JPH028982B2 - - Google Patents
Info
- Publication number
- JPH028982B2 JPH028982B2 JP12257685A JP12257685A JPH028982B2 JP H028982 B2 JPH028982 B2 JP H028982B2 JP 12257685 A JP12257685 A JP 12257685A JP 12257685 A JP12257685 A JP 12257685A JP H028982 B2 JPH028982 B2 JP H028982B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- cement
- treatment liquid
- rodax
- fumax
- 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 - Lifetime
Links
- 239000007788 liquid Substances 0.000 claims description 28
- 238000011282 treatment Methods 0.000 claims description 22
- 239000004568 cement Substances 0.000 claims description 18
- 239000000203 mixture Substances 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 13
- 229920001732 Lignosulfonate Polymers 0.000 claims description 10
- 239000007787 solid Substances 0.000 claims description 9
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 7
- 239000003245 coal Substances 0.000 claims description 7
- 229910052717 sulfur Inorganic materials 0.000 claims description 7
- 239000011593 sulfur Substances 0.000 claims description 7
- 229910052783 alkali metal Inorganic materials 0.000 claims description 6
- 150000001340 alkali metals Chemical class 0.000 claims description 6
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 6
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 6
- 238000000197 pyrolysis Methods 0.000 claims description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 13
- 239000003638 chemical reducing agent Substances 0.000 description 12
- 239000000126 substance Substances 0.000 description 12
- 150000003839 salts Chemical class 0.000 description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 239000000243 solution Substances 0.000 description 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 7
- 239000004567 concrete Substances 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 229910021529 ammonia Inorganic materials 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- LELOWRISYMNNSU-UHFFFAOYSA-N hydrogen cyanide Chemical compound N#C LELOWRISYMNNSU-UHFFFAOYSA-N 0.000 description 6
- NJYFRQQXXXRJHK-UHFFFAOYSA-N (4-aminophenyl) thiocyanate Chemical class NC1=CC=C(SC#N)C=C1 NJYFRQQXXXRJHK-UHFFFAOYSA-N 0.000 description 5
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 5
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 5
- 230000001737 promoting effect Effects 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 239000002585 base Substances 0.000 description 4
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 3
- 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 3
- 239000001110 calcium chloride Substances 0.000 description 3
- 229910001628 calcium chloride Inorganic materials 0.000 description 3
- 239000003153 chemical reaction reagent Substances 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 239000002440 industrial waste Substances 0.000 description 3
- 230000000979 retarding effect Effects 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- DHCDFWKWKRSZHF-UHFFFAOYSA-N sulfurothioic S-acid Chemical compound OS(O)(=O)=S DHCDFWKWKRSZHF-UHFFFAOYSA-N 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 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 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 2
- 239000000920 calcium hydroxide Substances 0.000 description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000005077 polysulfide Substances 0.000 description 2
- 229920001021 polysulfide Polymers 0.000 description 2
- 150000008117 polysulfides Polymers 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000003672 processing method Methods 0.000 description 2
- AEQDJSLRWYMAQI-UHFFFAOYSA-N 2,3,9,10-tetramethoxy-6,8,13,13a-tetrahydro-5H-isoquinolino[2,1-b]isoquinoline Chemical compound C1CN2CC(C(=C(OC)C=C3)OC)=C3CC2C2=C1C=C(OC)C(OC)=C2 AEQDJSLRWYMAQI-UHFFFAOYSA-N 0.000 description 1
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- QXKAIJAYHKCRRA-JJYYJPOSSA-N D-arabinonic acid Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)C(O)=O QXKAIJAYHKCRRA-JJYYJPOSSA-N 0.000 description 1
- 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 1
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 1
- 239000011398 Portland cement Substances 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000007824 aliphatic compounds Chemical class 0.000 description 1
- 125000002947 alkylene group Chemical group 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229920005551 calcium lignosulfonate Polymers 0.000 description 1
- RYAGRZNBULDMBW-UHFFFAOYSA-L calcium;3-(2-hydroxy-3-methoxyphenyl)-2-[2-methoxy-4-(3-sulfonatopropyl)phenoxy]propane-1-sulfonate Chemical compound [Ca+2].COC1=CC=CC(CC(CS([O-])(=O)=O)OC=2C(=CC(CCCS([O-])(=O)=O)=CC=2)OC)=C1O RYAGRZNBULDMBW-UHFFFAOYSA-L 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- ZBCBWPMODOFKDW-UHFFFAOYSA-N diethanolamine Chemical compound OCCNCCO ZBCBWPMODOFKDW-UHFFFAOYSA-N 0.000 description 1
- 150000002169 ethanolamines Chemical class 0.000 description 1
- 238000009415 formwork Methods 0.000 description 1
- 239000000174 gluconic acid Substances 0.000 description 1
- 235000012208 gluconic acid Nutrition 0.000 description 1
- 239000011440 grout Substances 0.000 description 1
- 125000004356 hydroxy functional group Chemical group O* 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000006072 paste Substances 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- OXNIZHLAWKMVMX-UHFFFAOYSA-N picric acid Chemical compound OC1=C([N+]([O-])=O)C=C([N+]([O-])=O)C=C1[N+]([O-])=O OXNIZHLAWKMVMX-UHFFFAOYSA-N 0.000 description 1
- WSHYKIAQCMIPTB-UHFFFAOYSA-M potassium;2-oxo-3-(3-oxo-1-phenylbutyl)chromen-4-olate Chemical compound [K+].[O-]C=1C2=CC=CC=C2OC(=O)C=1C(CC(=O)C)C1=CC=CC=C1 WSHYKIAQCMIPTB-UHFFFAOYSA-M 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000011150 reinforced concrete Substances 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000000176 sodium gluconate Substances 0.000 description 1
- 229940005574 sodium gluconate Drugs 0.000 description 1
- 235000012207 sodium gluconate Nutrition 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B18/00—Use of agglomerated or waste materials or refuse as fillers for mortars, concrete or artificial stone; Treatment of agglomerated or waste materials or refuse, specially adapted to enhance their filling properties in mortars, concrete or artificial stone
- C04B18/04—Waste materials; Refuse
- C04B18/06—Combustion residues, e.g. purification products of smoke, fumes or exhaust gases
- C04B18/062—Purification products of smoke, fume or exhaust-gases
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Ceramic Engineering (AREA)
- Combustion & Propulsion (AREA)
- Civil Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Description
(産業上の利用分野)
本発明は石炭乾溜ガスをフマツクス・ロダツク
ス法により処理して得られる処理液をセメント組
成物用促進剤として利用する発明、ならびに該処
理液を成分として含む減水剤組成物に関するもの
である。
(従来の技術)
セメント組成物(セメントペースト、モルタ
ル、グラウト、コンクリート等の総称)の強度発
現を促進するため促進剤を添加することは従来一
般に行なわれている。例えば低温時の施工、脱型
を早めて型枠の回転を早くする場合、等である。
また、遅延性を有する混和剤と併用してその遅延
性を打ち消す目的でも使用される。
従来、促進剤としては塩化カルシウムが安価で
かつ効果の大きい促進剤として一般に使用されて
きたが、このものは鉄筋コンクリート中の鉄筋を
発錆させるので近時その使用が厳しく規制される
に至つている。そこで塩化物を含まないいわゆる
ノンクロライド型促進剤が当業界において望まれ
ているが、現在提案されているノンクロライド型
促進剤は価格と効果との兼合い、すなわちコスト
パーフオーマンスの点で塩化カルシウムにくらべ
不満足なものである。
(発明が解決しようとする問題点)
本発明はコストパーフオーマンスのよいノンク
ロライド型促進剤を提供することを目的とするも
のである。さらに本発明は塩化物を含まない標準
形または促進形減水剤を提供することも目的とす
るものである。そして本発明は石炭乾溜ガスをフ
マツクス・ロダツクス法により処理して得られる
処理液を促進剤として利用することによりこれら
の目的を達成し得たものである。ところで上記処
理液は産業廃棄物であるが、本発明はこの産業廃
棄物の有効利用をも目的とするものである。
(発明を解決するための手段)
本発明は、第1に、石炭乾溜ガスをフマツク
ス・ロダツクス法により処理して得られるアルカ
リ金属ベースまたはアルカリ土金属ベースの処理
液(遊離硫黄等の懸濁物を除去したもの)を固形
分換算でセメント重量基準0.02〜2.0重量%含有
することを特徴とするセメント組成物、である。
(以下第1発明と記す)
さらに、本発明は、第2に、セメント重量基準
で、
(イ) 上記処理液(懸濁物を除去したもの)を固形
分換算0.05〜1.0重量%
(ロ) リグニンスルホン酸塩を0.01〜0.25重量%
(ハ) オキシカルボン酸塩を0.01〜0.10重量%かつ
(ロ)と(ハ)の合計を0.05重量%以上
(ニ) アルカノールアミンを0.002〜0.02重量%含
有することを特徴とするセメント組成物、であ
る。(以下第2発明と記す)
上記フマツクス・ロダツクス法とは石炭乾溜中
の硫化水素、シアン化水素、アンモニア等の有害
物質を除去する処理法として我国において開発さ
れた処理法であつて、国内各所において実施され
ている。これについては硫酸協会発行の「硫酸と
工業」誌昭和50年6月号9〜13頁に記載がある
が、その概要を述べれば次の通りである。石炭乾
溜ガス中の硫化水素をアルカリ性水溶液に吸収さ
せ、ついでこの吸収液を酸化触媒(例えばピクリ
ン酸)存在下に空気と接触させると硫化水素が酸
化されて硫黄が遊離する。これをフマツクス工程
という。遊離した硫黄は吸収液中のアルカリ性物
質および硫化水素と共に反応して多硫化塩とな
る。一方、乾溜ガス中のシアン化水素は吸収液中
にシアン塩として存在するが、これと前記多硫化
塩とが反応してロダン塩が生成する。これをロダ
ツクス法という。かくて、フマツクス・ロダツク
ス法処理により乾溜ガス中の硫化水素およびシア
ン化水素はロダン塩となつて除去される。従つて
フマツクス・ロダツクス処理液中にはロダン塩が
主成分として存在するが、このほかチオ硫酸塩、
その他の副生物も含まれる。
上記吸収液中のアルカリ性物質としてアンモニ
ア、水酸化ナトリウム、水酸化カルシウム等種々
のものが使用でき、それに応じて処理液中の塩は
該アルカリ性物質の塩となる。そして、使用した
アルカリ性物質の名を冠して何々ベースの処理液
という。例えば水酸化ナトリウムを使用したとき
はナトリウムベースといゝ、水酸化カルシウムを
使用したときはカルシウムベースという。通常、
吸収液中のアルカリ性物質としてアンモニアが用
いられるが、アンモニアベースの処理液はセメン
ト組成物に添加した場合アンモニアガスを遊離し
取扱上適当でないから、本発明においてはアルカ
リ金属ベースまたはアルカリ土金属ベースの処理
液が選ばれる。さらに、フマツクス・ロダツクス
法処理液中には遊離硫黄等の懸濁物が浮遊してお
り、これら懸濁物の存在は処理液の混和剤として
の利用に種々不利な結果をもたらすのでこれを除
去する。また、懸濁物除去のほか多少の処理を施
したものも本発明における処理液に含まれるもの
とする。かかる多少の処理とは、濃縮または冷却
時析出する物質の除去、活性炭処理による微量フ
エノール類の除去、塩変換、等である。なお、ア
ンモニアベースの処理液から塩変換によりアルカ
リ金属ベースやアルカリ土金属ベースとなし得
る。
本発明に使用されるフマツクス・ロダツクス法
処理液(アルカリ金属ベースまたはアルカリ土金
属ベースであつてかつ硫黄等の懸濁物質を除去し
たもの)中の固形分の組成は、全固形分中ロダン
塩が約75〜93%、(通常85〜90%)チオ硫酸塩が
約2〜15%(通常5〜10%)で両者合計約90〜95
%で、残りは各種副生物である。
本発明に使用される上記フマツクス・ロダツク
ス法処理液はこれをセメント組成物に添加すると
セメント組成物の強度発現を促進する促進効果を
示す。そして該処理液の適当な使用量(セメント
重量基準の添加重量%)は0.02〜2.0%(好まし
くは0.05〜1.0%)である。これより少ないとき
は促進効果不充分であり、また、これより多くし
ても促進効果は頭打ちとなり経済的に不利とな
る。
本発明に使用される上記処理液は単味で使用さ
れるほか他の促進剤や減水剤と併用することがで
きる。また、各種混和材料(AE剤、膨張剤、粘
性付与剤、ポゾラン物質粉末、高炉水砕スラグ粉
末、等)とも併用できる。しかしながら、リグニ
ンスルホン酸塩、オキシカルボン酸塩およびアル
カノールアミン(特にトリエタノールアミン)の
3成分と併用するときは、性能のすぐれた標準形
または促進形減水剤を構成することがわかり、こ
こに第2発明を提供するに至つた。
第2発明における各添加成分の使用量は前述の
範囲内である。(ただしリグニンスルホン酸塩と
オキシカルボン酸塩の合計使用量は0.05%以上と
する。)この範囲は効果、経済性等の諸要素のバ
ランスを意図して多くの試験を重ねたうえ最適の
ものとして決定されたものである。第2発明にお
いて、各成分はそれぞれ所定の使用量となるよう
別々にセメント組成物に添加してもよく、また、
全成分を一剤に組成したものを添加してもよい。
(この場合には、各成分が所定の使用量となるよ
う一剤組成の混和剤の使用量および成分組成比を
定める)
第2発明におけるリグニンスルホン酸塩は亜硫
酸パルプ廃液より得られる混和剤品位のものであ
り、オキシカルボン酸塩は、同一分子内にヒドロ
キシ基とカルボキシ基の双方を有する脂肪族化合
物であるオキシカルボン酸(クエン酸、アラボン
酸、グルコン酸、グルコヘプトン酸、等)の水溶
性塩である。また、アルカノールアミンはアンモ
ニアにアルキレンオキサイドが付加した形の化合
物で、エチレンオキサイドが付加した形のエタノ
ールアミン類(モノエタノールアミン、ジエタノ
ールアミン、トリエタノールアミン)が好まし
く、特にトリエタノールアミンが好ましい。
リグニンスルホン酸塩およびオキシカルボン酸
塩は共に遅延形減水剤として知られており、これ
に塩化カルシウム等の促進剤を配合してその遅延
性を打消した標準形または促進形減水剤が提供さ
れている。本発明に使用される上記処理液をこれ
らに配合することにより遅延性を打消すことがで
きるがその配合量はかなり多い水準となる。一
方、リグニンスルホン酸塩とオキシカルボン酸塩
を併用すると各単味使用よりも減水剤としての性
能が相乗的に向上する。また、本発明に使用され
る上記処理液は単味で使用するよりもアルカノー
ルアミン、特にトリエタノールアミンの小量と併
用すると促進効果が相乗的に向上するので処理液
の配合量を大幅に低減できる。かくて上記4成分
を配合することにより全体としての使用量が少な
くてすみすぐれた性能のノンクロライド型の標準
形または促進形減水剤を提供することができた。
なおこの減水剤は必要に応じAE剤や各種混和材
料を併用できる。なお、リグニンスルホン酸塩ま
たはオキシカルボン酸塩単独に処理液とアルカノ
ールアミンを配合した3成分系減水剤も使用でき
る。
(発明の効果)
本発明によりコストパーフオーマンスのすぐれ
たノンクロライド型促進剤が提供され、さらに第
2発明によりすぐれた性能のノンクロライド型の
標準形または促進形減水剤が提供されるに至つ
た。加うるに、産業廃棄物であるフマツクス・ロ
ダツクス法処理液の有効利用が図られることにな
つた。これらの産業的意義は極めて大きい。
実施例 1
本例は第1発明の効果をコンクリート試験によ
り示したものである。
(1) コンクリート試験に用いた材料
セメント:普通ポルトランドセメント
粗骨材:硬質砂岩砕石、最大寸法20mm
細骨材:大井川産川砂
フマツクス・ロダツクス法処理液(懸濁物を除
去したもの):全固形分中ロダン塩が89%、チ
オ硫酸塩が5%であり、Aはナトリウムベー
ス、Bはカルシウムベースである。
ロダンナトリウム:試薬1級品
(2) コンクリートの配合
C=320Kg/m3、W=192Kg/m3、W/C=60
%、s/a=49%、スランプ=18±2cm、空気
=1.5〜2.2%
(3) 試験結果を第1表に示す。養生温度は20℃お
よび5℃。処理液使用量は固形分換算である。
(Industrial Application Field) The present invention relates to an invention in which a treatment liquid obtained by treating coal dry distillation gas by the Fumax Rodax method is used as an accelerator for cement compositions, and a water reducing agent composition containing the treatment liquid as a component. It is related to. (Prior Art) In order to promote the strength development of cement compositions (general term for cement paste, mortar, grout, concrete, etc.), it has been common practice to add an accelerator. For example, when performing construction at low temperatures, when demolding is accelerated to speed up the rotation of the formwork, etc.
It is also used in combination with an admixture that has retarding properties to cancel out the retarding properties. Calcium chloride has traditionally been used as an inexpensive and highly effective accelerator, but its use has recently been strictly regulated because it causes rust in the reinforcing bars in reinforced concrete. . Therefore, a so-called non-chloride type accelerator that does not contain chloride is desired in this industry, but the currently proposed non-chloride type accelerator has a balance between price and effectiveness, that is, from the point of view of cost performance, it is better to use calcium chloride. It is unsatisfactory compared to (Problems to be Solved by the Invention) An object of the present invention is to provide a non-chloride type accelerator with good cost performance. It is a further object of the present invention to provide standard or accelerated water reducers that are chloride-free. The present invention has achieved these objects by using a treatment liquid obtained by treating coal dry distilled gas by the Fumax Rodax method as an accelerator. By the way, the above-mentioned processing liquid is industrial waste, and the present invention also aims at the effective use of this industrial waste. (Means for Solving the Invention) The present invention firstly provides an alkali metal-based or alkaline earth metal-based treatment liquid (suspended substances such as free sulfur) obtained by treating coal dry distilled gas by a fumux-rodax method. This is a cement composition characterized by containing 0.02 to 2.0% by weight of cement (based on the weight of cement) in terms of solid content.
(hereinafter referred to as the first invention) Furthermore, secondly, the present invention provides that (a) the above treatment liquid (from which suspended matter has been removed) is 0.05 to 1.0% by weight in terms of solid content (b) based on the weight of cement; 0.01 to 0.25% by weight of lignin sulfonate (c) 0.01 to 0.10% by weight of oxycarboxylate and
A cement composition characterized in that the total of (b) and (c) is 0.05% by weight or more and (d) alkanolamine is contained in an amount of 0.002 to 0.02% by weight. (Hereinafter referred to as the 2nd invention) The above-mentioned fumax-rodax method is a processing method developed in Japan as a processing method for removing harmful substances such as hydrogen sulfide, hydrogen cyanide, and ammonia during dry distillation of coal, and is implemented in various parts of the country. has been done. This is described in the June 1975 issue of the magazine ``Sulfuric Acid and Industry'' published by the Japan Sulfuric Acid Association, pages 9-13, and the summary is as follows. When hydrogen sulfide in coal dry distillation gas is absorbed into an alkaline aqueous solution and then this absorption liquid is brought into contact with air in the presence of an oxidation catalyst (for example, picric acid), hydrogen sulfide is oxidized and sulfur is liberated. This is called the fumatsu process. The liberated sulfur reacts with alkaline substances and hydrogen sulfide in the absorption liquid to form polysulfide salts. On the other hand, hydrogen cyanide in the dry distillation gas exists as a cyanide salt in the absorption liquid, and this reacts with the polysulfide salt to generate rhodan salt. This is called the Rodax method. Thus, hydrogen sulfide and hydrogen cyanide in the dry distilled gas are converted into rhodan salts and removed by the Fumax-Rodax process. Therefore, rhodan salt is present as the main component in the Fumax/Rhodacus treatment solution, but in addition, thiosulfate,
Other by-products are also included. Various alkaline substances such as ammonia, sodium hydroxide, calcium hydroxide, etc. can be used as the alkaline substance in the absorption liquid, and the salt in the treatment liquid accordingly becomes a salt of the alkaline substance. It is called a so-and-so-based processing solution, named after the alkaline substance used. For example, when sodium hydroxide is used, it is called sodium base, and when calcium hydroxide is used, it is called calcium base. usually,
Ammonia is used as the alkaline substance in the absorption liquid, but since an ammonia-based treatment liquid releases ammonia gas when added to a cement composition and is not suitable for handling, in the present invention, an alkali metal-based or alkaline earth metal-based treatment liquid is used. A processing solution is selected. Furthermore, suspended substances such as free sulfur are suspended in the treatment liquid of the Fumacs Rodax method, and the presence of these suspended substances has various disadvantageous effects on the use of the treatment liquid as an admixture, so they must be removed. do. In addition, the treatment liquid in the present invention includes those that have been subjected to some processing in addition to removal of suspended matter. Such minor treatments include removal of substances precipitated during concentration or cooling, removal of trace amounts of phenols by activated carbon treatment, salt conversion, and the like. Note that an ammonia-based treatment solution can be converted to an alkali metal base or an alkaline earth metal base by salt conversion. The composition of the solid content in the Fumax-Rhodacus process solution (based on alkali metals or alkaline earth metals and from which suspended solids such as sulfur have been removed) used in the present invention is as follows: about 75-93% (usually 85-90%) and about 2-15% (usually 5-10%) thiosulfate, totaling about 90-95%.
%, and the rest are various by-products. When added to a cement composition, the Fumax-Rhodax treatment solution used in the present invention exhibits a promoting effect of promoting strength development of the cement composition. The appropriate amount of the treatment liquid (added weight % based on cement weight) is 0.02 to 2.0% (preferably 0.05 to 1.0%). When the amount is less than this, the promoting effect is insufficient, and even when the amount is more than this, the promoting effect reaches a ceiling and becomes economically disadvantageous. The above treatment liquid used in the present invention can be used alone or in combination with other accelerators or water reducing agents. It can also be used in combination with various admixtures (AE agent, expansion agent, viscosity imparting agent, pozzolan substance powder, granulated blast furnace slag powder, etc.). However, when used in combination with the three components lignin sulfonate, oxycarboxylate and alkanolamine (particularly triethanolamine), it has been found to constitute an excellent performing standard or accelerated water reducer, and is hereby incorporated by reference. We have now provided two inventions. The amount of each additive component used in the second invention is within the above-mentioned range. (However, the total amount of lignin sulfonate and oxycarboxylate used must be 0.05% or more.) This range is the optimal one after many tests with the aim of balancing various factors such as effectiveness and economical efficiency. It was decided that In the second invention, each component may be added to the cement composition separately in a predetermined amount, and
It is also possible to add all components in one composition.
(In this case, the usage amount and component composition ratio of the admixture in the single-component composition are determined so that each component is used in the predetermined usage amount.) The lignin sulfonate in the second invention is an admixture grade obtained from sulfite pulp waste liquid. Oxycarboxylic acid salts are water-soluble compounds of oxycarboxylic acids (citric acid, arabic acid, gluconic acid, glucoheptonic acid, etc.), which are aliphatic compounds that have both hydroxy and carboxy groups in the same molecule. It's salt. Further, alkanolamine is a compound in which alkylene oxide is added to ammonia, and ethanolamines in which ethylene oxide is added (monoethanolamine, diethanolamine, triethanolamine) are preferable, and triethanolamine is particularly preferable. Both lignin sulfonates and oxycarboxylate salts are known as delayed-type water-reducing agents, and standard or accelerated-type water-reducing agents have been provided in which an accelerator such as calcium chloride is added to the lignin sulfonate and oxycarboxylate to counteract the retarding effect. There is. By blending the above-mentioned processing liquid used in the present invention with these, the retardation can be canceled out, but the amount to be blended is quite large. On the other hand, when a lignin sulfonate and an oxycarboxylic acid salt are used in combination, the performance as a water reducing agent is synergistically improved compared to when each is used alone. In addition, when the processing liquid used in the present invention is used in combination with a small amount of alkanolamine, especially triethanolamine, the promoting effect is synergistically improved rather than when used alone, so the amount of processing liquid to be blended can be significantly reduced. can. Thus, by blending the above-mentioned four components, it was possible to provide a non-chloride type standard or accelerated water reducing agent with excellent performance and requiring only a small amount of use as a whole.
Note that this water reducing agent can be used in combination with an AE agent or various admixtures if necessary. Note that a three-component water reducing agent in which a treatment liquid and an alkanolamine are blended with a lignin sulfonate or an oxycarboxylate alone can also be used. (Effects of the Invention) The present invention provides a non-chloride accelerator with excellent cost performance, and the second invention provides a non-chloride standard or accelerated water reducer with excellent performance. . In addition, efforts were made to make effective use of industrial waste treated by the Fumacs Rodax method. The industrial significance of these is extremely large. Example 1 This example shows the effect of the first invention through a concrete test. (1) Materials used for concrete tests Cement: Ordinary Portland cement Coarse aggregate: Hard sandstone crushed stone, maximum dimension 20 mm Fine aggregate: River sand from Oigawa River Fumax-Rhodax process solution (removed suspended matter): Total solid The content is 89% rhodan salt and 5% thiosulfate, with A being sodium-based and B being calcium-based. Rodan sodium: Reagent grade 1 (2) Concrete mix C = 320Kg/m 3 , W = 192Kg/m 3 , W/C = 60
%, s/a=49%, slump=18±2cm, air=1.5-2.2% (3) The test results are shown in Table 1. The curing temperature was 20℃ and 5℃. The amount of processing liquid used is based on solid content.
【表】
実施例 2
本例は第2発明の効果をコンクリート試験によ
り示したものである。
(1) コンクリート試験に用いた材料
セメント、粗骨材、細骨材は実施例1で用い
られたものと同一。
フマツクス・ロダツクス処理液は実施例1に
おけるAである。
オキシカルボン酸塩として試薬グルコン酸ナ
トリウムを、アルカノールアミンとして試薬ト
リエタノールアミンを用いた。
リグニンスルホン酸塩として混和剤品位のリ
グニンスルホン酸カルシウムを用いた。
(2) コンクリートの配合
第2表の試験番号No.7およびNo.13の場合
C=320Kg/m3、W=192Kg/m3、W/C=60
%、s/a=39%、スランプ=18±2cm、空気
=1〜2%
第2表の試験番号No.8〜No.12の場合
C=320Kg/m3、W=172Kg/m3、W/C=
53.8%、s/a=47%、スランプ=18±2cm、
空気=4±0.5%(AE剤添加により調整、)
(3) 試験結果を第2表に示す。養生温度は20゜お
よび5℃。処理液使用量は固形分換算である。[Table] Example 2 This example shows the effect of the second invention through a concrete test. (1) Materials used in concrete test Cement, coarse aggregate, and fine aggregate were the same as those used in Example 1. The Fumax Rodax treatment solution is A in Example 1. The reagent sodium gluconate was used as the oxycarboxylate salt, and the reagent triethanolamine was used as the alkanolamine. Admixture grade calcium lignosulfonate was used as the ligninsulfonate. (2) For test numbers No. 7 and No. 13 in Table 2 of concrete mix C = 320Kg/m 3 , W = 192Kg/m 3 , W/C = 60
%, s/a = 39%, slump = 18 ± 2 cm, air = 1 to 2% For test numbers No. 8 to No. 12 in Table 2 C = 320 Kg/m 3 , W = 172 Kg/m 3 , W/C=
53.8%, s/a=47%, slump=18±2cm,
Air = 4±0.5% (adjusted by adding AE agent) (3) The test results are shown in Table 2. The curing temperature was 20° and 5°C. The amount of processing liquid used is based on solid content.
【表】【table】
【表】
第2発明例は試験No.9〜12であるが、これは市
販の代表的なAE減水剤促進形(リグニンスルホ
ン酸ベースのもの)をその標準使用量0.25%使用
した場合と同等またはそれ以上の減水効果と促進
効果を示す。[Table] The second invention example is Test No. 9 to 12, which is equivalent to using a typical commercially available AE water reducer accelerated type (lignin sulfonic acid-based) at its standard usage amount of 0.25%. or more water reduction and promotion effects.
Claims (1)
より処理して得られるアルカリ金属ベースまたは
アルカリ土金属ベースの処理液(遊離硫黄等の懸
濁物を除去したもの)を固形分換算で、セメント
重量基準0.02〜2.0重量%含有することを特徴と
するセメント組成物。 2 セメント重量基準で (イ) 石炭乾溜ガスをフマツクス・ロダツクス法に
より処理して得られるアルカリ金属ベースまた
はアルカリ土金属ベースの処理液(遊離硫黄等
の懸濁物を除去したもの)を固形分換算0.05〜
1.0重量% (ロ) リグニンスルホン酸塩を0.01〜0.25重量% (ハ) オキシカルボン酸塩を0.01〜0.10重量%かつ
(ロ)と(ハ)の合計を0.05重量%以上 (ニ) アルカノールアミンを0.002〜0.02重量%含
有することを特徴とするセメント組成物。[Scope of Claims] 1. An alkali metal-based or alkaline earth metal-based treatment liquid (from which suspended matter such as free sulfur has been removed) obtained by treating coal dry distillation gas by the fumax-rodax method in terms of solid content. , 0.02 to 2.0% by weight based on cement weight. 2 Based on the weight of cement (a) The alkali metal-based or alkaline earth metal-based treatment liquid (from which suspended matter such as free sulfur has been removed) obtained by treating coal dry distilled gas by the Fumax-Rodax method is converted to solid content. 0.05~
1.0% by weight (b) 0.01 to 0.25% by weight of lignin sulfonate (c) 0.01 to 0.10% by weight of oxycarboxylate and
A cement composition characterized in that the total of (b) and (c) is 0.05% by weight or more and (d) alkanolamine is contained in an amount of 0.002 to 0.02% by weight.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60122576A JPS61286253A (en) | 1985-06-07 | 1985-06-07 | Cement composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60122576A JPS61286253A (en) | 1985-06-07 | 1985-06-07 | Cement composition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61286253A JPS61286253A (en) | 1986-12-16 |
| JPH028982B2 true JPH028982B2 (en) | 1990-02-28 |
Family
ID=14839325
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60122576A Granted JPS61286253A (en) | 1985-06-07 | 1985-06-07 | Cement composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61286253A (en) |
-
1985
- 1985-06-07 JP JP60122576A patent/JPS61286253A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61286253A (en) | 1986-12-16 |
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