CN108102859A - A kind of production method and equipment of alkaline functional drinks - Google Patents
A kind of production method and equipment of alkaline functional drinks Download PDFInfo
- Publication number
- CN108102859A CN108102859A CN201711136650.9A CN201711136650A CN108102859A CN 108102859 A CN108102859 A CN 108102859A CN 201711136650 A CN201711136650 A CN 201711136650A CN 108102859 A CN108102859 A CN 108102859A
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- CN
- China
- Prior art keywords
- retort
- valve
- magnesium
- sodium
- calcium
- Prior art date
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- Granted
Links
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 23
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Natural products O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 57
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 29
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 29
- 235000014101 wine Nutrition 0.000 claims abstract description 25
- 238000006243 chemical reaction Methods 0.000 claims abstract description 15
- 239000002994 raw material Substances 0.000 claims abstract description 8
- 239000011573 trace mineral Substances 0.000 claims abstract description 7
- 235000013619 trace mineral Nutrition 0.000 claims abstract description 7
- 239000000284 extract Substances 0.000 claims abstract description 6
- 238000001914 filtration Methods 0.000 claims description 37
- 239000000463 material Substances 0.000 claims description 33
- 239000007787 solid Substances 0.000 claims description 30
- 239000000047 product Substances 0.000 claims description 25
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 22
- 239000007788 liquid Substances 0.000 claims description 18
- 239000011777 magnesium Substances 0.000 claims description 15
- 229910052749 magnesium Inorganic materials 0.000 claims description 15
- 229940091250 magnesium supplement Drugs 0.000 claims description 15
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 claims description 14
- 229930013930 alkaloid Natural products 0.000 claims description 14
- 150000003797 alkaloid derivatives Chemical class 0.000 claims description 14
- -1 polypropylene Polymers 0.000 claims description 14
- 238000009423 ventilation Methods 0.000 claims description 14
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 13
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 12
- 239000011575 calcium Substances 0.000 claims description 12
- 229960005069 calcium Drugs 0.000 claims description 12
- 229910052791 calcium Inorganic materials 0.000 claims description 12
- 239000003795 chemical substances by application Substances 0.000 claims description 12
- 239000011591 potassium Substances 0.000 claims description 11
- 229910052700 potassium Inorganic materials 0.000 claims description 11
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 11
- 235000011181 potassium carbonates Nutrition 0.000 claims description 11
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 10
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 10
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 10
- 150000001413 amino acids Chemical class 0.000 claims description 10
- 239000011734 sodium Substances 0.000 claims description 10
- 229910052708 sodium Inorganic materials 0.000 claims description 10
- 239000013589 supplement Substances 0.000 claims description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 9
- 240000002853 Nelumbo nucifera Species 0.000 claims description 8
- 235000006508 Nelumbo nucifera Nutrition 0.000 claims description 8
- 235000006510 Nelumbo pentapetala Nutrition 0.000 claims description 8
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 8
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 8
- 239000000920 calcium hydroxide Substances 0.000 claims description 8
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 8
- QWDJLDTYWNBUKE-UHFFFAOYSA-L magnesium bicarbonate Chemical compound [Mg+2].OC([O-])=O.OC([O-])=O QWDJLDTYWNBUKE-UHFFFAOYSA-L 0.000 claims description 8
- 239000002370 magnesium bicarbonate Substances 0.000 claims description 8
- 229910000022 magnesium bicarbonate Inorganic materials 0.000 claims description 8
- 235000014824 magnesium bicarbonate Nutrition 0.000 claims description 8
- 235000007319 Avena orientalis Nutrition 0.000 claims description 7
- 238000000605 extraction Methods 0.000 claims description 7
- 235000007558 Avena sp Nutrition 0.000 claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 241000196324 Embryophyta Species 0.000 claims description 6
- 229910052799 carbon Inorganic materials 0.000 claims description 6
- 239000000835 fiber Substances 0.000 claims description 6
- 229960003975 potassium Drugs 0.000 claims description 6
- SCVFZCLFOSHCOH-UHFFFAOYSA-M potassium acetate Chemical compound [K+].CC([O-])=O SCVFZCLFOSHCOH-UHFFFAOYSA-M 0.000 claims description 6
- 238000011144 upstream manufacturing Methods 0.000 claims description 6
- 241000209763 Avena sativa Species 0.000 claims description 5
- 240000000249 Morus alba Species 0.000 claims description 5
- 235000008708 Morus alba Nutrition 0.000 claims description 5
- 235000005035 Panax pseudoginseng ssp. pseudoginseng Nutrition 0.000 claims description 5
- 235000003140 Panax quinquefolius Nutrition 0.000 claims description 5
- 235000002594 Solanum nigrum Nutrition 0.000 claims description 5
- 240000002307 Solanum ptychanthum Species 0.000 claims description 5
- NKWPZUCBCARRDP-UHFFFAOYSA-L calcium bicarbonate Chemical compound [Ca+2].OC([O-])=O.OC([O-])=O NKWPZUCBCARRDP-UHFFFAOYSA-L 0.000 claims description 5
- 229910000020 calcium bicarbonate Inorganic materials 0.000 claims description 5
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 5
- 235000008434 ginseng Nutrition 0.000 claims description 5
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 claims description 5
- 239000000347 magnesium hydroxide Substances 0.000 claims description 5
- 229910001862 magnesium hydroxide Inorganic materials 0.000 claims description 5
- 240000008397 Ganoderma lucidum Species 0.000 claims description 4
- 235000001637 Ganoderma lucidum Nutrition 0.000 claims description 4
- 239000004695 Polyether sulfone Substances 0.000 claims description 4
- 239000004743 Polypropylene Substances 0.000 claims description 4
- NIJJYAXOARWZEE-UHFFFAOYSA-N Valproic acid Chemical compound CCCC(C(O)=O)CCC NIJJYAXOARWZEE-UHFFFAOYSA-N 0.000 claims description 4
- 229920006393 polyether sulfone Polymers 0.000 claims description 4
- 229920001155 polypropylene Polymers 0.000 claims description 4
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 claims description 4
- 229940083542 sodium Drugs 0.000 claims description 4
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims description 3
- AEQDJSLRWYMAQI-UHFFFAOYSA-N 2,3,9,10-tetramethoxy-6,8,13,13a-tetrahydro-5H-isoquinolino[2,1-b]isoquinoline Chemical compound C1CN2CC(C(=C(OC)C=C3)OC)=C3CC2C2=C1C=C(OC)C(OC)=C2 AEQDJSLRWYMAQI-UHFFFAOYSA-N 0.000 claims description 3
- BCZXFFBUYPCTSJ-UHFFFAOYSA-L Calcium propionate Chemical compound [Ca+2].CCC([O-])=O.CCC([O-])=O BCZXFFBUYPCTSJ-UHFFFAOYSA-L 0.000 claims description 3
- 235000000604 Chrysanthemum parthenium Nutrition 0.000 claims description 3
- 241000723375 Colchicum Species 0.000 claims description 3
- 244000247747 Coptis groenlandica Species 0.000 claims description 3
- 235000002991 Coptis groenlandica Nutrition 0.000 claims description 3
- 235000000802 Leonurus cardiaca ssp. villosus Nutrition 0.000 claims description 3
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 3
- 239000006004 Quartz sand Substances 0.000 claims description 3
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 claims description 3
- 241001632005 Xylosalsola richteri Species 0.000 claims description 3
- UVNKIYPMUDFRGV-UHFFFAOYSA-N [Mg].C(CC)(=O)O Chemical compound [Mg].C(CC)(=O)O UVNKIYPMUDFRGV-UHFFFAOYSA-N 0.000 claims description 3
- 239000004330 calcium propionate Substances 0.000 claims description 3
- 235000010331 calcium propionate Nutrition 0.000 claims description 3
- FYPVXEILSNEKOO-UHFFFAOYSA-L calcium;butanoate Chemical compound [Ca+2].CCCC([O-])=O.CCCC([O-])=O FYPVXEILSNEKOO-UHFFFAOYSA-L 0.000 claims description 3
- 239000000919 ceramic Substances 0.000 claims description 3
- 239000013522 chelant Substances 0.000 claims description 3
- 230000001351 cycling effect Effects 0.000 claims description 3
- 239000003599 detergent Substances 0.000 claims description 3
- 239000003456 ion exchange resin Substances 0.000 claims description 3
- 229920003303 ion-exchange polymer Polymers 0.000 claims description 3
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 claims description 3
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 claims description 3
- 239000001095 magnesium carbonate Substances 0.000 claims description 3
- 229910000021 magnesium carbonate Inorganic materials 0.000 claims description 3
- OVGXLJDWSLQDRT-UHFFFAOYSA-L magnesium lactate Chemical compound [Mg+2].CC(O)C([O-])=O.CC(O)C([O-])=O OVGXLJDWSLQDRT-UHFFFAOYSA-L 0.000 claims description 3
- 239000000626 magnesium lactate Substances 0.000 claims description 3
- 235000015229 magnesium lactate Nutrition 0.000 claims description 3
- 229960004658 magnesium lactate Drugs 0.000 claims description 3
- 239000011572 manganese Substances 0.000 claims description 3
- 229910052748 manganese Inorganic materials 0.000 claims description 3
- 230000007246 mechanism Effects 0.000 claims description 3
- 239000012528 membrane Substances 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- AVTYONGGKAJVTE-OLXYHTOASA-L potassium L-tartrate Chemical compound [K+].[K+].[O-]C(=O)[C@H](O)[C@@H](O)C([O-])=O AVTYONGGKAJVTE-OLXYHTOASA-L 0.000 claims description 3
- 235000011056 potassium acetate Nutrition 0.000 claims description 3
- BWILYWWHXDGKQA-UHFFFAOYSA-M potassium propanoate Chemical compound [K+].CCC([O-])=O BWILYWWHXDGKQA-UHFFFAOYSA-M 0.000 claims description 3
- 239000004331 potassium propionate Substances 0.000 claims description 3
- 235000010332 potassium propionate Nutrition 0.000 claims description 3
- 239000001472 potassium tartrate Substances 0.000 claims description 3
- 229940111695 potassium tartrate Drugs 0.000 claims description 3
- 235000011005 potassium tartrates Nutrition 0.000 claims description 3
- 239000004576 sand Substances 0.000 claims description 3
- 235000015424 sodium Nutrition 0.000 claims description 3
- HELHAJAZNSDZJO-OLXYHTOASA-L sodium L-tartrate Chemical compound [Na+].[Na+].[O-]C(=O)[C@H](O)[C@@H](O)C([O-])=O HELHAJAZNSDZJO-OLXYHTOASA-L 0.000 claims description 3
- 239000001632 sodium acetate Substances 0.000 claims description 3
- 235000017281 sodium acetate Nutrition 0.000 claims description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 3
- 235000017550 sodium carbonate Nutrition 0.000 claims description 3
- 239000000176 sodium gluconate Substances 0.000 claims description 3
- 235000012207 sodium gluconate Nutrition 0.000 claims description 3
- 229940005574 sodium gluconate Drugs 0.000 claims description 3
- JXKPEJDQGNYQSM-UHFFFAOYSA-M sodium propionate Chemical compound [Na+].CCC([O-])=O JXKPEJDQGNYQSM-UHFFFAOYSA-M 0.000 claims description 3
- 239000004324 sodium propionate Substances 0.000 claims description 3
- 235000010334 sodium propionate Nutrition 0.000 claims description 3
- 229960003212 sodium propionate Drugs 0.000 claims description 3
- 239000001433 sodium tartrate Substances 0.000 claims description 3
- 229960002167 sodium tartrate Drugs 0.000 claims description 3
- 235000011004 sodium tartrates Nutrition 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 238000000108 ultra-filtration Methods 0.000 claims description 3
- 229960000604 valproic acid Drugs 0.000 claims description 3
- CYDQOEWLBCCFJZ-UHFFFAOYSA-N 4-(4-fluorophenyl)oxane-4-carboxylic acid Chemical compound C=1C=C(F)C=CC=1C1(C(=O)O)CCOCC1 CYDQOEWLBCCFJZ-UHFFFAOYSA-N 0.000 claims description 2
- 229910006367 Si—P Inorganic materials 0.000 claims description 2
- 229940024606 amino acid Drugs 0.000 claims description 2
- 239000004227 calcium gluconate Substances 0.000 claims description 2
- 235000013927 calcium gluconate Nutrition 0.000 claims description 2
- 229960004494 calcium gluconate Drugs 0.000 claims description 2
- NEEHYRZPVYRGPP-UHFFFAOYSA-L calcium;2,3,4,5,6-pentahydroxyhexanoate Chemical compound [Ca+2].OCC(O)C(O)C(O)C(O)C([O-])=O.OCC(O)C(O)C(O)C(O)C([O-])=O NEEHYRZPVYRGPP-UHFFFAOYSA-L 0.000 claims description 2
- 239000013078 crystal Substances 0.000 claims description 2
- 239000001755 magnesium gluconate Substances 0.000 claims description 2
- 235000015778 magnesium gluconate Nutrition 0.000 claims description 2
- 229960003035 magnesium gluconate Drugs 0.000 claims description 2
- IAKLPCRFBAZVRW-XRDLMGPZSA-L magnesium;(2r,3s,4r,5r)-2,3,4,5,6-pentahydroxyhexanoate;hydrate Chemical compound O.[Mg+2].OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C([O-])=O.OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C([O-])=O IAKLPCRFBAZVRW-XRDLMGPZSA-L 0.000 claims description 2
- 235000007686 potassium Nutrition 0.000 claims description 2
- PHZLMBHDXVLRIX-UHFFFAOYSA-M potassium lactate Chemical compound [K+].CC(O)C([O-])=O PHZLMBHDXVLRIX-UHFFFAOYSA-M 0.000 claims description 2
- 239000001521 potassium lactate Substances 0.000 claims description 2
- 235000011085 potassium lactate Nutrition 0.000 claims description 2
- 229960001304 potassium lactate Drugs 0.000 claims description 2
- VZOPRCCTKLAGPN-ZFJVMAEJSA-L potassium;sodium;(2r,3r)-2,3-dihydroxybutanedioate;tetrahydrate Chemical compound O.O.O.O.[Na+].[K+].[O-]C(=O)[C@H](O)[C@@H](O)C([O-])=O VZOPRCCTKLAGPN-ZFJVMAEJSA-L 0.000 claims description 2
- 238000004064 recycling Methods 0.000 claims description 2
- 239000001540 sodium lactate Substances 0.000 claims description 2
- 235000011088 sodium lactate Nutrition 0.000 claims description 2
- 229940005581 sodium lactate Drugs 0.000 claims description 2
- 229940074446 sodium potassium tartrate tetrahydrate Drugs 0.000 claims description 2
- KREQQYRYTQIJGI-UHFFFAOYSA-N 2,3-dihydroxybutanedioic acid;magnesium Chemical compound [Mg].OC(=O)C(O)C(O)C(O)=O KREQQYRYTQIJGI-UHFFFAOYSA-N 0.000 claims 1
- 244000192528 Chrysanthemum parthenium Species 0.000 claims 1
- 244000131316 Panax pseudoginseng Species 0.000 claims 1
- SWEYNHYBJHPVJL-UHFFFAOYSA-N butanoic acid;sodium Chemical compound [Na].CCCC(O)=O SWEYNHYBJHPVJL-UHFFFAOYSA-N 0.000 claims 1
- NPGILLWFJVZZPP-UHFFFAOYSA-N carbon dioxide;lead Chemical compound [Pb].O=C=O NPGILLWFJVZZPP-UHFFFAOYSA-N 0.000 claims 1
- 125000004356 hydroxy functional group Chemical group O* 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 13
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract description 11
- 239000002253 acid Substances 0.000 abstract description 10
- 150000007524 organic acids Chemical class 0.000 abstract description 9
- 230000008569 process Effects 0.000 abstract description 5
- 239000003205 fragrance Substances 0.000 abstract description 2
- 238000007789 sealing Methods 0.000 abstract 1
- 239000000126 substance Substances 0.000 description 13
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 9
- 150000002895 organic esters Chemical class 0.000 description 9
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 8
- 235000019441 ethanol Nutrition 0.000 description 7
- FUZZWVXGSFPDMH-UHFFFAOYSA-N hexanoic acid Chemical compound CCCCCC(O)=O FUZZWVXGSFPDMH-UHFFFAOYSA-N 0.000 description 6
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 6
- 235000020097 white wine Nutrition 0.000 description 6
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 5
- 239000004575 stone Substances 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 4
- 240000004371 Panax ginseng Species 0.000 description 4
- 239000004310 lactic acid Substances 0.000 description 4
- 235000014655 lactic acid Nutrition 0.000 description 4
- 210000004185 liver Anatomy 0.000 description 4
- 150000008442 polyphenolic compounds Chemical class 0.000 description 4
- 235000013824 polyphenols Nutrition 0.000 description 4
- 235000019991 rice wine Nutrition 0.000 description 4
- 229930182490 saponin Natural products 0.000 description 4
- 235000017709 saponins Nutrition 0.000 description 4
- 150000007949 saponins Chemical class 0.000 description 4
- 239000011265 semifinished product Substances 0.000 description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- 239000002585 base Substances 0.000 description 3
- 235000013405 beer Nutrition 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 238000006386 neutralization reaction Methods 0.000 description 3
- 241000894007 species Species 0.000 description 3
- ODIGIKRIUKFKHP-UHFFFAOYSA-N (n-propan-2-yloxycarbonylanilino) acetate Chemical compound CC(C)OC(=O)N(OC(C)=O)C1=CC=CC=C1 ODIGIKRIUKFKHP-UHFFFAOYSA-N 0.000 description 2
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 240000007890 Leonurus cardiaca Species 0.000 description 2
- 241000320380 Silybum Species 0.000 description 2
- 235000010841 Silybum marianum Nutrition 0.000 description 2
- 244000269722 Thea sinensis Species 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 208000027418 Wounds and injury Diseases 0.000 description 2
- 230000004308 accommodation Effects 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 2
- VSGNNIFQASZAOI-UHFFFAOYSA-L calcium acetate Chemical compound [Ca+2].CC([O-])=O.CC([O-])=O VSGNNIFQASZAOI-UHFFFAOYSA-L 0.000 description 2
- 235000011092 calcium acetate Nutrition 0.000 description 2
- 239000001639 calcium acetate Substances 0.000 description 2
- 229960005147 calcium acetate Drugs 0.000 description 2
- ZFXVRMSLJDYJCH-UHFFFAOYSA-N calcium magnesium Chemical class [Mg].[Ca] ZFXVRMSLJDYJCH-UHFFFAOYSA-N 0.000 description 2
- 235000013339 cereals Nutrition 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 230000035622 drinking Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- LZCLXQDLBQLTDK-UHFFFAOYSA-N ethyl 2-hydroxypropanoate Chemical compound CCOC(=O)C(C)O LZCLXQDLBQLTDK-UHFFFAOYSA-N 0.000 description 2
- SHZIWNPUGXLXDT-UHFFFAOYSA-N ethyl hexanoate Chemical compound CCCCCC(=O)OCC SHZIWNPUGXLXDT-UHFFFAOYSA-N 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 229960001031 glucose Drugs 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 208000014674 injury Diseases 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 229940095060 magnesium tartrate Drugs 0.000 description 2
- MUZDLCBWNVUYIR-ZVGUSBNCSA-L magnesium;(2r,3r)-2,3-dihydroxybutanedioate Chemical compound [Mg+2].[O-]C(=O)[C@H](O)[C@@H](O)C([O-])=O MUZDLCBWNVUYIR-ZVGUSBNCSA-L 0.000 description 2
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 description 2
- 230000004060 metabolic process Effects 0.000 description 2
- 235000010755 mineral Nutrition 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 235000016709 nutrition Nutrition 0.000 description 2
- 230000035764 nutrition Effects 0.000 description 2
- 229920001568 phenolic resin Polymers 0.000 description 2
- 239000005011 phenolic resin Substances 0.000 description 2
- 239000001397 quillaja saponaria molina bark Substances 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 235000020095 red wine Nutrition 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 230000009919 sequestration Effects 0.000 description 2
- MFBOGIVSZKQAPD-UHFFFAOYSA-M sodium butyrate Chemical compound [Na+].CCCC([O-])=O MFBOGIVSZKQAPD-UHFFFAOYSA-M 0.000 description 2
- MSRILKIQRXUYCT-UHFFFAOYSA-M valproate semisodium Chemical compound [Na+].CCCC(C(O)=O)CCC.CCCC(C([O-])=O)CCC MSRILKIQRXUYCT-UHFFFAOYSA-M 0.000 description 2
- BYPIKLIXBPMDBY-UHFFFAOYSA-N 2-hydroxypropanoic acid;potassium Chemical compound [K].CC(O)C(O)=O BYPIKLIXBPMDBY-UHFFFAOYSA-N 0.000 description 1
- ZZUUMCMLIPRDPI-UHFFFAOYSA-N 2-hydroxypropanoic acid;sodium Chemical compound [Na].CC(O)C(O)=O ZZUUMCMLIPRDPI-UHFFFAOYSA-N 0.000 description 1
- 206010000087 Abdominal pain upper Diseases 0.000 description 1
- 241000790917 Dioxys <bee> Species 0.000 description 1
- 244000068988 Glycine max Species 0.000 description 1
- 235000010469 Glycine max Nutrition 0.000 description 1
- 208000013016 Hypoglycemia Diseases 0.000 description 1
- 229920000388 Polyphosphate Polymers 0.000 description 1
- 244000000231 Sesamum indicum Species 0.000 description 1
- 235000003434 Sesamum indicum Nutrition 0.000 description 1
- 229910001069 Ti alloy Inorganic materials 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 235000009754 Vitis X bourquina Nutrition 0.000 description 1
- 235000012333 Vitis X labruscana Nutrition 0.000 description 1
- 240000006365 Vitis vinifera Species 0.000 description 1
- 235000014787 Vitis vinifera Nutrition 0.000 description 1
- GCNLQHANGFOQKY-UHFFFAOYSA-N [C+4].[O-2].[O-2].[Ti+4] Chemical compound [C+4].[O-2].[O-2].[Ti+4] GCNLQHANGFOQKY-UHFFFAOYSA-N 0.000 description 1
- HIVGXUNKSAJJDN-UHFFFAOYSA-N [Si].[P] Chemical compound [Si].[P] HIVGXUNKSAJJDN-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001447 alkali salts Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 238000013124 brewing process Methods 0.000 description 1
- NEEHYRZPVYRGPP-IYEMJOQQSA-L calcium gluconate Chemical compound [Ca+2].OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C([O-])=O.OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C([O-])=O NEEHYRZPVYRGPP-IYEMJOQQSA-L 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- 235000012255 calcium oxide Nutrition 0.000 description 1
- 229940087373 calcium oxide Drugs 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 229940116333 ethyl lactate Drugs 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 210000004051 gastric juice Anatomy 0.000 description 1
- 235000001727 glucose Nutrition 0.000 description 1
- 230000002218 hypoglycaemic effect Effects 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- CJWQYWQDLBZGPD-UHFFFAOYSA-N isoflavone Natural products C1=C(OC)C(OC)=CC(OC)=C1C1=COC2=C(C=CC(C)(C)O3)C3=C(OC)C=C2C1=O CJWQYWQDLBZGPD-UHFFFAOYSA-N 0.000 description 1
- 150000002515 isoflavone derivatives Chemical class 0.000 description 1
- 235000008696 isoflavones Nutrition 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 210000003141 lower extremity Anatomy 0.000 description 1
- 159000000003 magnesium salts Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003387 muscular Effects 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000032696 parturition Effects 0.000 description 1
- 239000001205 polyphosphate Substances 0.000 description 1
- 235000011176 polyphosphates Nutrition 0.000 description 1
- LJCNRYVRMXRIQR-UHFFFAOYSA-L potassium sodium tartrate Chemical compound [Na+].[K+].[O-]C(=O)C(O)C(O)C([O-])=O LJCNRYVRMXRIQR-UHFFFAOYSA-L 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 235000015096 spirit Nutrition 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 210000002784 stomach Anatomy 0.000 description 1
- 230000002459 sustained effect Effects 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 210000001835 viscera Anatomy 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12G—WINE; PREPARATION THEREOF; ALCOHOLIC BEVERAGES; PREPARATION OF ALCOHOLIC BEVERAGES NOT PROVIDED FOR IN SUBCLASSES C12C OR C12H
- C12G3/00—Preparation of other alcoholic beverages
- C12G3/04—Preparation of other alcoholic beverages by mixing, e.g. for preparation of liqueurs
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Non-Alcoholic Beverages (AREA)
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Abstract
The invention discloses a kind of production methods and equipment of alkaline functional drinks, the alkaline functional alcohol product of gained of the invention is due to the use of common common a small amount of gas, instead of original organic acid in wine, and in the production process, it is sealed up for safekeeping together using more stable body trace element replenishers, and with a small amount of gas.After product is poured into cup, contained few micro- carbon dioxide meeting quick release in wine, and reach rapid equalisation with atmospheric level, so that the pH in wine is persistently risen in the range of product calibration, and the back reaction that fragrance loss declines with pH is not susceptible to during sealing up for safekeeping, and in the production process, can add in not because it is in weak acid or alkalescent, raw material or extract rich in high human body value content etc.；In other words, many problems this invention addresses alkaline functional wine in the prior art, and it is a kind of novel process that limitation is not made by existing drinks.
Description
Technical field
The invention belongs to drinks brewing technology fields, and in particular to a kind of production method and equipment of alkaline functional drinks.
Background technology
The pH of most of drinks is acidity.The pH such as Spirit, fermented wine are 4.5~5.5, and beer pH is 4.2~4.4.Wine
Ethyl alcohol in class in decomposable process, a large amount of acetaldehyde for being generated through enzyme metabolism, rest on liver, blood, in internal organs, can not be by
Rapid metabolization is adjusted and accumulated, the injury for causing human body very big, and reaction of being still drank after a night can be generated after drinking, and is sticked as alcohol reduces stomach
Film resists the ability (stomachache) of hydrochloric acid in gastric juice, the liver hypoglycemia for being persistently metabolized ethyl alcohol and generating, the acetaldehyde injury liver generated after metabolism
Dirty cell (burden of liver), lactic acid accumulation cause lower limb or Muscular stiffness, and (after enzyme is metabolized, alcohol is converted into acid, needs
Will more internal alkaline matter come reach body digestion and acid-base balance) etc..And alkaline drinks is just to prevent the above problem from giving birth to,
It compared with common drinks, will accelerate to be metabolized after drinking, and prevent be still drank after a night reaction and cylinder electrolyte loss, and reach promotion
The effect of soda acid cyclic balance.
In drinks brewing process, the aroma-producing substances such as numerous species organic acid and organic esters are generated, and it is traditional
Thus a variety of white wine of different brewage process are developed.The different proportion collocation of a variety of aroma-producing substances, forms various white wine
Main body fragrance, so as to develop the fragrant liquor of multiple types.For the making of past alkalescence drinks, additive neutralizes
Organic acid ingredient (acetic acid, lactic acid, caproic acid etc.) in white wine, but its aroma-producing substance (ethyl acetate, ethyl lactate, caproic acid
Ethyl ester ... etc.) in weakly alkaline semi-finished product or the environment that dispatches from the factory, organic esters can partly occur and generate back reaction
Situation (esters content number determines that white wine dispatches from the factory the classification quality degree of product), above-mentioned organic esters are converse
It answers or the situation of pH-value decline mainly has following two kinds：
(1) it is included in plant ash (potassium carbonate or saleratus) to neutralize the main materials of organic acid in wine
Basic mineral class substance.And the synthetic reaction of different organic esters, be ethyl alcohol with its organic acid ingredient (acetic acid,
Lactic acid, caproic acid etc.), it is slowly generated in the environment for fermenting or storing.When semi-finished product or the alkaline liquor that dispatches from the factory are in weakly alkaline ring
In border, different organic esters can take a turn for the worse reaction so that in part semi-finished product or the product that dispatches from the factory in perfumery
Matter, back reaction become organic acid, and with the alkali ion substance sustained response (potassium carbonate or saleratus) in it, so as to cause
The calibration mass of the semi-finished product of alkaline liquor or the product that dispatches from the factory (pH-value decline) is (organic with the aroma-producing substance back reaction in product
Ester type compound content reduce) quality it is unstable.
(2) it is basic mineral class substance (carbon included in calcium carbonate to neutralize the main materials of organic acid in wine
Sour calcium or calcium hydroxide).The carbon dioxide in air must be avoided contact with the alkaline liquor of its production, once it contacts or is exposed to
In air, i.e. quickly (pH-value quickly declines properties of product, and has phase using materials such as plant ash with above-mentioned for decline
The aroma-producing substance unstability of pass), so as in drinks soda acid property and quality and its on the pot-life, there is part to need to improve
Space.
(3) past technique is in alkaline drinks is made, frequently with it is long when immersion means, and for drinks quality inspection
In the solid content test stone of standard, it is often additional generate it is readily soluble and it is difficult filter out, and to the substance that test stone impacts, such as
The inorganic salts such as calcium bicarbonate, magnesium bicarbonate in detection process after being evaporated drinks, can generate the nothings such as calcium carbonate, magnesium hydroxide
Machine solid content and greatly increase the solid content evaluation value of its product.
The content of the invention
It is an object of the invention to overcome prior art defect, a kind of production method of alkaline functional drinks is provided.
Another object of the present invention is to provide for the equipment of above-mentioned production method.
Technical scheme is as follows：
A kind of production method of alkaline functional drinks, includes the following steps：
(1) raw material wine is sent into the first retort, the magnesium bicarbonate of 0.01~5.0wt ‰ is added in the first retort
It with the calcium hydroxide of 0.01~5.0wt ‰, is uniformly mixed with raw material wine therein, reacts 10s~100min, make the pH therein be
5.0~10.0, solid content therein and half solid content are then filtered out by the first filtering draw-out device, and are sent into the second reaction
In tank；
(2) into the material of the second retort, Xun Huan is passed through carbon dioxide 10s~100min, and the pH of control material is 4.5
~8.0, the calcium hydroxide wherein dissolved is made to be precipitated as calcium carbonate, and the magnesium bicarbonate dissolved is in the form of magnesium hydroxide
It is precipitated, solid content therein and half solid content is then filtered out by the second filtering draw-out device, and are sent into the 3rd retort；
(3) trace element hydroxy that can increase that 0.01~5.0wt ‰ is added into the material of the 3rd retort is mended
Agent is filled, is uniformly mixed with material therein, reacts 10s~100min, makes wherein material pH for 5.0~10.0, then by the
Three filtering draw-out devices filter out solid content therein and half solid content, and are sent into the 4th retort；
(4) material into the 4th retort continues cycling and is passed through carbon dioxide, and the pH of control material is 4.5~8.0, then
Solid content therein and half solid content are filtered out by the 4th filtering draw-out device, and are sent into the 5th retort；
(5) depending on product specification or the target pH of dispatching from the factory, to decide whether that the material into the 5th retort is passed through dioxy
Change carbon or ventilation cycle to adjust pH, after material reaches balance and stability, you can extract canned with completion.
In a preferred embodiment of the invention, described first to fourth filter core used in draw-out device is filtered
Pore radius is 1~100000nm.
It is further preferred that in the first to fourth filtering draw-out device material of filter core used for active carbon for liquor or
Paper roll, quartz sand, diatomite, magnetite, ceramics, stainless steel fibre, polypropylene, phenolic resin, stud, polyether sulfone fiber, silicon phosphorus
Crystalline substance, KDF, manganese sand, ion exchange resin or ultrafiltration membrane.
In a preferred embodiment of the invention, the trace element in the micro element supplement agent include calcium, potassium,
Magnesium, sodium and alkaloid.
It is further preferred that the micro element supplement agent includes calcium bicarbonate, calcium acetate, calcium propionate, calcium butyrate, grape
Calciofon, amino acid calcium, saleratus, potassium carbonate, potassium acetate, potassium propionate, valproic acid potassium, potassium lactate, potassium tartrate, glucose
Sour potassium, potassium amino acid, magnesium carbonate, propionic acid magnesium, magnesium valprote, magnesium lactate, magnesium tartrate, magnesium gluconate, amino acid-magnesium chelate, amino
Sour calcium and magnesium, sodium acid carbonate, sodium carbonate, sodium acetate, sodium propionate, sodium vedproate, sodium butyrate, sodium lactate, sodium tartrate, potassium tartrate
Sodium, sodium gluconate, amino acid sodium and alkaloid, the source of the alkaloid include ginseng, ganoderma lucidum, black nightshade, oat, Changchun it is new,
The coptis, lotus seeds, HERBA DENDROBII, motherwort, colchicum, camplotheca acuminata, Salsola richteri, lotus leaf and mulberry leaf.
Another technical solution of the present invention is as follows：
A kind of equipment for above-mentioned production method, including one first retort, one second retort, one the 3rd reaction
Tank, one the 4th retort, one the 5th retort, a carbon dioxide ventilation control device, the first to the 5th air valve, first to fourth
Filtering draw-out device and first to fourth valve, the inlet of the first to the 5th retort are respectively positioned on top, and liquid outlet is respectively positioned on
Lower part, first to fourth valve are three-dimensional valve；
First retort, inlet connection upstream equipment, liquid outlet pass sequentially through the first filtering draw-out device and the
One valve connects the inlet of the second retort；
Second retort, liquid outlet passes sequentially through the second filtering draw-out device and the second valve connects the 3rd retort
Inlet；
3rd retort, liquid outlet passes sequentially through the 3rd filtering draw-out device and the 3rd valve connects the 4th retort
Inlet；
4th retort, liquid outlet passes sequentially through the 4th filtering draw-out device and the 4th valve connects the 5th retort
Inlet；
The liquid outlet connection downstream extraction and filling apparatus of 5th retort；
Carbon dioxide ventilation control device is respectively communicated with the second retort, the 4th reaction by the first to the 3rd air valve respectively
The top of tank and the 5th retort, wherein, carbon dioxide ventilation control device connects the 3rd air valve by the 4th air valve, by the
Five air valves are respectively communicated with the first and second air valves, and the second retort, the 4th retort and the 5th retort are respectively equipped with first
To third gas circulator.
In a preferred embodiment of the invention, it is respectively equipped with first to the 5th in the described first to the 5th retort
Rabbling mechanism.
In a preferred embodiment of the invention, the bottom of the described first to the 5th retort be respectively equipped with first to
5th detergent line.
In a preferred embodiment of the invention, the described first to the 5th retort is respectively equipped with first to the 5th
PH detects display device.
In a preferred embodiment of the invention, the 5th to the 12nd valve is further included, wherein, the 7th and the 11st
Valve is two way valve, remaining is three-dimensional valve；
5th valve is arranged on the inlet of the first retort, and passes through the 7th valve connection the second filtering draw-out device；The
Six valves are arranged on the upstream of the 5th valve, and pass through the top that the 8th valve connects the 3rd retort；8th valve passes through the 9th
Valve connects the 3rd valve, and passes through the 9th valve and connect the tenth valve；4th filtering draw-out device is connected by the tenth valve
4th valve；12nd valve is respectively communicated with the first and second valves, and passes through the 11st valve and connect the 4th valve.
Beneficial effects of the present invention are as follows：
1st, the present invention seals up for safekeeping after a small amount of carbon dioxide is dissolved in wine so that organic esters therein persistently exist
In the environment of partial neutral, therefore the opposite back reaction for being less likely to occur organic esters, alkaline drinks production can be improved
The quality and stability of product；
2nd, the alkaline alcohol product of present invention gained is due to wherein containing part carbonic acid, simultaneously because in the method for the present invention
In allow to increase micro element supplement agent hydroxy and be dissolved in drinks, by taking potassium carbonate as an example, make the excessive titanium dioxide of its contact
Carbon, and then it is changed into saleratus, saleratus is weak base compared to potassium carbonate, and is not easy that neutralization reaction occurs with carbonic acid；It is producing
After product unlatching is poured into cup, drinks discharge a small amount of carbon dioxide, and the density of carbon dioxide gas Fast-Balance in air, simultaneously
Saleratus one in wine loses carbonate, and is recovered to potassium carbonate and is dissolved in wine so that the pH in wine persistently rises to product
In the range of quality demarcation, at this time such as the back reaction of generation organic esters, the back reaction time is not easy to quick to hair
Raw product special flavour generates variation；Micro element supplement agent hydroxy can be increased using other, property is also a small amount of because using
Carbon dioxide sequestration and generate the similar raised resilient characteristics of pH, in other words, method of the invention solves alkaline drinks and exists
The problems of the prior art.
3rd, in the present invention, no matter it needs the species of pretreatment liquor as white wine, yellow rice wine, rice wine, beer, red wine or other steamings
Wine and fermented wine are evaporated, can its soda acid property be improved through accommodation by such technique.
4th, the drinks main body of the present invention, can for a weak acid and a small amount of bicarbonate and acylate and the environment deposited
Depending on product demand situation in the production process or back segment, it is directly a small amount of to add in and impregnate whether containing being in neutrality or faintly acid
(the numerous Polyphenols extraction of substance of such as tea polyphenols, isoflavones, oat, milk thistle or several acidic group amino acid etc.) or
Be in neutrality or alkalescent (such as ginseng, ganoderma lucidum, black nightshade, oat, Changchun are new, the extraction of lotus leaf, mulberry leaf alkaloid and saponins etc.),
Rich in the food such as the cereal of human nutrition value content, plant, saponin(e and alkaloid or its active principle, and product with
The active principle added on a small quantity is not easy to react to each other again and cause the influence of product qualitative change.
5th, in the present invention, using in calcium hydroxide and magnesium bicarbonate and in wine after organic acid, then it is allowed to and titanium dioxide
Carbon reacts, solid that reaction product filters out for convenience or half solid calcium carbonate or magnesium hydroxide, therefore the present invention is in drinks matter
In the solid content test stone for measuring test stone, compared to technique in the past, occupy not generating difficulty and filter out and test stone can be made
Into the advantage (such as calcium bicarbonate, magnesium bicarbonate inorganic salts) for influencing substance.
6th, in present invention process, original contained organic acid (acetic acid, lactic acid, caproic acid) in drinks is made to be changed into solubility
Organic acid calcium salt or magnesium salts, it is comparatively higher and effective in human absorptivity for inorganic calcium magnesium salts, and reduce
Human body excessively absorbs the calculus risk after inorganic calcium magnesium salts.
7th, for the present invention compared to the processing method of alkaline drinks in the past, energy source consumption is small (being not required to by distillation), during production
Between fast (being not necessary to by staticly settling), and put into after raw material it is a small amount of filter out object and sediment, be not required to using complicated neutralization
Processing is more advantageous to environmental protection with saving the requirement of the energy.
8th, equipment of the invention can ensure uninterrupted continuous production alkalescence drinks when equipment component needs repairing replacement
Product.
Description of the drawings
Fig. 1 is the structure diagram of the equipment used in the present invention.
Specific embodiment
Technical scheme is further detailed and described below by way of specific embodiment combination attached drawing.
A kind of production method of alkalescence drinks, the equipment used is as shown in Figure 1, including one first retort 1, one second
The 5th retort 5 of the 4th retort 4,1 of the 3rd retort 3,1 of retort 2,1, a carbon dioxide ventilation control device 6,
One to the 5th air valve 9a~9e, first to fourth the 13,23,33,43 and first to the 12nd valve 8a~81 of filtering draw-out device；
The inlet of first to the 5th retort 1~5 is respectively positioned on top, and liquid outlet is respectively positioned on lower part, is inside respectively equipped with
First to the 5th rabbling mechanism 10~50, bottom are respectively equipped with the first to the 5th detergent line 11,21,31,41 and 51, in addition,
First to the 5th retort 1,2,3,4 and 5 is respectively equipped with the first to the 5th pH detection display devices 12,22,32,42 and 52；
The pore radius of filter core used is 1~100000nm in first to fourth filtering draw-out device, and the material of filter core is excellent
Elect active carbon for liquor or paper roll, quartz sand, diatomite, magnetite, ceramics, stainless steel fibre, polypropylene (PP), phenolic resin as
(PF), stud (pure titanium or titanium alloy), polyether sulfone fiber (PES), Si-P crystal (polyphosphate), KDF (pltine), manganese sand
(manganese dioxide), ion exchange resin or ultrafiltration membrane；
In first to the 12nd valve, the 7th and the 11st valve be two way valve, remaining is three-dimensional valve；
First retort 1, inlet connection upstream equipment, liquid outlet pass sequentially through 13 He of the first filtering draw-out device
First valve 8a connects the inlet of the second retort 2；
Second retort 2, liquid outlet pass sequentially through the second filtering draw-out device 23 and the 3rd are connected with the second valve 8b instead
Answer the inlet of tank 3；
3rd retort 3, liquid outlet pass sequentially through the 3rd filtering draw-out device 33 and the 4th are connected with the 3rd valve 8c instead
Answer the inlet of tank 4；
4th retort 4, liquid outlet pass sequentially through the 4th filtering draw-out device 43 and the 5th are connected with the 4th valve 8d instead
Answer the inlet of tank 5；
The liquid outlet connection downstream extraction and filling apparatus of 5th retort 5；
Carbon dioxide ventilation control device 6 respectively by first to the 3rd air valve 9a~9c be respectively communicated with the second retort 2,
The top of 4th retort 4 and the 5th retort 5, wherein, carbon dioxide ventilation control device 6 passes through the 4th air valve 9d connections the
Three air valve 9c are respectively communicated with the first and second air valve 9a and 9b, and the second retort 2, the 4th retort 4 by the 5th air valve 9e
First is respectively equipped with to third gas circulator 24,44 and 54 with the 5th retort 5；
5th valve 8e is arranged on the inlet of the first retort 1, and passes through the second filtering of the 7th valve 8g connections and extract dress
Put 23；6th valve 8f is arranged on the upstream of the 5th valve 8e, and passes through the top that the 8th valve 8h connects the 3rd retort 3；The
Eight valve 8h connect the 3rd valve 8c by the 9th valve 8i, and pass through the 9th valve 8i and connect the tenth valve 8j；4th filtering
Draw-out device 43 connects the 4th valve 8d by the tenth valve 8i；12nd valve 81 be respectively communicated with the first and second valve 8a,
8b, and pass through the 11st valve 8k and connect the 4th valve 8d；
From the foregoing, it will be observed that the first retort 1 and the second retort 2 are first group, the 3rd retort 3 and the 4th retort 4 are
Second group, the 5th retort 5 is the 3rd group, and when needing replacing part or repair for wherein any one group, remaining two groups can
By pipeline connection, the uninterrupted function of producing alkaline drinks is realized.
The production method specifically comprises the following steps：
(1) raw material wine is sent into the first retort 1, the bicarbonate of 0.01~5.0wt ‰ is added in the first retort 1
‰ calcium hydroxide of magnesium and 0.01~5.0wt, is uniformly mixed with raw material wine therein, reacts 10s~100min, makes the pH therein be
5.0~10.0, solid content therein and half solid content are then filtered out by the first filtering draw-out device 13, and it is anti-to be sent into second
It answers in tank 2；
(2) by carbon dioxide ventilation control device 6 and first gas circulator 24 into the material of the second retort 2
Cycling is passed through carbon dioxide 10s~100min, and the pH of control material is 4.5~8.0, and the calcium hydroxide for making wherein to dissolve is with carbonic acid
The form of calcium is precipitated, and the magnesium bicarbonate wherein dissolved is precipitated in the form of magnesium hydroxide, then extracts dress by the second filtering
It puts 23 and filters out solid content therein and half solid content, and be sent into the 3rd retort 3；
(3) trace element hydroxy that can increase that 0.01~5.0wt ‰ is added into the material of the 3rd retort 3 is mended
Filling agent, (trace element in the micro element supplement agent includes calcium, potassium, magnesium and sodium and alkaloid, and the trace element is mended
Fill agent be particularly preferred as it is inorganic or organic containing the basic salt such as calcium, potassium, magnesium and sodium and alkaloid, such as：Calcium bicarbonate, calcium acetate,
Calcium propionate, calcium butyrate, calcium gluconate, amino acid calcium, saleratus, potassium carbonate, potassium acetate, potassium propionate, valproic acid potassium, lactic acid
Potassium, potassium tartrate, K-IAO, potassium amino acid, magnesium carbonate, propionic acid magnesium, magnesium valprote, magnesium lactate, magnesium tartrate, glucose
Sour magnesium, amino acid-magnesium chelate, amino acid calcium and magnesium, sodium acid carbonate, sodium carbonate, sodium acetate, sodium propionate, sodium vedproate, sodium butyrate, lactic acid
Sodium, sodium tartrate, sodium potassium tartrate tetrahydrate, sodium gluconate, amino acid sodium and alkaloid, the source of the alkaloid include ginseng, spirit
Sesame, black nightshade, oat, Changchun are new, the coptis, lotus seeds, HERBA DENDROBII, motherwort, colchicum, camplotheca acuminata, Salsola richteri, lotus leaf and mulberry leaf),
It is uniformly mixed with material therein, reacts 10s~100min, it is 5.0~10.0 to make wherein material pH, then passes through the 3rd filtering
Draw-out device 33 filters out solid content therein and half solid content, and is sent into the 4th retort 4；
(4) by carbon dioxide ventilation control device 6 and second gas circulator 44 into the material of the 4th retort 4
Continuous Xun Huan is passed through carbon dioxide, and the pH of control material is 4.5~8.0, then filters out it by the 4th filtering draw-out device 43
In solid content and half solid content, and be sent into the 5th retort 5 in；
(5) depending on product specification or the target pH of dispatching from the factory, to decide whether through carbon dioxide ventilation control device 6 and
Material of three gas-recycling plants 54 into the 5th retort 5 is passed through carbon dioxide or ventilation cycle to adjust pH, treats that material reaches
To after balance and stability, you can extract canned with completion.
The alkaline alcohol product of gained of the invention is due to wherein containing part carbonic acid, simultaneously because in the method for the invention
Allowing to, which increases micro element supplement agent hydroxy, is dissolved in drinks, by taking potassium carbonate as an example, it is made to contact excess carbon dioxide,
And then it is changed into saleratus, saleratus is weak base compared to potassium carbonate, and is not easy that neutralization reaction occurs with carbonic acid；In product
After unlatching is poured into cup, drinks discharge a small amount of carbon dioxide, and the density of carbon dioxide gas Fast-Balance in air, while wine
In saleratus one lose carbonate, and be recovered to potassium carbonate and be dissolved in wine so that the pH in alkaline drinks persistently rises to
In the range of product quality calibration, the back reaction of organic esters such as occurs at this time, the back reaction time is not easy to quickly
Variation is generated to product special flavour occurs；Micro element supplement agent hydroxy can be increased using other, property is also because using
A small amount of carbon dioxide sequestration and generate the similar raised resilient characteristics of pH, in other words, method of the invention solves alkaline liquor
Class in the prior art the problem of.
Further, the invention in the production process, no matter it needs the species of pretreatment liquor as white wine, yellow rice wine, rice wine, beer
Wine, red wine or other Spirits and fermented wine can improve its soda acid property by such technique through accommodation.And the present invention
Drinks main body is a weak acid and a small amount of bicarbonate and acylate and the environment deposited, can made depending on product demand situation
It is directly a small amount of to add in and impregnate whether containing being in neutrality or faintly acid (such as different Huang of tea polyphenols, soybean during work or back segment
Numerous Polyphenols extraction of substance such as ketone, oat, milk thistle or several acidic group amino acid etc.) or be in neutrality or alkalescent (such as people
The extraction alkaloid and saponins etc. such as ginseng, ganoderma lucidum, black nightshade, oat, Changchun new, lotus leaf, mulberry leaf), rich in being worth to human nutrition
The food such as cereal, plant, saponin(e and the alkaloid of content or its active principle, and product and the active principle that adds on a small quantity,
It is not easy to react to each other again and cause the influence of product qualitative change.
The foregoing is only a preferred embodiment of the present invention, therefore cannot limit the scope that the present invention is implemented according to this, i.e.,
According to the equivalent changes and modifications that the scope of the claims of the present invention and description are made, all should still belong in the range of the present invention covers.
Claims (10)
1. a kind of production method of alkaline functional drinks, it is characterised in that：Include the following steps：
(1) by raw material wine be sent into the first retort in, added in the first retort 0.01~5.0wt ‰ magnesium bicarbonate and
The calcium hydroxide of 0.01~5.0wt ‰ is uniformly mixed with raw material wine therein, is reacted 10s~100min, is made the pH therein be
5.0~10.0, solid content therein and half solid content are then filtered out by the first filtering draw-out device, and are sent into the second reaction
In tank；
(2) into the material of the second retort, cycle is passed through carbon dioxide 10s~100min, the pH of control material for 4.5~
8.0, the calcium hydroxide wherein dissolved is made to be precipitated as calcium carbonate, and the magnesium bicarbonate dissolved is analysed in the form of magnesium hydroxide
Go out, solid content therein and half solid content are then filtered out by the second filtering draw-out device, and are sent into the 3rd retort；
(3) 0.01~5.0wt ‰ is added into the material of the 3rd retort can increase micro element supplement agent hydroxy,
It is uniformly mixed with material therein, reacts 10s~100min, it is 5.0~10.0 to make wherein material pH, then passes through the 3rd filtering
Draw-out device filters out solid content therein and half solid content, and is sent into the 4th retort；
(4) material into the 4th retort continues cycling and is passed through carbon dioxide, and the pH of control material is 4.5~8.0, is then passed through
4th filtering draw-out device filters out solid content therein and half solid content, and is sent into the 5th retort；
(5) depending on product specification or the target pH of dispatching from the factory, to decide whether that the material into the 5th retort is passed through carbon dioxide
Or ventilation cycle to be to adjust pH, after material reaches balance and stability, you can extract canned with completion.
2. production method as described in claim 1, it is characterised in that：Used in the first to fourth filtering draw-out device
The pore radius of filter core is 1~100000nm.
3. production method as claimed in claim 2, it is characterised in that：It is used in the first to fourth filtering draw-out device
The material of filter core is active carbon for liquor or paper roll, quartz sand, diatomite, magnetite, ceramics, stainless steel fibre, polypropylene, phenolic aldehyde tree
Fat, stud, polyether sulfone fiber, Si-P crystal, KDF, manganese sand, ion exchange resin or ultrafiltration membrane.
4. production method as described in claim 1, it is characterised in that：Trace element in the micro element supplement agent includes
Calcium, potassium, magnesium, sodium and alkaloid.
5. production method as claimed in claim 4, it is characterised in that：The micro element supplement agent includes calcium bicarbonate, second
Sour calcium, calcium propionate, calcium butyrate, calcium gluconate, amino acid calcium, saleratus, potassium carbonate, potassium acetate, potassium propionate, valproic acid
Potassium, potassium lactate, potassium tartrate, K-IAO, potassium amino acid, magnesium carbonate, propionic acid magnesium, magnesium valprote, magnesium lactate, tartaric acid
Magnesium, magnesium gluconate, amino acid-magnesium chelate, amino acid calcium and magnesium, sodium acid carbonate, sodium carbonate, sodium acetate, sodium propionate, sodium vedproate, butyric acid
Sodium, sodium lactate, sodium tartrate, sodium potassium tartrate tetrahydrate, sodium gluconate, amino acid sodium and alkaloid, the source of the alkaloid include
Ginseng, ganoderma lucidum, black nightshade, oat, Changchun are new, the coptis, lotus seeds, HERBA DENDROBII, motherwort, colchicum, camplotheca acuminata, Salsola richteri, lotus leaf
And mulberry leaf.
6. a kind of equipment of production method for described in any claim in claim 1 to 5, it is characterised in that：Including
One first retort, one second retort, one the 3rd retort, one the 4th retort, one the 5th retort, a carbon dioxide lead to
Gas control device, the first to the 5th air valve, first to fourth filtering draw-out device and first to fourth valve, first to the 5th is anti-
The inlet of tank is answered to be respectively positioned on top, liquid outlet is respectively positioned on lower part, and first to fourth valve is three-dimensional valve；
First retort, inlet connection upstream equipment, liquid outlet pass sequentially through the first filtering draw-out device and the first valve
The inlet of door the second retort of connection；
Second retort, liquid outlet passes sequentially through the second filtering draw-out device and the second valve connects the feed liquor of the 3rd retort
Mouthful；
3rd retort, liquid outlet passes sequentially through the 3rd filtering draw-out device and the 3rd valve connects the feed liquor of the 4th retort
Mouthful；
4th retort, liquid outlet passes sequentially through the 4th filtering draw-out device and the 4th valve connects the feed liquor of the 5th retort
Mouthful；
The liquid outlet connection downstream extraction and filling apparatus of 5th retort；
Carbon dioxide ventilation control device respectively by the first to the 3rd air valve be respectively communicated with the second retort, the 4th retort and
The top of 5th retort, wherein, carbon dioxide ventilation control device connects the 3rd air valve by the 4th air valve, passes through the 5th gas
Valve is respectively communicated with the first and second air valves, and the second retort, the 4th retort and the 5th retort are respectively equipped with first to
Three gas-recycling plants.
7. equipment as claimed in claim 6, it is characterised in that：First to is respectively equipped in described first to the 5th retort
Five rabbling mechanisms.
8. equipment as claimed in claim 6, it is characterised in that：The bottom of described first to the 5th retort is respectively equipped with first
To the 5th detergent line.
9. equipment as claimed in claim 6, it is characterised in that：Described first to the 5th retort is respectively equipped with first to
Five pH detect display device.
10. equipment as claimed in claim 6, it is characterised in that：The the 5th to the 12nd valve is further included, wherein, the 7th and
11 valves are two way valve, remaining is three-dimensional valve；
5th valve is arranged on the inlet of the first retort, and passes through the 7th valve connection the second filtering draw-out device；6th valve
Door is arranged on the upstream of the 5th valve, and passes through the top that the 8th valve connects the 3rd retort；8th valve passes through the 9th valve
The 3rd valve is connected, and passes through the 9th valve and connects the tenth valve；4th filtering draw-out device connects the 4th by the tenth valve
Valve；12nd valve is respectively communicated with the first and second valves, and passes through the 11st valve and connect the 4th valve.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711136650.9A CN108102859B (en) | 2017-11-16 | 2017-11-16 | Method and equipment for producing alkaline functional wine |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711136650.9A CN108102859B (en) | 2017-11-16 | 2017-11-16 | Method and equipment for producing alkaline functional wine |
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| CN108102859B CN108102859B (en) | 2024-04-05 |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006166889A (en) * | 2004-12-13 | 2006-06-29 | Yoshiaki Nagaura | Discovery of new extraction method |
| CN101705165A (en) * | 2009-11-16 | 2010-05-12 | 刘辉 | Beer and manufacturing method thereof |
| CN201473511U (en) * | 2009-08-31 | 2010-05-19 | 澎湖第一酒厂股份有限公司 | Alkaline wine preparation device |
| CN202744528U (en) * | 2012-08-24 | 2013-02-20 | 王国仁 | Alkaline wine processing device |
| CN104974897A (en) * | 2014-04-11 | 2015-10-14 | 王衍洲 | Preparation method of alkaline liquor solution |
-
2017
- 2017-11-16 CN CN201711136650.9A patent/CN108102859B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006166889A (en) * | 2004-12-13 | 2006-06-29 | Yoshiaki Nagaura | Discovery of new extraction method |
| CN201473511U (en) * | 2009-08-31 | 2010-05-19 | 澎湖第一酒厂股份有限公司 | Alkaline wine preparation device |
| CN101705165A (en) * | 2009-11-16 | 2010-05-12 | 刘辉 | Beer and manufacturing method thereof |
| CN202744528U (en) * | 2012-08-24 | 2013-02-20 | 王国仁 | Alkaline wine processing device |
| CN104974897A (en) * | 2014-04-11 | 2015-10-14 | 王衍洲 | Preparation method of alkaline liquor solution |
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| CN108102859B (en) | 2024-04-05 |
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