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WO1999065600A1 - A method for formulating particles - Google Patents

A method for formulating particles Download PDF

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Publication number
WO1999065600A1
WO1999065600A1 PCT/NO1999/000172 NO9900172W WO9965600A1 WO 1999065600 A1 WO1999065600 A1 WO 1999065600A1 NO 9900172 W NO9900172 W NO 9900172W WO 9965600 A1 WO9965600 A1 WO 9965600A1
Authority
WO
WIPO (PCT)
Prior art keywords
particles
solution
inert
formulating
medium
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.)
Ceased
Application number
PCT/NO1999/000172
Other languages
French (fr)
Inventor
Ola Jonassen
Ingvald STRØMMEN
Per Arne Schieflo
Odilio Alves-Filho
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.)
Leiv Eiriksson Nyfotek AS
Original Assignee
Leiv Eiriksson Nyfotek AS
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 Leiv Eiriksson Nyfotek AS filed Critical Leiv Eiriksson Nyfotek AS
Priority to CA002333995A priority Critical patent/CA2333995C/en
Priority to EP99925481A priority patent/EP1091799A1/en
Priority to JP2000554470A priority patent/JP2002518155A/en
Priority to US09/701,551 priority patent/US6363743B1/en
Priority to AU41746/99A priority patent/AU4174699A/en
Publication of WO1999065600A1 publication Critical patent/WO1999065600A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/003Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic followed by coating of the granules
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/02Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops

Definitions

  • the present invention is related to a method for formulating particles from solutions for processing in a fluid bed.
  • the method according to the invention may be utilized to produce frozen fluidable particles of solutions thereby using an inert medium in such a way that the solutions may be dried in a fluidized drying chamber.
  • the inert medium as such is disappearing by supplication during drying or already during the formulation of the particles.
  • the method also may be utilized for particle formation if the need for further processing is not drying, but may be performed in a fluid bed.
  • the solution to be dried is cooled down to the initial freezing point. Thereafter the solution is mixed with the inert medium under pressure, thereafter to be expanded to compact, frozen particles comprising the inert medium as well as the solution in a frozen state.
  • the fluidable particles may be produced from the inert medium which thereafter is covered by the solution.
  • the particles normally are produced in a size of 0,5 to 5 mm.
  • the inert medium to be sublimized during drying or expansion can be for example be N 2 , C0 2 or such.
  • Equipment necessary for forming the method may be constructed for batch or continuous operation whether two components are mixed in a pressurised container.
  • the pressurised container should have valve for expansion of the mixture to particle shape. This is performed in a cold room in such a way that the particles do not melt.
  • the mixing relation as well as the pressure in the container and thereby also the temperature of the expanded particles, are adjusted in such a way that the desired density is achieved for the particles.
  • the desired density is desired partly based on the fluidising properties of the particles in the following drying chambers and the defined claims for the dried end product.
  • the clean inert particles initially are produced in an equipment corresponding with the equipment described above, or in another way, for example by granulation.
  • the particles are covered with the solution which already is undercooled to the initial freezing point.
  • the thickness and the initial temperature of the layer for the clean inert particles have to be adjusted to ensure that melting is avoided.
  • Addition of the layer may be performed in an ordinary industrial equipment for this purpose in a batch or continuous production process.
  • the equipment is arranged in a cold room.
  • the following drying is performed in a normal fluidized drying chamber having a lower temperature than the lowest melting temperature of the particles.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Drying Of Solid Materials (AREA)
  • Freezing, Cooling And Drying Of Foods (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

Method for formulating particles from solutions, wherein cooling the solution down to the initial freezing point, to mix the solution under pressure with an inert medium, to expand the solution to solid, fluidable frozen particles comprising the insert medium and the solution in a frozen shape.

Description

A method for formulating particles
5 The present invention is related to a method for formulating particles from solutions for processing in a fluid bed.
For drying known methods are utilizing among others mixture of solutions where the dried end product is mixed with 0 a return flow with the product. Such a method, however, includes very different resting times for the product which is recirculated in relation to products not being recirculated. Additionally the flow of products substantially is increased through the drying chamber. s The solution is spread out or in other way laid on inert particles having a layer which thereafter is dried. The layer is peeled in the drying chamber thereafter to be taken out as dried powder in a cyclon, or the particles are taken out of the chamber for peeling. Such a method easily pollutes the dried o product from the inert particles. Furthermore, the inert particles which substantially do not pollute, are relatively heavy particles needing very large amounts of energy supplied to the fans to maintain the particles in fluidized condition.
With the method according to the present invention 5 substantial advantages are achieved in relation to known methods, whereby the advantages with the known method substantially are maintained and the disadvantages avoided. In this way a strongly reduced recilient time is achieved, strongly reduced flow of products through the dryer, no o pollution of the product from the inert particles, reduced claim for energy for the fans and furthermore also a possibility to control the density and porousity of the end product .
The above mentioned advantages are achieved with the 5 method according to the invention as defined with features stated in the claims.
The method according to the invention may be utilized to produce frozen fluidable particles of solutions thereby using an inert medium in such a way that the solutions may be dried in a fluidized drying chamber. The inert medium as such is disappearing by supplication during drying or already during the formulation of the particles. The method also may be utilized for particle formation if the need for further processing is not drying, but may be performed in a fluid bed. According to the invention the solution to be dried, is cooled down to the initial freezing point. Thereafter the solution is mixed with the inert medium under pressure, thereafter to be expanded to compact, frozen particles comprising the inert medium as well as the solution in a frozen state. Alternatively, the fluidable particles may be produced from the inert medium which thereafter is covered by the solution. This certainly must be made in such a way that the particles as such do not melt. The particles normally are produced in a size of 0,5 to 5 mm. The inert medium to be sublimized during drying or expansion, can be for example be N2, C02 or such.
Equipment necessary for forming the method may be constructed for batch or continuous operation whether two components are mixed in a pressurised container. The pressurised container should have valve for expansion of the mixture to particle shape. This is performed in a cold room in such a way that the particles do not melt.
The mixing relation as well as the pressure in the container and thereby also the temperature of the expanded particles, are adjusted in such a way that the desired density is achieved for the particles. The desired density is desired partly based on the fluidising properties of the particles in the following drying chambers and the defined claims for the dried end product.
By production of inert particles to be covered with the solution, the clean inert particles initially are produced in an equipment corresponding with the equipment described above, or in another way, for example by granulation. The particles are covered with the solution which already is undercooled to the initial freezing point. The thickness and the initial temperature of the layer for the clean inert particles have to be adjusted to ensure that melting is avoided. Addition of the layer may be performed in an ordinary industrial equipment for this purpose in a batch or continuous production process. Preferably the equipment is arranged in a cold room. The following drying is performed in a normal fluidized drying chamber having a lower temperature than the lowest melting temperature of the particles.
By drying the particle formulation in a closed circuit having low temperature, substantial quality advantages are achieved in relation to known drying processes, especially because volatile components such as aromatic components are preserved.

Claims

P a t e n t C l a i m s
1. Method for formulating particles from solutions, CHARACTERIZED IN cooling the solution down to the initial 0 freezing point, to mix the solution under pressure with an inert medium, to expand the solution to solid, fluidable frozen particles comprising the inert medium and the solution in a frozen shape.
2. Method by formulating particles from solutions, s CHARACTERIZED IN producing fluidable particles of the inert medium and to cover the particles with the solution.
3. Method according to claim 2, CHARACTERIZED IN covering the particles with the solution in such a way that particles do not melt. o 4. Method according to preceding claims,
CHARACTERIZED IN to manufacture particles in a range of 0,5 to 5 mm.
5. Method according to preceding claims, CHARACTERIZED IN to use for example N2, C02 or such as inert 5 medium, which will sublimes during drying or by expansion.
0
PCT/NO1999/000172 1998-06-02 1999-06-01 A method for formulating particles Ceased WO1999065600A1 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
CA002333995A CA2333995C (en) 1998-06-02 1999-06-01 A method for formulating particles
EP99925481A EP1091799A1 (en) 1998-06-02 1999-06-01 A method for formulating particles
JP2000554470A JP2002518155A (en) 1998-06-02 1999-06-01 How to make particles
US09/701,551 US6363743B1 (en) 1998-06-02 1999-06-01 Method for formulating particles
AU41746/99A AU4174699A (en) 1998-06-02 1999-06-01 A method for formulating particles

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NO19982501 1998-06-02
NO19982501A NO311164B1 (en) 1998-06-02 1998-06-02 Process for freeze-drying of solutions

Publications (1)

Publication Number Publication Date
WO1999065600A1 true WO1999065600A1 (en) 1999-12-23

Family

ID=19902098

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/NO1999/000172 Ceased WO1999065600A1 (en) 1998-06-02 1999-06-01 A method for formulating particles

Country Status (6)

Country Link
EP (1) EP1091799A1 (en)
JP (1) JP2002518155A (en)
AU (1) AU4174699A (en)
CA (1) CA2333995C (en)
NO (1) NO311164B1 (en)
WO (1) WO1999065600A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004078187A1 (en) * 2003-03-06 2004-09-16 Sinvent As Dried blood plasma product

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4073158A (en) * 1974-11-07 1978-02-14 Jacques Guiller Apparatus for freezing small drops of liquid
GB1559920A (en) * 1976-12-30 1980-01-30 Boehringer Mannheim Gmbh Process and device for the production of frozen granulates
FR2396248B1 (en) * 1977-06-30 1980-03-14 Guiller Jacques
EP0478118A1 (en) * 1990-08-31 1992-04-01 Taiyo Sanso Co., Ltd. Apparatus for producing frozen particles
RU2023319C1 (en) * 1991-05-05 1994-11-15 Московская государственная академия химического машиностроения Process of manufacture of finely divided powder materials
WO1995022036A1 (en) * 1994-02-09 1995-08-17 Kinerton Limited Process for drying a material from solution
WO1996019922A1 (en) * 1994-12-23 1996-07-04 Tetra Laval Holdings & Finance Method and arrangement for cooling of a pumpable liquid with or without particles
FR2756196A1 (en) * 1996-11-25 1998-05-29 Air Liquide Granule preparation process

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4073158A (en) * 1974-11-07 1978-02-14 Jacques Guiller Apparatus for freezing small drops of liquid
GB1559920A (en) * 1976-12-30 1980-01-30 Boehringer Mannheim Gmbh Process and device for the production of frozen granulates
FR2396248B1 (en) * 1977-06-30 1980-03-14 Guiller Jacques
EP0478118A1 (en) * 1990-08-31 1992-04-01 Taiyo Sanso Co., Ltd. Apparatus for producing frozen particles
RU2023319C1 (en) * 1991-05-05 1994-11-15 Московская государственная академия химического машиностроения Process of manufacture of finely divided powder materials
WO1995022036A1 (en) * 1994-02-09 1995-08-17 Kinerton Limited Process for drying a material from solution
WO1996019922A1 (en) * 1994-12-23 1996-07-04 Tetra Laval Holdings & Finance Method and arrangement for cooling of a pumpable liquid with or without particles
FR2756196A1 (en) * 1996-11-25 1998-05-29 Air Liquide Granule preparation process

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
DATABASE WPI Week 199526, Derwent World Patents Index; AN 1995-198965 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004078187A1 (en) * 2003-03-06 2004-09-16 Sinvent As Dried blood plasma product

Also Published As

Publication number Publication date
JP2002518155A (en) 2002-06-25
AU4174699A (en) 2000-01-05
EP1091799A1 (en) 2001-04-18
CA2333995C (en) 2009-01-13
NO982501L (en) 1999-12-03
NO311164B1 (en) 2001-10-22
NO982501D0 (en) 1998-06-02
CA2333995A1 (en) 1999-12-23

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