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CN105815445B - Thawing method for frozen concentrated milk - Google Patents

Thawing method for frozen concentrated milk Download PDF

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Publication number
CN105815445B
CN105815445B CN201510005790.7A CN201510005790A CN105815445B CN 105815445 B CN105815445 B CN 105815445B CN 201510005790 A CN201510005790 A CN 201510005790A CN 105815445 B CN105815445 B CN 105815445B
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heat exchanger
frozen
freeze concentration
concentrated milk
heating
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CN105815445A (en
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林雅婷
刘凯崴
陈欣乔
曾柏澄
郑景元
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Uni President Enterprises Corp
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Abstract

本发明提供了一种冷冻浓缩乳解冻方法,其利用切削机将大型的冷冻浓缩乳冰块切削形成冷冻浓缩乳冰屑,再将其送入热交换器中进行初步加热,使冷冻浓缩乳冰屑融解形成冷冻浓缩乳泥状物,最后再将冷冻浓缩乳泥状物与热水一起投入溶解桶中进行升温溶解、搅拌以及混合,形成方便后续加工的乳原料。本发明的冷冻浓缩乳解冻方法能够提升解冻效率、保留乳原料风味、并且将冷冻浓缩乳冰块完全融解。

The invention provides a method for thawing frozen concentrated milk, which uses a cutting machine to cut large frozen concentrated milk ice cubes to form frozen concentrated milk ice chips, and then sends them to a heat exchanger for preliminary heating to make frozen concentrated milk ice. The chips are melted to form a frozen concentrated milk slurry, and finally the frozen concentrated milk slurry is put into a dissolving barrel with hot water for heating, dissolving, stirring and mixing to form a milk raw material that is convenient for subsequent processing. The frozen concentrated milk thawing method of the present invention can improve the thawing efficiency, retain the flavor of the milk raw materials, and completely melt the frozen concentrated milk ice cubes.

Description

冷冻浓缩乳解冻方法Frozen Concentrated Milk Thawing Method

技术领域technical field

本发明涉及一种冷冻浓缩乳解冻方法,特别涉及一种借由切削机进行冷冻浓缩乳冰块的切削动作,再利用热交换器对冷冻浓缩乳冰屑进行初步加热,借此提升冷冻浓缩乳的解冻效率,以达到增加冷冻浓缩乳还原成乳制品产能的目的。The invention relates to a method for thawing frozen and concentrated milk, in particular to a method of cutting frozen and concentrated milk ice cubes by means of a cutting machine, and then using a heat exchanger to initially heat the frozen and concentrated milk ice chips, thereby improving the quality of the frozen and concentrated milk. The thawing efficiency is improved to achieve the purpose of increasing the production capacity of frozen concentrated milk into dairy products.

背景技术Background technique

现有技术的冷冻浓缩乳解冻方法,一般会将冷冻浓缩乳冰块自冷冻库中取出后,放置于4~7℃冷藏解冻48-72小时,再将其投入溶解桶中与热水混合,并且升温至60℃,以形成液态乳原料半成品。In the prior art thawing method of frozen concentrated milk, the ice cubes of frozen concentrated milk are generally taken out from the freezer, placed in a refrigerated thaw at 4-7°C for 48-72 hours, and then put into a dissolving bucket and mixed with hot water. And the temperature is raised to 60° C. to form semi-finished liquid milk raw material.

但现有方法的溶解桶的升温需要有其他加热设备的辅助,若该溶解桶的加热辅助设备为蒸气加热,则易于桶内产生焦化物质,影响冷冻浓缩乳的味道;若该溶解桶的加热辅助设备为水循环加热,不但升温缓慢,历时长,也容易因为于溶解桶中连续投入的自然融解后的冷冻浓缩乳冰块因融解不完全而含有冷冻硬块,使溶解桶升温效能不佳,且所述冷冻硬块易造成溶解桶中的搅拌器因难以搅动而损坏。故现阶段需要一种能够提升解冻效率,不影响乳原料风味,并且不会有冷冻硬块残留导致搅拌器损坏的冷冻浓缩乳解冻方法。However, the heating of the dissolving barrel of the existing method needs the assistance of other heating equipment. If the heating auxiliary equipment of the dissolving barrel is steam heating, it is easy to produce coking substances in the barrel, which affects the taste of frozen concentrated milk; if the heating of the dissolving barrel The auxiliary equipment is water circulation heating, which not only raises the temperature slowly and takes a long time, but also tends to contain frozen hard blocks due to the incomplete melting of the naturally thawed frozen concentrated milk ice cubes continuously put into the dissolving tank, which makes the heating efficiency of the dissolving tank poor, and The frozen hard block is easy to cause damage to the stirrer in the dissolving bucket because it is difficult to stir. Therefore, at this stage, there is a need for a thawing method for frozen condensed milk that can improve the thawing efficiency, does not affect the flavor of the milk raw material, and does not cause damage to the stirrer due to frozen hard lumps.

发明内容Contents of the invention

为了解决现有技术蒸汽加热容易影响冷冻浓缩乳的味道,而水循环加热升温慢且容易使冷冻浓缩乳溶解不完全的问题,本发明提出了一种能够提升解冻效率、保留乳原料风味、并且将冷冻浓缩乳冰块完全融解的冷冻浓缩乳解冻方法。In order to solve the problem that steam heating easily affects the taste of frozen condensed milk in the prior art, while water circulation heating is slow to heat up and easily dissolves frozen condensed milk. A frozen condensed milk thawing method in which ice cubes of frozen condensed milk are completely thawed.

为达到上述发明目的,本发明所采用的技术手段为提供一种冷冻浓缩乳解冻方法,其是包括以下步骤:In order to achieve the above-mentioned purpose of the invention, the technical means adopted in the present invention is to provide a method for thawing frozen concentrated milk, which comprises the following steps:

切削,以一切削机将冷冻浓缩乳冰块切削形成冷冻浓缩乳冰屑,再将所述冷冻浓缩乳冰屑送入一具有加热管的热交换器中;Cutting, using a cutting machine to cut the frozen condensed milk ice cubes to form frozen condensed milk ice chips, and then sending the frozen condensed milk ice chips into a heat exchanger with a heating tube;

初步加热,以所述热交换器中的加热管对所述冷冻浓缩乳冰屑进行初步加热,将所述冷冻浓缩乳冰屑融解形成冷冻浓缩乳泥状物,再将所述冷冻浓缩乳泥状物投入一溶解桶中;以及Preliminary heating, using the heating tube in the heat exchanger to initially heat the frozen condensed milk ice chips, melting the frozen concentrated milk ice chips to form a frozen concentrated milk puree, and then the frozen concentrated milk puree The solid is dropped into a dissolving bucket; and

升温溶解,于所述溶解桶中加入热水升温,将所述溶解桶内的所述冷冻浓缩乳泥状物再一次升温溶解,并且使所述冷冻浓缩乳泥状物经搅拌后完全溶解于热水中形成液体乳原料半成品。Warming up and dissolving, adding hot water into the dissolving barrel to raise the temperature, heating and dissolving the frozen concentrated milk puree in the dissolving barrel again, and completely dissolving the frozen concentrated milk puree in the The semi-finished product of liquid milk raw material is formed in hot water.

本发明的有益效果在于简单利用切削步骤使原本一大块的冷冻浓缩乳冰块被切削成多个冷冻浓缩乳冰屑,再利用初步加热步骤将多个冷冻浓缩乳冰屑送入热交换器中先行加热,使冷冻浓缩乳冰屑投入溶解桶前已融解形成冷冻浓缩乳泥状物,最后再以热水进行再一次的升温溶解以及搅拌,并且使冷冻浓缩乳泥状物完全溶解于热水中,形成液态乳原料半成品。上述切削以及初步加热步骤使得冷冻浓缩乳冰块可以快速融解并与热水进行混和搅拌,使投入溶解桶中进行搅拌的冷冻浓缩乳不会有较大的冷冻硬块存在,有效避免搅拌器的损坏,并且减少制作的时间,提升冷冻浓缩乳还原成乳制品的产能。The beneficial effect of the present invention is that the original large block of frozen concentrated milk ice is cut into a plurality of frozen concentrated milk ice chips by simply using the cutting step, and then the multiple frozen concentrated milk ice chips are sent to the heat exchanger by the preliminary heating step Heating in the medium first, so that the frozen condensed milk ice chips are melted before being put into the dissolving bucket to form a frozen condensed milk slurry, and finally, the hot water is used to dissolve and stir again, and the frozen condensed milk slurry is completely dissolved in the hot water. In the water, the liquid milk raw material semi-finished product is formed. The above cutting and preliminary heating steps enable the ice cubes of frozen concentrated milk to be melted quickly and mixed with hot water for stirring, so that the frozen concentrated milk put into the melting bucket for stirring will not have large frozen lumps, effectively avoiding the damage of the agitator , and reduce the production time, and increase the production capacity of frozen concentrated milk into dairy products.

较佳的是,所述切削机与所述热交换器之间设置有一泵。此技术手段简单利用泵的抽取,将切削机切削而成的冷冻浓缩乳冰屑输送进入热交换器中进行初步加热,不但节省人力的花费,泵的运作使切削后浓缩乳冰屑于热交换器中以稳定速度输送,避免过度加热情形,使热交换器中较不会有焦化物的产生,可以有效保留乳原料风味,避免焦化物的焦味影响乳品的品质。Preferably, a pump is arranged between the cutting machine and the heat exchanger. This technical method simply uses the pump to pump the frozen concentrated milk ice chips cut by the cutting machine into the heat exchanger for preliminary heating. It is transported at a stable speed in the heat exchanger to avoid excessive heating, so that there will be less coke in the heat exchanger, which can effectively preserve the flavor of milk raw materials and avoid the burnt smell of coke from affecting the quality of dairy products.

更佳的是,所述热交换器为夹套管式热交换器、壳管式热交换器或板式热交换器,其中又以夹套管式热交换器为优先选择。此技术手段利用上述热交换器作为本发明的初步加热的加热工具,使冷冻浓缩乳冰屑借由与热交换器中的介质进行热交换反应,进一步融解形成冷冻浓缩乳泥状物,再投入溶解桶中与热水混合搅拌。其中经过热交换能力、生产压力、卡垢程度、清洗难度以及设备投资成本等多项因素的考量与评估,以夹套管式热交换器为最佳的选择,但使用者也可以将夹套管式热交换器任意置换为壳管式热交换器或是板式热交换器,甚至是其它种本案未提及的热交换器种类,此置换动作均不影响本案所提供的冷冻浓缩乳解冻方法的功效。More preferably, the heat exchanger is a jacketed tube heat exchanger, a shell and tube heat exchanger or a plate heat exchanger, and the jacketed tube heat exchanger is preferred. This technical means utilizes the above-mentioned heat exchanger as the heating tool for preliminary heating of the present invention, so that the frozen condensed milk ice crumbs are further melted to form a frozen condensed milk slurry by heat exchange reaction with the medium in the heat exchanger, and then put into Mix and stir with hot water in a dissolving bucket. Among them, after consideration and evaluation of many factors such as heat exchange capacity, production pressure, fouling degree, cleaning difficulty and equipment investment cost, the jacketed tube heat exchanger is the best choice, but users can also use the jacket Any replacement of the tube heat exchanger with a shell-and-tube heat exchanger or a plate heat exchanger, or even other types of heat exchangers not mentioned in this case, will not affect the thawing method of frozen concentrated milk provided in this case. effect.

附图说明Description of drawings

下面结合附图及实施例对本发明的冷冻浓缩乳解冻方法作进一步详细说明。The method for thawing frozen concentrated milk of the present invention will be described in further detail below in conjunction with the accompanying drawings and examples.

图1是本发明的夹套管式热交换器的立体示意图。Fig. 1 is a schematic perspective view of a jacketed tube heat exchanger of the present invention.

图2是本发明的夹套管式热交换器的加热管管径截面示意图。Fig. 2 is a schematic cross-sectional view of the diameter of the heating tube of the jacketed tube heat exchanger of the present invention.

图3是本发明的壳管式热交换器的立体示意图。Fig. 3 is a schematic perspective view of the shell-and-tube heat exchanger of the present invention.

图4是本发明的壳管式热交换器的加热管管径截面示意图。Fig. 4 is a schematic cross-sectional view of the diameter of the heating tube of the shell-and-tube heat exchanger of the present invention.

图5是本发明的板式热交换器的立体示意图。Fig. 5 is a schematic perspective view of the plate heat exchanger of the present invention.

图6是本发明的板式热交换器的板状结构截面示意图。Fig. 6 is a schematic cross-sectional view of the plate structure of the plate heat exchanger of the present invention.

附图标记说明:10.夹套管式热交换器,11.加热管,111.内层管,112.外层管,20.壳管式热交换器,21.加热管,211.内管,211A.微管,212.外管,30.板式热交换器,31.加热板,311.加热管。Explanation of reference signs: 10. Jacketed tube heat exchanger, 11. Heating tube, 111. Inner tube, 112. Outer tube, 20. Shell and tube heat exchanger, 21. Heating tube, 211. Inner tube , 211A. Microtube, 212. Outer tube, 30. Plate heat exchanger, 31. Heating plate, 311. Heating tube.

具体实施方式Detailed ways

为了对本发明的技术特征、目的和效果有更加清楚的理解,现对照附图说明本发明的具体实施方式。In order to have a clearer understanding of the technical features, purposes and effects of the present invention, the specific implementation manners of the present invention will now be described with reference to the accompanying drawings.

实施例1Example 1

本实施例解冻冷冻浓缩乳的方法为:将1吨的-18℃的冷冻浓缩乳冰块自冷冻库中取出,并直接以切削机将冷冻浓缩乳冰块切削成冷冻浓缩乳冰屑,再将冷冻浓缩乳冰屑以泵抽取,进而送入一夹套管式热交换器中进行初步加热,该夹套管式热交换器以70℃至80℃热水作为热源进行加热,使冷冻浓缩乳冰屑融化并持续升温至30℃至40℃之间,而该切削与初步加热的工作效率为1吨/小时至1.5吨/小时,即每小时可以切削并且加热处理1吨至1.5吨的冷冻浓缩乳冰块和冰屑。The method for thawing frozen concentrated milk in this embodiment is as follows: take 1 ton of -18°C frozen concentrated milk ice cubes out of the freezer, and directly use a cutting machine to cut the frozen concentrated milk ice cubes into frozen concentrated milk ice chips, and then The frozen condensed milk chips are pumped out, and then sent to a jacketed tube heat exchanger for preliminary heating. The jacketed tube heat exchanger uses hot water at 70°C to 80°C as a heat source to heat the frozen condensed milk. Milk ice chips melt and continue to heat up to 30°C to 40°C, and the cutting and preliminary heating work efficiency is 1 ton/hour to 1.5 tons/hour, that is, it can cut and heat 1 ton to 1.5 tons per hour Freeze condensed milk ice cubes and ice chips.

接着将冷冻浓缩乳冰屑经初步加热融解后形成的冷冻浓缩乳泥状物投入溶解桶中,并同时于溶解桶中加入60℃至75℃的热水进行升温溶解以及搅拌,使溶解桶内的冷冻浓缩乳泥状物再一次升温溶解5分钟至15分钟,并且完全溶解于热水中,最终形成液态乳原料半成品。实施例1从-18℃的冷冻浓缩乳冰块自冷冻库中取出至冷冻浓缩乳泥状物完全溶解于热水中形成液态乳原料半成品历时约1.1小时至1.5小时。Then put the frozen condensed milk slurry formed after the initial heating and melting of the frozen condensed milk ice chips into the dissolving bucket, and at the same time add hot water from 60°C to 75°C to the dissolving bucket to heat up and dissolve and stir, so that the liquid in the dissolving bucket The frozen condensed milk puree was once again heated and dissolved for 5 to 15 minutes, and completely dissolved in hot water to finally form a semi-finished liquid milk raw material. Example 1 It takes about 1.1 hours to 1.5 hours from the ice cubes of frozen concentrated milk at -18°C taken out of the freezer until the frozen concentrated milk puree is completely dissolved in hot water to form a semi-finished liquid milk raw material.

实施例2Example 2

本实施例解冻冷冻浓缩乳的方法为:将1吨的-18℃的冷冻浓缩乳冰块自冷冻库中取出,并直接以一切削机将冷冻浓缩乳冰块切削成冷冻浓缩乳冰屑,再将冷冻浓缩乳冰屑以泵抽取,进而送入壳管式热交换器中进行初步加热,该壳管式热交换器以70℃至80℃热水作为热源进行加热,使冷冻浓缩乳冰屑融化并持续升温至30℃至40℃,而该切削与初步加热的工作效率为1吨/小时至1.5吨/小时,即每小时可以切削并且加热处理1吨至1.5吨的冷冻浓缩乳冰块和冰屑。The method for thawing frozen concentrated milk in this embodiment is as follows: take out 1 ton of -18°C frozen concentrated milk ice cubes from the freezer, and directly use a cutting machine to cut the frozen concentrated milk ice cubes into frozen concentrated milk ice chips, Then pump the frozen concentrated milk ice chips, and then send them into the shell-and-tube heat exchanger for preliminary heating. Chips melt and continue to heat up to 30°C to 40°C, while the cutting and preliminary heating work efficiency is 1 ton/hour to 1.5 tons/hour, that is, 1 ton to 1.5 tons of frozen concentrated milk ice can be cut and heated per hour Blocks and icicles.

接着将冷冻浓缩乳冰屑经初步加热融解后形成的冷冻浓缩乳泥状物投入溶解桶中,并同时于溶解桶中加入60℃至75℃的热水进行升温溶解以及搅拌,使溶解桶内的冷冻浓缩乳泥状物再一次升温溶解5分钟至15分钟,并且完全溶解于热水中,最终形成液态乳原料半成品。实施例2从-18℃的冷冻浓缩乳冰块自冷冻库中取出至冷冻浓缩乳泥状物完全溶解于热水中形成液态乳原料半成品历时约1.1小时至1.5小时。Then put the frozen condensed milk slurry formed after the initial heating and melting of the frozen condensed milk ice chips into the dissolving bucket, and at the same time add hot water from 60°C to 75°C to the dissolving bucket to heat up and dissolve and stir, so that the liquid in the dissolving bucket The frozen condensed milk puree was once again heated and dissolved for 5 to 15 minutes, and completely dissolved in hot water to finally form a semi-finished liquid milk raw material. Example 2 It takes about 1.1 hours to 1.5 hours from the ice cubes of frozen concentrated milk at -18°C taken out of the freezer until the frozen concentrated milk puree is completely dissolved in hot water to form a semi-finished liquid milk raw material.

实施例3Example 3

本实施例解冻冷冻浓缩乳的方法为:将1吨的-18℃的冷冻浓缩乳冰块自冷冻库中取出,并直接以切削机将冷冻浓缩乳冰块切削成冷冻浓缩乳冰屑,再将冷冻浓缩乳冰屑以泵抽取,进而送入板式热交换器中进行初步加热,该板式热交换器以70℃至80℃热水作为热源进行加热,使冷冻浓缩乳冰屑融化并持续升温至30℃至40℃,而该切削与初步加热的工作效率为1吨/小时至1.5吨/小时,即每小时可以切削并且加热处理1吨至1.5吨的冷冻浓缩乳冰块和冰屑。The method for thawing frozen concentrated milk in this embodiment is as follows: take 1 ton of -18°C frozen concentrated milk ice cubes out of the freezer, and directly use a cutting machine to cut the frozen concentrated milk ice cubes into frozen concentrated milk ice chips, and then The frozen condensed milk ice chips are pumped, and then sent to the plate heat exchanger for preliminary heating. The plate heat exchanger uses 70°C to 80°C hot water as the heat source to melt the frozen condensed milk ice chips and continue to heat up to 30°C to 40°C, and the cutting and preliminary heating work efficiency is 1 ton/hour to 1.5 tons/hour, that is, 1 ton to 1.5 tons of frozen condensed milk ice cubes and ice chips can be cut and heated per hour.

接着将冷冻浓缩乳冰屑经初步加热融解后形成的冷冻浓缩乳泥状物投入溶解桶中,并同时于溶解桶中加入60℃至75℃的热水进行升温溶解以及搅拌,使溶解桶内的冷冻浓缩乳泥状物再一次升温溶解5分钟至15分钟,并且完全溶解于热水中,最终形成液态乳原料半成品。实施例3从-18℃的冷冻浓缩乳冰块自冷冻库中取出至冷冻浓缩乳泥状物完全溶解于热水中形成液态乳原料半成品历时约1.1小时至1.5小时。Then put the frozen condensed milk slurry formed after the initial heating and melting of the frozen condensed milk ice chips into the dissolving bucket, and at the same time add hot water from 60°C to 75°C to the dissolving bucket to heat up and dissolve and stir, so that the liquid in the dissolving bucket The frozen condensed milk puree was once again heated and dissolved for 5 to 15 minutes, and completely dissolved in hot water to finally form a semi-finished liquid milk raw material. Example 3 It takes about 1.1 hours to 1.5 hours from the ice cubes of frozen concentrated milk at -18°C taken out of the freezer until the frozen concentrated milk puree is completely dissolved in hot water to form a semi-finished liquid milk raw material.

比较例comparative example

本比较例解冻冷冻浓缩乳的方法为现有技术的一般工艺:将1吨的-18℃的冷冻浓缩乳冰块自冷冻库中取出后,放置于4℃至7℃冷藏解冻约48小时至72小时(4℃下解冻约需72小时、7℃下解冻约需48小时),再将未完全融解的冷冻浓缩乳固态、液态混合物投入溶解桶中与75℃的热水混合,并且以加热设备(蒸气加热或水循环加热)辅助升温至60℃至75℃,同时以搅拌器进行搅拌20分钟至30分钟,使冷冻浓缩乳固态、液态混合物完全溶解于热水中,以形成液态乳原料半成品。比较例从-18℃的冷冻浓缩乳冰块自冷冻库中取出至冷冻浓缩乳固态、液态混合物完全溶解于热水中形成液态乳原料半成品历时至少48.5小时。The method for thawing frozen concentrated milk in this comparative example is a general process of the prior art: after taking out 1 ton of frozen concentrated milk ice cubes at -18°C from the freezer, place them at 4°C to 7°C for about 48 hours to refrigerate and thaw. 72 hours (it takes about 72 hours to thaw at 4°C, and about 48 hours to thaw at 7°C), then put the incompletely thawed frozen concentrated milk solid and liquid mixture into the dissolving bucket, mix it with hot water at 75°C, and heat Equipment (steam heating or water circulation heating) assists in raising the temperature to 60°C to 75°C, while stirring with a stirrer for 20 minutes to 30 minutes, so that the solid and liquid mixture of frozen concentrated milk is completely dissolved in hot water to form semi-finished liquid milk raw materials . COMPARATIVE EXAMPLE It takes at least 48.5 hours from the ice cube of frozen concentrated milk at -18°C taken out of the freezer until the solid and liquid mixture of the frozen concentrated milk is completely dissolved in hot water to form a semi-finished liquid milk raw material.

此处先比较实施例1至3的夹套管式热交换器、壳管式热交换器以及板式热交换器的结构特性与其各项优缺点。Here, the structural characteristics and various advantages and disadvantages of the jacketed tube heat exchangers, shell and tube heat exchangers and plate heat exchangers in Examples 1 to 3 are compared first.

如图1及图2所示,夹套管式热交换器10包括弯曲且层叠设置的加热管11,该加热管11为双层管结构,内层管111用于容置并且输送冷冻浓缩乳,外层管112用于容置冷(热)介质,并且借由改变外层管112内的冷(热)介质对内层管111的冷冻浓缩乳进行升温或降温。As shown in Figures 1 and 2, the jacketed tube heat exchanger 10 includes curved and stacked heating tubes 11. The heating tubes 11 have a double-layer tube structure, and the inner tube 111 is used to accommodate and transport frozen concentrated milk. , the outer tube 112 is used to accommodate the cold (hot) medium, and by changing the cold (hot) medium in the outer tube 112, the temperature of the frozen condensed milk in the inner tube 111 is raised or lowered.

如图3及图4所示,壳管式热交换器20包括一直条状的加热管21,该加热管21同样为双层管结构,内管211集合了多条平行且间隔设置的微管211A,作为容置并且输送冷冻浓缩乳使用,外管212用于容置冷(热)介质,并且借由改变外层管内的冷(热)介质对内层管的冷冻浓缩乳进行升温或降温。As shown in Figures 3 and 4, the shell-and-tube heat exchanger 20 includes a straight heating tube 21, which is also a double-layer tube structure, and the inner tube 211 is composed of a plurality of parallel and spaced apart micro-tubes. 211A, used as accommodating and transporting frozen condensed milk, the outer tube 212 is used to accommodate cold (hot) medium, and by changing the cold (hot) medium in the outer tube to raise or lower the temperature of the frozen condensed milk in the inner tube .

如图5及图6所示,板式热交换器30包括多块层叠设置的加热板31,并且由多组加热板组间隔设置组合而成,所述加热板31中形成可供液体流通的多槽孔加热管311,供容置并且输送冷冻浓缩乳使用,加热板31的一侧用于容置冷(热)介质,并且借由改变加热板31一侧的冷(热)介质对加热管311内的冷冻浓缩乳进行升温或降温。As shown in Figures 5 and 6, the plate heat exchanger 30 includes a plurality of stacked heating plates 31, and is composed of multiple sets of heating plates arranged at intervals. Slotted heating pipe 311 is used for accommodating and transporting frozen condensed milk. One side of heating plate 31 is used to accommodate cold (hot) medium, and by changing the cold (hot) medium on one side of heating plate 31 to the heating tube The frozen concentrated milk in 311 is heated or cooled.

表1:本发明实施例1至3的夹套管式热交换器、壳管式热交换器以及板式热交换器的优缺点Table 1: Advantages and disadvantages of jacketed tube heat exchangers, shell and tube heat exchangers and plate heat exchangers of Embodiments 1 to 3 of the present invention

夹套管式热交换器Jacketed tube heat exchanger 壳管式热交换器shell and tube heat exchanger 板式热交换器plate heat exchanger 加热管管径Heating pipe diameter Big middle Small 热交换能力heat exchange capacity Low middle high 生产压力production pressure Low middle high 卡垢程度(焦化物)Scale degree (coke) Low middle high 清洗难度cleaning difficulty Low middle high 投资成本cost of investment Low high middle

夹套管式热交换器10因为其加热管11的管径较大,故容置于加热管11管内的冷冻浓缩乳与加热管11管壁的接触总面积相对较小,造成夹套管式热交换器10的热交换能力较差;但冷冻浓缩乳通过加热管11的压力(生产压力)、加热管11内的卡垢程度、加热管11的清洗难度以及设备的投资成本均较低,故本案以夹套管式热交换器10为第一优先选择。Because of the large diameter of the heating tube 11 of the jacketed tube heat exchanger 10, the total contact area between the frozen condensed milk contained in the heating tube 11 and the tube wall of the heating tube 11 is relatively small, resulting in a jacketed tube heat exchanger. The heat exchange capacity of the heat exchanger 10 is relatively poor; but the pressure (production pressure) of the frozen concentrated milk passing through the heating pipe 11, the degree of fouling in the heating pipe 11, the difficulty of cleaning the heating pipe 11 and the investment cost of the equipment are all relatively low. Therefore, in this case, the jacketed tube heat exchanger 10 is the first preferred choice.

而壳管式热交换器20的加热管21的内管211集合了多条平行且间隔设置的微管211A,所述微管211A的管径小于夹套管式热交换器10的加热管11的管径,故容置于微管211A内的冷冻浓缩乳与微管211A管壁的接触总面积相对较大,使壳管式热交换器20的热交换能力较夹套管式热交换器10为佳;但冷冻浓缩乳通过壳管式热交换器20的加热管21的压力、加热管21内的卡垢程度、加热管21的清洗难度以及设备的投资成本均较高,故在成本以及工艺方便性的考量下,本案还是以夹套管式热交换器10为第一优先选择。The inner tube 211 of the heating tube 21 of the shell-and-tube heat exchanger 20 is assembled with a plurality of parallel and spaced apart microtubes 211A, and the diameter of the microtubes 211A is smaller than that of the heating tube 11 of the jacketed tube heat exchanger 10. Therefore, the total area of contact between the frozen condensed milk contained in the microtube 211A and the wall of the microtube 211A is relatively large, so that the heat exchange capacity of the shell-and-tube heat exchanger 20 is higher than that of the jacketed tube heat exchanger. 10 is preferred; but the pressure of the heating tube 21 of the frozen concentrated milk passing through the shell-and-tube heat exchanger 20, the degree of fouling in the heating tube 21, the difficulty of cleaning the heating tube 21 and the investment cost of the equipment are all high, so in the cost And considering the convenience of the process, the jacketed tube heat exchanger 10 is still the first priority in this case.

另板式热交换器30虽然具有最佳的热交换能力,且投资成本介于夹套管式热交换器10与壳管式热交换器20之间,但其加热板31中的多个蜂巢状加热管311的管径非常细小,不利于冷冻浓缩乳的输送,易容易造成冷冻浓缩乳的焦化卡垢,且一旦卡垢后又难以清洗,故纵然其板式热交换器30的设备投资成本介于夹套管式热交换器10与壳管式热交换器20之间,但后续的维修保养非常麻烦且棘手,故本案还是以夹套管式热交换器10为第一优先选择。Although the other plate heat exchanger 30 has the best heat exchange capacity, and the investment cost is between the jacketed tube heat exchanger 10 and the shell and tube heat exchanger 20, but the plurality of honeycombs in the heating plate 31 The diameter of the heating pipe 311 is very small, which is not conducive to the transportation of the frozen concentrated milk, and it is easy to cause the coking and fouling of the frozen concentrated milk, and once the fouling is difficult to clean, so even if the equipment investment cost of the plate heat exchanger 30 is low Between the jacketed tube heat exchanger 10 and the shell and tube heat exchanger 20, but subsequent maintenance is very troublesome and tricky, so the jacketed tube heat exchanger 10 is still the first priority in this case.

接着比较实施例1至3与比较例的工艺差异。实施例1至3均为将冷冻浓缩乳冰块自冷冻库中取出后,先以切削机将冷冻浓缩乳冰块切削成冷冻浓缩乳冰屑,再将其送入一热交换器中进行初步加热,最后将初步加热融解后形成的冷冻浓缩乳泥状物投入溶解桶中与热水混合并同时进行升温搅拌,本案工艺相较于比较例是先将冷冻浓缩乳冰块以自然融解方式解冻,再将未完全融解的冷冻浓缩乳固态、液态混合物投入溶解桶中与热水混合,并同时以加热设备升温加热以及搅拌,实施例1至3更能有效率地将冷冻浓缩乳冰块确实融解,并且不会有未完全融解的冷冻硬块存在,使搅拌器不会因为冷冻硬块的存在而损坏,甚至能省下近97%的比较例的工艺时间。Then compare the process differences between Examples 1 to 3 and Comparative Example. In Examples 1 to 3, after the frozen concentrated milk ice cubes are taken out from the freezer, the frozen concentrated milk ice cubes are first cut into frozen concentrated milk ice chips by a cutting machine, and then sent to a heat exchanger for preliminary processing. Heating, and finally put the frozen condensed milk slurry formed after the initial heating and melting into the dissolving bucket, mix with hot water and heat up and stir at the same time. Compared with the comparative example, the process of this case is to thaw the frozen condensed milk ice cubes in a natural way , and then put the incompletely melted frozen condensed milk solid and liquid mixture into the dissolving bucket and mix it with hot water, and at the same time use heating equipment to heat up and stir. Embodiments 1 to 3 can more effectively freeze the frozen condensed milk ice cubes. Melting, and there will be no incompletely thawed frozen solids, so that the stirrer will not be damaged due to the existence of frozen solids, and even nearly 97% of the process time of the comparative example can be saved.

综上所述,本案所提供的冷冻浓缩乳解冻方法相较于现有技术的一般工艺,明显有提升冷冻浓缩乳解冻速率以及增加冷冻浓缩乳还原成乳制品产能的功效;此外,本案冷冻浓缩乳解冻方法的切削后的初步加热步骤,使投入溶解桶中进行搅拌的冷冻浓缩乳不会有较大的冷冻硬块存在,有效避免搅拌器损坏的可能,降低冷冻浓缩乳解冻工艺所需花费的设备维修、保养费用,亦等同于降低冷冻浓缩乳的生产成本。In summary, compared with the general process of the prior art, the thawing method of frozen concentrated milk provided in this case has the effect of significantly increasing the thawing rate of frozen concentrated milk and increasing the production capacity of frozen concentrated milk into dairy products; in addition, the frozen concentrated milk in this case The initial heating step after cutting of the milk thawing method makes the frozen concentrated milk put into the dissolving tank for stirring will not have large frozen lumps, effectively avoids the possibility of damage to the agitator, and reduces the cost of the frozen concentrated milk thawing process Equipment maintenance and maintenance costs are also equivalent to reducing the production cost of frozen concentrated milk.

以上所述仅为本发明示意性的具体实施方式,并非用以限定本发明的范围。任何本领域的技术人员,在不脱离本发明的构思和原则的前提下所作的等同变化与修改,均应属于本发明保护的范围。而且需要说明的是,本发明的各组成部分并不仅限于上述整体应用,本发明的说明书中描述的各技术特征可以根据实际需要选择一项单独采用或选择多项组合起来使用,因此,本发明理所应当地涵盖了与本案创新点有关的其他组合及具体应用。The above descriptions are only illustrative specific implementations of the present invention, and are not intended to limit the scope of the present invention. Any equivalent changes and modifications made by those skilled in the art without departing from the concept and principle of the present invention shall fall within the protection scope of the present invention. And it should be noted that each component of the present invention is not limited to the above-mentioned overall application, and each technical feature described in the description of the present invention can be selected to be used alone or in combination according to actual needs. Therefore, the present invention It should naturally cover other combinations and specific applications related to the innovation of this case.

Claims (3)

1. a kind of freeze concentration cream defreezing method, which is characterized in that the freeze concentration cream defreezing method the following steps are included:
Cutting cuts freeze concentration cream ice cube to form freeze concentration cream ice bits with a cutter, then the freeze concentration is newborn Ice bits are sent into a heat exchanger with heating tube;
Preliminary heating tentatively heats freeze concentration cream ice bits with the heating tube in the heat exchanger, described first The heat source temperature of step heating is 70 DEG C -80 DEG C, and freeze concentration cream ice bits are melted to form freeze concentration cream purees, work Make freeze concentration cream ice cube and the ice bits/hour that efficiency is 1 ton -1.5 tons, then freeze concentration cream purees investment one is molten It solves in bucket;And
Rising temperature for dissolving hot water heating is added in Yu Suoshu dissolving bucket, by the freeze concentration cream purees in the dissolving bucket Rising temperature for dissolving again, and make to be dissolved completely in after the freeze concentration cream purees is agitated and form fluid milk original in hot water Expect semi-finished product.
2. freeze concentration cream defreezing method as described in claim 1, which is characterized in that the cutter and the heat exchanger Between be provided with a pump.
3. freeze concentration cream defreezing method as claimed in claim 1 or 2, which is characterized in that the heat exchanger is jacketed pipe Formula heat exchanger, shell and tube heat exchanger or heat-exchangers of the plate type.
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201479830U (en) * 2009-08-06 2010-05-26 上海沃迪科技有限公司 Beverage and dairy food processing device
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US7059140B2 (en) * 2001-12-12 2006-06-13 John Zevlakis Liquid milk freeze/thaw apparatus and method
US20050260329A1 (en) * 2004-05-18 2005-11-24 Christianita Yusuf Production of liquid center filled confections

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201479830U (en) * 2009-08-06 2010-05-26 上海沃迪科技有限公司 Beverage and dairy food processing device
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