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US20150053570A1 - Method for producing amino acid and production apparatus therefor - Google Patents

Method for producing amino acid and production apparatus therefor Download PDF

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Publication number
US20150053570A1
US20150053570A1 US14/229,987 US201414229987A US2015053570A1 US 20150053570 A1 US20150053570 A1 US 20150053570A1 US 201414229987 A US201414229987 A US 201414229987A US 2015053570 A1 US2015053570 A1 US 2015053570A1
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US
United States
Prior art keywords
reaction tank
pump
weight percent
tank
pipes
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.)
Abandoned
Application number
US14/229,987
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English (en)
Inventor
Min-Yen LEE
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Assigned to CHANG, TING-YU reassignment CHANG, TING-YU ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: LEE, MIN-YEN
Publication of US20150053570A1 publication Critical patent/US20150053570A1/en
Abandoned legal-status Critical Current

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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C227/00—Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • C07C227/28—Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton from natural products
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B3/00—Electrolytic production of organic compounds
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B3/00—Electrolytic production of organic compounds
    • C25B3/01—Products
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • 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
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/582—Recycling of unreacted starting or intermediate materials

Definitions

  • the present invention relates to a method for producing amino acids and, in particular, to a method for hydrolyzing feather waste to extract the amino acids, and an apparatus is used to produce the amino acids.
  • the feather waste contains a lot of protein, such as by chemical method to degradation of amino acids, which avoids the pollution generated feather waste, but also has good economic returns, after all is the best way to deal with feathers.
  • feather waste into a container, with the feather waste having a pH value between 8 to 9.5;
  • An advantage of the present invention provides a method for hydrolyzing feather waste to produce the amino acids.
  • FIG. 1 is a block diagram showing a method for producing amino acids according to the present invention.
  • FIG. 2 shows a perspective view of an apparatus used to produce the amino acids according to the present invention and illustrates feather waste to be collected into a first reaction tank.
  • FIG. 3 shows a partial, continued view of the apparatus shown in FIG. 2 and illustrates an alkaline solution, the feather waste and water to be mixed in the first reaction tank to produce a preproduct.
  • FIG. 4 shows a continued view of the apparatus shown in FIG. 3 and illustrates the preproduct to be delivered into a second reaction tank.
  • FIG. 5 shows a continued view of the apparatus shown in FIG. 4 and illustrates an electrolyser conducting electrolysis of the preproduct in the second reaction tank.
  • FIG. 6 shows a continued view of the apparatus shown in FIG. 5 and illustrates the preproduct to be electrolyzed to produce a first product.
  • FIG. 7 shows a continued view of the apparatus shown in FIG. 6 and illustrates an acid solution to be mixed with the first product to produce a second product via neutralization reaction.
  • FIG. 8 shows a continued view of the apparatus shown in FIG. 7 and illustrates the electrolyser conducting electrolysis of the second product in the second reaction tank.
  • FIG. 9 shows a continued view of the apparatus shown in FIG. 8 and illustrates a third product delivered from the second reaction tank to a product tank.
  • FIGS. 1 through 9 show the method and a production apparatus according to the present invention shown in the drawings.
  • the method for producing amino acids comprising:
  • feather waste A into a container and the feather waste A having a pH value between 8 to 9.5, preferably between 9 and 9.5;
  • an alkaline solution B which has a pH value of between 10 and 12, preferably between 10.5 and 11, with from 30 weight percent to 40 weight percent of the feather waste A and from 52 weight percent to 65 weight percent of water, preferably in an amount of 65 weight percent, at room temperature (e.g., 20 degrees Celsius to 30 degrees Celsius) for 12 to 48 hours, preferably mixed for 24 to 48 hours, to produce a preproduct C;
  • the second product F with smaller molecule clusters is suitable for use as fertilizer. Moreover, if desired, the second product F can be electrolyzed again to produce a third product G, which has much smaller molecule clusters to be absorbed by plants easily.
  • the apparatus for producing amino acids according to the present invention includes a first reaction tank 10 , a first solution tank 20 , a second reaction tank 30 , an electrolyser 40 , and a second solution tank 50 .
  • the first reaction tank 10 is adapted for collecting and mixing feather waste A, an alkaline solution B, and water therein.
  • the first reaction tank 10 includes a stirring unit 11 mounted thereon, and a conveyor belt 12 connected thereto for delivering feather waste A.
  • the stirring unit 11 includes a motor 111 and a plurality of mixing blades 112 being actuateable by the motor 111 and rotatable in the first reaction tank 10 .
  • the first solution tank 20 is one-way connected with the first reaction tank 10 and adapted to store and deliver an alkaline solution B to the first reaction tank 10 .
  • the feather waste A, the alkaline solution B, and water are mixed together in the first solution tank 20 to produce a preproduct C.
  • the second reaction tank 30 is one-way connected with the first reaction tank 10 and adapted to store the preproduct C.
  • the electrolyser 40 is electronically connected to the second reaction tank 30 and can conduct electrolysis of the preproduct C in the second reaction tank 30 to produce a first product D.
  • the second solution tank 50 is one-way connected with the second reaction tank 30 and adapted to store and deliver an acid solution E to the second reaction tank 30 .
  • the acid solution E and the first product D are mixed together in the second solution tank 50 to produce a second product F via neutralization reaction.
  • the apparatus includes a product tank 60 one-way connected with the second reaction tank 30 .
  • the electrolyser 40 can conduct electrolysis of the second product F in the second reaction tank 30 to produce a third product G, which has much smaller molecule clusters to be absorbed by plants easily.
  • the apparatus includes a delivering unit 70 , which includes first, second, third, and fourth delivering assemblies 70 a, 70 b, 70 c, and 70 d.
  • the first delivering assembly 70 a is connected between the first reaction tank 10 and the first solution tank 20 and includes a first pump 71 a, and two first pipes 72 a.
  • One of the two first pipes 72 a is connected between the first reaction tank 10 and the first pump 71 a, and the other one of the two first pipes 72 a is connected between the first pump 71 a and the first solution tank 20 .
  • the alkaline solution B is one-way delivered from the first solution tank 20 to the first reaction tank 10 via the first pump 71 a operating.
  • the second delivering assembly 70 b is connected between the first reaction tank 10 and the second reaction tank 30 and includes a second pump 71 b and two second pipes 72 b.
  • One of the two second pipes 72 b is connected between the first reaction tank 10 and the second pump 71 b, and the other one of the two second pipes 72 b is connected between the second pump 71 b and the second reaction tank 30 .
  • the preproduct C is one-way delivered from the first reaction tank 10 to the second reaction tank 30 via the second pump 71 b operating.
  • the third delivering assembly 70 c is connected between the second solution tank 50 and the second reaction tank 30 and includes a third pump 71 c and two third pipes 72 c.
  • One of the two third pipes 72 c is connected between the second solution tank 50 and the third pump 71 c, and the other one of the two second pipes 72 c is connected between the third pump 71 c and the second reaction tank 30 .
  • the acid solution E is one-way delivered from the second solution tank 50 to the second reaction tank 30 via the third pump 71 c operating.
  • the fourth delivering assembly 70 d is connected between the second reaction tank 30 and the product tank 60 and includes a fourth pump 71 d and two fourth pipes 72 d.
  • One of the two fourth pipes 72 d is connected between the second reaction tank 30 and the fourth pump 71 d, and the other one of the two fourth pipes 72 d is connected between the fourth pump 71 d and the product tank 60 .
  • the third product G is one-way delivered from the second reaction tank 30 to the product tank 60 via the fourth pump 71 d operating.
  • the apparatus further includes a casing 80 .
  • the first reaction tank 10 , the first solution tank 20 , the second reaction tank 30 , the electrolyser 40 , the second solution tank 50 , the product tank 60 , and the delivering unit 70 are mounted in the casing 80 .
  • the casing 80 includes two lateral portions 81 , and a first control box 82 is mounted on one of the two lateral portions 81 and electronically connected with the electrolyser 40 , the first pump 71 a, and the second pump 71 b, and a second control box 83 is mounded on the other one of the two lateral portions 81 and electronically connected with the third pump 71 c and the fourth pump 71 d.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Fertilizers (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Processing Of Solid Wastes (AREA)
US14/229,987 2013-08-22 2014-03-30 Method for producing amino acid and production apparatus therefor Abandoned US20150053570A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
TW102129959 2013-08-22
TW102129959A TW201508007A (zh) 2013-08-22 2013-08-22 水解胺基酸製法

Publications (1)

Publication Number Publication Date
US20150053570A1 true US20150053570A1 (en) 2015-02-26

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
US14/229,987 Abandoned US20150053570A1 (en) 2013-08-22 2014-03-30 Method for producing amino acid and production apparatus therefor

Country Status (5)

Country Link
US (1) US20150053570A1 (zh)
JP (1) JP2015040345A (zh)
KR (1) KR20150022683A (zh)
CN (2) CN104419949B (zh)
TW (1) TW201508007A (zh)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105175161A (zh) * 2015-10-22 2015-12-23 浙江省农业科学院 一种复合氨基酸液肥及其制备方法
CN108101716A (zh) * 2018-03-02 2018-06-01 广州惠农农业科技有限公司 一种有机肥及其制备方法

Family Cites Families (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51115280A (en) * 1975-04-03 1976-10-09 Shigeo Otake Process for treating waste liquid from paste-foods production
JPS602393B2 (ja) * 1981-09-25 1985-01-21 株式会社ユアサコーポレーション アミノ酸の製造法
US4386110A (en) * 1982-01-08 1983-05-31 Hiroshima Prefecture Electrical treatment method of soybean protein
US4551274A (en) * 1983-08-22 1985-11-05 Ralston Purina Company Electrolytic treatment of vegetable protein
BE904225A (fr) * 1985-02-14 1986-05-29 Fuji Oil Co Ltd Procede de fractionnement de proteines.
DE3712825A1 (de) * 1987-04-15 1988-11-03 Diamalt Ag Gesamteiweiss-abbauprodukt
JPH01175994A (ja) * 1987-12-28 1989-07-12 Tosoh Corp 蛋白質部分分解物の製造法
JP2804950B2 (ja) * 1992-07-22 1998-09-30 開成科学株式会社 アミノ酸含有肥料の製造方法
CN1209203C (zh) * 2002-12-18 2005-07-06 吕谦 一种羽毛粉的加工处理方法
CN101476134A (zh) * 2007-12-31 2009-07-08 宁波海硕生物科技有限公司 复合银板改性阴极电解生产l-半胱氨酸盐酸盐一水物
CN101372503B (zh) * 2008-08-06 2011-06-15 西北师范大学 从羽毛中提取角蛋白的方法
CN101575749B (zh) * 2009-04-03 2010-12-08 东华大学 一种角蛋白晶须增强的同质复合纤维及其制备方法
TW201111393A (en) * 2009-09-18 2011-04-01 Univ Nat Taiwan Electrolysis for protein modification
CN101724376B (zh) * 2009-12-14 2011-07-27 东北林业大学 利用强碱性降解大豆蛋白制备的木材胶黏剂及其制备方法
CN101979428B (zh) * 2010-10-09 2012-09-19 天津工业大学 一种动物毛发溶解剂及角蛋白溶液的制备方法和用途
CN102416196A (zh) * 2011-02-14 2012-04-18 蒙一纯 一种生物医学工程用角蛋白材料的制备方法
CN102370044A (zh) * 2011-09-30 2012-03-14 哈尔滨工业大学 高蛋白质消化效率的大米蛋白的提取方法
CN102517600B (zh) * 2011-12-07 2014-08-13 四川大学 一种带毛动物皮或毛的电降解方法
CN102719933B (zh) * 2012-07-11 2014-12-17 成都起点投资有限公司 一种羽毛蛋白纤维制备方法
CN102775489A (zh) * 2012-07-31 2012-11-14 上海全宇生物科技遂平有限公司 一种角蛋白质固体及其制备方法

Also Published As

Publication number Publication date
TW201508007A (zh) 2015-03-01
TWI482780B (zh) 2015-05-01
CN104419949B (zh) 2017-04-26
CN203782246U (zh) 2014-08-20
KR20150022683A (ko) 2015-03-04
JP2015040345A (ja) 2015-03-02
CN104419949A (zh) 2015-03-18

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Legal Events

Date Code Title Description
AS Assignment

Owner name: CHANG, TING-YU, TAIWAN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:LEE, MIN-YEN;REEL/FRAME:032577/0739

Effective date: 20140326

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION