYSA-N 2-phenylethenesulfonic acid Chemical compound OS(=O)(=O)C=CC1=CC=CC=C1 AGBXYHCHUYARJY-UHFFFAOYSA-N 0.000 description 5
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 5
- 230000003068 static effect Effects 0.000 description 5
- 239000003245 coal Substances 0.000 description 4
- 239000003431 cross linking reagent Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 150000002739 metals Chemical class 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000002006 petroleum coke Substances 0.000 description 4
- YBYIRNPNPLQARY-UHFFFAOYSA-N 1H-indene Chemical compound C1=CC=C2CC=CC2=C1 YBYIRNPNPLQARY-UHFFFAOYSA-N 0.000 description 3
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 3
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 3
- OBNZQBVPDZWAEB-UHFFFAOYSA-N 2-phenylprop-1-ene-1-sulfonic acid Chemical compound OS(=O)(=O)C=C(C)C1=CC=CC=C1 OBNZQBVPDZWAEB-UHFFFAOYSA-N 0.000 description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 3
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 3
- 239000011335 coal coke Substances 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 239000003381 stabilizer Substances 0.000 description 3
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 description 2
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- FXNDIJDIPNCZQJ-UHFFFAOYSA-N 2,4,4-trimethylpent-1-ene Chemical group CC(=C)CC(C)(C)C FXNDIJDIPNCZQJ-UHFFFAOYSA-N 0.000 description 2
- UVDYBBRVDUKNFV-UHFFFAOYSA-N 2-(prop-2-enoylamino)ethanesulfonic acid Chemical compound OS(=O)(=O)CCNC(=O)C=C UVDYBBRVDUKNFV-UHFFFAOYSA-N 0.000 description 2
- XFCMNSHQOZQILR-UHFFFAOYSA-N 2-[2-(2-methylprop-2-enoyloxy)ethoxy]ethyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCOCCOC(=O)C(C)=C XFCMNSHQOZQILR-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- 239000006229 carbon black Substances 0.000 description 2
- 239000003575 carbonaceous material Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 229920001038 ethylene copolymer Polymers 0.000 description 2
- STVZJERGLQHEKB-UHFFFAOYSA-N ethylene glycol dimethacrylate Substances CC(=C)C(=O)OCCOC(=O)C(C)=C STVZJERGLQHEKB-UHFFFAOYSA-N 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- HJWLCRVIBGQPNF-UHFFFAOYSA-N prop-2-enylbenzene Chemical compound C=CCC1=CC=CC=C1 HJWLCRVIBGQPNF-UHFFFAOYSA-N 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000004449 solid propellant Substances 0.000 description 2
- 238000006277 sulfonation reaction Methods 0.000 description 2
- AKEJUJNQAAGONA-UHFFFAOYSA-N sulfur trioxide Inorganic materials O=S(=O)=O AKEJUJNQAAGONA-UHFFFAOYSA-N 0.000 description 2
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 2
- KEQGZUUPPQEDPF-UHFFFAOYSA-N 1,3-dichloro-5,5-dimethylimidazolidine-2,4-dione Chemical compound CC1(C)N(Cl)C(=O)N(Cl)C1=O KEQGZUUPPQEDPF-UHFFFAOYSA-N 0.000 description 1
- CBQFBEBEBCHTBK-UHFFFAOYSA-N 1-phenylprop-2-ene-1-sulfonic acid Chemical compound OS(=O)(=O)C(C=C)C1=CC=CC=C1 CBQFBEBEBCHTBK-UHFFFAOYSA-N 0.000 description 1
- IGGDKDTUCAWDAN-UHFFFAOYSA-N 1-vinylnaphthalene Chemical compound C1=CC=C2C(C=C)=CC=CC2=C1 IGGDKDTUCAWDAN-UHFFFAOYSA-N 0.000 description 1
- PRAMZQXXPOLCIY-UHFFFAOYSA-N 2-(2-methylprop-2-enoyloxy)ethanesulfonic acid Chemical group CC(=C)C(=O)OCCS(O)(=O)=O PRAMZQXXPOLCIY-UHFFFAOYSA-N 0.000 description 1
- ONUXAGYOFJLIQM-UHFFFAOYSA-N 2-ethenylnaphthalene-1-sulfonic acid Chemical compound C1=CC=C2C(S(=O)(=O)O)=C(C=C)C=CC2=C1 ONUXAGYOFJLIQM-UHFFFAOYSA-N 0.000 description 1
- XEEYSDHEOQHCDA-UHFFFAOYSA-N 2-methylprop-2-ene-1-sulfonic acid Chemical compound CC(=C)CS(O)(=O)=O XEEYSDHEOQHCDA-UHFFFAOYSA-N 0.000 description 1
- GQTFHSAAODFMHB-UHFFFAOYSA-N 2-prop-2-enoyloxyethanesulfonic acid Chemical group OS(=O)(=O)CCOC(=O)C=C GQTFHSAAODFMHB-UHFFFAOYSA-N 0.000 description 1
- NYUTUWAFOUJLKI-UHFFFAOYSA-N 3-prop-2-enoyloxypropane-1-sulfonic acid Chemical group OS(=O)(=O)CCCOC(=O)C=C NYUTUWAFOUJLKI-UHFFFAOYSA-N 0.000 description 1
- DBCAQXHNJOFNGC-UHFFFAOYSA-N 4-bromo-1,1,1-trifluorobutane Chemical compound FC(F)(F)CCCBr DBCAQXHNJOFNGC-UHFFFAOYSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004641 Diallyl-phthalate Substances 0.000 description 1
- 239000002879 Lewis base Substances 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- OKKRPWIIYQTPQF-UHFFFAOYSA-N Trimethylolpropane trimethacrylate Chemical compound CC(=C)C(=O)OCC(CC)(COC(=O)C(C)=C)COC(=O)C(C)=C OKKRPWIIYQTPQF-UHFFFAOYSA-N 0.000 description 1
- GCNKJQRMNYNDBI-UHFFFAOYSA-N [2-(hydroxymethyl)-2-(2-methylprop-2-enoyloxymethyl)butyl] 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCC(CO)(CC)COC(=O)C(C)=C GCNKJQRMNYNDBI-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 125000002947 alkylene group Chemical group 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- QUDWYFHPNIMBFC-UHFFFAOYSA-N bis(prop-2-enyl) benzene-1,2-dicarboxylate Chemical compound C=CCOC(=O)C1=CC=CC=C1C(=O)OCC=C QUDWYFHPNIMBFC-UHFFFAOYSA-N 0.000 description 1
- 239000002802 bituminous coal Substances 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000010000 carbonizing Methods 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- XTHPWXDJESJLNJ-UHFFFAOYSA-N chlorosulfonic acid Substances OS(Cl)(=O)=O XTHPWXDJESJLNJ-UHFFFAOYSA-N 0.000 description 1
- 239000011280 coal tar Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000000875 corresponding effect Effects 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000003009 desulfurizing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- NVVZQXQBYZPMLJ-UHFFFAOYSA-N formaldehyde;naphthalene-1-sulfonic acid Chemical compound O=C.C1=CC=C2C(S(=O)(=O)O)=CC=CC2=C1 NVVZQXQBYZPMLJ-UHFFFAOYSA-N 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 150000007527 lewis bases Chemical class 0.000 description 1
- 239000003077 lignite Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 150000002762 monocarboxylic acid derivatives Chemical class 0.000 description 1
- 150000002763 monocarboxylic acids Chemical class 0.000 description 1
- ZIUHHBKFKCYYJD-UHFFFAOYSA-N n,n'-methylenebisacrylamide Chemical compound C=CC(=O)NCNC(=O)C=C ZIUHHBKFKCYYJD-UHFFFAOYSA-N 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- UIIIBRHUICCMAI-UHFFFAOYSA-N prop-2-ene-1-sulfonic acid Chemical compound OS(=O)(=O)CC=C UIIIBRHUICCMAI-UHFFFAOYSA-N 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000003476 subbituminous coal Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 238000001238 wet grinding Methods 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Landscapes
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
- Liquid Carbonaceous Fuels (AREA)
Description
技術分野
本発明は、石炭や石油コークスに代表されるよ
うな炭素質微粉体の水スラリーに用いられる分散
剤に関する。
従来技術
石油価格の高騰やエネルギー資源の多様化の観
点から、近年、石炭の利用が注目されている。石
炭は固体燃料でありハンドリングの点で難点があ
るので、これを微粉砕して水スラリーとすること
が提案されてきた。石炭や石油コークスのような
固体燃料を水スラリーとすることにより、パイプ
輸送が可能となり液体燃料と同様に扱うことがで
きる。水スラリーは、脱水処理することなくその
ままボイラ等で燃焼したり、あるいは輸送効率の
観点から高濃度化することが必要となる。しか
し、石炭や石油コークスなどの炭素質微粉体をそ
のまま水中に分散しただけでは50%以上の高濃度
スラリーを得ることは困難であり、また、静置し
ておくと炭素質微粉体が沈降して不均一になり貯
蔵安定性の点でも問題がある。
そこで、スラリー中に分散安定剤を添加して高
濃度化および分散安定性を改善することが提案さ
れてきている。このような分散安定剤としては、
たとえば、ナフタレンスルホン酸ホルマリン縮合
物(特開昭56−21636号公報)、アクリル酸または
メタクリル酸と他のビニルモノマーとの共重合物
(特開昭56−57890号公報)、アクリル酸とマレイ
ン酸との共重合物(特開昭56−57890号公報)、分
子内に活性水素基を有する化合物のアルキレンオ
キシド付加物を架橋した架橋ポリエーテル化合物
(特開昭58−118893号公報)、スルホン化コ−ルタ
−ルまたはホルムアルデヒド縮合物(特開昭58−
23889号公報)、スチレンスルホン酸とビニル化合
物との共重合物の塩のような水溶性芳香族重合
物、およびα−オレフインと無水マレイン酸やア
クリル酸などとの共重合物のような水溶性脂肪重
合物を含む添加剤(特開昭59−166591号公報)が
報告されている。
しかしながら、これら従来の分散剤は相応の効
果が見受けられるものの、スラリーの高濃度化お
よび静置安定性のいずれにおいても未だ不十分で
あり、いつそうの改善がまたれていた。
発明の目的
本発明は、炭素質微粉体の水スラリーに添加し
てとき、スラリーの低粘度化および流動性の向上
性に優れて高濃度化が実現でき、しかも、長期間
における静置安定性が得られる分散剤を提供する
ことを目的とする。
発明の構成
本発明の炭素質微粉体の水スラリー用分散剤
は、以下の(A)成分と(B)成分とを含有することを特
徴とする。
(A)成分:次の(A1)および(A2)の重合体の中
から選ばれる1種または2種以上のスルホン酸
基含有芳香族炭化水素系重合体
(A1):(a)重合性芳香族スルホン酸系モノマー
群および(b)重合性炭化水素系モノマー群の中
から選ばれた1種または2種以上のモノマー
を重合して得られる重合体であつて、前記(a)
成分を必須成分として含む重合体。
(A2):重合性炭化水素系モノマー群の中から
選ばれた1種または2種以上のモノマーを重
合して得られるポリマーであつて、重合性芳
香族系モノマーを少なくとも1種必須成分と
して含むポリマーをスルホン化して得られる
重合体
(B)成分:重合性脂肪族不飽和スルホン酸系モノマ
ーの重合体
以下、本発明についてさらに詳細に説明する。
(A)成分の重合体は、分子内にスルホン酸基
を含む芳香族炭化水素を構成単位として含むもの
である。そして、このスルホン酸基がモノマーに
由来するもの、即ち、スルホン酸基を含む芳香族
炭化水素モノマーを単独であるいは他のノモノマ
ーとともに重合せしめたものが、(A1)の重合体
である。一方、モノマーを重合して重合体を得た
のちに、重合体中の芳香族基にスルホン酸基を導
入したものが、(A1)の重合体である。
(A1)の重合体は、以下の(a)群および(b)群の
中から選ばれた1種以上のモノマーからなる重合
体であつて、少なくとも(a)群モノマーに由来する
構成単位を含むものである。
(a) 重合性芳香族スルホン酸系モノマー
(b) 重合性炭化水素系モノマー
(A1)の重合体中における(a)群の芳香族スル
ホン酸系モノマーの占める割合は、40〜100モル
%が好ましく、より好ましくは50〜100モル%で
ある。このように(b)群のモノマーを用いることな
く、(a)群の芳香族スルホン酸系モノマーだけで、
(A1)の重合体を構成することもできる。
(a)群モノマーの具体例としてはスチレンスルホ
ン酸、α−メチルスチレンスルホン酸、ビニルト
ルエンスルホン酸、ビニルナフタレンスルホン
酸、またはこれらの塩が挙げられる。塩を形成す
る対イオンとしては、ナトリウム、カリウムなど
の1価金属、マグネシウム、カルシウムなどの2
価金属、アルミニウムなどの3価金属、アンモニ
ウム、有機アミンなどが例示され、これらの中で
もナトリウム、カリウム、アンモニウムが好まし
い。
(b)群モノマーの具体例としては、スチレン、α
−メチルスチレン、ビニルトルエン、エチレン、
ブテン、ブタジエン、ジイソブチレンが挙げられ
る。
(a)群モノマーと(b)群モノマーとの共重合体とし
ては、スチレンスルホン酸・スチレン共重合体、
スチレンスルホン酸・ブタジエン共重合体、スチ
レンスルホン酸・ブテン共重合体、α−メチルス
チレンスルホン酸・エチレン共重合体、α−メチ
ルスチレンスルホン酸・ジイソブチレン共重合体
が例示される。
(A1)の重合体の分子量は、重量平均分子量
で700〜70万が適当であり、好ましくは
1000〜50万である。
(A2)の重合体は、炭化水素系モノマーの少
なくとも1種のポリマーであつて、芳香族系モノ
マーを少なくとも1種を必須成分として含むポリ
マーのスルホン化物、またはその塩である。この
芳香族系モノマーとしては、スチレン、α−メチ
ルスチレン、ビニルトルエン、ビニルナフタレ
ン、インデンなどが挙げられ、また、芳香族系以
外の炭化水素系モノマーとしては、エチレン、ブ
テン、ブタジエン、ジイソブチレンが挙げられ
る。これらモノマーの重合体中に占める芳香族系
モノマーの割合は30〜100モル%が適当であり、
好ましくは50〜100モル%である。この重合体の
具体例としては、ポリスチレン、スチレン・エチ
レン共重合体、スチレン・ジイソブチレン共重合
体、スチレン・ビニルトルエン・α−メチルスチ
レン・インデン共重合体のような石油樹脂が挙げ
られる。このような重合体をスルホン化し、また
はさらに塩とすることにより(A2)の重合体が
得られる。スルホン化は、無水硫酸、クロルスル
ホン酸、無水硫酸・ルイス塩基錯体などのスルホ
ン化剤を用い、任意のスルホン化方法を適用する
ことにより行うことができる。(A2)の重合体の
分子量は、重量平均分子量で700〜70万が適当で
あり、好ましくは1000〜50万である。(A2)の重
合体の塩としては、(A1)の重合体と同じものが
例示される。
(A)成分のスルホン酸基含有芳香族炭化水素系重
合体は、(A1)の重合体と(A2)の重合体を任意
の割合で混合して用いることもできる。
(B)成分の重合性脂肪族不飽和スルホン酸系モノ
マーの重合体としては、分子量700〜20万のもの
が適当であり、好ましくは1000〜10万である。こ
のモノマーの具体例としては、アリルスルホン
酸、メタリルスルホン酸などのオレフインスルホ
ン酸、アクリル酸2−スルホエチル、メタクリル
酸2−スルホエチル、アクリル酸3−スルホプロ
ピルなどのスルホン酸基含有不飽和モノカルボン
酸エステル、2−アクリルアミドエタンスルホン
酸、2−アクリルアミド−2−メチルプロパンス
ルホン酸などのスルホン酸基含有不飽和モノカル
ボン酸アミド、アリルオキシエタンスルホン酸、
アリルオキシプロパンスルホン酸などのスルホン
酸含有アリルエーテルおよびこれらの塩が含まれ
る。脂肪族不飽和スルホン酸の塩を構成する対イ
オンは、(A)成分における対イオンと同様である。
(A)成分と(B)成分との配合は重量比で(A)成分/(B)
成分=1/9〜20/1の範囲が適当であり、好ま
しくは1/5〜15/1の範囲である。この比率が
1/9より小さいと分散性が劣化し、また、15/
1より大きいと静置安定性が劣る。
本発明の(A)成分または(B)成分は、その重合時に
架橋剤を用いることができ、架橋剤としてはジビ
ニルベンゼン、メチレンビスアクリルアミド、エ
チレングリコールジメタクリレート、ジエチレン
グリコールジメタクリレート、ポリエチレングリ
コールジメタクリレート、トリメチルロールプロ
パンジメタクリレート、トリメチロールプロパン
トリメタクリレート、ジアリルフタレートなどが
例示できる。(A),(B)成分のいずれの場合も、架橋
剤は、0〜5モル%用いるのが適当であり、好ま
しくは0.01〜3モル%である。架橋剤の配合量が
多くなりすぎると水溶性が低下し、好ましくな
い。
本発明の分散剤は、炭素質微粉体の水スラリー
中に、0.05〜3重量%、好ましくは0.1〜2重量
%の範囲で含まれるように添加するのが適当であ
る。
炭素質微粉体としては、無煙炭、瀝青炭、亜瀝
青炭、褐炭などの石炭;石油コークス、化学プラ
ントから副生するカーボンブラツク、有機物を炭
化して得られるカーホンブラツク、木炭などエネ
ルギー源として用いられものが使用される。
また、石炭のように灰分を多く含むものは、浮
選法、水中造粒法(Oil Agglomeration法)など
を適用して脱灰ならびに脱硫処理を施し、クリー
ン化することが好ましい。これらの炭素質は、実
質上1mm以上のものが含まれないように微粉化さ
れるが、燃料としての燃焼性を考慮して74μm以
下の含有量が50重量%以上とすることが好まし
く、さらに好ましくは60〜100重量%である。
炭素質微粉体の水スラリーは、乾式粉砕法また
は湿式粉粉砕法により炭素質を粉砕して水スラリ
ー化することに得ることができ、分散剤は最終水
スラリーに含まれるように適宜の工程で添加する
ことができる。たとえば、乾式粉砕法で炭素質微
粉体を得た場合は、分散剤を水に溶解または分散
させ、これに微粉体を加えて適当な混合装置によ
り高濃度水スラリーを調整すればよい。また、湿
式粉砕法を採用する場合は、湿式粉砕に用いる水
中に分散剤を予め添加するようにしてもよいし、
湿式粉砕中もしくは粉砕後に添加するようにして
もよい。
水スラリー中の炭素質微粉体の濃度は、微粉体
の種類、平均粒径、粒度分布などにもよるが、本
発明の分散剤を添加することにより十分に高める
ことができ、たとえば80重量%程度まで可能であ
る。
発明の効果
本発明の分散剤によれば、(A)スルホン酸基含有
芳香族炭化水素系重合体と(B)脂肪族不飽和スルホ
ン酸系モノマーの重合体とを併用することによ
り、炭素質微粉体水スラリーの流動性および静置
安定性を相剰的に改善することができる。よつ
て、従来よりも高濃度の水スラリーが得られると
ともに、長期に亘つて安定に貯蔵することができ
る。
本発明の安定剤を添加した炭素質微粉体水スラ
リーは、電力や一般産業用のボイラー燃料として
のみならず、製鉄分野における高炉や冶金炉で使
用されるコークスの節減のための助燃剤などとし
ても有用である。
実施例
所定の分散剤を水に溶解し、これに炭素質微粉
体を所定量(乾燥基準)になるように室温にて少
量づつ加えた。全量加え終つた後、ホモミキサー
(特殊機化工業製)にて3000rpmで10分間攪拌し
て高濃度水スラリーを約500g調整した。
次に、このスラリーの流動性および静置安定性
を評価した。
(1) 流動性
25℃にて粘度を測定した。
○:良好
△:不十分
×:不良
(2) 静置安定性
スラリーを内径6cmの500mlシリンダーに全量
入れ、直径5mm、長さ40cmで重量を50gに調整し
たガラス棒を上記スラリーの表面から自然落下さ
せ、シリンダーの底部に到達するまでの時間を調
製直後と室温で1ケ月静置後の2回測定して、棒
貫入時間とした。計測は最長180秒までとし、こ
れ以上要するものはこの時の底部からの高さを、
圧密層の高さとして測定した。
○:良好
×:不良
水スラリーの調整に用いた炭素質微粉体の粒度
分布を表−1に、また石炭の分析値を表−2に示
した。
本発明の分散剤の(A)成分の性状を表−3に、ま
た、(B)成分の性状を表−4に示した。
(A)成分および(B)成分を配合した本発明の分散剤
を用いた水スラリーの測定結果を表−5に示し
た。なお、表−6に比較例として、分散剤無添加
のもの(実験No.65)、本発明の(A)成分または(B)成
分を単独で使用したもの(実験No.66,67)、公知
の分散剤の代表例(実験No.68〜70)についての測
定結果を示した。
TECHNICAL FIELD The present invention relates to a dispersant used in an aqueous slurry of carbonaceous fine powder such as coal or petroleum coke. BACKGROUND ART In recent years, the use of coal has been attracting attention from the viewpoint of soaring oil prices and diversification of energy resources. Since coal is a solid fuel and is difficult to handle, it has been proposed to pulverize it into a water slurry. By turning solid fuels such as coal or petroleum coke into a water slurry, it becomes possible to transport them through pipes and handle them in the same way as liquid fuels. The water slurry needs to be burned as it is in a boiler or the like without being dehydrated, or it needs to be highly concentrated from the viewpoint of transportation efficiency. However, it is difficult to obtain a slurry with a high concentration of 50% or more by simply dispersing carbonaceous fine powder such as coal or petroleum coke in water, and if left standing, the carbonaceous fine powder will settle. It becomes non-uniform and there is also a problem in terms of storage stability. Therefore, it has been proposed to add a dispersion stabilizer to the slurry to increase the concentration and improve the dispersion stability. Such dispersion stabilizers include:
For example, naphthalene sulfonic acid formalin condensate (JP 56-21636), copolymer of acrylic acid or methacrylic acid with other vinyl monomers (JP 56-57890), acrylic acid and maleic acid. (Japanese Patent Application Laid-Open No. 56-57890), crosslinked polyether compounds obtained by crosslinking alkylene oxide adducts of compounds having active hydrogen groups in the molecule (Japanese Patent Application Laid-Open No. 118893/1982), sulfonated Coal tar or formaldehyde condensate
23889), water-soluble aromatic polymers such as salts of copolymers of styrene sulfonic acid and vinyl compounds, and water-soluble aromatic polymers such as copolymers of α-olefin with maleic anhydride, acrylic acid, etc. An additive containing a fatty polymer has been reported (Japanese Unexamined Patent Publication No. 166591/1983). However, although these conventional dispersants have been shown to have a corresponding effect, they are still insufficient in terms of increasing the concentration of slurry and static stability, and improvements have not yet been made. Purpose of the Invention The present invention provides that when carbonaceous fine powder is added to an aqueous slurry, it is possible to achieve a high concentration by reducing the viscosity of the slurry and improving fluidity, and furthermore, it has stable stability over a long period of time. The purpose of the present invention is to provide a dispersant that provides the following. Structure of the Invention The dispersant for water slurry of carbonaceous fine powder of the present invention is characterized by containing the following components (A) and (B). Component (A): One or more sulfonic acid group-containing aromatic hydrocarbon polymers selected from the following polymers (A 1 ) and (A 2 ) (A 1 ): (a) A polymer obtained by polymerizing one or more monomers selected from the group of polymerizable aromatic sulfonic acid monomers and (b) the group of polymerizable hydrocarbon monomers, said (a)
A polymer containing the following components as essential components. (A 2 ): A polymer obtained by polymerizing one or more monomers selected from the group of polymerizable hydrocarbon monomers, which contains at least one polymerizable aromatic monomer as an essential component. Polymer (B) component obtained by sulfonating the containing polymer: Polymer of polymerizable aliphatic unsaturated sulfonic acid monomer The present invention will be described in more detail below. The polymer of component (A) contains an aromatic hydrocarbon containing a sulfonic acid group in the molecule as a structural unit. The polymer (A 1 ) is one in which the sulfonic acid group is derived from a monomer, that is, one in which an aromatic hydrocarbon monomer containing a sulfonic acid group is polymerized alone or together with other monomers. On the other hand, the polymer (A 1 ) is obtained by polymerizing monomers to obtain a polymer, and then introducing sulfonic acid groups into the aromatic groups in the polymer. The polymer (A 1 ) is a polymer consisting of one or more monomers selected from the following groups (a) and (b), and includes at least a structural unit derived from the monomers of group (a). This includes: (a) Polymerizable aromatic sulfonic acid monomer (b) Polymerizable hydrocarbon monomer The proportion of the aromatic sulfonic acid monomer of group (a) in the polymer of (A 1 ) is 40 to 100 mol%. is preferable, and more preferably 50 to 100 mol%. In this way, without using the monomers of group (b), only the aromatic sulfonic acid monomers of group (a) can be used.
It is also possible to constitute a polymer of (A 1 ). Specific examples of group (a) monomers include styrene sulfonic acid, α-methylstyrene sulfonic acid, vinyltoluenesulfonic acid, vinylnaphthalenesulfonic acid, or salts thereof. Counterions that form salts include monovalent metals such as sodium and potassium, and divalent metals such as magnesium and calcium.
Examples include valent metals, trivalent metals such as aluminum, ammonium, and organic amines, and among these, sodium, potassium, and ammonium are preferred. Specific examples of group (b) monomers include styrene, α
-methylstyrene, vinyltoluene, ethylene,
Examples include butene, butadiene, and diisobutylene. Copolymers of group (a) monomers and group (b) monomers include styrene sulfonic acid/styrene copolymers,
Examples include styrenesulfonic acid/butadiene copolymer, styrenesulfonic acid/butene copolymer, α-methylstyrenesulfonic acid/ethylene copolymer, and α-methylstyrenesulfonic acid/diisobutylene copolymer. The weight average molecular weight of the polymer (A 1 ) is suitably 700 to 700,000, preferably 1000 to 500,000. The polymer (A 2 ) is a sulfonated product of at least one type of hydrocarbon monomer and includes at least one aromatic monomer as an essential component, or a salt thereof. Examples of aromatic monomers include styrene, α-methylstyrene, vinyltoluene, vinylnaphthalene, and indene. Examples of non-aromatic hydrocarbon monomers include ethylene, butene, butadiene, and diisobutylene. Can be mentioned. The appropriate proportion of aromatic monomers in the polymer of these monomers is 30 to 100 mol%,
Preferably it is 50 to 100 mol%. Specific examples of this polymer include petroleum resins such as polystyrene, styrene/ethylene copolymer, styrene/diisobutylene copolymer, and styrene/vinyltoluene/α-methylstyrene/indene copolymer. By sulfonating such a polymer or further converting it into a salt, the polymer (A 2 ) can be obtained. Sulfonation can be carried out by applying any sulfonation method using a sulfonating agent such as sulfuric anhydride, chlorosulfonic acid, or a sulfuric anhydride/Lewis base complex. The weight average molecular weight of the polymer (A 2 ) is suitably 700 to 700,000, preferably 1000 to 500,000. Examples of the salt of the polymer (A 2 ) include the same salts as the polymer (A 1 ). The sulfonic acid group-containing aromatic hydrocarbon polymer of component (A) can also be used by mixing the polymer of (A 1 ) and the polymer of (A 2 ) in any ratio. The polymer of component (B), a polymerizable aliphatic unsaturated sulfonic acid monomer, has a molecular weight of 700 to 200,000, preferably 1,000 to 100,000. Specific examples of this monomer include olefin sulfonic acids such as allylsulfonic acid and methallylsulfonic acid, unsaturated monocarboxylic acids containing sulfonic acid groups such as 2-sulfoethyl acrylate, 2-sulfoethyl methacrylate, and 3-sulfopropyl acrylate. acid ester, unsaturated monocarboxylic acid amide containing a sulfonic acid group such as 2-acrylamidoethanesulfonic acid, 2-acrylamidoethanesulfonic acid, allyloxyethanesulfonic acid,
Included are sulfonic acid-containing allyl ethers such as allyloxypropanesulfonic acid and salts thereof. The counter ion constituting the salt of aliphatic unsaturated sulfonic acid is the same as the counter ion in component (A). The composition of component (A) and component (B) is the weight ratio of component (A)/(B).
A suitable range of components is 1/9 to 20/1, preferably 1/5 to 15/1. If this ratio is less than 1/9, dispersibility will deteriorate, and 15/
If it is larger than 1, the static stability will be poor. For component (A) or component (B) of the present invention, a crosslinking agent may be used during polymerization, and examples of the crosslinking agent include divinylbenzene, methylene bisacrylamide, ethylene glycol dimethacrylate, diethylene glycol dimethacrylate, polyethylene glycol dimethacrylate, Examples include trimethylolpropane dimethacrylate, trimethylolpropane trimethacrylate, and diallyl phthalate. In both components (A) and (B), it is appropriate to use the crosslinking agent in an amount of 0 to 5 mol%, preferably 0.01 to 3 mol%. If the amount of the crosslinking agent is too large, the water solubility will decrease, which is not preferable. The dispersant of the present invention is suitably added to the aqueous slurry of carbonaceous fine powder in an amount of 0.05 to 3% by weight, preferably 0.1 to 2% by weight. Examples of carbonaceous fine powder include coals such as anthracite, bituminous coal, subbituminous coal, and lignite; petroleum coke, carbon black by-produced from chemical plants, carbon black obtained by carbonizing organic matter, and charcoal used as energy sources. is used. In addition, it is preferable to clean coal containing a large amount of ash by deashing and desulfurizing it by flotation, oil agglomeration, or the like. These carbonaceous materials are pulverized so that they do not substantially contain anything larger than 1 mm, but in consideration of combustibility as a fuel, it is preferable that the content of carbon particles below 74 μm is 50% by weight or more. Preferably it is 60 to 100% by weight. A water slurry of carbonaceous fine powder can be obtained by pulverizing carbonaceous material into a water slurry using a dry pulverization method or a wet pulverization method, and the dispersant is added in an appropriate step so as to be included in the final water slurry. Can be added. For example, when carbonaceous fine powder is obtained by dry pulverization, a dispersant may be dissolved or dispersed in water, the fine powder may be added thereto, and a highly concentrated water slurry may be prepared using an appropriate mixing device. In addition, when adopting a wet pulverization method, a dispersant may be added in advance to the water used for wet pulverization, or
It may be added during or after wet milling. Although the concentration of carbonaceous fine powder in the water slurry depends on the type of fine powder, average particle size, particle size distribution, etc., it can be sufficiently increased by adding the dispersant of the present invention, for example, 80% by weight. It is possible to some extent. Effects of the Invention According to the dispersant of the present invention, carbonaceous The fluidity and static stability of the fine powder water slurry can be mutually improved. Therefore, a water slurry with a higher concentration than before can be obtained and can be stored stably for a long period of time. The carbonaceous fine powder water slurry to which the stabilizer of the present invention has been added can be used not only as a boiler fuel for electric power and general industries, but also as a combustion improver to reduce coke used in blast furnaces and metallurgical furnaces in the steel manufacturing field. is also useful. Example A predetermined dispersant was dissolved in water, and carbonaceous fine powder was added little by little at room temperature to a predetermined amount (dry basis). After adding the entire amount, the mixture was stirred for 10 minutes at 3000 rpm using a homo mixer (manufactured by Tokushu Kika Kogyo) to prepare approximately 500 g of highly concentrated water slurry. Next, the fluidity and static stability of this slurry were evaluated. (1) Fluidity Viscosity was measured at 25°C. ○: Good △: Insufficient ×: Poor (2) Static stability Pour the entire slurry into a 500 ml cylinder with an inner diameter of 6 cm, and insert a glass rod with a diameter of 5 mm, a length of 40 cm, and a weight of 50 g from the surface of the slurry. The time required for the rod to reach the bottom of the cylinder was measured twice, immediately after preparation and after being left at room temperature for one month, to determine the rod penetration time. The maximum measurement time is 180 seconds, and if it takes longer than that, the height from the bottom at this time,
It was measured as the height of the consolidated layer. ○: Good ×: Poor Table 1 shows the particle size distribution of the carbonaceous fine powder used for preparing the water slurry, and Table 2 shows the analysis values of the coal. The properties of component (A) of the dispersant of the present invention are shown in Table 3, and the properties of component (B) are shown in Table 4. Table 5 shows the measurement results of the water slurry using the dispersant of the present invention containing component (A) and component (B). In addition, Table 6 shows, as comparative examples, those without the addition of a dispersant (Experiment No. 65), those using component (A) or (B) of the present invention alone (Experiment No. 66, 67), Measurement results for representative examples of known dispersants (Experiment Nos. 68 to 70) are shown.
【表】【table】
【表】【table】
【表】【table】
【表】【table】
【表】【table】
【表】【table】
【表】【table】
【表】【table】
【表】【table】
Claims (1)
から選ばれる1種または2種以上のスルホン酸
基含有芳香族炭化水素系重合体 (A1):(a)重合性芳香族スルホン酸系モノマー
群および(b)重合性炭化水素系モノマー群の中
から選ばれた1種または2種以上のモノマー
を重合して得られる重合体であつて、前記(a)
成分を必須成分として含む重合体。 (A2):重合性炭化水素系モノマー群の中から
選ばれた1種または2種以上のモノマーを重
合して得られるポリマーであつて、重合性芳
香族系モノマーを少なくとも1種必須成分と
して含むポリマーをスルホン化して得られる
重合体 と、 (B):重合性脂肪族不飽和スルホン酸系モノマーの
重合体 とを含有することを特徴とする炭素質微粉体の水
スラリー用分散剤。[Scope of Claims] 1 (A): One or more sulfonic acid group-containing aromatic hydrocarbon polymers selected from the following polymers (A 1 ) and (A 2 ) (A 1 ): A polymer obtained by polymerizing one or more monomers selected from (a) a group of polymerizable aromatic sulfonic acid monomers and (b) a group of polymerizable hydrocarbon monomers. The above (a)
A polymer containing the following components as essential components. (A 2 ): A polymer obtained by polymerizing one or more monomers selected from the group of polymerizable hydrocarbon monomers, which contains at least one polymerizable aromatic monomer as an essential component. 1. A dispersant for an aqueous slurry of carbonaceous fine powder, comprising: a polymer obtained by sulfonating a polymer containing the same; and (B): a polymer of a polymerizable aliphatic unsaturated sulfonic acid monomer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60015469A JPS61176695A (en) | 1985-01-31 | 1985-01-31 | Dispersant for aqueous slurry of carbonaceous fine powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60015469A JPS61176695A (en) | 1985-01-31 | 1985-01-31 | Dispersant for aqueous slurry of carbonaceous fine powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61176695A JPS61176695A (en) | 1986-08-08 |
| JPH0445554B2 true JPH0445554B2 (en) | 1992-07-27 |
Family
ID=11889655
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60015469A Granted JPS61176695A (en) | 1985-01-31 | 1985-01-31 | Dispersant for aqueous slurry of carbonaceous fine powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61176695A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022239391A1 (en) | 2021-05-12 | 2022-11-17 | 東洋システム株式会社 | Battery performance evaluation device and battery performance evaluation method |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20020028860A1 (en) * | 1999-04-16 | 2002-03-07 | E. Michael Kerr | Method of modifying rheology of slurries in mineral processing |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5411508U (en) * | 1977-06-27 | 1979-01-25 | ||
| JPH0144646Y2 (en) * | 1981-04-09 | 1989-12-25 | ||
| JPS59117720U (en) * | 1983-01-30 | 1984-08-08 | 共栄工業株式会社 | Partition panel with cord storage area |
-
1985
- 1985-01-31 JP JP60015469A patent/JPS61176695A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022239391A1 (en) | 2021-05-12 | 2022-11-17 | 東洋システム株式会社 | Battery performance evaluation device and battery performance evaluation method |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61176695A (en) | 1986-08-08 |
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| JPH0329115B2 (en) |