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CN102669729A - Loach processing technology - Google Patents

Loach processing technology Download PDF

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Publication number
CN102669729A
CN102669729A CN2012101273011A CN201210127301A CN102669729A CN 102669729 A CN102669729 A CN 102669729A CN 2012101273011 A CN2012101273011 A CN 2012101273011A CN 201210127301 A CN201210127301 A CN 201210127301A CN 102669729 A CN102669729 A CN 102669729A
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loach
dried
extraction
treatment
degreasing
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姚东瑞
周鸣谦
刘云鹤
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Jiangsu Ocean University
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Jiangsu Ocean University
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Abstract

本发明是一种泥鳅的处理工艺,其步骤如下:采用烘干或真空冷冻干燥的方法将泥鳅的含水量降至5%以下,制成干泥鳅;将干泥鳅放入超临界萃取装置的萃取釜中进行脱脂处理;萃取参数如下:流体为超临界CO2、流量为15~30L/h,萃取压力22~35MPa,萃取温度30~50℃,分离压力10~16MPa,分离温度50~60℃,处理时间0.5~1.5h;经脱脂处理后,得到脱脂干泥鳅与泥鳅鱼油。本发明工艺采用超临界流体处理的方法有效地除去了干泥鳅中的鱼油,从而使干泥鳅能够避免氧化,可以长时间保存,处理过后的干泥鳅可以进行更好的粉碎,制成泥鳅粉,并副产得到品质优良的泥鳅鱼油。还能显著降低泥鳅粉中的微生物含量,使后续制成的泥鳅粉更加安全。The invention relates to a process for treating loach, the steps of which are as follows: the water content of loach is reduced to less than 5% by drying or vacuum freeze-drying to make dried loach; the dried loach is put into a supercritical extraction device for extraction Degreasing treatment is carried out in the kettle; the extraction parameters are as follows: the fluid is supercritical CO 2 , the flow rate is 15-30L/h, the extraction pressure is 22-35MPa, the extraction temperature is 30-50°C, the separation pressure is 10-16MPa, and the separation temperature is 50-60°C , the treatment time is 0.5-1.5h; after degreasing treatment, degreasing dried loach and loach fish oil are obtained. The process of the present invention adopts the supercritical fluid treatment method to effectively remove the fish oil in the dried loach, so that the dried loach can avoid oxidation and can be stored for a long time, and the dried loach after treatment can be better crushed to make loach powder. And the by-product is high-quality loach fish oil. It can also significantly reduce the microbial content in the loach powder, making the subsequent loach powder safer.

Description

一种泥鳅的处理工艺A kind of processing technology of loach

技术领域 technical field

本发明涉及一种食品的处理方法,特别是一种泥鳅的处理工艺 The invention relates to a food processing method, in particular to a loach processing technology .

背景技术 Background technique

传统中医认为泥鳅肉或全体可入药,具有滋阴清热、补脾益气、祛湿、兴阳等药用功效,记载于《本草纲目》和《中药大辞典》等文献中。在民间偏方中,还有食用泥鳅降火的方法。现代生物学的深入研究表明,从泥鳅中提取的天然多糖、糖蛋白和多肽类物质,经动物实验研究表明其具有抗炎、降转氨酶、除黄疸和保护肝脏的作用。目前,利用泥鳅保健及药用功效而开发的产品主要有泥鳅粉。现有泥鳅粉的加工方法主要采用烘干或真空冷冻干燥的方法将泥鳅中的水分除去成为干泥鳅,然后再进行粉碎加工成泥鳅粉。由于泥鳅含有一定的脂肪,随着水分被干燥后,干泥鳅中脂肪的质量百分数约在4%~6%,在加工过程中未将其除去,易造成后面的粉碎工序中泥鳅粉结成团,致使粉碎粒度不能很细。科研人员的分析表明,泥鳅脂肪中含有超过50%的不饱和脂肪酸,如果贮存条件不当容易被氧化,造成干泥鳅或泥鳅粉具有酸败味,严重影响产品的保质期。同时泥鳅脂肪中的不饱和脂肪酸中含有丰富的DHA、EPA等保健成分,如果进行提取分离可以充分利用泥鳅资源。 Traditional Chinese medicine believes that loach meat or the whole body can be used as medicine, which has medicinal effects such as nourishing yin and clearing heat, invigorating spleen and Qi, dispelling dampness, and invigorating yang, which are recorded in "Compendium of Materia Medica" and "Dictionary of Chinese Medicine". Among the folk remedies, there is also a method of eating loach to reduce fire. The in-depth study of modern biology shows that the natural polysaccharides, glycoproteins and polypeptides extracted from loach have anti-inflammatory, transaminase-lowering, jaundice-removing and liver-protecting effects through animal experiments. At present, the products developed by utilizing the health care and medicinal effects of loach mainly include loach powder. The processing method of existing loach powder mainly adopts the method of drying or vacuum freeze-drying to remove the moisture in the loach to become dried loach, and then pulverizes and processes into loach powder. Because loach contains a certain amount of fat, the mass percentage of fat in dried loach is about 4% to 6% after the water is dried. If it is not removed during processing, it will easily cause loach powder to form agglomerates in the subsequent crushing process. , so that the crushing particle size cannot be very fine. The analysis of scientific researchers shows that loach fat contains more than 50% unsaturated fatty acids. If the storage conditions are improper, it is easy to be oxidized, resulting in a rancid smell of dried loach or loach powder, which seriously affects the shelf life of the product. Simultaneously, the unsaturated fatty acid in the loach fat contains rich DHA, EPA and other health-care components, and if the extraction and separation are carried out, the loach resources can be fully utilized.

现有的水产品脂肪即鱼油分离方法主要有加热法、溶剂法等,但加热法提取温度高会影响干泥鳅的药用功效,而溶剂法会造成泥鳅粉及鱼油中有溶剂残留,影响产品的质量。如何在加工过程中有效的除去泥鳅的脂肪,并且不影响泥鳅的药用功效,同时还能充分利用其鱼油,在现有技术中未见合适的解决方案。 The existing methods for separating fish oil from aquatic products mainly include heating and solvent methods, but the high extraction temperature of the heating method will affect the medicinal efficacy of dried loach, and the solvent method will cause solvent residues in loach powder and fish oil, which will affect the product. the quality of. How to effectively remove the fat of loach during processing without affecting the medicinal efficacy of loach, and at the same time make full use of its fish oil, there is no suitable solution in the prior art.

发明内容 Contents of the invention

本发明所要解决的技术问题是针对现有技术的不足,提供一种工艺更为合理、能够避免干泥鳅氧化、增长保存时间并副产泥鳅鱼油的泥鳅的处理工艺。 The technical problem to be solved by the present invention is to provide a loach treatment process with a more reasonable process, which can avoid the oxidation of dried loach, prolong the storage time and produce loach fish oil by-product.

本发明所要解决的技术问题是通过以下的技术方案来实现的。本发明是一种泥鳅的处理工艺,其特点是,其步骤如下: The technical problem to be solved by the present invention is achieved through the following technical solutions. The present invention is a kind of processing technology of loach, it is characterized in that, its step is as follows:

(1)采用烘干或真空冷冻干燥的方法将泥鳅的含水量降至5%以下,制成干泥鳅; (1) The water content of the loach is reduced to less than 5% by drying or vacuum freeze-drying to make dried loach;

(2)将干泥鳅放入超临界萃取装置的萃取釜中进行脱脂处理;萃取参数如下:流体为超临界CO2、流量为15~30L/h,萃取压力22~35MPa,萃取温度30~50℃,分离压力10MPa~16MPa,分离温度50℃~60℃,处理时间0.5~1.5h; (2) Put the dried loach into the extraction kettle of the supercritical extraction device for degreasing treatment; the extraction parameters are as follows: the fluid is supercritical CO 2 , the flow rate is 15-30L/h, the extraction pressure is 22-35MPa, and the extraction temperature is 30-50 ℃, separation pressure 10MPa~16MPa, separation temperature 50℃~60℃, treatment time 0.5~1.5h;

(3)经脱脂处理后,得到脱脂干泥鳅与泥鳅鱼油。 (3) After degreasing treatment, degreasing dried loach and loach fish oil are obtained.

本发明泥鳅的处理工艺技术方案中,进一步优选的技术方案或技术特征如下: In the processing technical scheme of loach of the present invention, further preferred technical scheme or technical feature are as follows:

1、步骤(1)中:干燥至泥鳅的含水量优选为4%。 1. In step (1): drying until the water content of the loach is preferably 4%.

2、在脱脂处理前,还可以对干泥鳅进行切段处理,切成长度为3~4cm的干泥鳅段。 2. Before the degreasing treatment, the dried loach can also be cut into sections, and cut into sections of dried loach with a length of 3 to 4 cm.

3、步骤(2)中,优选的萃取参数如下:CO2流量为20L/h,萃取压力25MPa,萃取温度40℃,分离压力14MPa,分离温度55℃,处理时间1 h。 3. In step (2), the preferred extraction parameters are as follows: CO 2 flow rate is 20L/h, extraction pressure is 25MPa, extraction temperature is 40°C, separation pressure is 14MPa, separation temperature is 55°C, and treatment time is 1 h.

与现有技术相比,本发明工艺采用超临界流体处理的方法有效地除去了干泥鳅中的鱼油,从而使干泥鳅能够避免氧化,可以长时间保存,处理过后的干泥鳅可以进行更好的粉碎,制成泥鳅粉,并副产得到品质优良的泥鳅鱼油,可以进一步加工利用。通过本发明工艺的处理,还能显著降低泥鳅粉中的微生物含量,使后续制成的泥鳅粉更加安全。 Compared with the prior art, the process of the present invention adopts the method of supercritical fluid treatment to effectively remove the fish oil in the dried loach, so that the dried loach can avoid oxidation and can be preserved for a long time, and the dried loach after the treatment can be better preserved. Pulverize to make loach powder, and obtain high-quality loach fish oil as a by-product, which can be further processed and utilized. Through the treatment of the process of the invention, the microbial content in the loach powder can also be significantly reduced, so that the subsequently prepared loach powder is safer.

具体实施方式 Detailed ways

以下进一步描述本发明的具体技术方案,以便于本领域的技术人员进一步地理解本发明,而不构成对其权利的限制。 The specific technical solutions of the present invention are further described below, so that those skilled in the art can further understand the present invention, without limiting their rights.

实施例1,一种泥鳅的处理工艺,其步骤如下: Embodiment 1, a kind of processing technology of loach, its step is as follows:

(1)采用烘干或真空冷冻干燥的方法将泥鳅的含水量降至5%以下,制成干泥鳅; (1) The water content of the loach is reduced to less than 5% by drying or vacuum freeze-drying to make dried loach;

(2)将干泥鳅放入超临界萃取装置的萃取釜中进行脱脂处理;萃取参数如下:流体为超临界CO2、流量为15L/h,萃取压力22MPa,萃取温度30℃,分离压力10MPa,分离温度50℃,处理时间0.5; (2) Put the dried loach into the extraction kettle of the supercritical extraction device for degreasing treatment; the extraction parameters are as follows: the fluid is supercritical CO 2 , the flow rate is 15L/h, the extraction pressure is 22MPa, the extraction temperature is 30°C, and the separation pressure is 10MPa. Separation temperature 50°C, processing time 0.5;

(3)经脱脂处理后,得到脱脂干泥鳅与泥鳅鱼油。 (3) After degreasing treatment, degreasing dried loach and loach fish oil are obtained.

实施例2,一种泥鳅的处理工艺,其步骤如下: Embodiment 2, a kind of processing technology of loach, its step is as follows:

(1)采用烘干或真空冷冻干燥的方法将泥鳅的含水量降至5%以下,制成干泥鳅; (1) The water content of the loach is reduced to less than 5% by drying or vacuum freeze-drying to make dried loach;

(2)将干泥鳅放入超临界萃取装置的萃取釜中进行脱脂处理;萃取参数如下:流体为超临界CO2、流量为30L/h,萃取压力35MPa,萃取温度50℃,分离压力16MPa,分离温度60℃,处理时间1.5h; (2) Put the dried loach into the extraction kettle of the supercritical extraction device for degreasing treatment; the extraction parameters are as follows: the fluid is supercritical CO 2 , the flow rate is 30L/h, the extraction pressure is 35MPa, the extraction temperature is 50°C, and the separation pressure is 16MPa. Separation temperature 60°C, treatment time 1.5h;

(3)经脱脂处理后,得到脱脂干泥鳅与泥鳅鱼油。 (3) After degreasing treatment, degreasing dried loach and loach fish oil are obtained.

实施例3,一种泥鳅的处理工艺,其步骤如下: Embodiment 3, a kind of processing technology of loach, its steps are as follows:

(1)采用烘干或真空冷冻干燥的方法将泥鳅的含水量降至4%,制成干泥鳅; (1) Use drying or vacuum freeze-drying method to reduce the water content of loach to 4% to make dried loach;

(2)将干泥鳅放入超临界萃取装置的萃取釜中进行脱脂处理;萃取参数如下:流体为超临界CO2、流量为20L/h,萃取压力25MPa,萃取温度40℃,分离压力14MPa,分离温度55℃,处理时间1 h; (2) Put the dried loach into the extraction kettle of the supercritical extraction device for degreasing treatment; the extraction parameters are as follows: the fluid is supercritical CO 2 , the flow rate is 20L/h, the extraction pressure is 25MPa, the extraction temperature is 40°C, and the separation pressure is 14MPa. The separation temperature is 55°C, and the treatment time is 1 h;

(3)经脱脂处理后,得到脱脂干泥鳅与泥鳅鱼油。 (3) After degreasing treatment, degreasing dried loach and loach fish oil are obtained.

以下为经本实施例工艺处理与未经处理干泥鳅的比较: Following is the comparison of the unprocessed dry loach through the present embodiment process treatment:

不同泥鳅脱脂处理方法效果的比较 Comparison of Effects of Different Loach Degreasing Treatment Methods

项  目project 可被粉碎的最小目数/目The smallest mesh/mesh that can be crushed 保质期/月Shelf life/month 是否有溶剂残留Is there any solvent residue 霉菌/cfu/gMold/cfu/g 本发明工艺处理的干泥鳅The dried loach processed by the process of the present invention 6060 ≥12≥12 none 2×102×10 22 采用石油醚脱脂的干泥鳅Dried loach defatted with petroleum ether 5050 1212 have 2×102×10 33 未经脱脂处理的干泥鳅Unskimmed dried loach 3030 33 none 3×103×10 33

由以上比较可知,本发明技术处理的干泥鳅因脱去脂肪,其保质期更长,可被粉碎的目数更小,可作为生产泥鳅粉的优质原料,同时还得到优质泥鳅鱼油可被加工利用,该方法明显优于已有技术。 From the above comparison, it can be seen that the dry loach processed by the technology of the present invention has a longer shelf life because of defat, and the mesh size that can be crushed is smaller. It can be used as a high-quality raw material for producing loach powder, and high-quality loach fish oil can be processed and utilized simultaneously. , this method is significantly better than the prior art.

实施例4,实施例1或2或3所述的泥鳅的处理工艺中:在脱脂处理前,对干泥鳅进行切段处理,切成长度为3~4cm的干泥鳅段。 Embodiment 4, in the treatment process of the loach described in embodiment 1 or 2 or 3: before the degreasing treatment, the dried loach is cut into sections, and the length is cut into dry loach sections of 3-4 cm.

Claims (4)

1.一种泥鳅的处理工艺,其特征在于,其步骤如下: 1. a processing technology of loach, is characterized in that, its step is as follows: (1)采用烘干或真空冷冻干燥的方法将泥鳅的含水量降至5%以下,制成干泥鳅; (1) The water content of the loach is reduced to less than 5% by drying or vacuum freeze-drying to make dried loach; (2)将干泥鳅放入超临界萃取装置的萃取釜中进行脱脂处理;萃取参数如下:流体为超临界CO2、流量为15~30L/h,萃取压力22~35MPa,萃取温度30~50℃,分离压力10MPa~16MPa,分离温度50℃~60℃,处理时间0.5~1.5h; (2) Put the dried loach into the extraction kettle of the supercritical extraction device for degreasing treatment; the extraction parameters are as follows: the fluid is supercritical CO 2 , the flow rate is 15-30L/h, the extraction pressure is 22-35MPa, and the extraction temperature is 30-50 ℃, separation pressure 10MPa~16MPa, separation temperature 50℃~60℃, treatment time 0.5~1.5h; (3)经脱脂处理后,得到脱脂干泥鳅与泥鳅鱼油。 (3) After degreasing treatment, degreasing dried loach and loach fish oil are obtained. 2.根据权利要求1所述的泥鳅的处理工艺,其特征在于,步骤(1)中:干燥至泥鳅的含水量为4%。 2. The process for treating loach according to claim 1, characterized in that in step (1): drying until the water content of loach is 4%. 3.根据权利要求1所述的泥鳅的处理工艺,其特征在于:在脱脂处理前,对干泥鳅进行切段处理,切成长度为3~4cm的干泥鳅段。 3. The treatment process of loach according to claim 1, characterized in that: before the degreasing treatment, the dried loach is cut into sections, and the dried loach is cut into lengths of 3 to 4 cm. 4.根据权利要求1或2或3所述的泥鳅的处理工艺,其特征在于,步骤(2)中,萃取参数如下:CO2流量为20L/h,萃取压力25MPa,萃取温度40℃,分离压力14MPa,分离温度55℃,处理时间1 h。 4. The treatment process for loach according to claim 1, 2 or 3, characterized in that in step (2), the extraction parameters are as follows: CO2 flow rate is 20L/h, extraction pressure is 25MPa, extraction temperature is 40°C, separation The pressure is 14MPa, the separation temperature is 55°C, and the treatment time is 1 h.
CN2012101273011A 2012-04-27 2012-04-27 Loach processing technology Pending CN102669729A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104814468A (en) * 2015-01-12 2015-08-05 朱绿定 Processing method for loach powder

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1171210A (en) * 1997-08-15 1998-01-28 姚儒英 Method for producing meat and fish mixed food and its products
CN1879655A (en) * 2006-05-16 2006-12-20 武汉工程大学 Method for preparing oral liquid of sturgeon cartilage
CN101983586A (en) * 2010-10-22 2011-03-09 淮海工学院 Immediately-edible loach foodstuff and preparation method thereof
CN102108318A (en) * 2010-04-07 2011-06-29 北京洪源澳达生物技术发展有限公司 Crocodile grease and preparation method and use thereof
CN102370195A (en) * 2010-08-23 2012-03-14 陕西理工学院 Production method for degreased instant giant salamander meat powder

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1171210A (en) * 1997-08-15 1998-01-28 姚儒英 Method for producing meat and fish mixed food and its products
CN1879655A (en) * 2006-05-16 2006-12-20 武汉工程大学 Method for preparing oral liquid of sturgeon cartilage
CN102108318A (en) * 2010-04-07 2011-06-29 北京洪源澳达生物技术发展有限公司 Crocodile grease and preparation method and use thereof
CN102370195A (en) * 2010-08-23 2012-03-14 陕西理工学院 Production method for degreased instant giant salamander meat powder
CN101983586A (en) * 2010-10-22 2011-03-09 淮海工学院 Immediately-edible loach foodstuff and preparation method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104814468A (en) * 2015-01-12 2015-08-05 朱绿定 Processing method for loach powder

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Application publication date: 20120919