IE960182A1 - Production method - Google Patents
Production methodInfo
- Publication number
- IE960182A1 IE960182A1 IE960182A IE960182A IE960182A1 IE 960182 A1 IE960182 A1 IE 960182A1 IE 960182 A IE960182 A IE 960182A IE 960182 A IE960182 A IE 960182A IE 960182 A1 IE960182 A1 IE 960182A1
- Authority
- IE
- Ireland
- Prior art keywords
- cellulosic material
- grinder
- classifier
- drive
- coarse
- Prior art date
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
- D21B1/06—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by dry methods
- D21B1/063—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by dry methods using grinding devices
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Mechanical Engineering (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Paper (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Abstract
Coarse cellulosic material is delivered into a feed hopper (1) having an outlet fitted with a rotary valve (2). The coarse material is blown to a grinder (10) and classifier (11). The grinder (10) has a drive unit with a power load monitor (12) fitted with a controller (13). The classifier (11) is driven by a variable speed drive unit (15) which is also controlled by the controller (13). A fan (20) with a variable speed drive unit (21) draws ground and classified cellulosic material into a receiving bin (23) for separation in a separator screen unit (30). The operating speed of the fan (20) and the operating conditions of the grinder (10) and classifier (11) are controlled to optimise the processing of the cellulosic material.<Fig.1>
Description
Production Method method for producing cellulosecarboxymethylcellulose and the Introduction The specifications for cellulose based excipients, particularly pharmaceutical excipients, are high in order to comply with processing and regulatory requirements. Such cellulose products generally have a high value, however, there is a need to optimise the processing method to minimise losses and to provide a range of such cellulose-based products which meet these requirements.
Statements of Invention According to the invention, there is provided a method for producing cellulose-based excipients comprising the steps of:setting a desired operating load on a grinder; delivering coarse cellulosic material from a feed hopper to the grinder; grinding the coarse cellulosic material; classifying the ground cellulosic material in a grinder having a classifier drive unit; controlling the classifier drive unit in accordance with the operating load on the grinder; OPEN TO PUBl >C INSPECTION UNDER SECTION 23 AND RULE 23 f.
NO. 1530.......,OF - 2 drawing the ground and classified cellulosic material into a grinder receiving bin; delivering the ground and classified cellulosic material to a separator; separating the classified cellulosic material into cellulosic material of a desired size and oversize material; delivering the cellulosic material of desired size into a holding bin; and packing the cellulosic material from the holding bin.
In one embodiment of the invention, the ground and classified material is drawn into the grinder receiving bin by a fan having a variable speed drive and the method includes the step, prior to delivery of the coarse cellulosic material to the grinder, of setting the speed of the fan drive to a desired speed matched to the coarse cellulosic material.
Preferably, the method includes the step of delivering the oversize cellulosic material from the separator to the feed hopper for recycling.
In one embodiment of the invention, the operating load on the grinder drive is sensed by sensing the operating power of the grinder drive, the classifier drive unit is a variable speed drive and the classifier drive unit is controlled by varying the drive speed of the classifier in accordance with the operating power of the grinder drive.
,E 960182 In a preferred arrangement, a rotary air valve is provided at the feed hopper outlet and the coarse cellulosic material is delivered from the feed hopper to the grinder by a blower unit.
Preferably, the method includes the step of de-bagging coarse cellulosic materials into the feed hopper.
Detailed Description of the Invention The invention will be more clearly understood from the following description thereof given by way of example only with reference to the accompanying drawing which is a schematic diagram illustrating the method for producing cellulose-based pharmaceutical excipients according to the invention.
Referring to the drawing, there is illustrated a method for producing cellulose-based excipients and in this case pharmaceutical excipients such as carboxymethylcellulose and the like. The method is in this case used in the production of three different types of cellulose-based excipients. These may be a blend of different excipients. Equivalent equipment used in processing different cellulosic materials are illustrated in some cases for clarity as separate items but are assigned the same reference numerals.
In the method of the invention, coarse cellulosic material is delivered into a feed hopper 1 having an outlet fitted in this case with a fixed speed rotary valve 2. The coarse cellulosic material is blown by a blower unit 3 along a common supply line 4 to a grinder/classifier unit . The grinder/classifier unit 5 comprises a grinder 10 and a classifier 11. The grinder 10 has a drive unit with an associated power load, in this case, operating amps - 4 monitor 12 fitted with a controller 13. The classifier 11 is driven by a variable speed drive unit 15, the operation of which is controlled by the controller 13.
A fan 20 fitted with a variable speed drive unit 21 draws ground and classified cellulosic material along a delivery line 22 to a grinder receiving bin 23. Air is exhausted through a plurality of air filter socks 25. The receiving bin 23 has an outlet fitted with a rotary valve 27 through which the ground and classified cellulosic material is delivered to a separator screen unit 30. The screen unit may have any size of aperture fitted to achieve separation into a desired size fraction and oversize. The desired size fraction is delivered through a rotary valve by a blower unit 32 along an output line 35. The oversize material is recovered and delivered along a recycling line 38 to the feed hopper 1. In some cases, the cellulosic material with the desired size distribution is delivered into a silo 40 and collected in a holding bin 41 available for packaging on demand. In another case, the cellulosic material is blended for improved consistency in a blender unit 45 fitted with a blending screw prior to delivery to a silo 40.
In the method of the invention, cellulose-based excipients are produced by first setting, using the variable speed drive unit 21, an operating speed for the fan 20 matched to the cellulosic material being processed. A desired operating load on the grinder 10 is then set using the amp sensing unit 12 linked to the controller 13 for controlling the speed control unit 15 of the classifier 11. The fan 20 and blower unit 3 are operated to release the valve 2, allowing coarse cellulosic material to be delivered along the feed line 4 to the grinder 10. The coarse cellulosic material is ground in the grinder 10 and then classified in the classifier 11. The drive unit 15 of the classifier 11 is controlled in accordance with the operating load on the grinder 10. The fan 20 draws the ground and classified cellulosic material into the grinder receiving bin 23. On operation of the rotary valve 27, the cellulosic material is delivered to the separator unit 30 where the cellulosic material is separated into cellulosic material of a desired size and oversize material which is recycled to the feed hopper 1.
The invention provides an optimised process for producing not only one but several different cellulose-based excipients, particularly pharmaceutical excipients. The particle size range of the cellulosic material is consistent and a wider range, particularly fine grades, of particle sizes may be produced. As any oversize material is recycled, the yield is optimised. The throughput of cellulosic material is maximised as the residence time in the grinder/classifier unit is optimised. The invention also provides a method of production of cellulosic material in which the energy requirement is optimised.
The invention is not limited to the embodiments hereinbefore described which may be varied in detail.
Claims (8)
1. A method for producing cellulose-based excipients comprising the steps of :setting a desired operating load on a grinder; 5 delivering coarse cellulosic material from a feed hopper to the grinder; grinding the coarse cellulosic material; classifying the ground cellulosic material in a grinder having a classifier drive unit; 10 controlling the classifier drive unit in accordance with the operating load on the grinder; drawing the ground and classified cellulosic material into a grinder receiving bin; 15 delivering the ground and classified cellulosic material to a separator; separating the classified cellulosic material into cellulosic material of a desired size and oversize material; 20 delivering the cellulosic material of desired size into a holding bin; and packing the cellulosic material from the holding bin. - Ί
2. A method as claimed in claim 1 wherein the ground and classified material is drawn into the grinder receiving bin by a fan having a variable speed drive and the method includes the step, prior to delivery 5 of the coarse cellulosic material to the grinder, of setting the speed of the fan drive to a desired speed matched to the coarse cellulosic material.
3. A method as claimed in claim 1 or 2 including the step of delivering the oversize cellulosic material 10 from the separator to the feed hopper for recycling.
4. A method as claimed in any preceding claim wherein the operating load on the grinder drive is sensed by sensing the operating power of the grinder drive, the classifier drive unit is a variable speed drive and 15 the classifier drive unit is controlled by varying the drive speed of the classifier in accordance with the operating power of the grinder drive.
5. A method as claimed in any preceding claim wherein a rotary air valve is provided at the feed hopper 20 outlet and the coarse cellulosic material is delivered from the feed hopper to the grinder by a blower unit.
6. A method as claimed in any preceding claim including the step of de-bagging one or more coarse cellulosic 25 materials into the feed hopper.
7. A method for producing cellulose-based excipients substantially as hereinbefore described with reference to the accompanying drawing.
8. Cellulose-based excipients whenever produced by a 30 method as claimed in any preceding claim.
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IE960182A IE960182A1 (en) | 1996-02-29 | 1996-02-29 | Production method |
AU22276/97A AU2227697A (en) | 1996-02-29 | 1997-02-28 | Production method |
PCT/IE1997/000012 WO1997032073A1 (en) | 1996-02-29 | 1997-02-28 | Production method |
AT97905372T ATE191247T1 (en) | 1996-02-29 | 1997-02-28 | PRODUCTION METHOD |
DE69701564T DE69701564T2 (en) | 1996-02-29 | 1997-02-28 | PRODUCTION METHOD |
EP97905372A EP0883711B1 (en) | 1996-02-29 | 1997-02-28 | Production method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IE960182A IE960182A1 (en) | 1996-02-29 | 1996-02-29 | Production method |
Publications (1)
Publication Number | Publication Date |
---|---|
IE960182A1 true IE960182A1 (en) | 1997-09-10 |
Family
ID=11041086
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
IE960182A IE960182A1 (en) | 1996-02-29 | 1996-02-29 | Production method |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP0883711B1 (en) |
AT (1) | ATE191247T1 (en) |
AU (1) | AU2227697A (en) |
DE (1) | DE69701564T2 (en) |
IE (1) | IE960182A1 (en) |
WO (1) | WO1997032073A1 (en) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1285414C (en) | 2005-07-21 | 2006-11-22 | 江苏科行环境工程技术有限公司 | Energy-saving environment-friendly type industrial residue closed-circuit high-yield super-fine mill controlling technique and equipment thereof |
CA2638150C (en) | 2008-07-24 | 2012-03-27 | Sunopta Bioprocess Inc. | Method and apparatus for conveying a cellulosic feedstock |
CA2638160C (en) | 2008-07-24 | 2015-02-17 | Sunopta Bioprocess Inc. | Method and apparatus for conveying a cellulosic feedstock |
CA2638159C (en) | 2008-07-24 | 2012-09-11 | Sunopta Bioprocess Inc. | Method and apparatus for treating a cellulosic feedstock |
CA2650913C (en) | 2009-01-23 | 2013-10-15 | Sunopta Bioprocess Inc. | Method and apparatus for conveying a cellulosic feedstock |
CA2650919C (en) | 2009-01-23 | 2014-04-22 | Sunopta Bioprocess Inc. | Method and apparatus for conveying a cellulosic feedstock |
CA2638157C (en) | 2008-07-24 | 2013-05-28 | Sunopta Bioprocess Inc. | Method and apparatus for conveying a cellulosic feedstock |
US9127325B2 (en) | 2008-07-24 | 2015-09-08 | Abengoa Bioenergy New Technologies, Llc. | Method and apparatus for treating a cellulosic feedstock |
US8915644B2 (en) | 2008-07-24 | 2014-12-23 | Abengoa Bioenergy New Technologies, Llc. | Method and apparatus for conveying a cellulosic feedstock |
PL2467532T3 (en) | 2009-08-24 | 2014-11-28 | Abengoa Bioenergy New Tech Llc | Method for producing ethanol and co-products from cellulosic biomass |
WO2011140222A1 (en) | 2010-05-07 | 2011-11-10 | Abengoa Bioenergy New Technologies, Inc. | Process for recovery of values from a fermentation mass obtained in producing ethanol and products thereof |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB850917A (en) * | 1958-07-12 | 1960-10-12 | Svenska Tandsticks Aktiebolage | Improvements in plants for disintegrating materials |
US4867383A (en) * | 1985-02-11 | 1989-09-19 | Kimberly-Clark Corporation | Method and system for processing wastepaper |
-
1996
- 1996-02-29 IE IE960182A patent/IE960182A1/en not_active IP Right Cessation
-
1997
- 1997-02-28 EP EP97905372A patent/EP0883711B1/en not_active Expired - Lifetime
- 1997-02-28 AU AU22276/97A patent/AU2227697A/en not_active Abandoned
- 1997-02-28 AT AT97905372T patent/ATE191247T1/en not_active IP Right Cessation
- 1997-02-28 DE DE69701564T patent/DE69701564T2/en not_active Expired - Lifetime
- 1997-02-28 WO PCT/IE1997/000012 patent/WO1997032073A1/en active IP Right Grant
Also Published As
Publication number | Publication date |
---|---|
DE69701564D1 (en) | 2000-05-04 |
EP0883711A1 (en) | 1998-12-16 |
EP0883711B1 (en) | 2000-03-29 |
ATE191247T1 (en) | 2000-04-15 |
DE69701564T2 (en) | 2000-07-27 |
AU2227697A (en) | 1997-09-16 |
WO1997032073A1 (en) | 1997-09-04 |
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Legal Events
Date | Code | Title | Description |
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MM9A | Patent lapsed through non-payment of renewal fee |