CN114045198A - Muskmelon distillation extraction method applied to muskmelon wine - Google Patents
Muskmelon distillation extraction method applied to muskmelon wine Download PDFInfo
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- 235000009847 Cucumis melo var cantalupensis Nutrition 0.000 title claims abstract description 124
- 235000014101 wine Nutrition 0.000 title claims abstract description 77
- 238000004821 distillation Methods 0.000 title claims abstract description 36
- 238000000605 extraction Methods 0.000 title claims abstract description 16
- 244000241257 Cucumis melo Species 0.000 title 2
- 244000064895 Cucumis melo subsp melo Species 0.000 claims abstract description 122
- 238000000034 method Methods 0.000 claims abstract description 25
- 238000010438 heat treatment Methods 0.000 claims abstract description 20
- 235000009467 Carica papaya Nutrition 0.000 claims description 17
- 241000219173 Carica Species 0.000 claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 238000007599 discharging Methods 0.000 claims description 7
- 230000032683 aging Effects 0.000 claims description 6
- 235000006264 Asimina triloba Nutrition 0.000 claims description 4
- 240000006432 Carica papaya Species 0.000 claims description 4
- 241001608711 Melo Species 0.000 claims description 2
- 239000003205 fragrance Substances 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 2
- 239000000796 flavoring agent Substances 0.000 abstract description 2
- 235000019634 flavors Nutrition 0.000 abstract description 2
- 230000000052 comparative effect Effects 0.000 description 15
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 9
- 241000196324 Embryophyta Species 0.000 description 4
- 239000000126 substance Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- -1 Hexanoic acid ethyl ester Ethyl acetate Butyric acid ethyl ester Lactic acid ethyl ester Hexanoic acid Chemical compound 0.000 description 1
- BTYMTWWNCHIQIZ-UHFFFAOYSA-N acetic acid;butanoic acid Chemical compound CC(O)=O.CC(O)=O.CCCC(O)=O BTYMTWWNCHIQIZ-UHFFFAOYSA-N 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 238000013124 brewing process Methods 0.000 description 1
- 230000008094 contradictory effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 235000019990 fruit wine Nutrition 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000011514 vinification Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12H—PASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
- C12H6/00—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages
- C12H6/02—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages by distillation
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- Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Food Science & Technology (AREA)
- Wood Science & Technology (AREA)
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention provides a muskmelon distillation extraction method applied to a muskmelon wine, which comprises the steps of adding muskmelon wine fermented grains into a first distiller and a plurality of second distiller; the heater heats the first distiller, and the muskmelon fermented grains in the first distiller generate wine steam which enters the connected second distiller through the connecting pipe. According to the invention, the fermented muskmelon grains in the first distiller are directly heated, so that the fermented muskmelon grains in the first distiller are distilled, and in the process of distilling the fermented muskmelon grains in the second distiller, the wine steam generated in the first distiller or the previous second distiller is matched with the heater for double heating, so that the distillation effect of the fermented muskmelon grains is improved, and the wine steam generated in the first distiller or the previous second distiller can be purified, so that the distilled muskmelon wine is rich in wine flavor, the complex fragrance components in the wine is avoided, and the yield and the quality of the fermented muskmelon wine are improved.
Description
Technical Field
The invention relates to the technical field of brewing, in particular to a muskmelon distillation extraction method applied to a muskmelon wine.
Background
The pawpaw is commonly called as shine skin pawpaw, dalong wood, Fengshui tree, muskmelon and plum, and is a unique rare fruit tree species in China; the papaya is a tall deciduous tree which is dry-tolerant and waterlogging-tolerant, does not select soil, and can be grown to 5-7 m in the adult period and the age of the tree is more than one hundred years.
In the brewing process of the papaya wine, the papaya wine has certain defects aiming at the papaya distillation extraction method applied to the papaya wine, so that the water content of the obtained papaya wine is low, and the wine has complicated fragrance components, thus seriously affecting the yield and quality of the wine and being not beneficial to the production of the papaya wine.
Disclosure of Invention
The invention aims to solve the defects and provides a muskmelon distillation and extraction method applied to the muskmelon wine.
In order to solve the technical problems, the invention adopts the following technical scheme: a muskmelon distillation extraction method applied to a muskmelon wine comprises the following steps:
1) adding the fermented pawpaw wine into the first distiller and the second distiller respectively;
2) heating the first distiller, and introducing liquor steam generated by the fermented muskmelon grains in the first distiller into the fermented muskmelon grains in the first second distiller;
3) heating the second distillers, and sequentially introducing the wine steam generated by the fermented muskmelon grains in the previous second distiller into the fermented muskmelon grains in the next second distiller;
4) and introducing the liquor steam generated by the muskmelon fermented grains in the last second distiller into a condenser, and collecting the muskmelon liquor generated in the condenser.
Further, the heating process of the heater comprises the following steps:
step 1, the start phase: distilling at 65-75 deg.C, and storing the collected fructus melo wine water when the wine output is 0.6-0.8% of the fermented grains;
step 2, intermediate stage: distilling at 80-95 deg.C, and storing the collected muskmelon liquor water separately when the liquor output is 50-65% of the muskmelon fermented grains;
Further, the muskmelon wine collected in the step 2 is stored in a tank for more than one year, and then the white spirit is artificially aged.
Further, the method for artificially aging the white spirit includes, but is not limited to, heating or microwave treatment of the white spirit.
Further, the condenser cools the produced muskmelon liquor, so that the temperature of the collected muskmelon liquor is 20-30 ℃.
The utility model provides a distillation plant is applied to be applied to the muskmelon distillation extraction method of muskmelon wine, includes first distiller, a plurality of distiller, heater and condenser, the heater is used for right first distiller and a plurality of the distiller heats, first distiller passes through the connecting pipe intercommunication second distiller and connecting pipe insert the bottom of distiller is a plurality of the distiller sets up according to the preface and passes through the input tube intercommunication, is located the second distiller of rear side and passes through air feed pipe intercommunication condenser, is provided with on the condenser to be used for carrying out the discharging pipe of discharging to the muskmelon wine.
Further, the input pipe is arranged on the front second distiller, and the other end of the conveying pipe is inserted into the bottom of the rear second distiller.
Compared with the prior art, the invention has the following beneficial effects: according to the invention, the fermented muskmelon grains in the first distiller are directly heated, so that the fermented muskmelon grains in the first distiller are distilled, and in the process of distilling the fermented muskmelon grains in the second distiller, the wine steam generated in the first distiller or the previous second distiller is matched with the heater for double heating, so that the distillation effect of the fermented muskmelon grains is improved, and the wine steam generated in the first distiller or the previous second distiller can be purified, so that the distilled muskmelon wine is rich in wine flavor, the complex fragrance components in the wine is avoided, and the yield and the quality of the fermented muskmelon wine are improved.
Drawings
The accompanying drawings, which are incorporated in and constitute a part of this application, illustrate embodiments of the invention and, together with the description, serve to explain the invention and not to limit the invention. In the drawings:
fig. 1 is a schematic diagram of the present invention.
FIG. 2 is a schematic view of a distillation apparatus of the present invention.
In the figure: 1. a first distiller; 2. a second distiller; 3. a heater; 4. a condenser; 5. a connecting pipe; 6. an input tube; 7. an air supply pipe; 8. and (4) discharging the pipe.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. The embodiments and features of the embodiments in the present application may be combined with each other without conflict. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
It should be noted that if directional indications (such as up, down, left, right, front, and back … …) are involved in the embodiment of the present invention, the directional indications are only used to explain the relative positional relationship between the components, the movement situation, and the like in a specific posture, and if the specific posture is changed, the directional indications are changed accordingly.
In addition, if there is a description of "first", "second", etc. in an embodiment of the present invention, the description of "first", "second", etc. is for descriptive purposes only and is not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include at least one such feature. In addition, the meaning of "and/or" appearing throughout includes three juxtapositions, exemplified by "A and/or B" including either A or B or both A and B. In addition, "a plurality" means two or more. In addition, technical solutions between various embodiments may be combined with each other, but must be realized by a person skilled in the art, and when the technical solutions are contradictory or cannot be realized, such a combination should not be considered to exist, and is not within the protection scope of the present invention.
Example 1
A muskmelon distillation extraction method applied to a muskmelon wine comprises the following steps:
1) adding fermented papaya grains into the first distiller 1 and the second distiller 2;
2) heating the first distiller 1, and introducing liquor steam generated by the fermented muskmelon grains in the first distiller 1 into the fermented muskmelon grains in the first second distiller 2;
3) heating the second distillers 2, and sequentially introducing the wine steam generated by the fermented muskmelon grains in the previous second distiller 2 into the fermented muskmelon grains in the next second distiller 2;
4) and (3) introducing the liquor steam generated by the muskmelon fermented grains in the last second distiller (2) into a condenser (4), and collecting the muskmelon liquor generated in the condenser (4).
Further, the heating process of the heater 3 includes the following steps:
step 1, the start phase: the distillation temperature is 65 ℃, and the collected muskmelon liquor is stored independently after the liquor output is 0.6 percent of the muskmelon fermented grains;
step 2, intermediate stage: the distillation temperature is 80 ℃, and the collected muskmelon liquor is stored independently after the liquor output is 50 percent of the muskmelon fermented grains;
Further, the muskmelon wine collected in the step 2 is stored in a full tank for one year, and then the white spirit is artificially aged.
Further, the method for artificially aging the white spirit is to heat the white spirit.
Further, the condenser 4 cools the produced muskmelon liquor, so that the temperature of the collected muskmelon liquor is 20 ℃.
The utility model provides a distillation plant, is applied to be applied to the muskmelon distillation extraction method of muskmelon wine, including first distiller 1, a plurality of second distiller 2, heater 3 and condenser 4, heater 3 is used for right first distiller 1 and a plurality of second distiller 2 heats, first distiller 1 communicates through connecting pipe 5 second distiller 2 and connecting pipe 5 insert the bottom of second distiller 2 is a plurality of second distiller 2 sets up according to the preface and through input tube 6 intercommunication, and the second distiller 2 that is located the rear passes through air feed pipe 7 intercommunication condenser 4, is provided with on the condenser 4 to be used for carrying out exhaust discharging pipe 8 to the muskmelon wine.
Further, the input pipe 6 is provided on the former second distiller 2 and the other end of the delivery pipe is inserted into the bottom of the latter second distiller 2.
Example 2:
a muskmelon distillation extraction method applied to a muskmelon wine comprises the following steps:
1) adding fermented papaya grains into the first distiller 1 and the second distiller 2;
2) heating the first distiller 1, and introducing liquor steam generated by the fermented muskmelon grains in the first distiller 1 into the fermented muskmelon grains in the first second distiller 2;
3) heating the second distillers 2, and sequentially introducing the wine steam generated by the fermented muskmelon grains in the previous second distiller 2 into the fermented muskmelon grains in the next second distiller 2;
4) and (3) introducing the liquor steam generated by the muskmelon fermented grains in the last second distiller (2) into a condenser (4), and collecting the muskmelon liquor generated in the condenser (4).
Further, the heating process of the heater 3 includes the following steps:
step 1, the start phase: the distillation temperature is 70 ℃, and the collected muskmelon liquor is stored independently after the liquor output is 0.7 percent of the muskmelon fermented grains;
step 2, intermediate stage: the distillation temperature is 87 ℃, and the collected muskmelon liquor is stored independently after the liquor output is 57 percent of the muskmelon fermented grains;
Further, the muskmelon wine collected in the step 2 is stored in a tank for two years, and then the white spirit is artificially aged.
Further, the method for artificially aging the white spirit is to heat the white spirit.
Further, the condenser 4 cools the produced muskmelon liquor, so that the temperature of the collected muskmelon liquor is 25 ℃.
The utility model provides a distillation plant, is applied to be applied to the muskmelon distillation extraction method of muskmelon wine, including first distiller 1, a plurality of second distiller 2, heater 3 and condenser 4, heater 3 is used for right first distiller 1 and a plurality of second distiller 2 heats, first distiller 1 communicates through connecting pipe 5 second distiller 2 and connecting pipe 5 insert the bottom of second distiller 2 is a plurality of second distiller 2 sets up according to the preface and through input tube 6 intercommunication, and the second distiller 2 that is located the rear passes through air feed pipe 7 intercommunication condenser 4, is provided with on the condenser 4 to be used for carrying out exhaust discharging pipe 8 to the muskmelon wine.
Further, the input pipe 6 is provided on the former second distiller 2 and the other end of the delivery pipe is inserted into the bottom of the latter second distiller 2.
Example 3:
a muskmelon distillation extraction method applied to a muskmelon wine comprises the following steps:
1) adding fermented papaya grains into the first distiller 1 and the second distiller 2;
2) heating the first distiller 1, and introducing liquor steam generated by the fermented muskmelon grains in the first distiller 1 into the fermented muskmelon grains in the first second distiller 2;
3) heating the second distillers 2, and sequentially introducing the wine steam generated by the fermented muskmelon grains in the previous second distiller 2 into the fermented muskmelon grains in the next second distiller 2;
4) and (3) introducing the liquor steam generated by the muskmelon fermented grains in the last second distiller (2) into a condenser (4), and collecting the muskmelon liquor generated in the condenser (4).
Further, the heating process of the heater 3 includes the following steps:
step 1, the start phase: the distillation temperature is 75 ℃, and the collected muskmelon liquor is stored independently after the liquor output is 0.8 percent of the muskmelon fermented grains;
step 2, intermediate stage: the distillation temperature is 95 ℃, and the collected muskmelon liquor is stored independently after the liquor output is 65 percent of the muskmelon fermented grains;
Further, the muskmelon wine collected in the step 2 is stored in a tank for three years, and then the white spirit is artificially aged.
Further, the method for artificially aging the white spirit is to perform microwave treatment on the white spirit.
Further, the condenser 4 cools the produced muskmelon liquor, so that the temperature of the collected muskmelon liquor is 30 ℃.
The utility model provides a distillation plant, is applied to be applied to the muskmelon distillation extraction method of muskmelon wine, including first distiller 1, a plurality of second distiller 2, heater 3 and condenser 4, heater 3 is used for right first distiller 1 and a plurality of second distiller 2 heats, first distiller 1 communicates through connecting pipe 5 second distiller 2 and connecting pipe 5 insert the bottom of second distiller 2 is a plurality of second distiller 2 sets up according to the preface and through input tube 6 intercommunication, and the second distiller 2 that is located the rear passes through air feed pipe 7 intercommunication condenser 4, is provided with on the condenser 4 to be used for carrying out exhaust discharging pipe 8 to the muskmelon wine.
Further, the input pipe 6 is provided on the former second distiller 2 and the other end of the delivery pipe is inserted into the bottom of the latter second distiller 2.
Comparative example 1:
this comparative example differs from example 2 only in that: the second distiller 2 is not provided with the heater 3.
Comparative example 2:
this comparative example differs from example 2 only in that: the second distiller 2 is not provided.
The muskmelon fermented grains are fermented grains which are obtained by fermenting muskmelon serving as a raw material through a fruit wine making process in the prior art.
The weight of the wine produced in the middle stage of step 2 of the method described in the above three examples and two comparative examples was measured, the alcohol content of the wine sample at 20 ℃ was measured by the alcohol meter method in the national standard GB/T10345-2007 method for analyzing white spirit, and the weight of the wine at 60 ° alcohol content was calculated by referring to the alcohol content, and the results are shown in table 1:
TABLE 1 weight of wine, alcohol and 60% wine
| Weight of wine (kg) | Degree of alcohol (°) | 60 degree folded wine weight (kg) | |
| Example 1 | 50kg | 62.4 | 51.93 |
| Example 2 | 57kg | 74.1 | 73.01 |
| Example 3 | 65kg | 65.7 | 72.61 |
| Comparative example 1 | 57kg | 40.5 | 36.44 |
| Comparative example 2 | 57kg | 60.8 | 57.12 |
As can be seen from Table 1, in comparative example 2 and comparative example 1 and comparative example 2, for the same volume and same quality of fermented muskmelon grains, the alcohol degrees obtained by different methods are different, the alcohol degree of the wine produced by the method of the present invention is significantly higher than that of the comparative example, and the method of example 2 is better when the wine weight is reduced to 60 degrees by comparison.
The contents of the aroma substances in the liquors obtained in the above examples and comparative examples were measured by a conventional gas chromatography, and the results are shown in Table 2:
TABLE 2 fragrance substance content
| Hexanoic acid ethyl ester | Ethyl acetate | Butyric acid ethyl ester | Lactic acid ethyl ester | Hexanoic acid | Acetic acid | Butyric acid | Acetic acid | |
| Example 1 | 6.72 | 3.18 | 0.68 | 5.82 | 0.61 | 0.48 | 0.45 | 0.49 |
| Example 2 | 6.84 | 3.42 | 0.75 | 6.08 | 0.62 | 0.51 | 0.47 | 0.51 |
| Example 3 | 6.52 | 3.61 | 0.78 | 5.93 | 0.55 | 0.54 | 0.49 | 0.5 |
| Comparative example 1 | 6.18 | 3.04 | 0.59 | 5.69 | 0.53 | 0.43 | 0.38 | 0.42 |
| Comparative example 2 | 2.12 | 1.25 | 0.21 | 3.45 | 0.32 | 0.24 | 0.07 | 0.18 |
As can be seen from Table 2, in comparative example 2, the content of the aromatic substances is generally low without the second distiller, that is, it can be confirmed that the method can purify the aroma of alcohol by using a plurality of second distiller, thereby improving the aroma of wine and avoiding the miscellaneous taste of wine.
It will be evident to those skilled in the art that the invention is not limited to the details of the foregoing illustrative embodiments, and that the present invention may be embodied in other specific forms without departing from the spirit or essential attributes thereof. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein.
Claims (7)
1. A muskmelon distillation extraction method applied to a muskmelon wine is characterized by comprising the following steps: the method comprises the following steps:
1) adding fermented pawpaw wine into the first distiller (1) and the second distiller (2) respectively;
2) heating the first distiller (1), and introducing liquor steam generated by the muskmelon fermented grains in the first distiller (1) into the muskmelon fermented grains in the first second distiller (2);
3) heating the second distillers (2), and sequentially introducing the wine steam generated by the fermented muskmelon grains in the previous second distiller (2) into the fermented muskmelon grains in the next second distiller (2);
4) and (3) introducing the liquor steam generated by the muskmelon fermented grains in the last second distiller (2) into a condenser (4), and collecting the muskmelon liquor generated in the condenser (4).
2. The method for distilling and extracting muskmelon applied to papaya wine as claimed in claim 1, wherein the method comprises the following steps: the process of heating by the heater (3) comprises the following steps:
step 1, the start phase: distilling at 65-75 deg.C, and storing the collected fructus melo wine water when the wine output is 0.6-0.8% of the fermented grains;
step 2, intermediate stage: distilling at 80-95 deg.C, and storing the collected muskmelon liquor water separately when the liquor output is 50-65% of the muskmelon fermented grains;
step 3, later stage: the distillation temperature is 100-105 ℃, and the collected muskmelon wine water is stored separately.
3. The method for distilling and extracting muskmelon applied to papaya wine as claimed in claim 2, wherein the method comprises the following steps: and (3) storing the muskmelon wine water collected in the step (2) in a full tank for more than one year, and then carrying out artificial aging on the white spirit.
4. The method for distilling and extracting muskmelon applied to papaya wine as claimed in claim 3, wherein the method comprises the following steps: methods for artificially aging white spirit include, but are not limited to, heating or microwave treatment of white spirit.
5. The method for distilling and extracting the muskmelon applied to the muskmelon wine as claimed in any one of claims 1 to 4, wherein the method comprises the following steps: the condenser (4) cools the produced muskmelon liquor, so that the temperature of the collected muskmelon liquor is 20-30 ℃.
6. A distillation apparatus, characterized by: applied to the muskmelon distillation and extraction method applied to the muskmelon wine as in any one of claims 1 to 5, comprising a first distiller (1), a plurality of second distiller (2), a heater (3) and a condenser (4), wherein the heater (3) is used for heating the first distiller (1) and the plurality of second distiller (2), the first distiller (1) is communicated with the second distiller (2) through a connecting pipe (5), the connecting pipe (5) is inserted into the bottom of the second distiller (2), the plurality of second distiller (2) are sequentially arranged and communicated through an input pipe (6), the second distiller (2) positioned at the rearmost part is communicated with the condenser (4) through an air feed pipe (7), and a discharge pipe (8) for discharging the muskmelon wine is arranged on the condenser (4).
7. Distillation apparatus according to claim 6, wherein: the input pipe (6) is arranged on the front second distiller (2) and the other end of the conveying pipe is inserted into the bottom of the rear second distiller (2).
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| CN107164193A (en) * | 2017-07-03 | 2017-09-15 | 绵竹市剑西酒业有限责任公司 | A kind of bent wine distiller |
| CN208803048U (en) * | 2018-08-16 | 2019-04-30 | 广东誉马庄园葡萄酒业有限公司 | A kind of foreign wine production line |
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