JPS6347760B2 - - Google Patents
Info
- Publication number
- JPS6347760B2 JPS6347760B2 JP10759880A JP10759880A JPS6347760B2 JP S6347760 B2 JPS6347760 B2 JP S6347760B2 JP 10759880 A JP10759880 A JP 10759880A JP 10759880 A JP10759880 A JP 10759880A JP S6347760 B2 JPS6347760 B2 JP S6347760B2
- Authority
- JP
- Japan
- Prior art keywords
- calcium
- weight
- grease
- base oil
- amount
- 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
- -1 alicyclic carboxylic acid Chemical class 0.000 claims description 57
- 239000004519 grease Substances 0.000 claims description 44
- 239000002199 base oil Substances 0.000 claims description 39
- 239000011575 calcium Substances 0.000 claims description 39
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 38
- 229910052791 calcium Inorganic materials 0.000 claims description 38
- 150000005846 sugar alcohols Polymers 0.000 claims description 27
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 22
- 239000004215 Carbon black (E152) Substances 0.000 claims description 13
- 229930195733 hydrocarbon Natural products 0.000 claims description 13
- 150000002430 hydrocarbons Chemical class 0.000 claims description 13
- 239000003795 chemical substances by application Substances 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 239000012188 paraffin wax Substances 0.000 claims description 4
- 239000000654 additive Substances 0.000 description 16
- 238000007127 saponification reaction Methods 0.000 description 13
- 238000000034 method Methods 0.000 description 12
- 239000003921 oil Substances 0.000 description 12
- 235000019198 oils Nutrition 0.000 description 12
- 230000000996 additive effect Effects 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 9
- 239000002253 acid Substances 0.000 description 8
- 230000018044 dehydration Effects 0.000 description 8
- 238000006297 dehydration reaction Methods 0.000 description 8
- 239000000344 soap Substances 0.000 description 7
- 239000003760 tallow Substances 0.000 description 7
- 238000007792 addition Methods 0.000 description 6
- 235000015278 beef Nutrition 0.000 description 6
- 238000002474 experimental method Methods 0.000 description 6
- 239000003925 fat Substances 0.000 description 6
- 235000019197 fats Nutrition 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 239000002562 thickening agent Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 5
- 125000004432 carbon atom Chemical group C* 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- 238000005187 foaming Methods 0.000 description 5
- 235000014113 dietary fatty acids Nutrition 0.000 description 4
- 239000000194 fatty acid Substances 0.000 description 4
- 229930195729 fatty acid Natural products 0.000 description 4
- 150000004665 fatty acids Chemical class 0.000 description 4
- 239000011541 reaction mixture Substances 0.000 description 4
- ULQISTXYYBZJSJ-UHFFFAOYSA-N 12-hydroxyoctadecanoic acid Chemical compound CCCCCCC(O)CCCCCCCCCCC(O)=O ULQISTXYYBZJSJ-UHFFFAOYSA-N 0.000 description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 150000007513 acids Chemical class 0.000 description 3
- 150000007933 aliphatic carboxylic acids Chemical class 0.000 description 3
- 229910052783 alkali metal Inorganic materials 0.000 description 3
- 229910052788 barium Inorganic materials 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000011156 evaluation Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 239000010689 synthetic lubricating oil Substances 0.000 description 3
- VZFUCHSFHOYXIS-UHFFFAOYSA-N Cycloheptanecarboxylic acid Chemical compound OC(=O)C1CCCCCC1 VZFUCHSFHOYXIS-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- 239000003963 antioxidant agent Substances 0.000 description 2
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 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
- 235000011116 calcium hydroxide Nutrition 0.000 description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- JBDSSBMEKXHSJF-UHFFFAOYSA-N cyclopentanecarboxylic acid Chemical compound OC(=O)C1CCCC1 JBDSSBMEKXHSJF-UHFFFAOYSA-N 0.000 description 2
- DMBHHRLKUKUOEG-UHFFFAOYSA-N diphenylamine Chemical compound C=1C=CC=CC=1NC1=CC=CC=C1 DMBHHRLKUKUOEG-UHFFFAOYSA-N 0.000 description 2
- UKMSUNONTOPOIO-UHFFFAOYSA-N docosanoic acid Chemical compound CCCCCCCCCCCCCCCCCCCCCC(O)=O UKMSUNONTOPOIO-UHFFFAOYSA-N 0.000 description 2
- POULHZVOKOAJMA-UHFFFAOYSA-N dodecanoic acid Chemical compound CCCCCCCCCCCC(O)=O POULHZVOKOAJMA-UHFFFAOYSA-N 0.000 description 2
- IPCSVZSSVZVIGE-UHFFFAOYSA-N hexadecanoic acid Chemical compound CCCCCCCCCCCCCCCC(O)=O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 description 2
- 239000010687 lubricating oil Substances 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000011347 resin Chemical class 0.000 description 2
- 229920005989 resin Chemical class 0.000 description 2
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 description 1
- 229940114072 12-hydroxystearic acid Drugs 0.000 description 1
- KIHBGTRZFAVZRV-UHFFFAOYSA-N 2-Hydroxyoctadecanoic acid Natural products CCCCCCCCCCCCCCCCC(O)C(O)=O KIHBGTRZFAVZRV-UHFFFAOYSA-N 0.000 description 1
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 description 1
- HNNQYHFROJDYHQ-UHFFFAOYSA-N 3-(4-ethylcyclohexyl)propanoic acid 3-(3-ethylcyclopentyl)propanoic acid Chemical compound CCC1CCC(CCC(O)=O)C1.CCC1CCC(CCC(O)=O)CC1 HNNQYHFROJDYHQ-UHFFFAOYSA-N 0.000 description 1
- ZRPLANDPDWYOMZ-UHFFFAOYSA-N 3-cyclopentylpropionic acid Chemical compound OC(=O)CCC1CCCC1 ZRPLANDPDWYOMZ-UHFFFAOYSA-N 0.000 description 1
- NKFIBMOQAPEKNZ-UHFFFAOYSA-N 5-amino-1h-indole-2-carboxylic acid Chemical compound NC1=CC=C2NC(C(O)=O)=CC2=C1 NKFIBMOQAPEKNZ-UHFFFAOYSA-N 0.000 description 1
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 description 1
- 235000021357 Behenic acid Nutrition 0.000 description 1
- NLZUEZXRPGMBCV-UHFFFAOYSA-N Butylhydroxytoluene Chemical compound CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 NLZUEZXRPGMBCV-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 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 1
- 239000005639 Lauric acid Substances 0.000 description 1
- OYHQOLUKZRVURQ-HZJYTTRNSA-N Linoleic acid Chemical compound CCCCC\C=C/C\C=C/CCCCCCCC(O)=O OYHQOLUKZRVURQ-HZJYTTRNSA-N 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 1
- 239000005642 Oleic acid Substances 0.000 description 1
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 description 1
- 235000019482 Palm oil Nutrition 0.000 description 1
- 235000021314 Palmitic acid Nutrition 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- YSMRWXYRXBRSND-UHFFFAOYSA-N TOTP Chemical compound CC1=CC=CC=C1OP(=O)(OC=1C(=CC=CC=1)C)OC1=CC=CC=C1C YSMRWXYRXBRSND-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 229940116226 behenic acid Drugs 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 159000000007 calcium salts Chemical class 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 125000000113 cyclohexyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 description 1
- YFPCLQKFNXUAAK-UHFFFAOYSA-N cyclopentyl acetate Chemical compound CC(=O)OC1CCCC1 YFPCLQKFNXUAAK-UHFFFAOYSA-N 0.000 description 1
- YMGUBTXCNDTFJI-UHFFFAOYSA-N cyclopropanecarboxylic acid Chemical compound OC(=O)C1CC1 YMGUBTXCNDTFJI-UHFFFAOYSA-N 0.000 description 1
- SZXQTJUDPRGNJN-UHFFFAOYSA-N dipropylene glycol Chemical compound OCCCOCCCO SZXQTJUDPRGNJN-UHFFFAOYSA-N 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- FPIQZBQZKBKLEI-UHFFFAOYSA-N ethyl 1-[[2-chloroethyl(nitroso)carbamoyl]amino]cyclohexane-1-carboxylate Chemical compound ClCCN(N=O)C(=O)NC1(C(=O)OCC)CCCCC1 FPIQZBQZKBKLEI-UHFFFAOYSA-N 0.000 description 1
- 230000003631 expected effect Effects 0.000 description 1
- 235000021323 fish oil Nutrition 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000004678 hydrides Chemical class 0.000 description 1
- 125000001183 hydrocarbyl group Chemical group 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 description 1
- 235000020778 linoleic acid Nutrition 0.000 description 1
- OYHQOLUKZRVURQ-IXWMQOLASA-N linoleic acid Natural products CCCCC\C=C/C\C=C\CCCCCCCC(O)=O OYHQOLUKZRVURQ-IXWMQOLASA-N 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- OFUAIAKLWWIPTC-UHFFFAOYSA-L magnesium;naphthalene-2-carboxylate Chemical compound [Mg+2].C1=CC=CC2=CC(C(=O)[O-])=CC=C21.C1=CC=CC2=CC(C(=O)[O-])=CC=C21 OFUAIAKLWWIPTC-UHFFFAOYSA-L 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- WQEPLUUGTLDZJY-UHFFFAOYSA-N n-Pentadecanoic acid Natural products CCCCCCCCCCCCCCC(O)=O WQEPLUUGTLDZJY-UHFFFAOYSA-N 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 1
- 235000021313 oleic acid Nutrition 0.000 description 1
- 239000002540 palm oil Substances 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 150000003077 polyols Chemical class 0.000 description 1
- 229920001451 polypropylene glycol Polymers 0.000 description 1
- 235000015277 pork Nutrition 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000003449 preventive effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- TUNFSRHWOTWDNC-HKGQFRNVSA-N tetradecanoic acid Chemical compound CCCCCCCCCCCCC[14C](O)=O TUNFSRHWOTWDNC-HKGQFRNVSA-N 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 239000012905 visible particle Substances 0.000 description 1
Landscapes
- Lubricants (AREA)
Description
本発明はパラフイン系炭化水素基油からカルシ
ウム系グリースを製造する方法に関する。
カルシウム石けんを主増稠剤とするカルシウム
系グリースにおいては基油としてパラフイン系炭
化水素油を使用するとグリース化が困難なため、
基油は実際上ナフテン系炭化水素油に限定されて
しまうという制約がある。すなわちカルシウム系
グリースの場合基油としてパラフイン系潤滑油を
使用すると満足なグリース化が難しく、通常の方
法では粒状塊が生成したり、外観が不均一な形状
を呈するなど、性能的にも、商品としても満足な
グリースを製造することは難しい。
本発明者はこれらの問題点につき種々検討した
結果、多価アルコールと脂環式カルボン酸もしく
はその塩との共存下にけん化を行なうことによ
り、従来至難とされてきたパラフイン系炭化水素
基油を使用してカルシウム系グリースを製造でき
ることを見出して本発明を完成した。
すなわち本発明の要旨は、パラフイン系炭化水
素基油中において、0.1〜2.0重量%の多価アルコ
ールおよび少なくとも0.1重量%の脂環式カルボ
ン酸もしくはそのアルカリ土類金属塩の存在下
で、けん化されるべき脂肪材料をカルシウムけん
化剤によりけん化することを特徴とするカルシウ
ム系グリースの製造方法に存する。
本発明で基油となるパラフイン系炭化水素油と
しては、粘度指数約70以上、パラフイン分(n―
d―M分析法によるCp分)約55%以上のものが
使用できる。基油の粘度は約8cSt以上、好ましく
は約8〜850cSt、更に好ましくは約30〜400cSt
(40℃)のものが適当であり、また鉱油潤滑油の
ほか、液状ポリオレフインなどパラフイン系炭化
水素油に属する合成潤滑油も使用できる。基油は
また全体として上記に規定したパラフイン系であ
るなら少量のナフテン系炭化水素油等を含んでも
よいし、パラフイン系炭化水素油が主体(基油の
約70%以上、好ましくは約80重量%程度以上)で
あれば例えばエステル系合成潤滑油、シリコーン
油等炭化水素油以外の合成潤滑油を含むこともで
き、これらはけん化反応後に添加するのがよい。
パラフイン系基油中においてけん化反応を行な
い、カルシウム石けん増稠剤を形成する際、系内
に存在させる多価アルコールの例としては、エチ
レングリコール,プロピレングリコール,グリセ
リン,ジエチレングリコール,ジプロピレングリ
コール,液状ポリエチレングリコール,液状ポリ
プロピレングリコール,ポリオキシエチレン―オ
キシプロピレングリコールなどのポリオキシアル
キレン系ポリエーテルポリオール,ポリグリセリ
ンなどがある。多価アルコールの炭素数は2〜
500、特に2〜70、殊に2〜6程度のものが好ま
しい。多価アルコールの使用量は反応混合物中約
0.1〜2.0重量、好ましくは約0.3〜1.5重量%であ
る。またこの多価アルコールと併用する脂環式カ
ルボン酸もしくはそのアルカリ土類金属塩の例と
してはシクロペンタンカルボン酸,シクロヘキサ
ンカルボン酸,シクロヘプタンカルボン酸,シク
ロプロパンカルボン酸,ナフテン酸,シクロペン
チル酢酸,シクロヘキシル酢酸,シクロペンチル
プロピオン酸(これらの酸は核にアルキル基等炭
化水素置換基があつてもよい。)、およびこれらの
バリウム,マグネシウム,カルシウム等アルカリ
土類金属塩がある。脂環式カルボン酸もしくはそ
のアルカリ土類金属塩の好ましい炭素数は4〜
60、特に4〜30程度である。脂環式カルボン酸の
アルカリ金属塩は多価アルコールと併用しても稠
度収率(増稠剤量を一定にした場合は他より稠度
値の小さいグリースが得られるとき、あるいは稠
度を一定にした場合は他より少ない増稠剤量で所
定のグリースが得られるとき、いずれも稠度収率
が高いあるいは収率が高いという。逆の場合は稠
度収率あるいは収率が低いという。
“NLGI SPOKESMAN”誌,22巻,509頁
1959年2月および「丸善石油技報」第20号75頁,
1975年参照。)が低く、不適当である。脂環式カ
ルボン酸もしくはそのアルカリ土類金属塩の使用
量は反応混合物中少なくとも0.1重量%以上が必
要で、特に約0.5〜5重量%が好ましい。
多価アルコールおよび、脂環式カルボン酸もし
くはそのアルカリ土類金属塩の使用量は上記規定
量よりも少ないと効果がなくグリース化が困難で
あり、また多すぎても満足なグリース構造が形成
されなかつたり、混和稠度値が急に大きい値とな
つたり、あるいは脱水工程で発泡を生じて満足な
グリース化が達成されないという現象が生起する
などのため、本発明の目的が達成されない。これ
ら添加物の添加割合は重量比で多価アルコール1
に対し脂環式カルボン酸もしくはそのアルカリ土
類金属塩約2〜10の割合が好ましい。多価アルコ
ールと、脂環式カルボン酸もしくはそのアルカリ
土類金属塩は単独で使用しても目的は達せられな
いし、けん化が実質的に終了した後で添加しても
効果がない。
けん化されるべき脂肪材料としては通常カルシ
ウム石けん系グリースの製造に使用されている材
料が使用でき、その例としては脂肪族カルボン
酸,脂環式カルボン酸,樹脂酸などがある。脂環
式カルボン酸を使用する場合は前述したように多
すぎないようにすることが好ましく、従つて脂肪
族カルボン酸との混合物として使用することが好
ましい。けん化されるべき脂肪材料として油脂を
使用するとけん化反応に困難を生じ、また脱水工
程で発泡現象を生じて脱水困難になるなどの問題
があり好ましくない。油脂を脂肪材料の一部とし
て使用する場合少量にとどめるのがよい。脂肪族
カルボン酸は直鎖,分岐,飽和,不飽和のいずれ
でもよく、一般に炭素数約10〜30,特に約12〜24
のものが好ましく、その例としてはやし油酸,牛
脂酸,豚脂酸,植物油酸,魚油酸,これらの水素
化物,ラウリン酸,パルミチン酸,ミリスチン
酸,ステアリン酸,ベヘニン酸,オレイン酸,リ
ノール酸,ヒドロキシステアリン酸,オキソ合成
法やコツホ反応法による合成脂肪酸等がある。脂
環式カルボン酸,樹脂酸は炭素数4〜60、特に10
〜30程度のものが好ましい。これら脂肪材料をけ
ん化するカルシウム系けん化剤の例としては水酸
化カルシウム、あるいは酸化カルシウム等があ
る。カルシウムけん化剤を主体(けん化剤の約70
%重量%以上、好ましくは約80重量%程度以上)
とし、これにリチウム,ナトリウム,バリウム,
マグネシウム等の酸化物,水酸化物など他の金属
けん化剤を補助的に併用してもよい。けん化反応
により形成されるカルシウム系石けん増稠剤の量
はけん化反応混合物中約2〜50重量%、特に約5
〜20重量%が適当である。
本発明によるグリース化は基油としてナフテン
系基油の代りにパラフイン系基油を使用しかつ多
価アルコールと脂環式カルボン酸もしくはそのア
ルカリ土類金属塩とを存在させる以外常法による
ことができる。そのグリース化の一例を示すなら
ば基油,脂肪材料,多価アルコール、および脂環
式カルボン酸もしくはそのアルカリ土類金属塩を
加圧釜もしくは開放釜に入れ約60〜80℃に加熱し
て撹拌混合する。これにカルシウム系けん化剤と
水を加え内容物を撹拌しながら約80〜160℃で約
0.5〜4時間程度加熱してけん化反応を行なわせ
る。その後温度を約80〜110℃程度に保ちカルシ
ウム石けんの結晶生成を行なわせる。この段階で
反応混合物中の水分量を調節(蒸発させるかもし
くは補給する。適当な水分量は適宜実験により定
めることができる。通常水分量は約0.3〜3.0重量
%程度が好ましい。)し、また必要があれば残り
の基油を加える。その後内容物を冷却し、稠度を
調節するために更に基油の添加が必要であれば加
え、また必要により酸化防止剤,防食剤,その他
慣用のグリース添加剤を加える。また反応中ある
いはその後の工程における内容物の撹拌は釜内に
設けた撹拌羽根による方法、反応釜の一端から内
容物を抜き出して再度釜内へ循環する方法、内容
物をミルに通してミリングする方法等がある。本
発明におけるグリース化方法はパラフイン系基油
中においてカルシウム石けんの生成および結晶生
成が行なえるなら上記以外の方法も当然採用でき
る。本発明においては前記したように必要により
適宜グリース添加剤、例えばジフエニルアミン、
ジブチルパラクレゾールのような酸化防止剤,ト
リクレジルホスフエートのような極圧剤、その他
油性向上剤,防錆剤,構造安定剤,粘度指数向上
剤などを加えてもよく、これらの添加剤は通常そ
れぞれ約5重量%程度以下である。
本発明によるとパラフイン系炭化水素基油を用
いて外観の良好なカルシウム系グリースを製造す
ることができ、稠度収率もよい。製造されたグリ
ースは外観,性能ともナフテン系基油を用いて製
造された従来のカルシウム系グリースとほぼ同等
で、パラフイン系基油から従来至難とされてきた
カルシウム系グリースを容易に製造することに成
功したものである点工業的に非常に有利である。
次に実施例,比較例により本発明を説明する。
実施例,比較例において使用した基油A〜Eは第
1表の性状を有するものであり、多価アルコール
a〜d,脂環式カルボン酸e〜i,および脂環式
カルボン酸のアルカリ土類金属塩j〜lは第2表
に示すものを使用した。以下多価アルコールは添
加物(1)と略称し、脂環式カルボン酸もしくはその
アルカリ土類金属塩は添加物(2)と略称することが
ある。
The present invention relates to a method for producing calcium-based grease from paraffinic hydrocarbon base oil. Calcium-based greases that use calcium soap as the main thickener are difficult to form into grease when paraffin-based hydrocarbon oils are used as the base oil.
There is a restriction that the base oil is actually limited to naphthenic hydrocarbon oil. In other words, in the case of calcium-based grease, it is difficult to obtain a satisfactory grease when paraffin-based lubricating oil is used as the base oil, and the normal method produces granular lumps and has an uneven appearance, resulting in poor performance and product quality. However, it is difficult to produce a satisfactory grease. As a result of various studies regarding these problems, the present inventors have found that by saponifying polyhydric alcohols and alicyclic carboxylic acids or their salts in the coexistence, paraffinic hydrocarbon base oils, which have been considered extremely difficult, can be produced. The present invention was completed based on the discovery that calcium-based grease can be produced using the above-described method. That is, the gist of the present invention is that a paraffinic hydrocarbon base oil is saponified in the presence of 0.1 to 2.0% by weight of a polyhydric alcohol and at least 0.1% by weight of an alicyclic carboxylic acid or an alkaline earth metal salt thereof. The present invention relates to a method for producing a calcium-based grease, which comprises saponifying a fatty material to be processed using a calcium saponifying agent. The paraffinic hydrocarbon oil used as the base oil in the present invention has a viscosity index of about 70 or more and a paraffin content (n-
Cp content (Cp content determined by dM analysis method) of approximately 55% or more can be used. The viscosity of the base oil is about 8 cSt or more, preferably about 8 to 850 cSt, more preferably about 30 to 400 cSt.
(40°C) is suitable, and in addition to mineral oil lubricating oil, synthetic lubricating oil belonging to the paraffinic hydrocarbon oils such as liquid polyolefin can also be used. The base oil may also contain a small amount of naphthenic hydrocarbon oil, etc., if it is entirely paraffinic as defined above, or it may contain mainly paraffinic hydrocarbon oil (about 70% or more of the base oil, preferably about 80% by weight). % or more), synthetic lubricating oils other than hydrocarbon oils such as ester-based synthetic lubricating oils and silicone oils can also be included, and these are preferably added after the saponification reaction. When performing a saponification reaction in a paraffinic base oil to form a calcium soap thickener, examples of polyhydric alcohols present in the system include ethylene glycol, propylene glycol, glycerin, diethylene glycol, dipropylene glycol, and liquid polyethylene glycol. Examples include glycol, liquid polypropylene glycol, polyoxyalkylene-based polyether polyols such as polyoxyethylene-oxypropylene glycol, and polyglycerin. The number of carbon atoms in polyhydric alcohol is 2~
500, especially about 2 to 70, especially about 2 to 6 is preferred. The amount of polyhydric alcohol used in the reaction mixture is approx.
0.1-2.0% by weight, preferably about 0.3-1.5% by weight. Examples of alicyclic carboxylic acids or alkaline earth metal salts thereof used in combination with this polyhydric alcohol include cyclopentanecarboxylic acid, cyclohexanecarboxylic acid, cycloheptanecarboxylic acid, cyclopropanecarboxylic acid, naphthenic acid, cyclopentyl acetate, and cyclohexyl. Examples include acetic acid, cyclopentylpropionic acid (these acids may have a hydrocarbon substituent such as an alkyl group in the nucleus), and their alkaline earth metal salts such as barium, magnesium, and calcium. The preferred carbon number of the alicyclic carboxylic acid or its alkaline earth metal salt is 4 to 4.
60, especially about 4 to 30. Alkali metal salts of alicyclic carboxylic acids have a high consistency yield even when used in combination with polyhydric alcohols (if the amount of thickener is kept constant, a grease with a lower consistency value than others can be obtained, or if the consistency is kept constant) If a given grease can be obtained with a smaller amount of thickener than the others, it is said to have a high consistency yield or high yield.In the opposite case, it is said to have a low consistency yield or yield. “NLGI SPOKESMAN” Magazine, vol. 22, p. 509
February 1959 and “Maruzen Oil Technical Report” No. 20, p. 75,
See 1975. ) is low and inappropriate. The amount of the alicyclic carboxylic acid or alkaline earth metal salt used in the reaction mixture must be at least 0.1% by weight, and preferably about 0.5 to 5% by weight. If the amount of polyhydric alcohol and alicyclic carboxylic acid or its alkaline earth metal salt used is less than the above specified amount, it will be ineffective and difficult to form a grease, and if it is too much, a satisfactory grease structure will not be formed. The object of the present invention cannot be achieved because the mixing consistency value suddenly becomes large, or foaming occurs during the dehydration process and satisfactory greasing cannot be achieved. The addition ratio of these additives is 1 part polyhydric alcohol by weight.
The preferred ratio is about 2 to 10 parts of the alicyclic carboxylic acid or its alkaline earth metal salt. If the polyhydric alcohol and the alicyclic carboxylic acid or its alkaline earth metal salt are used alone, the purpose will not be achieved, and if added after saponification is substantially completed, there will be no effect. The fatty materials to be saponified can be those normally used in the production of calcium soap based greases, examples of which include aliphatic carboxylic acids, cycloaliphatic carboxylic acids, and resin acids. When using an alicyclic carboxylic acid, it is preferable not to use too much as mentioned above, and therefore it is preferable to use it as a mixture with an aliphatic carboxylic acid. The use of fats and oils as the fatty material to be saponified is not preferred because it causes difficulties in the saponification reaction and also causes problems such as foaming during the dehydration process, making dehydration difficult. When using fats and oils as part of the fat ingredients, it is best to limit the amount to a small amount. Aliphatic carboxylic acids may be linear, branched, saturated, or unsaturated, and generally have about 10 to 30 carbon atoms, especially about 12 to 24 carbon atoms.
Preferred examples include palm oil acid, beef tallow acid, pork fat acid, vegetable oil acid, fish oil acid, hydrides thereof, lauric acid, palmitic acid, myristic acid, stearic acid, behenic acid, oleic acid, and linoleic acid. , hydroxystearic acid, and synthetic fatty acids produced by the oxo synthesis method and the Kotsuho reaction method. Alicyclic carboxylic acids and resin acids have 4 to 60 carbon atoms, especially 10 carbon atoms.
~30 is preferred. Examples of calcium-based saponifying agents for saponifying these fatty materials include calcium hydroxide and calcium oxide. Mainly calcium saponifiers (about 70% of saponifiers)
(% weight % or more, preferably about 80 weight % or more)
To this, lithium, sodium, barium,
Other metal saponifying agents such as oxides and hydroxides such as magnesium may also be used in combination. The amount of calcium-based soap thickener formed by the saponification reaction is about 2 to 50% by weight in the saponification reaction mixture, especially about 5% by weight.
~20% by weight is suitable. Greasing according to the present invention can be carried out by any conventional method except that a paraffinic base oil is used instead of a naphthenic base oil and a polyhydric alcohol and an alicyclic carboxylic acid or an alkaline earth metal salt thereof are present. can. An example of making a grease is to put the base oil, fatty material, polyhydric alcohol, and alicyclic carboxylic acid or its alkaline earth metal salt into a pressure cooker or an open cooker, heat it to about 60-80℃, and stir. Mix. Add calcium-based saponification agent and water to this and heat the contents to about 80 to 160℃ while stirring.
The mixture is heated for about 0.5 to 4 hours to carry out the saponification reaction. Thereafter, the temperature is maintained at about 80 to 110°C to allow calcium soap to form crystals. At this stage, the amount of water in the reaction mixture is adjusted (evaporated or replenished. The appropriate amount of water can be determined by appropriate experiments. Usually, the amount of water is preferably about 0.3 to 3.0% by weight), and Add the remaining base oil if necessary. The contents are then cooled and further additions of base oil are added if necessary to adjust the consistency, as well as antioxidants, corrosion inhibitors, and other conventional grease additives, if necessary. The contents can be stirred during the reaction or in subsequent steps by using a stirring blade installed inside the reaction vessel, by extracting the contents from one end of the reaction vessel and circulating them back into the vessel, or by passing the contents through a mill for milling. There are methods etc. Naturally, methods other than those described above can also be used for the greasing method of the present invention as long as calcium soap and crystals can be produced in paraffinic base oil. In the present invention, as described above, appropriate grease additives such as diphenylamine,
Antioxidants such as dibutyl para-cresol, extreme pressure agents such as tricresyl phosphate, other oiliness improvers, rust preventives, structural stabilizers, viscosity index improvers, etc. may be added, and these additives are usually about 5% by weight or less each. According to the present invention, a calcium-based grease with good appearance can be produced using a paraffinic hydrocarbon base oil, and the consistency yield is also good. The manufactured grease has almost the same appearance and performance as conventional calcium-based grease manufactured using naphthenic base oil, and it is now possible to easily manufacture calcium-based grease from paraffinic base oil, which has traditionally been considered extremely difficult. The fact that it has been successful is very advantageous from an industrial perspective. Next, the present invention will be explained with reference to Examples and Comparative Examples.
The base oils A to E used in Examples and Comparative Examples have the properties shown in Table 1, and contain polyhydric alcohols a to d, alicyclic carboxylic acids e to i, and alkaline base oils of alicyclic carboxylic acids. The metal salts j to l shown in Table 2 were used. Hereinafter, the polyhydric alcohol may be abbreviated as additive (1), and the alicyclic carboxylic acid or its alkaline earth metal salt may be abbreviated as additive (2).
【表】【table】
【表】
また生成グリースの外観は次の5段階で評価し
た。
5… 良質のナフテン系基油を用いて製造したカ
ルシウム系グリースと同等の外観で光択があ
り、目視では粒子の存在が全くみられないも
の。
4… 評価が5と3の中間でそのどちらにも該当
しないと判断されるもの。
3… 直径0.5m/m以下の粒子が全体の50%以
上の割合で存在するもの。
2… 評価が3と1の中間でそのどちらにも該当
しないと判断されるもの。
1… 直径1.0m/m以上の粒子が全体の50%以
上の割合で存在するもの、または試料作成後24
時間を経過して1重量%以上の油の離しようが
みられるもの。
生成グリースの硬さはJlS K2220―1980の5.3
項に規定される混和稠度値で評価した。値が小さ
いほど硬いことをあらわす。
実施例 1
けん化反応釜として加熱型で単式撹拌羽根(回
転数15rpm)を有する容量4のオートクレーブ
を用い、この反応釜中に総量2Kgとなるように配
合した全ての原材料すなわち基油,けん化される
べき脂肪材料,けん化剤,けん化促進剤,多価ア
ルコール、および脂環式カルボン酸もしくはその
アルカリ土類金属塩を投入した。脂肪材料として
は中和価202,沃素価47.7の牛脂直分解脂肪酸
12.5重量%,けん化促進剤としては苛性ソーダ
(試薬1級)0.05重量%を使用した。けん化剤と
しては純度96.2重量%の消石灰を用い、その量は
けん化反応を行なつた後生成物中に遊離アルカリ
値(Ca(OH)2として)が0.05〜0.10重量%残存す
るように調節して投入した。このほかオートクレ
ーブを加圧するため上記原材料に対し水を5重量
%加えた。この後オートクレーブを密閉し、60分
間加熱撹拌して内容物温度135℃,圧力約2.2Kg/
cm3(ゲージ圧)に達した時点で、内容物を開放釜
に流出させた。開放釜は加熱型で複式撹拌羽根
(回転数は内羽根20rpm,外羽根15rpm)を有す
る容量5のものを用いた。内容物を開放釜に流
出後、温度100〜105℃で内容物の水分含有量が
0.8〜1.2重量%の範囲内となるように余分の水分
を蒸発させ、脱水した。水分調整後内容物を撹拌
しながら約30分で内容物温度を60℃まで徐冷した
後、開放釜より内容物を取り出し、室温まで放冷
して仕上げた。使用した基油,添加物(1)および添
加物(2)の種類、生成グリースの性状を第3表に示
す。[Table] The appearance of the produced grease was evaluated on the following five scales. 5... Appears to be similar in appearance to calcium-based grease manufactured using high-quality naphthenic base oil, and has no visible particles. 4... Items with an evaluation between 5 and 3 that are judged to fall under neither. 3... Particles with a diameter of 0.5m/m or less exist in a proportion of 50% or more of the total. 2... Those whose evaluation is between 3 and 1 and are judged to fall under neither. 1... Particles with a diameter of 1.0 m/m or more exist in a proportion of 50% or more of the total, or 24 days after sample preparation.
Items that show 1% by weight or more of oil separating over time. The hardness of the generated grease is 5.3 of JLS K2220-1980.
Evaluation was made using the mixing consistency value specified in Section 1. The smaller the value, the harder it is. Example 1 A heated autoclave with a capacity of 4 and equipped with a single stirring blade (rotation speed 15 rpm) was used as the saponification reaction vessel, and all raw materials, that is, base oil, which were blended in the reaction vessel in a total amount of 2 kg, were saponified. A saponifying agent, a saponifying accelerator, a polyhydric alcohol, and an alicyclic carboxylic acid or an alkaline earth metal salt thereof were added. The fat material is beef tallow directly decomposed fatty acids with a neutralization value of 202 and an iodine value of 47.7.
12.5% by weight, and 0.05% by weight of caustic soda (grade 1 reagent) was used as a saponification accelerator. Slaked lime with a purity of 96.2% by weight was used as the saponification agent, and the amount was adjusted so that the free alkali value (as Ca(OH) 2 ) remained in the product after the saponification reaction was 0.05 to 0.10% by weight. I put it in. In addition, 5% by weight of water was added to the above raw materials to pressurize the autoclave. After that, the autoclave was sealed and heated and stirred for 60 minutes to keep the contents at a temperature of 135°C and a pressure of about 2.2 kg/kg.
Once cm 3 (gauge pressure) was reached, the contents were drained into the open kettle. The open pot was of a heating type and had a capacity of 5 and had multiple stirring blades (inner blade 20 rpm, outer blade 15 rpm). After the contents are poured into an open pot, the moisture content of the contents is reduced at a temperature of 100 to 105℃.
Excess water was evaporated and dehydrated to a concentration of 0.8 to 1.2% by weight. After adjusting the moisture content, the contents were slowly cooled to 60°C over about 30 minutes while stirring, and then the contents were taken out from the open pot and left to cool to room temperature for finishing. Table 3 shows the base oil used, the types of additive (1) and additive (2), and the properties of the resulting grease.
【表】【table】
【表】
上記にみられるように、パラフイン系基油を使
用した場合、多価アルコールと脂環式カルボン酸
もしくはそのアルカリ土類金属塩とを併用するこ
とにより、これらの単独添加、あるいは無添加
(後の比較例参照。)では全く得ることの不可能で
あつた外観の良好な、しかも硬いカルシウム系グ
リースを得ることができた。生成グリースは外観
および硬さ以外の性状も正常であつた。
上表中多価アルコールの添加量は0.5重量%、
脂環式カルボン酸もしくはそのアルカリ土類金属
塩の添加量は2重量%で実験を行なつたが、さら
にこれら添加物の添加量を変えて実験を行なつた
ところ、多価アルコールの添加量は0.1〜2重量
%、脂環式カルボン酸もしくはそのアルカリ土類
金属塩0.1重量%以上で効果があり、この範囲外
では少ないと効果がなく、多すぎる脱水工程で発
泡現象を生じたり、稠度収率が悪くなるなど満足
なグリース化が行なえなかつた。多価アルコール
0.1〜1.5重量%,脂環式カルボン酸もしくはその
アルカリ土類金属塩0.5〜5重量%の添加範囲が
特に効果的で、多価アルコール1重量部に対し脂
環式カルボン酸もしくはそのアルカリ土類金属塩
2〜10重量部の添加割合で使用したときに最も効
果的であつた。
また上記実験番号6と同様にしてカルシウムナ
フテネート以外にマグネシウムナフテネート,バ
リウムナフテネートを添加して実験を行なつたと
ころ、いずれも良好なカルシウム系グリースが得
られたが、脂環式カルボン酸のアルカリ土類金属
塩としてはカルシウム塩が最も効果的であつた。
実施例 2
基油Cの代りに他の基油を用い、実施例1の実
験番号1〜6と同様にしてカルシウム系グリース
を製造した。その結果を第4表に示す。基油C以
外のパラフイン系炭化水素基油を用いても良好な
カルシウム系グリースが得られた。[Table] As shown above, when paraffinic base oil is used, polyhydric alcohols and alicyclic carboxylic acids or their alkaline earth metal salts can be used together, either alone or without their addition. It was possible to obtain a calcium-based grease with good appearance and hardness, which was completely impossible to obtain using the method (see Comparative Example below). The resulting grease had normal properties other than appearance and hardness. The amount of polyhydric alcohol added in the above table is 0.5% by weight.
Experiments were conducted with the amount of alicyclic carboxylic acid or its alkaline earth metal salt added at 2% by weight, but when the amount of these additives added was changed, the amount of polyhydric alcohol added was is effective at 0.1 to 2% by weight, alicyclic carboxylic acid or its alkaline earth metal salt at 0.1% by weight or more, and if the amount is less than this range, it is ineffective, and too much dehydration process may cause foaming or increase the consistency. Greasing could not be achieved satisfactorily due to poor yield. polyhydric alcohol
Addition ranges of 0.1 to 1.5% by weight and 0.5 to 5% by weight of alicyclic carboxylic acid or its alkaline earth metal salt are particularly effective. It was most effective when the metal salt was added in an amount of 2 to 10 parts by weight. In addition, in the same manner as in Experiment No. 6 above, an experiment was conducted in which magnesium naphthenate and barium naphthenate were added in addition to calcium naphthenate, and good calcium-based greases were obtained in both cases. Among the alkaline earth metal salts, calcium salts were the most effective. Example 2 Calcium-based grease was produced in the same manner as in Experiment Nos. 1 to 6 of Example 1, using another base oil instead of base oil C. The results are shown in Table 4. Even when a paraffinic hydrocarbon base oil other than base oil C was used, a good calcium-based grease was obtained.
【表】
比較例 1
多価アルコール,脂環式カルボン酸,そのアル
カリ土類金属塩を全く添加しない以外実施例1と
同様にしてカルシウム系グリースを製造した。結
果を第5表に示す。粘度指数20の良質のナフテン
系基油を使用した場合良好なカルシウム系グリー
スが得られたが、パラフイン系基油を使用した場
合満足なグリースは得られなかつた。[Table] Comparative Example 1 A calcium-based grease was produced in the same manner as in Example 1 except that no polyhydric alcohol, alicyclic carboxylic acid, or alkaline earth metal salt thereof was added. The results are shown in Table 5. When a high-quality naphthenic base oil with a viscosity index of 20 was used, a good calcium-based grease was obtained, but when a paraffinic base oil was used, a satisfactory grease could not be obtained.
【表】
比較例 2
脂環式カルボン酸、そのアルカリ土類金属塩を
添加しなかつた以外実施例1と同様にしてパラフ
イン系基油からカルシウム系グリースを製造し
た。結果を第6表に示す。多価アルコールのみを
添加した場合グリースとして製品化できるほどの
卓抜した効果は認められなかつた。[Table] Comparative Example 2 A calcium-based grease was produced from a paraffinic base oil in the same manner as in Example 1 except that an alicyclic carboxylic acid and its alkaline earth metal salt were not added. The results are shown in Table 6. When only polyhydric alcohol was added, no outstanding effect was observed to the extent that it could be commercialized as a grease.
【表】
(注) 添加剤(1);添加量1重量%。
また多価アルコールの添加量を変えた以外同様
にしてカルシウム系グリースを製造したが多価ア
ルコールの添加量を変えても満足なグリースは得
られなかつた。多価アルコールの添加量が2重量
%をこえると脱水工程で発泡を生じ、脱水操作が
困難となつた。
比較例 3
多価アルコールを添加しなかつた以外実施例1
と同様にしてパラフイン系基油からカルシウム系
グリースを製造した。結果を第7表に示す。脂環
式カルボン酸のみを添加した場合もやはりグリー
スとして製品化が可能なほどの改善効果は認めら
れなかつた。[Table] (Note) Additive (1); Addition amount: 1% by weight.
Calcium-based grease was produced in the same manner except that the amount of polyhydric alcohol added was changed, but a satisfactory grease could not be obtained even if the amount of polyhydric alcohol added was changed. When the amount of polyhydric alcohol added exceeds 2% by weight, foaming occurred during the dehydration process, making the dehydration operation difficult. Comparative Example 3 Example 1 except that polyhydric alcohol was not added
Calcium-based grease was produced from paraffinic base oil in the same manner as above. The results are shown in Table 7. Even when only the alicyclic carboxylic acid was added, no improvement effect was observed to the extent that it could be commercialized as a grease.
【表】
(注) 添加物(2);添加量1重量%。
また脂環式カルボン酸hの添加量を変えた以外
実験番号25と同様にしてカルシウム系グリースを
製造したところ、脂環式カルボン酸添加量を3重
量%と多くすることにより外観評価4のものが得
られたが混和稠度347と稠度収率が悪く、工業的
には実用性に乏しいものしか得られなかつた。他
の添加物e,f,g,iについても傾向は添加物
hと同じであつた。
比較例 4
多価アルコールを添加しなかつた以外実施例1
と同様にしてパラフイン系基油からカルシウム系
グリースを製造した。結果を第8表に示す。脂環
式カルボン酸のアルカリ土類金属塩のみを添加し
た場合もやはり満足なグリースは得られなかつ
た。[Table] (Note) Additive (2); Addition amount: 1% by weight.
In addition, calcium-based grease was manufactured in the same manner as in Experiment No. 25 except that the amount of alicyclic carboxylic acid h added was changed, and by increasing the amount of alicyclic carboxylic acid added to 3% by weight, the appearance rating was 4. was obtained, but the consistency yield was poor, with a mixing consistency of 347, and the product was of poor industrial practicality. The trend was the same for the other additives e, f, g, and i as for the additive h. Comparative Example 4 Example 1 except that polyhydric alcohol was not added
Calcium-based grease was produced from paraffinic base oil in the same manner as above. The results are shown in Table 8. Even when only an alkaline earth metal salt of an alicyclic carboxylic acid was added, a satisfactory grease could not be obtained.
【表】
(注) 添加物(2);添加量3重量%。
比較例 5
脂環式カルボン酸もしくはそのアルカリ土類金
属塩の代りに脂環式カルボン酸のアルカリ金属塩
を用いた以外実施例1と同様にしてパラフイン系
基油からカルシウム系グリースを製造した。結果
を第9表に示す。満足なグリースはやはり得られ
なかつた。[Table] (Note) Additive (2); Added amount: 3% by weight.
Comparative Example 5 A calcium-based grease was produced from a paraffinic base oil in the same manner as in Example 1 except that an alkali metal salt of an alicyclic carboxylic acid was used instead of the alicyclic carboxylic acid or its alkaline earth metal salt. The results are shown in Table 9. I still couldn't get a satisfactory amount of grease.
【表】
添加物(3);アルカリ金属ナフテ
ネートで、添加量は2.5重量%。
比較例 6
二価アルコールの代りに牛脂を用い、また牛脂
と牛脂直分解脂肪酸の合計使用量を13.0重量%と
した(牛脂はけん化されるとカルシウム石けん増
稠剤となる。)以外、実施例1と同様にしてパラ
フイン系基油からカルシウム系グリースを製造し
た。結果を第10表に示す。二価アルコールを使用
せず脂肪材料として油脂を使用した場合けん化反
応が困難であり、また脱水工程で発泡が生じて脱
水困難になるなどの問題があり、期待した効果は
得られなかつた。[Table] Additive (3); Alkali metal naphthene
The amount added is 2.5% by weight.
Comparative Example 6 Examples except that beef tallow was used instead of dihydric alcohol, and the total amount of beef tallow and tallow directly decomposed fatty acids was 13.0% by weight (beef tallow becomes a calcium soap thickener when it is saponified). Calcium-based grease was produced from paraffinic base oil in the same manner as in Example 1. The results are shown in Table 10. When fats and oils are used as the fatty material without using dihydric alcohol, there are problems such as the saponification reaction is difficult and foaming occurs during the dehydration process, making dehydration difficult, and the expected effects cannot be obtained.
【表】
(注) 添加物(2);添加量2重量%。
実施例 3
牛脂直分解脂肪酸の代りに12―ヒドロキシステ
アリン酸を使用した以外実施例1と同様にしてパ
ラフイン系基油からカルシウム系グリースを製造
した。実施例1で得られたとほぼ同等の良好なカ
ルシウム系グリースが得られた。[Table] (Note) Additive (2); Added amount 2% by weight.
Example 3 Calcium-based grease was produced from paraffinic base oil in the same manner as in Example 1, except that 12-hydroxystearic acid was used instead of beef tallow directly decomposed fatty acids. A good calcium-based grease almost equivalent to that obtained in Example 1 was obtained.
Claims (1)
〜2.0重量%の多価アルコールおよび少なくとも
0.1重量%の脂環式カルボン酸もしくはそのアル
カリ土類金属塩の存在下で、けん化されるべき脂
肪材料をカルシウムけん化剤によりけん化するこ
とを特徴とするカルシウム系グリースの製造方
法。1 In paraffin hydrocarbon base oil, 0.1
~2.0% by weight polyhydric alcohol and at least
A method for producing calcium-based grease, which comprises saponifying a fatty material to be saponified with a calcium saponifying agent in the presence of 0.1% by weight of an alicyclic carboxylic acid or an alkaline earth metal salt thereof.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10759880A JPS5731999A (en) | 1980-08-04 | 1980-08-04 | Preparation of grease |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10759880A JPS5731999A (en) | 1980-08-04 | 1980-08-04 | Preparation of grease |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5731999A JPS5731999A (en) | 1982-02-20 |
JPS6347760B2 true JPS6347760B2 (en) | 1988-09-26 |
Family
ID=14463218
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10759880A Granted JPS5731999A (en) | 1980-08-04 | 1980-08-04 | Preparation of grease |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5731999A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100441060B1 (en) * | 2002-07-24 | 2004-07-19 | 주식회사 윤 영 | A oil composite for inserting buffer bush of vehicle |
US7407920B2 (en) * | 2004-07-29 | 2008-08-05 | Crompton Corporation | Overbased calcium salicylate greases |
WO2007143454A2 (en) * | 2006-05-31 | 2007-12-13 | Shell Oil Company | Process and apparatus for preparing a soap concentrate, a lubricating composition, and combinations thereof |
JP6843289B6 (en) * | 2020-04-27 | 2021-04-14 | シェルルブリカンツジャパン株式会社 | Method for manufacturing grease composition and grease composition |
-
1980
- 1980-08-04 JP JP10759880A patent/JPS5731999A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS5731999A (en) | 1982-02-20 |
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