JPH0242467B2 - - Google Patents
Info
- Publication number
- JPH0242467B2 JPH0242467B2 JP62113217A JP11321787A JPH0242467B2 JP H0242467 B2 JPH0242467 B2 JP H0242467B2 JP 62113217 A JP62113217 A JP 62113217A JP 11321787 A JP11321787 A JP 11321787A JP H0242467 B2 JPH0242467 B2 JP H0242467B2
- Authority
- JP
- Japan
- Prior art keywords
- blood
- iron
- hemoglobin
- powder
- blood powder
- 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
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 101
- 239000008280 blood Substances 0.000 claims description 51
- 210000004369 blood Anatomy 0.000 claims description 51
- 229910052742 iron Inorganic materials 0.000 claims description 51
- 239000000843 powder Substances 0.000 claims description 38
- 108010054147 Hemoglobins Proteins 0.000 claims description 24
- 102000001554 Hemoglobins Human genes 0.000 claims description 24
- 229920001661 Chitosan Polymers 0.000 claims description 9
- 244000144972 livestock Species 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 244000144977 poultry Species 0.000 claims description 6
- 239000010802 sludge Substances 0.000 claims description 6
- 239000005996 Blood meal Substances 0.000 claims description 5
- 108091005804 Peptidases Proteins 0.000 claims description 5
- 102000035195 Peptidases Human genes 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims 1
- 229940024999 proteolytic enzymes for treatment of wounds and ulcers Drugs 0.000 claims 1
- 238000010298 pulverizing process Methods 0.000 claims 1
- 238000000034 method Methods 0.000 description 12
- 238000007796 conventional method Methods 0.000 description 11
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 235000013305 food Nutrition 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 241000283690 Bos taurus Species 0.000 description 6
- 239000003814 drug Substances 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 5
- 230000007062 hydrolysis Effects 0.000 description 5
- 238000006460 hydrolysis reaction Methods 0.000 description 5
- 238000011084 recovery Methods 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 208000007502 anemia Diseases 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 150000003278 haem Chemical class 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 235000013594 poultry meat Nutrition 0.000 description 4
- 102000004190 Enzymes Human genes 0.000 description 3
- 108090000790 Enzymes Proteins 0.000 description 3
- 241001465754 Metazoa Species 0.000 description 3
- 208000007536 Thrombosis Diseases 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 229940079593 drug Drugs 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 235000011121 sodium hydroxide Nutrition 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000013076 target substance Substances 0.000 description 3
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 208000015710 Iron-Deficiency Anemia Diseases 0.000 description 2
- 238000000862 absorption spectrum Methods 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229920006317 cationic polymer Polymers 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 235000021067 refined food Nutrition 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 210000002784 stomach Anatomy 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- IMWCPTKSESEZCL-SPSNFJOYSA-H (e)-but-2-enedioate;iron(3+) Chemical compound [Fe+3].[Fe+3].[O-]C(=O)\C=C\C([O-])=O.[O-]C(=O)\C=C\C([O-])=O.[O-]C(=O)\C=C\C([O-])=O IMWCPTKSESEZCL-SPSNFJOYSA-H 0.000 description 1
- UJKPHYRXOLRVJJ-MLSVHJFASA-N CC(O)C1=C(C)/C2=C/C3=N/C(=C\C4=C(CCC(O)=O)C(C)=C(N4)/C=C4\N=C(\C=C\1/N\2)C(C)=C4C(C)O)/C(CCC(O)=O)=C3C Chemical compound CC(O)C1=C(C)/C2=C/C3=N/C(=C\C4=C(CCC(O)=O)C(C)=C(N4)/C=C4\N=C(\C=C\1/N\2)C(C)=C4C(C)O)/C(CCC(O)=O)=C3C UJKPHYRXOLRVJJ-MLSVHJFASA-N 0.000 description 1
- 241000283086 Equidae Species 0.000 description 1
- 241000287828 Gallus gallus Species 0.000 description 1
- 206010018910 Haemolysis Diseases 0.000 description 1
- 206010067482 No adverse event Diseases 0.000 description 1
- 239000004365 Protease Substances 0.000 description 1
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 description 1
- 102000005158 Subtilisins Human genes 0.000 description 1
- 108010056079 Subtilisins Proteins 0.000 description 1
- 241000282887 Suidae Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000012503 blood component Substances 0.000 description 1
- 235000013330 chicken meat Nutrition 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000012790 confirmation Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 235000015872 dietary supplement Nutrition 0.000 description 1
- 210000002249 digestive system Anatomy 0.000 description 1
- 238000006911 enzymatic reaction Methods 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 210000001035 gastrointestinal tract Anatomy 0.000 description 1
- 239000003676 hair preparation Substances 0.000 description 1
- 229960003569 hematoporphyrin Drugs 0.000 description 1
- 108010036302 hemoglobin AS Proteins 0.000 description 1
- 230000008588 hemolysis Effects 0.000 description 1
- 239000012770 industrial material Substances 0.000 description 1
- -1 inorganic iron) Chemical compound 0.000 description 1
- 235000000396 iron Nutrition 0.000 description 1
- 229940082629 iron antianemic preparations Drugs 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 1
- NPFOYSMITVOQOS-UHFFFAOYSA-K iron(III) citrate Chemical compound [Fe+3].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NPFOYSMITVOQOS-UHFFFAOYSA-K 0.000 description 1
- 210000004185 liver Anatomy 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 150000004033 porphyrin derivatives Chemical class 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000001694 spray drying Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000012085 test solution Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Landscapes
- Coloring Foods And Improving Nutritive Qualities (AREA)
- Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
- Medicines Containing Material From Animals Or Micro-Organisms (AREA)
Description
本発明は、家畜類、家禽類の血液をもとにして
得られる鉄高含有血粉に関する。
「産業上の利用分野」
家畜、家禽の屠殺に際して出る血液に関して
は、種々の加工がほどこされ、食品、医薬品の原
料としてまた、工業用素材として有効利用されて
いる。
ことに、血液中の血餅を構成するヘモグロビン
は加水食品であるハムの着色剤や結着剤として多
く利用され、今後もその方面の利用は拡大すると
いわれている。一方、最近のヘモグロビンの新し
い応用分野に、鉄の供給源として貧血者向けの栄
養補助食品、あるいは医薬品への利用が着目され
るようになつてきている。
従来の鉄欠乏性貧血患者、又は貧血体質の人に
はその治療や予防を目的として、硫酸第1鉄、酸
化鉄の様な無機鉄、クエン酸鉄、フマール酸鉄の
様な有機鉄(以下無機鉄を含めて非ヘム鉄とい
う)などの鉄剤を含む医薬品や食品が用いられる
のが一般的であつたが、これら非ヘム鉄は、概し
て体内における吸収効率が低く、それなりの効果
を求めようとする場合、摂取量を多くする必要が
あり、消化器官、特に胃を荒らす場合が多いこと
から敬遠されがちであつた。
他方、ヘモグロビン中に含まれる鉄(以下ヘム
鉄という)は、前述の非ヘム鉄に比して、生物学
的利用率も高く、胃を始めとする消化器管への弊
害もほとんど無く、新しい鉄供給源として見直さ
れてきている。
ウシ、ブタ、馬、ニワトリなどの家畜、家禽類
の血液中成分の10〜15%を占めるヘモグロビン
は、分子量60000〜70000程の蛋白質で、その1分
子に4分子のプロトヘムが結合している。ヘモグ
ロビン1分子中に含まれる鉄は、0.18〜0.24%程
で、食物として人が摂取した場合、ヘモグロビン
は消化吸収され、含まれる鉄は、人のヘモグロビ
ンの合成に利用される。
我々人間は、ヘモグロビンをそのまま食べる習
慣は無く、普通は動物のレバー料理、又は肉料理
などで、知らず知らずのうちに摂つている訳であ
るが、前述した様に、貧血の予防、治療を目的と
した場合は、ヘモグロビンを直接摂つた方が、食
物量、効率の面からしても、好ましいことは言う
までもない。
「従来の技術」
動物の血液からヘモグロビンを得るには、血液
を摂取したのち溶血させ、遠心分離機によつて血
餅部分を分取し、水、有機溶媒等による洗浄によ
つて、繊維質、塩などの不純物を取り除いて精製
される。
蛋白を主体とするヘモグロビンは、安定化のた
め、濃縮乾燥操作によつて得られる粉体(血粉=
ヘモグロビン)の型で、市場に提供されるのが一
般的である。この血粉を可食グレートに仕上げ、
一部貧血者向けの、食品に利用するわけである
が、血粉中の鉄含量は前にも述べた如く、高々の
0.24%程のものであり、例えば、成人女性の1日
の鉄必要量10mgを、血粉のみから摂取しようと仮
定すると、利用効率を考慮に入れると、10g以上
を食べる必要があり、血液特有の生臭さも手伝つ
て、とても摂取不可能な量となつてしまう。こう
したことから、ヘモグロビンをある種の蛋白分解
酵素を用いて処理し、蛋白含量の少ない、つまり
鉄含有率の高い血粉を製造し、前述の用途に供し
ようとする動きが見られる。
そうした鉄高含有血粉製造の従来例の一例を明
記すると以下の様である。
〔従来法〕
不純物を取除いた新鮮な牛血液100を遠心分
離し、血餅約40Kgを得る。これに2.5倍量の水を
加えて溶血させたのち、苛性ソーダの適量を用い
てPHを8.5に調整する。撹拌下に蛋白分解酵素
(アルカラーゼ0.6L ノボインダストリー社製)
1.2Kgを加えて、温度50℃で3時間加水分解を行
なう。反応終了後、系の温度を上昇させて酵素を
失活させた後、PHを塩酸を用いて4.0以下に調整
する。この際、析出する析出物(鉄含有率の高い
ヘモグロビン分解物)を遠心分離機を用いて、ペ
ースト状に回収し、さらにこのペーストを、水を
加えて洗浄することにより、塩等の夾雑物を取除
いた後、再度遠心分離機を用いてペースト状に目
的物を回収する。次いで、スプレードライヤーを
用いて乾燥し、鉄高含有血粉2.0Kgを得る。ここ
で得られた血粉は鉄を1.1%含有している。
しかし、鉄高含有血粉の市場への供給能力、商
品価値を考え合わせた場合、こうした従来の方法
では、次の様な問題があることが否めない。その
1つは、製造工程中、系のPHを酸性側へ移行させ
ることによつて析出してくる目的物(鉄高含有ヘ
モグロビン)は、非常に微細な結晶であること
や、共存する分解液がアミノ酸等を多量に含むた
め、気泡性に富むことなどから、遠心分離機やフ
イルタープレス、その他の回収機による回収効率
が非常に悪く、回収コストが高くつくことにな
り、必然的に製品単価にはね返り市場性も低くな
る。実際、前述の製造法によれば、鉄含量の理論
値からしても3.5Kg程の血粉が得られても良い筈
であるが、2.0Kg(57%の収率)と、回収率が悪
い。他方、得られた鉄高含有血粉は、血液由来物
特有の生臭さを持つており、未加工の血粉に比し
て、使用量が少なくて済むと言つても、やはり食
品として口にし難い欠点は、解消されていない。
「発明が解決しようとする問題点」
本発明者らは、既に動物の血液の有効利用を目
的として、一連のボルフイリン化合物に着目し、
ヘモグロビンから得られるヘマトポルフイリン
等、ポルフイン誘導体を用いた毛髪剤への応用に
ついて、特許公報昭59−14003、昭56−4532に示
される様な開発を行なつているが、本発明は、血
液の有効利用の一端である、鉄高含有血粉の食
品、医薬品への応用を考えるとき、前述した従来
法に見られる種々の欠点を改良し、市場性を向上
させることを目的として、鋭意研究した。
〔発明の構成〕
本発明は、家畜類、家禽類の血液からヘモグロ
ビンを分離、これを加水分解することによつて鉄
として0.3%以上を含む、生臭い味を持たない、
鉄高含有血粉と、及びその製造法にある。製造法
としては、工程中に天然カチオン高分子であるキ
トサンを使用することを特徴とする。詳しくは以
下に開示する。
実施例 1
不純物を取除いた新鮮な牛血液1000Kgを遠心分
離し、血餅約400Kgを得る。これに2.5倍量の水を
加えて溶血させる。(別に出発原料として牛血液
を同様に溶血させ、ヘモグロビンのみを遠心分離
機等で回収し、噴霧乾燥法などで乾燥させ血粉と
なしたのち、殺菌処理を行なつて可食グレードと
して場市されている、一般名ヘモグロビンパウダ
ー150Kgを1500の水に分散させたものでも可能)
次いで苛性ソーダの適量を用いて、PHを8.5に
調整した後、撹拌下に蛋白分解酵素8〜12Kgを加
えて、温度50℃で4〜5時間加水分解を行なう。
酵素反応終了後、系の温度を上昇させて、酵素を
失活させた後、系の温度を40℃以下に降温させ、
塩酸を用いてPHを4.0〜6.0、望ましくは5.5に調整
する。
この操作によつて、次第に不溶物(鉄含量が高
いヘモグロビン分解物)が析出する。次いで、こ
れとは別にキトサン500gを、水100に撹拌下に
分散させたのち、希塩酸を用いてキトサンを溶解
させて調整した粘稠な液を、緩やかに撹拌しなが
ら加える。次いで苛性ソーダを用いて系のPHを
7.0付近に上げる。この際、不溶物はキトサン溶
液の添加によつて相互に凝集し、大きな粒子とな
つて系に懸濁される。
次いでフイルタープレス機を用いて、不溶物を
スラツジとして回収する。スラツジは湿体重量と
して、凡そ200Kg程の物である。スラツジは、再
度反応タンクに返し、2000程の水を加えて撹拌
しながら水洗を行なう。
0.5〜1時間程の水洗後、再びフイルタープレ
ス機を用いて、鉄含量が高いヘモグロビン分解物
のスラツジを回収する。次に減圧乾燥機を用い
て、70〜80℃の温度で乾燥した後、粉砕し、目的
とする鉄高含有血粉を得る。これによつて得られ
る鉄高含有血粉の鉄含有量は、1.0〜1.2%程であ
り、出発原料牛血液1000Kg(牛ヘモグロビンパウ
ダー150Kg)から、35〜40Kg程の鉄高含有血粉が
得られ、収率は90〜95%の高い値となる。
また得られた血粉は、従来法によつて得られた
血粉に比して生臭い臭い、味が極端に少なく、食
品としての価値も、非常に高いものであつた。
(物性及び作用又は効果の確認)
前記実施例で示す鉄高含有血粉に係る物性等の
特徴についての試験の結果を、第1〜2表及び第
1〜3図、第4図に示す。
尚、第4図において用いた検液は、あらかじ
め、試料0.5gを1%NaOH1中に溶解したもの
を用いて行なつた。又、第4図の成績結果(O.D
値)から、本法によつて得られた鉄高含有血粉を
求めてみると、その成績結果は、第2表に示すご
とくとなる。
The present invention relates to blood meal with high iron content obtained from the blood of livestock and poultry. ``Industrial Application Fields'' The blood produced when livestock and poultry are slaughtered is subjected to various processes and is effectively used as a raw material for foods and medicines, as well as as an industrial material. In particular, hemoglobin, which constitutes blood clots, is often used as a coloring agent and binding agent for ham, which is a hydrated food, and it is said that its use in this field will continue to expand in the future. On the other hand, recently, attention has been focused on new fields of application of hemoglobin, such as its use as a source of iron in nutritional supplements for anemic patients and in pharmaceuticals. For patients with conventional iron deficiency anemia or people with anemia predisposition, inorganic iron such as ferrous sulfate and iron oxide, and organic iron (hereinafter referred to as iron) such as iron citrate and iron fumarate are recommended for the treatment and prevention of iron deficiency anemia. It was common to use pharmaceuticals and foods containing iron preparations such as non-heme iron (including inorganic iron), but these non-heme irons generally have low absorption efficiency in the body, so it is difficult to obtain a certain effect. However, it has tended to be avoided because it requires a large intake amount and often irritates the digestive system, especially the stomach. On the other hand, iron contained in hemoglobin (hereinafter referred to as heme iron) has a higher bioavailability than the non-heme iron mentioned above, has almost no adverse effects on the gastrointestinal tract including the stomach, and is a new It is being reconsidered as a source of iron supply. Hemoglobin, which accounts for 10 to 15% of the blood components of livestock such as cows, pigs, horses, and chickens, and poultry, is a protein with a molecular weight of about 60,000 to 70,000, and each molecule has four molecules of protoheme bound to it. Iron contained in one molecule of hemoglobin is about 0.18 to 0.24%, and when ingested by humans as food, hemoglobin is digested and absorbed, and the iron contained is used for the synthesis of human hemoglobin. We humans do not have the habit of eating hemoglobin as it is; we usually consume it in animal liver dishes or meat dishes without realizing it, but as mentioned above, it is used for the prevention and treatment of anemia. In this case, it goes without saying that ingesting hemoglobin directly is preferable in terms of food quantity and efficiency. ``Prior art'' To obtain hemoglobin from animal blood, the blood is ingested, hemolysed, the clot portion is separated using a centrifuge, and the fibrous material is separated by washing with water, organic solvents, etc. It is purified by removing impurities such as salt. Hemoglobin, which is mainly composed of proteins, is made into a powder (blood powder =
Hemoglobin) is commonly offered on the market. This blood powder is made into an edible grade,
It is used in food for some anemic people, but as mentioned earlier, the iron content of blood powder is at most
For example, if we assume that an adult woman's daily iron requirement of 10 mg is ingested only from blood meal, then taking utilization efficiency into account, it is necessary to eat more than 10 g, and the amount of iron that is unique to blood Coupled with the fishy smell, the amount is almost impossible to ingest. For this reason, there is a movement to process hemoglobin with a certain type of proteolytic enzyme to produce blood powder with a low protein content, that is, a high iron content, and to use it for the above-mentioned purposes. An example of a conventional method for producing blood powder with high iron content is as follows. [Conventional method] Centrifuge 100 kg of fresh bovine blood from which impurities have been removed to obtain approximately 40 kg of blood clot. Add 2.5 times the volume of water to hemolyze it, then adjust the pH to 8.5 using an appropriate amount of caustic soda. Add proteolytic enzyme (Alcalase 0.6L, manufactured by Novo Industries) while stirring.
Add 1.2 kg and perform hydrolysis at a temperature of 50°C for 3 hours. After the reaction is completed, the temperature of the system is increased to inactivate the enzyme, and then the pH is adjusted to 4.0 or less using hydrochloric acid. At this time, the precipitate (decomposed product of hemoglobin with high iron content) is collected into a paste using a centrifuge, and this paste is washed with water to remove impurities such as salt. After removing the substance, use a centrifuge again to collect the target substance in a paste form. Next, it is dried using a spray dryer to obtain 2.0 kg of iron-rich blood powder. The blood meal obtained here contains 1.1% iron. However, when considering the ability to supply blood powder with high iron content to the market and the commercial value, it is undeniable that these conventional methods have the following problems. One of these is that during the manufacturing process, the target substance (iron-rich hemoglobin) that precipitates by shifting the pH of the system to the acidic side is a very fine crystal, and the coexisting decomposed liquid contains a large amount of amino acids, etc., and is highly foamy, making recovery efficiency with centrifuges, filter presses, and other recovery equipment extremely poor, resulting in high recovery costs, which inevitably leads to lower product prices. As a result, marketability will decline. In fact, according to the above-mentioned production method, it should be possible to obtain about 3.5 kg of blood meal based on the theoretical value of iron content, but the recovery rate is only 2.0 kg (57% yield), which is poor. . On the other hand, the obtained blood powder with high iron content has a fishy odor characteristic of blood-derived substances, and even though it can be used in a smaller amount than unprocessed blood powder, it still has the disadvantage of being difficult to consume as food. has not been resolved. "Problems to be Solved by the Invention" The present inventors have already focused on a series of volujirin compounds for the purpose of effectively utilizing animal blood.
Regarding the application of porphyrin derivatives such as hematoporphyrin obtained from hemoglobin to hair preparations, as shown in patent publications 14003/1982 and 4532/1982, the present invention When considering the application of iron-rich blood powder to foods and medicines, which is one of the effective uses of iron-rich blood powder, we conducted intensive research with the aim of improving the various shortcomings seen in the conventional methods mentioned above and improving marketability. . [Structure of the Invention] The present invention separates hemoglobin from the blood of livestock and poultry and hydrolyzes it to produce a hemoglobin that contains 0.3% or more of iron and does not have a fishy taste.
High iron content blood powder and its manufacturing method. The manufacturing method is characterized by the use of chitosan, a natural cationic polymer, during the process. Details are disclosed below. Example 1 1000 kg of fresh bovine blood from which impurities have been removed is centrifuged to obtain approximately 400 kg of blood clot. Add 2.5 times the amount of water to this to cause hemolysis. (Separately, bovine blood is similarly hemolysed as a starting material, only the hemoglobin is recovered using a centrifuge, etc., and it is dried using a spray drying method to form blood powder, which is then sterilized and marketed as an edible grade. It is also possible to disperse 150kg of hemoglobin powder in 1500ml of water) Next, adjust the pH to 8.5 using an appropriate amount of caustic soda, add 8 to 12kg of protease while stirring, and adjust the temperature. Hydrolysis is carried out at 50°C for 4-5 hours.
After the enzymatic reaction is completed, the temperature of the system is raised to inactivate the enzyme, and then the temperature of the system is lowered to 40°C or less,
Adjust the pH to 4.0-6.0, preferably 5.5 using hydrochloric acid. By this operation, insoluble matter (decomposed hemoglobin product with high iron content) is gradually precipitated. Next, separately, 500 g of chitosan was dispersed in 100 g of water with stirring, and then a viscous liquid prepared by dissolving chitosan using dilute hydrochloric acid was added while stirring gently. Then, use caustic soda to adjust the pH of the system.
Raise it to around 7.0. At this time, the insoluble matter is mutually aggregated by the addition of the chitosan solution, and suspended in the system as large particles. The insoluble matter is then recovered as sludge using a filter press. The wet weight of sludge is approximately 200 kg. The sludge is returned to the reaction tank, and about 2,000 ml of water is added and washed while stirring. After washing with water for about 0.5 to 1 hour, the filter press machine is used again to recover the sludge of hemoglobin decomposition product with high iron content. Next, it is dried at a temperature of 70 to 80°C using a vacuum dryer, and then pulverized to obtain the desired iron-rich blood powder. The iron content of the iron-rich blood powder obtained by this method is about 1.0 to 1.2%, and from 1000 kg of starting material bovine blood (150 kg of bovine hemoglobin powder), about 35 to 40 kg of iron-rich blood powder can be obtained. The yield is as high as 90-95%. In addition, the obtained blood powder had an extremely low fishy odor and taste compared to blood powder obtained by conventional methods, and its value as a food product was also very high. (Confirmation of physical properties and actions or effects) The results of tests regarding the physical properties and other characteristics of the iron-rich blood powder shown in the above examples are shown in Tables 1 and 2, and Figures 1 and 3, and Figure 4. The test solution used in FIG. 4 was prepared by dissolving 0.5 g of the sample in 1% NaOH1. In addition, the results shown in Figure 4 (OD
When the iron-rich blood powder obtained by this method was determined from the results (value), the results were as shown in Table 2.
【表】【table】
【表】【table】
本発明(実施例)により得られた鉄高含有血粉
は、鉄として0.3%以上を含み、血液由来物質特
有の、生臭い味が殆ど無いことが、大きな特徴で
ある。また、酵素による加水分解終了後、目的物
を回収するために、PHを4.0以下に調整して析出
させなければならなかつた従来法に比して、PH
6.0〜7.0の中性域で効率よく回収できるため、従
来法で得た鉄高含有血粉の様に、食した時の低PH
による刺激味が、全くないことも大きなメリツト
である。
また、天然カオチン性高分子キトサンを用いた
ことは、次の点でも製造効果の向上に役立つてい
る。つまり従来法によつては、加水分解後にPHを
調整することによつて、析出する目的物(鉄高含
有血粉となる)があまりにも微細であるため、固
〜液分離が非常に困難で、一般的なバツチ、連続
遠心分離機による回収や、フイルタープレス機な
どによる回収が商業ベースでは、殆んど不可能で
あつた。この点、キトサンにより凝集した目的物
は、大きな塊状を形成し、最も操作性の良いフイ
ルタープレス機で効率よく回収できることとなつ
た。
本発明による効果は、上記した如くであり、収
率的にも良好で操作性に優れていること、また従
来、加工食品、医薬品への血粉の利用に当つて、
臭い、味の欠点から用途が限定されてきたわけで
あるが、本発明によつて加工食品、医薬品への応
用が大きく拡大することと期待できる。
尚、本発明による実施例1に示す方法によれ
ば、その最終的に得られたところの鉄高含有血粉
には、工程中に用いたキトサンが微量に存在する
ことが推定されるも、第1〜4図に示す赤外部、
紫外部〜可視部にかけてのスペクトルからは、基
本的な点において、特に違いは確認出来なかつ
た。
A major feature of the high-iron-containing blood powder obtained according to the present invention (example) is that it contains 0.3% or more of iron and has almost no fishy taste, which is characteristic of blood-derived substances. In addition, compared to the conventional method, in which the PH had to be adjusted to 4.0 or less before precipitation in order to recover the target product after the completion of hydrolysis by enzymes, the PH
Because it can be efficiently recovered in the neutral range of 6.0 to 7.0, it has a low pH when eaten, unlike iron-rich blood powder obtained by conventional methods.
Another big advantage is that there is no irritating taste. In addition, the use of natural cationic polymer chitosan helps to improve the production efficiency in the following ways. In other words, in the conventional method, by adjusting the PH after hydrolysis, the target substance to be precipitated (which becomes iron-rich blood powder) is so fine that it is extremely difficult to separate solid from liquid. On a commercial basis, recovery using conventional batches, continuous centrifuges, filter presses, etc. is almost impossible. In this respect, the target product agglomerated by chitosan forms large lumps and can be efficiently recovered using a filter press machine, which has the highest operability. The effects of the present invention are as described above, including good yield and excellent operability, and conventional use of blood powder for processed foods and medicines.
Although its uses have been limited due to its odor and taste, it is expected that the present invention will greatly expand its application to processed foods and pharmaceuticals. In addition, according to the method shown in Example 1 according to the present invention, although it is estimated that a trace amount of chitosan used during the process is present in the finally obtained iron-rich blood powder, Infrared light shown in Figures 1 to 4,
From the spectra from the ultraviolet region to the visible region, no particular differences could be confirmed in fundamental respects.
第1〜3図は、KBr錠剤法による、赤外線吸
収スペクトルである。第1図は、本法による鉄高
含有血粉、第2図は、従来法による鉄高含有血
粉、第3図は、未処理血粉(酸素分解する前のも
の)。第4図は、本発明法による鉄高含有血粉、
従来法による鉄高含有血粉、未処理血粉(酸素分
解する前のもの)の紫外部、可視部吸収スペクト
ルを示す。第4図中、Aは本法による鉄高含有血
粉、Bは、従来法による鉄高含有血粉、Cは、加
水分解する前の未処理血粉。
Figures 1 to 3 are infrared absorption spectra obtained by the KBr tablet method. Figure 1 shows high iron content blood powder produced by the present method, Figure 2 shows high iron content blood powder produced by the conventional method, and Figure 3 shows untreated blood powder (before oxygen decomposition). Figure 4 shows iron-rich blood powder produced by the method of the present invention.
The ultraviolet and visible absorption spectra of iron-rich blood powder and untreated blood powder (prior to oxygen decomposition) obtained using the conventional method are shown. In FIG. 4, A is blood powder with high iron content obtained by the present method, B is blood powder with high iron content obtained by the conventional method, and C is untreated blood powder before hydrolysis.
Claims (1)
グロビンに、蛋白分解酵素を反応させ、加水分解
後の溶液に、キトサン溶解液を添加した後、スラ
ツジとして回収、次に、乾燥、粉砕して得られ
た、血液由来の特有の生臭い味が殆ど無く、且
つ、定量するとき、鉄として0.3%以上を含有す
ることを特徴とする、鉄高含有血粉。 2 家畜類、家禽類の血液をもとに得られたヘモ
グロビンに、蛋白分解酵素を反応させ、加水分解
後の溶液に、キトサン溶解液を添加した後、スラ
ツジとして回収することを特徴とする、鉄高含有
血粉の製造法。[Claims] 1. Hemoglobin obtained from the blood of livestock and poultry is reacted with proteolytic enzymes, and a chitosan solution is added to the hydrolyzed solution, which is then collected as a sludge. Next, a blood meal with high iron content, which is obtained by drying and pulverizing, is characterized by having almost no characteristic fishy taste derived from blood, and containing 0.3% or more of iron when quantitatively determined. 2. Hemoglobin obtained from the blood of livestock and poultry is reacted with a proteolytic enzyme, and a chitosan solution is added to the hydrolyzed solution, which is then recovered as a sludge. A method for producing iron-rich blood powder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62113217A JPS63276460A (en) | 1987-05-08 | 1987-05-08 | High iron content blood powder and its manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62113217A JPS63276460A (en) | 1987-05-08 | 1987-05-08 | High iron content blood powder and its manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63276460A JPS63276460A (en) | 1988-11-14 |
| JPH0242467B2 true JPH0242467B2 (en) | 1990-09-21 |
Family
ID=14606541
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62113217A Granted JPS63276460A (en) | 1987-05-08 | 1987-05-08 | High iron content blood powder and its manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63276460A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2524538B2 (en) * | 1990-05-02 | 1996-08-14 | 旭化成工業株式会社 | Method for producing heme iron composite |
-
1987
- 1987-05-08 JP JP62113217A patent/JPS63276460A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63276460A (en) | 1988-11-14 |
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