CN108378274A - A kind of sauce salts down food desalter and desalination process - Google Patents
A kind of sauce salts down food desalter and desalination process Download PDFInfo
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- CN108378274A CN108378274A CN201810241255.5A CN201810241255A CN108378274A CN 108378274 A CN108378274 A CN 108378274A CN 201810241255 A CN201810241255 A CN 201810241255A CN 108378274 A CN108378274 A CN 108378274A
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L5/00—Preparation or treatment of foods or foodstuffs, in general; Food or foodstuffs obtained thereby; Materials therefor
- A23L5/20—Removal of unwanted matter, e.g. deodorisation or detoxification
- A23L5/23—Removal of unwanted matter, e.g. deodorisation or detoxification by extraction with solvents
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L19/00—Products from fruits or vegetables; Preparation or treatment thereof
- A23L19/20—Products from fruits or vegetables; Preparation or treatment thereof by pickling, e.g. sauerkraut or pickles
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/90—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in food processing or handling, e.g. food conservation
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Abstract
本发明涉及一种酱腌食品脱盐装置与脱盐方法。一种酱腌食品脱盐装置,它的密封仓(1)分别连通真空压缩泵(2)、进料阀(3)、排料阀(4)和排水阀(5)。一种酱腌食品脱盐方法,任意一次脱盐时间为3-30分钟,任意一次脱盐过程中酱腌食品与脱盐水含盐量的重量份数之比为1:0.2-0.8,酱腌食品与脱盐水的重量份数之比为1:0.5-1.5。本发明不但为企业解决了废水排放问题,而且大幅度减少了我国水资源的消耗和废水排放对生态环境造成的压力,有效地实现了脱盐水的零排放,大大降低了企业的生产成本,节约了宝贵的自然资源,践行了我国政府一贯倡导的走可持续发展的道路。
The invention relates to a desalting device and a desalting method for pickled food. A desalting device for pickled food, the sealed chamber (1) of which is respectively connected with a vacuum compression pump (2), a feed valve (3), a discharge valve (4) and a drain valve (5). A method for desalting pickled food, the desalination time of any one time is 3-30 minutes, the ratio of the weight parts of the salt content of the pickled food to the desalted water in any one desalination process is 1:0.2-0.8, and the salt content of the pickled food and desalted The ratio of parts by weight of water is 1:0.5-1.5. The invention not only solves the problem of wastewater discharge for enterprises, but also greatly reduces the pressure on the ecological environment caused by the consumption of water resources and wastewater discharge in my country, effectively realizes zero discharge of desalinated water, greatly reduces the production cost of enterprises, and saves It saves precious natural resources and practices the road of sustainable development that the Chinese government has always advocated.
Description
技术领域technical field
本发明涉及酱腌食品加工技术领域,尤其是涉及一种酱腌食品脱盐装置与脱盐方法。The invention relates to the technical field of pickled food processing, in particular to a desalination device and method for pickled food.
背景技术Background technique
浸泡稀释脱盐目前是酱腌食品行业普遍采用的脱盐方法,其实质就是在常态下将酱腌食品(例如酱菜、榨菜、泡菜等)放到水(食用管道水)中浸泡,经过一定时间后酱腌食品中含盐量被稀释(即脱盐),这种方法耗水量大,脱盐时间较长,按现有技术的脱盐方法将酱腌食品的含盐度从脱盐前的15-16%脱盐到脱盐后的4-6%计算,耗水量通常是酱腌食品重量的8-10倍,脱盐时间约1-2小时,脱盐均匀度约为80-90%,并且浸泡过的脱盐水平均含盐度约为1.5%,这部分含盐水除少量回用外,其余全部作为废水集中收集处理后随污水排放,如按国家规定的含盐度为0.3%的废水排放标准,还需要消耗5倍的水进行稀释,由此可见,现有技术的脱盐技术每一吨酱腌食品所消耗的水总量约为40吨。Soaking and dilution desalination is currently a desalination method commonly used in the pickled food industry. Its essence is to soak pickled foods (such as pickles, pickled vegetables, kimchi, etc.) in water (edible pipeline water) under normal conditions, and after a certain period of time The salt content in the pickled food is diluted (i.e. desalination), this method consumes a lot of water and takes a long time to desalinate. According to the desalination method of the prior art, the salinity of the pickled food is desalinated from 15-16% before desalination to Calculated at 4-6% after desalination, the water consumption is usually 8-10 times the weight of pickled food, the desalination time is about 1-2 hours, the desalination uniformity is about 80-90%, and the soaked desalted water contains an average of salt The salinity of this part is about 1.5%. Except for a small amount of reuse, the rest of this part of the brine is collected and treated as wastewater and then discharged with the sewage. Diluted with water, it can be seen that the total amount of water consumed by the desalination technology of the prior art per ton of pickled food is about 40 tons.
按我国年产酱腌食品总量500万吨计算,每年酱腌食品的脱盐耗水量约20000万吨,加上排放消耗的稀释水,全国全年总耗水量约达100000万吨,折算成本费用约20亿元/年,随污水排放的盐总量约300万吨,折算经济损失约24亿元/年。Calculated on the basis of the total annual production of 5 million tons of pickled food in my country, the annual desalination water consumption of pickled food is about 200 million tons, plus the dilution water consumed by discharge, the total annual water consumption in the country is about 1,000,000 tons, converted into cost About 2 billion yuan/year, the total amount of salt discharged with sewage is about 3 million tons, and the converted economic loss is about 2.4 billion yuan/year.
另一方面,由于现有技术的脱盐方法耗水量大,水资源浪费严重,以及大量的盐分随污水排放,导致我国水资源更加紧缺,造成土质和生态环境的日益恶化,近年来,我国对生态资源和环境保护出台了一系列强制性政策和措施,目前国内大部分酱腌食品加工企业已经濒临缴纳高额的排污费用和生存竞争压力的困境。On the other hand, due to the large water consumption of the existing desalination method, the serious waste of water resources, and the discharge of a large amount of salt with the sewage, the shortage of water resources in my country has resulted in the deterioration of soil quality and ecological environment. In recent years, my country's ecological A series of mandatory policies and measures have been issued for resource and environmental protection. At present, most domestic pickled food processing enterprises are on the verge of paying high sewage charges and surviving the predicament of competitive pressure.
发明目的purpose of invention
本发明为简洁和统一技术特征的概念表述,将脱盐水和酱腌食品中的含盐量用百分比表示,其中分子表示盐的重量份数,分母表示脱盐水或酱腌食品的重量份数,例如含盐量为8%的脱盐水或酱腌食品是指在108份的重量份数中,盐的重量份数为8份,脱盐水或酱腌食品的重量份数为100份。本发明将不含盐的水(食用管道水)定义为含盐量为0%的脱盐水。本发明以1Kg作为一份(单位)重量份数。The present invention is a conceptual expression of concise and unified technical features, and expresses the salt content in desalinated and pickled foods in percentages, wherein the numerator represents the parts by weight of salt, and the denominator represents the parts by weight of desalinated or pickled foods, For example, the desalinated or pickled food with a salt content of 8% means that in 108 parts by weight, the parts by weight of salt are 8 parts, and the parts by weight of desalted water or pickled food are 100 parts. The present invention defines salt-free water (edible pipe water) as desalinated water with a salt content of 0%. In the present invention, 1Kg is regarded as a part (unit) by weight.
本发明所要解决的技术问题是提供一种克服现有技术缺陷的、解决酱腌食品脱盐耗水巨大、提高酱腌食品的含盐量均匀度、缩短脱盐时间、对脱盐水进行循环利用实现废水零排放的一种酱腌食品脱盐装置与脱盐方法。本发明解决其技术问题采用的技术方案是:一种酱腌食品脱盐装置,它的密封仓1分别连通真空压缩泵2、进料阀3、排料阀4和排水阀5。本发明所要解决的技术问题还可进一步通过如下技术方案加以解决:排水阀5依次连通第二进水阀12、第二盐水罐13、第二出水阀14、进水泵9、密封仓1;排水阀5与第二进水阀12之间设有多通管11,多通管11连通排水阀5和第二进水阀12,多通管11依次连通第三进水阀6、第三盐水罐7、第三出水阀8和进水泵9;多通管11依次连通第一进水阀20、第一盐水罐21、第一出水阀22、资源回收机构18、给水泵19、第四进水阀15、第四盐水罐16、第四出水阀17 、进水泵9,给水管23经给水阀10连通第四进水阀15;排水阀5与多通管11之间设有脱盐水循环机构,脱盐水循环机构为循环泵24连通排水阀5和多通管11,多通管11连通密封仓1和/或循环泵24连通排水阀5和多通管11,多通管11依次连通冲水阀25、排料阀4。本发明解决其技术问题采用的技术方案是:一种酱腌食品脱盐方法,开启进料阀3,将酱腌食品和脱盐水置入密封仓1内,关闭进料阀3,开启真空压缩泵2,对酱腌食品至少进行一次脱盐,任意一次脱盐时间为3-30分钟, 任意一次脱盐过程中酱腌食品与脱盐水中含盐量的重量份数之比为1:0.2-0.8,酱腌食品与脱盐水的重量份数之比为1:0.5-1.5,至少一次脱盐后,关闭真空压缩泵2,开启排水阀5排出脱盐水后开启排料阀4排出酱腌食品,关闭排料阀4和排水阀5。本发明所要解决的技术问题还可进一步通过如下技术方案加以解决:开启排水阀5后开启第二进水阀12,向第二盐水罐13注入脱盐水后关闭排水阀5和第二进水阀12,开启第二出水阀14、进水泵9向密封仓1内注入脱盐水后关闭第二出水阀14、进水泵9;开启排水阀5后开启第三进水阀6,经多通管11向第三盐水罐7注入脱盐水后关闭排水阀5和第三进水阀6,开启第三出水阀8、进水泵9向密封仓1注入脱盐水后关闭第三出水阀8、进水泵9;开启排水阀5后开启第一进水阀20,经多通管11向第一盐水罐21注入脱盐水后关闭排水阀5和第一进水阀20,开启第一出水阀22和第四进水阀15,脱盐水经资源回收机构18处理后,由给水泵19抽取脱盐水注入第四盐水罐16后关闭第一出水阀22和第四进水阀15,或开启给水阀10、第四进水阀15,给水管23向第四盐水罐16注入脱盐水后关闭给水阀10、第四进水阀15后开启第四出水阀17、进水泵9向密封仓1注入脱盐水后关闭第四出水阀17、进水泵9;开启真空压缩泵2后开启排水阀5、循环泵24、冲水阀25,使得脱盐水自密封仓1、排水阀5、循环泵24、多通管11、冲水阀25、排料阀4回流至密封仓1和/或开启排水阀5、循环泵24,使得脱盐水自密封仓1、排水阀5、循环泵24、多通管11回流至密封仓1,关闭真空压缩泵2后关闭排水阀5、循环泵24、冲水阀25。本发明可在密封仓1上设置一个减压阀28,以在开启排料阀4之前释放密封仓1内的真空负压,还可在密封仓1上设置自带叶片27的搅拌机26,以在对酱腌食品脱盐时搅拌酱腌食品,加速酱腌食品与脱盐水的交换时间,提高酱腌食品的脱盐均匀度。本发明中的连通是指关联的两个技术特征之间的直接连通或经管道连通。本发明中的真空压缩泵、搅拌机、循环泵、进水泵、多通管、资源回收机构、给水泵和所有阀门均为现有技术,密封仓和盐水罐采用机械加工方法制造。本发明可根据不同消费者的口感对酱腌食品脱盐出不同的含盐量。本发明由于采用上述技术方案,其脱盐过程中的耗水量仅为现有技术浸泡式稀释脱盐方法的1-2%,酱腌食品的脱盐均匀度达到98%-100%,脱盐时间约提高50%。本发明不但为企业解决了废水排放问题,而且大幅度减少了我国水资源的消耗和废水排放对生态环境造成的压力,有效地实现了脱盐水的零排放,大大降低了企业的生产成本,节约了宝贵的自然资源,践行了我国政府一贯倡导的走可持续发展的道路。The technical problem to be solved by the present invention is to provide a method that overcomes the defects of the prior art, solves the huge water consumption of pickled food desalination, improves the uniformity of salt content of pickled food, shortens the desalination time, and recycles desalted water to realize waste water. A zero-emission desalination device and desalination method for pickled food. The technical solution adopted by the present invention to solve the technical problem is: a pickled food desalination device, its sealed chamber 1 is connected to the vacuum compression pump 2, the feed valve 3, the discharge valve 4 and the drain valve 5 respectively. The technical problems to be solved by the present invention can be further solved by the following technical solutions: the drain valve 5 is connected to the second water inlet valve 12, the second brine tank 13, the second water outlet valve 14, the water inlet pump 9, and the sealing chamber 1 in sequence; A multi-way pipe 11 is provided between the valve 5 and the second water inlet valve 12. The multi-way pipe 11 is connected to the drain valve 5 and the second water inlet valve 12. The multi-way pipe 11 is connected to the third water inlet valve 6 and the third brine in turn. tank 7, third water outlet valve 8 and water inlet pump 9; the multi-way pipe 11 is sequentially connected to the first water inlet valve 20, the first brine tank 21, the first water outlet valve 22, the resource recovery mechanism 18, the feedwater pump 19, the fourth water inlet The water valve 15, the fourth brine tank 16, the fourth outlet valve 17, the water inlet pump 9, the water supply pipe 23 is connected to the fourth water inlet valve 15 through the water supply valve 10; the desalinated water circulation mechanism is arranged between the drain valve 5 and the multi-way pipe 11 , the desalinated water circulation mechanism is that the circulation pump 24 is connected to the drain valve 5 and the multi-way pipe 11, the multi-way pipe 11 is connected to the sealing chamber 1 and/or the circulation pump 24 is connected to the drain valve 5 and the multi-way pipe 11, and the multi-way pipe 11 is connected to the flushing water in turn. Valve 25, discharge valve 4. The technical solution adopted by the present invention to solve the technical problem is: a method for desalting pickled food, opening the feed valve 3, putting the pickled food and desalted water into the sealed chamber 1, closing the feed valve 3, and opening the vacuum compression pump 2. Desalt the pickled food at least once, and the desalination time for any one time is 3-30 minutes. The weight ratio of food and desalinated water is 1:0.5-1.5. After at least one desalination, close the vacuum compression pump 2, open the drain valve 5 to discharge the desalinated water, open the discharge valve 4 to discharge the pickled food, and close the discharge valve 4 and drain valve 5. The technical problem to be solved by the present invention can be further solved by the following technical solutions: open the second water inlet valve 12 after opening the drain valve 5, and close the drain valve 5 and the second water inlet valve after injecting desalted water into the second brine tank 13 12. Open the second water outlet valve 14 and the water inlet pump 9 to inject desalted water into the sealed chamber 1, then close the second water outlet valve 14 and the water inlet pump 9; Inject desalted water into the third salt water tank 7, close the drain valve 5 and the third water inlet valve 6, open the third water outlet valve 8, and the water inlet pump 9, inject desalted water into the sealed chamber 1, and then close the third water outlet valve 8 and the water inlet pump 9 Open the first water inlet valve 20 after opening the drain valve 5, inject desalted water into the first salt water tank 21 through the multi-way pipe 11, close the drain valve 5 and the first water inlet valve 20, and open the first water outlet valve 22 and the fourth The water inlet valve 15, after the desalted water is processed by the resource recovery mechanism 18, the desalted water is pumped by the feedwater pump 19 and injected into the fourth brine tank 16, and then the first water outlet valve 22 and the fourth water inlet valve 15 are closed, or the water supply valve 10 and the second water inlet valve are opened. Four water inlet valves 15, water supply pipe 23 inject desalted water into the fourth brine tank 16 and then close the water supply valve 10, fourth water inlet valve 15 and then open the fourth water outlet valve 17, water inlet pump 9 inject desalted water into the sealed chamber 1 and then close The fourth water outlet valve 17, the water inlet pump 9; after opening the vacuum compression pump 2, open the drain valve 5, the circulation pump 24, and the flushing valve 25, so that the desalinated water self-sealing chamber 1, the drain valve 5, the circulation pump 24, and the multi-way pipe 11 , flushing valve 25, and discharge valve 4 return to the sealed chamber 1 and/or open the drain valve 5 and circulation pump 24, so that the desalted water flows back from the sealed chamber 1, drain valve 5, circulation pump 24, and multi-way pipe 11 to the sealed chamber. Storehouse 1, close drain valve 5, circulation pump 24, flushing valve 25 after closing vacuum compression pump 2. The present invention can be provided with a decompression valve 28 on the sealed bin 1, to release the vacuum negative pressure in the sealed bin 1 before opening the discharge valve 4, also can be provided with the agitator 26 of self-contained blade 27 on the sealed bin 1, with Stir the pickled food when desalting the pickled food, speed up the exchange time of the pickled food and desalinated water, and improve the uniformity of desalination of the pickled food. Communication in the present invention refers to direct communication or communication through pipelines between two related technical features. The vacuum compression pump, mixer, circulation pump, water inlet pump, multi-way pipe, resource recovery mechanism, water feed pump and all valves in the present invention are all prior art, and the sealed chamber and brine tank are manufactured by mechanical processing. The invention can desalinate pickled foods to obtain different salt contents according to the tastes of different consumers. Because the present invention adopts the above technical scheme, the water consumption in the desalination process is only 1-2% of that of the prior art soaking dilution desalination method, the desalination uniformity of pickled food reaches 98%-100%, and the desalination time is increased by about 50% %. The invention not only solves the problem of wastewater discharge for enterprises, but also greatly reduces the pressure on the ecological environment caused by the consumption of water resources and wastewater discharge in my country, effectively realizes zero discharge of desalinated water, greatly reduces the production cost of enterprises, and saves It saves precious natural resources and practices the road of sustainable development that the Chinese government has always advocated.
本发明与现有技术的有益效果对比如下:The beneficial effect contrast of the present invention and prior art is as follows:
1)现有脱盐技术的每吨酱腌食品耗水量(含排放稀释耗水)约40吨,本发明耗水量仅为0.5-1吨,例如,一家年产酱腌食品1.5万吨的企业,现有技术所耗脱盐水用量约为 60万吨,每吨按(含排污费)2元计,脱盐水成本约120万元/年。本发明中的脱盐水与酱腌食品的最佳重量份数配比为1:1,每吨酱腌食品仅需要补充消耗0.5-1吨的水,比现有技术的脱盐方法减少98-99%的水,其中从12%含盐量的脱盐水中可提取回收12%的食盐,再用来腌制酱菜。1) The water consumption per ton of pickled food in the existing desalination technology is about 40 tons (including water consumption for discharge and dilution), but the water consumption of the present invention is only 0.5-1 ton. For example, an enterprise with an annual production of 15,000 tons of pickled food, The amount of desalted water consumed by the existing technology is about 600,000 tons, and the cost of desalted water is about 1.2 million yuan per year based on 2 yuan per ton (including sewage charges). The optimal weight ratio of desalted water and pickled food in the present invention is 1:1, and only 0.5-1 ton of water needs to be supplemented for each ton of pickled food, which is 98-99% less than the desalination method of the prior art. % of water, wherein 12% of salt can be extracted and recovered from desalinated water with 12% salt content, and then used to pickle pickles.
2)本发明所消耗的水约为0.5-1吨/吨酱腌食品,若以一家年产酱腌食品1.5万吨的企业为例,可节约98.75%的水,耗水成本1.5万元/年,加上资源回收机构对脱盐水的处理成本按120元/吨计,共90万元/年,合计成本91.5万元/年,减去资源回收机构提取食盐120kg/吨(共900吨/年,折算全年食盐回收成本72万元),全年脱盐生产成本仅19.5万元,节约成本比例为83%/年。2) The water consumed by the present invention is about 0.5-1 ton per ton of pickled food. Taking an enterprise with an annual output of 15,000 tons of pickled food as an example, 98.75% of water can be saved, and the cost of water consumption is 15,000 yuan/ton Years, plus the cost of desalted water treatment by resource recovery agencies at 120 yuan/ton, a total of 900,000 yuan/year, the total cost is 915,000 yuan/year, minus the 120kg/ton of salt extracted by resource recovery agencies (a total of 900 tons/ In 2009, the annual salt recycling cost was 720,000 yuan), the annual desalination production cost was only 195,000 yuan, and the cost saving ratio was 83%/year.
附图说明Description of drawings
下面结合附图和本发明的具体实施例对本发明作进一步详细描述:The present invention will be described in further detail below in conjunction with accompanying drawing and specific embodiment of the present invention:
图 1、图2、图3、图4、图5 是本发明的结构示意图。Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5 are structural schematic diagrams of the present invention.
具体实施方式Detailed ways
参见图 5 ,本发明的密封仓1分别连通真空压缩泵2、进料阀3、排料阀4和排水阀5,排水阀5依次连通第二进水阀12、第二盐水罐13、第二出水阀14、进水泵9,排水阀5与第二进水阀12之间设有多通管11,多通管11连通排水阀5和第二进水阀12,多通管11依次连通第三进水阀6、第三盐水罐7、第三出水阀8和进水泵9;多通管11依次连通第一进水阀20、第一盐水罐21、第一出水阀22、资源回收机构18、给水泵19、第四进水阀15、第四盐水罐16、第四出水阀17 、进水泵9,给水管23经给水阀10连通第四进水阀15;排水阀5与多通管11之间设有脱盐水循环机构;脱盐水循环机构为循环泵24连通排水阀5和多通管11,多通管11依次连通冲水阀25、排料阀4,密封仓1上设置自带叶片27的搅拌机26,密封仓1连通减压阀28。Referring to Fig. 5, the airtight chamber 1 of the present invention communicates with the vacuum compression pump 2, the feed valve 3, the discharge valve 4 and the drain valve 5 respectively, and the drain valve 5 communicates with the second water inlet valve 12, the second brine tank 13, the second Two water outlet valves 14, water inlet pumps 9, multiway pipes 11 are arranged between the drain valve 5 and the second water inlet valve 12, and the multiway pipes 11 communicate with the drain valve 5 and the second water inlet valve 12, and the multiway pipes 11 communicate in turn The third water inlet valve 6, the third brine tank 7, the third water outlet valve 8, and the water inlet pump 9; the multi-way pipe 11 is sequentially connected to the first water inlet valve 20, the first brine tank 21, the first water outlet valve 22, resource recovery Mechanism 18, water feed pump 19, fourth water inlet valve 15, fourth salt water tank 16, fourth water outlet valve 17, water inlet pump 9, water supply pipe 23 communicates with the fourth water inlet valve 15 through water feed valve 10; drain valve 5 and multiple There is a desalinated water circulation mechanism between the pipes 11; the desalinated water circulation mechanism is that the circulation pump 24 is connected to the drain valve 5 and the multi-way pipe 11, and the multi-way pipe 11 is connected to the flushing valve 25 and the discharge valve 4 in sequence. Stirrer 26 with blade 27, sealed chamber 1 communicates with decompression valve 28.
下列实施例设定真空压缩泵、循环泵、进水泵、给水泵、搅拌机和所有阀门的初始状态均为关闭状态。The following embodiments assume that the initial states of the vacuum compression pump, circulating pump, water inlet pump, feed water pump, mixer and all valves are closed.
实施例1-5是本发明脱盐装置的实施例。Embodiments 1-5 are embodiments of the desalination device of the present invention.
实施例1:参见图 1,开启进料阀3,将酱腌食品和脱盐水置入密封仓1,开启真空压缩泵2对酱腌食品至少进行一次脱盐,任意一次脱盐时间为3-30分钟,优选10分钟,任意一次脱盐过程中酱腌食品与脱盐水中含盐量的重量份数之比为1:0.2-0.8,优选1:0.5,酱腌食品与脱盐水的重量份数之比为1:0.5-1.5,优选1:1。如实现预期的脱盐指标,则关闭真空压缩泵2,开启排水阀5排出脱盐水,开启排料阀4取出酱腌食品后关闭排水阀5、排料阀4,从而完成一次脱盐,否则需用小于该次脱盐后的酱腌食品含盐量的脱盐水对酱腌食品进行多次脱盐。Embodiment 1: See Figure 1, open the feed valve 3, put the pickled food and desalted water into the sealed chamber 1, and turn on the vacuum compression pump 2 to desalt the pickled food at least once, and the desalination time for any one time is 3-30 minutes , preferably 10 minutes, the ratio of the parts by weight of the pickled food to the salt content in the desalted water in any one desalination process is 1:0.2-0.8, preferably 1:0.5, the ratio of the parts by weight of the pickled food to the desalted water is 1:0.5-1.5, preferably 1:1. If the expected desalination index is achieved, turn off the vacuum compression pump 2, open the drain valve 5 to discharge the desalted water, open the discharge valve 4 to take out the pickled food, and then close the drain valve 5 and the discharge valve 4 to complete a desalination, otherwise it is necessary to use Desalting the pickled food with desalinated water less than the salt content of the pickled food after this desalination is performed multiple times.
本实施例可对酱腌食品至少进行一次脱盐,直至满足国家标准或行业标准规定的酱腌食品含盐量的技术指标。In this embodiment, the pickled food can be desalted at least once until the technical index of the salt content of the pickled food is met by the national standard or industry standard.
实施例2:参见图 2,本实施例在实施例1的基础上,增设了一个盐水罐(第二盐水罐13),可将密封仓1内已对酱腌食品脱过盐的脱盐水注入该盐水罐内,并经进水泵9抽取至密封仓1内,以供下一批次的酱腌食品脱盐之用。Embodiment 2: Referring to Fig. 2, on the basis of embodiment 1, this embodiment adds a brine tank (the second brine tank 13), which can inject the desalted water that has desalted the pickled food in the sealed chamber 1 In the brine tank, it is drawn into the sealed chamber 1 through the water inlet pump 9 for the desalination of the next batch of pickled foods.
实施例3:参见图 3,本实施例在实施例2的基础上,增设了多通管11,并经多通管11再设置一个盐水罐(第三盐水罐7),也可将密封仓1内已对酱腌食品脱过盐的脱盐水注入该盐水罐内,并经进水泵9抽取至密封仓1内,以供下一批次的酱腌食品脱盐之用。Embodiment 3: Referring to Fig. 3, on the basis of Embodiment 2, this embodiment adds a multi-way pipe 11, and a brine tank (the third brine tank 7) is set through the multi-way pipe 11, and the sealed chamber can also be The desalted salt water that has been desalinated from the pickled food in 1 is poured into the brine tank, and is drawn into the sealed chamber 1 by the water inlet pump 9 for desalination of the next batch of pickled food.
实施例4:参见图 4,本实施例在实施例3的基础上,经多通管11还设置了一个盐水罐(第一盐水罐21),可将密封仓1内已对酱腌食品脱过盐的脱盐水注入该盐水罐内,并经资源回收机构18进行盐水分离,提取的盐可用来腌制酱腌食品,提取的水由给水泵19抽取至另一盐水罐内(第四盐水罐16),再经进水泵9抽取至密封仓1内,以供下一批次的酱腌食品脱盐之用。Embodiment 4: Referring to Fig. 4, on the basis of Embodiment 3, a brine tank (the first brine tank 21) is also provided through the multi-way pipe 11 in this embodiment, which can remove the pickled food in the sealed chamber 1. The salted desalinated water is injected into the brine tank, and the brine is separated by the resource recovery mechanism 18. The extracted salt can be used to marinate pickled food, and the extracted water is pumped into another brine tank by the feed water pump 19 (fourth brine tank 16), and then pumped into the sealed chamber 1 through the water inlet pump 9 for the desalination of the next batch of pickled foods.
实施例5:参见图 5,本实施例在实施例4的基础上,在排水阀5与多通管11之间设置了脱盐水循环机构,脱盐水循环机构为循环泵24连通排水阀5和多通管11,多通管11连通密封仓1和/或循环泵24连通排水阀5和多通管11,多通管11依次连通冲水阀25、排料阀4,可在开启真空压缩泵2对酱腌食品进行脱盐的过程中开启脱盐水循环机构,用以加强脱盐水的活性,以提高酱腌食品脱盐的均匀度。Embodiment 5: Referring to FIG. 5, on the basis of Embodiment 4, a desalinated water circulation mechanism is set between the drain valve 5 and the multi-way pipe 11. The desalinated water circulation mechanism is that the circulation pump 24 communicates with the drain valve 5 and the multi-way Pipe 11, multi-way pipe 11 is connected to seal chamber 1 and/or circulating pump 24 is connected to drain valve 5 and multi-way pipe 11, and multi-way pipe 11 is connected to flush valve 25 and discharge valve 4 in turn, and can be used to turn on vacuum compression pump 2 In the process of desalting pickled food, the desalinated water circulation mechanism is opened to strengthen the activity of desalinated water, so as to improve the uniformity of desalination of pickled food.
实施例6-10是本发明对应于实施例1-5的脱盐方法实施例。Embodiments 6-10 are examples of the desalination method corresponding to Embodiments 1-5 of the present invention.
实施例6:参见图 1,开启进料阀3,勾兑脱盐水,即,将盐和含盐量为0%的脱盐水(食用管道水)均匀搅拌后并用现有技术的流量计注入密封仓1内,用现有技术的盐度计测定酱腌食品的含盐量,称取酱腌食品并将酱腌食品置入密封仓1内,开启真空压缩泵2对酱腌食品至少进行一次脱盐,任意一次脱盐时间为3-30分钟,优选10分钟,任意一次脱盐过程中酱腌食品与脱盐水中含盐量的重量份数之比为1:0.2-0.8,优选1:0.5,酱腌食品与脱盐水的重量份数之比为1:0.5-1.5,优选1:1,若取含盐量为16%的酱腌食品,则取含盐量为8%的脱盐水对酱腌食品进行脱盐,该次脱盐后酱腌食品和脱盐水中盐的重量份数均为(16+8)/2=12份(12Kg),即酱腌食品和脱盐水的含盐量均为12%,酱腌食品和水的重量份数均为100份(100 Kg)。如实现预期的脱盐指标,则关闭真空压缩泵2,开启排水阀5排出脱盐水,开启排料阀4取出酱腌食品后关闭排水阀、排料阀,从而完成一次脱盐,否则需用小于该次脱盐后的酱腌食品中含盐量的脱盐水对酱腌食品进行多次脱盐,直至实现预期的脱盐指标。Embodiment 6: Referring to Figure 1, open the feed valve 3, and blend the desalinated water, that is, evenly stir the salt and desalinated water (edible pipeline water) with a salt content of 0%, and inject it into the sealed chamber with a flow meter of the prior art In 1, measure the salt content of the pickled food with a salinity meter of the prior art, weigh the pickled food and place the pickled food in the sealed chamber 1, and turn on the vacuum compression pump 2 to desalinate the pickled food at least once , the desalination time for any one time is 3-30 minutes, preferably 10 minutes, and the ratio of the parts by weight of the pickled food to the salt content in the desalted water in any one desalination process is 1:0.2-0.8, preferably 1:0.5, the pickled food The ratio of parts by weight to desalinated water is 1:0.5-1.5, preferably 1:1. If pickled food with a salt content of 16% is taken, then the desalinated food with a salt content of 8% is used to treat the pickled food. Desalting, after this desalination, the weight parts of salt in pickled food and desalted water are both (16+8)/2=12 parts (12Kg), that is, the salt content of pickled food and desalted water is 12%, and pickled food The parts by weight of water and water are 100 parts (100 Kg). If the expected desalination index is achieved, turn off the vacuum compression pump 2, open the drain valve 5 to discharge the desalted water, open the discharge valve 4 to take out the pickled food, and then close the drain valve and the discharge valve to complete desalination once, otherwise it will take less than this The desalination of the salt content in the pickled food after the first desalination is performed on the pickled food for many times until the expected desalination index is achieved.
实施例7:参见图2,本实施例在实施例6的基础上,将实施例1中第一次脱盐、第二次脱盐或第三次脱盐分别生成的含盐量为12%、8%或4%的脱盐水储存在盐水罐(第二盐水罐13)内,以供对下一批次的酱腌食品脱盐之用。Example 7: Referring to Figure 2, on the basis of Example 6, the salt content of the first desalination, the second desalination or the third desalination in Example 1 is respectively 12% and 8%. Or 4% desalinated water is stored in the brine tank (the second brine tank 13) for desalting the next batch of pickled food.
实施例8:参见图3,本实施例在实施例2的基础上,经多通管11增设了一个盐水罐(第三盐水罐7),将实施例1中第一次脱盐、第二次脱盐或第三次脱盐分别生成的含盐量为12%、8%或4%的脱盐水储存在盐水罐内,以供对下一批次的酱腌食品脱盐之用。Embodiment 8: Referring to Fig. 3, on the basis of Embodiment 2, this embodiment adds a brine tank (the third brine tank 7) through the multi-way pipe 11, and desalination for the first time and second time in Embodiment 1 Desalination or desalination for the third time generates desalted water with a salt content of 12%, 8% or 4% and is stored in a brine tank for use in desalting the next batch of pickled foods.
实施例9:参见图4,本实施例在实施例3的基础上,经多通管11再设置了一个盐水罐(第一盐水罐21),可将密封仓1内已对酱腌食品脱过盐的脱盐水注入该盐水罐内,并经资源回收机构18进行盐水分离,提取的盐可用来腌制酱腌食品,提取的水由给水泵19抽取至另一盐水罐内(第四盐水罐16),再经进水泵9抽取至密封仓1内,以供下一批次的酱腌食品脱盐之用。Embodiment 9: Referring to Fig. 4, on the basis of Embodiment 3, a brine tank (the first brine tank 21) is set up through the multi-way pipe 11 in this embodiment, so that the pickled food in the sealed chamber 1 can be detached. The salted desalinated water is injected into the brine tank, and the brine is separated by the resource recovery mechanism 18. The extracted salt can be used to marinate pickled food, and the extracted water is pumped into another brine tank by the feed water pump 19 (fourth brine tank 16), and then pumped into the sealed chamber 1 through the water inlet pump 9 for the desalination of the next batch of pickled foods.
实施例10:参见图5,本实施例进一步以将含盐量为16%的酱腌食品脱盐成含盐量为4%的酱腌食品为例对本发明作详细描述,开启进料阀3,勾兑脱盐水,即,将8 Kg的盐和100Kg的含盐量为0%的脱盐水(食用管道水)均匀搅拌后生成含盐量为8%的脱盐水(即在108份的重量份数中,盐的重量份数为8份,脱盐水的重量份数为100份。)并用现有技术的流量计经进料阀3注入密封仓1内,用现有技术的盐度计测定酱腌食品的含盐量,取含盐量为16%的酱腌食品(即在116份的重量份数中,盐的重量份数为16份,酱腌食品的重量份数为100份。)经进料阀3置入密封仓1内,开启真空压缩泵2对酱腌食品进行第一次脱盐,并开启脱盐水循环机构,用以加强脱盐水的活性,以提高酱腌食品脱盐的均匀度。第一次脱盐时间为10分钟,第一次脱盐后的酱腌食品的含盐量降为(16+8)/2=12%,开启排水阀5和第一进水阀20,将含盐量为12%的脱盐水注入第一盐水罐21,再经资源回收机构18进行盐水分离,资源回收机构18可分离提取出12份重量份数(12Kg)的盐和100份重量份数(100Kg)含盐量为0%的脱盐水,分离提取出的盐可用来腌制酱腌食品,分离提取出的100份重量份数的水由给水泵19抽取至第四盐水罐16,再经进水泵9抽取至密封仓1内,以供下一批次的酱腌食品作第三次脱盐之用。Embodiment 10: Referring to Fig. 5, this embodiment further describes the present invention in detail by desalting the pickled food with a salt content of 16% into a pickled food with a salt content of 4%, and opening the feed valve 3, Blending desalinated water, that is, 8 Kg of salt and 100 Kg of 0% desalinated water (edible pipeline water) are evenly stirred to generate desalinated water with a salt content of 8% (that is, in 108 parts by weight Among them, the parts by weight of salt are 8 parts, and the parts by weight of desalted water are 100 parts.) And use the flowmeter of prior art to inject in the sealed chamber 1 through feed valve 3, measure sauce with the salinity meter of prior art For the salt content of the pickled food, get the pickled food with a salt content of 16% (that is, in 116 parts by weight, the parts by weight of salt are 16 parts, and the parts by weight of the pickled food are 100 parts.) Put it into the sealed chamber 1 through the feed valve 3, turn on the vacuum compression pump 2 to desalinate the pickled food for the first time, and open the desalinated water circulation mechanism to strengthen the activity of desalinated water and improve the uniformity of desalination of the pickled food . The first desalination time is 10 minutes, the salt content of the pickled food after the first desalination is reduced to (16+8)/2=12%, open the drain valve 5 and the first water inlet valve 20, and reduce the salt content to 12% desalinated water is injected into the first brine tank 21, and then the brine is separated by the resource recovery mechanism 18. The resource recovery mechanism 18 can separate and extract 12 parts by weight (12Kg) of salt and 100 parts by weight (100Kg) of salt The salt content is 0% desalinated water, the separated and extracted salt can be used to marinate pickled food, and the separated and extracted 100 parts by weight of water is pumped to the fourth brine tank 16 by the feed water pump 19, and then passed through the water inlet pump 9 It is extracted into the airtight chamber 1 for the third desalination of the next batch of pickled food.
勾兑含盐量为4%的脱盐水注入密封仓1,开启真空压缩泵2对含盐量为12%的酱腌食品进行第二次脱盐,第二次脱盐时间为10分钟,第二次脱盐后的酱腌食品的含盐量降为(12+4)/2=8%,开启排水阀5和第二进水阀12,将含盐量为8%的脱盐水注入第二盐水罐13,再经进水泵9抽取至密封仓1内,以供下一批次的酱腌食品作第一次脱盐之用。Blend the desalted water with a salt content of 4% and inject it into the sealed chamber 1, and turn on the vacuum compression pump 2 to desalt the pickled food with a salt content of 12% for the second time. The second desalination time is 10 minutes, and the second desalination After the salt content of the pickled food is reduced to (12+4)/2=8%, the drain valve 5 and the second water inlet valve 12 are opened, and the desalted water with a salt content of 8% is injected into the second salt water tank 13, and then It is drawn into the sealed chamber 1 through the water inlet pump 9 for the first desalination of the next batch of pickled food.
取含盐量为0%的脱盐水(食用管道水)注入密封仓1,开启真空压缩泵2对含盐量为8%的酱腌食品进行第三次脱盐,第三次脱盐时间为10分钟,第三次脱盐后的酱腌食品的含盐量降为(8+0)/2=4%,开启排水阀5和第三进水阀6,将含盐量为4%的脱盐水注入第三盐水罐7,再经进水泵9抽取至密封仓1内,以供下一批次的酱腌食品作第二次脱盐之用。至此,实现了预期的将含盐量为16%的酱腌食品脱盐成含盐量为4%的酱腌食品的脱盐指标,关闭真空压缩泵2和脱盐水循环机构,开启排水阀5排出脱盐水,开启排料阀4取出酱腌食品后关闭排水阀、排料阀,从而完成整个脱盐过程。Take desalted water with a salt content of 0% (edible pipeline water) and inject it into the sealed chamber 1, and turn on the vacuum compression pump 2 to desalinate the pickled food with a salt content of 8% for the third time, and the third desalination time is 10 minutes , the salt content of the pickled food after the third desalination is reduced to (8+0)/2=4%, the drain valve 5 and the third water inlet valve 6 are opened, and the desalted water with a salt content of 4% is injected into the third The brine tank 7 is drawn into the sealed chamber 1 through the water inlet pump 9, so that the next batch of pickled foods can be desalinated for the second time. So far, the expected desalination index of desalting the pickled food with a salt content of 16% into the pickled food with a salt content of 4% has been achieved, the vacuum compression pump 2 and the desalinated water circulation mechanism are closed, and the drain valve 5 is opened to discharge the desalted water , open the discharge valve 4 to take out the pickled food and then close the drain valve and the discharge valve to complete the whole desalination process.
本实施例第三次脱盐所用含盐量为0%的脱盐水(食用管道水)也可开启给水阀10、第四进水阀15由进水管23注入第四盐水罐16,并经进水泵9注入密封仓1。The desalinated water (edible pipeline water) with a salt content of 0% used for the third desalination in this embodiment can also be opened to the water supply valve 10, and the fourth water inlet valve 15 is injected into the fourth brine tank 16 through the water inlet pipe 23, and then passed through the water inlet pump 9 into the sealed chamber 1.
本发明的脱盐方法包括使用但不限于使用本发明的脱盐装置。The desalination method of the present invention includes, but is not limited to, the use of the desalination device of the present invention.
上述实施例是对本发明所作出的进一步详细说明,不应认为上述实施例已穷尽了本发明的全部实施例。对于本发明所属技术领域的普通技术人员而言,在不脱离本发明构思的前提下,还可以做出若干简单的推演、替换、互换,都应当视为属于本发明权利要求的保护范围。The above-mentioned embodiments are further detailed descriptions of the present invention, and it should not be considered that the above-mentioned embodiments have exhausted all the embodiments of the present invention. For those of ordinary skill in the technical field of the present invention, without departing from the concept of the present invention, some simple deduction, replacement, and exchange can also be made, which should be regarded as belonging to the protection scope of the claims of the present invention.
Claims (10)
- The food desalter 1. a kind of sauce salts down, it is characterized in that:Its gas-tight silo(1)It is respectively communicated with vacuum compression pump(2), inlet valve (3), blow-off valve(4)And drain valve(5).
- The food desalter 2. a kind of sauce according to claim 1 salts down, it is characterized in that:Drain valve(5)It is sequentially communicated second Inlet valve(12), the second brine tank(13), the second outlet valve(14), intake pump(9), gas-tight silo(1).
- The food desalter 3. a kind of sauce according to claim 2 salts down, it is characterized in that:Drain valve(5)With the second inlet valve (12)Between be equipped with more siphunculus(11), more siphunculus(11)Communicated drainage valve(5)With the second inlet valve(12), more siphunculus(11)Successively It is connected to third inlet valve(6), third brine tank(7), third outlet valve(8)And intake pump(9).
- The food desalter 4. a kind of sauce according to claim 3 salts down, it is characterized in that:More siphunculus(11)It is sequentially communicated first Inlet valve(20), the first brine tank(21), the first outlet valve(22), resource reclaim mechanism(18), feed pump(19), the 4th water inlet Valve(15), the 4th brine tank(16), the 4th outlet valve(17), intake pump(9), feed pipe(23)Through water-supply valve(10)Connection the Four inlet valves(15).
- The food desalter 5. a kind of sauce according to claim 4 salts down, it is characterized in that:Drain valve(5)With more siphunculus(11) Between be equipped with desalination water circulation mechanism, desalination water circulation mechanism be circulating pump(24)Communicated drainage valve(5)With more siphunculus(11), more Siphunculus(11)Communication seals storehouse(1)And/or circulating pump(24)Communicated drainage valve(5)With more siphunculus(11), more siphunculus(11)Successively It is connected to flashing valve(25), blow-off valve(4).
- The food desalination process 6. a kind of sauce salts down, it is characterized in that it includes the following steps:Open inlet valve(3), by sauce salt down food and Desalted water is placed in gas-tight silo(1)It is interior, close inlet valve(3), open vacuum compression pump(2), the sauce food that salts down is at least carried out once Desalination, an arbitrary desalination time are 3-30 minute, and sauce salts down salt content in food and desalted water in an arbitrary desalination processes The ratio between parts by weight be 1:0.2-0.8, salt down the ratio between the parts by weight of food and desalted water of sauce are 1:0.5-1.5, at least one After secondary desalination, vacuum compression pump is closed(2), open drain valve(5)Blow-off valve is opened after discharge desalted water(4)Discharge sauce salts down food Product close blow-off valve(40 and drain valve(5).
- The food desalination process 7. a kind of sauce according to claim 6 salts down, it is characterized in that:Open drain valve(5)After open Two inlet valves(12), to the second brine tank(13)Drain valve is closed after injection desalted water(5)With the second inlet valve(12), open the Two outlet valves(14), intake pump(9)To gas-tight silo(1)The second outlet valve is closed after interior injection desalted water(14), intake pump(9).
- The food desalination process 8. a kind of sauce according to claim 7 salts down, it is characterized in that:Open drain valve(5)After open Three inlet valves(6), through more siphunculus(11)To third brine tank(7)Drain valve is closed after injection desalted water(5)With third inlet valve (6), open third outlet valve(8), intake pump(9)Third outlet valve is closed after injecting desalted water to gas-tight silo 1(8), intake pump (9).
- The food desalination process 9. a kind of sauce according to claim 8 salts down, it is characterized in that:Open drain valve(5)After open One inlet valve(20), through more siphunculus(11)To the first brine tank(21)Drain valve is closed after injection desalted water(5)With the first water inlet Valve(20), open the first outlet valve(22)With the 4th inlet valve(15), desalted water is through resource reclaim mechanism(18)After processing, by giving Water pump(19)It extracts desalted water and injects the 4th brine tank(16)After close the first outlet valve(22)With the 4th inlet valve(15), or open Open water-supply valve(10), the 4th inlet valve(15), feed pipe(23)To the 4th brine tank(16)Water-supply valve is closed after injection desalted water (10), the 4th inlet valve(15)The 4th outlet valve is opened afterwards(17), intake pump(9)To gas-tight silo(1)It is closed after injection desalted water 4th outlet valve(17), intake pump(9).
- The food desalination process 10. a kind of sauce according to claim 9 salts down, it is characterized in that:Open vacuum compression pump(2)After open Open drain valve(5), circulating pump(24), flashing valve(25)So that desalted water self sealss storehouse(1), drain valve(5), circulating pump(24)、 More siphunculus(11), flashing valve(25), blow-off valve(4)It is back to gas-tight silo(1)And/or open drain valve(5), circulating pump(24), Make desalted water self sealss storehouse(1), drain valve(5), circulating pump(24), more siphunculus(11)It is back to gas-tight silo(1), close vacuum Compression pump(2)After close drain valve(5), circulating pump(24), flashing valve(25).
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CN113729146A (en) * | 2021-09-30 | 2021-12-03 | 四川省食品发酵工业研究设计院有限公司 | Full-automatic vacuum dynamic desalting equipment and vacuum desalting method |
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CN113729146A (en) * | 2021-09-30 | 2021-12-03 | 四川省食品发酵工业研究设计院有限公司 | Full-automatic vacuum dynamic desalting equipment and vacuum desalting method |
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Application publication date: 20180810 |