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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
181	Method of drying toilet soap compositions	GB3176064	1964-08-05	GB1063715A	1967-03-30
Liquid toilet soap compositions are dried by a process comprising heating the liquid soap to above the boiling temperature of water while being stirred, passing it along the bores of upwardly extending tubes of a vaporizing drier, then to a separating vessel from the top of which steam is drawn off, and then passing the soap to another, preferably similar, dryer and separator. A plant suitable for carrying out the process is described in detail.
182	A continuous process for gradual drying under vacuum and simultaneously refining of soap	DEM0031128	1956-07-17	DE1109305B	1961-06-22	MAZZONI CARLO; MAZZONI GIUSEPPE

183	Apparatus for crystallization, cooling and drying of liquid or pasty products, especially soap, vacuum	DEK0027240	1955-11-02	DE1021830B	1958-01-02

184	SOAP COMPOSITION	IE51855	1955-09-14	IE21988L	1956-03-15

185	Room or spray tower and in particular equipment for drying, granulation, crystallization and cooling solutions or mixtures in industrial products, in particular detergents or the like	FR1073973D	1952-10-23	FR1073973A	1954-09-30

186	Procedimento per la fabbricazione di pezzi di sapone e impianto per la realizzazione di questo procedimento.	CH276721D	1951-01-04	CH276721A	1951-07-31	GIUSEPPE MAZZONI

187	Process and apparatus for drying, cooling and deodorising soap	GB2783746	1946-09-17	GB640908A	1950-08-02
Soap is dried, cooled and deodorized by spraying hot soap paste into a chamber maintained under vacuum, maintaining relative movement between the spray and a surface which receives the spray, and scraping the receiving surface to remove the soap deposited thereon. Soap paste is sucked from saponification boiler 1 (see Fig. 1) through filter-box 2 by pump 3, and is then passed through preheater 7 where it may be heated to a temperature higher than 100 DEG C. The hot paste is fed to evaporator 4, which is maintained under vacuum by column 5 and pump 6, through nozzles P which are carried on a rotating shaft. violent vaporization of water takes place from the paste, and fine soap powder is thrown against the wall of the evaporator to form a film. The wall has a jacket 8 through which a warm fluid is circulated. Dry soap is removed from the wall by scrapers R (Fig. 2) which rotate together with nozzles P, and is withdrawn as powder from the base of the evaporator. In the modification shown in Fig. 6, stationary nozzles 22 spray paste onto three rotating cylinders 241. The base of the evaporator may be fitted with a conveyer, and if desired, with a device for extruding the soap in the form of little cylinders. If a not-too-dry product is required, the preheater is out out, and the receiving surface is cooled.
188	Improvements in or relating to apparatus for drying or crystallisation by spraying	GB3659246	1946-12-11	GB628758A	1949-09-05
Apparatus for drying or crystallizing comprises a chamber having at its lower part a gas inlet in its upper part a gas outlet, and therebetween a centrifugal sprayer for the material to be treated, characterized in that the vertical position of the sprayer can be adjusted throughout the whole distance between the gas inlet and outlet. The dried or crystalline product collects at the bottom of the chamber. The cylindrical chamber 1, which has a height equal to its diameter, is provided with one or more tangential air inlets 9 and an outlet 10 surrounded by a flange 12. Mounted coaxially within the chamber is rotary sprayer 2 which is adjusted in height by screw-jack 8 so that the time of fall of the larger particles to the level of inlet 9 equals the time of rise of the smaller particles to the level of the air outlet. The height of the inlet orifices may be regulated by means of obturators, and that of the outlet orifice by vertically displacing flange 12 relative to chamber 1. The drying of milk, blood, and egg-white is referred to.
189	Method and apparatus for drying, vacuum concentration and distillation products of all kinds	FR922381D	1946-02-14	FR922381A	1947-06-06

190	Verfahren zur Überführung flüssiger Stoffe in Pulverform.	CH245661D	1942-08-01	CH245661A	1946-11-30	NIRO ATOMIZER AKTIESELSKABET

191	A process for the manufacture of soaps and soap-containing substances	DEI0041236	1931-04-12	DE635091C	1936-09-10

192	An improved method of drying material and a conveyor mechanism used in connection with same	GB3450234	1934-11-30	GB448123A	1936-06-02
448,123. Drying extruded material. SWIFT & CO., Union Stock Yards, Chicago, U.S.A.-(Assignees of Walter, C. T.) Nov. 30, 1934, No. 34502. Convention date, Dec. 21, 1933. [Class 34 (ii)] [See also Groups V, XXIV, and XXX] A method of laying out extruded material to be dried consists in laying out simultaneously a transverse series of string-like lengths of the material, each in a zigzag path on a moving conveyer substantially lengthwise thereof. In the construction shown in Figs. 1 and 3, a carriage 1, adapted to be reciprocated on racks 3, is provided with extrusion dies 12 which receive soap in plastic form pumped through pipes connected by unversal joints and communicating with a source of supply of soap. The carriage is connected by a link 31 and a swivel joint 32 to an endless chain 28 which is driven by an electric motor, and travels at a faster rate than that of an endless conveyer 10. Spring buffers 29, 30 absorb the energy of the carriage during its reversal of direction. The rails 3 are given lateral movement on rails 8 by means of cams 39, 40, which are driven by a motor 36 and are connected to rigid members 41, 42. The soap extruded from the dies 12 falls on the conveyer 10 in zigzag strings or tubes 26, as shown in' Fig. 2. The link 31 as shown in Fig. 9 comprises two enclosed coil springs 102, 105 bearing against collars between which is a slidable piston 100, the spring 102 resisting tension and the spring 105 resisting compression. In the construction shown in Fig. 4, the rail assembly for the carriage 1 has no independent lateral movement, but is inclined slightly in the direction of motion of the conveyer belt so that the strings of soap are laid on the conveyer 10 in the form shown in Fig. 5. An extrusion die is shown in Fig. 7. Plastic soap enters under pressure through a pipe 53 and passes to an outlet 63 through a conical passage 64 formed by a detachable plate 56 and a spindle 45. The spindle is driven by gearing in a chamber 71 containing oil 75, which is prevented by a shield 85 from entering a hole 65 extending the length of the spindle. Air under pressure enters the chamber 71 through a pipe 76 and as it passes out through the hole 65 assists in the extrusion of soap in tubular form.
193	Drying apparatus for soap	DES0078678	1927-03-06	DE483339C	1929-09-28

194	Installation with self-croûteur dryer for the continuous manufacture of soaps and household	FR640132D	1927-02-08	FR640132A	1928-07-06

195	Drying plant for soap mass with an endless conveyor belt of individual plates	DEL0061415	1924-10-14	DE448575C	1927-08-22	WIEMER KURT

196	A method of drying soap	DER0065623	1925-10-08	DE438347C	1926-12-15

197	Apparatus for drying soap masses	DER0060717		DE409129C	1925-01-31

198	Drying means for Seifenstuecke	DEY0000431		DE367158C	1923-01-18

199	Quick drying and drying system with vacuum and a closed long pasta or cut	FR354805D	1905-05-13	FR354805A	1905-10-14

200		SE9152D		SE9152C1	1898-08-06

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