CN1186992C - Tomato product finely processing method - Google Patents

Tomato product finely processing method Download PDF

Info

Publication number
CN1186992C
CN1186992C CNB021245762A CN02124576A CN1186992C CN 1186992 C CN1186992 C CN 1186992C CN B021245762 A CNB021245762 A CN B021245762A CN 02124576 A CN02124576 A CN 02124576A CN 1186992 C CN1186992 C CN 1186992C
Authority
CN
China
Prior art keywords
tomato
lycopene
extract
skin
extraction
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
CNB021245762A
Other languages
Chinese (zh)
Other versions
CN1463623A (en
Inventor
赵文军
吴雪萍
王旭
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.)
Xinjiang Technical Institute of Physics and Chemistry of CAS
Original Assignee
Xinjiang Technical Institute of Physics and Chemistry of CAS
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 Xinjiang Technical Institute of Physics and Chemistry of CAS filed Critical Xinjiang Technical Institute of Physics and Chemistry of CAS
Priority to CNB021245762A priority Critical patent/CN1186992C/en
Publication of CN1463623A publication Critical patent/CN1463623A/en
Application granted granted Critical
Publication of CN1186992C publication Critical patent/CN1186992C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Preparation Of Fruits And Vegetables (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)

Abstract

The present invention relates to a preparation method for further processing tomato products. In the method, low-carbon polar organic solvents containing water are used for extracting tomato concentrate or tomato flavor substances in peel residue, and then, the low polar solvents are used for extracting out lycopene; finally, edible additives enriching diet tomato fiber are obtained. The method can be used for producing highly purified lycopene powder having high yield, the purity of the lycopene powder is larger than 50%, the highest purity can reach 95%, and the present invention can be conveniently applied to medicine and health products. Simultaneously, the tomato flavor substances enriching beta-carotene, xanthophyll and other kinds of carotenoid, other vitamins, organic acids, tomato lipid, flavone, sugar and the aromatic substances of tomatoes can be also produced, and the tomato flavor substances can be used as food additives for the nutrient enrichment or the seasoning of drink and food. In addition, the obtained residue can be directly used or processed as diet fiber in food industry or other industries.

Description

A kind of tomato product deep-processing method
Technical field
The present invention relates to a kind of deep process technology of tomato product, especially to the extraction of tomato flavor thing and lycopene
Background technology
Be extensive use of tomato product in the grocery trade, existing at present several different methods is used for the tomato product of production different cultivars.Because have multiple nutritional components in the tomato, its process technology is the emphasis that people pay close attention to always.
Lycopene is a kind of of carotenoid, have many physiological functions, the discovered in recent years lycopene has the antioxygenic property stronger than other carotenoid, discover that in addition content of lycopene is crossed low relevant with some chronic disease and tumour in the human body, as: prostate cancer, the cancer of the uterus, artery sclerosis etc., also relevant with people's life-span simultaneously, therefore developing lycopene is the big problem that present people pay close attention to.
In the tomato except that being rich in lycopene, also be rich in class carrot vitamin and other vitamins such as beta carotene, lutein, contain organic acid, tomato lipid, oryzanol, flavonoids, sugar and tomato aromatic substance etc. simultaneously, higher nutritive value is arranged, can be used as the tomato flavor material and be used for beverage and food additives such as flavouring and beverage, cold drink, to strengthen nutrition and the mouthfeel or the performance of food.
At present, abroad openly the patent of tomato deep processing is more, for example, and EP0844831, CN1251745, US5858700, US5965183 etc.Need material through oven dry or freeze drying before in its disclosed method, extracting lycopene, extract with low polar solvent then, and higher in its resulting lycopene extract owing to resin object content, for the lycopene that obtains higher degree also needs complicated aftertreatment technology.In order to reduce the resin object of lycopene extract, a kind of sig water treatment process of using has earlier been proposed among the Chinese patent CN1298904.Obviously need special-purpose drying equipment in the method to many reported in literature, and fail tomato is more comprehensively fully utilized.
The existing tomato in China plantation and the processing place of production because special region, climatic factor makes that the content of lycopene of its tomato is higher, become the strongest raw material of lycopene processing mainly in western part.For this reason, the present invention proposes a kind of production method that fully utilizes the tomato product deep processing of tomato production high-purity lycopene powder, tomato flavor thing and dietary fiber after testing through years of researches.
Summary of the invention
The object of the invention is, a kind of tomato product deep-processing method is provided, this method at first utilizes moisture low-carbon (LC) polar organic solvent to extract tomato flavor thing in tomato concentrate or the skin slag, utilize low polar solvent to extract lycopene then, obtain being rich in the edible additive of tomato dietary fiber at last.Utilize this method high produced in yields to go out highly purified lycopene powder, its purity reaches as high as 95% greater than 50%, can be conveniently used in medicine, the health products.Also can produce the tomato flavor thing of carotenoid such as being rich in beta carotene, lutein and other vitamin, organic acid, tomato lipid, flavones, sugar and tomato aromatic substance simultaneously, can be used as fortification or seasoning that food additives are applied to the diet product.In addition also can be directly or after processing, be used for food or other industry as dietary fiber with the residue that obtains.
Tomato product deep-processing method of the present invention follows these steps to carry out:
The extraction of a, tomato flavor thing
At first utilize directly to mix with miscible organic low-carbon alcohols, the ketone solvent of water and carry out lixiviate with the wet tomato skin of tomato concentrate or pulverizing, wherein organic low-carbon alcohols is methyl alcohol or ethanol, ketone is acetone or butanone, solid-liquid ratio is 1: 1.5-1: 10, the moisture content that mixes the total material in back is controlled at 5%-40%, extraction temperature is 50 ℃-90 ℃, the lixiviate mode adopts single jar of extracted many times or the lixiviate of multiple tank adverse current, also can adopt continuous extraction equipment, obtain corresponding extract, through being evaporated near doing, the paste behind the decompression desolventizing is the tomato flavor thing; For the ease of the slag charge drying, can be with isolated slag charge with organic low-carbon alcohols, ketone solvent in normal temperature-85 ℃ direct drip washing solid slag, leacheate and extract merge, and are evaporated near doing, the paste behind the decompression desolventizing gets the tomato flavor thing; The tomato flavor thing can be directly used in the allotment of tomato drink or cold drink, then with remaining solid slag under 400-600Pa pressure, 50 ℃-85 ℃ of temperature heating decompression removes residual organic solvent, and can to obtain red recrement standby;
The extraction of b, lycopene
The recrement that obtains is added low polar organic solvent acetone or butanone or ether or propyl ether or ethyl acetate or benzinum or carrene, solid-liquid ratio is 1: 2-1: 8, extract in 50 ℃-85 ℃ heating, extracting mode adopts single jar of extracted many times or the lixiviate of multiple tank adverse current, direct crystallization was separated out crystal after isolated extract concentrated through reducing pressure, or in the crystallization feed liquid, add the absolute ethyl alcohol of 1-2 times of volume, promote the red crystallization of tomato to separate out, can obtain lycopene powder by washing, vacuum drying through isolated lycopene;
C, with remaining residue under 2000-5000Pa pressure, remove solvent under 60 ℃ of-85 ℃ of heating conditions of temperature, be white or faint yellow easy moisture absorption powder material through the recrement behind the desolventizing, this material is rich in tomato dietary fiber.
The tomato concentrate is the moisture tomato concentrate or the moisture tomato solid content of bright tomato after making beating, separation skin seed, centrifugal dehydration of finished product or semi-finished product catsup or tomato meal or the processing of other method; Tomato skin is the tomato skin after skin or seed separate.
The specific embodiment
Embodiment 1
The extraction of a, tomato flavor thing
After mixing, 7 liter of 95% food grade ethanol carries out stirring and leaching with adding in 4 kilograms of commercial finished product catsup, the moisture content about 35% that mixes the total material in back, extraction temperature is 50 ℃, 15 minutes time, the lixiviate mode adopts single jar repeatedly to extract, after telling extract, the food grade ethanol that in the slag charge of isolating the extract first time, adds 2 liter 95% again, in 50 ℃ of heating, stirred 20 minutes, after isolating secondary raffinate, use 1 liter of 95% food grade ethanol in the direct drip washing solid slag of normal temperature again, leacheate and preceding secondary raffinate merge, and are evaporated near doing, paste behind the decompression desolventizing is tomato flavor thing 820 grams, can be directly used in the allotment of tomato drink or cold drink; Then with the solid slag of gained under 400Pa pressure, 75 ℃ of heating decompressions of temperature remove residual ethanol, and can to obtain red recrement 327 grams standby.
The extraction of b, lycopene
The recrement 327 that obtains is restrained the low polar organic solvent ethyl acetate that adds 950 milliliters, in 80 ℃ of water-baths, added hot reflux 25 minutes, after hot pressing leaches extract, use 2 * 700 milliliters of food grade ethyl acetate in 80 ℃ of water-baths, to add hot reflux 25 minutes again, extract secondary respectively, isolated extract and extract merging for the first time, being evaporated to 50 milliliters promptly has lycopene crystal to separate out, the absolute ethyl alcohol that in the crystallization feed liquid, adds 1 times of volume then again, promote the red crystallization of tomato to separate out, the suction filtration solid is through washing, vacuum drying can obtain lycopene powder 1.9 grams.With thin-layer chromatography (TLC) analysis is single spot, and measuring its purity with high pressure lipuid chromatography (HPLC) (HPLC) is 91.3%; Crystalline mother solution through concentrate 15 gram resin object, this resin object contains a spot of lycopene.
C, again with remaining residue under 2000Pa pressure, remove organic solvent under 70 ℃ of heating conditions of temperature, be easily moisture absorption powder materials of 306 gram whites through the recrement behind the desolventizing, this material is rich in tomato dietary fiber.
Embodiment 2
The extraction of a, tomato flavor thing
Acetone mixing carrying out lixiviate with 40 liter 85% of 4 kilograms of tomato meals adding, the moisture content 15% that mixes the total material in back, extraction temperature is 50 ℃, 20 minutes time, the lixiviate mode adopts continuous extraction equipment, leaching liquor is through being evaporated near doing, and the paste behind the decompression desolventizing is 3 kilograms of tomato flavor things, and the tomato flavor thing can be directly used in the allotment of tomato drink or cold drink.
The extraction of b, lycopene
With the each respectively organic solvent-acetone that adds 10 liters of the recrement that obtains, in 65 ℃ of water-baths, added hot reflux 25 minutes, extract secondary, hot pressing leaches extract, isolated extract merges, and decompression has lycopene crystal to separate out after concentrating, and adds the absolute ethyl alcohol of 1.5 times of volumes then in the crystallization feed liquid again, promote the red crystallization of tomato to separate out, isolated lycopene can obtain lycopene powder through washing, vacuum drying.
C, again with remaining residue under 3000Pa pressure, remove solvent under 70 ℃ of heating conditions of temperature, be faint yellow easy moisture absorption powder material through the recrement behind the desolventizing, this material is rich in tomato dietary fiber.
Embodiment 3
The extraction of a, tomato flavor thing
With the methyl alcohol lixiviate of the moisture tomato solid content of 40 kilograms of bright tomatoes after making beating, separation skin seed, centrifugal dehydration with 15 liters, the moisture content that mixes the total material in back is controlled at 5%-25%, and extraction temperature is 45 ℃, and the lixiviate mode adopts the multiple tank adverse current; Isolated extract is through being evaporated near doing, and the desolventizing that reduces pressure again obtains paste and is the tomato flavor thing, can be directly used in the allotment of tomato drink or cold drink; Then with remaining solid slag under 600Pa pressure, 65 ℃ of temperature heating decompression removes residual solvent, and can to obtain red recrement standby.
The extraction of b, lycopene
The low polar organic solvent benzinum that the recrement that obtains is added 1500 milliliters, in 85 ℃ of water-baths, added hot reflux 30 minutes, after hot pressing leaches extract, in 85 ℃ of water-baths, added hot reflux 25 minutes with 1200 milliliters of benzinums again, extract secondary respectively, isolated extract and extract merging for the first time, decompression has lycopene crystal to separate out after concentrating, and isolated lycopene can obtain lycopene powder through washing, vacuum drying.
C, again with remaining residue under 5000Pa pressure, remove solvent under 85 ℃ of heating conditions of temperature, be the easy moisture absorption powder material of white through the recrement behind the desolventizing, this material is rich in tomato dietary fiber.
Embodiment 4
The extraction of a, tomato flavor thing
Wet tomato skin after 4 kilograms of pulverizing mixed with 15 liters of butanone carry out lixiviate, the moisture content that mixes the total material in back is controlled at 40%, extraction temperature is 45 ℃, 30 minutes time, the lixiviate mode adopts single jar repeatedly to extract, isolating for the first time, the skin slag of extract adds 8 liters of butanone again, in 45 ℃ of heating, stirred 30 minutes, isolate secondary raffinate after, use 1 liter of butanone in the direct drip washing solid slag of normal temperature again, leacheate and preceding secondary raffinate merge, be evaporated near doing, the paste behind the decompression desolventizing is the tomato flavor thing, can be directly used in the allotment of tomato drink or cold drink; Then with remaining solid slag under 600Pa pressure, 85 ℃ of temperature heating decompression removes residual solvent, and can to obtain red recrement standby.
The extraction of b, lycopene
The low polar organic solvent carrene that the recrement that obtains is added 1100 milliliters, in 65 ℃ of water-baths, added hot reflux 35 minutes, after hot pressing leaches extract, in 60 ℃ of water-baths, added hot reflux 45 minutes with 1200 milliliters of carrene again, extract secondary respectively, isolated extract and extract merging for the first time, decompression has lycopene crystal to separate out after concentrating, the absolute ethyl alcohol that in crystalline mother solution, adds 2 times of volumes then again, promote the red crystallization of tomato to separate out, isolated lycopene can obtain lycopene powder through washing, vacuum drying.

Claims (2)

1, a kind of tomato product deep-processing method is characterized in that following these steps to carrying out:
The extraction of a, tomato flavor thing
At first utilize directly to mix with miscible organic low-carbon alcohols, the ketone solvent of water and carry out lixiviate with the wet tomato skin of tomato concentrate or pulverizing, wherein organic low-carbon alcohols is methyl alcohol or ethanol, ketone is acetone or butanone, solid-liquid ratio is 1: 1.5-1: 10, the moisture content that mixes the total material in back is controlled at 5%-40%, extraction temperature is 50 ℃-90 ℃, the lixiviate mode adopts single jar of extracted many times or the lixiviate of multiple tank adverse current, also can adopt continuous extraction equipment, obtain corresponding extract, through being evaporated near doing, the paste behind the decompression desolventizing is the tomato flavor thing; For the ease of the slag charge drying, can be with isolated slag charge with organic low-carbon alcohols, ketone solvent in normal temperature-85 ℃ direct drip washing solid slag, leacheate and extract merge, and are evaporated near doing, the paste behind the decompression desolventizing gets the tomato flavor thing; The tomato flavor thing can be directly used in the allotment of tomato drink or cold drink, then with remaining solid slag under 400-600Pa pressure, 50 ℃-85 ℃ of temperature heating decompression removes residual organic solvent, and can to obtain red recrement standby;
The extraction of b, lycopene
The recrement that obtains is added low polar organic solvent acetone or butanone or ether or propyl ether or ethyl acetate or benzinum or carrene, solid-liquid ratio is 1: 2-1: 8, extract in 50 ℃-85 ℃ heating, extracting mode adopts single jar of extracted many times or the lixiviate of multiple tank adverse current, direct crystallization was separated out crystal after isolated extract concentrated through reducing pressure, or in the crystallization feed liquid, add the absolute ethyl alcohol of 1-2 times of volume, promote the red crystallization of tomato to separate out, can obtain lycopene powder by washing, vacuum drying through isolated lycopene;
C, with remaining residue under 2000-5000Pa pressure, remove solvent under 60 ℃ of-85 ℃ of heating conditions of temperature, be white or faint yellow easy moisture absorption powder material through the recrement behind the desolventizing, this material is rich in tomato dietary fiber.
2, tomato product deep-processing method according to claim 1, the tomato concentrate that it is characterized in that indication in a step are the moisture tomato concentrate or the moisture tomato solid content of bright tomato after making beating, separation skin seed, centrifugal dehydration of finished product or semi-finished product catsup or tomato meal or the processing of other method; Tomato skin is the tomato skin after skin or seed separate.
CNB021245762A 2002-06-20 2002-06-20 Tomato product finely processing method Expired - Fee Related CN1186992C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB021245762A CN1186992C (en) 2002-06-20 2002-06-20 Tomato product finely processing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB021245762A CN1186992C (en) 2002-06-20 2002-06-20 Tomato product finely processing method

Publications (2)

Publication Number Publication Date
CN1463623A CN1463623A (en) 2003-12-31
CN1186992C true CN1186992C (en) 2005-02-02

Family

ID=29743854

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB021245762A Expired - Fee Related CN1186992C (en) 2002-06-20 2002-06-20 Tomato product finely processing method

Country Status (1)

Country Link
CN (1) CN1186992C (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101823934B (en) * 2010-04-16 2013-05-29 蒲陆梅 Novel process for extracting high-purity lycopene from tomato
CN103919067A (en) * 2014-04-02 2014-07-16 浙江小二黑食品有限公司 New method for preparing tomato powder
CN105341583A (en) * 2015-11-19 2016-02-24 中粮屯河股份有限公司 Lycopene fiber and lycopene oil resin, and preparation methods thereof
CN105942327B (en) * 2016-05-20 2022-12-13 江南大学 Tomato powder product characterized by three highs of lycopene and preparation method thereof
CN106479671A (en) * 2016-12-02 2017-03-08 晨光生物科技集团股份有限公司 A kind of technique producing Tomato Seed crude oil using wet Fructus Lycopersici esculenti seed peel slag
CN107467573A (en) * 2017-08-25 2017-12-15 武汉华康臣生物科技有限公司 A kind of lycopene extraction method and special diet tomato nutrient powder
CN110710662A (en) * 2019-11-20 2020-01-21 合肥工业大学 Processing technology of tomato powder rich in cis-lycopene
CN112120225B (en) * 2020-09-29 2023-03-10 江南大学 Resource utilization method for incompletely ripe tomatoes
CN115316665A (en) * 2022-06-24 2022-11-11 万宝甲由(北京)科技有限责任公司 Composition preparation containing water-soluble dietary fiber of tomato and lycopene and preparation method thereof

Also Published As

Publication number Publication date
CN1463623A (en) 2003-12-31

Similar Documents

Publication Publication Date Title
CN101948897B (en) Method for extracting shinyleaf yellowhorn oil, shinyleaf yellowhorn polysaccharide and shinyleaf yellowhorn protolysate peptide from shinyleaf yellowhorn
CN106805180A (en) A kind of method that polyphenol substance is extracted in desmoenzyme and the ultrasonically treated endotesta walnut kernel by band
CN101288496A (en) Health-care composite beverage
CN1186992C (en) Tomato product finely processing method
CN110746515B (en) Lycium barbarum polysaccharide, lycium barbarum red element and lycium barbarum polypeptide prepared by synchronous separation and preparation method thereof
CN101429347A (en) Process for producing beet red pigment
CN105996028B (en) Ginger extract, ginger fiber and preparation method of ginger extract and ginger fiber
CN1530376A (en) Extraction of eight products, such as pectine, naringin, etc.
CN107616397A (en) A kind of compound bee honey drink of ganoderma lucidum cordyceps sinensis and preparation method thereof
CN109646502A (en) One kind is rich in flavones Europe Lee fat capsule content and preparation method thereof
CN104366332B (en) A kind of deep working method of chilli seed
CN110150516A (en) A kind of white radishes rice syrup beverage and preparation method
CN103462170B (en) Instant selenium-enriched sweet potato solid beverage and preparing method
CN112314945A (en) Method for preparing high-activity cranberry extract by sectional extraction method
CN104365842A (en) Coconut shred yoghourt capable of dispelling effects of alcohol, protecting liver and improving eyesight and preparation method of coconut shred yoghourt capable of dispelling effects of alcohol, protecting liver and improving eyesight
CN101611878A (en) The preparation method of carotenoids in the Momordica cochinchiensis fruit
CN104223077B (en) Sea shrimp lemon smell of vinegar dendrobium candidum particle electuary and preparation method thereof
EP2796058B1 (en) Antioxidant ingredient with low calorie content, method for obtaining same and use thereof
CN103535835B (en) Solid beverage prepared by a kind of pollen soluble extract
CN109770353A (en) Deep-sea fish oil soft capsules and preparation method thereof
CN1180710C (en) Method of producing natural nutrient food with stabilized rice bran
AU2018100981A4 (en) Sweet potato sitosterol glucoside saturated fatty acid ester, extract, preparation methods and application thereof
CN1121519A (en) Food melanin extracting method
Ahmed et al. Apple Wastes and By-Products: Chemistry, Processing, and Utilization
CN110923053A (en) Method for extracting tea oil with high freezing resistance

Legal Events

Date Code Title Description
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
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
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee