CN102342471B - Method for preparing amomun kravanh volatile oil microcapsule by using ultrasonic - Google Patents

Method for preparing amomun kravanh volatile oil microcapsule by using ultrasonic Download PDF

Info

Publication number
CN102342471B
CN102342471B CN2011102899545A CN201110289954A CN102342471B CN 102342471 B CN102342471 B CN 102342471B CN 2011102899545 A CN2011102899545 A CN 2011102899545A CN 201110289954 A CN201110289954 A CN 201110289954A CN 102342471 B CN102342471 B CN 102342471B
Authority
CN
China
Prior art keywords
volatile oil
ultrasonic
amomum cardamomum
beta
temperature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2011102899545A
Other languages
Chinese (zh)
Other versions
CN102342471A (en
Inventor
李超
商学兵
耿中华
赵节昌
崔珏
王乃馨
肖佰惠
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Xuzhou University of Technology
Original Assignee
Xuzhou University of Technology
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Xuzhou University of Technology filed Critical Xuzhou University of Technology
Priority to CN2011102899545A priority Critical patent/CN102342471B/en
Publication of CN102342471A publication Critical patent/CN102342471A/en
Application granted granted Critical
Publication of CN102342471B publication Critical patent/CN102342471B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Manufacturing Of Micro-Capsules (AREA)
  • Cosmetics (AREA)

Abstract

The invention discloses a method for preparing an amomun kravanh volatile oil microcapsule by using ultrasonic and belongs to the field of food processing. The method is characterized by comprising the following steps of: firstly, adding beta-cyclodextrin serving as a wall material into hot water to prepare a beta-cyclodextrin aqueous solution, and stirring until the beta-cyclodextrin is dissolved totally for later use; secondly, adding amomun kravanh volatile oil serving as a core material into the solution while stirring, and homogenizing to obtain emulsion; thirdly, putting the emulsion into ultrasonic equipment for performing ultrasonic operation; and finally, refrigerating, extracting, filtering, freezing and drying to obtain an amomun kravanh volatile oil microcapsule product. The amomun kravanh volatile oil microcapsule prepared by using the method is solid powder; by the method, the amomun kravanh volatile oil can be separated from outside air, so volatilization of the amomun kravanh volatile oil is avoided and the preservation time of the amomun kravanh volatile oil can be prolonged effectively; and furthermore, the preparation for the amomun kravanh volatile oil microcapsule by using the ultrasonic is simple, quick and feasible.

Description

A kind of method of utilizing ultrasonic wave to prepare Amomum cardamomum volatile oil microcapsules
Technical field
The invention belongs to the spice manufacture field, relate to a kind of method of utilizing ultrasonic wave to prepare Amomum cardamomum volatile oil microcapsules.
Background technology
Amomum cardamomum is the dry mature fruit of zingiberaceous plant Amomum cardamomum (Amomum Kravanh Pirre Ex Grgnep.) or amomum compactum Soland ex Maton (Amomum Compactum Soland ex Maton), main product is in states such as Malaysia, Indonesia, Sri Lanka, also produce in the West Indies in addition, in recent years in Guangxi, Hainan large tracts of land introduces a fine variety, but still take import as excellent.Its flavor is hot, warm in nature, the dampness elimination promoting the circulation of qi, and warming middle energizer to stop vomiting, appetite-stimulating indigestion-relieving, volatile oil have antibechic, eliminate the phlegm, relieving asthma, antibiotic effect.
Microcapsules technology refers to utilize natural or synthesized polymer material, and with solid, the liquid that disperses, or even gaseous matter wraps up, and forms the technology of the fine particle with semi permeability or sealing cyst membrane.The process of parcel is microencapsulation, and the fine particle of formation is called microcapsules.Can realize many purposes behind the microencapsulation: improve the physical property (color, outward appearance, apparent density, dissolubility) that is wrapped material, make material avoid the impact of environment, improve the stability of material, shielding taste and smell, reduce material toxicity, with inconsistent material isolation, control as required the release of material, etc.
Amomum cardamomum volatile oil is in storage process, and some volatile component can change, and particularly when temperature was high, its harmful variation was more obvious.Therefore in order to expand its range of application, avoid loss of effective components, adopt microcapsules technology that oil is become pressed powder by liquid state, greatly keep its fragrance ingredient, thereby enlarge it in the range of application of food industry.
Summary of the invention
The preparation method who the purpose of this invention is to provide a kind of Amomum cardamomum volatile oil microcapsules, i.e. a kind of method of utilizing ultrasonic wave to prepare Amomum cardamomum volatile oil microcapsules.
For achieving the above object, the present invention adopts following technical scheme: at first take beta-schardinger dextrin-as the wall material, it is joined the mass ratio that is prepared into beta-schardinger dextrin-and water in 70 ℃~90 ℃ the hot water is the solution of 8g/100g~12g/100g, stirs for subsequent use until completely dissolved; Next mass ratio of controlling beta-schardinger dextrin-and core-Amomum cardamomum volatile oil is 10g/g~14g/g, after while stirring Amomum cardamomum volatile oil being joined mentioned solution, adopting the beta-schardinger dextrin-aqueous solution that high-pressure homogeneous equipment will add Amomum cardamomum volatile oil is that 60 ℃~90 ℃, pressure are homogeneous 2~3 times under the condition of 15MPa~25MPa in temperature, each homogeneous 3min~5min gets emulsion; Then this emulsion is put into ultrasonic device, ultrasonic 60min~80min under the condition of control ultrasonic power 50W~100W, ultrasonic temperature 50 C~70 ℃ and dutycycle 5s/5s; Subsequently the emulsion after ultrasonic being put into temperature is that 0 ℃~4 ℃ refrigerator and cooled are hidden 24h, adopts Medium speed filter paper to filter under vacuum 0.08MPa~0.10MPa and 5 ℃~35 ℃ conditions of temperature the refrigeration liquid after the refrigeration, gets filter cake; At last with filter cake freeze drier vacuum less than 20Pa, condenser temperature-45 ℃~-60 ℃ conditions under drying totally, get Amomum cardamomum volatile oil microcapsule product.The microcapsule embedded rate of Amomum cardamomum volatile oil is greater than 70%.
Owing to having adopted above technical scheme, the present invention has the following advantages:
1, the prepared Amomum cardamomum volatile oil microcapsules of the present invention are a kind of pressed powders, and the method can separate the air of Amomum cardamomum volatile oil with the external world, has avoided the volatilization of Amomum cardamomum volatile oil, can effectively prolong the holding time of Amomum cardamomum volatile oil;
2, the present invention utilizes ultrasonic wave to prepare Amomum cardamomum volatile oil microcapsules, and is easy and simple to handle, quick, feasible.
The specific embodiment
The invention will be further elaborated by the following examples:
Embodiment 1:
At first take beta-schardinger dextrin-as the wall material, it is joined the mass ratio that is prepared into beta-schardinger dextrin-and water in 80 ℃ the hot water is the solution of 10g/100g, stirs for subsequent use until completely dissolved; Next mass ratio of controlling beta-schardinger dextrin-and core-Amomum cardamomum volatile oil is 10g/g, after while stirring Amomum cardamomum volatile oil being joined mentioned solution, adopting the beta-schardinger dextrin-aqueous solution that high-pressure homogeneous equipment will add Amomum cardamomum volatile oil is that 70 ℃, pressure are homogeneous 3 times under the condition of 20MPa in temperature, each homogeneous 4min gets emulsion; Then this emulsion is put into ultrasonic device, ultrasonic 60min under the condition of control ultrasonic power 75W, 55 ℃ of ultrasonic temperature and dutycycle 5s/5s; Subsequently the emulsion after ultrasonic being put into temperature is that 1 ℃ of refrigerator and cooled is hidden 24h, adopts Medium speed filter paper to filter under vacuum 0.08MPa and 28 ℃ of conditions of temperature the refrigeration liquid after the refrigeration, gets filter cake; At last with filter cake freeze drier vacuum less than 20Pa, condenser temperature-50 ℃ condition under drying totally, get Amomum cardamomum volatile oil microcapsule product.
The mensuration of microcapsules sample embedding rate:
(1) microcapsule product surface Determination of oil:
Accurately take by weighing the 2g microcapsule product, divide 3 addings with the benzinum of 50ml, each evenly vibration, filter, merging filtrate, concentrated with the Rotary Evaporators rotation, draw the quality of product surface oil with weight reduction.
(2) the total Determination of oil of microcapsule product:
Make solvent with benzinum, accurately take by weighing microcapsule product 2g, measure its total oil content with the Soxhlet extraction process.
(3) calculating of embedding rate
Amomum cardamomum volatile oil microcapsule product by above-mentioned technique preparation is carried out the mensuration of embedding rate, the result is 77.68%.
Embodiment 2:
At first take beta-schardinger dextrin-as the wall material, it is joined the mass ratio that is prepared into beta-schardinger dextrin-and water in 85 ℃ the hot water is the solution of 9g/100g, stirs for subsequent use until completely dissolved; Next mass ratio of controlling beta-schardinger dextrin-and core-Amomum cardamomum volatile oil is 13g/g, after while stirring Amomum cardamomum volatile oil being joined mentioned solution, adopting the beta-schardinger dextrin-aqueous solution that high-pressure homogeneous equipment will add Amomum cardamomum volatile oil is that 80 ℃, pressure are homogeneous 3 times under the condition of 15MPa in temperature, each homogeneous 5min gets emulsion; Then this emulsion is put into ultrasonic device, ultrasonic 80min under the condition of control ultrasonic power 50W, 65 ℃ of ultrasonic temperature and dutycycle 5s/5s; Subsequently the emulsion after ultrasonic being put into temperature is that 2 ℃ of refrigerator and cooled are hidden 24h, adopts Medium speed filter paper to filter under vacuum 0.10MPa and 30 ℃ of conditions of temperature the refrigeration liquid after the refrigeration, gets filter cake; At last with filter cake freeze drier vacuum less than 20Pa, condenser temperature-45 ℃ condition under drying totally, get Amomum cardamomum volatile oil microcapsule product.Its embedding rate is 75.66% after measured.
Embodiment 3:
At first take beta-schardinger dextrin-as the wall material, it is joined the mass ratio that is prepared into beta-schardinger dextrin-and water in 90 ℃ the hot water is the solution of 12g/100g, stirs for subsequent use until completely dissolved; Next mass ratio of controlling beta-schardinger dextrin-and core-Amomum cardamomum volatile oil is 12g/g, after while stirring Amomum cardamomum volatile oil being joined mentioned solution, adopting the beta-schardinger dextrin-aqueous solution that high-pressure homogeneous equipment will add Amomum cardamomum volatile oil is 90 ℃, for the first time pressure 25MPa, homogeneous 2 times under the condition of pressure 20MPa for the second time in temperature, each homogeneous 3min gets emulsion; Then this emulsion is put into ultrasonic device, ultrasonic 70min under the condition of control ultrasonic power 100W, ultrasonic temperature 70 C and dutycycle 5s/5s; Subsequently the emulsion after ultrasonic being put into temperature is that 4 ℃ of refrigerator and cooled are hidden 24h, adopts Medium speed filter paper to filter under vacuum 0.09MPa and 25 ℃ of conditions of temperature the refrigeration liquid after the refrigeration, gets filter cake; At last with filter cake freeze drier vacuum less than 20Pa, condenser temperature-55 ℃ condition under drying totally, get Amomum cardamomum volatile oil microcapsule product.Its embedding rate is 73.87% after measured.

Claims (1)

1. method of utilizing ultrasonic wave to prepare Amomum cardamomum volatile oil microcapsules, it is characterized in that: at first take beta-schardinger dextrin-as the wall material, it is joined the mass ratio that is prepared into beta-schardinger dextrin-and water in 70 ℃~90 ℃ the hot water is the solution of 8g/100g~12g/100g, stirs for subsequent use until completely dissolved; Next mass ratio of controlling beta-schardinger dextrin-and core Amomum cardamomum volatile oil is 10g/g~14g/g, Amomum cardamomum volatile oil is joined mentioned solution after, homogeneous gets emulsion; Then this emulsion is put into ultrasonic device, ultrasonic 60min~80min under the condition of control ultrasonic power 50W~100W, ultrasonic temperature 50 C~70 ℃ and dutycycle 5s/5s; At last refrigeration, suction filtration, freeze drying get Amomum cardamomum volatile oil microcapsule product; The microcapsule embedded rate of Amomum cardamomum volatile oil is greater than 70%;
Described homogeneous is that to adopt the beta-schardinger dextrin-aqueous solution that high-pressure homogeneous equipment will add Amomum cardamomum volatile oil be that 60 ℃~90 ℃, pressure are homogeneous 2~3 times under the condition of 15MPa~25MPa, at every turn homogeneous 3min~5min in temperature;
Described refrigeration is that the emulsion after ultrasonic is put into temperature is that 0 ℃~4 ℃ refrigerator and cooled are hidden 24h;
Described suction filtration is to adopt Medium speed filter paper to filter under vacuum 0.08MPa~0.10MPa and 5 ℃~35 ℃ conditions of temperature the refrigeration liquid after the refrigeration, gets filter cake;
Described freeze drying be with filter cake freeze drier vacuum less than 20Pa, condenser temperature-45 ℃~-60 ℃ conditions under drying totally, get Amomum cardamomum volatile oil microcapsule product.
CN2011102899545A 2011-09-22 2011-09-22 Method for preparing amomun kravanh volatile oil microcapsule by using ultrasonic Expired - Fee Related CN102342471B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011102899545A CN102342471B (en) 2011-09-22 2011-09-22 Method for preparing amomun kravanh volatile oil microcapsule by using ultrasonic

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011102899545A CN102342471B (en) 2011-09-22 2011-09-22 Method for preparing amomun kravanh volatile oil microcapsule by using ultrasonic

Publications (2)

Publication Number Publication Date
CN102342471A CN102342471A (en) 2012-02-08
CN102342471B true CN102342471B (en) 2013-04-10

Family

ID=45541849

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011102899545A Expired - Fee Related CN102342471B (en) 2011-09-22 2011-09-22 Method for preparing amomun kravanh volatile oil microcapsule by using ultrasonic

Country Status (1)

Country Link
CN (1) CN102342471B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104017639B (en) * 2014-06-25 2016-04-13 贵州大学 A kind of production method of Vegetable oil lipoprotein microcapsule
CN106377358A (en) * 2016-08-29 2017-02-08 中天(中国)工业有限公司 Low-sensitized absorptive article containing enzymes

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101574523A (en) * 2008-05-09 2009-11-11 北京因科瑞斯医药科技有限公司 Inclusion compound of water-soluble derivatives of cyclodextrin of volatile oil and preparation method thereof
CN101757641A (en) * 2009-11-13 2010-06-30 段洪东 Preparation technique of cardamom volatile oil inclusion complex
CN101822713A (en) * 2010-05-06 2010-09-08 茂名学院 Method for preparing pogostemon cablin volatile oil beta-cyclodextrin clathrate compound by ultrasonic method

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102100713B (en) * 2009-12-18 2013-05-08 中国科学院兰州化学物理研究所 Method for preparing water-soluble marigold yellow pigment microcapsules

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101574523A (en) * 2008-05-09 2009-11-11 北京因科瑞斯医药科技有限公司 Inclusion compound of water-soluble derivatives of cyclodextrin of volatile oil and preparation method thereof
CN101757641A (en) * 2009-11-13 2010-06-30 段洪东 Preparation technique of cardamom volatile oil inclusion complex
CN101822713A (en) * 2010-05-06 2010-09-08 茂名学院 Method for preparing pogostemon cablin volatile oil beta-cyclodextrin clathrate compound by ultrasonic method

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
李锦莲等.正交实验法优选草豆蔻挥发油β-环糊精包合工艺.《黑龙江医药科学》.2007,(第05期), *
杨红艳等.β-环糊精包合肉豆蔻挥发油的工艺研究.《中国药业》.2009,(第07期), *
程黎晖等.细辛挥发油β-环糊精包结工艺的研究.《中国中药杂志》.2006,(第11期), *

Also Published As

Publication number Publication date
CN102342471A (en) 2012-02-08

Similar Documents

Publication Publication Date Title
CN103333268B (en) The preparation method of lycium ruthenicum polysaccharide
CN103689552B (en) Flavored low-fat white mushroom crisp chip and preparation method thereof
CN103250783B (en) A kind of method extending walnut kernel storage period
CN103948035A (en) Peony seed oil microcapsules as well as preparation method and application thereof
CN103555417A (en) Low-temperature cold-squeezing method of green camellia oil without damaging nutrient substances
CN102342471B (en) Method for preparing amomun kravanh volatile oil microcapsule by using ultrasonic
CN104472673B (en) A kind of melon and fruit carpopodium preservation method
CN103749812B (en) A kind of processing method of radix tetrastigme tea
CN103931810A (en) Preparation method of instant black tea concentrated juice
CN103555426A (en) Preparation method for cumin essential oil with cooked flavor
CN103444863B (en) Preservation method for blueberries
CN102559383B (en) Preparation method of elsholtzia volatile oil microcapsule
CN102349584B (en) Method for preparing myristica oil microcapsule by utilizing ultrasonic waves
CN104799240A (en) Preparation method of micro-encapsulated scallion oil powder
CN104489609A (en) Seasoning salt and production method thereof
CN104783291B (en) A kind of solid beverage of birch juice and preparation method thereof
CN104292196B (en) One extracts ascorbic method from sweet tea
CN103704377B (en) Preparation method of low-benzopyrene tea oil
CN104498192A (en) Preparation method and application of florists chrysanthemum extract
CN103622134A (en) Method of preparing antioxidant and antibacterial food preservative by using molasses as raw material
CN105532856A (en) Preparation method of fruit and vegetable preservative using millet bran wax
CN101253888A (en) Preparation of natural rice antistaling agent taking ginger aqueous extract as principal ingredient
CN111481645A (en) Method for extracting amomum tsao-ko total flavonoids
CN105660828B (en) A kind of drying and dehydrating method of Buddha's hand Chinese yam
CN106721836B (en) A method of the fresh particle electuary of matrimony vine is prepared using medlar fresh fruit using squeezing method

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130410

Termination date: 20130922