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61. 发明专利

AT21205T 未知
公开(公告)号：AT21205T
公开(公告)日：1986-08-15
申请号：AT82903230
申请日：1982-11-10
申请人： ALPEN DAIRY FOODS
发明人： KILROY STANLEY ALAN ROBERT
IPC分类号： A23C15/12 , A23C15/02 , A23C15/04 , A23C15/16 , A23D7/00 , A23D7/005 , A23D7/02 , A23D5/02 , A23D3/02

62. 发明专利

DE2108750A1 未知
公开(公告)号：DE2108750A1
公开(公告)日：1971-09-16
申请号：DE2108750
申请日：1971-02-24
IPC分类号： A23C15/04 , A23C15/02

63. 发明专利

DE1417445A1 未知
公开(公告)号：DE1417445A1
公开(公告)日：1970-04-23
申请号：DE1417445
申请日：1958-08-28
申请人： UTA PATENTVERWALTUNG GMBH
发明人： PETER HUSSMANN DR
IPC分类号： A23B5/02 , A23C1/04 , A23C15/04 , A23C15/14 , A23C19/086 , A23D7/00 , A23D9/00 , A23D9/05 , A23F3/28 , A23F5/34 , A23L2/08 , A23L2/10 , A23L3/46 , A23L3/50 , B01D1/14 , B01D1/18 , B01D53/26 , F24F3/14 , F26B3/092 , F26B3/12 , F26B21/08
摘要： 953,185. Spray evaporators ; drying air; revivifying silica gel. BIRS BRIT A.G. July 28, 1960 [Aug. 10, 1959], No. 26363/60. Addition to 886,533. Headings B1B and B1L. In the spray-evaporation of liquids according to the parent Specification the air supplied to the evaporator-tower is filtered atmospheric air which has been dried by passing it through two beds of silica gel I, II, the air being cooled between these two adsorption stages by contacting it with masses of concrete or porcelain in heat-regenerator 3. At the same time, the bed of silica gel III, which has been exhausted in a previous cycle, is regenerated by another current of air. This second current is heated in heat-regenerators 4 and 2, these heat-regenerators having been heated, e.g. to 80-100 C., in a previous cycle ; and the air is then raised to about 160 C. in heat-exchanger W 1 before being introduced into adsorption bed III. The air leaving adsorption bed III is used to heat regenerator 1 before it is discharged from the system. The adsorption beds are regenerated in turn ; and the regenerators are alternately heated and cooled in two groups. If desired, the stream of fresh air leaving adsorption bed II may be passed through a fifth heat-regenerator 5 and a heat-exchanger W 2 before being introduced into the evaporator-tower. The regenerator 5 may be successively heated and cooled by using it as a heat exchanger for both air streams alternately within a particular cycle.

64. 发明专利

DE1417444A1 未知
公开(公告)号：DE1417444A1
公开(公告)日：1969-11-06
申请号：DE1417444
申请日：1958-05-12
申请人： UTA PATENTVERWALTUNG GMBH
发明人： PETER HUSSMANN DR
IPC分类号： A23B5/02 , A23C1/04 , A23C15/04 , A23C15/14 , A23C19/086 , A23D7/00 , A23D9/00 , A23D9/05 , A23F3/28 , A23F5/34 , A23L2/08 , A23L2/10 , A23L3/46 , A23L3/50 , B01D1/14 , B01D1/18 , B01D53/26 , F24F3/14 , F26B3/092 , F26B3/12 , F26B21/08
摘要： 953,185. Spray evaporators ; drying air; revivifying silica gel. BIRS BRIT A.G. July 28, 1960 [Aug. 10, 1959], No. 26363/60. Addition to 886,533. Headings B1B and B1L. In the spray-evaporation of liquids according to the parent Specification the air supplied to the evaporator-tower is filtered atmospheric air which has been dried by passing it through two beds of silica gel I, II, the air being cooled between these two adsorption stages by contacting it with masses of concrete or porcelain in heat-regenerator 3. At the same time, the bed of silica gel III, which has been exhausted in a previous cycle, is regenerated by another current of air. This second current is heated in heat-regenerators 4 and 2, these heat-regenerators having been heated, e.g. to 80-100 C., in a previous cycle ; and the air is then raised to about 160 C. in heat-exchanger W 1 before being introduced into adsorption bed III. The air leaving adsorption bed III is used to heat regenerator 1 before it is discharged from the system. The adsorption beds are regenerated in turn ; and the regenerators are alternately heated and cooled in two groups. If desired, the stream of fresh air leaving adsorption bed II may be passed through a fifth heat-regenerator 5 and a heat-exchanger W 2 before being introduced into the evaporator-tower. The regenerator 5 may be successively heated and cooled by using it as a heat exchanger for both air streams alternately within a particular cycle.

65. 发明专利

OA1351A 未知
公开(公告)号：OA1351A
公开(公告)日：1969-02-15
申请号：OA50596
申请日：1964-11-14
申请人： BIRS BETEILIGUNGS UND VERMAL T
IPC分类号： A23B5/02 , A23C1/04 , A23C15/04 , A23C15/14 , A23C19/086 , A23D7/00 , A23D9/00 , A23D9/05 , A23F3/28 , A23F5/34 , A23L2/08 , A23L2/10 , A23L3/46 , A23L3/50 , B01D1/14 , B01D1/18 , B01D53/26 , F24F3/14 , F26B3/092 , F26B3/12 , F26B21/08 , A23D5/02 , A23P1/00
CPC分类号： A23B5/022 , A23C1/04 , A23C15/04 , A23C15/14 , A23C19/086 , A23D7/003 , A23D9/00 , A23D9/05 , A23F3/28 , A23F5/34 , A23L2/08 , A23L2/10 , A23L3/46 , A23L3/50 , B01D1/14 , B01D1/18 , B01D53/26 , F24F3/1411 , F24F2003/1458 , F26B3/0926 , F26B3/12 , F26B21/083 , Y02P60/853 , Y02P70/34 , Y02P70/40

66. 发明专利

NL107423C 未知
公开(公告)号：NL107423C
公开(公告)日：1964-02-17
申请号：NL227836
申请日：1958-05-16
IPC分类号： A23B5/02 , A23C1/04 , A23C15/04 , A23C15/14 , A23C19/086 , A23D7/00 , A23D9/00 , A23D9/05 , A23F3/28 , A23F5/34 , A23L2/08 , A23L2/10 , A23L3/46 , A23L3/50 , B01D1/14 , B01D1/18 , B01D53/26 , F24F3/14 , F26B3/092 , F26B3/12 , F26B21/08
摘要： 953,185. Spray evaporators ; drying air; revivifying silica gel. BIRS BRIT A.G. July 28, 1960 [Aug. 10, 1959], No. 26363/60. Addition to 886,533. Headings B1B and B1L. In the spray-evaporation of liquids according to the parent Specification the air supplied to the evaporator-tower is filtered atmospheric air which has been dried by passing it through two beds of silica gel I, II, the air being cooled between these two adsorption stages by contacting it with masses of concrete or porcelain in heat-regenerator 3. At the same time, the bed of silica gel III, which has been exhausted in a previous cycle, is regenerated by another current of air. This second current is heated in heat-regenerators 4 and 2, these heat-regenerators having been heated, e.g. to 80-100 C., in a previous cycle ; and the air is then raised to about 160 C. in heat-exchanger W 1 before being introduced into adsorption bed III. The air leaving adsorption bed III is used to heat regenerator 1 before it is discharged from the system. The adsorption beds are regenerated in turn ; and the regenerators are alternately heated and cooled in two groups. If desired, the stream of fresh air leaving adsorption bed II may be passed through a fifth heat-regenerator 5 and a heat-exchanger W 2 before being introduced into the evaporator-tower. The regenerator 5 may be successively heated and cooled by using it as a heat exchanger for both air streams alternately within a particular cycle.

67. 发明专利

GB637792A Improvements in a process of treating cream 未知
公开(公告)号：GB637792A
公开(公告)日：1950-05-24
申请号：GB2430046
申请日：1946-08-15
申请人： CREAMERY PACKAGE MFG CO
IPC分类号： A23C15/02 , A23C15/04
摘要： 637,792. Butter ; dehydrated butter oil. THORNTON, A. A. (Creamery Package Mfg. Co.). Aug. 15, 1946, No. 24300. [Class 84] [Also in Groups II and XIII] Butter or dehydrated butter oil is obtained by heating cream to a temperature at which the milk fat is substantially liquified and the cream then separated to produce a portion having a fat content in excess of its serum content, such portion then having passed through a homogenizing machine for the purpose of breaking the envelopes of substantially all of the fat globules to release the liquified fat to form a continuous phase in which the serum is disposed in droplets, thus producing a mixture in which the components are in unstable readily separable relation. Preferably the heated cream after pasteurization is separated to 75 to 80 per cent fat in centrifuge 6 (Fig. 1) and then lead continuously to homogenizing machine 11 of the pressure valve type, which causes an inversion of phases resulting in the fat globules uniting in continuous liquid form. Alternatively a colloid mill of the revolving disc type may be used. The fat in serum mixture then passes to serum separator 49 in which the serum sinks immediately to the bottom from which it is withdrawn via pipe 64. This serum may be returned to the initially heated cream. The supernatant layer of about 98 per cent fat is removed via pipe 63 and may be dehydrated to produce a butter oil with only 0.05 per cent of moisture either by centrifugal action of by spraying into a vessel at 78‹ C. under a vacuum of 68.3 centimetres of mercury. Alternatively, the 98 per cent fat material is forced through composition control pump 116 by means of which salt and serum are blended in calculated quantities from supply reservoir 161 to produce a butter of desired composition (see Group II). It then passes through chiller 217 (see Group XIII) where the butter is cooled to 7‹-13‹ C. It then passes through pipe 245 to form tube 250 after which it is cut and packed. Hydrogenated vegetable oils, honey and maple sugar may be added to the butter.

68. 发明专利

FR588993A 未知
公开(公告)号：FR588993A
公开(公告)日：1925-05-18
申请号：FR588993D
申请日：1924-08-19
申请人： MILK OIL CORP
IPC分类号： A23C15/04

69. 发明申请

WO2018229347A1 BUTTER AND METHOD FOR ITS PRODUCTION 审中-公开
公开(公告)号：WO2018229347A1
公开(公告)日：2018-12-20
申请号：PCT/FI2018/050469
申请日：2018-06-15
申请人： VALIO LTD
发明人： MUURONEN, Klaus , HEINO, Antti , VALKONEN, Niina
IPC分类号： A23C15/04 , A23C15/06 , A23C15/12
摘要： The invention relates to a method of making a butter product, comprising the steps of: providing a butter raw material having a fat content at least 35% by weight; adjusting the nonfat dry matter of the butter raw material to a range of 0.15% to 1.8% by weight; optionally churning the butter raw material to provide butter; adjusting the pH to provide the butter product having a pH in the range of 4.5 to 8.5. The invention also relates to butter having having a fat content of at least 80% by weight, a nonfat dry matter in the range of 0.15% to 1.8% by weight and a pH in the range of 4.5 to 8.5.

70. 发明申请

WO01028348A1 A METHOD OF FORMING A BUTTER/MARGARINE BLEND 审中-公开
标题翻译：一种形成BUTTER / MARGARINE BLEND的方法
公开(公告)号：WO01028348A1
公开(公告)日：2001-04-26
申请号：PCT/US2000/041264
申请日：2000-10-18
IPC分类号： A23C15/04 , A23C15/12 , A23C15/16 , A23D7/00 , A23D7/02 , A23C15/02
CPC分类号： A23C15/04 , A23C15/126 , A23C15/16 , A23D7/001 , A23D7/02
摘要： A method of forming a butter/margarine blend that includes removing water (24) of butterfat (30, 31) from a feed material (12) that includes butter to yield an intermediate (40), combining a non-dairy fat (44) with the intermediate (40) to form an intermediate blend (46), and processing the intermediate blend (46) to form the butter/margarine blend.
摘要翻译：一种形成黄油/人造奶油混合物的方法，其包括从包含黄油的进料（12）中除去乳脂（30,31）的水（24），以产生中间体（40），将非乳制脂肪（44），与中间体（40）形成中间体共混物（46），并加工中间体共混物（46）以形成黄油/人造黄油混合物。

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