CA1070654A - Grinding method for cellulose - Google Patents

Abstract

Grinding Method for Cellulose A b s t r a c t A method of reducing the particle size of cellulose compounds selected from the group consisting of cellulose and ether derivatives thereof which comprises grinding said compounds in a vibrator mill in the presence of air and in the presence of sufficient water to yield a product having a water content of from 2 to 10% by weight, wherein at least 50% of the particles in the product have a particle size of 100µ or less, a product obtained by said method and a binder composition containing said product.

Description

1070~54 "Grind~ method for Cellulose"

This invention relates to a new method of reducing - the particle size of cellulose and ether derivatives thereof. Vibration mills can be used for comminuting a variety of materials, particularly mineral substances S for example stone or cement.
Ho~-ever the comminution of cellulose derivatives, - e.g, cellulose ethers, in ball mills or vibration mills has presented certain difficulties. Thus, it is only possible to grind in vibration mills those cellulose derivatives which have a relatively high friability and whichare therefore relatively easily ground, e.g. hydroxy-ethyl cellulose. For fine grindir.g the operation must be carried out under a protective gas, e.g. in the presence of liquid nitrogen, in order to prevent explosions.
Cellulose ethers may be comminuted in rotary mills.
However this has the disadvantage that a finely Oround product can only be obtained by means of several grinding operations and is thus inefficient from the point of view of the amount of work and energy required. Moreover a considerable amount of heat is generated which dries out ,

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the cellulose ether causing it to decompose at least partially and become electrostatically charged. This can easily lead to dust explosions.
In summary therefore~ according to the present state of the art, comminution of substantially amorphous and tough organic materials which are not readily friable cannot be carried out economically on known grinding apparatus without the risk of explosions occuring.
According to the present invention we now provide 10 a method of reducing the particle size of cellulose and/or ether derivatives thereof which comprises grinding cellulose and/or one or more ether derivatives thereof in a vibration mill in the presence of air and in the presence of sufficient water to yield a product having a water content of from 2 to 10 % by weight,preferably from 5 to 8 % by weight wherein at least 50 % of the particles in the product are of a particle size of 100~ or less.
The method according to the invention may be used for the comminution of cellulose or ether derivatives thereof, hereinafter referred to as cellulose ethers, . ~

for example alkyl, hydroxyalkyl, alkylhydroxylalkyl and carboxyalkyl celluloseethers having up to ~ arbon atoms in each alkyl group and ~p to 3 carbon atoms in each hydroxyalkyl group, e.g. methyl cellulos~, m~thylhy~roxy-S ethyl cellulose, methyl-hydroxypropyl cellulose, ethyl ce~lulose, ethyl-hydroxyethyl cellulose and mixed ethers of cellulose and carboxymethyl cellulose either alone or in admixture.
The process according to the invention has the advantage that grinding can be carried out in the absence of a protective gas and indeed in the presence of air, with no danger cf explosions. In generai high yields of product are obtained. It is only necessary for .he ground product - obtained to have the water content given above.
Providing the cellulosic starting material has a sufficiently high water content? grinding in the vibration mill may be effected without the addition of further water.
Appropriately, the starting material used,preferably a cellulose ether, has a water content of S to 14, preferably 7 to 10% by weight, in order to yield a product with the required water content and to warrant the proceSsing security-However if necessary water can be .

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added àuring the grin~lng operation. Since only one grinding operation is generally required and less air is required inside the vibration mill, less water is being - constantly removed from the atmosphere above the grinding ~5 material. The material to be processed thus comes into contact with more moisture in the vibration mill than in conventional grinding apparatus wherein the material must be subjected to several grinding processes and tends to dry out. This drying out leads to an increased risk of explosivn which is great]y reduced in the method according tc~ the present invention.
In the process according to the invention, th~
- retention time can be varied dependirlg on the desired proportions of fine and coarse particle in the pro~uct.
In general a product wherein at least 65, preferably at least 70% by weight, of the particles h~Je a particle size - ~ of 100~ or less is obtained in a good ~ield even wlth ~
relati~ely short ~ete~tion time e.g. 5 to 15 minutes, and single grindins operation.

If desired the cellulose ethers may be cross-linked ~ .

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before or after grinding e,g. by reaction with glyoxal with partial acetal formation. The amount of glyoxal reacted is preferably not more than 5% by weight of the cellulosic material. In this way enlargement of the S molecules is ob,tained, resulting in a reductions in the dissolution rate in water. Since water is not absorbed as quickly the tendency of the particles to clump together when mixe~ with water is reduced.
In addition to friable cellulose ethers, cellulose ethers e.g. methyl cellalose, which are amorphous and tough can be finely ground in a v~'bration mill using the ' method according to the invention. Sometimes a high yield ~: of she finely ground product can be obtained in a single grinding operation. The friability of methyl cellulose can also be increased by incorporating further ether groups e.g.
hydroxyethyl ether groups, whereby a mixed e~her is produced and/or by mixing hydroxyethyl cellulose therewith.
The proportion of hydroxyethyl ether groups introduced into methyl cellulose to form a mixed ether can be from 1.5 to 10~/o~ preferably up ro 6%, by weight of the total ether ~ ~ 6 ~
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groups, it being understood that in this context the term "ether group", does not refer to parts of the cellulose chain connected by ether linkages. The proportion of hydroxyethyl cellulose mixed into methyl cellulose ~y be S from 1.5 to 10%, preferably up to 6% by weight of the mixture.
In general, the vibration mill can be op~rated at 1~ relatively low frequencies, e g. 1,000 to 1800 rfee~. and small oscillation amplitudes, e.g. from 6 to 12 mm, so as to treat the material gently and not heat it too much.
Thermal decomposition of the cellulose or cellulose ether can th~s be kept at a relatively low level, in contrast to the previously known methods with se~eral grinding operations.
Moreover, the lower frequencies and 5m~11 amplitudes mean that any foreign bodies present in the material WL11 not cause sparking.
The starting material may if desired be ground in its natural state or it may compressed prior to grinding depending on the desired size of the specificsurface area and bulk weight of the product. In general powders with a high specific surface area and other special properties, _ 7 _ ` 10706S4 e.g. good flow properites and high bulk density, can be obtained using the methGd of th~ pres~nt invention. For example,woolly or coarse methyl cellulose can be converted into a flowing powder with a relati~ely high bulk weight S which is very easy to measure out ar.d package. The use of a vibration mill as compared to other grinding methods is adventageou~ since the interior surface of the particles is much more retained but only the projecting ed~es ~nd spikes are removed to a much greater extent.
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In general, if an uncompressed starting material with a moisture content of at least lO~ by weight is used, the bulk weight ~ the ground product may be increased, for example, to l.4 to 2.9 times ~ s value in a single grinding operation. For example, if an uncompressed ~tarting material with a bulk weight of 120 to 200, preferably 140 to 170 g/l is used, a ground product with a bulk weight of fro~ 280 to 350, preferably 290 to 32Q g/l can g~nerally be obtained.
On the other hand, highly compressed coarse granulates which are slow to dissolve in water may be converted i ~ into powders with a lower bulk weight and a higher desired - ~

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specific surface ares, by grindin~ in a vibration mill by the method according to the invention. Thus, for example, a compressed granulate with a bulk weight of 4~0 to 520, preferably 490 to 510 g/l, can in general be converted in S one grinding operation, to a product with a bulk weight of 370 to 450, preferably 390 to 420 g/l. In general the difference between the bulk weight of the starting rnaterial and that of the ground material is substantially less than for uncompressed starting materials, rather the bulk weight tends to remain virtually constan~. The startin~material may, i' desired~be compressed in conventional manner, e.g.
in a kneader with addition ~ water, optionally foll~ ea by-extrusion, prior to grinding.
The solubility of the ground material depends on its bulk weight. Cellulose and cellulose ethers in the form of extremely fine powders with a h;gh specific surface area can thus be produced by the method according to the invention which can be wetted quickly and go into solution quickly.
The finely ground products produced by the method _ 9 _ according to the in~ention can be used in many ways, particularly in binder ccmpositions for use in the building industry and by handymen. lhey may thus be used for examp]e as additives for mortar, gravel, cement and gypsum, in wall-paper pastes, in cellulose filler compositions used as moulding compounds, and as additives for synthetic resins, particularly for producing moulded and/or otherwise decorated synthetic resin surfaces. The prOducts produced according to the in~ention, particularly the cellulose ethers, are preferably used as additives for plaster compositior.s for use in the building trade, particularly for machine plaster compositions which ~generally contain inorganic components and a minor proportion of methyl cellulose and/or mixed ethers thereof. The plaster composition must be capable of being wetted with water ext.emel~ quickly, must not become lumpy and must bind water uniformly so that cracks in the finished plaster surface do not appear. A very high level of water retention is required. The powdered cellulose component in the plaster composition fulfills these functions.

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l~e following Examples serve to illustrate the method according to the present invention.
- Example 1 A wad of methylhydroxyethyl celLulose with a bulk -~ 5 weight of 150 g/l is ground in a vibration mill at room temperature and in the presence of air at a throughput rate of 20 kg/per hour, A ground material is obtained 'having the following composition according to screen analysis: <100~ 75%,100 to 125~ 10%, 125 ~ 200~ 13% and 200 to 300~ 2%, residual water content: 4.6 % of initial water content. The bulk weight of ~e product is 300 g/l~
the specific surface area is 0.6 m2/g. The particle ' ,size is made more uniform in known manner, i,e. by screening and regrinding the coarse portions.
Comparison -:
If the same starting material is grou,~d in a ha~mer mill, no powder is obtained. The wadd~ character of the methyIhydroxyethyl cellulose remains so that is it almost impossible to screen. The poor flowing properties of the material ma~e it virtually impossible to process.

Example 2 .
- Pre-compressed methyl cellulose granulate with a ~ bulk weight of 480 g/l and with 85% of the particles having a particle size of > 200~ and 5% of the particles a particle size of ~ S00~ is ground to a powder in a vibration mill with a throughput of 105 kg/per hour.
According,to the screen analysis, the ground material has the following particle size distribution: <100~ ~%, 100 ' to 125~ 11%, 125 to 200~ 10% and 200 to 300~ 3%, The bulk weight of the product is reduced to 405 g/l and the ' specific surface area increased from <O.lm2/g to 0.2m2/g. -~
Residual water content: 3.8 % of initial water content.
Co~parison , , , m e same granulate as used in Example 2 above is ground in a conventional hammer mill, Three times as much grinding energy is reguired to grind it to a powder - of comparable fineness, The bulk weight remains almost constant at 490 g/l and the specific surface area of -~ <O.lm2/g is not perceptibly altered.
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, ExamE~3 Commercial hydroxyethyl cellulose with a bulk weight of 540 g/l and a screen analysis as follows: ~ 300~ 50%, 180 to 300~ 45% and < 180~
approximately 5%; is ground in a vibration mill at room temperature and in the presence of air at a throughput of 180 kg/h. After a single grinding operation, a powdered ground material is obtained with the following screen analysis: > 125~ 20%, 60 to 125~ approximately 30%, ~ 60~ approximately 50%. The bulk weight is increased to 550 g/l. Residual water content:
42% of initial water content.

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Carboxymethyl cellulose with a bulk weight of 440 g/l and a screen analysis as follows: > 1,000~ up to approximately 5%, 750 to 1,000~
approximately 30%, 500 to 750~ up to approximately 45%, 180 to 500~ approxi-mately 50%, < 180~ up to approximately 5%; is ground in a vibration mill at room temperature in the presence of air at a throughput of 140 kg/h.
After one grinding operation, a powder is obtained with the following particle size distribution:

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>300~ about 4%, 180 to 300~ about 10%, 60 to 180~
~60~ 55%. The bulk weight is increased to 530 g/l.
; Residual water content: 3.9% of initial water content.
Ex~ 5 Coarsely comminuted cellulose with a bulk weight of ca.40 g/] is ground in a vibration mill to produce iine, flowing cellulose powder. After being ground once, the cellulose powder has a fines content of 50% with a particle size of ~ lO0 ~. The fines portion can be concentrated by screening. The bulk weight of the cellulose powder obtained is 150-180 g/l.~ Residual wat~r content: 2.8 % initial water content.

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Claims (10)

THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:

1. A method of reducing the particle size of cellulose compounds selected from the group consisting of cellulose and ether derivatives thereof which comprises grinding said compounds in a vibration mill in the presence of air and in the presence of sufficient water to yield a product having a water content of from 2 to 10 % by weight, wherein at least 50 % of the particles in the product have a particle size of 100 or less.

2. A method as claimed in claim 1 wherein the cellulose compound is selected from the group consisting of alkyl, hydroxyalkyl, alkyl-hydroxyalkyl and carboxyalkyl cellulose wherein the alkyl contains up to 2 carbon atoms and the hydroxyalkyl contains up to 3 carbon atoms is ground.

3. A method as claimed in claim 1 wherein a starting material selected from the group consisting of an uncompressed material having a bulk density of from 120 to 200 g/l and a compressed starting material having a bulk density of from 480 to 520 g/l is ground in a single grinding operation to yield a product having a bulk density of from 280 to 350 and 370 to 450 g/l respectively.

4. A process as claimed in claim 3 wherein the starting material has been compressed by treatment in a kneader with addition of water optionally followed by extrusion.

5. A method as claimed in claim 1 or 2 or 3 wherein the vibration mill is operated at a vibration frequency of from 1000 to 1800 rotations/
min. and at a vibration amplitude of from 6 to 12 mm.

6. A method as claimed in claim 1 or 2 or 3 wherein a starting material having a water content of at least 10 % by weight is ground in a single grinding operation to yield a product having a bulk density of from 1.4 to 2.9 times that of the starting material.

7. A method as claimed in claim 1 or 2 or 3 wherein prior to or subsequent to grinding the cellulose ether is reacted with up to 5 %
by weight of the cellulose ether, of glyoxal with partial acetal forma-tion and cross-linking.

8. A method as claimed in claim 1 or 2 or 3 wherein a mixed cellulose ether wherein at least 90 % by weight of the ether groups are methyl ether groups is ground.

9. A method as claimed in claim 1 or 2 or 3 wherein from 1.5 to 10 % by weight of the ether groups in the mixed cellulose ether are hydroxyethyl ether groups.

10. A method as claimed in claim 1 or 2 or 3 wherein a compressed methyl cellulose granulate is ground in a single grinding operation to a free-flowing powder having a bulk density of from 370 to 450 g/l.