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voltage of a einphasennetzes, through a transformer is fed from a mehrphasennetz

机译:变压器的电压通过变压器从变压器中馈入

摘要

246,098. Corn Products Refining Co., (Assignees of Newkirk, W. B.). Jan. 17, 1925, [convention date]. Glucose.-Crystalline glucose is obtained by incompletely melting glucose, which has been prepared from starch by the ordinary processes of conversion and crystallization, and subjecting the magma to final crystallization while keeping the solid phase dispersed through the liquid. In one method, impure anhydrous dextrose is incompletely melted and then crystallized with gentle agitation at about. 120‹ F. or above to favour the production of anhydrous crystals. The mass is next centrifuged, and washed. The tem. perature may be reduced, after a certain amount of solid dextrose forms, to increase the yield. In another form, impure hydrate glucose is incompletely melted and then crystallized as before but within the hydrate range of temperature (i.e. up to 105‹ F.) or at higher temperatures up to 130‹ F. The conditions under which the anhydrous or hydrate forms of alpha- or #-glucose are formed in the crystallization are also described. The production of block sugar by carrying crystallization up to, or nearly to the point of solidification and subsequently removing the mother liquor by centrifuging or pressing is also mentioned. Specifications 227,140 and 232,160 are referred to. The Specification as open to inspection under Sect. 91 (3) (a) comprises also the addition of hydrate seed crystals in the crystallization of the incompletely melted hydrate. Crystalline glucose is also prepared from the starch-converted glucose by bringing about supersaturation in a solution of such high purity that crystallization is initiated substantially as scon as supersaturation takes place. In one method the sugar which may be hydrate or anhydrous or a mixture of both, is completely melted to a density of 40‹ BÚ. or thereabouts, and then crystallized in motion at about 120‹ F. or above, anhydrous crystals being obtained without seeding. Seed crystals may be added under some conditions. As the solid phase increases the temperature may be lowered, causing more rapid crystallization. A lower initial temperature may also be employed if liberal feeding with anhydrous crystals is effected at the start. In another method the solutions employed consist of liquors of high purity, e.g. 93 per cent and higher, obtained by carrying out the conversion of the starch by acid, e.g. hydrochloric acid, in open vessels instead of under pressure or by starting with a starch suspension of lower density, e.g. 6‹ instead of 12‹ BÞ., or by using a shorter time for the conversion, e.g. 21-22 minutes. In a further method, the solutions consist of converted liquors of ordinary puritv mixed with re-melted glucose. From these liquors either the hydrate or anhydrous form of glucose can be prepared, according to the temperature employed in crystallization and the purity of the liquor used. the anhydrous form tending to crystallize out from the purer and the hydrate from the less pure liquors. This subject-matter does not appear in the Specification as accepted,
机译:246,098。玉米产品精炼公司(Newkirk的受让人,W。B.)。 1925年1月17日,[会议日期]。葡萄糖-结晶葡萄糖是通过不完全熔融葡萄糖而获得的,葡萄糖是通过转化和结晶的常规过程从淀粉制得的,并且使岩浆最终结晶,同时保持固相分散在液体中。在一种方法中,将不纯的无水右旋糖不完全熔化,然后大约在大约搅拌下结晶。 120英尺或以上,有利于生产无水晶体。接下来将该团块离心并洗涤。 tem。在一定量的固体葡萄糖形成后,可以降低性状,以提高产量。在另一种形式中,不纯的水合物葡萄糖会像以前一样不完全融化,然后结晶,但在水合物温度范围内(即最高105 ‹F)或在更高温度下最高130 ‹F。在无水或水合物形成的条件下还描述了在结晶中形成的α-或β-葡萄糖的残基。还提到了通过使结晶达到或接近凝固点并随后通过离心或压制除去母液来生产嵌段糖的方法。参考规格227,140和232,160。该规范可供本节检查。 91(3)(a)还包括在不完全熔化的水合物的结晶中添加水合物晶种。结晶葡萄糖也可以通过在高纯度的溶液中引起过饱和而由淀粉转化的葡萄糖制得,该溶液在发生过饱和时基本上像scon一样开始结晶。在一种方法中,糖可以是水合物,无水或两者的混合物,完全融化至密度为40 B ‹。或其附近,然后在约120?F或更高的温度下运动结晶,得到无籽无水晶体。在某些条件下可以添加晶种。随着固相增加,温度可能降低,从而导致更快的结晶。如果一开始就进行无水晶体的自由进料,那么也可以采用较低的初始温度。在另一种方法中,所用溶液由高纯度的液体组成,例如高纯度的液体。 93%或更高,这是通过用酸,例如碳酸氢钠,进行淀粉的转化而获得的。在开放容器中而不是在压力下或以较低密度的淀粉悬浮液(例如6 ‹而不是12 ‹BÞ,或使用较短的转换时间,例如21-22分钟。在另一种方法中,溶液由普通纯化的转化液与再熔融的葡萄糖混合而成。根据结晶中使用的温度和所用液体的纯度,可以从这些液体中制备葡萄糖的水合物或无水形式。无水形式倾向于从较纯净的液体中结晶出来,而水合物则从较纯净的液体中结晶出来。该主题未在规范中显示为被接受,

著录项

  • 公开/公告号DE000000472972A

    专利类型

  • 公开/公告日1929-03-08

    原文格式PDF

  • 申请/专利权人 AEG;

    申请/专利号DEA0046825D

  • 发明设计人

    申请日1926-01-19

  • 分类号

  • 国家 DE

  • 入库时间 2022-08-24 09:36:26

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