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序号	专利名	申请号	申请日	公开（公告）号	公开（公告）日	发明人
101	Soap drying process	GB5066163	1963-12-23	GB1018764A	1966-02-02	WARD NORMAN ERNEST
In a process for partially drying liquid soap in a plate type heat exchange having unrestricted outlet, steam is injected into the liquid soap prior to its introduction into the heat exchanger. This reduces the pressure drop across the heat exchanger by reducing blocking of the heat exchanger caused by solidified soap. The amount of steam, which may be superheated, saturated or wet, is preferably just sufficient to heat the soap to its boiling point at the pressure obtaining at the inlet of the heat exchanger. The liquid soap is suitably one containing 27-33 wt. per cent water, and may also contain free fatty acid, e.g. 2-12 wt. per cent.
102	Arrangement for the crystallisation, cooling and drying of fluid or paste-like material, particularly soaps, in a vacuum	GB3221256	1956-10-23	GB799927A	1958-08-13
Apparatus for the drying, cooling and crystallization of paste-like material, especially soap, in a vacuum comprises a container 1 within which a planetary roller 3 travels over the inner surface of a cylinder 2 and spreads the paste as a thin film on the cylinder and the roller. The roller is mounted in bearing arms carried by a shaft 4, which is driven from outside the container, so that the roller revolves around the shaft. A drive 7, taken from the shaft, causes the roller to turn about its own axis 5. Shaft 4 is hollow and serves, together with distributer 8, which is constructed with double walls so that it may be filled with hot or cold media according to requirements. Also, the hollow shaft 4 can be adapted for the conveyance of heating or cooling medium to roller 3. The liquid evaporates from the paste, and the vapours leave the container through suction pipe 10. The dried material is shaved off the roller and the cylinder by knives 9, and is withdrawn through outlet 11, which may be mounted on an extrusion press. In an alternative embodiment, the cylinder 2 is formed by the wall of the vacuum container itself.
103	Device for the crystallization, cooling and vacuum drying of liquid or pasty substances, in particular soaps	FR1158330D	1956-10-10	FR1158330A	1958-06-13

104	Drying machine for the production of sheet soap	GB1933154	1954-07-01	GB752517A	1956-07-11	VETTORELLO RODOLFO
A drying machine for the continuous production of sheet soap comprises a standard supporting a reel of paper to be coated with soap, a soap bath, a standard for the driving and winding mechanism for the finished sheet, and a tunnel type drier through which the coated sheet passes and which is heated by electric resistances and within which, by means of blowers, air streams are caused to flow to ensure drying of the sheet. As shown, the reel of paper 2 is freely supported on a standard 1 adjacent to the soap bath 3, which is provided with a cylinder 4, journalled on a bearing 5 and dipping in the bath, around which the paper sheet N passes as it is unwound from the reel 2. At the outlet of the bath, the sheet passes between rollers 6, 7 which are adjusted to control the thickness of the soap layers. The tunnel type drier is horizontal and is divided into two sections, 8, 9, maintained at different temperatures, through which the sheet N travels unsupported. The dried sheet leaves the tunnel and passes round an idling roller 10 to a winding-up cylinder 12 driven by a motor 13, the rollers 10 and 12 and the motor 13 being supported by another standard 14. The tunnel drier is preferably double-walled and heat insulated. Along the inner horizontal walls of the tunnel electric resistance units are arranged and are supplied with current to provide a preferred temperature of 100-120 DEG C. in the section 8 and a temperature of 200-220 DEG C in the section 9. A wire safety net may be positioned above the bottom heaters. Two air streams generated by blowers 20, 21 are admitted through ducts 18, 19 to the tunnel so as to skim both sides of the sheet N and assist in its drying. The warm air flows to the inlet end of the tunnel and is returned through a duct branching into two ducts to the blowers 20, 21 to form a closed circuit. At a certain humidity the air may be discharged through a stack 25 controlled by a gate 26. A third blower 27 for cooling the sheet may be provided.
105	Improved spraying means for drying, granulating, crystallizing and solidifying slurries or solutions, particularly of soaps, detergents and the like	GB2689352	1952-10-27	GB748647A	1956-05-09
A substantially cylindrical spray drying chamber 11 has its upper part in the form of a truncated cone and is provided, within this upper part, with a hood 10 having its walls parallel to the conical walls of the chamber; inside this hood is mounted a nozzle 9 through which the solution to be treated is sprayed into the chamber by means of a pump; just below the hood are mounted a plurality of nozzles 8 through which the solution is sprayed by means of compressed air; and ducts are provided for introducing the treating gas into the hood and into the top of the chamber. The apparatus may be used for drying, granulating, crystallizing and cooling solutions or slurries of industtrial products. The spray drying of soaps or synthetic detergents to produce hollow particles is referred to. The solution or slurry to be dried is blended in mixers 1, and is then pumped through filter 3 to nozzle 9, through which it is sprayed by the pressure of pump 4. The solution or slurry is also sprayed through nozzles 8 by means of compressed air from compressor 16; this air being preheated if desired in preheater 29. Hot gases are withdrawn from furnace 5 by fans 6 and 7, mixed with a regulated amount of cold air, and introduced into hood 10; temperature-controlled gas may also be introduced into the upper zone 26, middle zone 22, or lower zone of the chamber. These three zones discharge to cyclone separator 17 which is connected to fans 6 and 7 via fan 20 and refrigerator 21. Separator 17 is also connected with the vertex of cone 12, Iocated in the conical base of the drying chamber. Cold air enters the base of the chamber through openings 27, and causes cooling of the dried particles and separation of the fines. The granulated product is discharged through duct 25, while the fines are carried by the gas to separator 17. A perfuming set 14 is connected to the discharge duct 25.
106	Method and apparatus for drying, vacuum concentration and distillation products of all kinds	FR60465D	1950-07-24	FR60465E	1954-11-03

107	Apparatus and process for drying soap	GB1950244	1944-10-10	GB595194A	1947-11-28
595,194. Drying soap. JERGENS, A. N. Oct. 10, 1944, No. 19502. [Class 34 (ii)] [Also in Group XI] A semi-plastic mass of soap is dried by passing it, preferably in sheet form, through a dielectric heating zone or drying chamber 11, the plasticising liquids evaporated from the soap during this heating being removed from the opposed surfaces thereof by, for example, a continuous air current flowing in a direction counter to that of the said soap. In the specific apparatus shown the drying chamber comprises a number of aligned sections 53 through which the soap is conveyed on an endless belt 13 from a feed hopper 30 and associated pair of sheet-forming chill rolls 15, 16 at one end 10 to a delivery hopper 14 at the other end 12. The belt 13 is preferably a screen of electrically conducting material, spaced between endless side chains passing around pairs of end sprockets 44, 45 rotatably mounted in electrically insulated bearings on the frame 17 of the apparatus, and forms one heating electrode, the other electrode of opposite polarity being constituted by a number of conducting screens 64, one in each chamber section 53, stationarily mounted in spaced relation to the belt 13. Power is supplied to the electrodes 64 from a supply line 76 through a high frequency generator 68, the output terminals of the latter being connected, one by a lead 69 to an arm contacting a pick-up disc 71 on the end of the shaft of the sprockets 44 and the other by a lead 72 and branches 73 direct to the screens 64. The air current is circulated through the drying chamber by a fan 77 having an outlet 78 connected by conduits 79, 80 with the mid and delivery portions of the chamber and an inlet 86 in communication with said chamber, as shown, through air filters 81, 82, a conduit 83 with valve 89, a dehumidifier 84, and conduit 85. A by-pass 88 with valve 90 is provided between the conduits 83, 85, the valve 90 and the valve 89 in the conduit 83 serving to permit control of the humidity of the circulating air.
108	Improvements to methods and devices for dry, concentrate and crystallize	FR920502D	1942-08-01	FR920502A	1947-04-10

109	Improvements in and relating to the drying of soap and the manufacture of soap powder, flakes or the like	GB248944	1945-11-30	GB581203A	1946-10-04
Moisture is removed from liquid soap, which has been preformed, which is free of glycerine or fillers, and which contains about 70 per cent. of soap and about 30 per cent. of water, by spraying the liquid soap into a chamber maintained under such conditions of temperature and high vacuum that the temperature of the soap falls below its solidifying point immediately on entering the chamber, the dried or partially dried soap deposited from the spray being agitated. The liquid soap may be continuously sprayed into the chamber and the soap deposited from the spray continuously removed from the chamber, or alternatively a batch of liquid soap may be sprayed into the chamber, the water extracted being collected and the soap deposited from the spray being removed from the chamber only when the desired amount of water has been extracted. The heat necessary for the process may be provided by superheating the liquid soap prior to its entry to the chamber or by heating the chamber by means of a steam jacket or by means of a heating coil within the chamber, or by a combination of these means. The alkalinity of the product may be controlled by introducing into the liquid soap spray nozzle supply conduit, or into the chamber direct, during the process, carbon dioxide or a fatty acid. If the temperatures employed and degree of vacuum used is sufficient to deprive the liquid soap of all but about 5 per cent. of the moisture, a soap powder may be produced within the chamber, while if the process is carried out to leave larger proportions of moisture in the product a plastic solid may be produced. The plastic solid may leave the apparatus through an outlet provided with a die plate so that the soap is extruded in ribbon or bar form, and the ribbon can then be disintegrated into flakes or chips. In the drawing liquid soap is sprayed through nozzles e1 into a chamber f provided with an outlet conduit h through which water vapours and gases may be drawn away by steam ejectors or any suitable vacuum or pressure-reducing pump and with a helical agitating blade k mounted to revolve on a horizontal axis.
110	Apparatus for producing soaps from strangfoermigen halbfluessiger plastischerSeife or substances similar physical property	DES0116568	1934-12-22	DE657629C	1938-03-12

111	improved process for drying of various materials and transportutilisé mechanism for this purpose	FR783055D	1934-12-20	FR783055A	1935-07-08

112	Process and apparatus for drying and conditioning household soap	GB3088028	1928-10-25	GB325807A	1930-02-25
325,807. Tomlinsons (Rochdale), Ltd., and Tomlinson, J. N. Oct. 25, 1928. Soap tablets, blocks, bars, &c.- Bars of soap are carried by horizontal endless band conveyers a successively through a number of heating or drymg zones and a number of cooling or conditioning zones, the air which circulates in the first cooling zone being passed wholly or partly into the last heating zone. Air for the heating zones 1, 2 is drawn by fans e from the cooling zone 3 and is discharged by fans d, the air passing downwardly through the conveyers in zone 2 and upwardly in zone 1. Heaters are provided in side compartments in zones 1 and 2, the arrangement of heaters and fans being of the kind described in Specifications 173,234, 228,025, and 246,655, [all in Class 34 (ii), Drying systems &c.]. Cool air is drawn into zones 3, 4, 5 through side inlets f, g, h and is circulated and discharged through central outlets f<2>, g<2>, h<2> by fans f<1>, g<1>, h<1>, the air passing downwardly through the conveyers in zone 3 and upwardly in zones 4, 5.
113	Process for drying soaps or other substances in belt dryers, are in which the tapes moves at different speeds	DEST041858	1926-11-30	DE459102C	1928-04-25

114	Improvements in machines for making soap	FR597178D	1925-04-23	FR597178A	1925-11-14

115	A method for producing a gelatinous, dry Oberflaechenschicht on Seifenstuecken	DEY0000432	1920-04-02	DE394863C	1924-05-06

116	Improvements to soap driers	FR546099D	1922-01-19	FR546099A	1922-10-27

117	Quick drying and drying system with vacuum and a closed long pasta or cut	FR5493D		FR5493E	1906-04-24	BARTHELEMY DE CONSTANS ET

118	Nouvelle tablette détergente enrobée	FR2114279	2021-12-22	FR3130839B1	2023-12-01	ESPEIT JEAN-LOUIS; BROSSE JACQUES; OFRIDAM FABRICE
La présente divulgation concerne le domaine des tablettes pour l’entretien ménager et des tissus, notamment des tablettes détergentes. L’invention se rapporte en particulier à une tablette enrobée par une solution respectueuse de l’environnement à base d’un mélange de polymères d’origine naturelle qui permet d’éviter que les tablettes ne se fracturent ou ne s’écaillent au cours de leur fabrication, de leur transport et de leur utilisation.
119	Composición	ES13733438	2013-06-27	ES2706752T3	2019-04-01	CONSTANTINE MARK; CONSTANTINE MARGARET JOAN; AMBROSEN HELEN ELIZABETH
Una composición cosmética sólida que comprende: (i) azúcar; (ii) fibra de melón; y (iii) un jabón, en la que la composición cosmética sólida se prepara deshidratando una composición líquida que comprende: (a) melón; y (b) un jabón, en la que la fibra de melón es una fibra dietética insoluble.
120	Process for preparing a solid cosmetic composition	GB201211531	2012-06-29	GB2503492B	2018-10-17	MARK CONSTANTINE; MARGARET JOAN CONSTANTINE; HELEN AMBROSEN

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