GB2426973A - Method of deodorising dewater effluent - Google Patents

Method of deodorising dewater effluent Download PDF

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Publication number
GB2426973A
GB2426973A GB0608357A GB0608357A GB2426973A GB 2426973 A GB2426973 A GB 2426973A GB 0608357 A GB0608357 A GB 0608357A GB 0608357 A GB0608357 A GB 0608357A GB 2426973 A GB2426973 A GB 2426973A
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United Kingdom
Prior art keywords
sodium percarbonate
sodium
coated
effluent
percarbonate
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.)
Withdrawn
Application number
GB0608357A
Other versions
GB0608357D0 (en
Inventor
Philip Rutherford
Peter Carty
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.)
Probe Industries Ltd
Original Assignee
Probe Industries Ltd
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 Probe Industries Ltd filed Critical Probe Industries Ltd
Publication of GB0608357D0 publication Critical patent/GB0608357D0/en
Publication of GB2426973A publication Critical patent/GB2426973A/en
Withdrawn legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B15/00Peroxides; Peroxyhydrates; Peroxyacids or salts thereof; Superoxides; Ozonides
    • C01B15/055Peroxyhydrates; Peroxyacids or salts thereof
    • C01B15/10Peroxyhydrates; Peroxyacids or salts thereof containing carbon
    • C01B15/106Stabilisation of the solid compounds, subsequent to the preparation or to the crystallisation, by additives or by coating
    • 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
    • C02F1/68Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
    • 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
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/06Treatment of sludge; Devices therefor by oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/14Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F3/00Fertilisers from human or animal excrements, e.g. manure
    • 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
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/722Oxidation by peroxides
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/02Odour removal or prevention of malodour

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Water Supply & Treatment (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Treatment Of Sludge (AREA)

Abstract

A method of removing odours from effluents comprising contacting dewatered effluent with sodium percarbonate granules, wherein the granules are coated with a compound that is sparingly soluble in water. The granules may be coated with layers of a compound which includes alkali metal silicates, sulphates, carbonates and hydrogen carbonates, for example magnesium silicate, magnesium sulphate, magnesium carbonate, sodium silicate, sodium carbonate, sodium sulphate, sodium hydrogen carbonate or aluminium silicate. By adding the coated sodium percarbonate to sludge, the oxidising agent is present in the sludge for many days. Additionally an alkali, such as sodium carbonate, may be included so as to raise the pH of the sludge to more than 11. In the invention, dewatered sludge 1 is carried along a conveyer 2, a 1:1 mixture of coated sodium percarbonate and sodium carbonate is located in hopper 3, the sludge and the percarbonate mixture as deposited in the pre-mixer 4, this mixture is then carried along a screw conveyer 5 mixing the percarbonate and the sludge. The mixture is deposited in a storage or manuring container. The invention overcomes a problem nuisance odours in the use of sewage as a fertiliser.

Description

Method for treating effluent The invention relates to a method for
reducing nuisance odours present in effluent, and in particular to a method for reducing odours in sewage sludge.
Disposal of sewage is a major problem. There are approximately 9000 sewage treatment works in the United Kingdom alone, each producing over 200 tonnes of sewage waste and 11 billion litres of wastewater daily.
Typical methods for disposal include land fill, composting, burning and spreading on fields as a fertilizer.
The main problem of using sewage as a fertilizer is the nuisance odours. Sewage contains sulphur containing compounds including hydrogen sulphide and various mercaptans formed by anaerobic bacteria. These compounds are all foul-smelling and are highly volatile so need only be present at low concentrations to cause a nuisance. Sewage may be treated with oxidising agents in order to destroy these malodorous compounds. However, during subsequent storage, anaerobic conditions within a stockpile can cause these nuisance odours to be regenerated and then released once the stockpile is disturbed, for example for transport or land spreading. This is a real nuisance for the public and major reason for public opposition to land application of sewage.
Sewage must also be treated to reduce levels of pathogens before it can be used as a fertilizer.
This is usually achieved by the addition of lime to the dewatered sludge cake. Dewatered sludge cake typically comprises 7O8O% residual water, lime (CaO) reacts with the water to produce calcium hydroxide in an exothermic reaction. The heat produced pasteurises the cake, and also the pH of the cake is elevated to approximately pH 12, killing all bacteria.
The problems with using lime are that working conditions are not very favourable. Dissolving lime in water produces an output of heat of more than 1100 KJ per kg lime. This exothermic reaction increases the evolution of ammonia gas from the sludge. Ammonia is both unpleasant and dangerous to workers who may be overcome with the fumes. Ammonia can cause irritation to the eyes, nose and throat if not protected properly. Evolution of ammonia also reduces the N content of the sludge, so it has less value as a fertilizer. Liming also creates a very dusty atmosphere in the treatment plant which is unpleasant for workers.
In addition to the problems discussed above, when lime reacts with fats present in sewage sludge, fatty acid calcium salts are formed. These calcium salts are insoluble in water and form a precipitate (commonly known as lime soap), which stiffens up the cake and makes it more difficult to work with.
It would be desirable to provide an improved method for odour control in sewage waste.
One aspect of the invention provides a method for removing odours in dewatered effluent as specified in Claim 1.
A further aspect of the invention provides a product suitable for use with the method of the invention as specified in Claim 18.
A further aspect of the invention provides effluent treated according to the method of the invention as specified in Claim 20.
Preferred aspects of the invention are specified in the claims dependent on Claim 1.
The present invention offers an improved method that mitigates the aboveidentified problems, and provides longer term odour control in sewage waste.
The method of the invention uses an oxidising agent to destroy odours, the oxidising agent present in a stable form so that oxidising power continues to combat odours during storage for several weeks or months after mixing or processing.
Sodium percarbonate is an oxidising agent suitable for oxidising foulsmelling sulphur compounds found in sewage. Sodium percarbonate is an addition compound of sodium carbonate and hydrogen peroxide (2Na2CO33H2O2. It decomposes to oxygen, water and sodium carbonate, yielding approximately 13% of active oxygen. If sodium percarbonate is uncoated it decomposes rapidly in water. However, sodium percarbonate can be coated with layers of compounds which are sparingly soluble in water in order to improve stability. Coated sodium percarbonate is widely available commercially, for example from Solvay under the trade name OXPER .
Suitable coating compounds include alkali metal silicates, sulphates, carbonates and hydrogen carbonates; for example magnesium silicate, magnesium sulphate, magnesium carbonate, sodium silicate, sodium sulphate, sodium carbonate, sodium hydrogen carbonate or aluminium silicate.
By adding coated sodium percarbonate to sludge, the oxidising agent is present in the sludge for many days or weeks depending on the thickness of the coating or the number of coatings applied. The additive continues to oxidise the volatile sulphur compounds, removing odours for a long time after treatment. This is especially beneficial when transporting sludge.
Additionally treating sludge cake with an alkali, preferably sodium carbonate, raises the pH of the cake to more than pHil. This destroys virtually all pathogens in the cake. Table I summarises the maximum pH tolerance for a range of pathogens.
Table I - Maximum pH tolerances for various pathogens Pathogen Max. pH for pathogen growth Bacillus Cereus 9.3 Campy/obacterjejuni 9.5 Clostridium botu/inum 9 C/ostridiumpefringens 9 bscherichia co/i 9 Listeria monfytogenes 9.4 Sa/monella spp 9.5 Shie//a spp 9.3 Staphy/ococcus aureus 10 Vibrio cho/erae 10 Vibrio parahemo/yticus 11 Vibrio parahemo/gtica 11 Vibrio vunficus 10 Yersinia enteroco/itica 10 Sodium carbonate is a solid that dissolves in water with minimal generation of heat. As minimal heat is generated, minimal amounts of ammonia are released. This results in fertiliser with enhance N value compared to limed cake, and the working environment in the sewage works is much improved.
Addition of sodium carbonate to the sludge cake has further benefits to the sewage treatment process. Sodium carbonate will saponify fats in the sewage sludge fatty acid sodium salts which are soluble in water (crude soaps) and help to lubricate the sludge cake. This helps make the cake less viscous and much easier to handle.
Sewage comprises approximately 20g sulphur per m3., equivalent to 0.625 moles of sulphur per m3. Sodium percarbonate (2Na2CO33H2O2) yields approximately 13% of active oxygen on decomposition. In the preferred embodiment, SOOg of coated sodium percarbonate is added per m3 sludge cake, providing a three fold excess of active oxygen.
Sewage sludge cake comprises approximately 200g of fats per cubic metre. Taking the assumption that most of the fat present is present as oleic acid tryglycerides with an approximate molecular weight of 900, there are approximately 0.222 moles of fat per m3 sludge cake.
At least a three fold excess of alkali is required to saponify each ester group on the fat, this equates to 7lg of sodium carbonate. It is preferable to supply an excess of sodium carbonate. In the preferred embodiment, SOOg of sodium carbonate is added per m3 sludge cake, providing a seven fold excess of sodium carbonate.
Therefore, in a preferred embodiment, each m3 of dewatered sludge cake is treated with a mixture of 500g sodium percarbonate and 500g sodium carbonate.
The sodium percarbonate must be coated to improve stability within the sludge cake. Sodium percarbonate must be coated with compounds that are sparingly soluble in water. Coated sodium percarbonate is widely available commercially.
Suitable coating compounds include alkali metal silicates, suiphates, carbonates and hydrogen carbonates; for example magnesium silicate, magnesium sulphate, magnesium carbonate, sodium silicate, sodium sulphate, sodium carbonate, sodium hydrogen carbonate or aluminium silicate.
in the preferred embodiment granules of sodium percarbonate with several different coating thicknesses are used.
In the drawings, which illustrate preferred embodiments of the invention: Figure 1 is a schematic drawing of a sewage treatment works.
Referring to Figure 1, dewatered sewage sludge cake (1) is carried along a conveyor (2). A 1:1 mixture of coated sodium percarbonate and sodium carbonate is located in hopper (3). Sludge cake is deposited into the premixer (4) and a controlled amount of the sodium percarbonate/sodium carbonate mixture is deposited onto the sludge cake at regular intervals.
The mixture of sludge cake and sodium percarbonate and sodium carbonate is then carried along a screw conveyor (5). As the cake travels along the screw conveyer it is mixed, before the mixture is deposited into a storage or manuring container (6). The rate of addition of the sodium percarbonate/sodium carbonate mixture is controlled so that approximately every 1m3 of sludge cake is treated with approximately 1Kg of a 1:1 mixture by weight of coated sodium percarbonate:sodium carbonate.

Claims (21)

  1. Claims 1. A method for removing odours from effluent comprising contacting
    dewatered effluent with sodium percarbonate granules, wherein the granules are coated with a compound that is sparingly soluble in water.
  2. 2. A method as claimed in claim 1, wherein the dewatered effluent is further contacted with an alkali.
  3. 3. A method as claimed in claim 2, wherein the alkali is sodium carbonate.
  4. 4. A method as claimed in claim 3, wherein each cubic metre of effluent is contacted with an amount of coated sodium percarbonate in the range 200g to 1000g and an amount of sodium carbonate in the range 200g to l000g.
  5. 5. A method as claimed in claim 3, wherein each cubic metre of effluent is contacted with 500g coated sodium percarhonate and SOOg sodium carbonate.
  6. 6. A method as claimed in any preceding claim, wherein the effluent is sewage.
  7. 7. A method as claimed in any preceding claim, wherein the sodium percarbonate is coated with at least one compound selected from the group comprising: magnesium silicate; magnesium carbonate; magnesium sulphate; sodium silicate; sodium carbonate; sodium hydrogen carbonate or aluminium silicate.
  8. 8. A method as claimed in any preceding claim, wherein the coating amounts to 0.5 to 25 weight % of coating compound relative to sodium percarbonate.
  9. 9. A method as claimed in any preceding claim, wherein the sodium percarbonate is coated with a number of layers, n, wherein; when n = I the coating amounts to 0 to 1.5 weight % relative to sodium percarbonate; when n = 2 the coating amounts to 0 to 3 weight o,/ relative to sodium percarbonate; when n = 3 the coating amounts to 0 to 4.Sweight % relative to sodium percarbonate; when n = 4 the coating amounts to 0 to 6 weight % relative to sodium percarbonate; when n = 5 the coating amounts to 0 to 7. 5 weight % relative to sodium percarbonate; when n = 6 the coating amounts to 0 to 9 weight O,/ relative to sodium percarbonate; when n = 7 the coating amounts to 0 to 10.5 weight % relative to sodium percarbonate; when n = 8 the coating amounts to 0 to 12 weight % relative to sodium percarbonate; when n = 9 the coating amounts to 0 to 13.5 weight % relative to sodium percarbonate; and when n = 10 the coating amounts to 0 to 15 weight % relative to sodium percarbonate.
  10. 10. A method as claimed in claim 9, wherein the coated sodium percarbonate is a mixture of coated sodium percarbonate with n in the range I to 10.
  11. 11. A method as claimed in any preceding claim, wherein an amount of coated sodium percarbonate remains in the effluent in unreacted form for up to three months.
  12. 12. A method as claimed in claim 11, wherein an amoimt of coated sodium percarbonate remains in the effluent in unreacted form for up to two months.
  13. 13. A method as claimed in claim 11 or 12, wherein an amount of coated sodium percarbonate remains in the effluent in unreacted form for up to one month.
  14. 14. A method as claimed in any of claims 11 to 13, wherein an amount of coated sodium percarbonate remains in the effluent in unreacted form for up to 15 days.
  15. 15. A method as claimed in any of claims Ii to 14, wherein an amount of coated sodium percarbonate remains in the effluent in unreacted form for up to 10 days.
  16. 16. A method as claimed in any of claims 11 to 15, wherein an amount of coated sodium percarbonate remains in the effluent in unreacted form for up to 5 days.
  17. 17. A method as claimed in any of claims 11 to 16, wherein sodium percarbonate is a mixture of coated sodium percarbonate that remains in the effluent in unreacted form for up to 5 days; coated sodium percarbonate that remains in the effluent in unreacted form for up to 10 days; coated sodium percarbonate that remains in the effluent in unreacted form for up to days; and coated sodium percarbonate that remains in the effluent in unreacted form for more than 15 days.
  18. 18. A product suitable for use in the method as claimed in any of claims 3 to 17 comprising a mixture of sodium carbonate and coated sodium percarbonate.
  19. 19. A product as claimed in claim 18, wherein the mixture comprises sodium carbonate and coated sodium percarbonate in a ratio of 1:1 by weight.
  20. 20. Effluent treated according to the method claimed in any of claims I to 19.
  21. 21. Effluent treated with the product as claimed in claim 18 or 19.
GB0608357A 2005-04-28 2006-04-28 Method of deodorising dewater effluent Withdrawn GB2426973A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GBGB0508622.8A GB0508622D0 (en) 2005-04-28 2005-04-28 Method for treating effluent

Publications (2)

Publication Number Publication Date
GB0608357D0 GB0608357D0 (en) 2006-06-07
GB2426973A true GB2426973A (en) 2006-12-13

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GBGB0508622.8A Ceased GB0508622D0 (en) 2005-04-28 2005-04-28 Method for treating effluent
GB0608357A Withdrawn GB2426973A (en) 2005-04-28 2006-04-28 Method of deodorising dewater effluent

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GB (2) GB0508622D0 (en)
WO (1) WO2006114651A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009050191A2 (en) 2007-10-15 2009-04-23 Kemira Kemi Ab Process for the production of a granule of a coated oxidizing compound such granule and uses of the granule

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110606597A (en) * 2019-09-11 2019-12-24 崔玉祥 Treatment method for efficiently removing COD (chemical oxygen demand) in wastewater
DE102019134195A1 (en) * 2019-12-12 2021-06-17 Johannes Wissing Process and system for the treatment of olfactory contaminated substances
CN111253182A (en) * 2020-01-16 2020-06-09 常州市金太阳动物保健品有限公司 Wangcao polyoxin tablet and preparation method thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1384207A (en) * 1972-06-05 1975-02-19 Fmc Corp Odour abatement in animal wastes
GB1526129A (en) * 1975-10-09 1978-09-27 Tokai Electro Chemical Co Solid-liquid separation method for organic waste sludge
GB1583622A (en) * 1977-05-26 1981-01-28 Degussa Process for deodorising liquid manure and for removing noxious gases
JPH10118669A (en) * 1996-10-18 1998-05-12 Mitsubishi Gas Chem Co Inc Oxidizing treatment of organic matter
JPH1129797A (en) * 1997-07-11 1999-02-02 Mitsubishi Gas Chem Co Inc Peroxide-containing composition
WO2004094320A1 (en) * 2003-04-23 2004-11-04 Kemira Kemi Ab Method of treating digested sludge

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62121699A (en) * 1985-11-21 1987-06-02 Nippon Peroxide Co Ltd Method for deodorizing dehydrated cake
DE59301882D1 (en) * 1992-10-16 1996-04-18 Solvay Interox Gmbh Sodium percarbonates stabilized by coating
DE4311944A1 (en) * 1993-04-10 1994-10-13 Degussa Coated sodium percarbonate particles, process for their preparation and detergent, cleaning and bleaching compositions containing them
JPH11158016A (en) * 1997-11-25 1999-06-15 Mitsubishi Gas Chem Co Inc Sodium percarbonate-containing composition
JP2001321428A (en) * 2000-05-16 2001-11-20 Mitsubishi Gas Chem Co Inc Deodorant

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1384207A (en) * 1972-06-05 1975-02-19 Fmc Corp Odour abatement in animal wastes
GB1526129A (en) * 1975-10-09 1978-09-27 Tokai Electro Chemical Co Solid-liquid separation method for organic waste sludge
GB1583622A (en) * 1977-05-26 1981-01-28 Degussa Process for deodorising liquid manure and for removing noxious gases
JPH10118669A (en) * 1996-10-18 1998-05-12 Mitsubishi Gas Chem Co Inc Oxidizing treatment of organic matter
JPH1129797A (en) * 1997-07-11 1999-02-02 Mitsubishi Gas Chem Co Inc Peroxide-containing composition
WO2004094320A1 (en) * 2003-04-23 2004-11-04 Kemira Kemi Ab Method of treating digested sludge

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009050191A2 (en) 2007-10-15 2009-04-23 Kemira Kemi Ab Process for the production of a granule of a coated oxidizing compound such granule and uses of the granule
US8338341B2 (en) 2007-10-15 2012-12-25 Kemira Kemi Ab Process for the production of a granule of a coated oxidizing compound such granule and uses of the granule
US8501670B2 (en) 2007-10-15 2013-08-06 Kemira Chemicals Inc. Well treatment fluid compositions and methods of use that include a delayed release percarbonate formulation
US9150779B2 (en) 2007-10-15 2015-10-06 Kemira Chemicals Inc. Well treatment fluid compositions and methods of use that include a delayed release percarbonate formulation

Also Published As

Publication number Publication date
GB0508622D0 (en) 2005-06-08
WO2006114651A1 (en) 2006-11-02
GB0608357D0 (en) 2006-06-07

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