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Improved method for pasteurising or sterilising liquid and semi-liquid products

机译:对液体和半液体产品进行巴氏灭菌或灭菌的改进方法

摘要

789,767. Sterilizing liquids. LAGUILHARRE, P. R. Nov. 28,1955 [Sept. 20, 1955; Nov. 3, 1955], No. 34077/55. Class 49. In continuously pasteurizing and sterilizing liquid and semi-liquid foods by injection of hot vapour such as steam, the hot food so injected is subjected to at least one expansion down to a pressure between that corresponding to the initial temperature of the food being pasteurized or sterilized and that corresponding to the pasteurizing or sterilizing temperature, the vapour evolved during the expansion is removed and compressed to a pressure at least as high as that corresponding to the pasteurizing or sterilizing temperature and is injected into the food, which is preferably in subdivided form. With the apparatus of Fig. 1, milk pumped at 15 ‹ C. to a preheater 1 is there heated to 100 ‹ C., is fed through an atomizing nozzle 7 into a sterilizing chamber 5 and is there rapidly heated to 140‹ C. by steam introduced by a pipe 13; milk sterilized in the chamber 5 is fed into an expansion chamber 10, the temperature being so decreased to 100‹ C., and the vapours evolved are withdrawn to a compressor 12, there compressed to 3 kg./sq. cm. above atmospheric pressure, i.e. are brought to a temperature greater than the sterilizing temperature, and are then introduced through a valve 14 and the pipe 13 into the chamber 5, whereby the pressure falls to 2.7 kg./sq. cm. above atmospheric, i.e. the temperature falls to the sterilizing temperature 140‹ C.; milk pumped from the expansion chamber 10 is cooled further at 18; the continuous operation is initiated by a preliminary admission of steam by a pipe 15. With the apparatus of Fig. 2, there are successive expansions in chambers 10 and 24, the vapours evolved in the chamber 24 being compressed at 29 and further compressed at 30, where also the vapours evolved in the chamber 10 are compressed, and the compressed vapours being introduced by way of a valve 14a into the sterilizing chamber 5. With the apparatus of Fig. 3, vapours evolved in a single expansion chamber 10a are fed by a pipe 31 to a compressor 32 to which is fed also milk preliminarily heated at 1, and the mixture is fed into a conduit 33 which constitutes the sterilizing chamber; with the apparatus of Fig. 4, vapours evolved in successive expansion chambers 10b and 24b are fed to compressors 38 and 39 to which is fed also milk preliminarily heated at 1, and the mixture is fed into a sterilizing conduit 41; with the apparatus of Fig. 5, vapours evolved in a single expansion chamber 10a are compressed in two stages in compressors 45 and 46 to which is fed also milk preliminarily heated at 1, and the mixture is fed into a sterilizing conduit 47.
机译:789,767。消毒液体。拉奎尔哈雷,P。R.,1955年11月28日[9月。 1955年20日; [1955年11月3日],编号34077/55。第49类。在通过注入热蒸汽(例如蒸汽)对液体和半液体食品进行连续巴氏杀菌和消毒时,所注入的热食品要经受至少一个膨胀,直至压力降至与食品初始温度相对应的压力之间。进行巴氏灭菌或灭菌,并与巴氏灭菌或灭菌温度相对应,将膨胀过程中产生的蒸汽除去并压缩至至少与巴氏灭菌或灭菌温度相对应的压力,然后注入食品中,优选细分形式。使用图1所示的设备,将在15℃下泵送到预热器1的牛奶加热到100℃,通过雾化喷嘴7送入消毒室5,然后在那里迅速加热到140℃。通过管道13引入的蒸汽;在室5中灭菌的牛奶被送入膨胀室10,温度被降低到100℃,并且所产生的蒸汽被排出到压缩机12中,压缩机12被压缩到3kg./sq。厘米。高于大气压的压力,即达到高于灭菌温度的温度,然后通过阀14和管13引入腔室5,由此压力降至2.7kg / sq。厘米。高于大气温度,即温度降至灭菌温度140℃。从膨胀室10泵出的牛奶在18进一步冷却。连续操作是通过管道15预先进入蒸汽而开始的。对于图2所示的设备,在腔室10和24中有连续的膨胀,腔室24中放出的蒸气在29处被压缩,在30处被进一步压缩。在此,在腔室10中放出的蒸气也被压缩,并且经压缩的蒸气通过阀14a被引入到灭菌室5中。利用图3的设备,在单个膨胀室10a中放出的蒸气被供给。管道31通向压缩机32,压缩机32也被预先加热,牛奶也被预加热到该压缩机32,混合物被送入构成消毒室的导管33中。用图4的设备,在连续的膨胀室10b和24b中放出的蒸气被送入压缩机38和39,还向牛奶和压缩机中初步加热了1的牛奶,混合物被送入消毒导管41。在图5所示的装置中,在一个膨胀室10a中放出的蒸气在压缩机45和46中被两级压缩,还向牛奶中预先加热了温度为1的牛奶,并将混合物送入消毒导管47。

著录项

  • 公开/公告号GB789767A

    专利类型

  • 公开/公告日1958-01-29

    原文格式PDF

  • 申请/专利权人 PIERRE ROBERT LAGUILHARRE;

    申请/专利号GB19550034077

  • 发明设计人

    申请日1955-11-28

  • 分类号A23C3/037;A23L2/46;A23L3/24;

  • 国家 GB

  • 入库时间 2022-08-23 20:26:04

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