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公开(公告)号：KR101869168B1
公开(公告)日：2018-06-19
申请号：KR1020160162996
申请日：2016-12-01
Applicant: 강원대학교산학협력단
Abstract: 본발명은고온의스팀살균방법을이용한과채즙의갈변저해및 살균장치에관한것이다. 본발명에따른스팀살균방법및 스팀살균장치는높은온도의스팀을처리하고상변화를통해유입되는잠열로인해살균함으로써무즙을비롯한과채즙의갈변을억제할수 있으므로식품의가공및 가공의전처리에유용하게사용될수 있다.
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公开(公告)号：KR1020180062847A
公开(公告)日：2018-06-11
申请号：KR1020160162996
申请日：2016-12-01
Applicant: 강원대학교산학협력단
CPC classification number: A23B7/0053 , A23B7/06 , A23L3/005 , A23V2200/048 , A23V2200/24
Abstract: 본발명은고온의스팀살균방법을이용한과채즙의갈변저해및 살균장치에관한것이다. 본발명에따른스팀살균방법및 스팀살균장치는높은온도의스팀을처리하고상변화를통해유입되는잠열로인해살균함으로써무즙을비롯한과채즙의갈변을억제할수 있으므로식품의가공및 가공의전처리에유용하게사용될수 있다.
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公开(公告)号：KR20180028632A
公开(公告)日：2018-03-19
申请号：KR20160116175
申请日：2016-09-09
Applicant: 강원대학교산학협력단 , 대한민국(농촌진흥청장)
IPC: G01N33/00
CPC classification number: G01N33/0098 , G01N2333/415
Abstract: 본발명은대사체기술을이용한콩의퇴화종실판별방법에관한것으로, 본발명의식물의퇴화종실을판별하는방법을통해, 식물의퇴화종실을발아전에판별하고제거하여경제적인손실을예방할수 있으며, 발아율이매우높은고품질의종실만을선별함으로써종실품질향상에의한종실의부가가치를높일수 있다.
Abstract translation: 本发明能够防止经济损失通过该方法涉及一种方法，变性种子使用的代谢物的技术，以确定本发明的植物的变性种子确定大豆，确定发芽前植物的变性种子和去除，并且 通过仅选择具有非常高的发芽率的高质量苗，可以通过改善苗的质量来增加苗的附加值。
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公开(公告)号：KR101772538B1
公开(公告)日：2017-08-30
申请号：KR1020150102155
申请日：2015-07-20
Applicant: 강원대학교산학협력단
IPC: B65D81/34
Abstract: 본발명은마이크로웨이브오븐을이용하여조리할내용물에대해서내용물이조리되는동안균일한가열이일어날수 있도록제작된도넛형상을가지는마이크로웨이브오븐용포장용기에관한것으로, 본발명은저면의중심부가내측으로함몰되어형성된함몰부를가지며, 함몰부로부터연장되어라운딩형상의측면부를가지며, 측면부로부터연장되어라운딩된절곡부를가진다. 이에따라, 균일한가열이일어날수 있도록제작된도넛형상의포장용기를제공함으로써, 원하는온도와수분분포를위해제품의배합을수정하지않아도되는효과가있다.
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公开(公告)号：KR101742368B1
公开(公告)日：2017-05-31
申请号：KR1020150015069
申请日：2015-01-30
Applicant: 강원대학교산학협력단
Abstract: 본발명은야채와소스가혼합된레토르트제품을살균하기위한최소살균법에관한것으로, 보다상세하게는야채와소스가혼합물을 110~129℃의온도에서살균처리하는단계를포함하는레토르트살균방법을제공하고, 상기의방법으로살균처리된상온유통이가능한레토르트를제공하는것이다. 본발명에따른살균법을이용할시, 최소로살균을사면서야채의신선도와우수한조직감을살리고공정시간의단축으로에너지절약이가능한효과가있다.
Abstract translation: 本发明涉及一种最小巴氏灭菌消毒的蔬菜和调味汁混合蒸煮产品，更具体地涉及包括蔬菜和酱过程在110〜129℃的温度下灭菌混合物的步骤的蒸煮杀菌处理 以及通过上述方法可以在室温下循环的经消毒处理的蒸煮器。 当使用根据本发明的杀菌方法，该杀菌购买的最小提高的蔬菜和质地优良的新鲜度在处理时间缩短的可能节约能源的效果。
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Patent Agency Ranking
公开(公告)号：KR101701516B1
公开(公告)日：2017-02-02
申请号：KR1020100120506
申请日：2010-11-30
Applicant: 강원대학교산학협력단
Abstract: 본발명은추출수율을향상시킬수 있는대두유의추출방법에관한것으로서, 보다구체적으로본 발명은대두또는대두분말을초고압으로전처리하는단계를포함하는대두유추출방법에관한것이다. 본발명에따른대두유추출방법은이산화탄소초임계추출기로부터대두유를추출하거나또는유기용매를이용하여추출하기이전에대두또는대두분말을초고압가공에의한전처리과정을수행한다는점에특징이있으며, 이러한초고압전처리공정을수반한대두유추출방법은초고압전처리공정을수반하지않은대두유추출방법에비해추출수율과속도를현저하게향상시킬수 있으므로본 발명에따른대두유추출방법은추출시간의절감및 추출에사용되는에너지를매우효과적으로절감시킬수 있는효과가있다.
Abstract translation: 目的：提取大豆油的方法，显着提高产量和比例，与现有的不伴随使用超高压预处理方法比较，从而显着降低了提取豆油的能量和时间。 构成：提取大豆油的方法包括：通过超高压预处理大豆油或大豆粉末的工序; 另外，将预处理的原料填充到提取器中的步骤; 另外，通过将超临界二氧化碳放入提取器中提取大豆油; 超临界二氧化碳是温度为35-80℃，压力为100-900巴，流速为30-50克/分钟的二氧化碳。
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公开(公告)号：KR1020140087586A
公开(公告)日：2014-07-09
申请号：KR1020120158067
申请日：2012-12-31
Applicant: 강원대학교산학협력단
Abstract: The present invention relates to a method for making a dried sea cucumber using far-infrared radiation, and more specifically, the purpose of the present invention is to provide optimal far-infrared intensity, temperature, flow rate, moisture diffusion coefficient, and activation energy in making the dried sea cucumber using far-infrared radiation. The method for making a dried sea cucumber using far-infrared radiation according to the present invention can shorten the drying time, minimize the denaturation due to heat, reduce the energy consumption, improve the quality of the dried sea cucumber, and decrease the production cost, when compared with the method for making a dried sea cucumber through hot-air drying of a prior art.
Abstract translation: 本发明涉及使用远红外线辐射制造干海参的方法，更具体地说，本发明的目的是提供最佳的远红外强度，温度，流速，水分扩散系数和活化能 在使用远红外辐射制作干海参。 根据本发明的使用远红外辐射制造干海参的方法可以缩短干燥时间，使由热引起的变性最小化，降低能量消耗，提高干燥海参的质量，降低生产成本 与通过现有技术的热风干燥制造干海参的方法相比较。
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公开(公告)号：KR1020120124824A
公开(公告)日：2012-11-14
申请号：KR1020110042686
申请日：2011-05-04
Applicant: 강원대학교산학협력단 , 주식회사 두산에코비즈넷
Abstract: PURPOSE: A manufacturing method of nano-particles of thiamine di-lauryl sulfate(tds) and a nano-particle solution thereof are provided to enhance anti-fungal efficacy for various crop diseases generating pathogens. CONSTITUTION: A manufacturing method of nano-particles of thiamine di-lauryl sulfate(tds) comprises dry grinding process, consecutive pulse laser processes, and high pressure homogenizing process. The dry grinding process includes the following step: pulverizing the thiamin derivative into the particle size of 1-10 micro meters. The consecutive pulse laser process includes the following step: irradiating pulse laser into 3 steps according to the energy strength by consecutively agitating the thiamin derivative powder with water. The wavelength of the pulse laser is 300-500 nano meters, the pulse length is 10ns, and the pulse repetition rate is 10Hz. The consecutive pulse laser process additionally includes the following step: making the size of the thiamin derivative as 400-700 nano meters by adding a dispersing agent as 0.1-0.5% of the total volume of the thiamin derivative particle solution. [Reference numerals] (AA) A process; (B1) Dry pulverizing pre-processing; (B2) Condition: controlling the air flow rate as 12.000Nm^3h^-1 and the rotary moisture content as 5% or less; (C1) Consecutive pulse laser process; (C2) Condition: agitating the particle solution consecutively while irradiating pulse type laser step by step; (C3) Wavelength of 300-500nm; (C4) Pulse width: 10ns(FWHM); (C5) Pulse repeating rate: 10Hz; (DD) Irradiating the pulse energy at 100mJ for 5-7 minutes; (EE) Irradiating the pulse energy at 200mJ for 5-7 minutes; (FF) Irradiating the pulse energy at 300mJ for 5-7 minutes; (GG,HH) Addition; (II) Adding 0.1-0.5% of total volume of dispersing agent monolaurate particle solution after irradiating the pulse energy at 100mJ for 5-7 minutes; (JJ) Adding 0.1-0.5% of total volume of dispersing agent monolaurate particle solution after irradiating the pulse energy at 200mJ for 5-7 minutes; (K1) High pressure homogenization process; (K2) Condition: circulating 3-5 times at the pressure of 15000-20000 psi; (L1) Particle size: average 200 nm or less; (L2) Useable nano-particle content:85%; (MM) B process; (N1) Conventional dry pulverizing mono process; (N2) Condition: controlling the compressive strength as 34~37 kg/cm^2 and the moisture content as 2-6%; (N3) Particle size: average tens of μm; (N4) Useable nano-particle content:15%; (OO) C process; (P1) Conventional high pressure homonization mono-processing; (P2) Condition: 30000 psi pressure; (P3) Particle size: average 1μm; (P4) Useable nano particle content:5-10%
Abstract translation: 目的：提供硫代二月桂基硫酸硫胺素（tds）的纳米颗粒及其纳米颗粒溶液的制备方法，以提高产生病原体的各种作物疾病的抗真菌功效。 构成：硫酸二月桂基硫酸钠（tds）的纳米颗粒的制造方法包括干法研磨，连续脉冲激光处理和高压均质化工艺。 干磨工艺包括以下步骤：将硫胺素衍生物粉碎成1-10微米的粒径。 连续的脉冲激光工艺包括以下步骤：通过连续搅拌硫胺衍生物粉末，用脉冲激光照射能量强度3步。 脉冲激光波长为300-500纳米，脉冲长度为10ns，脉冲重复频率为10Hz。 连续脉冲激光工艺另外包括以下步骤：通过加入分散剂为硫胺衍生物颗粒溶液总体积的0.1-0.5％，使硫胺素衍生物的尺寸为400-700纳米。 （附图标记）（AA） （B1）干粉预处理; （B2）条件：将空气流量控制在12.000Nm ^ 3h ^ -1，旋转水分含量为5％以下; （C1）连续脉冲激光工艺; （C2）条件：一步一步照射脉冲型激光，连续搅拌粒子溶液; （C3）波长300-500nm; （C4）脉冲宽度：10ns（FWHM）; （C5）脉冲重复频率：10Hz; （DD）将脉冲能量以100mJ照射5-7分钟; （EE）将脉冲能量以200mJ照射5-7分钟; （FF）将脉冲能量以300mJ照射5-7分钟; （GG，HH）加法; （II）在100mJ照射脉冲能量5-7分钟后，加入分散剂单月桂酸酯颗粒溶液总体积的0.1-0.5％ （JJ）在200mJ下照射脉冲能量5-7分钟后，加入分散剂单月桂酸酯颗粒溶液总体积的0.1-0.5％ （K1）高压均质化工艺; （K2）条件：在15000-20000 psi的压力下循环3-5次; （L1）粒径：平均200nm以下; （L2）可使用的纳米粒子含量：85％; （MM）B工艺; （N1）常规干式粉碎单工艺; （N2）条件：控制抗压强度为34〜37 kg / cm ^ 2，水分含量为2-6％; （N3）粒径：平均数十μm; （N4）可使用的纳米颗粒含量：15％; （OO）C过程; （P1）常规高压单相加工; （P2）条件：30000 psi压力; （P3）粒径：平均1μm; （P4）可使用的纳米颗粒含量：5-10％
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公开(公告)号：KR1020120058964A
公开(公告)日：2012-06-08
申请号：KR1020100120506
申请日：2010-11-30
Applicant: 강원대학교산학협력단
Abstract: PURPOSE: A method for extracting soy bean oil is provided to remarkably improving yield and rate comparison with existing method not accompanying pretreatment process using ultra-high pressure, thereby remarkably reducing energy and time for extracting soy bean oil. CONSTITUTION: A method for extracting soy bean oil comprises: a step of pre-treating soybean oil or soybean powder by ultra-high pressure; additionally, a step of filling the pre-treated raw material into an extractor; and additionally, extracting soybean oil by putting supercritical carbon dioxide into the extractor; the supercritical carbon dioxide is carbon dioxide in the state with the temperature of 35-80 °C, the pressure of 100-900 bar, and the flow rate of 30-50 g/min.
Abstract translation: 目的：提取大豆油的方法，显着提高产量和比例，与现有的不伴随使用超高压预处理方法比较，从而显着降低了提取豆油的能量和时间。 构成：提取大豆油的方法包括：通过超高压预处理大豆油或大豆粉末的工序; 另外，将预处理的原料填充到提取器中的步骤; 另外，通过将超临界二氧化碳放入提取器中提取大豆油; 超临界二氧化碳是温度为35-80℃，压力为100-900巴，流速为30-50克/分钟的二氧化碳。
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