| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 81 | SOLID COMPOSITION COMPRISING SUGAR, MELON FIBRE, AND SOAP AND PROCESS FOR PREPARING | CA2874496 | 2013-06-27 | CA2874496C | 2020-05-05 | CONSTANTINE MARK; CONSTANTINE MARGARET JOAN; AMBROSEN HELEN ELIZABETH |
| The present invention provides a solid cosmetic composition comprising (i) sugar; (ii) a vegetable fibre, a fruit fibre or mixture thereof; and (iii) a soap; wherein the solid cosmetic composition is prepared by dehydrating a liquid composition comprising (i) sugar in an amount of 33.75 to 47 wt.%; (ii) a vegetable fibre, a fruit fibre or mixture thereof, in an amount of 3.75 to 4.75 wt.%; (iii) a soap in an amount of 20 to 75 wt.%; and (iv) water in an amount of 11 to 15 wt.%, wherein the amounts are based on the total combined amount of the sugar, the fibre, the soap and the water. | ||||||
| 82 | Composition | AU2013282957 | 2013-06-27 | AU2013282957A1 | 2015-01-15 | CONSTANTINE MARK; CONSTANTINE MARGARET JOAN; AMBROSEN HELEN ELIZABETH |
| The present invention provides a solid cosmetic composition comprising (i) sugar; (ii) a vegetable fibre, a fruit fibre or mixture thereof; and (iii) a soap; wherein the solid cosmetic composition is prepared by dehydrating a liquid composition comprising (i) sugar in an amount of 33.75 to 47 wt.%; (ii) a vegetable fibre, a fruit fibre or mixture thereof, in an amount of 3.75 to 4.75 wt.%; (iii) a soap in an amount of 20 to 75 wt.%; and (iv) water in an amount of 11 to 15 wt.%, wherein the amounts are based on the total combined amount of the sugar, the fibre, the soap and the water. | ||||||
| 83 | COMPOSITION | CA2874496 | 2013-06-27 | CA2874496A1 | 2014-01-03 | CONSTANTINE MARK; CONSTANTINE MARGARET JOAN; AMBROSEN HELEN ELIZABETH |
| The present invention provides a solid cosmetic composition comprising (i) sugar; (ii) a vegetable fibre, a fruit fibre or mixture thereof; and (iii) a soap; wherein the solid cosmetic composition is prepared by dehydrating a liquid composition comprising (i) sugar in an amount of 33.75 to 47 wt.%; (ii) a vegetable fibre, a fruit fibre or mixture thereof, in an amount of 3.75 to 4.75 wt.%; (iii) a soap in an amount of 20 to 75 wt.%; and (iv) water in an amount of 11 to 15 wt.%, wherein the amounts are based on the total combined amount of the sugar, the fibre, the soap and the water. | ||||||
| 84 | Solvent removal process | AU5477196 | 1996-06-05 | AU5477196A | 1996-12-19 | DUVALL LANNY R; BROOKS BURTON; JESSUP WALTER |
| 85 | MX9305352 | 1993-09-01 | MX9305352A | 1994-04-29 | DIJK PAUL VAN; VEGA JOSE LUIS; FRANCE PAUL AMAAT RAYMOND G | |
| 86 | PROCEDE DE RECYCLAGE D'HUILES ET GRAISSES USAGEES. | BE9100322 | 1991-04-08 | BE1004720A3 | 1993-01-19 | |
| Le procédé consiste à ajouter à des huiles ou graisses usagées chauffées de la soude caustique dissoute dans de l'eau, à porter l'ensemble à l'ébullition, à laisser prendre en masse et à laver cette masse ou savon avec électrolyte, tel que du NaCl. Le séchage de masses ou savons lavés est réalisés par un passage au four à micro-ondes. | ||||||
| 87 | GRANULES FOR DETERGENT COMPOSITION | CA2040050 | 1991-04-09 | CA2040050A1 | 1991-10-13 | GOODMAN HOWARD; LYMATH GARY A; STOCKLEY DAVID J |
| A PROCESS FOR PREPARING GRANULES FOR DETERGENT COMPOSITIONS There is disclosed a process for preparing granules for incorporation into a detergent composition, which process comprises the steps of (a) tumbling together in a rotating pan a finely divided particulate smectite clay and a finely divided particulate zeolite in a weight ratio of from 1:9 to 9:1 whilst sufficient water is added slowly to the resultant mixture to bind the particles together to form granules of a mixture of said smectite clay and said zeolite; and (b) drying the resultant granules to reduce the water content to not more than 20% of the total weight of the granules. Also disclosed is a detergent composition including said granules. | ||||||
| 88 | BR8901588 | 1989-03-30 | BR8901588A | 1990-10-30 | SILVEIRA JOSE ROCHA DA | |
| 89 | DD22244280 | 1980-07-07 | DD151960B1 | 1989-04-12 | BERTHOLD HORST; SCHAEFER ANTON; SCHOLZ JOACHIM; SEDLAK HERBERT; WINTER HARALD | |
| 90 | PREPARATION OF SOLUTIONS OF METAL SOAPS IN AMINES | AU1488488 | 1988-02-16 | AU1488488A | 1988-10-10 | NELSON EDGAR N; SCULLY DANIEL F |
| 91 | METHOD OF AND DEVICE FOR THE EVAPORATIVE DRYING OF A COLLOIDAL ORGANIC MIXTURE OF SOLID MATTER AND WATER | DE3460252 | 1984-02-24 | DE3460252D1 | 1986-07-31 | TILS KARL DR ING |
| 92 | ES539823 | 1985-01-24 | ES539823A0 | 1985-11-16 | ||
| 93 | DD22244280 | 1980-07-07 | DD151960A1 | 1981-11-11 | BERTHOLD HORST; SCHAEFER ANTON; SCHOLZ JOACHIM; SEDLAK HERBERT; WINTER HARALD | |
| 94 | FR2209834B3 - | FR7343784 | 1973-12-07 | FR2209834B3 | 1976-10-15 | |
| 95 | IT7062773 | 1973-12-07 | IT999943B | 1976-03-10 | SCHEEN J | |
| 96 | POTASH SOAP | GB606272 | 1972-02-09 | GB1407985A | 1975-10-01 | |
| 1407985 Granular potassium soaps PROCTER & GAMBLE Ltd 8 Feb 1973 [9 Feb 1972] 6062/72 Heading C5D Granular free-blowing potassium or mixed sodium-potassium soaps having 16-24 carbon atoms and, in the case of the mixed soaps, having the molar ratio of sodium to potassium of not more than 1 : 2, are prepared by spraydrying an aqueous mixture of the soaps, together with 1 to 15% of free fatty acid based on the weight of the total fatty acid present and not more than 45% by wt. of said mixture of water. The fatty acids contain less than 1 % by wt. of unsaturated fatty acids having 3 or more double bonds in the molecule and are usually derived from hardened fats such as hardened tallow (iodine value 37) or hardened marine oil. Optional ingredients are (a) up to 6% wt. of sodium or potassium chloride and (b) up to 2% (as SiO 2 ) of sodium or potassium silicate. Spray cooling or "flash drying" processes may be used. Preferably, the soap mixture is heated to 100 to 250 C., usually 140-200 C., under sufficient pressure to prevent boiling and is allowed to expand through nozzles in a spraydrying tower in an air stream heated to 140 C. (flash drying). The granules contain 5 to 10% moisture. | ||||||
| 97 | AR25134373 | 1973-12-04 | AR200587A1 | 1974-11-22 | ||
| 98 | Toilet soap - prepd from tallow and coconut oil mixt,with heating before or after extrusion | FR7243657 | 1972-12-07 | FR2162564A1 | 1973-07-20 | |
| Toilet soap bar or cake, produced from a fat mixt. of 50-90% tallow and 50-10% coconut oil and contg. 20 (10-15) % water and pref. 5% fatty acid, is heated to 70-90 degrees C, before or after extrusion, to reduce tendency to pap up and rate of wear, without affecting foaming activity. | ||||||
| 99 | NL7216570A - | NL7216570 | 1972-12-06 | NL7216570A | 1973-06-13 | |
| 100 | GB1238485A - | GB1238485D | 1968-04-23 | GB1238485A | 1971-07-07 | |
| 1,238,485. Drying detergent materials. UNILEVER Ltd. 23 July, 1969 [23 April, 1968], No. 19241/68. Heading C5D. A moist mass of detergent material, e.g. soap, is dried by passing the mass through a heat exchanger under pressure, the process being characterized in that steam is injected and intimately mixed into the mass prior to its entry into the heat exchanger, the amount of steam injected being sufficient to raise the temperature of the mass to its boiling point at the elevated pressure in the heat exchanger but insufficient to produce a two-phase heterogeneous mixture of steam and heated detergent. The steam is preferably saturated. Mixing may be by mechanical in-line steam mixer, a dynamic steam mixer located axially or a static mixer. The detergent may also be superfatted soap or a non-soap detergent such as an olefin sulphonate, or a mixture thereof. Specification 1,018,764 is referred to. | ||||||
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