TW201827332A - Apparatus, method and system for generating hydrogen-containing liquid capable of generating a hydrogen-containing liquid of which the dissolved hydrogen concentration after 10 minutes exceeds 6 ppm and the dissolved hydrogen concentration after 24 hours exceeds 10 ppm - Google Patents
Apparatus, method and system for generating hydrogen-containing liquid capable of generating a hydrogen-containing liquid of which the dissolved hydrogen concentration after 10 minutes exceeds 6 ppm and the dissolved hydrogen concentration after 24 hours exceeds 10 ppm Download PDFInfo
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- TW201827332A TW201827332A TW106101638A TW106101638A TW201827332A TW 201827332 A TW201827332 A TW 201827332A TW 106101638 A TW106101638 A TW 106101638A TW 106101638 A TW106101638 A TW 106101638A TW 201827332 A TW201827332 A TW 201827332A
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- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 234
- 239000001257 hydrogen Substances 0.000 title claims abstract description 214
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 214
- 239000007788 liquid Substances 0.000 title claims abstract description 112
- 238000000034 method Methods 0.000 title abstract description 21
- 239000002775 capsule Substances 0.000 claims abstract description 93
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 40
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 33
- 238000006243 chemical reaction Methods 0.000 claims description 23
- 238000004519 manufacturing process Methods 0.000 claims description 18
- 239000007769 metal material Substances 0.000 claims description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 16
- 230000000052 comparative effect Effects 0.000 description 11
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 9
- 239000000463 material Substances 0.000 description 9
- 229910052751 metal Inorganic materials 0.000 description 9
- 239000002184 metal Substances 0.000 description 9
- 229910021645 metal ion Inorganic materials 0.000 description 9
- 229910052782 aluminium Inorganic materials 0.000 description 8
- 239000000126 substance Substances 0.000 description 8
- 239000002981 blocking agent Substances 0.000 description 6
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 6
- 239000000920 calcium hydroxide Substances 0.000 description 6
- 235000011116 calcium hydroxide Nutrition 0.000 description 6
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 6
- 239000003002 pH adjusting agent Substances 0.000 description 6
- 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 description 5
- 239000002253 acid Substances 0.000 description 5
- 150000002431 hydrogen Chemical class 0.000 description 5
- -1 hydrogen ions Chemical class 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 239000008280 blood Substances 0.000 description 4
- 210000004369 blood Anatomy 0.000 description 4
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 4
- 239000007924 injection Substances 0.000 description 4
- 238000002347 injection Methods 0.000 description 4
- 239000012528 membrane Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 230000035699 permeability Effects 0.000 description 4
- 239000008213 purified water Substances 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- 229920005989 resin Polymers 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 239000000292 calcium oxide Substances 0.000 description 3
- 235000012255 calcium oxide Nutrition 0.000 description 3
- 235000014171 carbonated beverage Nutrition 0.000 description 3
- 239000003729 cation exchange resin Substances 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 239000003456 ion exchange resin Substances 0.000 description 3
- 229920003303 ion-exchange polymer Polymers 0.000 description 3
- 239000008399 tap water Substances 0.000 description 3
- 235000020679 tap water Nutrition 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- RGHNJXZEOKUKBD-SQOUGZDYSA-N D-gluconic acid Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C(O)=O RGHNJXZEOKUKBD-SQOUGZDYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 241000405070 Percophidae Species 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 241001122767 Theaceae Species 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- 229940037003 alum Drugs 0.000 description 2
- 239000003957 anion exchange resin Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 235000013361 beverage Nutrition 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
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- 230000000694 effects Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 2
- 238000007689 inspection Methods 0.000 description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 2
- 239000000347 magnesium hydroxide Substances 0.000 description 2
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 210000000707 wrist Anatomy 0.000 description 2
- KIUKXJAPPMFGSW-DNGZLQJQSA-N (2S,3S,4S,5R,6R)-6-[(2S,3R,4R,5S,6R)-3-Acetamido-2-[(2S,3S,4R,5R,6R)-6-[(2R,3R,4R,5S,6R)-3-acetamido-2,5-dihydroxy-6-(hydroxymethyl)oxan-4-yl]oxy-2-carboxy-4,5-dihydroxyoxan-3-yl]oxy-5-hydroxy-6-(hydroxymethyl)oxan-4-yl]oxy-3,4,5-trihydroxyoxane-2-carboxylic acid Chemical compound CC(=O)N[C@H]1[C@H](O)O[C@H](CO)[C@@H](O)[C@@H]1O[C@H]1[C@H](O)[C@@H](O)[C@H](O[C@H]2[C@@H]([C@@H](O[C@H]3[C@@H]([C@@H](O)[C@H](O)[C@H](O3)C(O)=O)O)[C@H](O)[C@@H](CO)O2)NC(C)=O)[C@@H](C(O)=O)O1 KIUKXJAPPMFGSW-DNGZLQJQSA-N 0.000 description 1
- BJEPYKJPYRNKOW-REOHCLBHSA-N (S)-malic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O BJEPYKJPYRNKOW-REOHCLBHSA-N 0.000 description 1
- RBTBFTRPCNLSDE-UHFFFAOYSA-N 3,7-bis(dimethylamino)phenothiazin-5-ium Chemical compound C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 RBTBFTRPCNLSDE-UHFFFAOYSA-N 0.000 description 1
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- 241000293849 Cordylanthus Species 0.000 description 1
- RGHNJXZEOKUKBD-UHFFFAOYSA-N D-gluconic acid Natural products OCC(O)C(O)C(O)C(O)C(O)=O RGHNJXZEOKUKBD-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 235000011054 acetic acid Nutrition 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- BJEPYKJPYRNKOW-UHFFFAOYSA-N alpha-hydroxysuccinic acid Natural products OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 description 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- LCQXXBOSCBRNNT-UHFFFAOYSA-K ammonium aluminium sulfate Chemical compound [NH4+].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O LCQXXBOSCBRNNT-UHFFFAOYSA-K 0.000 description 1
- 150000008064 anhydrides Chemical class 0.000 description 1
- 210000001367 artery Anatomy 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- KDYFGRWQOYBRFD-NUQCWPJISA-N butanedioic acid Chemical compound O[14C](=O)CC[14C](O)=O KDYFGRWQOYBRFD-NUQCWPJISA-N 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 125000002843 carboxylic acid group Chemical group 0.000 description 1
- 238000005341 cation exchange Methods 0.000 description 1
- 229940023913 cation exchange resins Drugs 0.000 description 1
- 235000015165 citric acid Nutrition 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000013373 food additive Nutrition 0.000 description 1
- 239000002778 food additive Substances 0.000 description 1
- 239000000174 gluconic acid Substances 0.000 description 1
- 235000012208 gluconic acid Nutrition 0.000 description 1
- 229920002674 hyaluronan Polymers 0.000 description 1
- 229960003160 hyaluronic acid Drugs 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 235000011167 hydrochloric acid Nutrition 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 230000000968 intestinal effect Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000004310 lactic acid Substances 0.000 description 1
- 235000014655 lactic acid Nutrition 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 239000001630 malic acid Substances 0.000 description 1
- 235000011090 malic acid Nutrition 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 229960000907 methylthioninium chloride Drugs 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000002101 nanobubble Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000036542 oxidative stress Effects 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 235000011007 phosphoric acid Nutrition 0.000 description 1
- 239000002504 physiological saline solution Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
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- 239000011701 zinc Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
Abstract
Description
本發明係有關於一種用以產生含有氫之液體的產生裝置、產生方法以及產生套組。 The present invention relates to a production apparatus, a production method, and a production kit for producing a liquid containing hydrogen.
本專利申請人係以前提議一種對生物適用液之氫添加器具,該氫添加器具係具有:鋁等之氫產生系統,係藉由與水分反應而產生氫氣;及氫氣泡形成體,係具有單向閥收容氫產生系統(專利文獻1)。 The present applicant has previously proposed a hydrogen addition device for a biologically applicable liquid, the hydrogen addition device having a hydrogen generating system such as aluminum, which generates hydrogen by reacting with moisture; and a hydrogen bubble forming body having a single The hydrogen generation system is housed in the valve (Patent Document 1).
【先行專利文獻】 [Prior patent documents]
【專利文獻】 [Patent Literature]
[專利文獻1]日本專利第4652479號公報 [Patent Document 1] Japanese Patent No. 4652479
根據多篇論文等,報告藉由將含氫液體取入生物的體內,可得到抑制氧化壓力等之效用。可是,即使藉飲用等將液體取入體內,亦有量的極限。因此,期望開發即使是相同的量亦含有高濃度氫之液體的產生裝置。本專利申請人係根據以前所提議之該以往的專利,成功地產生10分鐘後之氫濃度為5ppm、24小時後之氫濃度為7ppm的含氫液體,但是在相同的條件無法產生10分鐘後之氫濃度為6ppm、24小時後之氫 濃度超過10ppm的含氫液體。 According to various papers and the like, it is reported that the effect of suppressing oxidative stress and the like can be obtained by taking a hydrogen-containing liquid into a living body. However, even if the liquid is taken into the body by drinking or the like, there is a limit. Therefore, it is desirable to develop a production apparatus that contains a liquid of a high concentration of hydrogen even in the same amount. The applicant of the present patent succeeded in producing a hydrogen-containing liquid having a hydrogen concentration of 5 ppm after 10 minutes and a hydrogen concentration of 7 ppm after 24 hours, according to the prior patent proposed above, but after the same condition could not be produced for 10 minutes. The hydrogen-containing liquid having a hydrogen concentration of 6 ppm and a hydrogen concentration of more than 10 ppm after 24 hours.
本發明所欲解決之課題係提供一種可產生10分鐘後之溶解氫濃度為6ppm、24小時後之溶解氫濃度超過10ppm的含氫液體之含氫液體的產生裝置、產生方法以及產生套組。 SUMMARY OF THE INVENTION The object of the present invention is to provide a hydrogen generating liquid generating apparatus, a production method and a production kit which can produce a hydrogen-containing liquid having a dissolved hydrogen concentration of 6 ppm after 10 minutes and a dissolved hydrogen concentration of more than 10 ppm after 24 hours.
本發明係在含氫液體的產生裝置,藉由將該膠囊之容積(Vml)對該氫產生劑之重量(Wg)的比(V/W)設定成11.4以下,設定成8.2以下更佳,解決該課題,該產生裝置係包括:氫產生劑,係與水分反應而產生氫氣;膠囊,係裝入該氫產生劑,並向外部排出在內部所產生之氫氣;以及容器,係裝入是在該膠囊之內部所產生的氫氣之添加對象的液體。 In the present invention, the ratio of the volume (Vml) of the capsule (Vg) to the weight (Wg) of the hydrogen generator is set to be 11.4 or less, and the ratio is set to 8.2 or less. To solve the problem, the production apparatus includes: a hydrogen generating agent that reacts with moisture to generate hydrogen; a capsule that is charged with the hydrogen generating agent and discharges hydrogen generated inside from the outside; and a container that is loaded A liquid to be added to the hydrogen gas generated inside the capsule.
若依據本發明,可產生10分鐘後之溶解氫濃度為6ppm、24小時後之溶解氫濃度超過10ppm的含氫液體。 According to the present invention, a hydrogen-containing liquid having a dissolved hydrogen concentration of 6 ppm after 10 minutes and a dissolved hydrogen concentration of more than 10 ppm after 24 hours can be produced.
1‧‧‧含氫液體的產生裝置 1‧‧‧Hydrogen-containing liquid generating device
10‧‧‧氫產生體 10‧‧‧ Hydrogen generator
11‧‧‧氫產生劑 11‧‧‧ Hydrogen generator
12‧‧‧袋體 12‧‧‧ bag body
20‧‧‧膠囊 20‧‧‧ capsules
21‧‧‧鴨嘴閥(單向閥、止回閥或氣體透過膜) 21‧‧‧ Duckbill valve (check valve, check valve or gas permeable membrane)
22‧‧‧膠囊本體 22‧‧‧Capsule body
23‧‧‧閥蓋 23‧‧‧ bonnet
24‧‧‧突起片 24‧‧‧protrusion
25‧‧‧狹縫 25‧‧‧slit
30‧‧‧容器 30‧‧‧ Container
31‧‧‧容器本體 31‧‧‧ container body
32‧‧‧蓋 32‧‧‧ Cover
L‧‧‧含有氫氣之液體 L‧‧‧Liquid containing hydrogen
第1圖係表示本發明之含氫液體的產生裝置之一實施形態的構成元件圖。 Fig. 1 is a view showing a constituent element of an embodiment of a hydrogen-containing liquid generating apparatus of the present invention.
第2A圖係表示第1圖之膠囊的立體圖。 Fig. 2A is a perspective view showing the capsule of Fig. 1.
第2B圖係沿著第2A圖之Ⅱ B-Ⅱ B線的剖面圖。 Fig. 2B is a cross-sectional view taken along line B-II B of Fig. 2A.
第2C圖係沿著第2A圖之Ⅱ C-Ⅱ C線的剖面圖。 Figure 2C is a cross-sectional view taken along line C-II C of Figure 2A.
第2D圖係沿著第2B圖之Ⅱ D-Ⅱ D線的箭視圖。 The 2D image is an arrow view along line D-II D of Figure 2B.
第3A圖係表示第1圖所示之含氫液體的產生裝置之使用方法的圖。 Fig. 3A is a view showing a method of using the apparatus for generating a hydrogen-containing liquid shown in Fig. 1.
第3B圖係表示第1圖所示之含氫液體的產生裝置之使用方法的圖。 Fig. 3B is a view showing a method of using the apparatus for generating a hydrogen-containing liquid shown in Fig. 1.
第3C圖係表示第1圖所示之含氫液體的產生裝置之使用方法的圖。 Fig. 3C is a view showing a method of using the apparatus for producing a hydrogen-containing liquid shown in Fig. 1.
第3D圖係表示第1圖所示之含氫液體的產生裝置之使用方法的圖。 Fig. 3D is a view showing a method of using the apparatus for generating a hydrogen-containing liquid shown in Fig. 1.
第3E圖係表示第1圖所示之含氫液體的產生裝置之使用方法的圖。 Fig. 3E is a view showing a method of using the apparatus for generating a hydrogen-containing liquid shown in Fig. 1.
第3F圖係表示第1圖所示之含氫液體的產生裝置之使用方法的圖。 Fig. 3F is a view showing a method of using the apparatus for producing a hydrogen-containing liquid shown in Fig. 1.
第3G圖係表示第1圖所示之含氫液體的產生裝置之使用方法的圖。 Fig. 3G is a view showing a method of using the apparatus for generating a hydrogen-containing liquid shown in Fig. 1.
第3H圖係表示第1圖所示之含氫液體的產生裝置之使用方法的圖。 Fig. 3H is a view showing a method of using the apparatus for generating a hydrogen-containing liquid shown in Fig. 1.
第4圖係表示本發明之含氫液體的產生裝置之其他的實施形態的構成元件圖。 Fig. 4 is a view showing a constituent element of another embodiment of the apparatus for producing a hydrogen-containing liquid of the present invention.
第5圖係表示第4圖所示之含氫液體的產生裝置之使用方法的圖。 Fig. 5 is a view showing a method of using the apparatus for generating a hydrogen-containing liquid shown in Fig. 4.
第6圖係表示本發明之含氫液體的產生裝置及方法產生含氫液體之第1、第2實施例及第1、第2比較例的圖形。 Fig. 6 is a view showing the first and second embodiments and the first and second comparative examples of the hydrogen-containing liquid generating apparatus and method of the present invention.
第7圖係表示本發明之含氫液體的產生裝置及方法產生含氫液體之第3、第4實施例及第3、第4比較例的圖形。 Fig. 7 is a view showing the third, fourth, and third and fourth comparative examples of the hydrogen-containing liquid generating apparatus and method of the present invention.
以下,說明本發明之含氫液體的產生裝置、產生 方法以及產生套組之一實施形態。本實施形態之含氫液體的產生裝置1包括:氫產生劑11,係與水分反應而產生氫氣;膠囊20,係具有在內部所產生之氫氣向外部被排出而來自外部的液體不會被導入的單向閥21(亦可是止回閥或氣體透過膜),並裝入該氫產生劑11;以及容器30,係裝入是在該膠囊20之內部所產生的氫氣之添加對象的液體L。 Hereinafter, an embodiment of a hydrogen-containing liquid generating apparatus, a production method, and a production kit of the present invention will be described. The hydrogen-containing liquid generating apparatus 1 of the present embodiment includes a hydrogen generating agent 11 that reacts with moisture to generate hydrogen gas, and the capsule 20 has a hydrogen gas generated inside that is discharged to the outside and the liquid from the outside is not introduced. a check valve 21 (which may also be a check valve or a gas permeable membrane) and charged with the hydrogen generating agent 11; and a container 30 for charging a liquid L to be added to the inside of the capsule 20 .
本實施形態之液體L包含是使用本實施形態的產生裝置1可使氫分子溶解之對象的液體之全部。液體L係除了水或溶液等以外,還包含飲用水、茶、咖啡等的各種飲料。又,包含在打針、點滴、打點滴等之用途所滲透壓調製的生理食鹽水、為了補充營養劑或電解質所調製的注射溶液、使藥劑溶解之注射溶液、輸血所使用之輸血製劑(輸血用血液)、本人血液、經腸液、為了保存內臟所調製之內臟保存液等。尤其,本實施形態之液體L包含可應用於包含人之動物或植物等之生物的液體。而且,使氫溶解於這種液體L,將依此方式所得之含氫液體利用自口或鼻之吸入或噴霧、自口之飲用、對皮膚或靜脈、動脈之注射等應用於各種生物。含氫液體,尤其含有過飽和之高濃度含氫液體的作用成分是氫,其作用係主要抑制氧化壓力。 The liquid L of the present embodiment includes all of the liquids to which the hydrogen molecules are dissolved by using the production apparatus 1 of the present embodiment. The liquid L contains various beverages such as drinking water, tea, and coffee in addition to water or a solution. In addition, physiological saline containing osmolarity for use in injection, drip, drip, etc., an injection solution prepared by supplementing a nutrient or an electrolyte, an injection solution for dissolving a drug, and a blood transfusion preparation for transfusion (blood for blood transfusion) ), my blood, intestinal fluid, visceral preservation solution prepared to preserve internal organs. In particular, the liquid L of the present embodiment contains a liquid which can be applied to an organism including a human animal or a plant. Further, hydrogen is dissolved in the liquid L, and the hydrogen-containing liquid obtained in this manner is applied to various organisms by inhalation or spraying from the mouth or nose, drinking from the mouth, injection into the skin or vein, arteries, or the like. The hydrogen-containing liquid, especially the active component containing a supersaturated high-concentration hydrogen-containing liquid, is hydrogen, and its action mainly suppresses the oxidative pressure.
本實施形態之氫產生劑11係與水分反應而產生氫氣的材料,具體而言,包含離子化傾向比氫強的金屬材料、及促進此金屬材料與水分之反應的反應促進劑。將在水所透過之袋體12裝入氫產生劑11者稱為氫產生體10。金屬材料係藉由與水分反應而產生氫氣的物質,包含離子化傾向比氫強之金屬單體或含有氫化金屬之氫化化合物等。若考慮與水分之反應性 的良好,適合使用金屬鈣、氫氧化鈣、金屬鎂、氫氧化鎂等。考慮反應產生物之安全性等,尤其適合使用金屬鎂。又,若考慮反應產生物之安全性或食品衛生法,適合使用鐵、鋁、鎳、鈷。其中尤其金屬鋁係從美觀、費用以及使用上之安全性的觀點亦適合使用。 The hydrogen generating agent 11 of the present embodiment is a material that reacts with water to generate hydrogen gas, and specifically includes a metal material having a higher ionization tendency than hydrogen and a reaction accelerator that promotes a reaction between the metal material and water. The hydrogen generator 11 is charged into the bag 12 through which the water passes. The metal material is a substance which generates hydrogen by reacting with moisture, and includes a metal monomer having a higher ionization tendency than hydrogen or a hydrogenated compound containing a hydrogenation metal. When considering the reactivity with water, it is suitable to use metal calcium, calcium hydroxide, magnesium metal, magnesium hydroxide or the like. Metal magnesium is particularly suitable in view of the safety of the reaction product and the like. Further, iron, aluminum, nickel, and cobalt are preferably used in consideration of the safety of the reaction product or the food hygiene method. Among them, metal aluminum is particularly suitable for use in terms of aesthetics, cost, and safety in use.
收容上述之金屬材料极反應促進劑的袋體12係由水所透過之材料所構成。本實施形態之袋體12係為了確實地隔離液體L、金屬材料以及反應促進劑所設置,可舉例表示不織布等之材料。這種袋體12係氫氣或水是透過,但是不會使金屬材料、反應促進劑、其反應殘渣透過。這種袋體12之孔尺寸係1000μm以下,係500μm以下較佳,係150μm以下更佳,係50μm以下尤其佳。就與此袋體12之孔尺寸的關係而言,金屬材料、反應促進劑之平均粒徑係如不會向袋體12之外部透過,且微粒子化所造成之活性的增大亦可期待的粒徑較佳。例如,金屬材料之平均粒徑係3000μm以下,係1000μm以下較佳,係500μm以下更佳,係250μm以下尤其佳。 The bag body 12 containing the above-mentioned metal material polar reaction accelerator is composed of a material through which water passes. The bag body 12 of the present embodiment can be exemplified by a material such as a nonwoven fabric in order to reliably separate the liquid L, the metal material, and the reaction accelerator. The bag 12 is permeated by hydrogen or water, but does not transmit the metal material, the reaction accelerator, and the reaction residue thereof. The pore size of the bag body 12 is preferably 1000 μm or less, preferably 500 μm or less, more preferably 150 μm or less, and particularly preferably 50 μm or less. Regarding the relationship between the pore size of the bag body 12, the average particle diameter of the metal material and the reaction accelerator is not transmitted to the outside of the bag body 12, and the increase in activity caused by the micronization can be expected. The particle size is preferred. For example, the average particle diameter of the metal material is 3,000 μm or less, preferably 1,000 μm or less, more preferably 500 μm or less, and particularly preferably 250 μm or less.
本實施形態之氫產生劑11係除了金屬材料以外,亦可因應於需要,含有金屬離子封鎖劑或pH調整劑等促進氫產生反應的反應促進劑。 The hydrogen generator 11 of the present embodiment may contain a reaction accelerator for promoting a hydrogen generation reaction, such as a metal ion blocking agent or a pH adjuster, in addition to a metal material.
作為在本實施形態可使用之金屬離子封鎖劑,包含水完全或幾乎不會溶解,並產生具有在膠囊20或袋體12的內部吸附金屬離子的性質之物質的物質。陽離子交換樹脂等不溶性或難溶性的金屬離子封鎖劑係適合使用。其中尤其,包含金屬離子之吸附,且釋出氫離子(H+)之以磺酸基為交換基之酸 性陽離子交換樹脂或以羰酸基為交換基之酸性陽離子交換樹脂的氫離子式陽離子交換樹脂係因為亦兼具作為pH調整劑的功能,所以更佳。 The metal ion blocking agent which can be used in the present embodiment contains a substance which completely or hardly dissolves, and which has a property of adsorbing metal ions inside the capsule 20 or the bag body 12. Insoluble or poorly soluble metal ion blocking agents such as cation exchange resins are suitable for use. In particular, hydrogen ion cation exchange of an acidic cation exchange resin containing a sulfonic acid group as an exchange group or an acid cation exchange resin having a carboxylic acid group exchange group, which contains adsorption of metal ions and releases hydrogen ions (H + ) The resin is more preferable because it also functions as a pH adjuster.
作為在本實施形態可使用之pH調整劑,包含具有藉由供給檸檬酸、己二酸、蘋果酸、醋酸、丁二酸、葡萄糖酸、乳酸、磷酸、鹽酸、硫酸等氫離子(H+)而抑制(中和或防止產生)氫氧化物離子(OH-)之性質的物質、及藉由接受水解而形成不溶性之氫氧化物來除去氫氧化物離子的物質。含有鋁離子之礦石等接受水解而形成不溶性之氫氧化物的pH調整劑係適合使用。其中尤其,硫酸銨鋁等之明礬係因為接受水解而產生不溶性之氫氧化鋁,另一方面,亦兼具作為對鎂離子或鈣離子之金屬離子封鎖劑(凝結劑)的功能,所以更佳。如上述所示,氫離子式陽螺紋部或明礬係因為以一劑兼具作為金屬離子封鎖劑的功能與作為pH調整劑的功能,所以是更佳的物質。 The pH adjuster which can be used in the present embodiment includes hydrogen ions (H + ) such as citric acid, adipic acid, malic acid, acetic acid, succinic acid, gluconic acid, lactic acid, phosphoric acid, hydrochloric acid or sulfuric acid. Further, a substance which suppresses (neutralizes or prevents generation of) hydroxide ions (OH - ) and a substance which removes hydroxide ions by receiving hydrolysis to form an insoluble hydroxide. A pH adjuster which is hydrolyzed to form an insoluble hydroxide such as an ore containing aluminum ions is suitably used. In particular, alum such as ammonium aluminum sulfate produces insoluble aluminum hydroxide by hydrolysis, and also functions as a metal ion blocking agent (coagulant) for magnesium ions or calcium ions. . As described above, the hydrogen ion type male thread portion or alum is a better material because it has a function as a metal ion blocking agent and a function as a pH adjusting agent.
進而,作為促進金屬材料之氫產生反應的氫產生反應促進劑,可使用酸或鹼劑等。作為酸,不特別限定為此,但是適合使用在反應後產生固態之沈澱物的酸、或離子交換樹脂等的固態酸等。又,在將鋁或鋅等之兩性金屬用作氫產生劑的情況,除了酸以外,亦可使用氫氧化鈣、氧化鈣、陰離子交換樹脂等鹼劑。其中尤其,氫氧化鈣(消石灰)、生石灰(氧化鈣)、燒結鈣、氧化鎂、氫氧化鎂、陰離子交換樹脂等是食品添加物的鹼劑係適合使用。與鋁等是食品添加物之離子化傾向比氫強的金屬反應而產生沈澱物的氫產生反應促進劑係因為抑制該金屬之金屬離子的氫產生反應後的再溶出,所以實質上 不會改變適用於生物之液體L的特性。 Further, as the hydrogen generation reaction accelerator for promoting the hydrogen generation reaction of the metal material, an acid or an alkali agent or the like can be used. The acid is not particularly limited thereto, but an acid which forms a solid precipitate after the reaction, a solid acid such as an ion exchange resin, or the like is suitably used. Further, when an amphoteric metal such as aluminum or zinc is used as the hydrogen generating agent, an alkali agent such as calcium hydroxide, calcium oxide or an anion exchange resin may be used in addition to the acid. Among them, calcium hydroxide (slaked lime), quicklime (calcium oxide), sintered calcium, magnesium oxide, magnesium hydroxide, anion exchange resin, and the like are suitable as an alkali agent for food additives. A hydrogen generation reaction accelerator which reacts with a metal such as aluminum, which has a higher ionization tendency than a hydrogen, and which generates a precipitate, suppresses re-dissolution after hydrogen generation reaction of the metal ion of the metal, and thus does not substantially change. Suitable for the properties of biological liquid L.
此外,為了抑制金屬材料之老化,金屬離子封鎖劑或pH調整劑等氫產生反應系所含之物質的水合數或含水率係少較佳。即,就水合數而言,3水合物以下,2水合物以下較佳,2水合物以下更佳,1水合物以下尤其佳,是無水合物或無水物較佳。就含水率而言,期望含水率40重量%以下,30重量%以下較佳,20重量%以下更佳,15重量%以下尤其佳。 Further, in order to suppress the aging of the metal material, the hydration number or the water content of the substance contained in the hydrogen generating reaction system such as the metal ion blocking agent or the pH adjusting agent is preferably small. In other words, the hydrate number is preferably 3 or less, 2 or less, more preferably 2 or less, and particularly preferably 1 or less, and is preferably anhydrate or an anhydride. The water content is desirably 40% by weight or less, preferably 30% by weight or less, more preferably 20% by weight or less, and particularly preferably 15% by weight or less.
本實施形態之金屬材料係藉由與水分接觸而在膠囊20內產生氫氣。在這種水分,包含自來水、淨水、離子交換水、精製水、純水、RO水等,但是不限定為此。亦可將上述之液體L本身用作水分。又,因為是水分,亦可是水蒸汽等之氣體。不論含有成分、硬度、液性係如何,只要是含有水分的液體或氣體,可用作本實施形態的水分。 The metal material of the present embodiment generates hydrogen gas in the capsule 20 by contact with moisture. The water content includes tap water, purified water, ion-exchanged water, purified water, pure water, RO water, and the like, but is not limited thereto. The above liquid L itself can also be used as moisture. Further, since it is moisture, it may be a gas such as water vapor. Regardless of the component, hardness, and liquidity, it can be used as the water of the present embodiment as long as it is a liquid or gas containing water.
作為與含有金屬材料之氫產生劑11反應的水分之量的標準,如後述所示,各袋體12瞬間浸漬於液體L等,是水分不殘留於收容氫產生體10之膠囊20之程量的少量較佳。例如,例如殘留於膠囊20內之水分量是10cc以下,是5cc以下較佳,是3cc以下更佳,是1cc以下尤其佳。為了防止這種多餘的水分從袋體12流出至膠囊20內,在膠囊20內或袋體12等含有吸水珠粒、離子交換樹脂(乾式離子交換樹脂係吸水性高而更佳)、吸水紙、玻尿酸、聚丙烯酸等具有吸水性之物質或材料較佳。 As a standard of the amount of moisture which reacts with the hydrogen generating agent 11 containing a metal material, as will be described later, each of the bags 12 is immersed in the liquid L or the like instantaneously, and the amount of moisture does not remain in the capsule 20 in which the hydrogen generating body 10 is accommodated. A small amount is preferred. For example, the amount of water remaining in the capsule 20 is 10 cc or less, preferably 5 cc or less, more preferably 3 cc or less, and particularly preferably 1 cc or less. In order to prevent such excess water from flowing out of the bag body 12 into the capsule 20, the capsule 20 or the bag body 12 or the like contains water absorbing beads and an ion exchange resin (dry ion exchange resin is more excellent in water absorption), and absorbent paper A substance or material having water absorption properties such as hyaluronic acid or polyacrylic acid is preferred.
本實施形態之膠囊20係隔離液體L與氫產生劑11,且經由膠囊20之鴨嘴閥21,將在氫產生體10所產生之氫氣送至 已裝入液體L的容器30內。含有膠囊20之本實施形態的產生裝置1係作為與裝入液體L之容器30不同的構件,或作為預先被裝入容器30之構造部,被收容於容器30。在第1圖表示作為與容器30不同之構件構成膠囊20的實施形態,在第4圖表示將膠囊20裝入容器30之一部分的實施形態,這些之細節將後述。 The capsule 20 of the present embodiment is a separator liquid L and a hydrogen generator 11, and the hydrogen gas generated in the hydrogen generator 10 is sent to the container 30 in which the liquid L is filled via the duckbill valve 21 of the capsule 20. The production device 1 of the present embodiment including the capsule 20 is housed in the container 30 as a member different from the container 30 in which the liquid L is loaded, or as a structure portion previously loaded into the container 30. Fig. 1 shows an embodiment in which the capsule 20 is configured as a member different from the container 30, and Fig. 4 shows an embodiment in which the capsule 20 is placed in one of the containers 30, and the details thereof will be described later.
在第2A圖~第2D圖表示本實施形態之膠囊20的第1實施形態。本實施形態之膠囊20包括膠囊本體22、閥蓋23以及鴨嘴閥21。膠囊本體22係由具有可承受氫產生劑11與水分之反應熱的程度之耐熱性的樹脂材料所成形之有底筒狀的構件,將氫產生體10裝入內部,並將閥蓋23安裝於上部開口。在膠囊本體22之外表面,一體地形成沿著圓周方向以既定間隔所設置的複數片突起片24。此突起片24係用以防止因氫產生劑11與水分之反應熱(亦與金屬材料之種類有關,亦有成為約200℃之高溫者)從膠囊本體22傳至容器30而使該容器30變形的構成。即,設置突起片24,藉由使膠囊20與容器30之接觸距離變長及/或使接觸面積變小,抑制向容器30所傳送的熱。此外,在第2A圖~第2D圖所示的實施形態,將突起片24設置於膠囊本體22之外表面,但是亦可將突起片設置於閥蓋23之外表面。 The first embodiment of the capsule 20 of the present embodiment is shown in Figs. 2A to 2D. The capsule 20 of the present embodiment includes a capsule body 22, a valve cover 23, and a duckbill valve 21. The capsule body 22 is a bottomed cylindrical member formed of a resin material having a heat resistance to withstand the heat of reaction of the hydrogen generating agent 11 and moisture, and the hydrogen generating body 10 is housed inside, and the valve cover 23 is installed. Open at the top. On the outer surface of the capsule body 22, a plurality of projecting pieces 24 which are provided at predetermined intervals in the circumferential direction are integrally formed. The protruding piece 24 is for preventing the heat of reaction between the hydrogen generating agent 11 and moisture (also related to the type of the metal material or the temperature of about 200 ° C) from the capsule body 22 to the container 30 to make the container 30 The composition of the deformation. That is, the projection piece 24 is provided, and the contact distance between the capsule 20 and the container 30 is lengthened and/or the contact area is made small, and the heat transmitted to the container 30 is suppressed. Further, in the embodiment shown in FIGS. 2A to 2D, the protruding piece 24 is provided on the outer surface of the capsule body 22, but the protruding piece may be provided on the outer surface of the valve cover 23.
本實施形態之膠囊20的閥蓋23掌管固持鴨嘴閥21,且封閉膠囊本體22之上部開口的功能。閥蓋23亦與膠囊本體22一樣,由具有可承受氫產生劑11與水分之反應熱的程度之耐熱性的樹脂材料所成形。 The valve cover 23 of the capsule 20 of the present embodiment functions to hold the duckbill valve 21 and close the upper portion of the capsule body 22. Similarly to the capsule body 22, the bonnet 23 is formed of a resin material having a heat resistance to withstand the heat of reaction of the hydrogen generating agent 11 and moisture.
鴨嘴閥21係由具有彈性之樹脂材料所成形,形成鳥嘴狀,並將狹縫25設置於前端的稜線部分。藉此,至膠囊 20內之內壓變高,藉鴨嘴閥21之本身彈性成為狹縫25封閉之狀態,膠囊20內之內壓變高時,抵抗本身彈性,將鴨嘴閥21的狹縫推寬,而排出氫氣。鴨嘴閥21是本發明之單向閥或止回閥的一例。 The duckbill valve 21 is formed of a resin material having elasticity to form a bird's beak, and the slit 25 is provided at a ridge portion of the front end. Thereby, the internal pressure in the capsule 20 becomes high, and the elasticity of the duckbill valve 21 becomes the state in which the slit 25 is closed, and when the internal pressure in the capsule 20 becomes high, the slit of the duckbill valve 21 is pushed against the elasticity of itself. It is wide and emits hydrogen. The duckbill valve 21 is an example of a check valve or a check valve of the present invention.
此外,替代是單向閥或止回閥之一例的鴨嘴閥21,在膠囊20的內部所產生之氫氣係向膠囊20的外部被排出,但是亦可將向膠囊20的內部不導入膠囊20之外部的液體之氫氣透過膜。又,如在後述之第4圖及第5圖之其他的實施形態的說明所示,將膠囊20固定於容器30的蓋32,與第4圖及第5圖之實施形態係相異(該圖之實施形態係將膠囊20設置於容器30的外部),但是亦可將膠囊20裝入容器30的內部。進而,在氫產生劑11混入容器30所裝入之液體L亦無問題的情況,係不限定為單向閥、止回閥、氫氣透過膜等,亦可是在膠囊20的內部所產生之氫氣係向膠囊20的外部被排出,膠囊20之外部的液體係向膠囊20的內部被導入。 Further, instead of the duckbill valve 21 which is an example of a check valve or a check valve, the hydrogen gas generated inside the capsule 20 is discharged to the outside of the capsule 20, but the inside of the capsule 20 may not be introduced into the capsule 20. The external liquid hydrogen permeates the membrane. Further, as described in the fourth embodiment and the fifth embodiment, which will be described later, the capsule 20 is fixed to the lid 32 of the container 30, which is different from the embodiment of Figs. 4 and 5. In the embodiment of the figure, the capsule 20 is placed outside the container 30, but the capsule 20 can also be placed inside the container 30. Further, when the hydrogen generating agent 11 is mixed into the liquid L in the container 30, there is no problem, and the present invention is not limited to a check valve, a check valve, a hydrogen permeable membrane, or the like, and may be hydrogen gas generated inside the capsule 20. The liquid is discharged to the outside of the capsule 20, and the liquid system outside the capsule 20 is introduced into the inside of the capsule 20.
本實施形態之容器30係上述之裝入液體L的容器,並包含下工夫使其內容物不會接觸大氣之密閉的容器。具有蓋之寶特瓶或鋁瓶等具有蓋的容器係包含於密閉的容器。密閉的容器30係以人手拿著易搖晃的方式具有可攜帶的形態與容量較佳。期望2L以下,1L以下較佳,0.5L以下尤其佳之容量之密閉的容器30,但是不限定為此。作為密閉之容器30的材質,較佳的係氫透過性低的容器。這是由於氫透過性愈低,所產生之氫逃往容器30之外部愈少。 The container 30 of the present embodiment is a container in which the liquid L is filled as described above, and includes a sealed container in which the contents are not exposed to the atmosphere. A container having a lid such as a lidt bottle or an aluminum bottle is contained in a sealed container. The hermetic container 30 is preferably portable and has a portable form and capacity. A sealed container 30 having a capacity of preferably 2 L or less, preferably 1 L or less, and particularly preferably 0.5 L or less is not limited thereto. The material of the sealed container 30 is preferably a container having low hydrogen permeability. This is because the lower the hydrogen permeability, the less hydrogen is generated to escape to the outside of the container 30.
容器30之氫透過性係如以下所示測量。即,參考 在日本特願2009-221567所記載之方法等,以成為測量對象之密閉容器內容積之20倍的體積產生穩定地保持大致飽和濃度(在20℃、一個氣壓為1.6ppm)的氫溶解水,且將裝滿淨水(使藤沢市自來水通過活性碳柱所處理的活性碳處理水等)之該密閉容器浸漬於該氫溶解水5小時。然後,測量該淨水之溶解氫濃度,溶解氫濃度是1000ppb以下,是500ppb以下較佳,是100ppb以下更佳,是10ppb以下尤其佳的容器30被包含於本實施形態之氫透過性低的容器。 The hydrogen permeability of the container 30 was measured as shown below. In the method described in Japanese Patent Application No. 2009-221567, the hydrogen is stably maintained at a substantially saturated concentration (at a temperature of 20 ° C and a gas pressure of 1.6 ppm) in a volume of 20 times the internal volume of the sealed container to be measured. The sealed container in which the water was filled with purified water (the activated carbon treated water treated with the activated carbon column of Fujisawa City) was immersed in the hydrogen-dissolved water for 5 hours. Then, the dissolved hydrogen concentration of the purified water is measured, and the dissolved hydrogen concentration is 1000 ppb or less, preferably 500 ppb or less, more preferably 100 ppb or less, and particularly preferably 10 ppb or less, the container 30 is contained in the embodiment having low hydrogen permeability. container.
本實施形態之容器30係不僅具有密閉性,而且具有可承受產生氫所造成之內壓的上升之耐壓性能較佳。是可承受在絕對壓力是0.11MPa,是0.4MPa較佳,是0.5MPa更佳,是0.8MPa更佳之內壓的耐壓容器。碳酸飲料用寶特瓶等係適合使用。本實施形態之容器30係為了可安全地開蓋而在口部具備在打開蓋之中途排洩壓力的機構(通氣槽)較佳。 The container 30 of the present embodiment is preferably not only airtight but also has a pressure resistance which can withstand an increase in internal pressure due to generation of hydrogen. It is a pressure-resistant container that can withstand an internal pressure of 0.11 MPa, 0.4 MPa, 0.5 MPa, and 0.8 MPa. It is suitable for use in carbonated beverages such as PET bottles. The container 30 of the present embodiment is preferably provided with a mechanism (ventilation groove) for discharging pressure in the mouth portion in the mouth to be safely opened.
在本實施形態所得之含氫液體係溶解氫濃度是8ppm以上,是10ppm以上較佳的含氫液體。在本實施形態過飽和含氫液體意指在常溫常壓之溶解度(1.6ppm)以上的溶解氫濃度,尤其8.0ppm以上、9.0ppm以上、10.0ppm以上的高濃度含氫液體。 The hydrogen-containing liquid system obtained in the present embodiment has a dissolved hydrogen concentration of 8 ppm or more and is preferably a hydrogen-containing liquid of 10 ppm or more. In the present embodiment, the supersaturated hydrogen-containing liquid means a dissolved hydrogen concentration at a normal temperature and normal pressure (1.6 ppm) or more, particularly a high-concentration hydrogen-containing liquid of 8.0 ppm or more, 9.0 ppm or more, and 10.0 ppm or more.
其次,一面參照第3A圖~第3H圖,一面說明本實施形態之含氫液體的產生裝置1的使用方法。 Next, a method of using the hydrogen-containing liquid generating apparatus 1 of the present embodiment will be described with reference to FIGS. 3A to 3H.
首先,如第3A圖所示,準備在袋體12內已裝入包含鋁或鎂等之金屬材料及反應促進劑之氫產生劑11的氫產生體10,如第3B圖所示,例如在容器30所裝入之液體L,浸泡約5~6 秒成袋體12變濕,然後,如第3C圖所示,在膠囊本體22之中,裝入剛才變濕之氫產生體10,並以閥蓋23蓋住。此外,在容器30預先將液體L裝滿至上部開口。即,預先將液體L裝滿成空氣儘量不會進入容器30的頂空間(head space)S。 First, as shown in FIG. 3A, a hydrogen generator 10 containing a metal material such as aluminum or magnesium and a hydrogen generator 11 of a reaction accelerator is placed in the bag body 12, as shown in FIG. 3B, for example, The liquid L contained in the container 30 is immersed for about 5 to 6 seconds, and the bag body 12 is wetted. Then, as shown in FIG. 3C, the hydrogen generator 10 which has just been wetted is placed in the capsule body 22, and Covered with a bonnet 23. Further, the liquid L is filled in the container 30 to the upper opening in advance. That is, the liquid L is filled in advance so that the air does not enter the head space S of the container 30 as much as possible.
接著,如第3D圖所示,將膠囊20裝入容器30並以蓋32蓋住。本實施形態之膠囊20係因為比重比液體L小而浮在容器30的液面,但是亦可使用比重比液體L大而沈入容器30內的液體L。不久,因氫產生劑11與水分的反應開始,在膠囊20內產生氫氣,其內壓稍微上升,而克服鴨嘴閥21之本身彈性時,鴨嘴閥21的狹縫25張開,而從該狹縫25排出氫氣。但,因為內壓變高,所以液體L不會從張開之狹縫25流入膠囊20內。 Next, as shown in Fig. 3D, the capsule 20 is placed in the container 30 and covered with a lid 32. The capsule 20 of the present embodiment is suspended in the liquid surface of the container 30 because the specific gravity is smaller than the liquid L. However, the liquid L having a larger specific gravity than the liquid L and sinking into the container 30 may be used. Soon, since the reaction of the hydrogen generating agent 11 with moisture starts, hydrogen gas is generated in the capsule 20, and the internal pressure thereof rises slightly, and when the elasticity of the duckbill valve 21 itself is overcome, the slit 25 of the duckbill valve 21 is opened, and from the narrow The slit 25 discharges hydrogen. However, since the internal pressure becomes high, the liquid L does not flow into the capsule 20 from the slit 25 which is opened.
從膠囊20的內部經由鴨嘴閥21向容器30的內部排出氫氣時,如第3E圖及第3F圖所示,氫氣就滯留於容器30的頂空間S(容器30之上部開口之附近的空間)。在此時,膠囊20係因氫產生劑11與水分之反應熱而成為比較高溫,但是因為與容器30之接觸係藉突起片24所進行,所以高溫之熱不會傳至接觸點。藉此,可防止容器30之變形等。 When hydrogen gas is discharged from the inside of the capsule 20 to the inside of the container 30 via the duckbill valve 21, as shown in Figs. 3E and 3F, hydrogen gas is retained in the head space S of the container 30 (space near the opening of the upper portion of the container 30). . At this time, the capsule 20 is relatively high in temperature due to the reaction heat of the hydrogen generating agent 11 and moisture, but since the contact with the container 30 is performed by the projection piece 24, the heat of high temperature is not transmitted to the contact point. Thereby, deformation or the like of the container 30 can be prevented.
此外,在膠囊20內,藉氫產生劑11與水分之反應所產生的氫氣係經由鴨嘴閥21被釋出至裝入液體L的容器30內,而將高壓、高濃度之氫氣相形成於頂空間S。此外,即使是以沈入液體L中之方式設置本實施形態之產生裝置1的情況,亦所產生之氫分子的大部分係不會溶解於液體L,而首先係移往容器30之頂空間的空氣相。將已將氫產生劑11裝入袋體12的氫產生體10裝入膠囊20時,氫氣係在適量地聚集於膠囊20的內 部後,才作為氫氣氣泡從鴨嘴閥21被排出。換言之,在被排出至液體L中時,因為氫分子係作為已具有某程度之大小的氫氣氣泡被釋出,又因為膠囊20作用為對氫氣的一種止動器,所以不會溶解於液體L,推測首先係移往容器30之頂空間的空氣相。 Further, in the capsule 20, hydrogen generated by the reaction of the hydrogen generating agent 11 and moisture is released into the container 30 filled with the liquid L via the duckbill valve 21, and a high-pressure, high-concentration hydrogen phase is formed on the top. Space S. Further, even in the case where the production apparatus 1 of the present embodiment is provided in such a manner that it sinks into the liquid L, most of the hydrogen molecules generated are not dissolved in the liquid L, but are first moved to the top space of the container 30. The air phase. When the hydrogen generating body 10 in which the hydrogen generating agent 11 has been charged into the bag body 12 is placed in the capsule 20, the hydrogen gas is collected from the inside of the capsule 20 in an appropriate amount, and is then discharged as a hydrogen gas bubble from the duckbill valve 21. In other words, when being discharged into the liquid L, since the hydrogen molecules are released as hydrogen bubbles having a certain degree of size, and since the capsule 20 acts as a stopper to the hydrogen gas, it does not dissolve in the liquid L. It is presumed that the air phase is moved to the top space of the container 30 first.
這藉目視亦被觀察到。例如,將本實施形態之產生裝置1裝入已裝入液體L的容器30內,並使容器30橫向地倒下,照這樣放置不久時,一面在膠囊20內所產生之氫氣間歇地從鴨嘴閥21以氫氣氣泡釋出,一面使氫氣相之體積逐漸地增大下去。換言之,因為所釋出之氫氣的氣泡大小係大,所以在水中上升並快速地移往密閉的容器30之頂空間的氣相。 This is also observed by visual inspection. For example, the generating device 1 of the present embodiment is placed in the container 30 in which the liquid L is filled, and the container 30 is laterally fallen. When it is placed so long, the hydrogen generated in the capsule 20 intermittently from the duckbill. The valve 21 is released by hydrogen gas bubbles, and the volume of the hydrogen phase is gradually increased. In other words, since the released hydrogen gas has a large bubble size, it rises in the water and rapidly moves to the gas phase of the top space of the closed vessel 30.
以往,不限定為氫分子,在利用所謂的起泡作用之氣體溶解技術,認為使氣體之氣泡大小儘量小,即延遲氣泡移往氣相的上升速度,這對製造高濃度之氣體溶液才是重要。含有氫、氧或臭氧之產業用氣體的微米氣泡化或奈米氣泡化係在申請本專利時,依然被認為是該業界之主要的技術課題之一。 Conventionally, it is not limited to hydrogen molecules, and in the gas dissolution technique using a so-called foaming action, it is considered that the bubble size of the gas is as small as possible, that is, the rate of rise of the bubble to the gas phase is delayed, which is to manufacture a gas solution having a high concentration. important. Microbubble or nanobubbles of industrial gases containing hydrogen, oxygen or ozone are still considered to be one of the major technical issues in the industry when applying for this patent.
相對地,本發明者們發現在包含家庭、職場、街上、商店等之各種的場所,在消費者在使用時欲產生高濃度含氫液體的機會,與其使氫分子直接溶解於包含飲用水、茶、咖啡等之飲料的液體,不如首先係將氫氣相形成於密閉的容器30內,且提高容器30的內壓,然後,適當地搖晃密閉的容器30,藉此,回收氣相之氫氣更佳。因此,為了提高含氫液體之溶解氫濃度,如第3G圖所示,將本實施形態之膠囊20裝入密閉的容器30內,且適當地搖晃密閉的容器30較佳。 In contrast, the present inventors have found that in various places including homes, workplaces, streets, shops, and the like, an opportunity for a high-concentration hydrogen-containing liquid to be generated by a consumer when using it, and a hydrogen molecule directly dissolved therein The liquid of the beverage such as tea or coffee is not formed by first forming a hydrogen phase in the sealed container 30, and the internal pressure of the container 30 is increased, and then the sealed container 30 is appropriately shaken, thereby recovering the hydrogen gas in the gas phase. Better. Therefore, in order to increase the dissolved hydrogen concentration of the hydrogen-containing liquid, as shown in Fig. 3G, the capsule 20 of the present embodiment is placed in the sealed container 30, and it is preferable to appropriately shake the sealed container 30.
在本實施形態之搖晃係藉由對密閉的容器30賦與 物理性撞擊,一面使位於氣相之氫氣與密閉之容器30內的液體L接觸,一面將液體L中之溶解氧氣等溶解氣體替換成氫氣。本實施形態之搖晃係除了使用手之自然的搖晃以外,還包含使用機械之人造的搖晃。利用搖晃器、攪拌器、超音波產生裝置等之搖晃係包含於這種人造性搖晃。又,目的在於更加儲存密閉的容器30內之往氣相的氫氣,在將膠囊20裝入密閉的容器30內,並在經過1分鐘後,經過2分鐘後較佳,經過4分鐘後更佳,經過8分鐘後愈佳,經過10分鐘後尤其佳,開始搖晃。又,搖晃時間係為了促進高壓、高濃度氫氣之對生物適用液的溶解,期望以自然搖晃5秒以上,10秒以上較佳,15秒以上更佳,30秒以上愈佳。又,考慮搖晃之容易性,期望在填充生物適用液後,亦在密閉容器設置於容器容量之15%以下,10%以下較佳,5%以下尤其佳之容量設置頂空間,根據以上之使用方法,如第3H圖所示,可得到含氫液體。 In the swaying system of the present embodiment, the gas in the gas phase is brought into contact with the liquid L in the sealed container 30 by the physical impact of the sealed container 30, and the dissolved gas such as dissolved oxygen in the liquid L is replaced. Hydrogen. In addition to the natural shaking of the hand, the shaking system of the present embodiment includes artificial shaking using a machine. A shaking system using a shaker, a stirrer, an ultrasonic generating device or the like is included in such artificial shaking. Further, the purpose is to further store the hydrogen gas in the gas phase in the sealed container 30, and to put the capsule 20 in the sealed container 30, and after 1 minute, it is preferable after 2 minutes, preferably after 4 minutes. The better after 8 minutes, especially after 10 minutes, start to shake. Further, the shaking time is to promote the dissolution of the biologically applicable liquid by the high-pressure and high-concentration hydrogen gas, and it is desirable to shake it naturally for 5 seconds or more, preferably 10 seconds or more, more preferably 15 seconds or more, and more preferably 30 seconds or more. Further, in consideration of the easiness of shaking, it is desirable to set the top space in a sealed container at a capacity of 15% or less, preferably 10% or less, and particularly preferably 5% or less, in accordance with the above method. As shown in Fig. 3H, a hydrogen-containing liquid can be obtained.
第4圖係表示本發明之含氫液體的產生裝置1之其他的實施形態的構成元件圖,第5圖係表示第4圖所示之含氫液體的產生裝置1之使用方法的圖(相當於第3D圖、第3E圖)。該圖所示之產生裝置1係將膠囊20裝入容器30之一部分的實施形態,具體而言,如第4圖所示,將膠囊20設置於容器30的蓋32,如第5圖所示,將蓋32安裝於容器30時,就從容器30的外部向容器30的內部釋出氫氣。即,如第3D圖及第3E圖所示,即使不將膠囊20裝置容器30內,亦向容器30的內部供給氫氣。 Fig. 4 is a view showing a component diagram of another embodiment of the hydrogen-containing liquid generating apparatus 1 of the present invention, and Fig. 5 is a view showing a method of using the hydrogen-containing liquid generating apparatus 1 shown in Fig. 4 (corresponding to Fig. 4 In the 3D and 3E drawings). The apparatus 1 shown in the figure is an embodiment in which the capsule 20 is placed in one of the containers 30. Specifically, as shown in Fig. 4, the capsule 20 is placed on the lid 32 of the container 30, as shown in Fig. 5. When the lid 32 is attached to the container 30, hydrogen gas is released from the outside of the container 30 to the inside of the container 30. That is, as shown in FIGS. 3D and 3E, even if the capsule 20 is not placed in the container 30, hydrogen gas is supplied to the inside of the container 30.
在如以上所示之構成及使用方法的產生裝置1,本 發明者們成功地產生溶解氫濃度為7ppm的含氫液體。但,在相同之條件無法產生氫濃度為8ppm,尤其超過10ppm的含氫液體。不過,因為若使氫產生劑11的重量增加,氫氣之產生量亦增加,所以可提高溶解氫濃度,但是如從上述之使用方法可理解,氫氣之產生量變多時,容器30內的內壓亦變高。因此,需要耐壓高的容器30。又,即使使氫產生劑11的重量增加,亦不會發生未反應之金屬材料殘留而造成浪費。因此,本發明者們重複專心檢討及嘗試錯誤的結果,將氫產生劑11之重量W(連莫耳數亦等價)、與膠囊20之容積V(包含膠囊本體22、閥蓋23以及鴨嘴閥21之內部的容積)的關係設定成既定值時,以適當之氫產生劑11的重量,成功地得到溶解氫濃度超過8ppm的含氫液體。以下,說明本發明之實施例及比較例。 In the apparatus 1 for producing and using the method as described above, the inventors succeeded in producing a hydrogen-containing liquid having a dissolved hydrogen concentration of 7 ppm. However, a hydrogen-containing liquid having a hydrogen concentration of 8 ppm, particularly more than 10 ppm, cannot be produced under the same conditions. However, since the amount of generated hydrogen gas is increased as the weight of the hydrogen generating agent 11 is increased, the dissolved hydrogen concentration can be increased. However, as understood from the above-described method of use, the internal pressure in the container 30 is increased when the amount of hydrogen generated is increased. It also became higher. Therefore, a container 30 having a high withstand pressure is required. Further, even if the weight of the hydrogen generating agent 11 is increased, the unreacted metal material does not remain and is wasted. Therefore, the present inventors repeatedly focused on reviewing and attempting the wrong result, and the weight W of the hydrogen generating agent 11 (equivalent to the molar number) and the volume V of the capsule 20 (including the capsule body 22, the valve cover 23, and the duckbill) When the relationship of the volume inside the valve 21 is set to a predetermined value, a hydrogen-containing liquid having a dissolved hydrogen concentration of more than 8 ppm is successfully obtained by the weight of the appropriate hydrogen generating agent 11. Hereinafter, examples and comparative examples of the present invention will be described.
[實施例] [Examples]
<<第1實施例>> <<First embodiment>>
作為金屬材料之金屬鋁粉末(和光純藥工業股份有限公司製,粒徑係53~150μm,80%以上)與氫氧化鈣(和光純藥工業股份有限公司製)以金屬鋁粉末為75重量%、氫氧化鈣為25重量%的比例混合,而得到0.66g的氫產生劑11。將此0.66g的氫產生劑11包入不織布(旭化成股份有限公司製Precise Regular C5160),並進行熱密封,藉此,得到氫產生體10。又,準備至口部之滿水填充容量為約530cc的碳酸飲料用保特瓶30,對其填充滿藤沢市自來水(水溫為14.6℃)。 Metallic aluminum powder as a metal material (manufactured by Wako Pure Chemical Industries, Ltd., particle size: 53 to 150 μm, 80% or more) and calcium hydroxide (manufactured by Wako Pure Chemical Industries, Ltd.) as a metal aluminum powder of 75% by weight Calcium hydroxide was mixed in a ratio of 25% by weight to obtain 0.66 g of a hydrogen generating agent 11. This hydrogen generating agent 11 of 0.66 g was placed in a nonwoven fabric (Precise Regular C5160, manufactured by Asahi Kasei Co., Ltd.), and heat-sealed to obtain a hydrogen generating body 10. In addition, the bottle 30 for carbonated beverages having a full water filling capacity of about 530 cc was filled in the mouth, and the tap water of the Fujisawa City was filled (the water temperature was 14.6 ° C).
準備內部之容積為5.4ml的膠囊20,如第3B圖所示,將該氫產生體10浸漬於容器30所裝入之自來水5~6秒而使其變 濕後,將此氫產生體10裝入膠囊本體22,再以閥蓋23蓋住。然後,如第3D圖所示,將膠囊20裝入容器30,再以閥蓋23蓋住。準備6套相同者。 A capsule 20 having a volume of 5.4 ml inside is prepared, and as shown in FIG. 3B, the hydrogen generator 10 is immersed in tap water charged in the container 30 for 5 to 6 seconds to be wetted, and then the hydrogen generator 10 is obtained. The capsule body 22 is loaded and covered with a valve cover 23. Then, as shown in Fig. 3D, the capsule 20 is placed in the container 30 and covered with a valve cover 23. Prepare 6 sets of the same person.
對放置10分鐘後及放置24小時後之各個,本發明者之一(具有平均體格之30歲的男性日本人)在慣用手握持保特瓶的中腹部,並僅使手腕左右地動作,藉此,如蓋在手腕上空畫半圓之弧般以2往返/秒之速度往返120次地搖晃(共60秒)。然後,測量各個之內容液體L的溶解氫濃度。在第1表及第6圖表示此結果。此外,溶解氫濃度判定試劑係使用MiZ股份有限公司製之溶解氫判定試劑(包含乙醇、亞甲藍以及白金膠體之酒精類9.88ml),滴定溶解氫濃度。 One of the inventors (a male Japanese with an average physique of 30 years old) held the mid-abdomen of the bottle with the usual hand, and only moved the wrist to the left and right, after each of the ten minutes of standing and after standing for 24 hours. In this way, if the cover is drawn on the wrist, the arc of a semicircle is shaken 120 times at a speed of 2 round trips/second (60 seconds in total). Then, the dissolved hydrogen concentration of each content liquid L was measured. This result is shown in Tables 1 and 6. Further, the dissolved hydrogen concentration determining reagent was a dissolved hydrogen determining reagent (9.88 ml of alcohol containing ethanol, methylene blue, and platinum colloid) manufactured by MiZ Co., Ltd., and the dissolved hydrogen concentration was titrated.
<<第2實施例>> <<2th embodiment>>
準備氫產生體10及容器30係採用相同之條件,膠囊20之內部的容積採用7.5ml者,測量在與該第1實施例相同之條件所得之內容液體L的溶解氫濃度。在第1表及第6圖表示此結果。 The hydrogen generating body 10 and the container 30 were prepared under the same conditions, and the volume of the inside of the capsule 20 was 7.5 ml, and the dissolved hydrogen concentration of the liquid L obtained under the same conditions as in the first example was measured. This result is shown in Tables 1 and 6.
<<第1比較例>> <<The first comparative example>>
準備氫產生劑11及容器30係採用相同之條件,膠囊20之內部的容積採用11.0ml者,測量在與該第1實施例相同之條件所得之內容液體L的溶解氫濃度。在第1表及第6圖表示此結果。 The hydrogen generating agent 11 and the container 30 were prepared under the same conditions. The volume of the inside of the capsule 20 was 11.0 ml, and the dissolved hydrogen concentration of the liquid L obtained under the same conditions as those in the first example was measured. This result is shown in Tables 1 and 6.
<<第2比較例>> <<2nd comparative example>>
準備氫產生劑11及容器30係採用相同之條件,膠囊20之內部的容積採用13.5ml者,測量在與該第1實施例相同之條件所得之內容液體L的溶解氫濃度。在第1表及第6圖表示此結果。 The hydrogen generating agent 11 and the container 30 were prepared under the same conditions, and the volume of the inside of the capsule 20 was 13.5 ml, and the dissolved hydrogen concentration of the liquid L obtained under the same conditions as those in the first example was measured. This result is shown in Tables 1 and 6.
<<考察>> <<Inspection>>
取該第1、第2實施例及第1、第2比較例之溶解氫濃度的變化率(一次微分值)時,在10分鐘後之溶解氫濃度,在第2實施例與第1比較例之間觀察到顯著差異。因此,要使10分鐘後之溶解氫濃度變成6ppm以上,將膠囊20之容積(Vml)對氫產生劑11之重量(Wg)的比(V/W)設定成11.4以下較佳。在此情況,24小時後之溶解氫濃度就超過8ppm。又,要使24小時後之溶解氫濃度變成10ppm以上,將膠囊20之容積(Vml)對氫產生劑11之重量(Wg)的比(V/W)設定成8.2以下較佳。 When the rate of change of the dissolved hydrogen concentration (primary differential value) in the first and second examples and the first and second comparative examples was taken, the dissolved hydrogen concentration after 10 minutes was obtained in the second example and the first comparative example. Significant differences were observed between. Therefore, it is preferable to set the ratio (V/W) of the volume (Vml) of the capsule 20 to the weight (Wg) of the hydrogen generator 11 to be 11.4 or less, so that the dissolved hydrogen concentration after 10 minutes becomes 6 ppm or more. In this case, the dissolved hydrogen concentration after 24 hours exceeded 8 ppm. Moreover, it is preferable to set the ratio (V/W) of the volume (Vml) of the capsule 20 to the weight (Wg) of the hydrogen generator 11 to 8.2 or less in order to make the dissolved hydrogen concentration after 24 hours into 10 ppm or more.
<<第3實施例>> <<3th embodiment>>
除了在第1實施例之氫產生體10的氫產生劑11採用0.65g、碳酸飲料用保特瓶之至口部的滿水填充容量採用300ml、膠囊20之內部的容積採用5.3ml以外,係在和第1實施例相同的條件產生含氫液體,測量所得之內容液體L的溶解氫濃度。在第2表及第7圖表示此結果。 In addition, 0.65 g of the hydrogen generating agent 11 of the hydrogen generator 10 of the first embodiment, 300 ml of the full water filling capacity of the bottle for the carbonated beverage to the mouth, and 5.3 ml of the volume of the inside of the capsule 20 are used. A hydrogen-containing liquid was produced under the same conditions as in the first embodiment, and the dissolved hydrogen concentration of the liquid L obtained was measured. This result is shown in Tables 2 and 7.
<<第4實施例>> <<Fourth embodiment>>
準備氫產生體10及容器30係採用和第3實施例相同之條件,膠囊20之內部的容積採用7.4ml者,測量在與該第3實施例相同之條件所得之內容液體L的溶解氫濃度。在第2表及第7圖表示此結果。 The hydrogen generating body 10 and the container 30 were prepared under the same conditions as those of the third embodiment, and the volume of the inside of the capsule 20 was 7.4 ml, and the dissolved hydrogen concentration of the liquid L obtained under the same conditions as those of the third example was measured. . This result is shown in Tables 2 and 7.
<<第3比較例>> <<3rd comparative example>>
準備氫產生體10及容器30係採用和第3實施例相同之條件,膠囊20之內部的容積採用10.9ml者,測量在與該第3實施例相同之條件所得之內容液體L的溶解氫濃度。在第2表及第7圖表示此結果。 The hydrogen generating body 10 and the container 30 were prepared under the same conditions as those of the third embodiment, and the volume of the inside of the capsule 20 was 10.9 ml, and the dissolved hydrogen concentration of the liquid L obtained under the same conditions as those in the third example was measured. . This result is shown in Tables 2 and 7.
<<第4比較例>> <<4th comparative example>>
準備氫產生體10及容器30係採用和第3實施例相同之條件,膠囊20之內部的容積採用13.3ml者,測量在與該第3實施例相同之條件所得之內容液體L的溶解氫濃度。在第2表及第7圖表示此結果。 The hydrogen generating body 10 and the container 30 were prepared under the same conditions as those of the third embodiment, and the volume of the inside of the capsule 20 was 13.3 ml, and the dissolved hydrogen concentration of the liquid L obtained under the same conditions as those of the third example was measured. . This result is shown in Tables 2 and 7.
<<考察>> <<Inspection>>
取該第3、第4實施例及第3、第4比較例之溶解氫濃度 的變化率(一次微分值)時,在10分鐘後之溶解氫濃度,在第4實施例與第3比較例之間觀察到顯著差異。因此,要使10分鐘後之溶解氫濃度變成6ppm以上,將膠囊20之容積(Vml)對氫產生劑11之重量(Wg)的比(V/W)設定成11.4以下較佳。在此情況,24小時後之溶解氫濃度就超過8ppm。又,要使24小時後之溶解氫濃度變成10ppm以上,將膠囊20之容積(Vml)對氫產生劑11之重量(Wg)的比(V/W)設定成8.2以下較佳。 When the rate of change of the dissolved hydrogen concentration (primary differential value) in the third and fourth examples and the third and fourth comparative examples was taken, the dissolved hydrogen concentration after 10 minutes was obtained in the fourth example and the third comparative example. Significant differences were observed between. Therefore, it is preferable to set the ratio (V/W) of the volume (Vml) of the capsule 20 to the weight (Wg) of the hydrogen generator 11 to be 11.4 or less, so that the dissolved hydrogen concentration after 10 minutes becomes 6 ppm or more. In this case, the dissolved hydrogen concentration after 24 hours exceeded 8 ppm. Moreover, it is preferable to set the ratio (V/W) of the volume (Vml) of the capsule 20 to the weight (Wg) of the hydrogen generator 11 to 8.2 or less in order to make the dissolved hydrogen concentration after 24 hours into 10 ppm or more.
Claims (8)
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