EP3931395A1 - Abscheidungsverminderung - Google Patents

Abscheidungsverminderung

Info

Publication number
EP3931395A1
EP3931395A1 EP20707095.4A EP20707095A EP3931395A1 EP 3931395 A1 EP3931395 A1 EP 3931395A1 EP 20707095 A EP20707095 A EP 20707095A EP 3931395 A1 EP3931395 A1 EP 3931395A1
Authority
EP
European Patent Office
Prior art keywords
bacteria
bacillus
bearing system
water bearing
derived
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.)
Pending
Application number
EP20707095.4A
Other languages
English (en)
French (fr)
Inventor
Frank DÜRKES
Stefan Franke
Pieter STEENBEEK
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.)
Servophil Ag
Original Assignee
Servophil Ag
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 Servophil Ag filed Critical Servophil Ag
Publication of EP3931395A1 publication Critical patent/EP3931395A1/de
Pending legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C5/00Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
    • D21C5/005Treatment of cellulose-containing material with microorganisms or enzymes
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/005Microorganisms or enzymes

Definitions

  • the present invention relates to a biological process for reducing the level of deposits formed in water bearing systems used in the processing of cellulose, especially water bearing systems used in the production of paper.
  • the invention relates to improving the efficiency of water bearing systems by reducing the level of deposits formed in the water bearing system .
  • the invention relates to improving paper production by reducing the level of deposits formed in a water bearing system used during the production of paper.
  • Paper is available in a variety of types, grades and weights for very different applications, including graphic paper; paper and board for packaging purposes; tissue and hygiene papers; and papers and board for special technical purposes.
  • paper In order to be able to cope with the multitude of applications, paper has different properties depending on the desired use. Such properties are obtained by utilising different complex formulations of the paper fibres, fillers and additives during the production process.
  • various deposits are formed within the paper manufacturing machinery and can build up on parts of the machinery. The formation of such deposits can result in unpleasant odours being generated, a reduction in the quality of paper produced, as well as a reduction in the efficiency of the production method. Accordingly, such deposits need to be removed from the machines, which can lead to production disturbances and a reduction in the manufacturing efficiencies.
  • Cellulose is an essential component of paper. It is a polysaccharide, i.e., a macromolecule made up of many sugar molecules. During the production of paper, various cellulose molecules and cellulose-containing fibres having a variety of different lengths are produced. Certain contaminating bacteria are able to digest and use the cellulose molecules and cellulose-containing fibres as an energy source. The contaminating bacteria digest the cellulose molecules and cellulose containing fibres. During this process certain saccharides (e.g., polysaccharides and monosaccharides) are excreted by the contaminating bacteria.
  • saccharides e.g., polysaccharides and monosaccharides
  • the excreted saccharides include one or more of alginates, dextrane, levane, and the monosaccharide components derived from D-Glucoronic-acid, D-Galacturonic-acid and D-Mannuronic-acid.
  • the industrial habitat lacks the necessary nitrogen compounds for the complete utilization of the cellulose derived energy source to build new cells, and hence excess sugars (i.e., the cellulose derived energy source) are excreted as the above recited saccharides.
  • the excreted saccharides form the basis of the deposits.
  • the excreted saccharides which can comprise up to 97 weight % water, are sticky and will generally adhere to parts of the water bearing systems; however, some of the saccharides can remain suspended within the water. A wide variety of particles can then adhere to the sticky saccharides, which reduce the flow speeds in the system, impair heat transfer, hinder gas exchange and allow the formation of oxygen-poor/oxygen-free areas where anaerobic bacteria can flourish resulting in unpleasant odours and corrosion to parts of the machinery, for example caused by the formation of corrosive hydrogen sulfide.
  • the present disclosure provides a method for reducing deposit formation in a water bearing system used in the processing of cellulose, the method comprising administering a composition comprising bacterial spores and/or bacteria derived from bacterial spores to the water bearing system, wherein the bacteria cannot digest cellulose but can digest one or more of the following saccharides: alginates, dextran, levan and monosaccharide components D-Glucoronic-acid, D-Galacturonic-acid and D-Mannuronic- acid.
  • the water bearing system can be any water bearing system used in the processing of cellulose wherein deposits are formed on parts of the water bearing system. Suitable water bearing systems include systems involved in wood, and wood pulp processing, and especially water bearing systems used in the production of paper.
  • the water bearing systems can be open or closed systems; however the present method is particularly suitable for reducing deposit formation in substantially closed water bearing systems (i.e., systems where over 80%, over 90% or over 95% of the water is recycled) and fully closed water bearing systems.
  • the present method is particularly suitable for use in reducing deposit formation in water bearing systems used in the production of paper, especially the white water circuit.
  • paper refers to any form of paper including graphic paper; paper and board for packaging purposes; tissue and hygiene papers and papers and board for special technical purposes.
  • Reducing deposit formation refers to lowering the amount and/or size of deposits formed on surfaces of the water bearing system.
  • the deposits are formed by the action of contaminating bacteria on cellulose molecules and cellulose containing fibres resulting in the production of saccharides that adhere to surfaces of water bearing systems.
  • a wide variety of particles e.g. additional polysaccharides, starch, glues, alkyl ketene dimers (AKD) and other organic or polymer-like deposits
  • a wide variety of particles e.g. additional polysaccharides, starch, glues, alkyl ketene dimers (AKD) and other organic or polymer-like deposits
  • the present method reduces the formation of deposits on the surface of the water bearing system, so that at least 10%, 50% or 90% fewer deposits are formed on the surface of the water bearing system when the composition comprising the bacterial spores and/or bacteria derived from bacterial spores is administered to the water bearing system.
  • the composition used in the method comprises: (1) bacterial spores that germinate and producederived bacteria; and/or (2) bacteria that are derived from bacterial spores.
  • derived bacteria refers to both bacteria derived from the bacterial spores present within the composition, and bacteria that have previously been derived from bacterial spores and are present within the composition.
  • the derived bacteria do not need to be directly derived from a bacterial spore but include subsequent generations of bacteria.
  • the derived bacteria can be any suitable bacteria that can breakdown the saccharides formed by the contaminating bacteria (i.e., the saccharide-producing bacteria) and thereby destabilize and at least partially break down the deposits.
  • the derived bacteria can digest one or more of the following saccharides: alginates, dextran, levan and monosaccharide components D-Glucoronic- acid, D-Galacturonic-acid and D-Mannuronic-acid. In certain embodiments the derived bacteria can digest at least two, three, four or more of the saccharides. In a particular embodiment the derived bacteria can digest all the saccharides.
  • the derived bacteria are not able to break down cellulose, and therefore will not contribute to forming the saccharides that form the basis of the deposits.
  • the bacterial spores and the derived bacteria are not pathogenic, i.e., they belong to risk group 1 ( ⁇ 3 of the Ordinance on Biological Substances).
  • the derived bacteria are genetically stable and therefore will not develop atypical characteristics during use in the water bearing system.
  • the spores and the derived bacteria are used in a water bearing system during the processing of cellulose, in particular during the production of paper, and therefore need to tolerate the conditions within such water bearing systems.
  • the bacteria will need to tolerate temperatures from 10-60°C, pH values from 5-8, and salt densities of 3-5 weight %).
  • the derived bacteria should remain stable in an aqueous solution and be able to multiply within the water bearing system.
  • the derived bacteria should also be able to colonise surfaces of the water bearing system, and, in certain embodiments, form a biolayer on surfaces of the water bearing system.
  • the derived bacteria use oxygen for metabolism (i.e., are aerobic) and are actively mobile. The use of oxygen prevents formation of corrosive hydrogen sulfide and sulfide-related material destruction. The ability to move actively enables active movement and spreading on the surfaces of the water bearing system.
  • bacterial spore derived bacteria provides the advantage of being able to produce, store and transport stable spore compositions. Accordingly, the bacterial spores can be stored for a prolonged period of time (i.e., for many months), and transported without any special requirements (e.g., temperature, nutrients, etc.).
  • the spores can be directly added to the system resulting in the production of the derived bacteria in the system.
  • the spores can also be formulated into a suitable composition/suspension (e.g., aqueous composition/suspension) prior to administration to the water bearing system.
  • bacterial spores encompasses all bacterial spores, and especially includes endospores.
  • Particularly suitable derived bacteria include bacteria of the genus Bacillus. a genus of bacteria with more than 200 species.
  • Particularly suitable bacterial spores and/or bacteria derived from bacterial spores for use in the method include:
  • Bacillus altitudinis e.g., deposited strain DSM21631
  • Bacillus amyloliquefacies e.g., deposited strains DSM 7, ATCC 23350;
  • Bacillus coagulans e.g., deposited strain DSM 2314
  • Bacillus kokeshiiformis e.g., deposited strains MO-04, JCM 19325.
  • Bacillus licheniformis e.g., deposited strains DSM 13, ATCC 14580, DSM 46308, DSM 8785;
  • Bacillus megaterium e.g., deposited strains DSM 32, ATCC 14581;
  • Bacillus pumilus e.g., deposited strains DSM 27, ATCC 7061;
  • Bacillus subtiHs e.g., deposited strains DSM 10, ATCC 6051, DSM 5749, DSM17299;
  • Bacillus thermoamylovorans e.g., deposited strain DSM 28625.
  • particularly suitable bacterial spores and/or bacteria derived from bacterial spores for use in the method include:
  • Bacillus amyloliquefacies e.g., deposited strains DSM 7, ATCC 23350;
  • Bacillus licheniformis e.g., deposited strains DSM 13, ATCC 14580
  • Bacillus megaterium e.g., deposited strains DSM 32, ATCC 14581
  • Bacillus pumilus e.g., deposited strains DSM 27, ATCC 7061;
  • Bacillus subtiHs e.g., deposited strains DSM 10, ATCC 6051, DSM 5749, DSM17299.
  • the bacteria used in the method can be obtained from numerous commercial sources, including official strain collections (DSMZ, ATCC etc.).
  • DSMZ official strain collections
  • ATCC ATCC etc.
  • the example strains indicated above are given as examples only.
  • any strain of the recited Bacillus species can be used in the methods described herein.
  • the composition comprising the bacterial spores and/or bacteria derived from the bacterial spores may include just the spores or just the derived bacteria, or a mixture of the spores and the derived bacteria.
  • the composition comprises the bacterial spores, and is substantially free of the derived bacteria, i.e., comprises less that 1%, or less than 0.1% of the derived bacteria.
  • the composition comprising the bacterial spores and/or bacteria derived from bacterial spores may include a mixture of different types of spores and/or derived bacteria, e.g., different species, or just one type (i.e., a single species).
  • the composition can comprise one or a plurality of the Bacillus bacterial species listed above. In some embodiments the composition comprises 3, 4 or 5 different Bacillus species selected from the bacterial species listed above. In one embodiment the composition comprises 5 different Bacillus species.
  • the 5 species can be any combination of the Bacillus species listed above, and in one particular embodiment the 5 different species are Bacillus amyloliquefacies (e.g., deposited strains DSM 7, ATCC 23350); Bacillus licheniformis (e.g., deposited strains DSM 13, ATCC 14580); Bacillus megaterium (e.g., deposited strains DSM 32, ATCC 14581); Bacillus pumilus (e.g., deposited strains DSM 27, ATCC 7061); and Bacillus subtilis (e.g., deposited strains DSM 10, ATCC 6051, DSM 5749, DSM17299).
  • Bacillus amyloliquefacies e.g., deposited strains DSM 7, ATCC 23350
  • Bacillus licheniformis e.g., deposited strains DSM 13, ATCC 14580
  • Bacillus megaterium e.g., deposited strains DSM 32, ATCC 145
  • An advantage of including a mixture of different types of spores and/or derived bacteria is that the derived bacteria may have a variety of characteristics to enable a broader range of functionality, e.g., can function to breakdown a greater variety of saccharides and/or can function to breakdown the saccharides under a variety of different conditions (e.g., temperature, pH, salt concentrations, etc.).
  • the composition comprising the bacterial spores and/or derived bacteria may additional comprise one or more additives. Suitable additives include the necessary media components to ensure that the spores and/or derived bacteria are maintained functionally. The media requirements for the spores and derived bacteria are well known to those skilled in the art.
  • the composition may additionally comprise an energy source for the derived bacteria to ensure that there is a sufficient initial energy source available for the derived bacteria on addition to the water bearing system. In one embodiment the composition comprising the bacterial spores and/or derived bacteria does not allow multiplication of the bacteria (e.g., due to the presence of only a minimal amount of an energy source). By preventing multiplication the concentration of the bacterial spores and/or derived bacteria is maintained.
  • a further addition component may be a pH modifying agent such as limewater (calcium hydroxide).
  • the present method reduces the level of deposit formation in water bearing systems, especially in water bearing systems used in the production of paper. Accordingly the method provides an improvement in paper productivity and in the ability to consistently produce quality paper.
  • the method can also reduce odours and damage to the water bearing system by reducing the level of anaerobic bacterial growth and the production of corrosive hydrogen sulphide. In particular, by reducing the level of deposits forming in the water bearing sytem, water flow in the system is not disrupted thereby avoiding the formation of areas where anaerobic bacterial growth can occur.
  • composition comprising the bacterial spores and/or derived bacteria can be administered to the water bearing system in any suitable manner.
  • the bacterial spores and/or derived bacteria containing composition maybe administered directly into the water bearing system. Such direct administration may be made at one site or at multiple sites within the water bearing system.
  • the administration may be made continuously or batch wise by any suitable method, such as a controllable and adjustable pump.
  • the bacterial spores and/or derived bacteria are generally suspended in an aqueous solution, and then administered to the water bearing system.
  • one or more suitable dosing points should be selected.
  • the added suspension should be mixed with the circulating water as quickly as possible in order to achieve successful dispersion within the water bearing system.
  • Addition of the bacterial spores and/or derived bacteria should be managed so that there is an energy source available for the spore forming bacteria. Accordingly, it is generally not recommended to add the bacterial spores and/or derived bacteria shortly after the water bearing system has been cleaned, since a sufficient amount of saccharide deposits must be present to act as an energy source for the derived bacteria.
  • bacterial spores and/or derived bacteria can be added to a clean water bearing system.
  • Addition of the bacterial spores and/or derived bacteria in a water bearing system that has already built up large deposits should also be avoided, as even successful growth and high degradation activity cannot degrade the deposit uniformly without the formation of large shreds.
  • the formation of such large shreds risks affecting quality of the product being produced in the water bearing system, e.g., paper quality.
  • the amount of bacterial spores and/or spore forming bacteria to be administered will depend on the size of the water bearing system, the level of deposits present within the system, and the expected rate of deposit generation. The required amount can be determined by one skilled in the art and adjusted over time.
  • the bacterial spores and/or derived bacteria bind to the deposits and/or surfaces of the water bearing system.
  • the bacteria then multiply and the spores germinate and produce derived bacteria.
  • the saccharides forming the basis of the deposits are metabolized by the derived bacteria.
  • the derived bacteria grow and multiply, the deposits on the surfaces in the water bearing system are colonised and reduced by the activity of the bacteria.
  • the bacteria can penetrate the deposits and degrade them below the surface. This can result in the detachment of small shreds of the degraded deposits.
  • the rate of growth of the derived bacteria may vary.
  • the conditions within the water bearing system can be adjusted to achieve a desired level of bacterial growth. Where this is not possible it may be necessary to add additional bacterial spores and/or derived bacteria to the system.
  • the bacteria will form spores (i.e., endospores). Accordingly, in order to compensate for any loss of the bacteria, e.g., via discharge from the water bearing system, and/or spore formation, the bacterial spores and/or derived bacteria material can be replenished. Such replenishment can occur continuously, batch wise, or when deemed necessary, i.e., when odour and/or significant deposit levels are detected.
  • One way to determine the effectiveness of the method is to measure the amount and/or rate of deposit formation in the water bearing system. Suitable methods for making such a measurement are well known to those skilled in the art.
  • a probe can be positioned within the water flow and measurements made to determine the amount and/or rate of deposit formation on the probe. Electrical capacity, heat exchange, ultrasonic, optical density, and weight measurements can be made to determine the amount and rate of deposit formation. It should be noted that when measuring the thickness of the deposits, the thickness seems to increase following exposure to the bacterial spores and/or spore forming bacteria, and then decreases. The reason for this contradictory signal is believed to be due to the initial loosening of the deposit resulting in an increase in water penetration temporarily swelling the deposit.
  • the amount of bacterial spores and/or derived bacteria added to the system can be adjusted. For example, if the amount of deposits is increasing, the amount of bacterial spores and/or derived bacteria added to the system can be increased. Alternatively, if the level of deposits is maintained at an acceptably low level, then the amount of bacterial spores and/or spore forming bacteria can be maintained. As those skilled in the art will appreciate such a feedback loop can be automated.
  • the measurement of the deposits is preferably made in the white water circuit of the paper manufacturing machine. Accordingly, when a probe is used to make the measurement it is preferred that the probe is positioned within the white water circuit of the paper manufacturing machine.
  • the present invention is also directed to a composition
  • a composition comprising bacterial spores and/or bacteria derived from the bacterial spores for administration into a water bearing system, wherein the bacteria cannot digest cellulose but can digest one or more of the following saccharides: alginates, dextran, levan and monosaccharide components D-Glucoronic-acid, D-Galacturonic- acid and D-Mannuronic-acid, and wherein the composition further comprises a stabilising agent and/or a non-biocidal-active quaternary ammonium compound.
  • the bacterial spores and/or bacteria derived from the bacterial spores are as defined above.
  • the composition comprising the bacterial spores and/or bacteria derived from the bacterial spores may include just the spores or just the derived bacteria, or a mixture of the spores and the derived bacteria.
  • the composition comprises the bacterial spores, and is substantially free of the derived bacteria, i.e., comprises less that 1%, or less than 0.1% of the derived bacteria.
  • composition comprising the bacterial spores and/or bacteria derived from bacterial spores, may include a mixture of different types of spores and/or derived bacteria, e.g., different species, or just one type (i.e., a single species).
  • the bacterial spores and/or bacteria derived from bacterial spores, as well as the mixtures thereof, are as defined above.
  • the stabilising agent can be any suitable stabilising agent such as glycerine. Suitable non-biocidal-active quaternary ammonium compounds are well know to those skilled in the art.
  • the composition comprising the bacterial spores and/or derived bacteria may, as indicated above, additional comprise one or more additional additives. Suitable additives include the necessary media components to ensure that the spores and/or derived bacteria are maintained functionally. The media requirements for the spores and derived bacteria are well known to those skilled in the art.
  • the composition may additionally comprise an energy source for the derived bacteria to ensure that there is a sufficient initial energy source available for the derived bacteria on addition to the water bearing system. In one embodiment the composition comprising the bacterial spores and/or derived bacteria does not allow multiplication of the bacteria (e.g., due to the presence of only a minimal amount of an energy source).
  • a further addition component may be a pH modifying agent such as limewater (calcium hydroxide).
  • a further aspect of the present invention is a water bearing system for use in processing cellulose, and having a biolayer of bacterial spores and/or bacteria derived from the bacterial spores formed on a surface of the system, wherein the bacteria cannot digest cellulose but can digest one or more of the following saccharides: alginates, dextran, levan and monosaccharide components D-Glucoronic-acid, D-Galacturonic-acid and D-Mannuronic-acid.
  • the bacterial spores and/or bacteria derived from the bacterial spores are as defined above.
  • the water bearing system can be any water bearing system for processing cellulose, and in certain embodiments is a water bearing system used in the manufacture of paper. In one embodiment the water bearing system is a white water circuit used in the production of paper.
  • the water bearing system having the biolayer can be formed by administering a composition of the bacterial spores and/or bacteria derived from the bacterial spores, and allowing the biolayer to form.
  • the biolayer can form on a surface of the system where deposits have or are expected to form.
  • Figure 1 shows a schematic representation of the mode of action of the method for reducing deposits using the bacterial spore composition disclosed herein.
  • Figure 2 shows the effect of the bacteria on the level of polymer build up.
  • Figure 3 shows the effect of the bacteria on deposit formation within the water bearing system of a paper mill.
  • Figure 4 shows the level of organic acids measured in the system overtime.
  • Figure 5 shows the effect of the bacteria on the disc filters within the paper mill.
  • Figure 6 shows the level of deposits on the walls of a paper mill measured using a heat exchange sensor.
  • Figure 7 shows a headspace gas chromatography of a tissue demonstrating that the level of volatile odour producing compounds within the tissue is reduced when bacteria are present within the water bearing system of the paper mill.
  • Figure 8 shows the effect of the bacteria on various parts of the paper mill.
  • Figure 9 shows chromatography of the headspace in the paper mill demonstrating that with the bacteria the odour level is reduced.
  • Figure 10 shows the effect of including the bacteria in the water cooling sytem of a paper mill.
  • Clean retention agent system through the use of the biological material in the fresh water A paper mill producing 100% recycled paper from waste paper was found to produce a strong odour.
  • the closed water system was found to be heavily contaminated with a variety of organic acids.
  • the system was cleaned, and the water changed. After operating for 7 days, 4.8 L/d of a bacterial spore mixture was administered to the system.
  • the bacterial spore mixture comprises bacterial spores of the following bacterial species Bacillus amyloliquefacies ; Bacillus licheniformis ; Bacillus megaterium, ⁇ Bacillus pumiius ; and Bacillus subtiiis.
  • limewater calcium hydroxide
  • the bacterial spore mixture was added to the system a year after the initial addition at a concentration of 5 L/d.
  • the system has been operated continuously for 2 years without any odour and without any detrimental levels of deposits forming.
  • a cylinder wet machine having a 98% closed circuit was used in the manufacture of cardboard from 100% waste paper continuously for 6 days a week.
  • Oxidative biocide l-Bromo-3-chloro-5,5-dimethylhydantoin (BCDMH) was used in the system to try and reduce odour and deposit formation. Chlorine bleaching lye was also used to try and reduce odour and deposit formation. Both approaches had limited success. 2 L of the bacterial spore mixture used in Example 2 was introduced into the Krofta overflow at a rate of 4.8 L/d. Within a few weeks the odour became noticeably better and the pH value dropped slightly. Limewater was added to increase the pH to a range from 6.3 to 7.3.
  • the bacterial spore mixture was added at a concentration of 4.5el l spores/L at a rate of 6 L/d, with the controlled addition of limewater to increase the pH to a range from 6.3 to 7.3. Biocides are no longer used in the factory.
  • Figure 4 shows the level of organic acids in system overtime. Without bacterial spores the amount of organic acids rises up to 7500 and 7300 mg/L. After addition bacterial spores the amount of the organic acids decreased to 6000 mg/L.
  • batches of tissue were produced with holes in the tissue and with stains on the tissue.
  • Example 2 The system was intensively cleaned and 2L of the bacterial spore mixture used in Example 2 was introduced in the clean water of the machine: 24 dosing pulses of 17 min each, 3.46 L/d. Bacterial spores are added at a concentration of 4.5el l/L.
  • Figure 5 shows the effect of the bacteria on the disc filters within the paper mill.
  • Example 2 The system was intensively cleaned and the bacterial spore mixture used in Example 2 was introduced in the clean water of the machine: 24 dosing pulses of 18 min each, 3.46 L/d.
  • This treatment resulted in a reduction in odour in the produced tissue and fewer deposits on the water bearing system.
  • Figure 6 shows measurments of the thickness of the deposits using heat exchange measurements (i.e., the amount of heat that is conducted through the walls of the water bearing system is measured, wherein the presence of deposits reduces the amount of heat conducted). Electrical capacity, ultrasonic, optical density, and weight measurments can also be used to determine the amount and rate of deposit formation. It should be noted that when measuring the thickness of the deposits, the thickness seems to increase following exposure to the bactierial spores and/or spore forming bacteria, and then decreases. The reason for this contradictory signal is believed to be due the initial loosening of the deposit resulting in an increase in water penetration temporarily swelling the deposit.
  • Figure 7 shows a headspace gas chromatography of tissue produced in the absence of the spore derived bacteria and a tissue produced in the presence of the spore derived bacteria. The result shows that the level of volatile odour producing compounds in the tissue is reduced when the bacteria are present within the water bearing system of the paper mill .
  • Figure 8 shows the effect of the addition of the bacterial spore mixture on various parts of the paper mill .
  • the heavy contamination of the white water and the disc filters can be seen, as well as the significantly cleaner surfaces obtained after running the system with the bacteria derived from the bacterial spores.
  • Tissue obtained from the paper mill operated with and without the addition of the bactierial spore mixture was tested using headspace gas chromatography.
  • Figure 9 shows that the level of volatile odour producing compounds in the tissue is reduced when the derived bacteria are present within the water bearing system of the paper mill.
  • Figure 10 shows the effect of the spore derived bacteria on the level of deposits in the cooling water system of a paper mill .
  • the functionality of the cooling water system was reduced due to the presence of significant deposits on the walls of the cooling water sytem and in the water itself.
  • the addition of the bacterial spore mixture resulted in significantly reduced deposits on the wall of the cooling water system and in the water itself.
  • the functionality of the cooling water system was significantly improved.
  • the added biological material is functional bacteria, such as probiotic bacteria and in particular bacteria germinated from spores.
  • the water-bearing circuit is a circuit on a paper machine.
  • the biological material in particular forms a thin protective film on the surfaces.
  • the biological material is dosed continuously or shockwise into the water-bearing circuit.
  • the biological material is prepared under specified conditions as regards concentration, pH, temperature and/or nutrient supply before dosing.
  • the deposits are at least partially organic in nature.

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  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • Chemical & Material Sciences (AREA)
  • Biochemistry (AREA)
  • Paper (AREA)
  • Apparatus For Disinfection Or Sterilisation (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)
EP20707095.4A 2019-02-25 2020-02-25 Abscheidungsverminderung Pending EP3931395A1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102019104735 2019-02-25
PCT/EP2020/054944 WO2020173963A1 (en) 2019-02-25 2020-02-25 Deposition reduction

Publications (1)

Publication Number Publication Date
EP3931395A1 true EP3931395A1 (de) 2022-01-05

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CN112725226B (zh) * 2020-12-28 2022-10-11 海南大学 产纤维素酶细菌c18的筛选及其微生物制剂的天然纤维素降解方法
CN112662582B (zh) * 2020-12-28 2022-10-11 海南大学 产纤维素酶的海洋细菌hn b15及其微生物制剂和天然纤维素的降解方法

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WO2001066471A2 (en) * 2000-03-08 2001-09-13 Hercules Incorporated Control of spore forming bacteria in aqueous systems
WO2004098291A2 (en) * 2003-03-17 2004-11-18 Novozymes Biologicals, Inc. Methods for inhibiting fungal growth in materials
DK1957415T3 (da) * 2005-11-11 2010-09-27 T T B S Llc Produkt til behandling af spildevand og kloak
JP2007261992A (ja) * 2006-03-28 2007-10-11 Eisai Seikaken Kk 土壌病害抑止剤
CA2808495A1 (en) * 2010-08-25 2012-03-01 Tate & Lyle Ingredients Americas Llc Synbiotic product
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EP3481203A1 (de) * 2016-07-08 2019-05-15 Novozymes BioAG A/S Sequenzielle zugabe von molekularen keimlingen mit bakteriensporen

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