CN101904528A - Method for producing plum juice via plum halogen desalination - Google Patents
Method for producing plum juice via plum halogen desalination Download PDFInfo
- Publication number
- CN101904528A CN101904528A CN 201010227224 CN201010227224A CN101904528A CN 101904528 A CN101904528 A CN 101904528A CN 201010227224 CN201010227224 CN 201010227224 CN 201010227224 A CN201010227224 A CN 201010227224A CN 101904528 A CN101904528 A CN 101904528A
- Authority
- CN
- China
- Prior art keywords
- plum
- halogen
- desalination
- juice
- producing
- 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.)
- Pending
Links
Images
Abstract
The invention provides a method for producing plum juice via plum halogen desalination, comprising the steps of: distilling plum halogen as the raw material under normal pressure to obtain fraction and thick residue, mixing the thick residue with edible alcohol and then extracting at 40 to 60 DEG C, cooling and filtering to obtain filtrate and salt, distilling the obtained filtrate, reclaiming the alcohol to obtain liquid, and merging the obtained fraction and the liquid to obtain the desalinated plum juice. The plum juice can be directly prepared into plum beverage after being diluted, for example, the plum juice can be made into plum wine or plum vinegar via the traditional fermentation technology. The invention has the advantages of stable technology, strong operability, low investment, high benefit and changeable production scale, thereby having very high economic and social benefit and being worthy of popularization and application.
Description
Technical field
The present invention relates to a kind of preparation method of plum juice, especially a kind of method with producing plum juice via plum halogen desalination belongs to the food and drink processing technique field.
Background technology
Plum halogen, promptly fruit plum salt marsh liquid is the discarded object in the plum embryo production process.The fruit plum is being made in the process of plum embryo, is needing with salt salt marsh fruit plum, concrete operations are: the amount that really adds 20～25 kilograms of salt by per 100 kilograms of bright plums, after fresh fruit plum and solid salt mixed, leave standstill the several months, wait to leach plum juice after, plum is pulled out be used to process the plum embryo again.During leaving standstill salt marsh, because the salt marsh effect, most of materials such as organic acid in the fresh fruit plum, sugar, amino acid, trace element, vitamin, flavones are leached, formed fruit plum salt marsh liquid---plum halogen (the former plum juice that contains NaCl20%～25%).Plum halogen is nutritious, has health-care efficacy.Also high just because of plum halogen salt content, add that the recovery and utilization technology difficulty is big etc. all multifactor, ignored its value by numerous plum embryo processing enterprise, usually plum halogen is toppled over, both caused the waste of resource, again ecological environment is worked the mischief.
Summary of the invention
Be comprehensive utilization plum halogen resource, making it turns waste into wealth, and economizes on resources, and protects environment, the invention provides a kind of method of producing plum juice via plum halogen desalination.
The present invention finishes by following technical proposal: a kind of method of producing plum juice via plum halogen desalination is characterized in that it is a raw material with plum halogen, process the following step:
A, plum halogen is distilled to thick liquid under normal pressure, fraction and thick shape residue, afterwards by 1: 1 volume ratio, be that 75～95% edible alcohol mixes with thick shape residue and mass concentration, must mixture;
Mixture to 40～60 of B, heating A step ℃ extracted 20～30 minutes, were cooled to 15～20 ℃ afterwards, filter, filtrate and salt;
C, B step gained filtrate is distilled, isolate liquid and alcohol, alcohol reclaims, filter liquide;
D, A step gained fraction and C step gained filter liquide merged after, promptly get the plum juice after the desalination.
The distillation of described A, C step adopts conventional distillation equipment of the prior art and method to finish.
The extraction of described B step adopts conventional extraction equipment of the prior art and method to finish; Filtration adopts conventional filtration Apparatus and method for of the prior art to finish.
Get the plum beverage after described D step gained plum juice directly dilutes, perhaps after conventional zymotechnique is handled, get plum wine or preserved plum vinegar.
The present invention compared with prior art has following advantage and effect: adopt such scheme, both contaminated environment that prior art can be difficult to handle, the plum halogen of wasting resource again becomes the salt of recyclable utilization, and can be made into preserved plum vinegar, plum beverage, plum wine be rich in the abundant nutrition material, and plum juice with various health care functions, making it turns waste into wealth, the recovery of plum halogen and the difficult problem of comprehensive utilization have fundamentally been solved, can be by the present invention with every 100kg plum halogen, be prepared into 90～95kg plum juice, reclaim simultaneously and obtain 15～25kg salt.Plum juice directly is mixed with the plum beverage after diluting, get plum wine or preserved plum vinegar after existing zymotechnique is handled.Technology of the present invention is stable, and is workable, invest little, high efficiency, production scale is changeable, so has very high economical, societal benefits, should vigorously promote the use.
Description of drawings
Fig. 1 is the present invention's process chart.
The specific embodiment
Below in conjunction with embodiment the present invention is described further.
Embodiment 1
1, be installed under the normal pressure with conventional electrothermic retorting 100 liters of plum halogen be distilled to thick liquid, 71 liters of fractions, in the thick shape residue of remainder, add 25 liters of concentration and be 95% edible alcohol, mixture;
2,1 step gained mixture is sent in the conventional extractor, be heated to 40 ℃ and carry out routine extraction 30 minutes, be cooled to 18 ℃ afterwards, after filtering with cotton, get 22 kilograms of 51 liters of filtrates and salt;
3,2 step gained filtrates are distilled with conventional electrothermic retorting pot after, distill out 25 liters of recovery of alcohol, liquid remaining in the boiler is shifted out, after filtration 21 liters of brown liquids;
4,71 liters of 1 step gained fractions are mixed for 21 liters with 3 step gained brown liquids, about 90 liters of plum juice.
Embodiment 2
1, under normal pressure 1000 milliliters of plum halogen are distilled to thick liquid with conventional distiller, get 730 milliliters of fractions, adding 300 ml concns are 85% edible alcohol in the thick shape residue of remainder, get mixture;
2,1 step gained mixture is sent in the conventional extractor, be heated to 50 ℃ and extracted 20 minutes, be cooled to 20 ℃ afterwards, filter, get 540 milliliters of filtrates and salt 108 grams with cotton;
3,2 step gained filtrates are distilled with conventional electrothermic retorting pot after, distill out 300 milliliters of recovery of alcohol, liquid remaining in the boiler is shifted out, after filtration 210 milliliters of brown liquids;
4,730 milliliters of 1 step gained fractions are mixed for 210 milliliters with 3 step gained brown liquids, 940 milliliters in plum juice.
Claims (4)
1. the method for a producing plum juice via plum halogen desalination is characterized in that it is a raw material with plum halogen, process the following step:
A, plum halogen is distilled to thick liquid under normal pressure, fraction and thick shape residue, afterwards by 1: 1 volume ratio, be that 75～95% edible alcohol mixes with thick shape residue and mass concentration, must mixture;
Mixture to 40～60 of B, heating A step ℃ extracted 20～30 minutes, were cooled to 15～20 ℃ afterwards, filter, filtrate and salt;
C, B step gained filtrate is distilled, isolate liquid and alcohol, alcohol reclaims, filter liquide;
D, A step gained fraction and C step gained filter liquide merged after, promptly get the plum juice after the desalination.
2. the method for producing plum juice via plum halogen desalination as claimed in claim 1 is characterized in that the distillation of described A, C step adopts conventional distillation equipment of the prior art and method to finish.
3. the method for producing plum juice via plum halogen desalination as claimed in claim 1 is characterized in that the extraction of described B step adopts conventional extraction equipment of the prior art and method to finish; Filtration adopts conventional filtration Apparatus and method for of the prior art to finish.
4. the method for producing plum juice via plum halogen desalination as claimed in claim 1 is characterized in that described D step gained plum juice directly gets the plum beverage after the dilution, perhaps after conventional zymotechnique is handled, gets plum wine or preserved plum vinegar.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010227224 CN101904528A (en) | 2010-07-15 | 2010-07-15 | Method for producing plum juice via plum halogen desalination |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010227224 CN101904528A (en) | 2010-07-15 | 2010-07-15 | Method for producing plum juice via plum halogen desalination |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101904528A true CN101904528A (en) | 2010-12-08 |
Family
ID=43260236
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201010227224 Pending CN101904528A (en) | 2010-07-15 | 2010-07-15 | Method for producing plum juice via plum halogen desalination |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101904528A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105326055A (en) * | 2015-11-23 | 2016-02-17 | 广东省农业科学院蚕业与农产品加工研究所 | Greengage bittern essence functional food containing rich phenolic substances and organic acid and preparation method of greengage bittern essence functional food |
| CN109055148A (en) * | 2018-09-30 | 2018-12-21 | 仲恺农业工程学院 | The method of production of plum halogen assembled alcoholic drinks |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1322479A (en) * | 2001-05-11 | 2001-11-21 | 周育红 | Simultaneous candied green plum and green plum wine producing process |
| CN101214074A (en) * | 2007-12-29 | 2008-07-09 | 广东省农业科学院蚕业与农产品加工研究所 | Greengage bittern health care beverage and preparation thereof |
-
2010
- 2010-07-15 CN CN 201010227224 patent/CN101904528A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1322479A (en) * | 2001-05-11 | 2001-11-21 | 周育红 | Simultaneous candied green plum and green plum wine producing process |
| CN101214074A (en) * | 2007-12-29 | 2008-07-09 | 广东省农业科学院蚕业与农产品加工研究所 | Greengage bittern health care beverage and preparation thereof |
Non-Patent Citations (3)
| Title |
|---|
| 《2009 年广东省食品学会年会论文集》 20091231 叶富根等 杨梅腌渍液脱盐及制备浓缩果汁的研究 第268-273页 1-4 , * |
| 《西南大学2006届硕士学位论文》 20061231 黄德民 梅卤无害化处理技术研究 第26页 1-4 , * |
| 《食品科技》 20011231 曾凡骏等 果梅浓缩液的提取工艺研究 第23-24页 1-4 , 第5期 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105326055A (en) * | 2015-11-23 | 2016-02-17 | 广东省农业科学院蚕业与农产品加工研究所 | Greengage bittern essence functional food containing rich phenolic substances and organic acid and preparation method of greengage bittern essence functional food |
| CN109055148A (en) * | 2018-09-30 | 2018-12-21 | 仲恺农业工程学院 | The method of production of plum halogen assembled alcoholic drinks |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105852189B (en) | A kind of method that utilization waste/hypo-tobacco leaf prepares tobacco extract | |
| CN103923749B (en) | Method for extracting Chinese eaglewood essential oil | |
| CN105925381A (en) | High value utilization method of gutter oil | |
| CN112940003B (en) | Method for continuously extracting sweet wormwood essential oil and artemisinin | |
| CN105087166A (en) | Method for extracting Jasminum sambac essential oil | |
| CN101265179A (en) | Technique for purifying lactate | |
| CN104726250B (en) | The brewage process of chestnut flower boy's wine | |
| CN101904528A (en) | Method for producing plum juice via plum halogen desalination | |
| CN1257142C (en) | Preparation for active octacosa alkanol and triaconta alkanol in rice bran | |
| CN102585890B (en) | Separation upgrading method for biological oil | |
| CN102517340A (en) | Process method for separating and drying lees produced in production process of ethanol with potatoes | |
| CN108795612A (en) | A kind of Chinese-wolfberry brandy and its production technology | |
| CN105238565A (en) | Extraction process for garlic essential oil | |
| CN102992951B (en) | Method for preparing high-purity refined methanol by three-tower rectification | |
| CN101029277A (en) | Method for recovering mixed oil by cottonseed protein extracting process | |
| CN101993127A (en) | High-efficiency extractant and extracting method for extracting naphthalenesulfonic acid waste liquid | |
| CN104232454B (en) | The method producing whiskey with waste yeast in beer production | |
| CN105237323B (en) | A kind of method extracting limonene from Fructus Litseae | |
| CN112126504A (en) | Method for extracting camphor oil | |
| CN100357315C (en) | Method for producing poisonless rape seed concentrate protein from coat removed cold pressed cake of rapeseed | |
| CN107162365A (en) | A kind of preparation method and its application method of deoiling of sludge medicament | |
| CN1709542A (en) | Method for extracting flavone substance from leaves of Diospyms kaki by double water-phase extraction | |
| CN101028999A (en) | Method for extracting cottonseed protein and recovering methanol | |
| CN1275931C (en) | Method and equipment for separating butyl acetate from waste water of extractive spent phase in fermentation liquid of penicillin | |
| CN101649127A (en) | Preparation technology of red pigments of red rice |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20101208 |