JP3518941B2 - Seed-derived mineral composition and method for producing the same - Google Patents
Seed-derived mineral composition and method for producing the sameInfo
- Publication number
- JP3518941B2 JP3518941B2 JP02344896A JP2344896A JP3518941B2 JP 3518941 B2 JP3518941 B2 JP 3518941B2 JP 02344896 A JP02344896 A JP 02344896A JP 2344896 A JP2344896 A JP 2344896A JP 3518941 B2 JP3518941 B2 JP 3518941B2
- Authority
- JP
- Japan
- Prior art keywords
- extraction
- seed
- calcium
- mineral
- magnesium
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 229910052500 inorganic mineral Inorganic materials 0.000 title claims description 73
- 239000011707 mineral Substances 0.000 title claims description 73
- 239000000203 mixture Substances 0.000 title claims description 24
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- IMQLKJBTEOYOSI-GPIVLXJGSA-N Inositol-hexakisphosphate Chemical compound OP(O)(=O)O[C@H]1[C@H](OP(O)(O)=O)[C@@H](OP(O)(O)=O)[C@H](OP(O)(O)=O)[C@H](OP(O)(O)=O)[C@@H]1OP(O)(O)=O IMQLKJBTEOYOSI-GPIVLXJGSA-N 0.000 claims description 42
- 235000002949 phytic acid Nutrition 0.000 claims description 41
- IMQLKJBTEOYOSI-UHFFFAOYSA-N Phytic acid Natural products OP(O)(=O)OC1C(OP(O)(O)=O)C(OP(O)(O)=O)C(OP(O)(O)=O)C(OP(O)(O)=O)C1OP(O)(O)=O IMQLKJBTEOYOSI-UHFFFAOYSA-N 0.000 claims description 40
- 239000000467 phytic acid Substances 0.000 claims description 38
- 229940068041 phytic acid Drugs 0.000 claims description 38
- 239000011777 magnesium Substances 0.000 claims description 33
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 28
- 239000011575 calcium Substances 0.000 claims description 28
- 229910052749 magnesium Inorganic materials 0.000 claims description 28
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 26
- 229910052791 calcium Inorganic materials 0.000 claims description 26
- 159000000007 calcium salts Chemical class 0.000 claims description 19
- 239000002994 raw material Substances 0.000 claims description 15
- 230000007935 neutral effect Effects 0.000 claims description 8
- 159000000000 sodium salts Chemical class 0.000 claims 1
- 238000000605 extraction Methods 0.000 description 69
- 235000010755 mineral Nutrition 0.000 description 68
- 229940091250 magnesium supplement Drugs 0.000 description 27
- 229960005069 calcium Drugs 0.000 description 25
- 241000209094 Oryza Species 0.000 description 13
- 235000007164 Oryza sativa Nutrition 0.000 description 13
- 238000000034 method Methods 0.000 description 13
- 235000009566 rice Nutrition 0.000 description 13
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 12
- 230000000694 effects Effects 0.000 description 9
- 239000007864 aqueous solution Substances 0.000 description 8
- 239000000463 material Substances 0.000 description 8
- 239000002904 solvent Substances 0.000 description 8
- 239000002253 acid Substances 0.000 description 7
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 235000019779 Rapeseed Meal Nutrition 0.000 description 5
- 230000007423 decrease Effects 0.000 description 5
- 235000013305 food Nutrition 0.000 description 5
- 239000004456 rapeseed meal Substances 0.000 description 5
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 4
- 239000001110 calcium chloride Substances 0.000 description 4
- 229910001628 calcium chloride Inorganic materials 0.000 description 4
- MKJXYGKVIBWPFZ-UHFFFAOYSA-L calcium lactate Chemical compound [Ca+2].CC(O)C([O-])=O.CC(O)C([O-])=O MKJXYGKVIBWPFZ-UHFFFAOYSA-L 0.000 description 4
- 239000001527 calcium lactate Substances 0.000 description 4
- 235000011086 calcium lactate Nutrition 0.000 description 4
- 229960002401 calcium lactate Drugs 0.000 description 4
- 230000001965 increasing effect Effects 0.000 description 4
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 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 3
- 102220547770 Inducible T-cell costimulator_A23L_mutation Human genes 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- 229910000019 calcium carbonate Inorganic materials 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
- 238000005259 measurement Methods 0.000 description 3
- 150000007522 mineralic acids Chemical class 0.000 description 3
- 238000010979 pH adjustment Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 235000021067 refined food Nutrition 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 238000003809 water extraction Methods 0.000 description 3
- 241001474374 Blennius Species 0.000 description 2
- 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 2
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000005862 Whey Substances 0.000 description 2
- 102000007544 Whey Proteins Human genes 0.000 description 2
- 108010046377 Whey Proteins Proteins 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 239000010432 diamond Substances 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000000174 gluconic acid Substances 0.000 description 2
- 235000012208 gluconic acid Nutrition 0.000 description 2
- 238000004128 high performance liquid chromatography Methods 0.000 description 2
- 239000004310 lactic acid Substances 0.000 description 2
- 235000014655 lactic acid Nutrition 0.000 description 2
- 229930014626 natural product Natural products 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 235000014347 soups Nutrition 0.000 description 2
- BJEPYKJPYRNKOW-REOHCLBHSA-N (S)-malic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O BJEPYKJPYRNKOW-REOHCLBHSA-N 0.000 description 1
- 240000002791 Brassica napus Species 0.000 description 1
- 235000004977 Brassica sinapistrum Nutrition 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- PHOQVHQSTUBQQK-SQOUGZDYSA-N D-glucono-1,5-lactone Chemical compound OC[C@H]1OC(=O)[C@H](O)[C@@H](O)[C@@H]1O PHOQVHQSTUBQQK-SQOUGZDYSA-N 0.000 description 1
- FEWJPZIEWOKRBE-JCYAYHJZSA-N Dextrotartaric acid Chemical compound OC(=O)[C@H](O)[C@@H](O)C(O)=O FEWJPZIEWOKRBE-JCYAYHJZSA-N 0.000 description 1
- 239000004278 EU approved seasoning Substances 0.000 description 1
- 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 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 1
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric acid Natural products [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 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
- BJEPYKJPYRNKOW-UHFFFAOYSA-N alpha-hydroxysuccinic acid Natural products OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 239000003957 anion exchange resin Substances 0.000 description 1
- 238000004380 ashing Methods 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 235000019658 bitter taste Nutrition 0.000 description 1
- 235000008429 bread Nutrition 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
- -1 calcium carbonate Chemical compound 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 235000015165 citric acid Nutrition 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 235000021438 curry Nutrition 0.000 description 1
- 235000013365 dairy product Nutrition 0.000 description 1
- 238000010908 decantation Methods 0.000 description 1
- 238000004042 decolorization Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 235000013373 food additive Nutrition 0.000 description 1
- 239000002778 food additive Substances 0.000 description 1
- 235000011194 food seasoning agent Nutrition 0.000 description 1
- 238000004108 freeze drying Methods 0.000 description 1
- 239000001530 fumaric acid Substances 0.000 description 1
- 235000011087 fumaric acid Nutrition 0.000 description 1
- 235000012209 glucono delta-lactone Nutrition 0.000 description 1
- 239000000182 glucono-delta-lactone Substances 0.000 description 1
- 229960003681 gluconolactone Drugs 0.000 description 1
- 230000009036 growth inhibition Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 150000002596 lactones Chemical class 0.000 description 1
- 239000012263 liquid product Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 239000011738 major mineral Substances 0.000 description 1
- 235000011963 major mineral Nutrition 0.000 description 1
- 239000001630 malic acid Substances 0.000 description 1
- 235000011090 malic acid Nutrition 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 235000013622 meat product Nutrition 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 235000012149 noodles Nutrition 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 235000021110 pickles Nutrition 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- 159000000001 potassium salts Chemical class 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
- 238000001694 spray drying Methods 0.000 description 1
- 239000011975 tartaric acid Substances 0.000 description 1
- 235000002906 tartaric acid Nutrition 0.000 description 1
- 235000019640 taste Nutrition 0.000 description 1
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 1
- 235000015099 wheat brans Nutrition 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Landscapes
- Coloring Foods And Improving Nutritive Qualities (AREA)
- Cereal-Derived Products (AREA)
- Seeds, Soups, And Other Foods (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、食品素材として有
用な種子起源ミネラル組成物、及びその製造方法に関す
る。TECHNICAL FIELD The present invention relates to a seed-derived mineral composition useful as a food material, and a method for producing the same.
【0002】[0002]
【従来の技術】近年栄養学の発展によって、ミネラルの
生理的意義が明らかになると共に、不足による影響等が
明らかにされ、ミネラル摂取の重要性が認識されてきて
いる。しかし、一方で、食品の加工等により、従来摂取
されていたこれらのミネラルが充分に摂取されていない
等の問題も明らかにされ、ミネラル素材の開発が注目を
集めており、特に天然物由来のミネラルに関心が高まっ
ている。天然物由来のミネラルとして、海草ミネラル、
苦汁あるいは乳清ミネラル等が開発されている。2. Description of the Related Art In recent years, with the development of nutritional science, the physiological significance of minerals has been clarified, and the effects of deficiency have been clarified, and the importance of mineral intake has been recognized. However, on the other hand, problems such as insufficient intake of these minerals that were conventionally ingested due to food processing etc. are also clarified, and the development of mineral materials has attracted attention, especially those derived from natural products. There is growing interest in minerals. As minerals derived from natural products, seaweed minerals,
Bitter or whey minerals have been developed.
【0003】[0003]
【発明が解決しようとする課題】しかし、これまで提案
されている天然物のミネラル素材のうち、海草ミネラル
は、灰化、酸抽出等抽出工程が複雑であるという問題が
ある。苦汁はマグネシウム、カリウム及び塩素が多くミ
ネラルバランスに問題がある。また、苦味が強いので使
用上制約がある。乳清ミネラルは原料、製造コスト等の
点で問題がある。種子は、マグネシウム、カリウム等の
主要ミネラルのほかに、亜鉛、銅、鉄等栄養学的に重要
なミネラルをバランスよく含んでいるにも関わらず、ミ
ネラルの生体利用を阻害するフィチン酸が多量に含まれ
ている等の理由からこれまでミネラル素材として充分に
活用されていなかった。またフィチン酸はカルシウムを
始めとするミネラルと不溶性の塩を形成するので、ミネ
ラル素材の幅広い適用性を阻害する。特開平7−879
30号公報において穀類種皮由来のマグネシウム補給用
組成物及びその製造方法が開示されているが、その抽出
工程は通常の酸を用いる方法であり、必然的に大部分の
フィチン酸も同時に抽出されてしまう。このような抽出
液からフィチン酸を除く方法として陰イオン交換樹脂処
理等あるが、コストの面で実用的でない。更に酸で抽出
した場合中和の工程も必要になる。一方、中性溶液で抽
出を行うと、フィチン酸の抽出を抑えられるがミネラル
の抽出が充分でない。フィチン酸の抽出を抑えながらミ
ネラルを抽出する技術として、特公昭57−39635
号公報が開示されている。ここでは、酒類製造に使用す
る米糠抽出液を得るに際し、炭酸カルシウム等の塩基性
のカルシウムを含む乳酸溶液で抽出することにより、無
機成分を含み、フィチン酸含量の少ない抽出液が得られ
ることが述べられている。しかしながら炭酸カルシウム
添加量を0.5%(w/w)(以下、%と略記する)以
上にするとフィチン酸の抽出は抑えられるが無機成分、
特にマグネシウムの抽出量が無添加時(2,300mg
%)の0.3%(70mg%)以下に低下することが示
されている。このような酒類製造用のミネラル含有水溶
液は、例えば、カルシウム含量が大きいと酵母の生育阻
害がある等、ミネラル含量、pH等に適切な範囲があ
り、添加するカルシウム塩量、抽出されるミネラル量等
も自ずから範囲が限定される。したがって、ミネラル塩
の添加量、抽出pHの広範囲な検討はなされていない。
本発明は、このような現状にかんがみてなされたもので
あり、食品素材としてのミネラル含量特にマグネシウム
含量が高く、かつ、フィチン酸含量の少ない種子起源ミ
ネラル組成物、及びその製造方法を提供することを目的
とする。However, among the natural mineral materials proposed so far, seaweed mineral has a problem that the extraction process such as ashing and acid extraction is complicated. Bitter soup has a large amount of magnesium, potassium and chlorine and has a problem with the mineral balance. In addition, since it has a strong bitterness, there are restrictions in use. Whey minerals have problems in terms of raw materials and manufacturing costs. Seeds contain not only major minerals such as magnesium and potassium, but also nutritionally important minerals such as zinc, copper, and iron in a well-balanced manner, but a large amount of phytic acid that inhibits bioavailability of minerals Until now, it has not been fully utilized as a mineral material because it is included. Phytic acid forms an insoluble salt with minerals such as calcium, which impedes the wide applicability of mineral materials. JP-A-7-879
No. 30, gazette discloses a magnesium supplement composition derived from cereal seed coat and a method for producing the same, but the extraction step is a method using an ordinary acid, and inevitably most phytic acid is also extracted at the same time. I will end up. As a method for removing phytic acid from such an extract, there is an anion exchange resin treatment, but it is not practical in terms of cost. Further, when extracting with an acid, a step of neutralization is also necessary. On the other hand, when the extraction is performed with a neutral solution, the extraction of phytic acid can be suppressed, but the extraction of minerals is not sufficient. As a technology for extracting minerals while suppressing the extraction of phytic acid, Japanese Patent Publication No. 57-39635
Japanese patent publication is disclosed. Here, when obtaining a rice bran extract used for liquor production, by extracting with a lactic acid solution containing basic calcium such as calcium carbonate, an extract containing an inorganic component and having a low phytic acid content may be obtained. Stated. However, when the amount of calcium carbonate added is 0.5% (w / w) (hereinafter abbreviated as%) or more, the extraction of phytic acid is suppressed, but the inorganic component,
Especially when the amount of magnesium extracted is not added (2,300 mg
%) Of 0.3% (70 mg%) or less. Such a mineral-containing aqueous solution for liquor production has an appropriate range of mineral content, pH, etc., such as yeast growth inhibition when the calcium content is large, and the amount of calcium salt to be added and the amount of mineral to be extracted. The range is naturally limited. Therefore, extensive studies on the amount of mineral salt added and the extraction pH have not been made.
The present invention has been made in view of such a current situation, and provides a seed-derived mineral composition having a high mineral content as a food material, particularly a high magnesium content, and a low phytic acid content, and a method for producing the same. With the goal.
【0004】[0004]
【課題を解決するための手段】本発明を概説すると、第
1の発明は、種子起源原料から抽出時に中性カルシウム
塩を添加して抽出されるミネラル組成物において、マグ
ネシウム:フィチン酸の比率が重量比で0.4以上であ
り、かつカルシウム:マグネシウムの比率が重量比で
0.9以上であることを特徴とする種子起源ミネラル組
成物に関し、第2の発明は、種子起源ミネラル抽出時に
中性カルシウム塩を種子起源原料湿重量に対して2%
(w/w)以上添加すること、及びpHを4〜5に調整
して抽出することを特徴とする上記種子起源ミネラル組
成物の製造方法に関する。To give a general description of the invention According to an aspect of the first invention, the neutral calcium during extraction from the seeds origin material
In a mineral composition extracted by adding a salt, the ratio of magnesium: phytic acid is 0.4 or more by weight ratio, and the ratio of calcium: magnesium is 0.9 or more by weight ratio. The second invention relates to a seed-origin mineral composition which comprises:
(W / w) The above method for producing a mineral composition derived from seed, which comprises adding at least (w / w) and adjusting the pH to 4 to 5 for extraction.
【0005】本発明者らは前記課題を解決するための手
段について鋭意検討した結果、カルシウム塩の濃度を高
め、酸性下で抽出することにより、種子起源原料からの
フィチン酸の抽出が抑えられ、かつミネラル成分特にマ
グネシウムの抽出率が低下しないことを見出し、本発明
を完成した。As a result of intensive studies on the means for solving the above-mentioned problems, the inventors of the present invention suppressed the extraction of phytic acid from seed-derived raw materials by increasing the concentration of calcium salt and extracting under acidic conditions, Moreover, they have found that the extraction rate of mineral components, especially magnesium, does not decrease, and completed the present invention.
【0006】本発明において、種子起源原料から抽出さ
れるマグネシウム含量が高く、かつ種子起源原料から抽
出されるフィチン酸含量が低いとは、通常の酸抽出すな
わちカルシウム塩無添加での酸抽出に比較して高い、低
いということであり、より具体的には、種子起源原料か
ら抽出される各マグネシウム:フィチン酸の比率が重量
比で0.4以上であることを特徴とする種子起源ミネラ
ル組成物を得ることが可能であることを意味する。In the present invention, the high magnesium content extracted from the seed-origin raw material and the low phytic acid content extracted from the seed-origin raw material are compared with ordinary acid extraction, that is, acid extraction without addition of calcium salt. The seed-derived mineral composition is characterized in that the ratio of each magnesium: phytic acid extracted from the seed-origin raw material is 0.4 or more by weight ratio. Means that it is possible to obtain
【0007】カルシウム塩の添加によってミネラル特に
マグネシウムの抽出効率が低下せず、フィチン酸の抽出
が抑えられる機作は完全には明らかではないが、溶解性
の低いフィチン(フィチン酸塩)として存在する種子起
源原料中のミネラル特にマグネシウムが、添加されたカ
ルシウムと交換反応を起こすことによって可溶化するも
のと推定される。またカルシウムのフィチン酸塩は他の
ミネラルのフィチン酸塩よりも溶解性が低いためにフィ
チン酸の抽出が抑えられるものと推定される。The mechanism by which the extraction efficiency of minerals, especially magnesium, is not lowered by the addition of calcium salt and the extraction of phytic acid is suppressed is not completely clear, but it exists as phytin (phytate) with low solubility. mineral particular magnesium seed origin in the raw material is presumed to be solubilized by Succoth to put the exchange reaction with the added calcium. Further, it is presumed that the extraction of phytic acid is suppressed because the phytate of calcium has lower solubility than the phytate of other minerals.
【0008】[0008]
【発明の実施の形態】以下、本発明を具体的に説明す
る。本発明で、ミネラルの抽出に用いる種子起源原料
は、種子そのもの、その加工品等のようなものでもよい
が、これまでミネラル含量が高いがフィチン酸含量も高
い等の理由で充分に用いられていなかった脱脂米糠、種
子かす、あるいは小麦ふすま等が用いられる。BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be specifically described below. In the present invention, the seed-origin raw material used for extracting the mineral may be seed itself, a processed product thereof or the like, but it has been sufficiently used so far because of its high mineral content but also high phytic acid content. Non-defatted rice bran, seed meal, wheat bran, etc., which were not used, are used.
【0009】本発明の種子起源ミネラル抽出時に添加す
る中性カルシウム塩の種類としては、抽出条件において
溶解している塩化カルシウム等の無機カルシウム塩や、
乳酸カルシウム等の有機カルシウム塩が好適であり、塩
基性のカルシウム塩、例えば炭酸カルシウム等は好まし
くない。また、カルシウム塩の添加量は、カルシウムと
して種子起源原料に対して2%以上で効果があり、2〜
5%の範囲が好ましい。2%を下回ると本発明の効果が
少なく、5%を上回ると抽出液中のカルシウム残存量が
大きくなるためマグネシウム素材としては適当ではな
い。The types of neutral calcium salts to be added when extracting seed-origin minerals of the present invention include inorganic calcium salts such as calcium chloride dissolved under extraction conditions, and
Organic calcium salts such as calcium lactate are preferred, but basic calcium salts such as calcium carbonate are not preferred. In addition, the addition amount of calcium salt is 2% or more as a calcium with respect to the seed-origin raw material, and is effective.
A range of 5% is preferable. If it is less than 2%, the effect of the present invention is small, and if it exceeds 5%, the amount of residual calcium in the extract becomes large, so that it is not suitable as a magnesium material.
【0010】種子起源ミネラルの抽出は、まず、中性
カルシウム塩を含有する抽出液に種子起源原料を投入
し、その後、pHを4〜5に調整して抽出する方法、
種子起源原料を後で混合した場合pH4〜5になるよう
に中性カルシウム塩及び酸の混合水溶液を予め調整し、
種子起源原料を投入して抽出する方法等があり、いずれ
の方法でもよいが、作業性からはの方法が好ましい。To extract seed-origin minerals, first, the seed-origin raw material is put into an extract containing a neutral calcium salt, and then the pH is adjusted to 4 to 5 for extraction.
When the seed-origin raw materials are later mixed, the mixed aqueous solution of the neutral calcium salt and the acid is preliminarily adjusted to pH 4-5,
There is a method in which a seed-origin raw material is charged and extracted, and any method may be used, but from the viewpoint of workability, the method is preferable.
【0011】抽出pHについては、pH4を大きく下回
ると、フィチン酸の抽出が充分抑えられず、pH5を大
きく上回るとミネラル類の抽出が充分でない。pH調整
はどのような方法によってもよいが、塩酸、硫酸、リン
酸等の無機酸、あるいは乳酸、酢酸、クエン酸、リンゴ
酸、アジピン酸、グルコン酸、コハク酸、酒石酸、フマ
ル酸等の有機酸によって行うことができる。グルコン酸
はグルコノデルタラクトンの水溶液中に生ずるので、該
ラクトンを、その水溶液として使用することも可能であ
る。本発明における種子起源ミネラルの抽出方法は、水
抽出、温水あるいは熱水抽出等一般に使用されるいずれ
の抽出方法でも使用できる。Regarding the extraction pH, if the pH is much lower than 4, the extraction of phytic acid cannot be sufficiently suppressed, and if it is much higher than pH 5, the extraction of minerals is not sufficient. The pH may be adjusted by any method, but inorganic acids such as hydrochloric acid, sulfuric acid and phosphoric acid, or organic acids such as lactic acid, acetic acid, citric acid, malic acid, adipic acid, gluconic acid, succinic acid, tartaric acid and fumaric acid It can be done with an acid. Since gluconic acid is produced in an aqueous solution of gluconodelta lactone, it is also possible to use the lactone as the aqueous solution. The seed-derived mineral extraction method of the present invention may be any extraction method commonly used such as water extraction, hot water extraction, or hot water extraction.
【0012】種子起源原料に対する抽出液量は特に制限
はないが、少なすぎると回収率が低下し、逆に多すぎる
と得られる抽出液のミネラル濃度が低下するため、一般
に、種子起源原料湿重量に対して5〜10倍量の抽出液
が用いられる。上記抽出操作の条件は、一般の水溶性成
分の抽出操作に準じて任意に決定できる。より具体的に
は、抽出温度としては、室温〜60℃程度が採用され
る。温度が低すぎると抽出率が低下し、逆に60℃を大
きく上回ると不必要な成分が抽出され、後処理が面倒に
なる。抽出時間は通常30〜60分程度で充分である。
また、上記2%以上のカルシウム塩添加量範囲(実施例
2の図1)及び抽出pH4〜5の範囲(実施例3の図
2)を考慮して、マグネシウム:フィチン酸の比率を算
出すると、重量比で0.4以上が好ましい範囲となる。
当該比率が0.4未満では、マグネシウムが少なく、フ
ィチン酸が多い本発明の種子起源ミネラル組成物として
は不適当な製品が得られる。There is no particular limitation on the amount of the extract liquid to the seed-origin raw material, but if it is too small, the recovery rate decreases, and conversely, if it is too large, the mineral concentration of the obtained extract liquid decreases. 5 to 10 times the amount of the extract is used. The conditions for the above extraction operation can be arbitrarily determined according to the general extraction operation for water-soluble components. More specifically, a room temperature to about 60 ° C. is adopted as the extraction temperature. If the temperature is too low, the extraction rate will decrease. On the contrary, if it exceeds 60 ° C., unnecessary components will be extracted, and the post-treatment will be troublesome. An extraction time of 30 to 60 minutes is usually sufficient.
Further, when the ratio of magnesium: phytic acid is calculated in consideration of the calcium salt addition amount range of 2% or more (FIG. 1 of Example 2) and the extraction pH 4 to 5 range (FIG. 2 of Example 3). A weight ratio of 0.4 or more is a preferable range.
When the ratio is less than 0.4, a product unsuitable as the seed-origin mineral composition of the present invention containing a small amount of magnesium and a large amount of phytic acid is obtained.
【0013】更に、得られた種子起源ミネラル組成物に
は抽出時に添加した中性カルシウム塩由来のカルシウム
が含まれており、そのマグネシウムとの含量比は、上記
2%以上のカルシウム塩添加量範囲(実施例2の図1)
及び抽出pH4〜5の範囲(実施例3の図2)を考慮す
ると、カルシウム:マグネシウムの比率が重量比で0.
9以上が好適な範囲となる。Further, the obtained seed-derived mineral composition contains calcium derived from the neutral calcium salt added at the time of extraction, and the content ratio with respect to magnesium is 2% or more of the above calcium salt addition amount range. (FIG. 1 of Example 2)
In consideration of the extraction pH range of 4 to 5 (FIG. 2 of Example 3), the calcium: magnesium ratio is 0.
A preferred range is 9 or more.
【0014】上記抽出液の固液分離は、常法に従って行
うことができる。例えば遠心分離、圧搾、ろ過、デカン
テーション等の操作、及びそれらを組合せた操作を例示
できる。上記操作の後、必要に応じ、pH調整、脱色、
減圧濃縮、膜濃縮、スプレードライ、凍結乾燥等の操作
を適宜行うことができ、これらにより、所望の液状形態
や、粉末状形態のミネラル組成物を得ることができる。
なお、抽出工程で添加されたカルシウムは抽出液に一部
残存するが、これはミネラル組成物中のカルシウム源と
して利用される。Solid-liquid separation of the above extract can be carried out by a conventional method. For example, operations such as centrifugation, squeezing, filtration, decantation, etc., and operations combining them can be exemplified. After the above operation, if necessary, pH adjustment, decolorization,
Operations such as vacuum concentration, membrane concentration, spray drying, and freeze-drying can be appropriately performed, and thus, the desired liquid form or powder form of the mineral composition can be obtained.
It should be noted that the calcium added in the extraction step partially remains in the extraction liquid, which is used as a calcium source in the mineral composition.
【0015】本発明で得られる種子起源ミネラル組成物
は、食品としての呈味性を損なうことがないのでそのま
ま食品として、あるいは食品添加物として各種の加工食
品等に添加配合して使用することができる。かかる加工
食品等は、液状品でも固形品でもよく、その代表例とし
ては、例えば、各種液体飲料製品、菓子類、調味料、ス
ープ、カレー、麺類、パン類、漬け物類、畜肉製品、乳
製品、シリアル等を例示できる。これらの加工食品に対
する本発明組成物の添加量は、特に限定されるものでは
ないが、通常0.1〜50%程度の範囲から選択される
のがよい。The seed-derived mineral composition obtained by the present invention does not impair the taste of foods, and therefore it can be used as a food as it is or as a food additive by adding it to various processed foods. it can. Such processed foods may be liquid products or solid products, and typical examples thereof include various liquid beverage products, confectionery, seasonings, soups, curries, noodles, breads, pickles, livestock meat products, dairy products. , Serial, etc. can be exemplified. The amount of the composition of the present invention added to these processed foods is not particularly limited, but is usually selected from the range of about 0.1 to 50%.
【0016】[0016]
【実施例】次に本発明の実施例を示すが、それによって
本発明が限定されるものではない。EXAMPLES Examples of the present invention will be shown below, but the present invention is not limited thereto.
【0017】実施例1 (カルシウム添加の効果)
68mMの塩化カルシウム水溶液(脱脂米糠湿重量に対
してカルシウムとして2.7%)、又はこれと当量の塩
化マグネシウム、塩化ナトリウム、あるいは塩化カリウ
ム溶液を用い、更にpH調整のために、最終で0.01
Nとなるように塩酸を添加し抽出溶媒とした。抽出は脱
脂米糠湿重量の10倍量の抽出溶媒を用いて60℃にて
1時間行った。更に、冷却及びろ過し、種子起源ミネラ
ル抽出液を得た。ミネラルは原子吸光法で測定し、フィ
チン酸はHPLC法で測定した。この抽出液のミネラル
及びフィチン酸の含量は表1の通りであった。測定結果
は脱脂米糠湿重量100gに対する抽出物の量で表し
た。Example 1 (Effect of Calcium Addition) A 68 mM calcium chloride aqueous solution (2.7% as calcium with respect to defatted rice bran wet weight) or an equivalent amount thereof to magnesium chloride, sodium chloride or potassium chloride solution was used. , 0.01 for final pH adjustment
Hydrochloric acid was added so as to obtain N, which was used as an extraction solvent. The extraction was performed at 60 ° C. for 1 hour using an extraction solvent in an amount 10 times the wet weight of defatted rice bran. Further, the mixture was cooled and filtered to obtain a seed-derived mineral extract. Minerals were measured by the atomic absorption method, and phytic acid was measured by the HPLC method. The mineral and phytic acid contents of this extract are shown in Table 1. The measurement result was expressed as the amount of extract per 100 g of defatted rice bran wet weight.
【0018】[0018]
【表1】 [Table 1]
【0019】以上のように、抽出溶媒にカルシウム塩を
添加することによってマグネシウムの抽出率が約2.5
倍になる等全般的にミネラルの抽出効率が高まり、フィ
チン酸の抽出が1/4以下に抑えられ優れた種子起源ミ
ネラル組成物が得られた。またこのような効果はカルシ
ウム塩のみでみられ、マグネシウム、ナトリウム、カリ
ウム塩等ではみられなかった。As described above, the extraction rate of magnesium is about 2.5 by adding calcium salt to the extraction solvent.
As a result, the extraction efficiency of minerals increased overall, and the extraction of phytic acid was suppressed to 1/4 or less, and an excellent seed-derived mineral composition was obtained. Moreover, such an effect was observed only with the calcium salt, but not with the magnesium, sodium, potassium salts and the like.
【0020】実施例2 (pHの抽出効率への影響)
68mMの塩化カルシウム水溶液(脱脂米糠湿重量に対
してカルシウムとして2.7%)を脱脂米糠湿重量の1
0倍量加え、更に塩酸でpHを3.7から5.9に調整
し実施例1と同様に抽出を行った。その結果を図1に示
す。図1において縦軸は、左からマグネシウム/フィチ
ン酸(Mg/Ph)比、ミネラル抽出量(mg%)、フ
ィチン酸(%)を示し、横軸は抽出液pHを示す。また
図1中、白四角印はカルシウム、白ひし形印はマグネシ
ウム、白丸印はフィチン酸、バツ印はMg/Ph比を意
味する。図1にみられるように、pH3.7ではマグネ
シウムの抽出は充分であったが、同時にフィチン酸も抽
出され、またpH5.4ではフィチン酸の抽出は抑えら
れたが、同時にマグネシウムの抽出を抑えられ共に抽出
条件として不充分であるのに対し、pH4.4ではマグ
ネシウムの抽出は良好で、かつフィチン酸の抽出は抑え
られることが確かめられた。Example 2 (Effect of pH on Extraction Efficiency) A 68 mM calcium chloride aqueous solution (2.7% as calcium based on the wet weight of defatted rice bran) was added to 1 wt.
The amount was added in an amount of 0 times, the pH was adjusted to 3.7 to 5.9 with hydrochloric acid, and extraction was performed in the same manner as in Example 1. The result is shown in FIG. In FIG. 1, the vertical axis represents the magnesium / phytic acid (Mg / Ph) ratio, the mineral extraction amount (mg%), and phytic acid (%) from the left, and the horizontal axis represents the extract pH. In FIG. 1, white squares represent calcium, white diamonds represent magnesium, white circles represent phytic acid, and crosses represent Mg / Ph ratio. As shown in FIG. 1, the extraction of magnesium was sufficient at pH 3.7, but phytic acid was also extracted at the same time, and the extraction of phytic acid was suppressed at pH 5.4, but the extraction of magnesium was suppressed at the same time. It was confirmed that the extraction conditions of pH 4.4 are good, and the extraction of phytic acid is suppressed, while the extraction conditions are insufficient.
【0021】実施例3 (カルシウム添加量の影響)
実施例2で抽出pHとして最適であったpH4.4で、
カルシウム添加量を変えて抽出条件を検討した。カルシ
ウム濃度を脱脂米糠湿重量に対して0〜4%となるよう
に調整した抽出溶媒を脱脂米糠湿重量に対して10倍量
加え、更に、塩酸を加えてpHを4.4に調整して、実
施例1と同様に抽出を行った。その結果を図2に示す。
図2において、縦軸は、左からカルシウム/マグネシウ
ム(Ca/Mg)比、Mg/Ph比、ミネラル抽出量
(mg%)、フィチン酸(%)を示し、横軸はカルシウ
ム添加量(g/100g米糠湿重量)を示す。また、図
2中の白四角印、白ひし形印、白丸印、及びバツ印は図
1と同義であり、白三角印はCa/Mg比を意味する。
図2にみられるように、カルシウム添加量が1%以下で
はフィチン酸の抽出量を充分に抑えられないが、2%以
上ではフィチン酸の抽出が充分に抑えられ、かつ、マグ
ネシウムの抽出量はほとんど低下しないことが確かめら
れた。Example 3 (Effect of Calcium Addition) At pH 4.4, which was the optimum extraction pH in Example 2,
The extraction conditions were examined by changing the amount of calcium added. An extraction solvent adjusted to have a calcium concentration of 0 to 4% relative to the wet weight of defatted rice bran was added in an amount 10 times the wet weight of defatted rice bran, and hydrochloric acid was added to adjust the pH to 4.4. The extraction was performed in the same manner as in Example 1. The result is shown in FIG.
In FIG. 2, the vertical axis represents the calcium / magnesium (Ca / Mg) ratio, the Mg / Ph ratio, the mineral extraction amount (mg%), and phytic acid (%) from the left, and the horizontal axis represents the calcium addition amount (g / 100 g rice bran wet weight) is shown. Further, the white square marks, white diamond marks, white circle marks, and cross marks in FIG. 2 have the same meanings as in FIG. 1, and the white triangle marks mean the Ca / Mg ratio.
As shown in FIG. 2, when the amount of calcium added is 1% or less, the amount of phytic acid extracted cannot be sufficiently suppressed, but when it is 2% or more, the amount of phytic acid extracted is sufficiently suppressed, and the amount of magnesium extracted is It was confirmed that there was almost no decrease.
【0022】実施例4 (菜種かすからの抽出)
菜種かすを用いて、実施例1と同様に、68mMの塩化
カルシウム水溶液(菜種かすに対してカルシウムとして
2.7%)を用い、更にpH調整のために最終濃度0.
01Nの塩酸を加え抽出溶媒とした。抽出は菜種かすの
10倍量の抽出溶媒を用いて60℃にて1時間行った。
更に、冷却及びろ過後、種子起源ミネラル抽出液を得
た。ミネラルは原子吸光法で測定し、フィチン酸はHP
LC法で測定した。この抽出液のミネラル及びフィチン
酸の含量は表2の通りであった。測定結果は菜種かす1
00gに対する抽出物の量で表した。Example 4 (Extraction from rapeseed meal) Using rapeseed meal, a 68 mM calcium chloride aqueous solution (2.7% as calcium relative to rapeseed meal) was used in the same manner as in Example 1 to further adjust the pH. For a final concentration of 0.
01N hydrochloric acid was added to serve as an extraction solvent. The extraction was performed at 60 ° C. for 1 hour using an extraction solvent in an amount 10 times that of rapeseed meal.
After cooling and filtration, a seed-derived mineral extract was obtained. Minerals are measured by atomic absorption method, phytic acid is HP
It was measured by the LC method. The mineral and phytic acid contents of this extract are shown in Table 2. The measurement result is rapeseed residue 1
The amount of the extract was expressed with respect to 00 g.
【0023】[0023]
【表2】 [Table 2]
【0024】菜種かすにおいても、カルシウム塩の添加
によって、ミネラルの抽出効率が高められ、フィチン酸
の抽出が抑えられ、優れた種子起源ミネラル組成物が得
られた。Also in rapeseed meal, the addition of calcium salt increased the extraction efficiency of minerals and suppressed the extraction of phytic acid, and an excellent seed-derived mineral composition was obtained.
【0025】実施例5 (乳酸カルシウムの添加効果)
68mMの乳酸カルシウム水溶液を用い、更にpH調整
のために最終濃度0.01Nの塩酸を加え抽出溶媒とし
た。抽出は脱脂米糠の10倍量の抽出溶媒を用いて60
℃にて1時間行った。抽出液は、ろ過後、種子起源ミネ
ラル抽出液を得た。ミネラルは原子吸光法で測定し、フ
ィチン酸はHPLC法で測定した。この抽出液のミネラ
ル及びフィチン酸の含量は表3の通りであった。測定結
果は脱脂米糠100gに対する抽出物の量で表した。Example 5 (Effect of Addition of Calcium Lactate) An aqueous solution of 68 mM calcium lactate was used, and hydrochloric acid having a final concentration of 0.01 N was further added as an extraction solvent for pH adjustment. Extraction was performed using 10 times the amount of extraction solvent of defatted rice bran.
It carried out at 1 degreeC for 1 hour. The extract was filtered to obtain a seed-derived mineral extract. Minerals were measured by the atomic absorption method, and phytic acid was measured by the HPLC method. The contents of minerals and phytic acid in this extract are shown in Table 3. The measurement result was represented by the amount of the extract per 100 g of defatted rice bran.
【0026】[0026]
【表3】 [Table 3]
【0027】乳酸カルシウムでも、マグネシウム等ミネ
ラルの抽出効率を高め、フィチン酸の抽出を抑える効果
があることが示され、優れた種子起源ミネラル組成物が
得られた。Calcium lactate was also shown to have an effect of enhancing the extraction efficiency of minerals such as magnesium and suppressing the extraction of phytic acid, and an excellent seed-derived mineral composition was obtained.
【0028】[0028]
【発明の効果】これまで充分に利用されていなかった種
子起源原料をミネラル源として有効に利用するために、
カルシウム塩を添加することによって有害なフィチン酸
を低減し、有用ミネラル特にマグネシウムの抽出効率を
高めることを簡単な工程で可能にし、有用な種子起源ミ
ネラル組成物を得ることができる。[Effects of the Invention] In order to effectively use seed-origin raw materials that have not been used sufficiently as mineral sources,
By adding a calcium salt, harmful phytic acid can be reduced, and the extraction efficiency of useful minerals, especially magnesium can be increased by a simple process, and a useful seed-derived mineral composition can be obtained.
【図1】抽出液のpHと、脱脂米糠のミネラル抽出量、
及びその組成比との関係を示す図である。[Fig. 1] pH of extract and mineral extraction amount of defatted rice bran,
It is a figure which shows the relationship with and its composition ratio.
【図2】カルシウム添加量と、脱脂米糠のミネラル抽出
量、及びその組成比との関係を示す図である。FIG. 2 is a diagram showing the relationship between the amount of calcium added, the amount of mineral extracted from defatted rice bran, and its composition ratio.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特公 昭57−39635(JP,B1) (58)調査した分野(Int.Cl.7,DB名) A23L 1/304 A23L 1/10 A23L 1/36 ─────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-B-57-39635 (JP, B1) (58) Fields investigated (Int.Cl. 7 , DB name) A23L 1/304 A23L 1/10 A23L 1 / 36
Claims (2)
ム塩を添加して抽出されるミネラル組成物において、マ
グネシウム:フィチン酸の比率が重量比で0.4以上で
あり、かつカルシウム:マグネシウムの比率が重量比で
0.9以上であることを特徴とする種子起源ミネラル組
成物。1. A neutral calciu when extracted from seed-origin raw material.
In the mineral composition extracted by adding sodium salt, the ratio of magnesium: phytic acid is 0.4 or more by weight ratio, and the ratio of calcium: magnesium is 0.9 or more by weight ratio. A seed-derived mineral composition comprising:
ム塩を種子起源原料湿重量に対して2%(w/w)以上
添加すること、及びpHを4〜5に調整して抽出するこ
とを特徴とする請求項1記載の種子起源ミネラル組成物
の製造方法。2. A feature of adding 2% (w / w) or more of a neutral calcium salt to a seed-origin raw material wet weight at the time of extracting seed-origin minerals and adjusting the pH to 4-5. The method for producing a seed-derived mineral composition according to claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP02344896A JP3518941B2 (en) | 1996-01-18 | 1996-01-18 | Seed-derived mineral composition and method for producing the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP02344896A JP3518941B2 (en) | 1996-01-18 | 1996-01-18 | Seed-derived mineral composition and method for producing the same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH09191857A JPH09191857A (en) | 1997-07-29 |
| JP3518941B2 true JP3518941B2 (en) | 2004-04-12 |
Family
ID=12110793
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP02344896A Expired - Lifetime JP3518941B2 (en) | 1996-01-18 | 1996-01-18 | Seed-derived mineral composition and method for producing the same |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3518941B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5211383B2 (en) * | 2009-04-22 | 2013-06-12 | 奥野製薬工業株式会社 | Food quality improver |
| JP5720033B2 (en) * | 2012-12-26 | 2015-05-20 | 奥野製薬工業株式会社 | Food quality improver |
-
1996
- 1996-01-18 JP JP02344896A patent/JP3518941B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH09191857A (en) | 1997-07-29 |
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