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51. 发明申请

WO98030309A1 SCREEN WITH IMPROVED STRENGTH PROPERTIES AND ASSEMBLY OF SUCH A SCREEN WITH A SUPPORT SCREEN 审中-公开
标题翻译：具有改进的强度特性的屏幕和具有支持屏幕的屏幕的组装
公开(公告)号：WO98030309A1
公开(公告)日：1998-07-16
申请号：PCT/NL1998/000024
申请日：1998-01-13
IPC分类号： B01D29/01 , B01D29/11 , B07B1/46 , C13B30/04
CPC分类号： C13B30/04 , B01D29/012 , B01D29/05 , B01D29/111 , B01D2201/184 , B07B1/4609
摘要： A screen for separating particulate materials from a liquid mass according to the invention comprises a pattern of slot-shaped passage openings for the liquid, wherein the pattern comprises first pattern elements (20; 30; 41; 51) having three groups of passage openings, the passage openings within a group having the same orientation, which is different from the orientation of the passage openings of the other groups within said first pattern element (20; 30; 41; 51), wherein a group of passage openings having a certain orientation within said first pattern element (20; 30; 41; 51) is also adjacent to groups of passage openings of neighbouring pattern elements (20; 30; 45; 55, 56), which groups have a different orientation. This arrangement of the passage openings achieves a high tensile strength and a high flexural stiffness off the screen, as a result of which the service life thereof is greater than that of known screens.
摘要翻译：根据本发明的用于从液体块分离颗粒材料的筛网包括用于液体的槽形通道开口的图案，其中所述图案包括具有三组通道开口的第一图案元件（20; 30; 41; 51）具有与所述第一图案元件（20; 30; 41; 51）内的其他组的通道开口的取向不同的组内具有相同取向的通道开口，其中具有一定方向的一组通道开口在所述第一图案元件（20; 30; 41; 51）内的所述组合也邻近相邻图案元件（20; 30; 45; 55,56）的通道开口的组，所述组具有不同的取向。这种通道开口的布置实现了高屏幕的拉伸强度和高弯曲刚度，因此其使用寿命大于已知屏幕的使用寿命。

52. 发明申请

WO2013082018A8 SYSTEM AND PROCESS FOR REFINING SUGAR 审中-公开
标题翻译：精制糖的系统和方法
公开(公告)号：WO2013082018A8
公开(公告)日：2014-07-03
申请号：PCT/US2012066634
申请日：2012-11-27
申请人： AMALGAMATED RES LLC
发明人： KEARNEY MICHAEL M , HIEB ALAN W , PRYOR TIMOTHY E , VELASQUEZ LAWRENCE
IPC分类号： C13B20/14 , C13B30/04 , C13B30/14 , C13B35/06
CPC分类号： C13B50/00 , C13B20/14 , C13B30/04 , C13B30/14 , C13B35/06
摘要： A system (10, 110) and process for refining raw sugar, comprising a melting unit (16, 116) configured to receive the raw sugar and an eluent to produce a melt liquor, a decolorization unit (24, 124) configured to receive the melt liquor and to produce a fine liquor, a crystallization unit (36, 136) configured to fractionate high-purity crystalline sucrose from the fine liquor and to provide a run-off syrup, a softening unit (46, 146) configured to receive the run-off syrup to produce a softened syrup, at least one separation unit (48, 148) configured to receive the softened syrup to produce a low-invert sucrose product, and a recycle line (52, 152) configured to relay the low-invert sucrose product from the at least one separation unit (48, 148) to the melting unit (16, 116).
摘要翻译：一种系统（10,110）和用于精制原糖的方法，包括被配置成接收原糖的洗涤单元（16,116）和洗脱液以产生熔融液体;脱色单元（24,124）熔化液体并产生细液;结晶单元（36,136），其被配置成从所述细液中分馏高纯度结晶蔗糖并提供流出液糖浆;软化单元（46,146），被配置为接收径流糖浆以产生软化的糖浆，至少一个分离单元（48,148），其构造成接收软化糖浆以产生低转化蔗糖产物;以及再循环管线（52,152）将蔗糖产物从至少一个分离单元（48,148）反转到熔化单元（16,116）。

53. 发明申请

WO00071758A1 SYSTEM AND METHOD FOR REFINING OF SUGAR 审中-公开
标题翻译：用于精制糖的系统和方法
公开(公告)号：WO00071758A1
公开(公告)日：2000-11-30
申请号：PCT/EP2000/004525
申请日：2000-05-19
IPC分类号： C13B20/06 , C13B30/04 , C13B30/14 , C13D3/06
CPC分类号： C13B20/06
摘要： A sugar refining process uses carbon dioxide obtained from a module containing a plurality of gas-permeable polymeric membranes. Flue gas from a boiler is scrubbed, and then passed through the gas-separation module. The output of the module contains an enhanced concentration of carbon dioxide, in the range of about 20 % by volume. The carbon dioxide enhanced gas is then directed into a reactor in which raw sugar is exposed to carbon dioxide to cause carbonation, an essential step in the decolorization of the raw sugar. The same boiler used to produce the carbon dioxide is also used to produce steam which drives the reaction. The present invention provides carbon dioxide for carbonation in a highly efficient manner, as the gas separation membrane has no moving parts and requires little maintenance. The invention is especially suited for retrofitting existing sugar refining plants, to improve their efficiency, at a relatively small cost.
摘要翻译：糖精炼方法使用从包含多个透气性聚合物膜的模块获得的二氧化碳。来自锅炉的烟气被擦洗，然后通过气体分离模块。模块的输出包含二氧化碳浓度的增加，在20体积％的范围内。然后将二氧化碳增强气体导入到反应器中，其中原糖暴露于二氧化碳以引起碳酸化，这是原糖脱色的关键步骤。用于生产二氧化碳的相同锅炉也用于产生驱动反应的蒸汽。本发明以高效的方式提供用于碳酸化的二氧化碳，因为气体分离膜没有移动部件并且几乎不需要维护。本发明特别适用于改造现有的糖精炼厂，以较低的成本提高其效率。

54. 发明授权

US11981968B2 Continuous method for obtaining a crystalline monosaccharide and device for continuous crystallization 有权
公开(公告)号：US11981968B2
公开(公告)日：2024-05-14
申请号：US17293097
申请日：2019-11-27
申请人： BMA BRAUNSCHWEIGISCHE MASCHINENBAUANSTALT AG
发明人： Mirko Löhn , Holger Fersterra
IPC分类号： C13B30/02 , C07H1/06 , C07H3/02 , C13B30/00 , C13B30/04
CPC分类号： C13B30/022 , C07H1/06 , C07H3/02 , C13B30/002 , C13B30/04
摘要： The invention relates to a continuous method for obtaining a crystalline monosaccharide, comprising: continuous crystallization of the monosaccharide in a main crystallizer (10), wherein crystallization by evaporation and/or crystallization by cooling is carried out continuously on a crystal suspension in the main crystallizer in order to allow crystals of the monosaccharide to grow in the crystal suspension; separation of crystals of the monosaccharide out of the crystal suspension to obtain crystalline monosaccharide; continuous formation of a mass of crystallization magma for the main crystallizer (10) in a cascade, wherein the cascade comprises at least one first stage (13) and a final stage (15) connected in series and each stage comprises at least one pre-crystallizer (13A, 15A), wherein, in the at least one pre-crystallizer (13A) of the first stage (13), a solution is seeded with monosaccharide by means of monosaccharide seed crystals in order to obtain a pre-crystallization magma, and a mass of crystallization magma for the downstream stage (14, 15) is formed from the pre-crystallization magma by means of crystallization by cooling and/or crystallization by evaporation, and wherein a solution containing monosaccharide and a mass of crystallization magma from the upstream stage is supplied to the at least one pre-crystallizer (15A, 15B, 15C) of the final stage (15) to obtain a pre-crystallization magma, and in the at least one pre-crystallizer (15A, 15B, 15C) of the final stage (15) a mass of crystallization magma for the main crystallizer (10) is formed from the pre-crystallisation magma by means of crystallization by cooling and/or crystallization by evaporation; the continuous supply of a solution containing the monosaccharide and a mass of crystallization magma from the at least one pre-crystallizer (15A, 15B, 15C) of the final stage (15) of the cascade to the main crystallizer (10) to provide the crystal suspension.

55. 发明申请

US20210404025A1 CONTINUOUS METHOD FOR OBTAINING A CRYSTALLINE MONOSACCHARIDE AND DEVICE FOR CONTINUOUS CRYSTALLIZATION 有权
公开(公告)号：US20210404025A1
公开(公告)日：2021-12-30
申请号：US17293097
申请日：2019-11-27
申请人： BMA BRAUNSCHWEIGISCHE MASCHINENBAUANSTALT AG
发明人： Mirko Löhn , Holger Fersterra
IPC分类号： C13B30/02 , C07H1/06 , C07H3/02 , C13B30/00 , C13B30/04
摘要： The invention relates to a continuous method for obtaining a crystalline monosaccharide, comprising: continuous crystallization of the monosaccharide in a main crystallizer (10), wherein crystallization by evaporation and/or crystallization by cooling is carried out continuously on a crystal suspension in the main crystallizer in order to allow crystals of the monosaccharide to grow in the crystal suspension; separation of crystals of the monosaccharide out of the crystal suspension to obtain crystalline monosaccharide; continuous formation of a mass of crystallization magma for the main crystallizer (10) in a cascade, wherein the cascade comprises at least one first stage (13) and a final stage (15) connected in series and each stage comprises at least one pre-crystallizer (13A, 15A), wherein, in the at least one pre-crystallizer (13A) of the first stage (13), a solution is seeded with monosaccharide by means of monosaccharide seed crystals in order to obtain a pre-crystallization magma, and a mass of crystallization magma for the downstream stage (14, 15) is formed from the pre-crystallization magma by means of crystallization by cooling and/or crystallization by evaporation, and wherein a solution containing monosaccharide and a mass of crystallization magma from the upstream stage is supplied to the at least one pre-crystallizer (15A, 15B, 15C) of the final stage (15) to obtain a pre-crystallization magma, and in the at least one pre-crystallizer (15A, 15B, 15C) of the final stage (15) a mass of crystallization magma for the main crystallizer (10) is formed from the pre-crystallisation magma by means of crystallization by cooling and/or crystallization by evaporation; the continuous supply of a solution containing the monosaccharide and a mass of crystallization magma from the at least one pre-crystallizer (15A, 15B, 15C) of the final stage (15) of the cascade to the main crystallizer (10) to provide the crystal suspension.

56. 发明授权

US09080221B2 System and process for refining sugar 有权
标题翻译：炼糖系统和工艺
公开(公告)号：US09080221B2
公开(公告)日：2015-07-14
申请号：US13684798
申请日：2012-11-26
申请人： Amalgamated Research LLC
发明人： Michael M. Kearney , Alan W. Hieb , Timothy E. Pryor , Lawrence Velasquez
IPC分类号： C13B50/00 , C13B20/14 , C13B30/04 , C13B30/14 , C13B35/06
CPC分类号： C13B50/00 , C13B20/14 , C13B30/04 , C13B30/14 , C13B35/06
摘要： A system and process for refining raw sugar, comprising a melting unit configured to receive the raw sugar and an eluent to produce a melt liquor, a decolorization unit configured to receive the melt liquor and to produce a fine liquor, a crystallization unit configured to fractionate high-purity crystalline sucrose from the fine liquor and to provide a run-off syrup, a softening unit configured to receive the run-off syrup to produce a softened syrup, at least one separation unit configured to receive the softened syrup to produce a low-invert sucrose product, and a recycle line configured to relay the low-invert sucrose product from the at least one separation unit to the melting unit.
摘要翻译：一种用于精制原糖的系统和方法，包括被配置为接收原糖和洗脱液以产生熔融液的熔化单元，被配置为接收熔融液并产生细液的脱色单元，被配置成分馏来自细液的高纯度结晶蔗糖并提供径流糖浆，软化单元构造成接收流失糖浆以产生软化糖浆，至少一个分离单元构造成接收软化糖浆以产生低转化蔗糖产物和再循环管线，其被配置为将低转化蔗糖产物从至少一个分离单元中继至熔化单元。

57. 发明授权

US5868851A Process for production of solid glucose 失效
标题翻译：固体葡萄糖生产工艺
公开(公告)号：US5868851A
公开(公告)日：1999-02-09
申请号：US908104
申请日：1997-08-11
申请人： Gene E. Lightner
发明人： Gene E. Lightner
IPC分类号： C13B20/16 , C13B30/04 , C13B30/06 , C13K1/04 , C13D3/16 , C13F1/04 , C13F1/06
CPC分类号： C13B30/04 , C13B20/165 , C13B30/06 , C13K1/04
摘要： A process to produce solid glucose from a hydrolyzate consisting of a mixture of glucose, water, and an acid used in the hydrolysis of a biomass material is covered herein. In the process, the hydrolyzate is concentrated, as required, to form two phases: a solid glucose phase and an acidic liquid phase. The phases are formed in a vessel where they are separated for recovery of the acidic liquid phase. The solid glucose phase, containing residual acidic liquid phase, is then extracted to remove most of the residual acid to produce solid glucose mostly free of acid. The recovered acid may then be recycled. The solid glucose may be further processed including purification and also drying.
摘要翻译：本文涵盖了由生物质材料水解中使用的葡萄糖，水和酸的混合物组成的水解产物产生固体葡萄糖的方法。在此过程中，根据需要浓缩水解产物，形成两相：固体葡萄糖相和酸性液相。这些相形成在容器中，在其中它们被分离以回收酸性液相。然后提取含有残留酸性液相的固体葡萄糖相以除去大部分残留的酸，以产生大部分不含酸的固体葡萄糖。然后可以回收回收的酸。可以进一步处理固体葡萄糖，包括纯化和干燥。

58. 发明授权

US4338201A Continuous separation system 失效
标题翻译：连续分离系统
公开(公告)号：US4338201A
公开(公告)日：1982-07-06
申请号：US213290
申请日：1980-12-05
申请人： Joseph C. V. Ducasse
发明人： Joseph C. V. Ducasse
IPC分类号： B01D33/00 , B01D47/00 , C13B30/04 , B01D33/24 , B01D37/00
CPC分类号： C13B30/04 , B01D33/17 , B01D33/466 , B01D33/58 , B01D33/60 , B01D33/72 , B01D47/00
摘要： A method of separating solids and liquid material in a slurry. The solids are continuously purged, washed, dried and removed with a minimum amount of mechanical handling. The slurry is continuously deposited on a moving horizontal rotary screen and condensible vapor is introduced above the layer while the pressure is reduced below the layer. Liquid is withdrawn from underneath the slurry layer with the vapor passing through the layer becoming superheated upon passage to evaporate further liquid from the solids. A stream of gas, which may be the same condensible vapor, is directed at the solids to entrain them and remove them from the screen.
摘要翻译：在浆料中分离固体和液体材料的方法。固体被持续清洗，洗涤，干燥并用最小量的机械处理除去。浆料连续地沉积在移动的水平旋转筛上，并且可压缩的蒸气被引入层上方，同时压力降低到该层以下。液体从淤浆层下方排出，通过层的蒸汽在通过时变得过热，从而从固体中蒸发更多的液体。可能是相同的可冷凝蒸汽的气流被引导到固体以夹带它们并将其从筛网上除去。

59. 发明授权

US4256582A Continuous separation system 失效
标题翻译：连续分离系统
公开(公告)号：US4256582A
公开(公告)日：1981-03-17
申请号：US66712
申请日：1979-08-15
申请人： Joseph C. V. Ducasse
发明人： Joseph C. V. Ducasse
IPC分类号： B01D33/00 , B01D47/00 , C13B30/04 , B01D33/24
CPC分类号： C13B30/04 , B01D33/17 , B01D33/466 , B01D33/58 , B01D33/60 , B01D33/72 , B01D47/00
摘要： A continuous separation system which continuously purges, washes, dries, and removes solids with a minimum amount of mechanical handling and consequential crystal breakage. A separator within the continuous separation system of the present invention comprises a stationary casing, a horizontal rotary screen within the casing, a fixed scraper mounted in the casing above the screen, an inlet conduit on one side of the scraper for depositing slurry on the screen to form a layer as the screen rotates, an outlet conduit on the other side of the scraper for carrying away dried solids, and gas nozzles for directing a gas stream at the solids as they encounter the scraper, entraining them, and directing them through the outlet conduit. The screen divides the casing interior into respective upper and lower chambers that are sealed from one another except through the screen. In operation, the gas stream carries the entrained solids to a separate receiver. The gas is then recirculated and enters the upper chamber of the separator at a slightly positive pressure. The lower chamber is evacuated so that a portion of the gas in the upper chamber passes through the slurry layer to displace liquid through the screen while further amounts of the gas cause additional drying of the solids so that they are of a suitably low liquid content when they encounter the fixed scraper and are entrained out of the separator.
摘要翻译：连续分离系统，连续清洗，洗涤，干燥和去除固体，最少量的机械处理和结果晶体破裂。在本发明的连续分离系统内的分离器包括固定壳体，壳体内的水平旋转屏幕，安装在屏幕上方壳体中的固定刮板，刮板一侧上的入口导管，用于在屏幕上沉积浆料当屏幕旋转时形成层，刮板另一侧的出口导管用于携带干燥的固体，以及气体喷嘴，用于在气体遇到刮刀时将气流引导至固体，夹带并引导它们通过出口导管。屏幕将壳体内部分成彼此密封的相应的上部和下部室，除了通过屏幕。在操作中，气流将夹带的固体携带到单独的接收器。然后气体再循环并以稍微正压力进入分离器的上腔室。下室被排空，使得上部室中的一部分气体通过浆料层以将液体移动通过筛网，而另外的量的气体引起固体的额外干燥，使得它们具有适当低的液体含量，他们遇到固定的刮刀并被夹带在分离器之外。

60. 发明授权

US3445283A Process for the preparation of instantaneously soluble,porous granular sugar 失效
标题翻译：制备可溶性多糖，多糖颗粒糖的方法
公开(公告)号：US3445283A
公开(公告)日：1969-05-20
申请号：US3445283D
申请日：1965-12-13
申请人： NISSIN SUGAR MFG CO LTD
发明人： AMANO MINORU , NISHIHASHI TORU , SHINADA SHOZO , ITO YUSHI
IPC分类号： C13B30/02 , C13B30/04 , C13F1/04
CPC分类号： C13B30/02 , C13B30/021 , C13B30/028 , C13B30/04

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