GB2083804A - A method of dewatering slurry - Google Patents

A method of dewatering slurry Download PDF

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Publication number
GB2083804A
GB2083804A GB8128287A GB8128287A GB2083804A GB 2083804 A GB2083804 A GB 2083804A GB 8128287 A GB8128287 A GB 8128287A GB 8128287 A GB8128287 A GB 8128287A GB 2083804 A GB2083804 A GB 2083804A
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GB
United Kingdom
Prior art keywords
slurry
centrifuge
dewatering
dewatered
crumb
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
GB8128287A
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GB2083804B (en
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Kloeckner Humboldt Deutz AG
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Kloeckner Humboldt Deutz AG
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Publication date
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Publication of GB2083804A publication Critical patent/GB2083804A/en
Application granted granted Critical
Publication of GB2083804B publication Critical patent/GB2083804B/en
Expired legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/38Treatment of water, waste water, or sewage by centrifugal separation
    • C02F1/385Treatment of water, waste water, or sewage by centrifugal separation by centrifuging suspensions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/20Agglomeration, binding or encapsulation of solid waste
    • B09B3/25Agglomeration, binding or encapsulation of solid waste using mineral binders or matrix
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/008Sludge treatment by fixation or solidification

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Treatment Of Sludge (AREA)
  • Processing Of Solid Wastes (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)

Abstract

A method of dewatering slurry in a centrifuge comprises adding to the slurry a rapidly hardening additive. The rapidly hardening additive is preferably cement.

Description

SF'tUlFlUA I IUN A method of dewatering slurry The invention relates to a method of dewatering slurry in a centrifuge, and is particularly suitable for dewatering a slurry which contains carbon.
The slurry, more particularly a slurry which contains carbon, is dewatered in a centrifuge in a manner known per se by adding flocking agents, in order to make it possible to separate very fine solid particles found in the slurry from the liquid. When it has been dewatered in this way the slurry is in the form of a doughy mass in most cases, which has to be subjected to a special subsequent treatment in order to enable it to be transported, stored or used in some other way. However, this involves high labour costs, capital costs and a large amount of time.
The invention therefore seeks to provide a method which will make it possible to dewater slurry, in a centrifuge while avoiding some or all of the above disadvantages and in which the solid end-product of the centrifuge is already in the form of a product which is easily transported and stored.
According to the invention, there is provided a method of dewatering slurry in a centrifuge, wherein a rapidly hardening additive is added to the slurry.
In this way the solids present in the slurry are consolidated during dewatering of the slurry in the centrifuge in an extremely advantageous manner and not only does this considerably assist the dewatering action but it also results in an end product which is in crumb form, as has been shown in practice, this end-product being very easily transported, stored or further processed without any subsequent treatment. Furthermore, in practical tests it was shown that the agglomerate-type product or crumb-like products, dewatered and extracted from the centrifuge, solidified noticeably after approximately two to three hours; but could be crushed easily. Samples of this dewatered product did not shown any tendency to dissolve in water either - even after several hours.
Cement, as the rapidly hardening additive, may be added to the slurry. The addition of cement to the slurry can be effected either in dry form or in the form of cement slurries, and this may be carried out independently of additions of flocking agent. As practical dewatering tests using slurry containing carbon have shown, in a solid sleeve screw centrifuge, particularly good results could be achieved when the quantity of cement added to the slurry as an additive was between 1 and 5%, more particularly 3%, by weight of the solids in the slurry. The solids extracted from the centrifuge during these tests had a relatively dry and crumb-like structure which could be easily loaded transported and stored. After approximately two to three hours of storage a distinct solidification of the crumb-like product was established.After storage for approximately 20 hours a further solidification of the crumb-like product was ascertained and the crumb-like product was very easily crushed; but did not show any signs of dissolving in water.
Because the slurry is dewatered by adding a rapidly hardening additive, the slurry can be transported, stored and/or utilized in a very advantageous manner immediately after dewatering without any special subsequent treatment. Therefore, in comparison to previously known methods, not only is there a substantial improvement in the dewatering action as a result of the present method but there is also an important reduction in labour and capital costs.
One embodiment of the invention will now be described in greater detail, by way of example: Flotation tailings with a solids concentration or with dry materials (TS), which make up 23 percent of the total, were dewatered in a solid sleeve screw centrifuge at 1450 revolutions of the drum per minute. Approximately 3% by weight PZ 35 (Portland Cement) i.e. 3% of the solids or the dry materials (TS), was then introduced into the centrifuge in dry form and mixed with the flotation tailings. At the same time a synthetic flocking agent, i.e. 2.5 kg per tonne of dry materials (TS), was added to the flotation tailings directly in the centrifuge inlet. The flotation tailings dewatered in this way in the solid sleeve screw centrifuge were crumb-like and clearly solidified after about 2 to 3 hours of storage.
Although these dewatered, crumb-like flotation tailings could be broken up and crushed very easily, there were, after storing the crumb-like flotation tailings for several days no signs of them dissolving in water.
The method according to the present invention is not restricted to this example. Apart from the slurries which contain carbon (such as flotation tailings) other types of slurry can also be dewatered profitably by the method according to the invention such as municipal slurry or sapropel. Furthermore, besides cement, ash can be used very profitably in accordance with the method of the invention, more particularly flue dust or flue dust combined with calcium hydroxide Ca (OH)2. Moreover, the additives such as cement or flue ash may be added to the slurry which is to be dewatered, directly before dewatering, in the centrifuge, either when dry or wet in the form of a sludge.
1. A method of dewatering slurry in a centrifuge, wherein a rapidly hardening additive is added to the slurry.
2. A method according to claim 1, wherein cement is added to the slurry as the rapidly hardening additive.
3. A method according to claim 1 or 2, wherein the quantity of additives added to the slurry is between 1 and 5% by weight of solid material in the slurry.
4. A method according to claim 3, wherein the quantity of additives is 3% of the solid material in the slurry.
5. A method according to any one of the preceding claims, wherein a flocking agent is also added to the slurry.
**WARNING** end of DESC field may overlap start of CLMS **.

Claims (6)

**WARNING** start of CLMS field may overlap end of DESC **. SF'tUlFlUA I IUN A method of dewatering slurry The invention relates to a method of dewatering slurry in a centrifuge, and is particularly suitable for dewatering a slurry which contains carbon. The slurry, more particularly a slurry which contains carbon, is dewatered in a centrifuge in a manner known per se by adding flocking agents, in order to make it possible to separate very fine solid particles found in the slurry from the liquid. When it has been dewatered in this way the slurry is in the form of a doughy mass in most cases, which has to be subjected to a special subsequent treatment in order to enable it to be transported, stored or used in some other way. However, this involves high labour costs, capital costs and a large amount of time. The invention therefore seeks to provide a method which will make it possible to dewater slurry, in a centrifuge while avoiding some or all of the above disadvantages and in which the solid end-product of the centrifuge is already in the form of a product which is easily transported and stored. According to the invention, there is provided a method of dewatering slurry in a centrifuge, wherein a rapidly hardening additive is added to the slurry. In this way the solids present in the slurry are consolidated during dewatering of the slurry in the centrifuge in an extremely advantageous manner and not only does this considerably assist the dewatering action but it also results in an end product which is in crumb form, as has been shown in practice, this end-product being very easily transported, stored or further processed without any subsequent treatment. Furthermore, in practical tests it was shown that the agglomerate-type product or crumb-like products, dewatered and extracted from the centrifuge, solidified noticeably after approximately two to three hours; but could be crushed easily. Samples of this dewatered product did not shown any tendency to dissolve in water either - even after several hours. Cement, as the rapidly hardening additive, may be added to the slurry. The addition of cement to the slurry can be effected either in dry form or in the form of cement slurries, and this may be carried out independently of additions of flocking agent. As practical dewatering tests using slurry containing carbon have shown, in a solid sleeve screw centrifuge, particularly good results could be achieved when the quantity of cement added to the slurry as an additive was between 1 and 5%, more particularly 3%, by weight of the solids in the slurry. The solids extracted from the centrifuge during these tests had a relatively dry and crumb-like structure which could be easily loaded transported and stored. After approximately two to three hours of storage a distinct solidification of the crumb-like product was established.After storage for approximately 20 hours a further solidification of the crumb-like product was ascertained and the crumb-like product was very easily crushed; but did not show any signs of dissolving in water. Because the slurry is dewatered by adding a rapidly hardening additive, the slurry can be transported, stored and/or utilized in a very advantageous manner immediately after dewatering without any special subsequent treatment. Therefore, in comparison to previously known methods, not only is there a substantial improvement in the dewatering action as a result of the present method but there is also an important reduction in labour and capital costs. One embodiment of the invention will now be described in greater detail, by way of example: Flotation tailings with a solids concentration or with dry materials (TS), which make up 23 percent of the total, were dewatered in a solid sleeve screw centrifuge at 1450 revolutions of the drum per minute. Approximately 3% by weight PZ 35 (Portland Cement) i.e. 3% of the solids or the dry materials (TS), was then introduced into the centrifuge in dry form and mixed with the flotation tailings. At the same time a synthetic flocking agent, i.e. 2.5 kg per tonne of dry materials (TS), was added to the flotation tailings directly in the centrifuge inlet. The flotation tailings dewatered in this way in the solid sleeve screw centrifuge were crumb-like and clearly solidified after about 2 to 3 hours of storage. Although these dewatered, crumb-like flotation tailings could be broken up and crushed very easily, there were, after storing the crumb-like flotation tailings for several days no signs of them dissolving in water. The method according to the present invention is not restricted to this example. Apart from the slurries which contain carbon (such as flotation tailings) other types of slurry can also be dewatered profitably by the method according to the invention such as municipal slurry or sapropel. Furthermore, besides cement, ash can be used very profitably in accordance with the method of the invention, more particularly flue dust or flue dust combined with calcium hydroxide Ca (OH)2. Moreover, the additives such as cement or flue ash may be added to the slurry which is to be dewatered, directly before dewatering, in the centrifuge, either when dry or wet in the form of a sludge. CLAIMS
1. A method of dewatering slurry in a centrifuge, wherein a rapidly hardening additive is added to the slurry.
2. A method according to claim 1, wherein cement is added to the slurry as the rapidly hardening additive.
3. A method according to claim 1 or 2, wherein the quantity of additives added to the slurry is between 1 and 5% by weight of solid material in the slurry.
4. A method according to claim 3, wherein the quantity of additives is 3% of the solid material in the slurry.
5. A method according to any one of the preceding claims, wherein a flocking agent is also added to the slurry.
6. A method of dewatering slurry substantially as described herein.
GB8128287A 1980-09-19 1981-09-18 A method of dewatering slurry Expired GB2083804B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19803035397 DE3035397A1 (en) 1980-09-19 1980-09-19 METHOD FOR DRAINING SLUDGE

Publications (2)

Publication Number Publication Date
GB2083804A true GB2083804A (en) 1982-03-31
GB2083804B GB2083804B (en) 1983-06-02

Family

ID=6112385

Family Applications (1)

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GB8128287A Expired GB2083804B (en) 1980-09-19 1981-09-18 A method of dewatering slurry

Country Status (5)

Country Link
AU (1) AU7544781A (en)
DE (1) DE3035397A1 (en)
ES (1) ES505526A0 (en)
GB (1) GB2083804B (en)
ZA (1) ZA816425B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0389089A2 (en) * 1989-03-23 1990-09-26 Alternative Technologies For Waste, Inc. Method and apparatus for centrifugally casting hazardous waste

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3442535A1 (en) * 1984-10-12 1986-04-17 Heinz Dorr Deponienbetrieb GmbH, 8960 Kempten Process for treating the supernatant water from faecal sludges, in particular from domestic sewage treatment plants
CN112373095B (en) * 2020-10-26 2022-09-30 永康市凡谷进出口有限公司 Kitchen waste sewage treatment device and treatment method thereof

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2624484A1 (en) * 1976-06-01 1977-12-15 Hutter Gmbh & Co Kg S Boiler heating surface flushing water treatment - by mixing dewatered sludge with cement binder and rapid hardener
DE2730009C2 (en) * 1977-07-02 1986-10-16 Cillichemie Ernst Vogelmann Gmbh & Co, 7100 Heilbronn Process to improve the filterability of sewage sludge

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0389089A2 (en) * 1989-03-23 1990-09-26 Alternative Technologies For Waste, Inc. Method and apparatus for centrifugally casting hazardous waste
EP0389089A3 (en) * 1989-03-23 1991-08-07 Alternative Technologies For Waste, Inc. Method and apparatus for centrifugally casting hazardous waste

Also Published As

Publication number Publication date
ES8603359A1 (en) 1985-06-01
AU7544781A (en) 1982-03-25
DE3035397A1 (en) 1982-05-06
ES505526A0 (en) 1985-06-01
GB2083804B (en) 1983-06-02
ZA816425B (en) 1982-09-29

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