CA2551051A1 - Process for production of glycine enriched nacl crystals with improved flow - Google Patents

Process for production of glycine enriched nacl crystals with improved flow Download PDF

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Publication number
CA2551051A1
CA2551051A1 CA002551051A CA2551051A CA2551051A1 CA 2551051 A1 CA2551051 A1 CA 2551051A1 CA 002551051 A CA002551051 A CA 002551051A CA 2551051 A CA2551051 A CA 2551051A CA 2551051 A1 CA2551051 A1 CA 2551051A1
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CA
Canada
Prior art keywords
glycine
brine
salt
saturated brine
washing
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.)
Granted
Application number
CA002551051A
Other languages
French (fr)
Other versions
CA2551051C (en
Inventor
Parthasarathi Dastidar
Pushpito Kumar Ghosh
Amar Ballabh
Darshak Rameshbhai Trivedi
Amitava Pramanik
Velayudhan Nair Gopa Kumar
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.)
Council of Scientific and Industrial Research CSIR
Hindustan Unilever Ltd
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
Publication of CA2551051A1 publication Critical patent/CA2551051A1/en
Application granted granted Critical
Publication of CA2551051C publication Critical patent/CA2551051C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01DCOMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D3/00Halides of sodium, potassium or alkali metals in general
    • C01D3/04Chlorides
    • C01D3/06Preparation by working up brines; seawater or spent lyes
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01DCOMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D3/00Halides of sodium, potassium or alkali metals in general
    • C01D3/26Preventing the absorption of moisture or caking of the crystals

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Seasonings (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)

Abstract

The present invention relates to a simple, economical, and efficient cyclic process for producing rhombic dodecahedron shaped glycine enriched, free flowing common salt from brine, said process comprising steps of adding glycine of concentration ranging between 10 to 25% to the saturated brine, evaporating the saturated brine containing glycine to obtain crystals having high content of glycine, with mother liquor, washing the crystals with saturated brine to obtain rhombic dodecahedron shaped glycine enriched common salt having glycine content ranging between 0.5 to 1.0% and a washed brine, combining the mother liquor and the washed brine to obtain resulting brine, subjecting the resultant brine to solar evaporation, and repeating the steps of (iii) to (v) to obtain rhombic dodecahedron shaped glycine enriched common salt from brine with glycine concentration ranging between 0.5 to 1.0%.

Claims (12)

1. A simple, economical, and efficient cyclic process for producing rhombic dodecahedron shaped glycine enriched, free flowing common salt from brine, said process comprising steps of:
(i) adding glycine of concentration ranging between 10 to 25% to the saturated brine, (ii) evaporating the saturated brine containing glycine to obtain crystals having high content of glycine, with mother liquor, (iii) washing the crystals with saturated brine to obtain rhombic dodecahedron shaped glycine enriched common salt having glycine content ranging between 0.5 to 1.0% and a washed brine, (iv) combining the mother liquor and the washed brine to obtain resulting brine, (v) subjecting the resultant brine to solar evaporation, and (vi) repeating the steps of (iii) to (v) to obtain rhombic dodecahedron shaped glycine enriched common salt from brine with glycine concentration ranging between 0.5 to 1.0%.
2. A process as claimed in Claim 1, wherein the brine is selected from a group comprising synthetic brines, natural brines including sea-, sub-soil and lake brines.
3. A process as claimed in Claim 1, wherein evaporation is conducted in the temperature range of 20-40 °C and more preferably solar evaporation under ambient condition.
4. A process as claimed in Claim 1, wherein the initial concentration of Glycine in saturated brine is maintained in the range 22-25 % (w/v).
5. A process as claimed in Claim 1, wherein co-crystallised Glycine can be largely removed from the salt by washing with saturated brine.
6. A process as claimed in Claim 1, wherein the volume of saturated brine taken for washing is such that the Glycine content of the brine becomes 22-25% after washing.
7. A process as claimed in Claim 1, wherein the washings can be directly subjected to solar evaporation to once again produce habit modified salt or combined with the mother liquor remaining after salt preparation and then subjected to solar evaporation.
8. A process as claimed in Claim 1, wherein washing of the salt with saturated brine has no deleterious effect on the morphology of the habit modified salt.
9. A process as claimed in Claim 1, wherein the habit-modified salt has improved flow characteristics because of its near spherical shape.
10. A process as claimed in Claim 1, wherein the habit modified salt has lesser tendency to stick to the surface of plastic.
11. A process as claimed in claim 1, wherein the glycine utilization efficacy is ranging between 95 to 100%.
12. A process as claimed in Claim 1, wherein the glycine in the salt can serve as flavorant, preservative and micronutrient as reported in the prior art on the properties of Glycine.
CA2551051A 2003-12-24 2003-12-24 Process for production of glycine enriched nacl crystals with improved flow Expired - Fee Related CA2551051C (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/IB2003/006237 WO2005066075A1 (en) 2003-12-24 2003-12-24 Process for production of glycine enriched sodium chloride crystals with improved flow

Publications (2)

Publication Number Publication Date
CA2551051A1 true CA2551051A1 (en) 2005-07-21
CA2551051C CA2551051C (en) 2011-08-02

Family

ID=34746632

Family Applications (1)

Application Number Title Priority Date Filing Date
CA2551051A Expired - Fee Related CA2551051C (en) 2003-12-24 2003-12-24 Process for production of glycine enriched nacl crystals with improved flow

Country Status (9)

Country Link
JP (1) JP4805677B2 (en)
CN (1) CN1972869B (en)
BR (1) BR0318682B1 (en)
CA (1) CA2551051C (en)
DE (1) DE10394353B4 (en)
GB (1) GB2440138B (en)
IL (1) IL176542A (en)
MX (1) MXPA06007390A (en)
WO (1) WO2005066075A1 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009087645A1 (en) * 2008-01-07 2009-07-16 Council Of Scientific & Industrial Research Free flowing 100 - 500 mm size spherical crystals of common salt and process for preparation thereof
GB0807919D0 (en) 2008-05-01 2008-06-04 Moorlodge Biotech Ventures Ltd
WO2010002712A2 (en) 2008-06-30 2010-01-07 3M Innovative Properties Company Method of crystallization
US9808030B2 (en) 2011-02-11 2017-11-07 Grain Processing Corporation Salt composition
CN103373735A (en) * 2012-04-27 2013-10-30 北京美华盛工程技术有限公司 Method for producing food-grade sodium chloride and potassium chloride salt with anti-blocking property
BR112015025834B1 (en) * 2013-04-10 2021-12-21 Smart Salt Inc HOMOGENEOUS CO-CRYSTALLIZED SALT PRODUCT, ITS USES AND ITS PREPARATION METHOD
US10881123B2 (en) * 2017-10-27 2021-01-05 Frito-Lay North America, Inc. Crystal morphology for sodium reduction
CN111302362B (en) * 2020-04-03 2021-05-07 天津科技大学 Large-particle spherical salt and preparation method thereof

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3856922A (en) * 1973-11-06 1974-12-24 R Bragdon Process for preparing substantially non-caking sodium chloride
JPH1142064A (en) * 1997-07-28 1999-02-16 Akou Kasei Kk Common salt composition having high mineral content
FI110474B (en) * 1999-01-27 2003-02-14 Modulpo Salts Oy Nutritional physiological salt product, its use and process for its preparation
JP2001061417A (en) * 1999-08-25 2001-03-13 Sanei Gen Ffi Inc Powdery substance-containing composition
KR100427012B1 (en) * 2000-01-12 2004-04-30 오성은 a manufacturing process of a pure salt
AU2001269122B2 (en) * 2000-08-14 2004-06-10 Unilever Plc Granulation process
JP4246407B2 (en) * 2001-04-27 2009-04-02 キッセイ薬品工業株式会社 Liquid seasoning

Also Published As

Publication number Publication date
CA2551051C (en) 2011-08-02
DE10394353B4 (en) 2014-09-11
CN1972869A (en) 2007-05-30
DE10394353T5 (en) 2006-11-23
JP4805677B2 (en) 2011-11-02
JP2007527834A (en) 2007-10-04
AU2003288642A1 (en) 2005-08-12
IL176542A (en) 2010-12-30
WO2005066075A1 (en) 2005-07-21
CN1972869B (en) 2011-03-30
IL176542A0 (en) 2006-10-05
BR0318682B1 (en) 2013-07-16
BR0318682A (en) 2006-12-12
GB0612958D0 (en) 2006-08-30
GB2440138A (en) 2008-01-23
GB2440138B (en) 2009-04-08
MXPA06007390A (en) 2007-03-23

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Effective date: 20181224