AU613402B2

AU613402B2 - A cleaning method and apparatus therefor

Info

Publication number: AU613402B2
Application number: AU22163/88A
Authority: AU
Inventors: Lars Ake Hilmer Hakansson
Original assignee: Individual
Current assignee: Individual
Priority date: 1987-09-21
Filing date: 1988-09-13
Publication date: 1991-08-01
Anticipated expiration: 2008-09-13
Also published as: AU2216388A; EP0309432B1; SE8801511L; JPH01159387A; ES2041338T3; EP0309432A2; EP0309432A3; SE8801511D0; DE3880246T2; DE3880246D1

Description

AUSTRALIA

PATENTS ACT 1952 3 COMPLETE SPECIFICATION 3 m

(ORIGINAL)

FOR OFFICE USE Short Title: Int. Cl: Application Number: Lodged: Complete Specification-Lodged: Accepted: Lapsed: Published: 0 Priority: S 0 °Related Art: o 0*o I TO BE COMPLETED BY APPLICANT 0 S I Name of Applicant: Lars Ake Hilmer HAKANSSON Address of Applicant: LINDOHALLSVAGEN SS-603 65 NORRKOPING

SWEDEN

Actual Inventor: S Address for Service: GRIFFITH HACK CO., 601 St. Kilda Road, Melbourne, Victoria 3004, Australia.

Complete Specification for the invention entitled: A CLEANING METHOD AND APPARATUS

THEREFOR

The following statement is a full description of this invention including the best method of performing it known to me:k Sa a A cleaning method and apparatus therefor a, a.

o a0 a ao 994 a 4 #a a 4 #4 4 *a 4 O 40 a a a 00~ 4 44 4 a The present invention relates to a method for cleaning objects and materials, and particularly, althoigh not exclusively, for removing organic substances such as hydrocarbons, greases, waxes, oils, tars, pitches, proteins and peptides, particularly oils and greases and their decomposition products for biodegradation thereof.

The invention also relates to apparatus for carrying out the method.

10 The invention relates more specifically, although not exclusively, to degreasing biologically objects which are contaminated with cutting oils, lubricants, grinding oils or process oils, prior to the further treatment of said objects.

Degreasing is an absolute necesrity when the objects concerned are to be treated by processes such as phosphating processes, electrolytic processes, varnishing etc., if good results are to be achieved.

Conventional degreasing of such objects is more often than not effected with a caustic soda solution, or lye, at high bath temperatures, which affords a good result initially.

However, the bath gradually becomes enriched with oils removed from the objects and the degreasing capacity of the bath will fall-off radically when the oil contents of the bath exceeds 0.5 by weight. This also applies to degreasing baths, which are maintained at temperatures of from 90 to 95 0 C. Objects which have been treated with a caustic soda solution are also difficult to wash clean.

Furthermore, processes which utilize caustic acid solu- 2 tions and high bath temperatures are hazardous to the environment.

According to the present invention, there is provided a method for cleaning objects, characterized by cleaning said objects by treating them with an aqueous tenside solution such as to emulsify the organic contaminants present, by stimulating the growth of microorganisms in the tenside solution for biodegradation of the organic substances, and by adding nutrient substances so that the tenside solution substantially is unaffected, the biodegradation being a performed separately from or simultaneously with the cleaning.

o a oc According to the present invention, there is further provided an apparatus which is to be used for cleaning objects in accordance with the abovementioned method characterized by a cleansing tank which is located above a washing liquid tank and above a rinsing liquid tank, the bottom of the cleansing tank being completely or partially oo o common with the ceiling of the washing liquid tank and the rinsing liquid tank.

In order that the invention might be more fully understood, embodiments of the invention will now be described in more So'* detail by way of example with reference to the accompanying S drawings, in which: Fig. 1 is a flow chart, illustrating a common bath for carrying out degreasing and biodegradation processes in accordance with Example 1, Fig. 2 is a flow chart illustrated separate units for effecting degreasing and biodegradation processes in accordance with Example 3, and Fig. 3 illustrates a preferred embodiment of apparatus for carrying out the method for cleaning objects.

When practicing an embodiment of the inventive method, the i 1

I-

3 objezts are instead washed with tensides which emulsify the organic substances, whereafter the emulsified hydrocarbons are degraded to carbon dioxide and water, by adding nutrient salts to the bath, so as to activate the microorganisms present in the contaminating substances and therewith result in the degradation of said substances. By composing a degreasing bath in accordance with an embodiment of the. invention and utilizing natural oil-consuming bacteria which accompany the contaminated objects, it is possible to degrease the objects while biologically reducing, at the same time, the entrant oils carried into the bath.

Tensides are thus able to be used for cleaning purposes instead of caustic soda solutions. Furthermore, the tensides are not consumed to the same extent as the caustic soda solutions used in conventional methods, because the cleaning bath composed in accordance with the invention can be used effectively for two years owing to the degradation 'i of entrant oils and greases. Conventional degreasing processes using caustic soda solutions can only be used effectively for a short period of time. Furthermore, the cleaning process of the embodiment can be carried out at a low temperature. These advantages afforded by the embodiment result in a considerable reduction in costs compared with prior art degreasing processes in which caustic soda solutions are used. The process of the 41 4* embodiment is also more friendly to the environment.

Objects or materials cleaned with the aid of tensides can S also be washed easily. Conventionally, the use of tensides *has been prohibited by the fact that their degreasing ability falls off rapidly with increasing oil levels, thereby necessitating quick replenishment of the tensides.

Because of the tenside costs incurred hereby, such replenishment has rendered the process highly expensive.

The proposed bacteria degradation or decomposition, of the N 3A contaminants present enables, for the first time, tensides to be used in an efficient and rational fashion.

In order to initiate the cleaning process it is necessary first to accumulate a given amount of organic substances such as oil and accompanying bacteria, prior to activation of the bacteriological life. The oil is preferably accumulated in the cleaning bath, by adding thereto a tenside solution of basic pH 7-14, particularly by adding a ibaic tenside solution of pH 9-11.

Cleaning can be effected with any kind of water-soluble tenside whatsoever, such as anionic, cationic, nonionic and amphoteric tensides. These can be tensides which are l not-readily degradable by microorganisms, such as the halogen-containing (chloro-bromo- and fluoro-containing) j tensides and heterocyclic tensides. Biodegradable tensides are preferably used, however, so that sludge, slime, S separated from the process will not contaminate the surroundings. It is correct procedure, however, to control o° the process so that the microorganisms will not degrade the tensides. This control process is preferably effected by o t 0 9 I* t4 4 ensuring that the hydrocarbon content of the bath will not fall beneath 50 mg/liter and that the tenside content will not rise above 15 by weight. By proceeding in this way it is ensured that the microorganisms will substantially degrade the organic contaminants present under all conditions and that the tensides are practically unaffected and regenerated and can be reused. The tensides will probably work at a pH of 7 up to an alkaline pH-value which will not block microbial growth. This pH-value is, at present, about 9.5, but may conceivably increase through genetic manipulation of the microorganisms. It has been found that good cleaning and degreasing results are achieved at alkaline pH-values above o Q It is also possible to draw off part of the cleaning liquid and to allow biodegradation to take place in a v separate unit or facility. In this case higher alkaline 1 pH-values can be used in the actual cleaning bath. Thus, when the cleaning and biodegradation processes are effected separately, the cleaning process can be carried out at "pH-values of from 7 to 14. When the cleaning processes and 0 00 "o 0 biodegradation processes are carried out in one and the same bath, the pH-value is preferably adjusted to between OQ 9.0 and :r Because organic substances such as oil and grease are emulsified continuously in the bath, the pH-value will decrease as a result of tensides being consumed and bound by the emulsified substances. When the pH-value has fallen to about 9.2-9.4, careful metering of nutrient solution to the bath can be commenced, so as to activate the latent bacteria culture in the bath. In the case of systems having a volumetric capacity of 2 m the system should be activated immediately, whereas systems having volumetric capacities in the order of 50-100 m 3 should not be activated until the oil content of the bith has risen to about 500-1000 mg/liter.

It is also important that fresh tensides are metered continuously to the bath, such as to maintain a constant tenside content and emulsifying capacity. The tenside content is preferably maintained at between 1-15 by weight, preferably between 2-5 by weight in the case of objects soiled to normal levels, and between 5 and 10 by weight in the case of heavily soiled or contaminated objects. When the cleaning and biodegradation processes are carried out separately from one another, the tenside content of the cleaning bath may be maintained at a high level, while the bath in which biogradation takes place is maintained at the aforesaid tenside level.

pa a 0 0 0 The content of organic substances should not fall beneath 50 mg/ in the biodegradation process, since bacteria can Sbegin to consume the tensides at lower contents of organic o contaminants. In the case of large bacteria populations, the pH-value may fall rapidly as a result of the high consumption of emulsifying chemicals and also as a result of acid generation by dead bacteria. The contaminant con- S" tent such as oil and grease should be maintained between o 50-1000 mg/4-, preferably between 50 and 250 mg/ml, by adding to the system nutrient substances and pH-increasing Ssubstances.

o The temperature has also a decisive significance on optimum cleaning capacity. When the cleaning and biode- :gradation processes are effected separately from one another, the temperature of the cleaning bath may be between 20 and 100 0 C. When cleaning and biodegradation are effected in one and the same bath, the bath should be maintained at a temperature of between 20 and 8000, preferably between 30 and 400C, and more preferably between 35 and 40°C, which has been found to be a splendid working range in the case of mesophilic bacteria.

Good cleaning results are obtained in this temperature ,s0 6 range while, at the same time, the low temperature used requires only a low energy input. In the case of certain degreasing processes used, for instance, to remove waxes and paraffins, the degreasing temperature must lie above 50-60 C, in which case it may be suitable to use separate facilities for degreasing and biodegradation purposes.

Conversion of the bacteria population takes place more rapidly at temperatures above 40 0 C, at which preferably termophilic bacteria are active, and consequently the content of organic contaminants should lie above 300 mg/liter in order to prevent the bacteria from attacking the degreasing chemicals.

O A high degree of bacteria activity is required when large quantities of organic contaminants enter the bath. Large numbers of bacteria are also killed therewith. Certain bacteria species when dead produce toxic substances which are liable to destroy the biological life. Consequently, 20 it is \to separate dead bacteria continuously from the cleaning bath. Since dead bacteria have a low 0a sedimentation rate (about 0.1 m/h) their separation from the bath may at times prove troublesome. The separating apparatus described in Swedish Patent Specification 7701734-1 is preferably used in this regard. ~Ts speo The method is preferably made aerobic by introducing air, which can be atomized with the aid of nozzles.

1 The tensides F- i eee are described in more detail hereinafter, wherein in the formulae recited R is an alkyl residue having a long chain with 8-20 carbon atoms, R' is a short alkyl residue having 1-8 carbon atoms or H, and X is an alkylene residue, particularly -(CH 2 )n when n is 1, 2 or 3.

The tensides 'in-3adtj-a--t- -rl may be anionic tensides, such as detergents and soaps, e.g. salts of carboxylic acids, suitably alkali, particularly potassium salts and amine salts (mono-, di- and triethanol amine salts), morpholine salts of fatty acids

R-COO-,

particularly having 12, 13, 14, 15, 16, 17 and 18 carbon atoms. There is also used salts of carboxylic acids having inserted ether-, carbon-, amide-, ester- and sulfonamide groups.

R-CONH-X-COO,

S o a 4 0

R

CH-SO NH-X-COO, R S o a' 0 6O

R-O-X-COO,

a *0

R-S-X-COO,

Sulfuric acid esters can also be used, such as sulfated oils and fatty acids, such as sulfuric acid esters

R-CH-X-C

1 OR OsO sulfated amides

R-CH-X-C

1NHR' 0s0 3 alkyl sulfates R-.0S0 3 sulfated fatty acids monoglycenides of the formula IR-C0O-CH 3- CH-CH2-OSO 3

O

1 9sulfatedii etherster '1 9s 9 O 99 99 9 9,999 988 9990 94 9s 4 91 989 4 9 O 9 09 9 4Q 9 9s 99 9 9~ 99 9994 9 99 94 9 CH 2

-COOR

I

-0 3S-CH-COOR, alkyl sulfonates having intermediate groups X RCOO-X-SQ R-CON-X-SO3

I

0 i 0S 3 alkyl phosphates

R-O-PO

3 10 Alkylaryl sulfonates can also be used, such as alkyl naphthalene sulf'onates Sa: 4 4 9 p4994 e 4sa and alkyl benzene sulfonates R

X

so and alkyl Phosphates and salts of alkyl benzene phosphonic, acids *a 0 0a 6 a a 4 a a a 4 0 0 04 0 0 SQ a so S Do 54 49 a O a as S BC Sd 0 4 R

PO

0a also used cationio tensides, particularly with chlorine or methylsulfate ions as catanions, e.g. amine salts, primary, secondary and teriary amine salts R-NH

R-NH

2 -'1 20

R-NH-RI

F'

primary, secondary and tertiary amine salts with inter- 25 mediate ions X l-cOO-X-NHRP

E-?ONH-X-NHB

3 B--X-NHfl 2 a r quarternary ammonium salts RI-NI-3' also with intermediate molecyles X as for the amine salts 1 phosphorjum salts #4 40 #4 0 O 4 4 44 0 4444 0 4~04044 4 4 44 0 O 4* 4 44 #4 0 44 4 #4 4 ~4 44 4 0 00 4 44 4 O ~4 400* 4 04 #4 0 #4 04 00 0 4 0 0 040040 4 4 1+ 15

R

and solfonium salts

R'

20 ,j- Amphoteric tensides can also be used, such as betaines f-N-X-COQ,

I

sulfobeta ines Rf FR-N-X ,SO 1 3' 12 and sulfate betain-es

I+

R-N-X-0-S0 3 Nonionic tensides can also be used, such as ethylene oxide such as alkyl polyethylene glycols 4 alkylene polvethyl ne glycols 4:E-k (O-CtA?-CH2)n,-OH, Acy]. polyethylene tgl'cols

R-CO(Q-CH

2 CH?)4 O{ a n z1-60 oxyethylated polypropylene glycols H (Q-GH 2

-CH

2 n (0-CH-.CH 2 rif(0-CH 2 nOH

CI

amine toxilate

(CH

2

CH

2 On H

RN

(CH 2 CH 0) nH 13 Among these compounds there is preferably used those which have a weak to average degree of oxyethylisation (n about 0.3-0.7x 2 where n is the number of moles ethylene oxide per mole of starting substance and c is the number of carbon atoms in the hydrophobic residue),. Fatty acid monoglycerides are also used R-COO-CH 2-CH-CH2-0,

OH

onhydrosorbite-monofatty acid esters to 4 4 15 B-COO-C H 0 4 46 11 1 fatty acid alkylene amides

R-CONH-X-QH,

"R-CON-X-OH

R-COO-C13 H020* 4 4 These tensides can either be used individually o in mixtures. Cationi0 and nonionic tensides and mixtures thereof are used in particular, especially nondionic ethylene oxice adducts. Examples of tensides which can be used in this regard include 616 Allrent (contains nontonic tensides 2-nonyl-pheno, cationi tensides alkyl polyglycolether ammonium methyl sulfate, tetra potassium pyrophosphate, sodium citrate, preservatives, isopropanol, 14 perfume, water and trisodium nitrilo triacetate). Via, Surf, Radion 0, Meggem 8510® (ethylene oxide adducts, glycols, phosphates, silicates). These detergents often contain an alkaline substance which will not block microbiological growth and auxiliary washing agents such as polyphosphates, The substances used to adjust the pH of the system shall be soluble in water, although they should not have a negative effect on the tensides and the microbiological conversion. Examples of such basic substances include alkali salts of basic pyrosulfates M P 2 0 7 where M goo signifies an alkali or alkali metal, preferably potassium, o spolyphosphates, tripolyphosphate, metasilicates such as 15 sodium metasilicate, and primary, secondary, tertiary o 0 6 amines, particularly water soluble and/or grease-emulsio 0o fying primary, secondary and tertiary alkanol amines a" s preferably having 1-10 carbon atoms and optionally substituted on the alkyl part, e.g. mono-, di- and triethanolamine, 2-aino-l-butanol, 2-amino-3-methyl- 0 -propanol, 2-amino-2-methyl-l,3-propandiol, 2-aminoow o% -2-ethyl-l,3-propandiol, tris(hydroximethyl)amino mrthane and isopropanol amine. These alkali substances can be S0a Icharged in mixtures with the tensides.

Tn the case of large bacteria populations, the pH-value o may fall rapidly due to high consumption of emulsifying chemicals and to the generation of acid by dead bacteria.

Consequently, in order to prevent the tenside-consumption from becoming excessive, the nutrient solution introduced to the bath may also contain a pH-increasing substance suitable for tensides, e.g. one of the aforementioned.

Preferably, sodium metasilicate or alternatively amines are used. Tensides based on sodium metasilicate are not suitable for use in a number of industrial surface- -treatment processes, such as electrolytic processes for applying chromium, nickel and other metals. In the case of these processes, the alkaline substance used must be based on amines.

The nutrient substances charged in ao'danoee th tho i At*-R are those conventionally used for the cultivation of ricroorganisms. These substances A-~ls44contain N, S, Mg, K, P, and a carbon source, and may also contain trace metals such as Zn, Mn, Cu, Co, Mo. A suitable mixture will contain one part by weight Mg 2 one part by weight S0 2 8 parts by weight K 32 parts by o weight PO 3 80 parts by weight NH a carbon source o in the form of glucose 1600 parts by weight, minor quanti- 15 ties of zink, manganese, copper, cobalt and molybdenum, o pH-increasing substances, e.g. alkali and pH-lowering *i acid, e.g. H 3 P04, 02 3000 parts by weight in the I form oxygen or air. The composition of the nutrient substances, however, forms part of the present state of the art and can be readily established by the skilled Q* person.

The microorganisms activated in ao:ord1n:s with th .priOnFt inv tion are the following: In mineral oils there are found Pseudomonas spp Pseudomonas pseudoalcaligenes Pseudomonas alcaligenes Alteromonas putrefaciens Pseudomonas stutzeri Aeromonas spp Enterobacteriaceae spp Klebsiella pneumoniae Enterobacter agglomerans Klebsiella oxytoca 16 Proteus vulgar'is Citrobacter diversus Esoherichia coli Citrobacter freundii Morganella morgani Thiobacillus spp Thiobacillus ferrooxidans Aerococcus viridans Cladisporium resinae Alkane oxidizing spp Acinetobacter spp Arthrobacter spp, 4: Nocardia spp Cyronebacterium spp Xanthornonas spp Brevibaoterium spp 04 a 0 In synthetic oils there are found 0 Pseudomonas spp Pseudornonas pseudoaloaligenes Pseudomonas aloaligenes 4 Pseudonionas fluorescens a 04 Pseudomonas putida 00 Aclnetohacter spp Aclnetobacter calcoaceticus Thiobacillus spp CC C 0 0 Thiobaillus thiooxidans .00044Flav'obacterium odoratum Enterobacteriaceae apt) Bacillus spp Alkane oxidizing spp Arthrobacter spp, Nocardia spp Corynebacterium spp Xanthomonas spp Brevibacterium spp

I

17 It is also possible to initiate a process by adding cultivated strains of the aforesaid bacteria. It is also possible to initiate a cleaning process by adding slime or sludge isolated from a previous process to the bath.

Tensides are able to be used effectively and in a rational manner to clean industrial goods prior to subjecting said goods to further treatment processes, degreasing of said goods having been previously effected mainly with caustic soda solutions. The method enables tensides to be used, because the content organic contaminants in the cleaning bath can be held constantly at a low level. When practising the present embodiment of the inventive method the bath can be used for a period of up to about 2 years as "opposed to a period of about 1 month as in the case of the earlier known cleaning method, depending upon the quantity o of contaminated objects, or goods, degreased :n the bath.

The objects cleaned in accordance with the embodiment can also be washed easily free from the cleaning solution.

Objects cleaned in accordance with the earlier known method 6 cannot be washed so readily, since caustic soda, or lye, is difficult to wash off. The present embodiment can also be carried out at low temperatures, in the region of 35 instead of the relatively high temperatures of 90-950C used in the earlier degreasing process. This means that energy 0• o can be saved. Since energy can be saved and the chemicals can be used more effectively, there is obtained a cost reduction of 60-80%.

Embodiments of the invention also relates to apparatus for It C, carrying out the cleaning method. Embodiments of this apparatus comprise a cleansing tank, a washing liquid tank and a rinsing liquid tank.

18 mr.i-totc c -ing.U..g.of-thc wah--..t liquid ta

R

nk and the -n-ing Tiquda n sp eely. The bottoms of the three tanks may be conical in shape.

The cleansing tank may have any desired shape, such as round, square, rectangular, although it is preferably open and round. The washing liquid and rinsing liquid tanks may also have any desired shape. The tanks are preferably closed. The rinsing liquid and washing liquid tanks may have a ceiling or roof whose total surface area is greater than or smaller than the bottom surface of the cleansing tank. These ceilings may also coincide fully or partially S4o with the bottom of the cleansing tank. Thus, the rinsing S liquid tank and washing liquid tank may project beyond the 15 bottom of the cleansing tank or coincide with the outer boundaries thereof, as illustrated in Fig. 3, or the o ceilings may leave part of the outer bottom surface of the cleansing tank free.

The thre tanks for cleansing and holding washing liquid o 4and rsisin liquid respectively are preferably configured o <in a first cylindrical tank having a conical bottom. The tank is first divided transversely of its longitudinal S axis, so as to obtain an upper, cleansing tank, and then diametrically downwards beneath the cleansing tank, so as to obtain a washing liquid tank and a rinsing liquid tank.

SPreferably, only the conical part of the first cylindrical tank is divided into a tank for washing liquid and a tank for rinsing liquid as illustrated in Fig. 3. The first cylindrical tank, however, may also be partitioned transversely to the longitudinal axis, above the conical part, so that the washing-liquid and rinsing-liquid tanks obtain an upper cylindrical part and a lower conical part.

Preferably, there are provided outlet openings from the cleansing tank to the washing liquid tank and the rinsing

I

r 19liquid tank respectively, and openings for further transportation of washing and rinsing liquid from respective washing and rinsing liquid tanks to the cleansing tank, closeable outlets from respective washing liquid and rinsing liquid tanks, closeable inlets for fresh water, washing liquid and additives to the washing liquid tank and a closeable inlet for supplying fresh water to the rinsing liquid tank.

The rinsing liquid and washing liquid tanks may include means for heating the contents of said tanks and also means for aerating said tanks. The washing liquid tank preferably includes aerating means. The washing liquid tank may also include agitating or stirring means.

Agitation of the tank contents, however, is preferably S°effected through aerating of the tank.

a o i.4 Referring to Fig. 3, when using the illustrated apparatus, 4 0 goods or objects A to be cleaned are placed in the o 0f o 0 cleansing tank 1, e.g. with the aid of a basket. The valve o 6 is opened and a pump activated, whereupon washing liquid comprising tenside and alkali is pumped up from the tank 2 and applied to the objects or goods under powerful pressure. This can either be carried out manually or 0 0 rer roc 00 0 I- ll- r~-rr I 99 99 99 9 9t 9 9 i 9994 9 9 99 9 99i 9 99 9* 9 8 9 9 9 99 99 9 9 88 9 99 *s 8 9 99, 8844a 9 994 a.

ao9, 99 9 rr. 4 .9999 through nozzles installed in the cleansing tank 1. The washing liquid emulsifies oil, grease and like contaminants. Subsequent to washing the objects, the valve 4 in the cleansing tank 1 is opened, and the used washing liquid is allowed to run back to the washing liquid tank 2. The valve 7 is then opened and a pump activated, whereupon rinsing water is sprayedl In t orlc:rit:d Iannar over the objects, to rinse washing liquid therefrom. The valve 5 in the cleansing tank 1 is then opened and the rinsing water is allowed to run back to the tank 3. After the apparatus has been used for some hours, oil and grease will have accumulated in the washing liquid in the tank 2. At this stage, continuous metering of tensides, alkali and nutrient salts can be commenced and the 15 pH-value adjusted to 8.5-9.5, so as to enable maximum growth of the microorganisms. The washing liquid tank, which in the case of the illustrated apparatus is the tank in which the contaminants are broken down biologically, is aerated and the contents thereof agitated with the aid of 20 air entering through an air conduit 16. The pH-value falls with increasing oil contents. The pH-value is therefore adjusted to the aforesaid pH-range, so as to maintain the oil content within the range of 100-500 mg/liter.

Under these conditions it is possible to effect continuously a degreasing process in which oil-contaminated objects are constantly introduced into the cleansing tank 1 and degreased with washing liquid based on tensides and alkali, which emulsifies oil and bacteria present therein upon contact with the objects, such that the bacteria are able subsequently to reduce the oil content of the washing liquid tank 2 to within the range of 100-500 mg/liter, said tank 2 functioning as a microorganism cultivating tank.

The method is facilitated by the fact that the lower part 21 of the apparatus is conical in shape. Because the washing liquid tank 2 is conical it has a confined lowest point to which contawinants and dead bacteria are able to sink and from which the contaminants can be removed continuously to a waste outlet, through the valve 8. The rinsing water tank 3 is also conical in shape and incorporates an outlet valve 9. The bacteria population can be run at low temperatures, preferably at 35-40°C in the case of a thermophilic proceis or at 40-600C in the case of mesophilic baceria. These temperature ranges can be maintained in the washing liquid tank 2 with the aid of the heating means 13. The tank contents may also be heated with hot o" air. The temperature of the contents of the rinsing water tank 3 can also be regulated, with the aid of the means 15 14, Optimization of the washing process for high bacteria populations, by adjusting the pH-value and the nutrient substances and fresh tensides, enables the tenside conoo sumption to be kept as low as 10% of the calculated amount of oil introduced to the system. Oxygen is supplied continuously, by aeration, and the oxygen blow is positioned o, in a manner such that dead bacteria and entrant cont- O- aminants can be removed continuously through the valve 6.

This affords optimum bacteria growth conditions and en- 1. a* ables tensides to be used effectively and rationally for degreasing industrial objects and goods.

&n\o or the wCAe Oo rxof I lae invention will now be described in more detail with reference to a number of working examples.

Example 1 A standard method carried out in a low-temperature cleaning system in which cleaning and biodegradation are effected in one and the same bath.

A stream of objects, or goods, to be cleansed are conveyed by a transverse conveyer or drum to the process bath 17 22 (see Fig. 1) and are left in the bath for about 2-20 minutes, so that oil and contaminants are washed off. Air is blown with a motor 18 and a fan 19 through line 20 into the bath continuously from the bottom of said bath, so as to thorougly agitate the bath contents and maximize the oxygen supply. Bath liquid is fed through a valve 21 with a pump 22 continuously from the bath to a separator unit 23, for extraction of contaminants and dead bacteria through a valve 24 to a sludge tank 25. Sludge, or slime, is withdrawn from the separator compression zone. Tensides are metered to the bath continuously from a tank 26 at the same rate as the tensides are consumed. Nutrient solution, o°Camex Bio 104-1, is metered to the bath intermittently from a tank 27, so as to maintain the set-,oint values set i on the pH-meter constant. The best mesophilic bacteria '*culture is obtained when the bath temperature is main- 0o 0 tained at 38 +l°C.

The nutrient solution and the tenside solution are fed through valves 28, 29, 30 and 31 respectively with pumps 4 32 and 33 and are mixed with separated solution from the oo separator 23 through valve 311 in a mixing unit 35 and fed to the process tank 17. A thermostate 36 and a heater 37 4 4 1 4 a# are placed in the process tank 16. Fresh water is fed into the tank 17 through a line 37.

a0 0 The tenside solution used is Camex Bio 104, which com- °0o, Vprises a mixture of 1-5 by weight sodium metasilicate, 5-10% tetrapotassium pyrophosphate, 5-10 nonionic and cationic tensides, having a pH of 13. This solution is diluted to a 5 %-tenside solution of pH The nutrient solution used has the following basic composition r 23 1.2 kg MgC126H20 magnesium chloride 1.8 kg KOH potassium hydroxide 3.3 kg H2SO 4 37 %-sulfuric acid 100 kg H 3

PO

4 85%-phosphoric acid 40 kg NH 4 C1 ammonium chloride kg glucose.

This solution is diluted with water to 300 liters.

2 kg of this basic solution is mixed with 210 kg

NH

4 SiO 3 and the mixture diluted to 600 liters.

The following operating parameters are maintained: 6* 46 44 4 6 4 4 44 4 44 4 4444 4 *4444 4 4 66 4 44 a 46 4 44 0 @4 4 p 4*4404 4 48*4 a 0* 4 4 44 44 4* 4 4 4 4 4~ t Ib Bath water Heating power Tenside concentration Temperature Air injection 0 Objects or goods to bath Production time Object surface area Object surface area Oil emulsified in bath Oil emulsified in bath Tenside consumption Quantity of tenside metered (24 h) 0B 104 30 Bacteria activity with normal operation Quantity of nutrient solution metered CB 104-1 to pH Sludge removed TS-content 5-8 25 m 3 20 kWh 38 0

C

180 m 3 /h 6000 tonnes/year 1700 h/year 600 000 m 2 /year 2800 m2/day 3000 kg/year 14 kg/day 1250 kg/year 0.15 kg/h 6 1.2 x 10 bact/ml 9.4-9.5 3 m3/year 24 Sludge removed TS-content 5-8% 10 1/day Bacteria activity sludge 2.4 x 10 7 bact./ml Normal oil or aromatic content of bath 50-250 mg/l Normal oil or aromatic content of the sludge 50-150 mg/l Example 2 Example 1 above is repeated but with the difference that the nutrient solution is mixed with amine instead of sodium silicate, in accordance with the following. 2 kg of basic solution are mixed with 400 kg alkaline amine such O as diethanol amine or trietanol amine. The mix is diluted 15 with water to 600 liters. This example is particularly suited for application with goods or objects which are to 04 be coated with chromium, nickel or other metals by 0 electrolytic coating procseses.

Example 3 o High-temperature degreasing bath and a separate unit for o,0 o biodegradation (Figure 2), 'o"o The objects or goods are passed through a washing machine 39 on a conveyor belt 10 ond then rinced in a rinoing unit 42. A 5%-tenside solution is mixed from the basic solution 40 Saccording to Example 1 at a temperature of 50-90QC, wherenfter the solution is applied under high pressure to the surfaces of the objects or goods, so as to dissolve and emulsify oil and contaminants present thereon. Washing and rincing is done through nozzzleQ 42. Part of tne washing liquid is transferred to a biodegradation unit 43 for the reduction of oil and contaminants. Nutrient solution as in example 1 is added to the bioderadation unit 43 from a tank I44 Fresh tenside solution is fed to the regeneration unit 43 from a tank I i! iThe temperature in the biodegradation unit is lowered to 20-30 0 C, upon oxygenation of the unit contents, by injecting air thereinto. Consequently, a mesophilic bacteria culture obtains optimized growth conditions when the flow passes through the biological unit. The flow is then passed to the central separation part, in which dead bacteria and sludge, slime, are passed to a compression zone for removal to a sludge tank 46. Air is also injected in the cleanin tank 39. Heaters are arranged in all tanks 39, 41 and 43.

The biodegradation process is controlled in the same manner as that described in Example 1 and the injection of air and metering of tensides is effected continuously, 15 whereas the alkaline nutrient solution in 1 iietered intero mittently, to a pH-value of 9.4-9.5.

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Claims

1. A method for cleaning objects, characterized by cleaning said objects by treating them with an aqueous tenside solution such as to emulsify the organic contaminants present, by stimulating the growth of microorganisms in the tenside solution for biodegradation of the organic substances, and by adding nutrient substances so that the tenside solution substantially is unaffected, the biodegradation being performed separately from or simultaneously with the cleaning.

2. A method according to Claim 1, characterized by maintaining the content of organic substances in the tenside solution at 50-1000mg/liter, by maintaining the tenside content at 1-15 by weight, by maintaining the temperature at 20-80°C during biodegradation, and by separating contaminants and dead bacteria from the tenside solution.

3. A method according to any one of claims 1-2, characterized by adjusting the pH-value of the tenside solution to 7 during biodegradation.

4. A method according to any one of claims 1-3, characterized by effecting the cleaning process and biodegradation process separately from one another; wherein cleaning is effected at pH 7-14 and a temperature of 20-100" C and biodegradation is effected from a pH of 8.5 to a pH-value which will not block biological growth. A method according to any one of claims 1-4, characterized by supplying oxygen to the system.

6. A method according to any one of claims characterized by vigorously agitating the system and by introducing the microorganisms into the system by adding 27 S- 27 thereto microorganisms strains or sludge separated from or produced in a previous cleaning process.

7. A method according to claim 2 characterized by maintaining the content of organic substances in the tenside solution at 50-250mg/litre.

8. A method according to claim 2 characterized by maintaining the tenside content at 2-5% by weight.

9. A method according to claim 3 characterized by 4 0 adjusting the pH-value of the tenside solution between and a pH which will not block bacteria growth under biodegradation. o a* A method according to claim 4 wherein cleaning is effected at a pH-value in the range of 8.5-9.7 and at a temperature of 20-400C.

11. A method according to claim 5 wherein said oxygen is supplied to the system by injecting air thereinto. 0 9

12. A method according to claim 6 wherein the vigorous 09° agitation of the system is achieved by injecting air into the system. F° 13. Apparatus when used in accordance with the method according to any one of claims 1-12, characterized by a cleansing tank which is located above a washing liquid tank and above a rinsing liquid tank, the bottom of the i cleansing tank being completely or partially common with the ceiling of the washing liquid tank and the rinsing liquid tank.

14. Apparatus according to claim 13 wherein at least one of said cleansing tank, washing liquid tank and said rinsing liquid tank has a conically shaped bottom. 28 Apparatus according to any of one of claims 13 and 14, characterized by closeable outlet opening, leading from the cleansing tank to the washing liquid tank and the rinsing liquid tank respectively; and by closeable outlet openings for further transportation of washing liquid and rinsing liquid respectively to the cleansing tank; by closeable outlets from the washing liquid tank and the rinsing liquid tank, by closeable inlets for introducing fresh water, washing liquid and additives to the washing liquid tank; and by a closeable inlet for introducing fresh water to the rinsing liquid tank. 'o'o 16. Apparatus according to any one of claims 13 to 0 0 characterized by means for heating the content of the 0: washing liquid and rinsing liquid tanks and, optionally, means for aerating the washing liquid tank. t 4 17. A method for cleaning objects substantially as t hereinbefore described with reference to and as shown in the accompanying drawings.

18. Apparatus for cleaning objects substantially as hereinbefore described with reference to and as shown in the accompanying drawings. it *0 DATED THIS 4TH DAY OF MARCH, 1991. i t LAR6 AKE HILMER HAKANSSON By His Patent Attorneys: GRIFFITH HACK CO. Fellows Institute of Patent Attorneys of Australia.