首页> 外国专利> Process for preparing fermented malt beverages using an excess of water in preparing the wort and then freeze concentrating the dilute wort prior to fermenting and finishing

Process for preparing fermented malt beverages using an excess of water in preparing the wort and then freeze concentrating the dilute wort prior to fermenting and finishing

机译:在麦芽汁制备中使用过量水制备发酵麦芽饮料的方法,然后在发酵和精加工之前冷冻浓缩稀麦芽汁

摘要

In the production of a fermented malt beverage, such as beer and ale, a dilute wort having an extract of less than 11 DEG Balling is made by preparing a malt mash, heating the mash, filtering the mash to produce a wort and boiling the wort in a brew kettle, utilizing 1.3-5 barrels of water per 100 pounds of brew materials, and the dilute wort is freeze concentrated, preferably to remove between 30 and 80 weight per cent of the water, to obtain a concentrated wort which can be readily fermented. (One barrel is stated to be the equivalent of 31 United States gallons.) The wort may be concentrated to a level greater than that desired for fermentation and thereafter diluted with water to the relatively lower extract level, between 11 and 13 DEG Balling, desired for the fermentation. The freeze concentration can be carried out batchwise using a plurality of alternate ice-generators and centrifuges connected in series. Alternatively, there may be employed a continuous two or three stage fractional crystallisation which involves cooling the dilute wort to produce a slurry of ice crystals and mother liquor, melting the crystals, passing at least a portion of the melt in contact with and counter-current to the crystals, and separating the mother liquor (concentrated wort) and the melted ice. The dilute wort may be freeze concentrated to remove 75 weight per cent water by cooling it to -4.4 DEG C. to form a slurry of ice crystals in mother liquor, passing the slurry (with 50 per cent ice solids) to a first crystal separation column to separate the ice crystals, cooling the mother liquor to -10.8 DEG C. to form a second slurry of ice crystals, passing the latter slurry (with 50 per cent ice solids) to a second crystal separation column to separate ice crystals, and withdrawing from the latter column the resulting mother liquor (concentrated wort). Hop flavour and aroma derived from extracted hop resins and hop oils are imparted to the beverage by adding hop extract to the wort subsequent to boiling of the wort in the brew kettle, such as to the wort cooled after the boiling, or to the fermented brew e.g. after finishing. The fermented brew itself may be freeze concentrated and the concentrate reconstituted by the addition of water and carbon dioxide; hop extract may be added to the concentrate or to the reconstituted product. The amount of hop extract is preferably sufficient to provide the finished beer with 275 p.p.m. of hop resin and 0.3 p.p.m. of hop oil. A small amount of hops may be added additionally to the wort and boiled therewith to assist in precipitating undesired proteins of high molecular weight, though the freeze concentration of the dilute wort and of the fermented brew promotes or causes the precipitation of such proteins and polysaccharides. The preparation of adjunct-containing malt mashes and worts is described in detail. After boiling, the wort can be strained to remove hops (if added during the boiling) and precipitates, and the pH can be adjusted by the addition of 0.3-0.5 per cent of potassium sulphate, potassium phosphate or lactic acid to maintain the pH at about 5 to 6.
机译:在生产啤酒和啤酒等麦芽发酵饮料时,通过制备麦芽糊状物,加热麦芽汁,过滤麦芽汁以产生麦芽汁并煮沸麦芽汁,制成提取率低于11度的稀麦芽汁。在酿造水壶中,每100磅酿造材料使用1.3-5桶水,然后将稀麦芽汁冷冻浓缩,最好除去30%至80%的水,以获得浓缩麦芽汁。发酵(据说一桶相当于31美制加仑。)麦芽汁可以浓缩到比发酵所需的浓度高的水平,然后用水稀释至提取物相对较低的水平,所需的11至13度之间的平衡。进行发酵冷冻浓缩可以使用多个串联的备用制冰机和离心机分批进行。可选择地,可以采用连续的两阶段或三阶段的分步结晶,其包括冷却稀麦芽汁以产生冰晶和母液的浆液,使晶体熔化,使至少一部分熔体与逆流接触并通过。结晶,然后分离母液(浓缩麦汁)和融化的冰。通过将稀麦芽汁冷却至-4.4℃,可以冷冻浓缩以除去75%(重量)的水,从而在母液中形成冰晶的浆液,然后将浆液(含50%的冰固体)送至第一次晶体分离。分离冰晶的塔,将母液冷却至-10.8℃,形成第二种冰晶浆,将后者的浆液(含50%的冰固体)送入第二个水晶分离柱,以分离冰晶,以及从后一列中取出所得母液(浓缩麦芽汁)。通过将啤酒花提取物在煮沸锅中煮沸的麦芽汁后,例如在煮沸后冷却的麦芽汁中或发酵后的啤酒中,将啤酒花提取物添加到麦芽汁中,可以将提取自啤酒花树脂和啤酒花油的啤酒花香精和香气赋予饮料。例如完成后。发酵的啤酒本身可以被冷冻浓缩,并通过添加水和二氧化碳来重构浓缩物。啤酒花提取物可以添加到浓缩液或重构产品中。啤酒花提取物的量优选足以为成品啤酒提供275 p.p.m.啤酒花树脂和0.3 p.p.m.啤酒花油。可以将少量啤酒花添加到麦芽汁中并与之煮沸,以帮助沉淀不希望的高分子量蛋白质,尽管稀麦芽汁和发酵酿造物的冷冻浓度促进或引起此类蛋白质和多糖的沉淀。详细描述了含附件的麦芽糊和麦芽汁的制备。煮沸后,麦芽汁可以过滤除去啤酒花(如果在煮沸过程中加入),并沉淀出来,可以通过添加0.3-0.5%的硫酸钾,磷酸钾或乳酸来调节pH值,以保持pH在大约5到6。

著录项

  • 公开/公告号US3361570A

    专利类型

  • 公开/公告日1968-01-02

    原文格式PDF

  • 申请/专利权人 PHILLIPS PETROLEUM COMPANY;

    申请/专利号US19630330254

  • 发明设计人 MALICK EMIL A.;

    申请日1963-12-13

  • 分类号C12C5/02;C12C7/047;C12C7/20;C12C7/28;C12C11/11;C12H6/04;

  • 国家 US

  • 入库时间 2022-08-23 12:57:43

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号